Energy Conservation Program: Test Procedure for Dedicated-Purpose Pool Pumps, 36858-36931 [2017-15464]
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DEPARTMENT OF ENERGY
10 CFR Parts 429 and 431
[EERE–2016–BT–TP–0002]
RIN 1904–AD66
Energy Conservation Program: Test
Procedure for Dedicated-Purpose Pool
Pumps
Office of Energy Efficiency and
Renewable Energy, Department of
Energy.
ACTION: Final rule.
AGENCY:
On September 20, 2016, the
U.S. Department of Energy (DOE) issued
a notice of proposed rulemaking (NOPR)
to establish a new metric, as well as new
definitions, test procedures, certification
requirements, enforcement testing
procedures, and labeling provisions for
dedicated-purpose pool pumps (DPPPs).
That proposed rulemaking serves as the
basis for the final rule. Specifically,
DOE is adopting a test procedure for
measuring the weighted energy factor
(WEF) for certain varieties of dedicatedpurpose pool pumps. This final rule
incorporates by reference certain
sections of the industry test standard
Hydraulic Institute (HI) 40.6–2014,
‘‘Methods for Rotodynamic Pump
Efficiency Testing’’ as the basis of the
adopted test procedure. The definitions,
test procedures, certification
requirements, enforcement testing
procedures, and labeling provisions are
based on the recommendations of the
DPPP Working Group, which was
established under the Appliance
Standards Rulemaking Federal Advisory
Committee (ASRAC).
DATES: The effective date of this rule is
September 6, 2017. Compliance with the
final rule will be mandatory for
representations of WEF and other
metrics addressed by the adopted test
procedure made on or after February 5,
2018. The incorporation by reference of
certain publications listed in this rule is
approved by the Director of the Federal
Register on September 6, 2017.
ADDRESSES: The docket, which includes
Federal Register notices, public meeting
attendee lists and transcripts,
comments, and other supporting
documents/materials, is available for
review at www.regulations.gov. All
documents in the docket are listed in
the www.regulations.gov index.
However, some documents listed in the
index, such as those containing
information that is exempt from public
disclosure, may not be publicly
available.
A link to the docket Web page can be
found at https://www.regulations.gov/
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SUMMARY:
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docket?D=EERE-2016-BT-TP-0002. The
docket Web page will contain simple
instructions on how to access all
documents, including public comments,
in the docket.
For further information on how to
review the docket, contact the
Appliance and Equipment Standards
Program staff at (202) 586–6636 or by
email: ApplianceStandardsQuestions@
ee.doe.gov.
FOR FURTHER INFORMATION CONTACT:
Ms. Ashley Armstrong, U.S.
Department of Energy, Office of Energy
Efficiency and Renewable Energy,
Building Technologies Office, EE–5B,
1000 Independence Avenue SW.,
Washington, DC 20585–0121.
Telephone: (202) 586–6590. Email:
Ashley.Armstrong@ee.doe.gov.
Ms. Mary Greene, U.S. Department of
Energy, Office of the General Counsel,
GC–33, 1000 Independence Avenue
SW., Washington, DC 20585–0121.
Telephone: (202) 586–1817. Email:
Mary.Greene@hq.doe.gov.
SUPPLEMENTARY INFORMATION: This final
rule incorporates by reference into 10
CFR parts 429 and 431 the following
industry standards:
(1) Hydraulic Institute (HI) 40.6–2014,
(‘‘HI 40.6–2014–B’’) ‘‘Methods for
Rotodynamic Pump Efficiency Testing,’’
except for section 40.6.4.1, ‘‘Vertically
suspended pumps’’; section 40.6.4.2,
‘‘Submersible pumps’’; section 40.6.5.3,
‘‘Test report’’; section 40.6.5.5, ‘‘Test
conditions’’; section 40.6.5.5.2, ‘‘Speed
of rotation during testing’’; and section
40.6.6.1, ‘‘Translation of test results to
rated speed of rotation’’; and Appendix
A, Testing arrangements (normative):
A.7, ‘‘Testing at temperatures exceeding
30 °C (86 °F)’’; and Appendix B,
‘‘Reporting of test results (normative)’’),
copyright 2014.
Copies of HI 40.6–2014 can be
obtained from: The Hydraulic Institute
at 6 Campus Drive, First Floor North,
Parsippany, NJ 07054–4406, (973) 267–
9700, or by visiting www.pumps.org.
(2) Canadian Standards Association
(CSA) C747–2009 (Reaffirmed 2014),
‘‘Energy Efficiency Test Methods for
Small Motors,’’ CSA reaffirmed 2014,
section 1, ‘‘Scope’’; section 3,
‘‘Definitions’’; section 5, ‘‘General Test
Requirements’’; and section 6, ‘‘Test
Method.’’
Copies of CSA C747–2009 (RA 2014)
can be obtained from: 5060 Spectrum
Way, Suite 100, Mississauga, Ontario,
L4W 5N6, Canada, (800) 463–6727, or
by visiting www.csagroup.org.
(3) IEEE Std 113–1985, ‘‘IEEE Guide:
Test Procedures for Direct-Current
Machines,’’ copyright 1985, section 3.1,
‘‘Instrument Selection Factors’’; section
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3.4 ‘‘Power Measurement’’: section 3.5
‘‘Power Sources’’; section 4.1.2
‘‘Ambient Air’’; section 4.1.4 ‘‘Direction
of Rotation’’; section 5.4.1 ‘‘Reference
Conditions’’; and section 5.4.3.2
‘‘Dynomometer or Torquemeter
Method.’’
(4) IEEE Std 114–2010, ‘‘IEEE
Standard Test Procedure for SinglePhase Induction Motors,’’ approved
September 30, 2010, section 3.2, ‘‘Tests
with load’’; section 4 ‘‘Testing
facilities’’; section 5.2 ‘‘Mechanical
measurements’’; section 5.3
‘‘Temperature measurements’’; and
section 6 ‘‘Tests.’’
Copies of IEEE 113–1985 and IEEE
114–2010 and can be obtained from:
IEEE, 45 Hoes Lane, P.O. Box 1331,
Piscataway, NJ 08855–1331, (732) 981–
0060, or by visiting www.ieee.org.
(5) NSF International (NSF)/American
National Standards Institute (ANSI)
Standard 50–2015, (‘‘NSF/ANSI 50–
2015’’), ‘‘Equipment for Swimming
Pools, Spas, Hot Tubs and Other
Recreational Water Facilities,’’ Annex C,
‘‘(normative) Test methods for the
evaluation of centrifugal pumps,’’
section C.3, ‘‘Self-priming capability,’’
ANSI approved January 26, 2015.
Copies of NSF/ANSI 50–2015 can be
obtained from: NSF International, 789
N. Dixboro Road, Ann Arbor, MI 48105,
(743) 769–8010, or by visiting
www.nsf.org.
(6) UL 1081, (‘‘ANSI/UL 1081–2016’’),
‘‘Standard for Swimming Pool Pumps,
Filters, and Chlorinators,’’ 7th Edition,
ANSI approved October 21, 2016.
Copies of ANSI/UL 1081–2016 can be
obtained from: UL, 333 Pfingsten Road,
Northbrook, IL 60062, (847) 272–8800,
or by visiting https://ul.com.
See section IV.N for additional
information on these standards.
Table of Contents
I. Authority and Background
A. Authority
B. Background
II. Synopsis of the Final Rule
III. Discussion
A. General Comments
B. Definitions
1. Existing Pump Definitions
2. Definition of Dedicated-Purpose Pool
Pump
3. Pool Filter Pumps
4. Other Varieties of Dedicated-Purpose
Pool Pumps
5. Storable and Rigid Electric Spa Pumps
6. Applicability of Test Procedure Based on
Pump Configuration
7. Definitions Related to DedicatedPurpose Pool Pump Speed
Configurations and Controls
8. Basic Model
C. Rating Metric
D. Test Methods for Different DPPP
Categories and Configurations
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1. Self-Priming and Non-Self-Priming Pool
Filter Pumps
2. Waterfall Pumps
3. Pressure Cleaner Booster Pumps
4. Summary
E. Determination of Pump Performance
1. Incorporation by Reference of HI 40.6–
2014
2. Exceptions, Modifications and Additions
to HI 40.6–2014
F. Representations of Test Metrics
1. Representations of Primary Efficiency
Metrics
2. Definition of Representation
3. Impact on Voluntary and Other
Regulatory Programs
4. Request for Extension
G. Additional Test Methods
1. Determination of DPPP Capacity
2. Determination of Self-Priming Capability
3. Determination of Maximum Head
H. Energy Factor Test Method
I. Labeling Requirements
J. Replacement DPPP Motors
K. Certification and Enforcement
Provisions for Dedicated-Purpose Pool
Pumps
1. Sampling Plan
2. Certification Requirements
3. Enforcement Provisions
IV. Procedural Issues and Regulatory Review
A. Review Under Executive Order 12866
B. Review Under the Regulatory Flexibility
Act
1. Review of DPPP Manufacturers
2. Burden of Conducting the DOE DPPP
Test Procedure
C. Review Under the Paperwork Reduction
Act of 1995
D. Review Under the National
Environmental Policy Act of 1969
E. Review Under Executive Order 13132
F. Review Under Executive Order 12988
G. Review Under the Unfunded Mandates
Reform Act of 1995
H. Review Under the Treasury and General
Government Appropriations Act, 1999
I. Review Under Executive Order 12630
J. Review Under Treasury and General
Government Appropriations Act, 2001
K. Review Under Executive Order 13211
L. Review Under Section 32 of the Federal
Energy Administration Act of 1974
M. Congressional Notification
N. Description of Materials Incorporated by
Reference
V. Approval of the Office of the Secretary
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I. Authority and Background
Pumps are included in the list of
‘‘covered equipment’’ for which the U.S.
Department of Energy (DOE) is
authorized to establish and amend
energy conservation standards (ECSs)
and test procedures (TPs). (42 U.S.C.
6311(1)(A)) Dedicated-purpose pool
pumps (DPPPs), which are the subject of
this rulemaking, are a kind of pump for
which DOE is authorized to establish
test procedures and energy conservation
standards. In 2016, DOE published in
the Federal Register two final rules
establishing energy conservation
standards and a test procedure for
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commercial and industrial pumps. 81
FR 4368 (Jan. 26, 2016) and 81 FR 4086
(January 25, 2016), respectively.
However, dedicated-purpose pool
pumps were specifically excluded from
those final rules. Based on
recommendations of the industry and
DOE’s own analysis, DOE determined
that dedicated-purpose pool pumps
have a unique application and
equipment characteristics that merit a
separate analysis. As a result, DOE
initiated separate rulemakings to
establish energy conservation standards
and test procedures for dedicatedpurpose pool pumps. The following
sections discuss DOE’s authority to
establish test procedures for dedicatedpurpose pool pumps and relevant
background information regarding
DOE’s consideration of establishing
Federal regulations for this equipment.
A. Authority
Title III of the Energy Policy and
Conservation Act of 1975, as amended,
(42 U.S.C. 6291, et seq.; ‘‘EPCA’’ or, ‘‘the
Act’’) sets forth a variety of provisions
designed to improve energy efficiency.1
Part C of Title III, which for editorial
reasons was codified as Part A–1 upon
incorporation into the U.S. Code (42
U.S.C. 6311–6317), establishes the
Energy Conservation Program for
Certain Industrial Equipment. ‘‘Pumps’’
are listed as a type of industrial
equipment covered by EPCA, although
EPCA does not define the term ‘‘pump.’’
(42 U.S.C. 6311(1)(A)) DOE defined
‘‘pump’’ in a test procedure final rule
(January 2016 general pumps test
procedure final rule) as equipment
designed to move liquids (which may
include entrained gases, free solids, and
totally dissolved solids) by physical or
mechanical action, and includes a bare
pump and, if included by the
manufacturer at the time of sale,
mechanical equipment, driver, and
controls. 81 FR 4086 (Jan. 25, 2016).
Dedicated-purpose pool pumps, which
are the subject of this final rule, meet
this definition of a pump and are
covered under the pump equipment
type.
Under EPCA, the energy conservation
program consists essentially of four
parts: (1) Testing, (2) labeling, (3)
Federal energy conservation standards,
and (4) certification and enforcement
procedures. The testing requirements
consist of test procedures that
manufacturers of covered products must
use as the basis for (1) certifying to DOE
1 All references to EPCA in this document refer
to the statute as amended through the Energy
Efficiency Improvement Act of 2015, Public Law
114–11 (Apr. 30, 2015).
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that their products comply with the
applicable energy conservation
standards adopted under EPCA, and (2)
making representations about the
efficiency of those products. Similarly,
DOE must use these test procedures to
determine whether the products comply
with any relevant standards
promulgated under EPCA.
Under 42 U.S.C. 6293, EPCA sets forth
the criteria and procedures DOE must
follow when prescribing or amending
test procedures for covered products.
EPCA provides that any test procedures
prescribed or amended under this
section shall be reasonably designed to
produce test results that measure energy
efficiency, energy use, or estimated
annual operating cost of a covered
product during a representative average
use cycle or period of use and shall not
be unduly burdensome to conduct. (42
U.S.C. 6293(b)(3))
In addition, if DOE determines that a
test procedure amendment is warranted,
DOE must publish a proposed test
procedure and offer the public an
opportunity to present oral and written
comments on it. (42 U.S.C. 6293(b)(2))
Finally, in any rulemaking to amend a
test procedure, DOE must determine to
what extent, if any, the proposed test
procedure would alter the measured
energy efficiency of any covered
product as determined under the
existing test procedure. (42 U.S.C.
6293(e)(1))
B. Background
Dedicated-purpose pool pumps are a
style of pump for which DOE has not
yet established a test procedure.
Although in 2016 DOE completed final
rules establishing energy conservation
standards (81 FR 4368 (Jan. 26, 2016);
January 2016 general pumps ECS final
rule) and a test procedure (81 FR 4086
(Jan. 25, 2016); January 2016 general
pumps test procedure final rule) for
certain categories and configurations of
pumps, DOE declined in those rules to
establish any requirements applicable to
dedicated-purpose pool pumps because
of their different equipment
characteristics and applications. 81 FR
4086, 4094 (Jan. 25, 2016).
To begin a separate rulemaking for
dedicated-purpose pool pumps, on May
8, 2015, DOE issued a Request for
Information (RFI), hereafter referred to
as the ‘‘May 2015 DPPP RFI.’’ The May
2015 DPPP RFI presented information
and requested public comment about
any definitions, metrics, test
procedures, equipment characteristics,
and typical applications relevant to
DPPP equipment. 80 FR 26475.
Following the publication of the May
2015 DPPP RFI, DOE began a process
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through the Appliance Standards
Rulemaking Federal Advisory
Committee (ASRAC) to discuss
conducting a negotiated rulemaking to
develop standards and a test procedure
for dedicated-purpose pool pumps as an
alternative to the traditional notice and
comment route that DOE had already
begun. (Docket No. EERE–2015–BT–
STD–0008) On August 25, 2015, DOE
published a notice of intent to establish
a negotiated rulemaking working group
for dedicated-purpose pool pumps (as
previously defined, the ‘‘DPPP Working
Group’’) to negotiate, if possible, Federal
standards for the energy efficiency of
dedicated-purpose pool pumps and to
announce the first public meeting. 80
FR 51483.
The DPPP Working Group met four
times between September and December
2015 2 and concluded its negotiations on
December 8, 2015, with a consensus
vote to approve a term sheet containing
recommendations to DOE on scope,
metric, and the basis of the test
procedure (‘‘December 2015 DPPP
Working Group recommendations’’).3
The term sheet containing these
recommendations is available in the
DPPP Working Group docket. (Docket
No. EERE–2015–BT–STD–0008, No. 51)
ASRAC subsequently voted
unanimously to approve the December
2015 DPPP Working Group
recommendations during a January 20,
2016, meeting. (Docket No. EERE–2015–
BT–STD–0008, No. 0052)
The DPPP Working Group also
requested, and was ultimately granted,
more time to discuss possible energy
conservation standards for this
equipment. (Docket No. EERE–2013–
BT–NOC–0005, No. 71 at pp. 20–52)
The meetings to discuss energy
conservation standards commenced on
March 21, 2016, (81 FR 10152, 10153)
and concluded on June 23, 2016, with
approval of a second term sheet (June
2016 DPPP Working Group
recommendations). This term sheet
contained Working Group
recommendations related to scope,
definitions, energy conservation
standards, performance standards or
design requirements for various styles of
pumps, applicable test procedure, and
labeling for dedicated-purpose pool
pumps. (Docket No. EERE–2015–BT–
2 Details of the negotiations sessions can be found
in the public meeting transcripts that are posted to
the docket for the DPPP Working Group (https://
www.regulations.gov/docket?D=EERE-2015-BTSTD-0008).
3 The ground rules of the DPPP Working Group
define consensus as no more than three negative
votes. (Docket No. EERE–2015–BT–0008–0016 at p.
3) Concurrence was assumed absent overt dissent,
evidenced by a negative vote. Abstention was not
construed as a negative vote.
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STD–0008, No. 82) The definitions,
DPPP test procedure, sampling
provisions, enforcement requirements,
and labeling requirements contained in
this final rule reflect the
recommendations of the DPPP Working
Group contained in both the December
2015 and June 2016 DPPP Working
Group recommendations.
On September 20, 2016, DOE
published a proposed test procedure
rulemaking for dedicated-purpose pool
pumps (September 2016 DPPP test
procedure NOPR), which proposed to
implement the recommendations of the
DPPP Working Group. 81 FR 64580. On
September 26, 2016, DOE held a public
meeting to discuss and request comment
on the September 2016 DPPP test
procedure NOPR (September 2016 DPPP
test procedure NOPR public meeting).
The test procedure adopted in this
final rule reflects certain
recommendations of the DPPP Working
Group, as well as input from interested
parties received in response to the
September 2016 DPPP test procedure
NOPR. Provisions of this final rule that
are directly pertinent to any of the
approved DPPP Working Group
recommendations are specified with a
citation to the December 2015 or June
2016 DPPP Working Group
recommendations and are noted with
the recommendation number (e.g.,
Docket No. EERE–2015–BT–STD–0008,
No. #, Recommendation #X at p. Y).
Additionally, in developing the
provisions of this final rule, DOE also
has referenced discussions from the
DPPP Working Group meetings
regarding potential actions or comments
that may not have been formally
approved as part of the DPPP Working
Group recommendations. These
references to discussions or suggestions
of the DPPP Working Group not found
in the DPPP Working Group
recommendations will have a citation to
meeting transcripts and the commenter,
if applicable (e.g., Docket No. EERE–
2015–BT–STD–0008, [Organization],
No. X at p. Y).
Finally, in this final rule, DOE
responds to all comments received from
interested parties in response to the
proposals presented in the September
2016 DPPP test procedure NOPR, either
during the September 2016 DPPP test
procedure NOPR public meeting or in
subsequent written comments. In
response to the September 2016 DPPP
test procedure NOPR, DOE received 11
written comments in addition to the
verbal comments made by interested
parties during the September 2016 DPPP
test procedure NOPR public meeting.
The commenters included: The
Southern California Gas Company
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(SCG), Southern California Edison
(SCE), and San Diego Gas and Electric
Company (SDG&E), collectively referred
to herein as the California InvestorOwned Utilities (CA IOUs); a joint
comment by the Appliance Standards
Awareness Project (ASAP) and the
Natural Resources Defense Council
(NRDC); 4 Pentair Aquatic Systems
(Pentair); Hayward Industries, Inc.
(Hayward); Waterway; Davey Water
Products Pty Ltd. (Davey); the California
Energy Commission (CEC); the
Association of Pool & Spa Professionals
(APSP); Nidec Motor Corporation
(Nidec); Zodiac Pool Systems, Inc.
(Zodiac); and the People’s Republic of
China (China). DOE identifies comments
received in response to the September
2016 DPPP test procedure NOPR by the
commenter, the number of document as
listed in the docket maintained at
www.regulations.gov (Docket No. EERE–
2016–BT–TP–0002), and the page
number of that document where the
comment appears (for example:
Hayward, No. 4 at p. 1). If a comment
was made verbally during the
September 2016 DPPP test procedure
NOPR public meeting, DOE will also
specifically identify those as being
located in the NOPR public meeting
transcript (for example: CA IOUs, public
meeting transcript, No. 3 at p. 66).
Regarding comments, during the
September 2016 DPPP test procedure
public meeting, Hayward inquired if it
was appropriate to suggest any
modifications to previously negotiated
language, if Hayward believed it could
be helpful. (Hayward, Public Meeting
Transcript, No. 3 at p. 20) DOE
requested feedback on a number of
items in the September 2016 DPPP test
procedure NOPR and welcomed
comment from interested parties on any
of the proposals contained in the NOPR.
DOE notes that DPPP Working Group
ground rules stipulate that each party,
except individuals that have previously
voted negatively on the final term sheet,
agrees not to file negative comments or
speak negatively on the proposed rule or
its preamble to the extent they have the
same substance and effect as the term
sheet. (Docket No. EERE–2015–BT–
STD–0008, No. 16 at p. 5) However,
these rules are not legally binding, but
instead are good-faith principles to
govern Working Group’s negotiations.
Under the Administrative Procedure
Act, DOE must consider all relevant
comments submitted concerning the
4 ASAP was present at the September 2016 DPPP
TP NOPR public meeting. When ASAP commented
at the public meeting, comments will be indicated
as ASAP. ASAP and NRDC submitted a joint
written comment and written comments will be
indicated as ASAP and NRDC.
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September 2016 DPPP test procedure
NOPR, and make modifications to the
proposals, as necessary, in this final
rule. (5 U.S.C. 553(c)) Specific required
modifications are discussed in their
relevant sections.
On January 18, 2017, DOE published
a direct final rule containing energy
conservation standards for dedicatedpurpose pool pumps (e.g., the January
2017 DPPP DFR), based on the
recommendations of the DPPP Working
Group, with a compliance date of July
19, 2021. 82 FR 5650. After reviewing
comments submitted during the 110-day
comment period, on May 26, 2017, DOE
published a confirmation of effective
date and compliance date for the DFR.
82 FR 24218.
II. Synopsis of the Final Rule
In this final rule, DOE is amending
subpart Y to 10 CFR part 431 to include
definitions and a test procedure
applicable to dedicated-purpose pool
pumps. However, DOE is establishing a
test procedure for only a specific subset
of dedicated-purpose pool pumps.
Specifically, this test procedure applies
only to self-priming and non-selfpriming pool filter pumps, waterfall
pumps, and pressure cleaner booster
pumps. The test procedure does not
apply to integral cartridge-filter pool
pumps, integral sand-filter pool pumps,
storable electric spa pumps, or rigid
electric spa pumps. The test procedure
is applicable to those varieties of pool
pumps for which DOE established
performance-based standards in the
January 2017 DPPP DFR (82 FR 5650,
5743), as well as additional categories of
dedicated-purpose pool pumps for
which the DPPP Working Group did not
propose standards. (See section III.B.6
for more information on the
applicability of the new test procedure
to different DPPP varieties).
In this final rule, DOE defines a new
metric, the weighted energy factor
(WEF), to characterize the energy
performance of dedicated-purpose pool
pumps within the scope of this test
procedure. As described further in
section III.C, WEF is determined as a
weighted average of water volumetric
flow rate divided by the input power to
the dedicated-purpose pool pump at
different load points. The specific load
points and weights depend on the
variety of the dedicated-purpose pool
pump and the number of operating
speeds with which it is distributed in
commerce. In addition, the DPPP test
procedure includes a test method to
determine the self-priming capability of
pool filter pumps to effectively
differentiate self-priming and non-selfpriming pool filter pumps. Finally, the
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DPPP test procedure provides optional
methods for determining the WEF for
replacement DPPP motors.
DOE’s new test method includes
measurements of volumetric flow rate
and input power, both of which are
required to calculate WEF, as well as
other quantities to effectively
characterize the rated DPPP
performance (e.g., head, hydraulic
output power, rotating speed). For
consistent and uniform measurement of
these values, DOE is incorporating by
reference the test methods established
in HI 40.6–2014, ‘‘Methods for
Rotodynamic Pump Efficiency Testing,’’
with certain exceptions. DOE reviewed
the relevant sections of HI 40.6–2014
and determined that HI 40.6–2014, in
conjunction with the additional test
methods and calculations adopted in
this test procedure, will produce test
results that reflect the energy efficiency,
energy use, or estimated operating costs
of a dedicated-purpose pool pump
during a representative average use
cycle. (42 U.S.C. 6314(a)(2)) DOE also
reviewed the burdens associated with
conducting the test procedure,
including HI 40.6–2014, and, based on
the results of such analysis, found that
the test procedure is not unduly
burdensome to conduct. (42 U.S.C.
6314(a)(2)) DOE’s analysis of the
burdens associated with the test
procedure is presented in section IV.B.
This final rule also establishes
requirements regarding the sampling
plan, certification requirements, and
representations for dedicated-purpose
pool pumps at subpart B of part 429 of
title 10 of the Code of Federal
Regulations. The sampling plan
requirements are similar to those for
several other types of commercial
equipment and are appropriate for
dedicated-purpose pool pumps based on
the expected range of measurement
uncertainty and manufacturing
tolerances for this equipment (see
section III.K.1 for more detailed
information). As DOE’s DPPP test
procedure contains methods for
calculating the energy factor (EF),5
overall (wire-to-water) efficiency, driver
power input, DPPP nominal motor
horsepower,6 DPPP motor total
5 EF is a metric that is common in the DPPP
industry and which describes the volume of water
provided by a dedicated-purpose pool pump
divided by the input power required to pump that
amount of water in units of gallons per watt-hour
(gal/Wh). The relevant test methods for determining
EF are described in section III.F.
6 In this final rule, DOE is adopting specific test
methods and metrics applicable to DPPP nominal
motor horsepower, DPPP total horsepower, DPPP
service factor, and rated hydraulic horsepower of
dedicated-purpose pool pumps. See section III.G.1
for a discussion of the different horsepower metrics
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horsepower, DPPP service factor, pump
power output (hydraulic horsepower),
and true power factor (PF), DOE also is
adopting provisions regarding allowable
representations of energy consumption,
energy efficiency, and other relevant
metrics manufacturers may make
regarding DPPP performance (section
III.H). DOE is also clarifying the
appropriate use of such metrics through
the use of two appendices: Appendix B,
which contains metrics and test
methods applicable to testing dedicatedpurpose pool pumps prior to the
compliance date of the established
energy conservation standards for such
equipment (i.e., prior to July 19, 2021),
and appendix C, which contains metrics
and test methods applicable to testing
dedicated-purpose pool pumps on or
after the compliance date of any
applicable energy conservation
standards (i.e., on and after July 19,
2021).
Starting on July 19, 2021, the
compliance date for the energy
conservation standards that DOE
established for dedicated-purpose pool
pumps, all dedicated-purpose pool
pumps within the scope of those
standards must be certified in
accordance with the amended subpart Y
of part 431 and the applicable sampling
requirements in 10 CFR 429.59. DOE is
also requiring that, beginning on July
19, 2021, certain certification and
compliance information must be
reported to DOE on an annual basis
(section III.K.2). Similarly, all
representations regarding the energy
efficiency or energy use of dedicatedpurpose pool pumps within the scope of
this DPPP test procedure should be
made by testing in accordance with the
adopted DPPP test procedure (appendix
B) beginning 180 days after the
publication date of this test procedure
final rule in the Federal Register. (42
U.S.C. 6314(d)(1)) DOE understands that
manufacturers of dedicated-purpose
pool pumps likely have historical test
data (e.g., existing pump curves) that
were developed with methods
consistent with the new DOE test
procedure. DOE also understands that
the DPPP test procedure is based on the
same testing methodology used to
generate most existing pump
performance information. Consequently,
DOE does not expect that manufacturers
will need to regenerate all of the
historical test data, as long as the
original rating method is consistent with
the methods adopted in this final rule,
and the original tested units remain
applicable to dedicated-purpose pool pumps and
the adopted testing requirements applicable to these
metrics.
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representative of the basic model’s
current design. If the testing methods
used to generate historical ratings for
DPPP basic models are substantially
different from those adopted in this
final rule or the manufacturer has
changed the design of the basic model,
the representations resulting from the
historical methods would no longer be
valid. This is discussed in more detail
in section III.F.
III. Discussion
In this final rule, DOE amends subpart
Y of 10 CFR part 431 to add a new DPPP
test procedure and related definitions,
amends 10 CFR 429.59 to add a new
sampling plan for dedicated-purpose
pool pumps, and amends 10 CFR
429.110 and 429.134 to add new
enforcement provisions for this
equipment. The amendments are shown
in Table III.1.
TABLE III.1—SUMMARY OF AMENDMENTS IN THIS FINAL RULE, THEIR LOCATION WITHIN THE CODE OF FEDERAL
REGULATIONS, AND THE APPLICABLE PREAMBLE DISCUSSION
Location
Amendment
10 CFR 429.59 ....................
Test Procedure Sampling
Plan and Certification
Requirements.
10 CFR 429.110 & 429.134
Enforcement Provisions ....
10 CFR 431.462 ..................
Definitions ..........................
10 CFR 431.464, Appendix
B, & Appendix C.
Test Procedure ..................
10 CFR 431.466 ..................
Labeling .............................
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The following sections discuss
comments received from interested
parties and DOE’s final adopted
provisions regarding (A) the scope of
this rulemaking; (B) definitions related
to the categorizing and testing of
dedicated-purpose pool pumps; (C) the
metric used to describe the energy
performance of dedicated-purpose pool
pumps; (D) the test procedure for
different varieties of dedicated-purpose
pool pumps; (E) the incorporation of HI
40.6–2014 as the test method for
determining pump performance; (F)
representations of energy use and
energy efficiency; (G) additional test
methods necessary to determine rated
hydraulic horsepower,7 other DPPP
horsepower metrics,8 and the selfpriming capability of dedicated-purpose
pool pumps; (H) labeling requirements
for dedicated-purpose pool pumps; (I)
an optional test method for replacement
DPPP motors; and (J) certification and
enforcement provisions for tested DPPP
models.
7 Rated hydraulic horsepower refers to the
hydraulic horsepower at maximum speed and full
impeller diameter on the reference curve for the
rated pump and is the metric DOE is referencing to
describe the capacity of dedicated-purpose pool
pumps. (See section III.G.1.)
8 DOE is adopting, based on the June 2016 DPPP
Working Group recommendations, standardized
methods for determining nominal motor
horsepower, total horsepower, and service factor of
a dedicated-purpose pool pump to support labeling
provisions. The adopted test methods are discussed
in section III.F and the labeling requirements are
discussed in section III.I.
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Minimum number of dedicated-purpose pool pumps to
be tested to rate a DPPP basic model, determination of representative values, and certification reporting requirements.
Method for DOE determination of compliance of DPPP
basic models.
Definitions pertinent to categorizing and testing of
dedicated-purpose pool pumps.
Instructions for determining the WEF (and other applicable performance characteristics) for applicable varieties of dedicated-purpose pool pumps and replacement DPPP motors.
Requirements for labeling dedicated-purpose pool
pumps.
A. General Comments
CA IOUs submitted a general
comment expressing their support of the
test procedure proposed in the
September 2016 DPPP test procedure
NOPR and stating that the proposal
reflected issues negotiated in the DPPP
Working Group in 2015 and 2016. CA
IOUs also encouraged DOE to publish a
final rule for both the test procedure and
energy conservation standards by the
end of 2016 so that the standards can
take effect as soon as possible. (CA
IOUs, No. 9 at pp. 1–2) DOE appreciates
the support of CA IOUs and has
finalized this test procedure final rule in
2016. DOE addressed the energy
conservation standards recommended
by the DPPP Working Group in the
January 2017 DPPP DFR. 82 FR 5650.
In response to the September 2016
DPPP test procedure NOPR, Hayward
raised concerns on the number of
requests for comment and new items
outside the DPPP Working Group
discussions and the possible need for a
supplemental NOPR (SNOPR).
(Hayward, Public Meeting Transcript,
No. 3 at pp. 5–6) DOE acknowledges
that in the September 2016 DPPP test
procedure NOPR, DOE proposed a new
DPPP test procedure, as well as several
items recommended by the DPPP
Working Group related to DPPP test
procedure, such as definitions and test
methods. In addition, the September
2016 DPPP test procedure NOPR
contained several items recommended
by the DPPP Working Group that are not
PO 00000
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discussion
Summary of additions
Frm 00006
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Section III.K and III.H.
Section III.K.
Section III.B.
Sections III.C, III.D, III.E,
III.H, III.F, and III.J.
Section III.I.
directly related to the DPPP test
procedure, such as labeling and
certification requirements. Finally, the
September 2016 DPPP test procedure
NOPR contained a number of items that
were not directly discussed or
recommended by the DPPP Working
Group, but are necessary to fully
implement DOE’s regulatory framework,
such as a sampling plan for the
determination of representative values
and enforcement requirements.
While DOE recognizes that the
number and breadth of the proposals
contained in the September 2016 DPPP
test procedure NOPR was significant,
DOE maintains that many of the items
are necessary to ensure DOE’s DPPP
regulations, once adopted, are
comprehensive and robust. For
example, the sampling plan provisions
are necessary to describe how to
determine uniform and consistent
representative values from the test
procedure results.
In addition, as discussed at length in
the DPPP Working Group negotiations,
the energy conservation standard
recommended by the DPPP Working
Group contains both performance and
prescriptive requirements for different
varieties of dedicated-purpose pool
pumps, which must be implemented in
a direct final rule. However, such a
direct final rule can only contain the
explicit consensus recommendations of
the DPPP Working Group, since any
additional provisions would not have
the opportunity for public comment
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through the direct final rule process.
Therefore, some items typically
implemented in standards rulemakings,
such as certification reporting
requirements and labeling provisions,
were included in the September 2016
DPPP test procedure NOPR, because,
while they implemented the
recommendations of the DPPP Working
Group, they contained additional details
and minor provisions not explicitly
recommended by the DPPP Working
Group (see section III.I and III.K.2 for
more information on the labeling and
certification provisions, respectively).
Therefore, while DOE understands
that the breadth of the proposals
contained in the September 2016 DPPP
test procedure NOPR may be greater
than typical test procedure NOPRs, DOE
believes that all the proposals are
necessary to fully implement the
recommendations of the DPPP Working
Group and ensure comprehensive and
robust DPPP regulations. In addition,
DOE notes that interested parties had
the opportunity to comment on all
DOE’s proposals in response to the
September 2016 DPPP test procedure
NOPR and DOE has provided answers to
all comments, and, where appropriate,
has amended its proposal in response to
the comments. Therefore, DOE believes
that an SNOPR is not necessary.
In written comments, APSP and
Pentair noted that DOE based the
various efficiency levels considered for
energy conservation standards during
the DPPP Working Group negotiations
on the WEF scores estimated for
individual pump models using data
from the ENERGY STAR Qualified
Products List database. Pentair
commented, and APSP agreed, that
analysis they conducted using actual
test data generated WEF scores that
were different from DOE’s estimates,
sometimes by up to 20 percent. APSP
and Pentair recommended that DOE
reevaluate the various efficiency levels
using actual test data instead of
estimates based on ENERGY STAR data
points. (APSP, No. 8 at p. 2; Pentair, No.
11 at p. 6) DOE interprets APSP and
Pentair’s comments to be specific to
self-priming pool filter pumps, which
are the only variety of pool pump that
are listed in the ENERGY STAR
Qualified Products List database.9
In response to APSP and Pentair, DOE
notes that the tested data points for all
self-priming pool filter pumps were
based on certification data from the
ENERGY STAR Qualified Products List
9 ENERGY STAR maintains a database of certified
products, including pool pumps. See https://
www.energystar.gov/productfinder/product/
certified-pool-pumps/results.
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database, as well as other entities
besides ENERGY STAR. DOE
incorporated certification data from the
CEC (including current and historical
data), APSP, and ENERGY STAR, and
included other data provided by DPPP
manufacturers in DOE’s Self-Priming
Pool Filter Pump database.10 (Docket
No. EERE–2015–BT–STD–0008, No. 94
at pp. 24–30) DOE presumes the data in
these databases to be accurate and
determined in accordance with the
appropriate test procedures. As
discussed further in section III.H, these
test procedures are consistent with the
test procedure recommended by the
DPPP Working Group and adopted by
DOE in this final rule. Therefore, the
data in the ENERGY STAR, CEC, and
APSP databases are deemed to be
consistent with data generated in
accordance with the adopted DPPP test
procedure.
DOE notes that WEF scores used to
establish efficiency levels for singlespeed and two-speed self-priming pool
filter pumps were directly calculated
from actual known test data points at
appropriate load points, and no
mathematical estimations were
employed. However, as discussed in the
DPPP Working Group, DOE
acknowledges that, for variable-speed
self-priming pool filter pumps, the WEF
scores used to establish efficiency levels
considered for energy conservation
standards were mathematically
estimated from certain known test data
points contained in DOE’s database.
(Docket No. EERE–2015–BT–STD–0008,
No. 94 at pp. 26–31)
DOE pursued the mathematical
estimation of WEF scores because the
variable-speed self-priming pool filter
pump performance data contained in
above-mentioned databases does not
always align with the load points (i.e.,
speed settings) needed to evaluate each
pump against the WEF metric.
Specifically, DOE’s mathematical
estimations were derived from a
regression analyses of known variablespeed self-priming pool filter pump data
points. Furthermore, as DOE described
during the DPPP Working Group
meetings, DOE used actual test stand
data provided by DPPP manufacturers to
validate the estimation methodology.
(Docket No. EERE–2015–BT–STD–0008,
No. 94 at pp. 28–34) Ultimately, DOE
publically presented its regression
methodology to the DPPP Working
Group for input and no members of the
DPPP Working Group offered sustained
objections to the methodology or results
10 Docket
No. EERE–2015–BT–STD–0008, No.
102.
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36863
during the Working Group meetings.11
(Docket No. EERE–2015–BT–STD–0008,
No. 94 at pp. 24–34)
In addition, and as discussed in the
DPPP Working Group, DOE
acknowledges that the estimated WEF
scores for variable-speed pumps are
subject to mathematically uncertainty.
As a part of the DPPP Working Group
meetings, DOE mathematically
quantified this uncertainty and
provided the DPPP Working Group with
a revised variable-speed efficiency level
option that would conservatively
account for this uncertainty. (Docket No.
EERE–2015–BT–STD–0008, No. 100 at
pp. 118–121) Ultimately, as a part of
their energy conservation standard
negotiations, the DPPP Working Group
decided not to account for such
uncertainty in the variable-speed
efficiency level. (Docket No. EERE–
2015–BT–STD–0008, No. 92 at pp. 281–
283) Consequently, DOE believes that
the concept of WEF score uncertainty
for variable-speed pumps was well
understood by the DPPP Working
Group, including the commenters.
In general, DOE developed efficiency
level options for the DPPP Working
Group based on the best data and
analytical methods that were available
at the time. In light of the concerns
raised by APSP and Pentair, DOE
reevaluated its variable-speed WEF
estimation methodology, but found no
technical inaccuracies. In the absence of
new data (noting that APSP and Pentair
did not submit to DOE any test data to
substantiate their claims), DOE has no
means to adjust its variable-speed WEF
estimation methodology at this time.
Furthermore, DOE believes that data
uncertainty concerns raised by APSP
and Pentair were sufficiently considered
by the DPPP Working Group, and
adjustment to DOE’s analysis, based on
new test data (if made available), would
not materially impact the
recommendations of the DPPP Working
Group. Therefore, DOE will not
reevaluate self-priming pool filter pump
efficiency levels using new test data, as
recommended by APSP and Pentair.
DOE notes that DOE established energy
conservation standards as part of the
January 2017 DPPP DFR. 82 FR 5650,
5743.
In written comments, Nidec stated
that it believed that there should be a
11 The CA IOUs initially objected to the results of
the regression methodology, saying that previous
CA IOU efforts had gathered data that did not fit
the regression trend presented by DOE. (Docket No.
EERE–2015–BT–STD–0008, CA IOUs, No. 94 at pp.
30–31) In a subsequent meeting the CA IOUs
rescinded their objection and stated that previous
CA IOUs analysis shows the same results as DOE’s
regression methodology. (Docket No. EERE–2015–
BT–STD–0008, CA IOUs, No. 95 at pp. 4–5).
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public comment period for the related
energy conservation standards and
requested information on the timing of
the ECS rulemaking as well as the
opportunity for public review and
comment. (Nidec, No. 10 at p. 4) DOE
notes that the related energy
conservation standards were negotiated
through the DPPP Working Group and
approved by ASRAC,12 and that notice
of all meetings were published in the
Federal Register.13 All meetings were
open and provided opportunity for
public comment. In addition, the public
had 110 days to submit public
comments on the DFR, which were
considered by DOE prior to confirming
the effective date and compliance date
for the energy conservation standards.
82 FR 24218; May 26, 2017.
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B. Definitions
In this final rule, DOE is adopting
definitions for the term dedicatedpurpose pool pump, several subvarieties of dedicated-purpose pool
pumps, and the variations of DPPP
operating speed configurations. DOE is
also adopting definitions pertinent to
categorizing and testing dedicatedpurpose pool pumps in accordance with
the DOE test procedure. In general,
ASAP and NRDC commented that they
agreed with DOE’s proposed definitions.
(ASAP and NRDC, No. 12 at p. 1) DOE
appreciates the support of ASAP and
NRDC. DOE presents these definitions
in the subsequent sections. In addition,
DOE is adopting definitions and
methods for determining several terms
related to describing DPPP capacity,
including ‘‘rated hydraulic
horsepower,’’ ‘‘dedicated-purpose pool
pump nominal motor horsepower,’’
‘‘dedicated-purpose pool pump service
factor,’’ and ‘‘dedicated-purpose pool
pump motor total horsepower.’’ These
terms are discussed in detail in section
III.G.1.
1. Existing Pump Definitions
DOE notes that because dedicatedpurpose pool pumps are a style of
pump, some terms defined at 10 CFR
431.462, as adopted in the January 2016
general pumps test procedure final rule,
also apply to dedicated-purpose pool
pumps, including bare pump,
mechanical equipment, driver, and
control. 81 FR 4086, 4090–4091 (Jan. 25,
2016). In addition, as dedicated-purpose
pool pumps are end suction pumps,
DOE believes the definition for end
suction pump established in the January
12 Docket
No. EERE–2013–BT–NOC–0005, No. 87.
https://www1.eere.energy.gov/buildings/
appliance_standards/standards.aspx?productid=67
and https://www.regulations.gov/docket?D=EERE2015-BT-STD-0008.
2016 general pumps test procedure final
rule also applies to dedicated-purpose
pool pumps. In the January 2016 general
pumps test procedure final rule, DOE
defined ‘‘end suction pump’’ as a singlestage, rotodynamic pump in which the
liquid enters the bare pump in a
direction parallel to the impeller shaft
and on the side opposite the bare
pump’s driver-end. The liquid is
discharged through a volute in a plane
perpendicular to the shaft. 81 FR 4086,
4146 (Jan. 25, 2016). DOE notes that, as
it is referenced in the definition for end
suction pump, the definition for
rotodynamic pump established in the
January 2016 general pumps test
procedure final rule also applies to
dedicated-purpose pool pumps. Id. at
4147.
In the September 2016 DPPP test
procedure NOPR, DOE used the term
‘‘dry rotor’’ as a part of the definition of
pressure cleaner booster pumps. 81 FR
64580, 64591 (Sept. 20, 2016). DOE also
discussed how the term ‘‘dry rotor
pump’’ applies to dedicated-purpose
pool pumps and asserted that, to DOE’s
knowledge, all dedicated-purpose pool
pumps are dry rotor (as defined in the
January 2016 general pumps final
rule 14). 81 FR 64580, 64587 (Sept. 20,
2016) DOE requested comment on the
assertion that all dedicated-purpose
pool pumps are dry rotor pumps.
In written comments, APSP,
Hayward, and Zodiac commented that
all of the dedicated-purpose pool pumps
covered by this rule are typically dry
rotor pumps. (APSP, No. 8 at p.3;
Hayward, No. 6 at p. 1; Zodiac, No. 13
at p. 1) However, APSP and Zodiac also
requested a clearer definition of dry
rotor and wet rotor style pumps. APSP,
No. 8 at p. 3; Zodiac, No. 13 at p. 1)
APSP, Hayward, and Zodiac also
inquired how a wet rotor pump (such as
a pump with a water-cooled motor) may
be impacted by the dry rotor definition.
(APSP, No. 8 at p.3; Hayward, No. 6 at
p. 1; Zodiac, No. 13 at p. 1)
In response to APSP and Zodiac’s
request for clarification regarding the
terms dry rotor and wet rotor, DOE
defined dry rotor and wet rotor pumps
in the January 2016 general pumps test
procedure final rule. 81 FR 4086, 4146
(Jan. 25, 2016). Dry rotor pump means
a pump in which the motor rotor is not
immersed in the pumped fluid.
Conversely, a wet rotor pump is one in
which the motor rotor is immersed in
the pumped liquid. Id. at 4101 (Jan. 25,
2016) The rotor is the portion of the
motor that rotates and provides torque
13 See
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14 DOE defines ‘‘dry rotor pump’’ as a pump in
which the motor rotor is not immersed in the
pumped fluid. 10 CFR 431.462.
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to output shaft (which may be integral
to the rotor). For most motors varieties,
including all known dedicated-purpose
pool pump motors, the rotor is an
internal component of the motor, which
resides inside the motor stator. If any
significant amount of liquid is present
in-between the stator and rotor during
operation, the rotation of the motor rotor
will cause the liquid to surround or
cover the rotor (i.e., immerse it).
Consequently, such a configuration
would be considered a wet rotor pump.
Alternatively, if a dedicated-purpose
pool pump has no significant amount of
liquid between stator and rotor, the
rotation of the rotation will not cause
the liquid to surround or cover the rotor
(i.e., immerse it), and thus such a
configuration would not be considered
a dry rotor pump. DOE notes that the
water-resistance of, or ability to
immerse, the exterior casing of a motor
has no relation to the definition of wet
rotor and dry rotor pump.
DOE believes these definitions are
clear and unambiguous and do not
require further clarification.
Regarding how a wet rotor pump
would be treated under DOE’s new
dedicated-purpose pool pump
regulations, DOE understands that
pressure cleaner booster pumps are the
only variety of dedicated-purpose pool
pump that use the term ‘‘dry rotor’’
within the definition (i.e., a pressure
cleaner booster pump is a dry rotor
pump). Consequently, the test
procedure will only be applicable to dry
rotor pressure cleaner booster pumps, as
non-dry rotor variants would not meet
the definition of a pressure cleaner
booster pump. The remaining varieties
of dedicated purpose pool pumps make
no specification to whether the pump is,
or is not, dry rotor. Consequently, both
dry rotor and non-dry rotor pumps will
meet certain definitions established in
this final rule, and would thus be
subject to the test procedure.
DOE received no other comments
regarding the use of dry rotor, within
the definition of pressure cleaner
booster pump. Therefore, the term dry
rotor pump will remain a part of the
definition of pressure cleaner booster
pump.
Additional definitions from the
January 2016 general pumps test
procedure final rule that apply to
dedicated-purpose pool pumps, include
the definition of basic model (discussed
further in section III.B.8), the definitions
incorporated by reference from HI 40.6–
2014 (discussed further in section
III.E.1), and the definition of selfpriming pump (discussed further in
section III.B.3.a). While other terms may
be applicable to the description of
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dedicated-purpose pool pumps, they are
not referenced in any of the DPPP
definitions or specifications of the DPPP
test procedure.
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2. Definition of Dedicated-Purpose Pool
Pump
Consistent with the recommendations
of the DPPP Working Group, DOE
proposed in the September 2016 DPPP
test procedure NOPR to define
dedicated-purpose pool pump as
follows:
Dedicated-purpose pool pump
comprises self-priming pool filter
pumps, non-self-priming pool filter
pumps, waterfall pumps, pressure
cleaner booster pumps, integral sandfilter pool pumps, integral-cartridge
filter pool pumps, storable electric spa
pumps, and rigid electric spa pumps. 81
FR 64580, 64587 (Sept. 20, 2016).
DOE received no comments in
response to the proposed definition of
dedicated-purpose pool pump.
Therefore, DOE is adopting the
definition of dedicated-purpose pool
pump as proposed in the September
2016 DPPP test procedure NOPR.
In the September 2016 DPPP test
procedure NOPR, DOE also proposed
definitions for each DPPP variety based
on DPPP Working Group
recommendations. These definitions are
discussed in more detail in sections
III.B.3, III.B.4, and III.B.5.
3. Pool Filter Pumps
Pool filter pumps are the most
common style of dedicated-purpose
pool pump. A ‘‘pool filter pump’’ or
‘‘pool circulation pump’’ is typically
used to refer to an end suction style
pump that circulates water through a
pool and filtration system and removes
large debris using a basket strainer or
other device. Consistent with the
recommendations of the DPPP Working
Group, in the September 2016 DPPP test
procedure NOPR, DOE proposed to
define pool filter pump as an end
suction pump that
(a) either:
(1) Includes an integrated basket
strainer, or
(2) does not include an integrated
basket strainer, but requires a basket
strainer for operation, as stated in
manufacturer literature provided with
the pump; and
(b) may be distributed in commerce
connected to, or packaged with, a sand
filter, removable cartridge filter, or other
filtration accessory, so long as the
filtration accessory is connected with
consumer-removable connections that
allow the pump to be plumbed to
bypass the filtration accessory. (Docket
No. EERE–2015–BT–STD–0008, No. 51
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19:37 Aug 04, 2017
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Recommendation #4 at pp. 2–3); 81 FR
64580, 64587 (Sept. 20, 2016).
In the September 2016 DPPP test
procedure NOPR, DOE requested
comment on the proposed definition of
pool filter pump. No comments,
negative or positive, were received
regarding the proposed definition of
pool filter pump. Therefore, in this final
rule, DOE adopts the definition of pool
filter pump as proposed in the
September 2016 DPPP test procedure
NOPR.
a. Definition of a Basket Strainer and
Filtration Accessories
The definition of pool filter pump
includes the use of a basket strainer to
differentiate pool filter pumps from
other varieties of end suction pumps. To
clearly and unambiguously establish
what would be considered a basket
strainer when applying the pool filter
pump definition, the DPPP Working
Group recommended to define ‘‘basket
strainer’’ as ‘‘a perforated or otherwise
porous receptacle that prevents solid
debris from entering a pump, when
mounted within a housing on the
suction side of a pump. The basket
strainer receptacle is capable of passing
spherical solids of 1 mm in diameter,
and can be removed by hand or using
only simple tools. Simple tools include
but are not limited to a screwdriver,
pliers, and an open-ended wrench.’’
(Docket No. EERE–2015–BT–STD–0008,
No. 51 Recommendation #4 at pp. 2–3)
To establish what would be
considered a ‘‘removable cartridge
filter’’ and to differentiate removable
cartridge filters from basket strainers,
the DPPP Working Group recommended
that the definitions of basket strainer
and removable cartridge filter include a
specification for the diameter of
spherical solid that the basket strainer
or filter component is capable of
passing. The DPPP Working Group
recommended a definition for
‘‘removable cartridge filter’’ as ‘‘a filter
component with fixed dimensions that
captures and removes suspended
particles from water flowing through the
unit. The removable cartridge filter is
not capable of passing spherical solids
of 1 mm in diameter, can be removed
from the filter housing by hand or using
only simple tools, and is not a sand
filter. Simple tools include but are not
limited to a screwdriver, pliers, and an
open-ended wrench.’’ (Docket No.
EERE–2015–BT–STD–0008, No. 51
Recommendation #4 at pp. 2–3)
Similarly, to clearly differentiate sand
filters from other filtration apparatuses,
such as basket strainers and removable
cartridge filters, the DPPP Working
Group recommended defining ‘‘sand
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filter’’ as ‘‘a device designed to filter
water through sand or an alternate sandtype media.’’ The definition for sand
filter is intended to include all depth
filters that allow fluid to pass through
while retaining particulates and debris
in a porous filtration medium. In the
DPPP equipment industry, such a filter
is most commonly made with sand, but
could also be made with other media
such as diatomaceous earth. (Docket No.
EERE–2015–BT–STD–0008, No. 58 at
pp. 91–96)
In the September 2016 DPPP test
procedure NOPR, DOE noted that these
definitions are useful in clearly
differentiating different styles of pool
filter pumps, including integral
cartridge-filter and sand-filter pool
pumps, from those that have nonintegral filtration accessories. As such,
DOE proposed adopting the definitions
for basket strainer, removable cartridge
filter, and sand filter, as recommended
by the DPPP Working Group. 81 FR
64580; 64587–88 (Sept. 20, 2016).
In response to the proposed definition
of basket strainer, Pentair submitted a
written comment stating that there is a
possibility of manufacturers using the
1mm size restriction as a loophole to
create a strainer basket with very small
openings, which would not meet DOE’s
definition for pool filter pumps. Pentair
acknowledged that doing so would
significantly limit the utility of the
pump in pool filtration applications.
However, Pentair noted that consumers
could throw away the original basket
strainer and replace it with one that has
more reasonable opening size. (Pentair,
No. 11 at p. 1)
In response, DOE acknowledges
Pentair’s concern regarding the potential
for manufacturers to circumvent the
regulation through adjusting the
opening size on the basket strainer. In
the DPPP Working Group negotiations,
the DPPP Working Group discussed the
opening size as the clearest and most
unambiguous way to differentiate
between basket strainers and removable
cartridge filters. During that discussion,
Hayward raised the possibility that the
filter basket opening size may limit
future design flexibility. DOE responded
that DOE definitions and analysis are
developed around filter basket designs
that are currently available on the
market. DOE also noted that a filtration
apparatus that does not meet the
definition established in this rule could
be considered in a future rulemakings,
if such designs are developed. (Docket
No. EERE–2015–BT–STD–0008, CA
IOUs, DOE, Waterway, and Zodiac, No.
53 at pp. 13–19) Also, as noted by
Pentair, the opening size of the basket
filter directly impacts its utility as a
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filtration device. Therefore, DOE
believes that the market will effectively
discourage manufacturers from
producing pool filter pumps with
ineffective basket filters. However, DOE
will monitor the market as this test
procedure and associated energy
conservation standards take effect and,
if DOE observes any such
circumvention, DOE may reconsider the
definition of basket strainer as
necessary.
DOE received no other comments
related to the proposed definitions of
basket strainer, removable cartridge
filter, or sand filter. Therefore, DOE is
adopting the definitions of these terms
as proposed in the September 2016
DPPP test procedure NOPR.
b. Self-Priming and Non-Self-Priming
Pool Filter Pumps
All pool filter pumps on the market
are either self-priming or non-selfpriming. Self-priming pumps are able to
lift liquid that originates below the
centerline of the pump inlet and, after
initial manual priming, are able to
subsequently re-prime without the use
of external vacuum sources, manual
filling, or a foot valve. In contrast, nonself-priming pumps must be manually
primed prior to start up each time.
Accordingly, self-priming pumps are
constructed in a different manner than
non-self-priming pumps and have
different energy use characteristics.
Specifically, self-priming pool filter
pumps typically incorporate a diffuser
that maintains the prime on the pump
between periods of operation. The
diffuser affects the energy performance
of the pump because it can decrease the
maximum achievable energy efficiency.
In addition, whether a pool filter
pump is self-priming or not also impacts
the typical applications for self-priming
versus non-self-priming pool filter
pumps. Specifically, in the DPPP
equipment industry, self-priming pool
filter pumps are often referred to as
‘‘inground pool pumps’’ and non-selfpriming pool filter pumps are often
referred to as ‘‘aboveground pool
pumps.’’ Accordingly, the DPPP
Working Group proposed to analyze
self-priming and non-self-priming pool
filter pumps separately. (Docket No.
EERE–2015–BT–STD–0008, No. 51
Recommendation #2A at p. 2)
In the September 2016 DPPP test
procedure NOPR, based on feedback
from the DPPP Working Group, DOE
proposed definitions for self-priming
and non-self-priming pool filter pumps,
as well as a method to differentiate the
two. Specifically, in the September 2016
DPPP test procedure NOPR, DOE
proposed the following definitions for
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self-priming and non-self-priming pool
filter pumps:
Self-priming pool filter pump means a
pool filter pump that is certified under
NSF/ANSI 50–2015 15 to be self-priming
or is capable of re-priming to a vertical
lift of at least 5.0 feet with a true
priming time less than or equal to 10.0
minutes, when tested in accordance
with NSF/ANSI 50–2015, and is not a
waterfall pump.
Non-self-priming pool filter pump
means a pool filter pump that is not
certified under NSF/ANSI 50–2015 to be
self-priming and is not capable of repriming to a vertical lift of at least 5.0
feet with a true priming time less than
or equal to 10.0 minutes, when tested in
accordance with NSF/ANSI 50–2015,
and is not a waterfall pump. 81 FR
64580, 64647–68 (Sept. 20, 2016).
The definitions are consistent with
the NSF/ANSI 50–2015 self-priming
designation such that any pumps
certified as self-priming under NSF/
ANSI 50–2015 would be treated as selfpriming pool filter pumps under the
DOE regulations, even if such a pump
was certified based on manufacturer’s
specified or recommended vertical lift
and/or true priming time. However, as
certification with NSF/ANSI 50–2015 is
voluntary, the definitions also adopt
specific criteria in terms of vertical lift
and true priming time that are
applicable to any pool filter pumps not
certified as self-priming under NSF/
ANSI 50–2015. The criterion for vertical
lift is specified as 5.0 feet, consistent
with the NSF/ANSI 50–2015
requirement. This ensures that all pool
filter pumps that can achieve a vertical
lift of 5.0 feet (within the required true
priming time), whether they are
certified with NSF/ANSI or not, would
be considered a self-priming pool filter
pump under DOE’s regulations.
The criterion for true priming time
recommended by the DPPP Working
Group and proposed in the September
2016 DPPP test procedure NOPR is 10.0
minutes, as opposed to the 6 minutes
specified in NSF/ANSI 50–2015. 81 FR
64580, 64589 and 64647 (Sept. 20,
2016). This is because the 6 minute
threshold is a minimum, and
manufacturers believed that some pool
filter pumps that are currently
considered self-priming pool filter
pumps in the industry have true
priming times greater than 6 minutes.
Thus, the DPPP Working Group
believed that 10.0 minutes was more
appropriate and comprehensive. 81 FR
15 NSF International (NSF)/ANSI Standard 50–
2015, (‘‘NSF/ANSI 50–2015’’), ‘‘Equipment for
Swimming Pools, Spas, hot Tubs and Other
Recreational Water Facilities.’’
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64580, 64589 (Sept. 20, 2016). DOE
proposed a vertical lift and true priming
time of 5.0 feet and 10.0 minutes in
order to clearly specify the appropriate
and required level of precision in the
definitions and test method. Id.
DOE notes that these definitions rely
on the NSF/ANSI 50–2015 test method
to determine self-priming capability.
DOE’s test procedure for determining
self-priming capability, including the
incorporation by reference of the NSF/
ANSI 50–2015 test method, is discussed
further in section III.G.2.
The definitions proposed for selfpriming and non-self-priming pool filter
pumps in the September 2016 DPPP test
procedure NOPR also explicitly exclude
waterfall pumps. As discussed in
section III.B.4.a, waterfall pumps are
pool filter pumps and could meet a
definition of either self-priming or nonself-priming, unless explicitly excluded
from those definitions. Because DOE
intended for these pumps to be treated
specifically as waterfall pumps, the
proposed definitions for self-priming
and non-self-priming pool filter pumps
both specifically excluded waterfall
pumps.
DOE notes that, in the January 2016
general pumps test procedure final rule,
DOE already defined the term ‘‘selfpriming pump’’ as a pump that (1) is
designed to lift liquid that originates
below the centerline of the pump inlet;
(2) contains at least one internal
recirculation passage; and (3) requires a
manual filling of the pump casing prior
to initial start-up, but is able to re-prime
after the initial start-up without the use
of external vacuum sources, manual
filling, or a foot valve. 81 FR 4086, 4147
(Jan. 25, 2016). However, in the
September 2016 DPPP test procedure
NOPR, DOE discussed how this
definition is not applicable to
dedicated-purpose pool pumps because
pool filter pumps typically do not
contain a recirculation passage to
accomplish the self-priming function.
Therefore, DOE proposed to revise the
definition of self-priming pump to
ensure the definition of self-priming is
comprehensive and consistent with the
new definitions for self-priming and
non-self-priming pool filter pump.
Specifically, DOE proposed in the
September 2016 DPPP test procedure
NOPR to modify the existing definition
of self-priming pump to also include
self-priming pool filter pumps, in
addition to the other referenced criteria.
81 FR 64580, 64648 (Sept. 20, 2016).
In response to DOE’s proposal, CEC
commented in support of DOE’s
proposal to differentiate self-priming
from non-self-priming pool pumps
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using the NSF/ANSI 50–2015. (CEC, No.
7 at p.2)
During the September 2016 public
meeting, Hayward requested
clarification of the reference to NSF/
ANSI 50–2015 asking if changes are
made to that standard, would
manufacturers be bound to those
changes. (Hayward, Public Meeting
Transcript, No. 3 at p. 20) As stated
during the September 2016 public
meeting, DOE incorporates by reference
a specific edition of a specific standard.
If that standard is updated, DOE would
need to update the reference within
their test procedure. Until such an
update is made, manufacturers are held
to the standard adopted in the DOE test
procedure.
Hayward also submitted a written
comment in response to DOE’s proposed
definition of self-priming and non-selfpriming pool filter pumps. Hayward
recommended that DOE remove the
requirement to test whether a non-selfpriming pump is capable of selfpriming. Hayward stated that requiring
pumps not marketed or sold as selfpriming pumps to be tested for selfpriming capability would be
unnecessarily burdensome. Hayward
recommended that the definition of
non-self-priming pumps be revised to
designate pumps that are ‘‘not marketed
or sold as self-priming,’’ rather than
pumps that are not capable of selfpriming. (Hayward, No. 6 at p.1)
In response to Hayward’s inquiry,
DOE clarifies that manufacturers may
certify their pump models to DOE as
non-self-priming without testing, so
long as manufacturers are certain that
the non-self-priming pump model has
vertical lift (of lack thereof) and true
priming time characteristics consistent
with DOE’s definition of non-selfpriming pool filter pump. That is, the
non-self-priming pump would meet the
definition of non-self-priming, if it were
to be tested in accordance with DOE’s
test method for verifying self-priming
capability (see section III.G.2).
Consequently, manufacturers are not
required to actually test each non-selfpriming pump model to prove that such
a pump is non-self-priming. However,
DOE will use the definition of non-selfpriming pool filter pump and the
additional test method described in
section III.G.2 to ensure that
manufacturers are properly categorizing
their pool filter pumps as either selfpriming or non-self-priming in
accordance with the adopted
definitions. Consequently, DOE believes
that the definition of non-self-priming
pool filter pumps does not introduce
any additional testing burden, as DOE
believes that manufacturers already
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know whether their pumps currently
marketed as ‘‘non-self-priming’’ would
meet the definition established in this
final rule. With no additional burden,
DOE believes that amending the
definition of non-self-priming pool filter
pumps is not warranted. In addition,
DOE notes that establishing a clear,
quantitative threshold to differentiate
self-priming and non-self-priming pool
filter pumps is important to confirm that
the pumps are appropriately
differentiated based on the utility (i.e.,
self-priming capability) they are able to
provide.
Hayward also requested clarification
regarding the definition of self-priming
pool filter pumps. APSP and Hayward
asked if 10 minutes is the maximum
time allowed to reach prime and meet
the self-priming requirement. (APSP,
No. 8 at p. 3; Hayward, No. 6 at p.1)
The proposed definition for a selfpriming pool filter pump allows
manufacturers to meet the definition of
self-priming pool filter pump in one of
two ways. Manufacturers may show that
a pool filter pump is self-priming by
certifying the pool filter pump as selfpriming in accordance with NSF/ANSI
50–2015. Alternatively, manufacturers
may show that a pool filter pump is a
self-priming pool filter pump by
demonstrating that a pump is capable of
re-priming to a vertical lift of at least 5.0
feet with a true priming time of less
than or equal to 10.0 minutes, without
certifying the pump to NSF/ANSI 50–
2015. 81 FR 64580, 64589. The NSF/
ANSI 50–2015 standard does not specify
a maximum true priming time. Section
C.3.5 of NSF/ANSI 50–2015 states that,
‘‘if a pump is to be designated as selfpriming, the true priming time for each
run shall not exceed 6 min or the
manufacturer’s recommended time,
whichever is greater.’’ To certify a
pump’s self-priming capability under
NSF/ANSI 50–2015, a manufacturer
could recommend a true priming time
greater than 10.0 minutes. Under the
proposed definition of self-priming pool
filter pump, if a pool filter pump has
true priming time greater than 10.0
minutes but is certified as self-priming
under NSF/ANSI 50–2015, that pump
would qualify as a self-priming pool
filter pump. However, if the pump is not
certified under NSF/ANSI 50–2015, the
pump must be capable of re-priming to
a vertical lift of 5.0 feet with a true
priming time of less than or equal to
10.0 minutes in order to be classified as
a self-priming pump.
In written comments, Pentair pointed
out that NSF requires pumps to prime
to 10 feet in order to be classified as
‘‘self-priming’’ without listing a
qualifying height, but allows a product
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to be certified as self-priming in the 5
to 10 foot range if accompanied by a
qualifying height and time to prime.
Pentair added that DOE’s proposal does
not require the listing of the qualifying
height and suggested that the definition
of self-priming pump should reflect the
non-qualified definition of 10 feet.
(Pentair, No. 11 at p. 1)
Pentair also disagreed with DOE’s
attempt to separate dedicated-purpose
pool pumps intended for aboveground
and inground applications by using
non-self-priming and self-priming
characteristics, respectively.
Specifically, Pentair argued that there
are many self-priming aboveground
pumps currently in the market that
would become non-viable under DOE’s
proposed definitions. Pentair further
notes that while modifications could be
made to these existing aboveground
pumps to prevent them from priming,
such changes would negatively impact
pump efficiency and reduce energy
savings for this category of non-selfpriming pumps. (Pentair, No. 11 at p. 2)
In response to Pentair’s comments
regarding DOE’s specified vertical lift of
5.0 feet, DOE recommended the vertical
lift of 5.0 feet based on the discussions
and recommendation of the DPPP
Working Group. (Docket No. EERE–
2015–BT–STD–0008, Hayward, No. 79
at pp. 160; Zodiac, No. 79 at pp. 161–
162) DOE notes that, as mentioned
previously, this ensures that all pool
filter pumps that can achieve a vertical
lift of 5.0 feet (within the required true
priming time), whether they are
certified with NSF/ANSI or not, would
be considered a self-priming pool filter
pump under DOE’s regulations. DOE
reviewed NSF/ANSI 50–2015 and notes
that, contrary to Pentair’s comment,
section 6.9.1 of NSF/ANSI 50–2015
requires that the maximum vertical lift
be specified if the pump is designated
as self-priming, as determined in
accordance with section C.3 of NSF/
ANSI 50–2015. NSF/ANSI 50–2015 does
not appear to provide the discretion
indicated by Pentair if the vertical lift is
10 feet. In this final rule, DOE is
adopting a definition specifying a
vertical lift of 5.0 feet, as proposed in
the September 2016 DPPP test
procedure NOPR, to maintain
consistency with NSF/ANSI 50–2015.
In response to Pentair’s comments
regarding the differentiation of selfpriming and non-self-priming pool filter
pumps, DOE proposed to differentiate
these two styles of pool filter pumps
based on the recommendations of the
DPPP Working Group. (Docket No.
EERE–2015–BT–STD–0008, No. 51
Recommendation #2A at p. 2) DOE
acknowledges that one factor associated
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with the differentiation of self-priming
and non-self-priming pool filter pumps
is their ability to service inground pools.
That is, the capability of a pump to selfprime is a fundamental utility
associated with the ability of a pump to
service an inground pool, as the pump
is typically installed on the ground next
to the pool, above the water line of the
pool. Therefore, the pump must be selfpriming in order to reliably circulate
water on a continual basis. Conversely,
pumps serving aboveground pools are
typically installed below the water line
and, therefore, gravity can serve to
maintain the prime in the pump.
Although pumps serving aboveground
pools could be self-priming or non-selfpriming, self-priming pumps do not
provide the same utility to aboveground
pools because they require
modifications that reduce the energy
efficiency benefits that self-priming
pumps provide. Non-self-priming
pumps do not require those
modifications, which benefits the
consumer and provides a distinct utility
to the end user. This utility is a feature
that allows DOE to separate the two
styles of pumps into distinct equipment
classes. In addition, self-priming pumps
are more efficient than non-self-priming
pumps, and merging the product classes
could result in the unavailability of the
feature that non-self-priming pumps
provide. For these reasons, consistent
with the recommendations of the DPPP
Working Group, in this final rule DOE
adopts definitions of non-self-priming
and self-priming pool filter pumps
based on their capability to self-prime.
DOE received no other comments
related to the proposed definitions for
self-priming and non-self-priming pool
filter pumps or the revision to the
definition of self-priming pump
established in the January 2016 general
pumps test procedure final rule.
However, in reviewing the definitions,
DOE notes that the vertical lift and true
priming time should refer to the DOE
test method to verifying self-priming
capability, which DOE is adopting in
this final rule (see section III.G.2) as
opposed to the test method in NSF/
ANSI 50–2015. As discussed in section
III.G.2, DOE’s test method for verifying
self-priming capability incorporates by
reference the test method in section C.3
of NSF/ANSI 50–2015, but also adds
several clarifications and additions to
improve the repeatability and
consistency of the test. DOE believes
this is consistent with the DPPP
Working Group’s intent, whereby a selfpriming pool filter pump would either
be certified with NSF/ANSI 50–2015 or
have the specified vertical lift and true
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priming time. DOE’s self-priming
capability test method is designed to
verify the criteria established by the
DPPP Working Group. Therefore, in this
final rule, DOE is adopting definitions
for self-priming and non-self-priming
pool filter pumps based on certification
with NSF/ANSI 50–2015 and the
criteria recommended by the DPPP
Working Group, as tested pursuant to
the DOE test procedure, with minor
modifications regarding the level of
precision required by the criteria. DOE
is also adopting the changes proposed to
the definition of self-priming pump to
align with the new definitions for selfpriming and non-self-priming pool filter
pumps.
c. Integral Cartridge-Filter and Integral
Sand-Filter Pool Pumps
Most self-priming and non-selfpriming filter pumps are installed in
permanent inground or aboveground
pools. However, a significant market
also exists for temporary pools; e.g.,
inflatable or collapsible pools that can
be deflated or collapsed when not in
use. Although temporary pools also
require dedicated-purpose pool pumps
to circulate and filter the water, these
pools are typically served by a unique
style of dedicated-purpose pool pump
that is exclusively distributed in
commerce with a temporary pool or as
a replacement pump for such a pool.
Some of these pumps are integrally and
permanently mounted to a filtration
accessory such as an integral cartridgefilter or sand-filter. These particular
pumps can only be operated with the
integral filtration accessory inline—the
filtration accessory cannot be plumbed
out for the purposes of testing. The
DPPP Working Group recommended
establishing prescriptive requirements
for these pumps, which requires that
timers be distributed in commerce with
the pumps. (Docket No. EERE–2015–
BT–STD–0008, No. 51,
Recommendation #2B at pp. 1–2) With
a prescriptive standard, the
performance-related metric (i.e., WEF)
and test procedure would not be
necessary and, therefore, not applicable.
To clearly differentiate integral
cartridge-filter and integral sand-filter
pool pumps from other varieties of
dedicated-purpose pool pumps, the
DPPP Working Group recommended
definitions for integral cartridge-filter
pool pump and integral sand-filter pool
pump. The recommended definitions
create differentiation based on the
physical construction of the pump.
(Docket No. EERE–2015–BT–STD–0008,
No. 51 Recommendation #4 at pp. 2–3)
In the September 2016 DPPP test
procedure NOPR, DOE proposed to
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adopt the definitions for integral
cartridge-filter pool pump and integral
sand-filter pool pump recommended by
the DPPP Working Group, with a few
minor changes to use consistent
terminology in both definitions.
Specifically, DOE proposed the
following definitions for integral
cartridge-filter pool pump and integral
sand-filter pool pump:
Integral cartridge-filter pool pump
means a pump that requires a removable
cartridge filter, installed on the suction
side of the pump, for operation; and the
cartridge filter cannot be bypassed.
Integral sand-filter pool pump means
a pump distributed in commerce with a
sand filter that cannot be bypassed. 81
FR 64580, 64590 (Sept. 20, 2016).
APSP stated that the proposed
definitions for integral cartridge-filter
pool pump and integral sand-filter pool
pump are acceptable and consistent
with DPPP Working Group meetings.
(APSP, No. 8 at p. 3) DOE appreciates
APSP’s comment. DOE received no
other comments related to the proposed
definitions for integral cartridge-filter
pool pump and integral sand-filter pool
pump. Therefore, DOE is adopting the
definitions as proposed in the
September 2016 DPPP test procedure
NOPR.
4. Other Varieties of Dedicated-Purpose
Pool Pumps
In addition to pool filter pumps, DOE
identified varieties of dedicated-purpose
pool pumps that are used to drive
auxiliary pool equipment such as pool
cleaners and water features. These
pumps, which include waterfall pumps
and pressure cleaner booster pumps, are
discussed in greater detail in the
following sections.
a. Waterfall Pumps
Within the pool pump industry, a
certain variety of pump exists, which is
specifically intended to pump water for
water features, such as waterfalls. These
pumps are similar in construction to
pool filter pumps, except that they only
have limited head and speed operating
ranges. DOE refers to these pumps as
waterfall pumps. Waterfall pumps meet
the definition of pool filter pump
discussed in section III.B.3.a, but are
always equipped with a lower speed
motor (approximately 1,800 rpm) in
order to provide the specific high flow,
low head characteristics required for
typical water feature applications. Based
on this unique construction and end
user utility, the DPPP Working Group
recommended to differentiate waterfall
pumps from self-priming and non-selfpriming pool filter pumps. (Docket No.
EERE–2015–BT–STD–0008, No. 51
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Recommendation #4 at pp. 2–4) In
accordance with the intent of the
December 2015 DPPP Working Group’s
recommendation, DOE proposed in the
September 2016 DPPP test procedure
NOPR to define waterfall pump as ‘‘a
pool filter pump with maximum head
less than or equal to 30 feet, and a
maximum speed less than or equal to
1,800 rpm.’’ 81 FR 64580, 64590 (Sept.
20, 2016). This definition uses
maximum head and a specific
maximum speed to distinguish waterfall
pumps from other varieties of pool filter
pumps.
During the September 2016 DPPP test
procedure NOPR public meeting,
Pentair pointed out that there was a
minor typo on page 81 FR 64590
regarding the description of waterfall
pumps. Pentair noted that the text read
‘‘the DPPP Working Group agreed that
all currently available waterfall pumps
utilize 4-pole motors, as their low flow
requirements do not necessitate the use
of a higher speed 2-pole motor’’ where
it should actually refer to their low head
requirements, not low flow
requirements. (Pentair, Public Meeting
Transcript, No. 3 at p. 74) APSP and
Pentair reiterated this point in their
written comments, pointing out that it is
the low head requirements that make
use of a higher speed 2-pole motor
unnecessary. (APSP, No. 8 at p. 2;
Pentair, No. 11 at p. 5) DOE agrees with
APSP and Pentair that the statement
should refer to the low head
requirements of waterfall pumps and
that the preamble text in the NOPR was
in error.
DOE received no other comments
related to the proposed definition of
waterfall pump. Therefore, DOE is
adopting the definition of waterfall
pump as proposed in the September
2016 DPPP test procedure NOPR, with
the clarification that the maximum head
value is the value certified to DOE.
b. Pressure Cleaner Booster Pumps
Pressure cleaner booster pumps
provide water pressure that is used to
propel pressure-side pool cleaners along
the bottom of the pool and remove
debris as the cleaner moves. To perform
this task, a pressure cleaner booster
pump must provide high head (i.e.,
pressure) at a low flow.
The DPPP Working Group
recommended that pressure cleaner
booster pumps be included as a variety
of dedicated-purpose pool pump,
subject to the test procedure, and
specifically considered in the analysis
to support potential energy conservation
standards. (Docket No. EERE–2015–BT–
STD–0008, No. 51, Recommendation #1
at p. 1, #2A at p. 2, and #6 at p. 5)
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However, the DPPP Working Group did
not recommend a definition of pressure
cleaner booster pump due to the
difficulty of effectively differentiating
pressure cleaner booster pumps from
other DPPP varieties. (Docket No. EERE–
2015–BT–STD–0008, No. 51
Recommendation #4 at p. 3) Instead, the
DPPP Working Group recommended
that DOE develop an appropriate
definition.
After considering the design,
construction, and performance of
pressure cleaner booster pumps, DOE
determined that the most effective
differentiator for pressure cleaner
booster pumps is the fact that they are
designed and marketed for a specific
pressure-side cleaning application.
Therefore, to effectively differentiate
pressure cleaner booster pumps from
other pump varieties, DOE proposed in
the September 2016 DPPP test
procedure NOPR to define ‘‘pressure
cleaner booster pump’’ as an end
suction, dry rotor pump designed and
marketed for pressure-side pool cleaner
applications, and which may be UL
listed under ANSI/UL 1081–2014,
‘‘Standard for Swimming Pool Pumps,
Filters, and Chlorinators.’’ 81 FR 64580,
65491–92 (Sept. 20, 2016).
In response to definition of pressure
cleaner booster pump proposed in the
September 2016 DPPP test procedure
NOPR, the CA IOUs suggested that DOE
should include the UL listing as a
requirement rather than an illustrative
characteristic. CA IOUs justified this
suggestion, by reasoning that in order to
be used on pools, most local inspection
authorities would want to see the UL
label. (CA IOUs, Public Meeting
Transcript, No. 3 at pp. 18–19)
Conversely, in written comments,
Hayward, APSP, and Zodiac asserted
that the phrase ‘‘be UL listed’’ should
not be included in the definition of
pressure cleaner booster pump as it
would require a manufacturer to work
solely with UL and that DOE should not
seek to require manufacturers to list
pressure cleaner booster pumps in
accordance with a 3rd party, voluntary
standard. (Hayward, No. 6, at p. 2;
APSP, No. 8 at p. 3; Zodiac, No. 13 at
pp. 1–2) Hayward, APSP, and Zodiac
further questioned the benefit of adding
a statement referencing the UL standard
since, while UL 1081 is the de facto
standard and is applicable to all DPPP,
it is not a requirement in the United
States to certify products to the standard
and it does not necessarily distinguish
a pressure cleaner booster pump from a
non-pressure cleaner booster pump. (Id.)
As noted during the September 2016
DPPP test procedure NOPR public
meeting, DOE does not wish to narrow
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or restrict the definition of pressure
cleaner booster pump to only those
pumps UL listed under ANSI/UL 1081,
because DOE is not fully confident that
all pressure cleaner booster pumps
require such a listing in order to be
installed in all pools in the United
States. This understanding is consistent
with Hayward, APSP, and Zodiac’s
written comments suggesting removing
the reference to ANSI/UL 1081
certification. Therefore, because it is
possible that some jurisdictions may not
require such a listing, DOE does not
wish to limit the definition of pressure
cleaner booster pump to pumps with a
UL listing if the pump is in fact
designed and marketed for pressure-side
pool cleaner applications. However,
DOE agrees with CA IOUs that the
majority of jurisdictions require UL
listing for installation of dedicatedpurpose pool pumps, including pressure
cleaner booster pumps, in pools. This is
why DOE believes that such listing is a
useful characteristic to use for
distinguishing pressure cleaner booster
pumps from other end suction pumps
not intended for pools. While helpful,
this reference does not require pressure
cleaner booster pumps to be certified
with UL or any other 3rd party entity.
The controlling criteria for determining
whether a pump meets DOE’s definition
of pressure cleaner booster pump is
whether that pump is designed and
marketed for pressure-side cleaner
applications. As such, DOE believes that
referencing ANSI/UL 1081 certification
continues to be a useful, illustrative
indicator for identifying pressure
cleaner booster pumps, although it is
not mandatory and pressure cleaner
booster pumps may still meet the
definition regardless of whether they are
certified under ANSI/UL 1081 or not.
That is, DOE believes the intended
application of the pump, as indicated by
the pump’s own marketing literature, is
the best indication of whether or not
that pump is a pressure cleaner booster
pump, regardless of whether the pump
is UL listed under ANSI/UL 1081.
APSP, Hayward, and Zodiac also
pointed out in their written comments
that the current edition of ANSI/UL
1081 is the 2016 version of the standard,
not the 2014 version proposed to be
incorporated by reference in the
September 2016 DPPP test procedure
NOPR. (APSP, No. 8 at p.3; Hayward,
No. 6 at pp. 1–2; Zodiac, No. 13 at pp.
1–2) DOE has reviewed ANSI/UL 1081–
2016 and finds it to be similar in
content and intent to the 2014 edition
of the standard. Therefore, in order to
reference the most recent and relevant
version, DOE is incorporating by
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reference ANSI/UL 1081–2016 in this
final rule.
No other comments were received
related to the proposed definition of
pressure cleaner booster pump.
Therefore, for the reasons discussed in
this section and the September 2016
DPPP test procedure NOPR, DOE is
adopting the definition of pressure
cleaner booster pump as proposed in the
September 2016 DPPP test procedure
NOPR, except the adopted definition
references ANSI/UL 1081–2016 instead
of ANSI/UL 1081–2014.
To provide clarity and remove
ambiguity when applying the definition
for pressure cleaner booster pump, DOE
also proposed a definition for ‘‘designed
and marketed’’ that DOE would use
when determining the applicability of
any DPPP test procedure or energy
conservation standards to such pumps.
Specifically, DOE proposed to define
‘‘designed and marketed’’ as meaning
that the equipment is specifically
designed to fulfill the indicated
application and, when distributed in
commerce, is designated and marketed
for that application, with the
designation on the packaging and all
publicly available documents (e.g.,
product literature, catalogs, and
packaging labels). 81 FR 64580, 64647
(Sept. 20, 2016).
In response to this proposal, CA IOUs
expressed concern that the inclusion of
‘‘designed and marketed’’ in the
definition of pressure cleaner booster
pump could create a loophole where
products could be used as pressure
cleaner booster pumps even if not
specifically marketed for that purpose
and, in turn, avoid regulation. (CA
IOUs, Public Meeting Transcript, No. 3
at pp. 23–24) ASAP also commented
that the proposed definition for
designed and marketed seemed to be
narrow, pointing to a scenario where a
pump is designed as a booster pump for
pool applications but is also marketed
by the manufacturer for another
application. ASAP requested
clarification if in this scenario the pump
in question would be required to meet
the standard. (ASAP, Public Meeting
Transcript, No. 3 at pp. 22–23) In
written comments, ASAP and NRDC
also encouraged DOE to attempt to
ensure that the definition for ‘‘designed
and marketed’’ does not contain any
loopholes. Specifically, ASAP and
NRDC supported the definition of
designed and marketed presented in the
regulatory text portion of the September
2016 DPPP test procedure NOPR over
the one presented in the preamble.16
16 The definition of designed and marketed
contained in the preamble (81 FR 64580, 6464592;
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Additionally, ASAP and NRDC
encouraged DOE to consider whether
removing the word ‘‘specifically’’ may
further reduce the possibility for
potential loopholes and suggested
removing the word ‘‘all’’ from ‘‘all
publicly available documents’’ to ensure
pumps are considered pressure cleaner
booster pumps in cases where the
designation is on some publicly
available documents, but not others.
(ASAP and NRDC, No. 12 at pp. 1–2)
Similarly, CA IOUs recommended that
DOE remove the word ‘‘specifically,’’ in
order to address pumps designed for
both pressure cleaner and domestic
water booster pump applications, and
change ‘‘all’’ to ‘‘any’’ publicly available
documents. (CA IOUs, No. 9 at pp. 2–
3)
In response to CA IOUs’ concern
about pumps used as pressure cleaner
booster pumps but not marketed as
such, DOE acknowledges that some
individuals may attempt to use
inappropriate pumps to run pressureside cleaner applications. However, it is
DOE’s understanding that pressure-side
pool cleaners are designed to be paired
with pumps with specific characteristics
(e.g., high head and low flow) and that
manufacturers all design and market
specific pumps intended for this
application. DOE also notes that pumps
without these specific characteristics
would not provide adequate utility in
the pressure-side pool application and
manufacturers would recommend
against the use of such pumps with their
pressure-side cleaners. Therefore, while
DOE acknowledges the concern of CA
IOUs, DOE cannot control the actions of
installers who may select inappropriate
pumps for pressure-side cleaner
applications, and DOE believes that all
pumps appropriate for pressure-side
pool cleaner applications are currently
specifically designed and marketed as
such. DOE will continue to monitor the
market to ensure that this continues to
be the case and that all pumps
appropriate for pressure-side pool
cleaner applications continue to be
characterized as pressure cleaner
booster pumps in the future.
In response to the concerns of ASAP,
NRDC, and CA IOUs regarding the
applicability of the designed and
marketed definition to pumps that may
be marketed for a variety of
applications, in addition to pressureside pool cleaner applications, DOE
agrees with the commenters.
Specifically, all pumps designed and
Sept. 20, 2016) did not exactly match the definition
of designed and marketed proposed in the
regulatory text (Id. at 64647). Specifically, the
preamble definition contained the words
‘‘exclusively’’ and ‘‘solely.’’
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marketed for pressure-cleaner booster
applications should be treated as
pressure cleaner booster pumps,
regardless of any other applications for
which they may be designed and
marketed. DOE acknowledges that the
definition of designed and marketed
that was presented in the preamble of
the September 2016 DPPP test
procedure NOPR (81 FR 64580, 64592)
was slightly different than that
contained in the proposed regulatory
text (Id. at 64647) and may have created
confusion regarding the applicability of
the designed and marketed definition.
Specifically, in the preamble, DOE
discussed defining the term designed
and marketed as meaning that the
equipment is exclusively designed to
fulfill the indicated application and,
when distributed in commerce, is
designated and marketed solely for that
application, with the designation on the
packaging and all publicly available
documents (e.g., product literature,
catalogs, and packaging labels). Id. DOE
notes that the definition presented in
the preamble was incorrect and the
definition presented in the regulatory
text on page 64647 of the NOPR was the
intended definition. DOE believes that
the definition contained in the
regulatory text, which does not refer to
the exclusivity of the design or that the
equipment would be solely marketed for
a specific purpose, is broader and
inclusive of pumps that would be
designed and marketed for pressure-side
cleaner applications in addition to other
applications. However, DOE agrees with
ASAP, NRDC, and CA IOUs, that
removal of the term ‘‘specifically’’
would help clarify this aspect of the
definition. In addition, DOE agrees that
changing from ‘‘all publicly available
documents’’ to ‘‘any publicly available
documents’’ best fulfills the intent of the
definition, as any marketing of a pump
as a pressure cleaner booster pump
would show that the pump is intended
to be treated as a pressure cleaner
booster pump.
Therefore, DOE is defining the term
‘‘designed and marketed’’ as set forth in
the regulatory text of this rule.
5. Storable and Rigid Electric Spa
Pumps
In addition to swimming pools,
dedicated-purpose pool pumps are also
used in spas to circulate and filter the
water and operate water jets. Similar to
swimming pools, spas can range in size
and construction style. Specifically,
spas can be portable or permanent
installations and can be constructed out
of a variety of materials depending on
the installation.
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Permanent, inground spas are
typically constructed similar to small
inground pools and use the same pumps
(i.e., self-priming pool filter pumps
described in section III.B.3.a) to operate
the spa. Conversely, for portable spas, a
specific-purpose pump is typically
distributed in commerce with the
portable spa that is specifically designed
and marketed for portable electric spa
applications only. Such portable electric
spa applications can be further
differentiated into two general
categories: Storable electric spas and
rigid electric spas. A storable electric
spa refers to an inflatable or otherwise
temporary spa that can be collapsed or
compacted into a storable unit. In
contrast, a rigid electric spa is
constructed with rigid, typically more
durable, materials and cannot be
collapsed or compacted for storage.
In the September 2016 DPPP test
procedure NOPR, consistent with the
recommendations of the DPPP Working
Group (Docket No. EERE–2015–BT–
STD–0008, No. 51 Recommendation #4
at p. 3), DOE proposed definitions for
‘‘storable electric spa pump’’ and ‘‘rigid
electric spa pump’’ to effectively
differentiate them from other varieties of
pumps. Specifically, DOE proposed to
define ‘‘storable electric spa pump’’ as
a pump that is distributed in commerce
with one or more of the following: (1)
An integral heater and (2) an integral air
pump. DOE also proposed to define
‘‘rigid electric spa pump’’ as an end
suction pump that does not contain an
integrated basket strainer or require a
basket strainer for operation as stated in
the manufacturer literature provided
with the pump, and meets the following
three criteria: (1) Is assembled with four
through bolts that hold the motor rear
endplate, rear bearing, rotor, front
bearing, front endplate, and the bare
pump together as an integral unit; (2) is
constructed with buttress threads at the
inlet and discharge of the bare pump;
and (3) uses a casing or volute and
connections constructed of a nonmetallic material. 81 FR 64580, 64592–
93 (Sept. 20, 2016).
DOE received no comments negative
or positive related to the proposed
definitions for storable electric spa
pump and rigid electric spa pump.
Therefore, DOE is adopting the
definitions for these terms as proposed
in the September 2016 DPPP test
procedure NOPR.
In addition, DOE notes that the
definitions for storable electric spa
pump, as well as the definitions for
integral cartridge-filter pool pump and
integral sand-filter pool pump (see
section III.B.3.c), all utilize the term
‘‘integral’’ as part of the definition. In
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support of these definitions, the DPPP
Working Group recommended a
definition for integral. (Docket No.
EERE–2015–BT–STD–0008, No. 51
Recommendation #4 at p. 7) In the
September 2016 DPPP test procedure
NOPR, DOE proposed the definition
recommended by the DPPP Working
Group and proposed defining the term
‘‘integral’’ as a part of the device that
cannot be removed without
compromising the device’s function or
destroying the physical integrity of the
unit. 81 FR 64580, 64592–93 (Sept. 20,
2016).
DOE received no comments related to
the proposed definition of the term
‘‘integral.’’ Therefore, DOE is adopting
the definition for integral as proposed in
the September 2016 DPPP test
procedure NOPR.
6. Applicability of Test Procedure Based
on Pump Configuration
In addition to specific definitions, the
DPPP Working Group also discussed
and provided recommendations
pertinent to the scope of applicability of
the DPPP test procedure. Ultimately, the
DPPP Working Group recommended
that the scope of the test procedure be
limited to only the following specific
varieties of dedicated-purpose pool
pumps:
• Self-priming pool filter pumps,
• non-self-priming pool filter pumps,
• waterfall pumps, and
• pressure cleaner booster pumps.
(Docket No. EERE–2015–BT–STD–
0008, No. 51, Recommendations #1,
#2A, and #2B at pp. 1–2;
Recommendation #6 at p. 5)
In addition, although not included in
the December 2015 DPPP Working
Group recommendations, the DPPP
Working Group discussed and
ultimately recommended not
considering a test procedure or
standards for self-priming and non-selfpriming pool filter pumps with a rated
hydraulic horsepower 17 greater than 2.5
hp. (Docket No. EERE–2015–BT–STD–
0008, No. 79 at pp. 33–54)
The DPPP Working Group also
recommended that the test procedure
and reporting requirements be
applicable to all self-priming pool filter
pumps—both those served by singlephase power and those served by threephase power.18 (Docket No. EERE–
17 See section III.G.1 for a discussion of
determination of rated hydraulic horsepower.
18 The Working Group recommended that the
scope of standards for self-priming pool filter
pumps only apply to self-priming pool filter pumps
served by single-phase power, while the
recommended test procedure and reporting
requirements would still be applicable to all selfpriming pool filter pumps—both those served by
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2015–BT–STD–0008, No. 82
Recommendations #3 at p. 2) Consistent
with the DPPP Working Group
recommendations, DOE proposed in the
September 2016 DPPP test procedure
NOPR that the test procedure, sampling
requirements, labeling, and related
provisions for dedicated-purpose pool
pumps apply to all self-priming pool
filter pumps and non-self-priming pool
filter pumps less than 2.5 rated
hydraulic horsepower, as well as
waterfall pumps and pressure cleaner
booster pumps, regardless of the phase
of the supplied power with which they
are intended to be used. 81 FR 64580,
64593 (Sept. 20, 2016).
Consistent with the December 2015
DPPP Working Group
recommendations, in the September
2016 DPPP test procedure NOPR, DOE
also proposed definitions for rigidelectric and storable-electric spa pumps
as a variety of dedicated-purpose pool
pump in this test procedure final rule,
but DOE did not propose test
procedures or reporting requirements
for them.
In the September 2016 DPPP test
procedure NOPR, DOE also specifically
proposed to exclude submersible pumps
from the scope of the DPPP test
procedure and proposed defining a
‘‘submersible pump’’ as a pump that is
designed to be operated with the motor
and bare pump fully submerged in the
pumped liquid. 81 FR 64580, 64594
(Sept. 20, 2016).
In written comments, CEC expressed
support of DOE’s proposal to set the
scope of the test procedure rulemaking
to include self-priming and non-selfpriming pool filter pumps, waterfall
pool pumps, and pressure cleaner
booster pumps. (CEC, No. 7 at p. 2) DOE
appreciates CEC’s support.
In response to DOE’s proposal
regarding the applicability of the
proposed test procedure to dedicatedpurpose pool pumps served by both
single- and three-phase power, Hayward
and APSP requested clarification as to
the scope of the rule and specifically if
it included three-phase dedicatedpurpose pool pumps. (Hayward, No. 6 at
p. 4; APSP, No. 8 at p. 5) Nidec
supported the DPPP Working Group’s
recommendation that any potential
energy conservation standards would
only apply to dedicated-purpose pool
pumps served by single-phase power.
However, Nidec recommended that the
test procedure and reporting
requirements only apply to dedicatedpurpose pool pumps served by singlephase power. Nidec stated that threesingle-phase power and those served by three-phase
power.
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phase motors used with dedicatedpurpose pool pumps are very energy
efficient and are already regulated.
Nidec suggested that three-phase
dedicated-purpose pool pumps and
related motors should not need further
testing nor reporting requirements.
(Nidec, No. 10 at p. 3)
In response to Hayward and APSP’s
request for clarification, DOE clarifies
that, as noted previously and discussed
in the September 2016 DPPP test
procedure NOPR, DOE’s proposed test
procedure would apply to self-priming
pool filter pumps and non-self-priming
pool filter pumps less than 2.5 rated
hydraulic horsepower, as well as
waterfall pumps and pressure cleaner
booster pumps, served by both singlephase power or three-phase power. In
response to Nidec’s comments regarding
the applicability of the proposed DOE
test procedure to three-phase
equipment, DOE believes that the
applicability of the DPPP test procedure
proposed in the September 2016 DPPP
test procedure NOPR is consistent with
the intent of the DPPP Working Group
exhibited in the June 2016 DPPP
Working Group recommendations,
where the Working Group
recommended that the test procedure
and reporting requirements would be
applicable to all self-priming pool filter
pumps served by single- and threephase power. (Docket No. EERE–2015–
BT–STD–0008, No. 82,
Recommendation #3 at p. 2) Although
the June 2016 DPPP Working Group
recommendations reference only selfpriming pool filter pumps, there is no
reason why DOE’s proposed DPPP test
procedure would not be applicable to
other varieties of dedicated-purpose
pool pumps served by single- or threephase power. In addition, the DPPP
Working Group did not recommend
restricting the scope of standards for any
of the other DPPP varieties based on the
phase of power with which it is
intended to be used. However, DOE
agrees with Nidec that three-phase
motors may already be regulated under
existing DOE test procedures and energy
conservation standards for electric
motors and small electric motors. As
discussed further in section III.G.1.b, in
this final rule, DOE is limiting the test
methods for motor horsepower metrics
(i.e., DPPP nominal motor horsepower,
DPPP service factor, and DPPP motor
total horsepower) to single-phase motors
because testing and rating of three-phase
motors is already regulated by DOE.
DOE agrees that, as stated by Nidec,
the applicability of the DPPP test
procedure and standards recommended
by the DPPP Working Group differ
slightly with respect to dedicated-
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purpose pool pumps that are supplied
by single-phase versus three-phase
power. Specifically, the DPPP Working
Group recommended that the scope of
standards for self-priming pool filter
pumps only apply to self-priming pool
filter pumps served by single-phase
power, while the recommended test
procedure and reporting requirements
would still be applicable to all selfpriming pool filter pumps—both those
served by single-phase power and those
served by three-phase power. (Docket
No. EERE–2015–BT–STD–0008, No. 82
Recommendations #3 at p. 2)
In response to the scope of test
procedure and metric applicability
proposed by DOE in the September 2016
DPPP test procedure NOPR, Pentair and
APSP commented that some form of
differentiation or exclusion should be
established for dedicated-purpose pool
pumps with nominal motor horsepower
greater than 3 hp. Pentair suggested that
the metric, as proposed in the NOPR,
potentially limits a manufacturer’s
ability to develop an optimal solution
for these lower head hydraulic systems,
because these pumps are typically
applied to pools with larger plumbing
and do not typically operate on curve C.
Pentair claimed that as a result, these
larger pumps will be eliminated from
the market. (Pentair, No. 11, at p. 2;
APSP, No 8 at pp. 3–4)
As discussed previously in this
section, the DPPP Working Group, of
which Pentair was a member,
recommended that the scope of the test
procedure be limited to self- and nonself-priming pool filter pumps, waterfall
pumps, and pressure cleaner booster
pumps. (Docket No. EERE–2015–BT–
STD–0008, No. 51, Recommendations
#1, #2A, and #2B at pp. 1–2;
Recommendation #6 at p. 5) In the
December 2015 DPPP Working Group
recommendations, the DPPP Working
Group discussed and ultimately
recommended not considering a test
procedure or standards for self-priming
and non-self-priming pool filter pumps
with a rated hydraulic horsepower
greater than 2.5 hp. (Docket No. EERE–
2015–BT–STD–0008, No. 79 at pp. 33–
54) However, the DPPP Working Group
did not recommend any other test
procedure differentiation or exclusions
based on nominal motor horsepower,
nor did the DPPP Working Group ask
DOE to pursue such action. Therefore,
the test procedure and standards
recommended by the DPPP Working
Group were intended to be applicable to
self-priming and non-self-priming pool
filter pumps with rated hydraulic
horsepower less than or equal to 2.5 hp,
which include some pool filter pumps
with a nominal motor horsepower
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greater than 3 hp,19 which are typically
installed into applications with larger
plumbing, for which the test procedure
would not be representative. (Docket
No. EERE–2015–BT–STD–0008, No. 94
at pp. 38–53; Docket No. EERE–2015–
BT–STD–0008, No. 95 at pp. 176–194;
Docket No. EERE–2015–BT–STD–0008,
No. 79 at pp. 39–40, 47–48) In response
to Pentair and APSP, DOE notes that
Pentair and APSP did not introduce any
new data indicating that the cutoff
should actually be a nominal motor
horsepower of 3 hp; rather they simply
indicated this was due to larger
plumbing systems not on curve C,
which the Working Group already
considered in making its cutoff
selection. Finally, the introduction of an
exclusion for pumps with greater than 3
nominal motor horsepower opens a
significant circumvention loophole risk.
For example, manufacturers of pumps
with 3 nominal motor horsepower could
decide to slightly increase the capacity
of the motor (with no change to the bare
pump), in order to avoid being subject
the test procedure and energy
conservation standards. Such a change
on nominal horsepower would have
little impact on the utility or production
cost of such a pump. Alternatively, any
change to a pump’s hydraulic
horsepower rating will directly impact
end-user utility (i.e., flow and head).
Consequently, DOE reaffirms its
conclusion that hydraulic horsepower,
rather than motor horsepower, should
be used to define the upper scope limit,
as hydraulic horsepower is more
directly tied to end-user utility (i.e.,
flow and head) than motor horsepower.
For these reasons, DOE is not adopting
an alternative scope limitation in this
final rule.
DOE did not receive any other
comments regarding the definition of
submersible pump, or the general scope
of applicability of the September 2016
DPPP test procedure NOPR.
Consequently, in this final rule, DOE is
adopting test methods for all selfpriming pool filter pumps and non-selfpriming pool filter pumps less than 2.5
rated hydraulic horsepower, as well as
waterfall pumps and pressure cleaner
booster pumps, including pumps served
by both single- and three-phase power,
with the exclusion of submersible
pumps. The specific test methods for
each of the applicable DPPP varieties
are discussed in more detail in section
III.D.
19 Nominal motor horsepower is approximately
equivalent to the rated hydraulic horsepower
divided by the pump efficiency and the motor
efficiency of the dedicated-purpose pool pump.
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7. Definitions Related to DedicatedPurpose Pool Pump Speed
Configurations and Controls
In addition to definitions of
dedicated-purpose pool pump and the
specific DPPP varieties, DOE also
proposed in the September 2016 DPPP
test procedure NOPR to establish
definitions to further differentiate
certain varieties of dedicated-purpose
pool pumps, based on the speed
configuration of the motor and/or the
presence of controls on the DPPP model
as distributed in commerce. These
definitions are discussed in section
III.B.7.a. For dedicated-purpose pool
pumps distributed in commerce with
applicable pool pump controls, DOE
also proposed a definition for ‘‘freeze
protection controls.’’ This is discussed
in section III.B.7.b.
a. DPPP Speed Configurations
In the June 2016 DPPP Working
Group recommendations, the DPPP
Working Group recommended
definitions for the following DPPP
speed configurations: Single-speed, twospeed, multi-speed, and variable-speed.
(Docket No. EERE–2015–BT–STD–0008,
No. 82, Recommendation #5A at p. 3) In
the September 2016 DPPP test
procedure NOPR, DOE proposed
adopting the DPPP Working Group’s
recommended definitions with a few
minor modifications for clarity and
consistency. 81 FR 64580, 64594–97
(Sept. 20, 2016). Specifically, DOE
proposed the following definitions for
single-speed, two-speed, multi-speed,
and variable-speed dedicated-purpose
pool pump:
• Single-speed dedicated-purpose
pool pump means a dedicated-purpose
pool pump that is capable of operating
at only one speed.
• Two-speed dedicated-purpose pool
pump means a dedicated-purpose pool
pump that is capable of operating at
only two different pre-determined
operating speeds, where the low
operating speed is less than or equal to
half of the maximum operating speed
and greater than zero, and must be
distributed in commerce either: (1) With
a pool pump control (i.e., variable speed
drive and user interface or switch) that
is capable of changing the speed in
response to user preferences; or (2)
Without a pool pump control that has
the capability to change speed in
response to user preferences, but
without which the pump is unable to
operate without the presence of such a
pool pump control.
• Multi-speed dedicated-purpose pool
pump means a dedicated-purpose pool
pump that is capable of operating at
more than two discrete pre-determined
operating speeds separated by speed
increments greater than 100 rpm, where
the lowest speed is less than or equal to
half of the maximum operating speed
and greater than zero, and must be
distributed in commerce with an onboard pool pump control (i.e., variable
speed drive and user interface or
programmable switch) that changes the
speed in response to pre-programmed
user preferences and allows the user to
36873
select the duration of each speed and/
or the on/off times.
• Variable-speed dedicated-purpose
pool pump means a dedicated-purpose
pool pump that is capable of operating
at a variety of user-determined speeds,
where all the speeds are separated by at
most 100 rpm increments over the
operating range and the lowest
operating speed is less than or equal to
one-third of the maximum operating
speed and greater than zero. Such a
pump must include a variable speed
drive and be distributed in commerce
either: (1) With a user interface that
changes the speed in response to preprogrammed user preferences and
allows the user to select the duration of
each speed and/or the on/off times; or
(2) without a user interface but be
unable to operate without the presence
of a user interface.
81 FR 64580, 64647–48 (Sept. 20,
2016).
DOE’s proposed definitions enable
each speed configuration to be
identified based on (1) the number of
operating speeds available to the pump;
(2) the minimum operating speed, or
turn-down ratio,20 of the pump; (3) the
pump’s ability to connect to a pool
pump control; and/or (4) the
characteristics of that pool pump
control. The pool pump control
varieties, pool pump control operating
characteristics, and requirements
regarding the inclusion of pool pump
controls applicable to each DPPP speed
configuration, as proposed in the
September 2016 DPPP test procedure
NOPR, are summarized in Table III.2.
TABLE III.2—SUMMARY OF APPLICABLE POOL PUMP CONTROL VARIETIES AND RELATED PROPOSED REQUIREMENTS FOR
EACH DPPP SPEED CONFIGURATION
DPPP speed configuration
definition
Applicable pool pump control
varieties
Two-Speed .....................................
Multi-Speed ....................................
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Variable-Speed ..............................
• Variable
interface
• Switch
• Variable
interface
• Switch
• Variable
interface
Pool pump control must be
pre-programmable
Inclusion of pool pump controls as
distributed in commerce
speed drive and user
or
No .................................................
Included.
speed drive and user
or
Yes ................................................
Included and on-board.
speed drive and user
Yes ................................................
Included or DPPP model cannot
operate without being installed
with such controls.
CEC, in written comments, supported
DOE’s proposal to establish definitions
for single-speed, two-speed, multispeed, and variable speed pool filter
pumps. (CEC, No. 7 at p. 2) DOE
appreciates the support of CEC.
In response to DOE’s proposed
definitions for two-speed dedicatedpurpose pool pump, Hayward suggested
a modification to the definitional
requirement that two-speed dedicatedpurpose pool pumps not be able to
operate at high speed without the
requisite control, instead of not able to
operate at all. That is, instead of being
unable to operate entirely, two-speed
dedicated-purpose pool pumps could be
allowed to function at a default lowspeed if they are operated without an
appropriate pool pump control.
20 The turn-down ratio for multi-speed pumps,
including two-speed pumps, describes the ability of
the pump to decrease speed relative to the
maximum operating speed and is calculated as the
maximum operating speed over the minimum
operating speed of the pump.
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(Hayward, Public Meeting Transcript,
No. 3 at pp. 21, 26–27) In response to
Hayward’s suggestion, CA IOUs stated
their support for DOE’s originally
proposed provision that does not allow
a two-speed dedicated-purpose pool
pump be considered a two-speed pump
unless it is unable to operate without an
appropriate pool pump control. (CA
IOUs, Public Meeting Transcript, No. 3
at p. 26–27)
In response to Hayward’s suggestion
regarding the definition of two-speed
dedicated-purpose pool pump, DOE
agrees with CA IOUs that the proposed
modification is not consistent with the
recommendations of the DPPP Working
Group. (Docket No. EERE–2015–BT–
STD–0008, No. 82, Recommendation
#5A at p. 3) The specific wording of the
DPPP speed configuration definitions
were discussed at length and in
significant detail during the DPPP
Working Group negotiations and, if fact,
were part of the final negotiation of
standard levels. (Docket No. EERE–
2015–BT–STD–0008, No. 91 at pp. 141–
183; Docket No. EERE–2015–BT–STD–
0008, No. 92 at pp. 215–222)
Specifically, certain members of the
DPPP Working Group voiced concern
that if two-speed dedicated-purpose
pool pumps were distributed in
commerce without any form of control
and were capable of being operated
without such a control, there would be
a significant risk that such pumps
would not be paired with an applicable
pool pump control in the field and
would not achieve the performance and
potential energy savings represented by
the WEF metric. (Docket No. EERE–
2015–BT–STD–0008, No. 91 at pp. 141–
183) DOE believes that if a two-speed
dedicated-purpose pool pump is
capable of operating, even at low speed,
without an applicable pool pump
control, this significantly increases the
risk that two-speed pool filter pumps
would be installed and operated
without an appropriate control. As the
two-speed dedicated-purpose pool
pump test points presume a low flow
and high flow test point, the two-speed
dedicated-purpose pool pump test
procedure is only appropriate and
representative of two-speed dedicatedpurpose pool pumps with controls that
enable operation at both speeds.
Therefore, to ensure that the test points
and resultant WEF metric for two-speed
dedicated-purpose pool pumps is
representative of actual performance of
the equipment in the field, DOE is
adopting the definition for two-speed
dedicated-purpose pool pump proposed
in the September 2016 DPPP test
procedure NOPR. Furthermore, DOE
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notes that the two-speed dedicatedpurpose pool pump definition does not
restrict DPPP manufacturers from
producing a pump that has two
operating speeds and can only be
operated at low speed without an
appropriate control, as described by
Hayward. However, in such a case the
pump would not meet the definition of
two-speed dedicated-purpose pool
pump and, therefore, would be tested
and subject to standards based on the
single-speed dedicated-purpose pool
pump test points. See section D.1 for
more discussion regarding the specific
test points for the different DPPP speed
configurations.
In response to DOE’s definition of a
two-speed dedicated-purpose pool
pump, Hayward and APSP also
requested clarification regarding the
meaning of the phrase ‘‘unable to
operate.’’ (Hayward, No. 6 at pp. 2;
APSP, No. 8 at p. 3) DOE clarifies that
the phrase ‘‘unable to operate’’ means
that the pump is non-operational and
could not be used to circulate water in
a pool. That is, the pump is unable to
provide any flow or head, and consumes
no energy.
Hayward and APSP also requested a
better definition of the term ‘‘pool pump
control.’’ Hayward and APSP both
commented that the two-speed
dedicated-purpose pool pump
definition includes a parenthetical
‘‘(i.e., variable speed drive and user
interface or switch)’’ that implies the
only two options for a pool pump
control are a switch or a variable speed
drive and user interface. (Hayward, No.
6 at pp. 2; APSP, No. 8 at p. 3)
DOE recognizes that the use of the
abbreviation ‘‘i.e.’’ 21 was used in error,
and may have caused confusion. DOE’s
intent was to use the abbreviation
‘‘e.g.,’’ 22 which would signify that a
variable speed drive and a user interface
or switch were just two examples of
possible technologies. That said, the
phrase ‘‘pool pump control’’ is not
explicitly defined in this final rule and
a pool pump control is not limited to
the two options used as examples. DOE
interprets the phrase ‘‘pool pump
control’’ as a general term that
encompasses any technology that is
capable of changing the speed in
response to user preferences. To clarify
DOE’s original intent, DOE has modified
the definition of two-speed dedicatedpurpose pool pump to replace ‘‘i.e.’’
with ‘‘e.g.’’
21 Latin for ‘‘id est.’’ Meaning ‘‘that is.’’ https://
www.merriam-webster.com/dictionary/i.e.
22 Latin for ‘‘exempli gratia.’’ Meaning ‘‘for
example.’’ https://www.merriam-webster.com/
dictionary/e.g.
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Similarly, Davey commented that the
proposed definition for variable-speed
dedicated purpose pool pumps may
hinder innovation of pump products
that do not require additional
controllers. For example, Davey
suggested that a dedicated-purpose pool
pump, with no pool pump control, but
which enables the user to set a duration
of operation at high speed and then
default to low speed operation might
improve efficiency. Davey also noted
that, under the proposed definition of
variable-speed dedicated-purpose pool
pump, a user could program the pump
to run at the highest speed all the time.
(Davey, No. 5 at pp. 2–3)
DOE notes that Davey’s comment
describes a configuration where a pump
is capable of operating at a high speed
and a low speed and is capable of
programming the duration of each speed
in response to user preferences. Such a
configuration would meet the proposed
definition of a two-speed dedicatedpurpose pool pump. As described
above, DOE proposed that a two-speed
dedicated-purpose pool pump be
defined as a dedicated-purpose pool
pump that is capable of operating at
only two different, pre-determined
operating speeds, where the low
operating speed is less than or equal to
half of the maximum operating speed
and greater than zero, and must be
distributed in commerce either: (1) With
a pool pump control (i.e., variable speed
drive and user interface or switch) that
sets the speed in response to user
preferences or (2) without a pool pump
control that has such capability but is
unable to operate without the presence
of such a pool pump control. 81 FR
64580, 64594 (Sept. 20, 2016). As noted
previously, DOE, in this final rule, is
altering the definition to refer to the
variable speed drive and user interface
or switch as illustrative examples with
the term ‘‘e.g.’’ and any pool pump
control capable of operating in the
manner described in the definition
would meet DOE’s definition of twospeed dedicated-purpose pool pump,
regardless of the control’s technology.
The DPPP Working Group discussed
the definition of variable-speed
dedicated-purpose pool filter pumps,
and took care to craft a definition that
is sufficiently broad so as to not restrict
innovation. Working Group members
agreed that the definition should not
specify whether the pool pump
controller is attached to or detached
from the motor, and the definition
should not specify whether the control
is sold with the pump or sold separately
from the pump. (Docket No. EERE–
2015–BT–STD–008, No. 91 at pp. 164–
166) Based on recommendations from
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the DPPP Working Group, DOE
proposed that a variable-speed drive be
defined as equipment capable of varying
the speed of the motor. 81 FR 64580,
64596 (Sept. 20, 2016) This definition is
very broad, and it only limits the
available technologies to the extent that
is required to describe the utility
inherent in a variable-speed dedicated
purpose pool pump. Similarly, the
September 2016 DPPP test procedure
NOPR implicitly defines a user interface
as a device that changes the speed in
response to pre-programmed user
preferences and allows the user to select
the duration of each speed and/or the
on/off times. 81 FR 64580, 64595 (Sept.
20, 2016) This definition is also broad,
and is only limited to the extent
necessary to capture the required
functionality of variable-speed
dedicated-purpose pool pumps. Based
on these points, DOE believes that the
definition of a variable-speed dedicatedpurpose pool filter pump is sufficiently
broad to allow a range of technologies
and innovative approaches, while
ensuring that any such technologies
would still provide the utility of a
variable-speed dedicated-purpose pool
pump consistent with the intent of the
DPPP Working Group.
DOE understands that equipment
covered by standards change as
manufacturers add new features to their
products and update their designs. DOE
will monitor the DPPP market for
changes in equipment and technology.
In the future, DOE may amend the
definitions of any of DPPP varieties or
speed configurations, or include new
varieties of dedicated-purpose pool
pumps, if necessary. In the meantime,
manufacturers may apply for a test
procedure waiver if they develop a
pump that meets the intent of the
variable-speed DPPP definition but does
not meet all of the definition’s criteria.
In general, any interested party may
submit a petition for a test procedure
waiver for a basic model of a covered
product if the basic model’s design
prevents it from being tested according
to the test procedures or cause the
prescribed test procedures to evaluate
the basic model in a manner so
unrepresentative of its true energy
consumption characteristics as to
provide materially inaccurate
comparative data. Additional details on
the petition for waiver process are
available at 10 CFR 431.401 and at
https://energy.gov/eere/buildings/testprocedure-waivers.
In addition, in reviewing the
proposed definitions, DOE also noticed
that the proposed definition for twospeed dedicated-purpose pool pump
was grammatically incorrect. In this
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final rule, DOE is correcting the
grammatical error, which does not affect
the intent or substance of the definition.
Specifically, the proposed definition
contained the final clause ‘‘but without
which the pump is unable to operate
without the presence of such a pool
pump control,’’ which this final rule
adopts as modified to read ‘‘but is
unable to operate without the presence
of such a pool pump control’’ in this
final rule.
Similarly, in reviewing the variablespeed DPPP definition, DOE noticed
that the last phrase refers generically to
a ‘‘user interface’’ when it is intended to
refer to a user interface with specific
characteristics and capabilities, as
referenced in the previous clause in the
definition. Therefore, in this final rule,
DOE is modifying the definition to
clarify that the definition is, in all
places, referring to a user interface that
changes the speed in response to preprogrammed user preferences and
allows the user to select the duration of
each speed and/or the on/off times. This
ensures that the two clauses in the
definition are mutually exclusive. DOE
is also updated the terminology in the
second clause to be grammatically
correct, consistent with the definition of
two-speed dedicated-purpose pool
pump. That is, DOE adopts a definition
with the final clause in the definition to
read ‘‘without a user interface that
changes the speed in response to preprogrammed user preferences and
allows the user to select the duration of
each speed and/or the on/off times, but
is unable to operate without the
presence of a user interface.’’
In addition to proposing definitions of
the various DPPP speed configurations,
in the September 2016 DPPP test
procedure NOPR, DOE proposed to
define variable-speed drive to mean
equipment capable of varying the speed
of the motor. 81 FR 64580, 64594–64597
(Sept. 20, 2016). This definition was
intended to clarify and support the
proposed definitions for two-speed,
multi-speed, and variable-speed
dedicated-purpose pool pump.
DOE received no comments regarding
the proposed definition of variablespeed drive. Therefore, DOE is adopting
the definition for variable speed drive as
proposed in the September 2016 DPPP
test procedure NOPR.
b. Freeze Protection Controls
DPPP Working Group recommended
additional prescriptive requirements for
dedicated-purpose pool pumps
distributed in commerce with ‘‘freeze
protection controls.’’ (Docket No. EERE–
2015–BT–STD–0008, No. 82,
Recommendation #6A at p. 4). Freeze
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protection controls are controls that, at
a certain ambient temperature, turn on
the dedicated-purpose pool pump to
circulate water for a period of time to
prevent the pool and water in plumbing
from freezing. These prescriptive freeze
control requirements are discussed in
section III.H.
To identify dedicated-purpose pool
pumps with freeze protection controls,
DOE proposed in the September 2016
DPPP test procedure NOPR to define
freeze protection controls as pool pump
controls that, at a certain ambient
temperature, turn on the dedicatedpurpose pool pump to circulate water
for a period of time to prevent the pool
and water in plumbing from freezing. 81
FR 64580, 64597 (Sept. 20, 2016).
DOE received no comments related to
the proposed definition of freeze
protection controls. Therefore, DOE is
adopting the definition of freeze
protection controls as proposed in the
September 2016 DPPP test procedure
NOPR. DOE did receive comments
related to the proposed test method for
verifying the presence and operation of
freeze protection controls, which are
discussed in section III.K.3.
8. Basic Model
For purposes of certification,
compliance, and enforcement, DOE
generally applies its energy
conservation standards to ‘‘basic
models’’ of consumer products and
commercial and industrial equipment.
For the purposes of applying the DPPP
regulations, DOE proposed in the
September 2016 DPPP test procedure
NOPR to define what constitutes a
‘‘basic model’’ of a dedicated-purpose
pool pump. 81 FR 64580, 64597 (Sept.
20, 2016). Applying this basic model
concept allows manufacturers to group
similar models within a basic model to
minimize testing burden, while
ensuring that key variables that
differentiate DPPP energy performance
and/or utility are maintained as separate
basic models.
In the September 2016 DPPP test
procedure NOPR, DOE proposed
adopting only the provisions of the
current pump basic model definition
that are applicable to dedicated-purpose
pool pumps, which includes all units of
a given product or equipment type (or
class thereof) manufactured by one
manufacturer, having the same primary
energy source, and having essentially
identical electrical, physical, and
functional (or hydraulic) characteristics
that affect energy consumption, energy
efficiency, water consumption, or water
efficiency. 81 FR 64580, 64597 (Sept.
20, 2016). Procedurally, to apply the
basic model concept to dedicated-
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purpose pool pumps, DOE proposed to
amend the definition of ‘‘basic model’’
for pumps that currently exists at 10
CFR 431.462, as established in the
January 2016 general pumps test
procedure final rule to also
accommodate dedicated-purpose pool
pumps. 81 FR 4086 (Jan. 25, 2016). The
current pumps basic model definition
contains several specific
accommodations regarding number of
stages for multistage pumps and
trimmed impellers and is applicable
only to those general pumps that were
the subject of the January 2016 general
pumps test procedure final rule.
Consequently, DOE proposed amending
the definition to clarify that the
multistage pump and trimmed impeller
provisions were only applicable to
pumps subject to the test procedure
established in the January 2016 general
pumps test procedure final rule. 81 FR
64580, 64597 (Sept. 20, 2016).
In response to DOE’s proposed
definition of basic model for dedicatedpurpose pool pumps, DOE received
several comments regarding how
different individual models could be
grouped under the basic model
provisions. Waterway commented that
sometimes a single individual model
has identical functional characteristics
to several other individual models, and
asked whether such individual models
may be grouped within the basic model.
(Waterway, Public Meeting Transcript,
No. 3 at p. 95)
In response to Waterway’s comment,
as discussed in the September 2016
DPPP test procedure NOPR public
meeting, models that have identical
electrical, physical, and functional (or
hydraulic) characteristics that affect
energy consumption, energy efficiency,
water consumption, or water efficiency,
fall within the same basic model for the
purposes of DOE certification, even if
they have different unique model
numbers in the manufacturer’s
catalogue. In such a case, a
manufacturer would just list all the
unique individual model numbers to
which a given basic model certification
applied in the certification report
submitted to DOE. (See section III.K.2
for more information on certification
reporting requirements.)
Pentair expressed concern regarding
using a basic model in certifying
products to DOE, stating that, in the
ENERGY STAR database, when models
are grouped under a single certification,
utilities often do not recognize models
that do not appear in the main column
listing the basic models. Pentair stated
that this makes it necessary to list each
unit separately in the ENERGY STAR
database, even if the performance is
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similar. (Pentair, Public Meeting
Transcript, No. 3 at pp. 32–33)
In response to Pentair’s comment,
DOE notes that it is at the
manufacturer’s discretion to group
individual models into a single basic
model to reduce testing and certification
burden or to test and certify each
individual model as a unique basic
model. Regardless of whether a
manufacturer chooses to group
individual models into a basic model for
purposes of certification, the
manufacturer would still be required to
specify in its certification the individual
model numbers that fall within the basic
model certified, and any representations
regarding an individual model made in
a certification report must be consistent
with representation as to that individual
model made to ENERGY STAR.
Hayward inquired if the same wet end
is used within a family, but the
horsepower of the motor and impeller
size changes, such individual models
could be grouped within the same basic
model. (Hayward, Public Meeting
Transcript, No. 3 at pp. 31–32) Hayward
and APSP also requested clarity on the
verbiage of the definition as well as
examples from other products. Hayward
and APSP asked whether the same
product but with a different name or
label for specific customers would be
the same ‘‘basic model.’’ Finally,
Hayward and APSP requested
elaboration on whether a single or
multi-stage pump within the same
performance category and WEF criteria
are considered within the same basic
model. (Hayward, No. 6 at p. 2; APSP,
No.8 at p. 4)
In response to Hayward and APSP’s
inquiry, DOE notes that, consistent with
DOE’s practice with other products and
equipment, DPPP manufacturers may
elect to group individual pump models
that are similar, but not identical, into
the same basic model to reduce testing
burden, provided all representations
regarding the energy use of pumps
within that basic model are identical
and based on the most consumptive
unit. See 76 FR 12422, 12423 (March 7,
2011).23 However, all individual models
23 These provisions allow manufacturers to group
individual models with essentially identical, but
not exactly the same, energy performance
characteristics into a basic model to reduce testing
burden. Under DOE’s certification requirements, all
the individual models within a basic model
identified in a certification report as being the same
basic model must have the same certified efficiency
rating and use the same test data underlying the
certified rating. The compliance, certification, and
enforcement (CCE) final rule also establishes that
the efficiency rating of a basic model must be based
on the least efficient or most energy consuming
individual model (i.e., put another way, all
individual models within a basic model must be at
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represented by the same basic model
must be in the same equipment class.24
DOE notes that because standards
recommended by the DPPP Working
Group in the June 2016 DPPP Working
Group recommendations and adopted
by DOE in the January 2017 DPPP DFR
differentiate and assign different
standards to dedicated-purpose pool
pumps based on their rated hydraulic
horsepower, this limits the ability of
manufacturers to group individual DPPP
models that vary in capacity. (Docket
No. EERE–2015–BT–STD–0008,
Recommendation #1, No. 82 at p. 1; 82
FR 5650, 5743) DOE agrees with
Hayward and APSP that a product with
different names or labels that is
otherwise the same could be grouped
within a basic model. Examples from
other products and equipment include
appliances with varying finishes
grouped into one basic model;
refrigerators with varying door opening
sides grouped into one basic model, or
air conditioners of varying voltages
grouped into one basic model. DOE
notes that the example related to all
stage versions of a multi-stage pump
being required to be in the same basic
model is a specific requirement for
general pumps that DOE does not apply
to dedicated-purpose pool pumps.
No additional comments were
received pertaining to DOE’s proposal to
adopt the general provisions of the
general pumps basic model definition.
Therefore, DOE is adopting the changes
to the definition of basic model in 10
CFR 431.462, as proposed in the
September 2016 DPPP test procedure
NOPR.
C. Rating Metric
Overall, the key objectives of any
DPPP metric are that it (1) be objectively
measurable, (2) be representative of the
energy use or energy efficiency of
dedicated-purpose pool pumps, (3)
provide an equitable differentiation of
performance among different DPPP
models and technologies, (4) be able to
compare the energy efficiency of a given
DPPP model to a minimum standard
level, and (5) provide the necessary and
sufficient information for purchasers to
make informed decisions regarding
DPPP selection.
As described in the September 2016
DPPP test procedure NOPR, the DPPP
Working Group focused on defining a
performance-based metric that is similar
to the energy factor (EF) metric
currently used to describe DPPP
least as energy efficient as the certified rating). 76
FR at 12428–29 (March 7, 2011).
24 DOE believes this is what Hayward is referring
to in their comment when they refer to
‘‘performance category and WEF criteria.’’
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36877
DOE agrees with the DPPP Working
Group that the recommended WEF
metric, as shown in equation (1),
provides a representative, objective, and
informative characterization of DPPP
performance. Consequently, in the
September 2016 DPPP test procedure
NOPR, DOE proposed to adopt the WEF
metric as the performance-based metric
for representing the energy performance
of certain styles of dedicated-purpose
pool pumps.
In the September 2016 DPPP test
procedure NOPR, DOE requested
feedback on the proposed metric. CEC
stated in written comments that CEC
supported DOE’s proposal to establish a
weighted energy factor metric. (CEC, No.
7 at p. 2)
APSP and Hayward commented that
they believe that equation (1) in the
September 2016 DPPP test procedure
NOPR (81 FR 64580, 64600),26 which is
used to determine WEF, does not
correctly result in the weighting of
energy factors at the specified load
points. (APSP, No. 8 at p. 4; Hayward,
No. 6 at pp. 2–3) Instead, APSP and
Hayward proposed using the following
equation (2), with all variables as
defined previously:
DOE responds that equation (1), as
published in the September 2016 DPPP
test procedure NOPR, correctly
describes the efficiency of DPPP
equipment and aligns with the
recommendation of the DPPP Working
Group. (Docket No. EERE–2015–BT–
STD–0008, No. 51, Recommendation #5
at p. 4) DOE notes that the DPPP
Working Group evaluated both methods
of calculating WEF, both the proposed
equation (1) and equation (2), as
recommended by APSP and Hayward.
(Docket No. EERE–2015–BT–STD–0008
No. 49 at pp. 6–9; Docket No. EERE–
2015–BT–STD–0008 No. 56 at pp. 24–
60) The DPPP Working Group
ultimately chose to use equation (1)
because it is more representative of the
energy savings to the customer. (Docket
No. EERE–2015–STD–0008 No. 50 at p.
3) Equation (2) is a weighting of the EF
values, which results in an exaggeration
of the benefits of multi-speed and
variable-speed technologies, while
equation (1) is a ratio of the amount of
water pumped over the amount of
energy consumed over a given period of
time in real-world applications. (Docket
No. EERE–2015–BT–STD–0008 No. 56
at pp. 29, 38, 60) That is,
mathematically, weighting the EF values
directly, as shown in equation (2),
results in a weighted average of the flow
values in the numerator, but equal
weighting of the denominator values,
meaning the flow at high speed is given
more weight than the associated power
value at high speed. To illustrate this,
the calculation of WEF, with both
equations, for a two-speed, multi-speed,
or variable-speed dedicated-purpose
pool pump with both a low speed and
high speed test point is shown in
equation (3).
25 As described in the September 2016 DPPP TP
NOPR, EF is used by California Title 20, APSP, and
ENERGY STAR to describe DPPP performance. 81
FR 64580, 64598–64600 (Sept. 20, 2016).
26 Equation (1) in the September 2016 DPPP TP
NOPR is identical to equation (1) in this document.
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depending on the specific DPPP variety
and speed configuration, as shown in
equation (1). The specific load points
and weights for each DPPP variety are
discussed in section III.D.
ER07AU17.000
Working Group recommended using the
WEF, which is defined as the ratio of
the volumetric flow provided by the
pump, divided by the input power to
the pump, at one or more load points,
where these load points are selected
Where:
WEF = weighted energy factor in kgal/kWh;
wi = weighting factor at each load point i;
Qi = flow at each load point i in gpm;
Pi = input power to the motor (or controls,
if present) at each load point i in W;
i = load point(s), defined uniquely for each
DPPP variety; and
n = number of load point(s), defined
uniquely for each speed configuration.
(Docket No. EERE–2015–BT–STD–0008, No.
51 Recommendation #5 at p. 4)
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performance by many existing
programs,25 but that also accounts for
the potential energy savings of
equipment with multiple operating
speeds. 81 FR 64580, 64597–64601
(Sept. 20, 2016). Ultimately, the DPPP
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Conversely, equation (1) correctly
accounts for the amount of power it
takes to provide a given amount of flow.
That is, equation (1) reflects the more
realistic case where a pump provides a
low flow rate for an associated amount
of power during a portion of the day and
a high flow rate for an associate amount
of power during another portion of the
day. If one were to calculate the ‘‘total
daily WEF,’’ one would sum the flow
rates throughout the day and the power
consumption throughout the day and
take a ratio of the two; both power and
flow values would be weighted
according to their proportional use
during the day. Therefore, equation (1)
is more representative of the energy
efficiency of dedicated-purpose pool
pumps over a typical cycle of use.
During the September 2016 DPPP test
procedure NOPR public meeting, CA
IOUs inquired about including standby
power as part of the metric for
dedicated-purpose pool pumps. (CA
IOUs, Public Meeting Transcript, No. 3
at pp. 91–92) In response to CA IOUs
inquiry, DOE explained that standby
power was discussed during the DPPP
Working Group meetings and,
ultimately, the DPPP Working Group
decided not to include standby power in
the WEF metric due to the negligible
impact any standby power
measurements would have on the final
WEF value. (Docket No. EERE–2015–
BT–STD–0008, No. 95 at pp. 229–30)
Consistent with the DPPP Working
Group recommendations, DOE did not
propose to include standby power
measurements nor reporting in the
September 2016 DPPP test procedure
NOPR. While DOE appreciates that
some dedicated-purpose pool pumps
with controls will consume standby
power in their idle state and the desire
to minimize this energy consumption,
DOE does not believe the additional
burden associated with dedicated
testing and reporting requirements
would be justified. Specifically, testing
of standby power for dedicated-purpose
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pool pumps would require an additional
test method and may require different or
more specialized power measurement
equipment to accurately capture the low
power during standby operation.
Furthermore, as the DPPP Working
Group did not recommend specific
requirements for standby energy
consumption, such testing would only
be informative and would not be
necessary to determine compliance of
dedicated-purpose pool pumps. DOE
does not believe the additional burden
associated with establishing test
requirements to measure standby energy
use of dedicated-purpose pool pumps is
justified at this time. Therefore, in this
final rule, DOE is not adopting testing
or reporting requirements for standby
power of dedicated-purpose pool
pumps.
In addition to WEF, in the September
2016 DPPP test procedure NOPR, DOE
also proposed an optional test method
for EF at multiple speeds and/or system
curves and to allow manufacturers and
industry to continue to describe the
energy performance of dedicatedpurpose pool pumps using the EF
metric. 81 FR 64580, 64627–64628
(Sept. 20, 2016). DOE typically only
includes one primary energy metric, the
DOE metric that is used for the energy
conservation standards, in the test
procedure to ensure standardization of
efficiency representations throughout
the industry and eliminates potential
confusion in the market place if
multiple non-equivalent metrics are
used to describe the same piece of
equipment. However, in this specific
case, DOE departed from typical
practice due to the interest expressed in
the use of the EF metric during the
DPPP Working Group negotiations. DOE
notes that, as discussed in more detail
in section III.F, representations of EF
will only be allowed until July 19, 2021,
the compliance date of standards for
dedicated-purpose pool pumps and, if
made, must be accompanied by a
representation of the DOE metric, WEF.
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D. Test Methods for Different DPPP
Categories and Configurations
As discussed in section III.C, DOE
will characterize the performance of
dedicated-purpose pool pumps
according to the WEF. Due to
differences in equipment design and
typical use profiles, the DPPP Working
Group recommended that unique
weights and load points be specified for
each DPPP variety and pump speed
configuration. Based on the
recommendations of the DPPP Working
Group, in the September 2016 DPPP test
procedure NOPR, DOE proposed unique
load points for the various speed
configurations (e.g., single-speed, twospeed, multi-speed, or variable-speed
dedicated-purpose pool pumps) of selfpriming and non-self-priming pool filter
pumps with a rated hydraulic
horsepower less than 2.5 hp (section
III.D.1). DOE also proposed unique load
points for waterfall pumps (section 0)
and pressure cleaner booster pumps
(section III.D.3), each of which reference
only a single load point. 81 FR 64580,
64601–64602 (Sept. 20, 2016). The load
points for self-priming and non-selfpriming pool filter pumps, waterfall
pumps, and pressure cleaner booster
pumps are discussed in the subsequent
sections.
1. Self-Priming and Non-Self-Priming
Pool Filter Pumps
As noted in section III.B.3.a, selfpriming and non-self-priming pool filter
pumps have different construction
characteristics and potentially different
applications. However, during the
Working Group meetings, the DPPP
Working Group discussed how the
performance of these two different
varieties of pumps is comparable in
most instances. (Docket No. EERE–
2015–BT–STD–0008, No. 57 at pp. 329–
331) Therefore, to provide comparable
ratings between self-priming and nonself-priming pool filter pumps, the
DPPP Working Group recommended the
same reference curve, curve C, for self-
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C was representative of 2.5-inch
plumbing. (CA IOUs, Public Meeting
Transcript, No. 3 at p. 37) In response
to CA IOUs observation, DOE agrees
with CA IOUs that many factors may
impact system head. DOE was simply
referring to the fact that curve C was
initially developed to be representative
of 2.5-inch plumbing,27 as is
acknowledged in section 4.1.2.1.3 of
ANSI/APSP/ICC–15a–2013.
Beyond the proposed system curve,
DOE also proposed specific load points
for each variety of self-priming and nonself-priming pool filter pump. The
specific load points for single-speed,
two-speed, multi-speed, and variablespeed pool filter pumps are discussed in
sections III.D.1.a, III.D.1.b, and III.D.1.c,
respectively.
a. Single-Speed Pool Filter Pumps
CEC, in written comments, supported
DOE’s proposal to establish a load point
for single-speed filter pumps. (CEC, No.
7 at p. 2) DOE received no other
comments related to the proposal to test
single-speed pool filter pumps at a
single load point based on the
maximum speed on curve C. Therefore,
DOE is adopting in this final rule the
proposed single load point for singlespeed pool filter pumps.
b. Two-Speed Pool Filter Pumps
Two-speed pumps, by definition and
design, are capable of operating at two
discrete speeds. In two-speed pool filter
pumps, the low speed setting is
designed to handle filtration and
provide an adequate turnover-rate,
while the high speed setting operation
is designed to be used intermittently for
short duration periods to operate
suction-side pool cleaners and ensure
proper mixing of the water. Consistent
with typical two-speed pool filter pump
design and the requirements of existing
regulatory programs, the DPPP Working
Group recommended testing two-speed
pool filter pumps (1) at the load point
corresponding to the pump’s maximum
speed of rotation on curve C and (2) at
the load point corresponding to half of
the maximum-speed flow rate with total
dynamic head at or above curve C.
27 PG&E developed curves A, B, and C based data
from an exercise by ADM Associates, Inc. in 2002,
EVALUATION OF YEAR 2001 SUMMER
INITIATIVES POOL PUMP PROGRAM and
contractor input. However, the actual data for the
curves are not contained in the ADM report (the
ADM report can be found at www.calmac.org/
publications/SI_Pool_Pump.pdf; Last accessed
April 4, 2016). Curves A and B are first formally
mentioned in a subsequent report by PG&E in Codes
and Standards Enhancement Initiative for FY 2004.
However, this report does not discuss the derivation
of the curves. (https://consensus.fsu.edu/FBC/PoolEfficiency/CASE_Pool_Pump.pdf; Last accessed
April 29, 2016).
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Single-speed pool filter pumps, by
definition and design, are only capable
of operating at one speed. In the
September 2016 DPPP test procedure
NOPR, consistent with the DPPP
Working Group recommendations
(Docket No. EERE–2015–BT–STD–0008,
No. 51 Recommendation #6 at p. 5),
DOE proposed testing single-speed pool
filter pumps at the pump’s maximum
speed of rotation on curve C. 81 FR
64580, 64603 (Sept. 20, 2016). That is,
the load point for single-speed pool
filter pumps would be specified as the
point of intersection between the
pump’s performance curve at its
maximum speed (which is its only
speed) and the system curve C, as
shown in Figure III.1. Id.
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priming and non-self-priming filter
pumps. (Docket No. EERE–2015–BT–
STD–0008, No. 51 Recommendation #6
at p. 5) Consistent with the DPPP
Working Group recommendations, in
the September 2016 test procedure
NOPR, DOE proposed that both selfpriming and non-self-priming pool filter
pumps be tested at specific load points
along curve C. 81 FR 64580, 64602–
64603 (Sept. 20, 2016).
During the September 2016 DPPP test
procedure NOPR public meeting, CA
IOUs did not object to the
recommendation, but noted that the
typical pipe size associated with these
curves is a generalization and the
overall plumbing system can affect the
curves as much as the pump size in
response to DOE’s assertion that curve
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(Docket No. EERE–2015–BT–STD–0008,
No. 51, Recommendation #6, at p. 5)
However, in the September 2016 DPPP
test procedure NOPR, DOE proposed
load points that were slightly modified
from those recommended by the DPPP
Working Group. Specifically, DOE
proposed the following two load points
for two-speed pool filter pumps: (1) A
high flow point at the maximum speed
on curve C and (2) a low flow point at
the low-speed setting on curve C. 81 FR
64580, 64604–64606 (Sept. 20, 2016). As
explained in the September 2016 DPPP
test procedure NOPR, the load points
recommended by the DPPP Working
Group are only possible for pumps with
the low-speed setting equivalent to onehalf of the rotating speed of the
maximum speed setting. DOE proposed
the modification because DOE believed
the DPPP Working Group
recommendation, as written, would not
provide equitable or representative
ratings for any two-speed pool filter
pumps with a low speed that was less
than one-half the maximum speed
setting. Id.
DOE also proposed certain criteria for
the low flow point to prevent
manufacturers from producing pumps
with unrepresentatively high (i.e.,
advantageous) WEF scores by designing
pumps with an extremely low speed
setting. Id. Specifically, DOE proposed
minimum flow rates for two-speed
pumps of 24.7 gpm for two-speed pool
filter pumps that have a rated hydraulic
horsepower less than or equal to 0.75 hp
(small pool filter pumps) and 31.1 gpm
for two-speed pool filter pumps that
have a rated hydraulic horsepower
greater than 0.75 (large pool filter
pumps). DOE’s proposed minimum flow
rates are consistent with the DPPP
Working Group’s recommended low
flow rates for multi-speed and variablespeed pool filter pumps. (Docket No.
EERE–2015–BT–STD–0008, No. 51,
Recommendation #6 at p. 5); 81 FR
64580, 64604–06 (Sept. 20, 2016). The
DPPP Working Group developed these
low flow rates based on the minimum
effective flow rates for typical pool
sizes. DOE believes these flow rates are
also representative of minimum flow
rates for two-speed pool filter pumps
and they will effectively prevent the
inclusion of unreasonably low speeds
on two-speed pool filter pumps for the
sole purpose of inflating WEF ratings.
81 FR 64580, 64604–06 (Sept. 20, 2016).
DOE believes that the proposed load
points for two-speed pool filter pumps
are representative of typical pool filter
pump operation and energy
performance, and the load points
characterize the efficiency of the pump
speeds and flow points in typical
applications (i.e., cleaning/mixing and
filtration). In addition, DOE believes
that the proposal is consistent with the
intent of the DPPP Working Group.
During the September 2016 DPPP test
procedure NOPR public meeting, CA
IOUs confirmed that two-speed pool
filter pumps with low speed below onehalf of maximum speed are a reasonable
scenario and supported DOE’s proposed
load points to address this scenario. (CA
IOUs, Public Meeting Transcript, No. 3
at pp. 39–41) ASAP, NRDC, and CEC, in
written comments, supported DOE’s
proposal to establish load points for
two-speed pool filter pumps and did not
articulate any different suggestions to
the proposed test procedure. (ASAP and
NRDC, No. 12 at p. 2; CEC, No. 7 at p.
2) ASAP and NRDC also commented
that proposed load points would
provide consistent and comparable
ratings among two-speed filter pumps.
(ASAP and NRDC, No. 12 at p. 2)
DOE appreciates the support of CA
IOUs, ASAP, NRDC, and CEC. DOE
received no other comments related to
the proposed test procedure for twospeed pool filter pumps. Therefore, DOE
is adopting in this final rule the
proposed load points at low and high
speed for two-speed pool filter pumps,
as well as the minimum flow rate
thresholds of 24.7 gpm for two-speed
pool filter pumps that have a hydraulic
output power less than or equal to 0.75
hp (small pool filter pumps) and a low
flow rate of 31.1 gpm for two-speed pool
filter pumps that have a hydraulic
output power greater than 0.75 and less
than 2.5 hp (large pool filter pumps).
c. Variable-Speed and Multi-Speed Pool
Filter Pumps
In accordance with the DPPP Working
Group recommendations, in the
September 2016 DPPP test procedure
NOPR, DOE proposed different
definitions for variable-speed and multispeed pool filter pumps (see section
III.B.7.a), but proposed the same test
procedure be applied to both speed
configurations. (Docket No. EERE–2015–
BT–STD–0008, No. 51,
Recommendation #6, at p. 5); 81 FR
64580, 64606–64610 (Sept. 20, 2016).
For variable- and multi-speed pool filter
pumps, DOE proposed two load points
that are generally representative of a
high-speed mixing/cleaning flow rate
and a low-speed filtration flow rate,
similar to two-speed pool filter pumps
(as discussed in section III.D.1.b).
However, the high-speed and low-speed
load points for variable- and multispeed equipment are specified in a
slightly different manner than for twospeed equipment. 81 FR 64580, 64606–
64610 (Sept. 20, 2016).
As DOE discussed in the September
2016 DPPP test procedure NOPR, the
DPPP Working Group recommended
(Docket No. EERE–2015–BT–STD–0008,
No. 51, Recommendation #6 at p. 5),
and DOE subsequently proposed, testing
multi- and variable-speed pool filter
pumps at two load points. These points
are (1) a high-flow load point that is
achieved by running the pump at 80
percent of flow rate at maximum speed
on or above curve C and (2) a low-flow
load point that is representative of a
specific, typical filtration flow rate, as
opposed to a specific speed setting or
relative reduction from maximum speed
(also on or above curve C), as
summarized in Table III.3. 81 FR 64580,
64606–64610 (Sept. 20, 2016).
TABLE III.3—VARIABLE- AND MULTI-SPEED LOAD POINTS RECOMMENDED BY DPPP WORKING GROUP AND PROPOSED BY
DOE IN SEPTEMBER 2016 DPPP TEST PROCEDURE NOPR
Flow rate
(gpm)
High Speed ..................
Low Speed ..................
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Load point
Head
(ft)
Qhigh (gpm) = 0.8×Qmax_speed@C *
Qlow (gpm) =
• If pump hydraulic hp at max speed on
curve C is >0.75, then Qlow = 31.1 gpm
• If pump hydraulic hp at max speed on
curve C is ≤0.75, then Qlow = 24.7 gpm
H ≥0.0082 × Qhigh2
H ≥0.0082 × Qlow2
Speed
(rpm)
Lowest available speed for which the pump
can achieve the specified flow rate (a
pump may vary speed to achieve this load
point).
* Qmax_speed@C = flow at maximum speed on curve C.
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36881
amount of flow that may be less than the
flow rate at maximum speed. Id. In the
September 2016 DPPP test procedure
NOPR, DOE discussed that, for multispeed pumps without a speed setting at
80 percent of the maximum speed
setting, the high flow point would be
determined at the maximum operating
speed of the pump and may not be on
curve C. 81 FR 64580, 64607 (Sept. 20,
2016). Such a pump would need to be
tested at a speed setting higher than 80
percent of maximum and throttled to a
head pressure higher than curve C to
achieve a flow rate of 80 percent of the
flow rate at maximum flow on curve C,
as shown in Figure III.2.
To specify the low flow points for
multi-speed and variable-speed pool
filter pumps, the DPPP Working Group
developed specific, discrete flow rates
that are representative of the typical
flow rates observed in the field. (Docket
No. EERE–2015–BT–STD–0008, No. 51,
Recommendation #6 at p. 5) That is, as
discussed in the September 2016 DPPP
test procedure NOPR, the DPPP
Working Group recommended that
‘‘small pool filter pumps’’ with rated
hydraulic horsepower values of less
than or equal 0.75 would be assigned a
flow rate of 24.7 gpm, which is
representative of the flow rate necessary
for filtration in smaller pools. The DPPP
Working Group also recommended that
‘‘large pool filter pumps’’ with rated
hydraulic horsepower values greater
than 0.75 and less than or equal to 2.5
would be assigned a flow rate of 31.1
gpm, which is representative of the flow
rate necessary for filtration in large
pools. The selected low flow rates for
small and large multi-speed and
variable-speed pool filter pumps are
intended to be representative of the
applications such pumps would
typically serve. The methodology for
developing the specific flow rates for
small and large multi-speed and
variable-speed pool filter pumps is
discussed at length in the September
2016 DPPP test procedure NOPR. 81 FR
64580, 64606–64610 (Sept. 20, 2016).
DOE’s proposal for the high flow and
low flow points for multi-speed and
variable-speed pumps does not
explicitly specify the speed at which the
pump operates at the high or low flow
points. Instead, DOE determined that
the low and high flow rates would be
achieved at the lowest available speed
while operating on or above curve C to
accommodate multi-speed pumps that
may not be capable of operating at the
exact speed that allows the pump to
achieve the required flow rate exactly
on curve C. For such a pump, DOE
established that the pump be tested at
the lowest available speed that can meet
the specified flow with a head point that
is at or above curve C. Id.
In the September 2016 DPPP test
procedure NOPR, DOE requested
comment on the treatment of multispeed pumps and the necessity to
throttle multi-speed pumps on the
maximum speed performance curve if
appropriate lower discrete operating
speeds are not available to achieve 80
percent of the flow rate at maximum
speed on curve C while still maintaining
head at or above curve C. 81 FR 64580,
64608 (Sept. 20, 2016).
In response, CEC supported DOE’s
proposal to establish load points for
multi-speed and variable-speed pool
filter pumps. However, CEC did not
advocate for any different values
compared to DOE’s proposal. (CEC, No.
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The high speed load point
corresponding to a flow rate of 80
percent of the flow at maximum speed
on curve C was recommended by the
DPPP Working Group to reflect that
multi- and variable-speed pool filter
pumps can be optimized to account for
the oversizing the typically occurs in
the field and provide a specific desired
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7 at p. 2). Pentair requested clarification
during the September 2016 DPPP test
procedure NOPR public meeting and in
written comments regarding whether
the high flow load point for multi-speed
and variable-speed pool filter pumps
was specified with respect to 80 percent
flow or 80 percent speed. (Pentair,
Public Meeting Transcript, No. 3 at p.
48; Pentair, No. 11 at p. 4) APSP
reiterated Pentair’s comments that flow
and speed were used interchangeably in
the September 2016 DPPP test
procedure NOPR and recommended that
the test procedure be standardized on a
percentage of flow requirements (APSP,
No. 8 at p. 2). Consistent with APSP’s
recommendation, in this final rule, DOE
clarifies that the high flow load point for
multi-speed and variable-speed pool
filter pumps is specified with respect to
at 80 percent of the flow rate at
maximum speed on curve C.
APSP and Pentair also commented
that throttling multi-speed pumps to
obtain 80 percent flow moves the pump
off of curve C, which is otherwise the
standardized performance curve
proposed by DOE in the test procedure
NOPR. Pentair commented that
throttling and testing off of curve C
makes direct product performance
comparisons impossible, and has the
potential to overstate the performance of
less efficient and less capable pumps.
(APSP, No. 8 at pp. 4–5; Pentair, No. 11,
at p. 2) Pentair similarly expressed
concern over the low flow load points.
Pentair agreed that 24.7 gpm and 31.1
gpm are reasonable minimum flow rates
for typical swimming pool applications.
However, Pentair stated that fixing the
low-speed load point at one of these two
values would create an unfair bias
against higher capacity pumps that are
designed for high-flow, low-head
systems. (Pentair, No. 11 at p. 2) At the
test procedure NOPR public meeting,
Pentair suggested that multi-speed
pumps that cannot be tested at 80
percent of the flow rate at maximum
speed on curve C be tested at their
maximum speed on curve C. (Pentair,
Public Meeting Transcript, No. 3 at pp.
42–43) Pentair did not provide a
specific recommendation for the low
flow load points.
In response to Pentair and APSP’s
dissatisfaction with DOE’s proposal to
allow throttling multi-speed pumps,
DOE agrees with Pentair and APSP’s
concerns that throttling and testing off
of curve C may result in WEF values
that are not directly representative of
the typical energy performance of the
pump in the field, as users are unlikely
to throttle pumps to compensate for
oversizing. In assessing Pentair and
APSP’s concerns, DOE recognized that
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the multi-speed pump load points
specified in the December 2015 DPPP
Working Group recommendations did
not explicitly mention or require
throttling. Specifically, for flow, the
term sheet stated ‘‘same method as
variable speed, but testing at closest
available speed that can meet the
specified flow (while at or above Qlow or
Qhigh, respectively).’’ For head, the term
sheet stated: ‘‘H ≥ 0.0082 × Qhigh2.’’
(Docket No. EERE–2015–BT–STD–0008,
No. 51, Recommendation #6 at p. 5)
Allowing flow to be ‘‘at or above’’ Qhigh
and ‘‘at or above’’ 0.0082 × Qhigh2 means
that a multi-speed pump that does not
have an 80 percent speed setting could
test exactly on curve C with a flow rate
at or above 80 percent of the flow rate
at maximum speed on curve C, as
suggested by Pentair, and still meet the
load point requirements laid out by the
DPPP Working Group in the December
2015 term sheet. Id.
Consequently, DOE acknowledges
that its proposal in the September 2016
DPPP test procedure NOPR to require
throttling of multi-speed pumps was
based on one possible interpretation of
the December 2015 DPPP Working
Group recommendations, while
Pentair’s proposal to test on curve C as
the lowest speed that resulted in a flow
rate at or above 80 percent of the flow
rate at maximum speed on curve C is
based on another possible
interpretation. That is, as written, the
December 2015 DPPP Working Group
recommendations allow multiple
interpretations of the appropriate load
points for multi-speed pool filter
pumps. In the September 2016 DPPP
test procedure NOPR, DOE proposed the
test method that required fixing the flow
point at 80 percent of the flow rate at
maximum speed on curve C (i.e., Qhigh
= 0.8 × Qmax_speed@C) because DOE’s test
procedure must be precise and
repeatable and, therefore, must provide
additional specificity beyond that
specified by the DPPP Working Group.
However, DOE acknowledges that
Pentair’s suggestion of fixing the head
value on curve C (H = 0.0082 × Qhigh2)
and allowing flow rates above 80
percent of the flow rate at maximum
speed on curve C is another viable
method to provide the requisite
additional specificity and precision in
the multi-speed test method. DOE also
acknowledges that, as mentioned by
Pentair and APSP, that throttling off of
curve C would be a departure from the
standardized system curve and would
result in WEF values that are less
representative of the typical energy
performance of such multi-speed
pumps. Instead, multi-speed pumps
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would more likely be operated on the
standardized system curve (i.e., curve C)
at the lowest speed available at or above
80 percent of the flow rate at maximum
speed on curve C (i.e., the flow rate the
DPPP Working Group believed was
‘‘required’’ for high flow mixing in
pumps that are oversized). Therefore, in
this final rule, DOE is revising the load
points for multi-speed pumps to require
the head value to be on curve C, as
suggested by Pentair, but allow the flow
value to be greater than or equal to 80
percent of the flow rate at maximum
speed on curve C. As noted previously,
this test method is consistent with that
recommended by the DPPP Working
Group.
With regard to the low flow load
points, DOE responds that the DPPP
Working Group recommended that the
low-speed load point for variable- and
multi-speed pumps be measured at
either 24.7 gpm or 31.1 gpm, depending
on the pump hydraulic horsepower at
maximum speed on curve C. (Docket
No. EERE–2015–BT–STD–0008, No. 51,
Recommendation #6 at p. 5) As
discussed at length in the September
2016 DPPP test procedure NOPR, the
DPPP Working Group recommended
these values to allow for more
comparable WEF values among pool
filter pumps intended to serve the same
size pools. 81 FR 64580, 64606–64610
(Sept. 20, 2016). While Pentair noted in
its comments that this construct may
bias higher capacity (high flow, low
head) pumps, DOE notes that in general,
higher capacity pumps have been
excluded from the scope of this
rulemaking. In addition, as discussed
previously, these low flow points were
chosen specifically to represent typical
filtration flow rates that would be
experienced in the majority of pools,
regardless of the size of the pump. That
is, the required filtration flow rate is
dictated more by the size of the pool
than the size of the pump. Converse to
Pentair’s observation, the ability of
larger pumps to reduce their speed to
achieve these low flow rates will
potentially result in higher (i.e., better)
WEF scores than slightly small
dedicated-purpose pool pumps serving
the same load.
For these reasons, DOE is adopting in
this final rule the low speed load points
of 24.7 gpm and 31.1 gpm, as proposed,
in the September 2016 DPPP TP NOPR.
However, for multi-speed pumps, DOE
acknowledges that the low speed may
not result in a flow rate that is exactly
24.7 or 31.1 gpm while on curve C and
throttling may be required to achieve
the flow points proposed in the NOPR.
As discussed previously, DOE agrees
with Pentair and APSP that throttling
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may not be representative of the
performance of multi-speed dedicatedpurpose pool pumps in the field.
Therefore, based on the same reasoning
as the high flow point, DOE is revising
the low flow point for multi-speed
dedicated-purpose pool pumps to also
require testing along curve C, but allow
36883
flow rates at or above the specified
values. Specifically, the adopted load
points are presented in Table III.4.
TABLE III.4—MULTI-SPEED AND VARIABLE-SPEED LOAD POINTS ADOPTED IN THIS FINAL RULE
Load point
Flow rate
(gpm)
Head
(ft)
Speed
(rpm)
High Speed
Low Speed
Qhigh (gpm) ≥0.8 × Qmax_speed@C *
Qlow (gpm) =
• If pump hydraulic hp at max speed on curve C is >0.75,
then Qlow ≥31.1 gpm
• If pump hydraulic hp at max speed on curve C is ≤0.75,
then Qlow ≥24.7 gpm
H = 0.0082 × Qhigh2 (i.e., on
Curve C)
H = 0.0082 × Qlow2 (i.e., on
Curve C)
Lowest available speed for
which the pump can achieve
the specified head value and
flow rate threshold (a pump
may vary speed to achieve
this load point).
mstockstill on DSK30JT082PROD with RULES2
* Qmax_speed@C = flow at maximum speed on curve C.
DOE believes that the load points
shown in Table III.4 are consistent with
the intent of the DPPP Working Group
while addressing the concerns brought
by Pentair and APSP for multi-speed
pool filter pumps.
With regard to the variable-speed load
points, DOE notes that the load points
recommended by the DPPP Working
Group were specified clearly as exactly
equivalent to 24.7 or 31.1 gpm for the
low flow load point and 80 percent of
the flow rate at maximum speed on
curve C for the high flow load point.
(Docket No. EERE–2015–BT–STD–0008,
No. 51, Recommendation #6 at p. 5) The
DPPP Working Group discussed and
recommended these load points based
on the understanding that a variablespeed dedicated purpose pool pump
would be equipped with a continuously
variable control that could exactly
achieve the load points specified in the
test procedure or desired by a user in
the field. However, DOE notes that the
definition for variable-speed dedicatedpurpose pool pump recommended by
the DPPP Working Group and adopted
by DOE references a maximum
increment between available operating
speeds of 100 rpm. Based on the
adopted definition it is possible that a
variable-speed dedicated-purpose pool
pump with extremely wide speed
increments (e.g., 95 rpm) will not be
able to exactly achieve the flow points
specified by the DPPP Working Group.
DOE notes that the definition for
variable-speed dedicated-purpose pool
pump was not finalized by the DPPP
Working Group until after the load
points for variable-speed dedicatedpurpose pool pump had already by been
established and approved. Therefore,
the DPPP Working Group did not
explicitly consider a scenario where a
variable-speed dedicated-purpose pool
pump would not be able to exactly
achieve the specified flow points.
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DOE believes that, similar to multispeed pool filter pumps, it is unlikely
that a user would throttle the pump in
the field to achieve a specific flow rate.
Instead, DOE believes it would be more
representative and consistent to also
require variable-speed pool filter pumps
to be tested on curve C at the lowest
speed that results in a flow rate at or
above the flow rate specified by the
DPPP Working Group, similar to the
load points specified for multi-speed
pool filter pumps. Therefore, DOE is
adopting, in this final rule, the same
load points for multi-speed and
variable-speed pool filter pumps, as
summarized in Table III.4.
In response to the multi-speed load
points proposed in the September 2016
DPPP test procedure NOPR, Hayward
commented that the proposed criteria
for multi-speed pumps would severely
penalize less capable multispeed pumps
[without a discrete operating speed at 80
percent of flow rate at maximum speed
on curve C]. (Hayward, No. 6 at p. 3) In
response to Hayward’s concerns
regarding the penalization of multispeed pumps, DOE acknowledges that
the test procedure (both as proposed in
the NOPR and as adopted in this final
rule) will indeed ‘‘penalize’’ (i.e.,
generate less advantageous WEF score
for) less capable multi-speed pumps that
cannot exactly achieve 80 percent of the
flow rate at maximum speed on curve C.
This is by-design and in agreement with
the recommendations of DPPP Working
Group, because such pumps provide the
end-user less utility and are more likely
to be run at higher-speeds and consume
more energy than pumps that can reach
80 percent of the flow rate at maximum
speed on curve C. Furthermore, the
disadvantage in WEF score is
commensurate with the reduced speed
capability of the pump—the closer the
pump can get to the 80 percent load
point (with speed reduction), the better
the pump’s WEF score will be. For this
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reason, DOE is adopting its proposals as
to the treatment of multi-speed pumps
in this final rule, except as noted in this
section.
Pentair raised a concern that an
unintended consequence of specifying
the high flow load point based on 80
percent flow was that manufacturers
may start designing pool filter pumps
with an 80 percent speed setting, even
if it is not the best optimization for the
pump for specific applications. (Pentair,
Public Meeting Transcript. No. 3 at p.
46) In response, DOE acknowledges
Pentair’s concern, but notes that the 80
percent load point was selected by the
DPPP Working Group to be
representative of the amount of ‘‘rightsizing’’ that would be possible in typical
applications. (EERE–2015–BT–STD–
0008, No. 57 at pp. 388–405; CA IOUs,
No. 53 at pp. 142–143; Waterway, No.
54 at p. 51) As such, DOE believes the
80 percent setting is representative of a
speed setting that would reliably result
in energy savings in the field for typical
applications. However, DOE
acknowledges that for some applications
the 80 percent speed setting may not be
the most appropriate choice. DOE notes
that, if specific applications necessitate
different speed settings, manufacturers
may continue to produce such
equipment to serve the market need for
equipment with specific speed settings.
The DOE test procedure does not affect
the flexibility of manufacturers to
produce equipment that is demanded by
the market; it just describes how to rate
such equipment.
Additionally, Hayward and APSP
pointed out a discrepancy between
Table 1 in the regulatory text of the
September 2016 DPPP test procedure
NOPR and the language presented in the
rest of the NOPR. Specifically, Hayward
noted that the required head for the
variable-speed and multi-speed high
flow load point should be ‘‘H ≥ 0.0082
× Qlow2,’’ rather than ‘‘H = 0.0082 ×
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Qlow2,’’ which was printed in Table 1 of
the September 2016 DPPP test
procedure NOPR. (Hayward, No. 6 at p.
3; APSP, No. 8 at p. 4) DOE agrees with
Hayward and APSP. A typographical
error occurred in Table 1 in the
September 2016 DPPP test procedure
NOPR and the equation should have
read ‘‘H ≥ 0.0082 × Qlow2’’ based on the
proposed load points for multi-speed
dedicated purpose pool pumps.
However, based on the adopted load
points, DOE is specifying the load
points as depicted in Table III.4, which
have the appropriate mathematical
operators.
During the September 2016 DPPP test
procedure NOPR public meeting,
Pentair also requested verification
regarding Figure III.5 in the September
2016 DPPP test procedure NOPR and a
similar figure in the September 2016
DPPP test procedure NOPR public
meeting presentation. (Pentair, Public
Meeting Transcript, No, 3, p. 54) DOE
acknowledged during the September
2016 DPPP test procedure NOPR public
meeting that the public meeting
presentation slide was correct and
Figure III.5 in the September 2016 DPPP
test procedure NOPR was incorrect.28
Accordingly, in this final rule, DOE
includes the corrected and clarified
version of the figure, which is labeled
Figure III.2 in this final rule.
APSP and Zodiac also requested
clarification regarding how the highspeed flow point is based on a flow rate
of 80 percent of the flow rate at
maximum speed on curve C and head at
or above curve C. (APSP, No. 8 at p. 4;
Zodiac, No. 13 at p. 2) DOE responds
that, as discussed in the September 2016
DPPP test procedure NOPR, the DPPP
Working Group recommended the high
speed load point corresponding to a
flow rate of 80 percent of the flow at
maximum speed on curve C to reflect
that multi- and variable-speed pool filter
pumps can be optimized to account for
the oversizing the typically occurs in
the field and provide a specific desired
amount of flow that may be less than the
flow rate at maximum speed. 81 FR
64580, 64606–64610 (Sept. 20, 2016).
Finally, APSP and Zodiac commented
that they would like to see a tolerance
for the 80 percent load point for multispeed and variable-speed pool filter
pumps, as a speed of 80.00 percent
exactly would be difficult to achieve.
(APSP, No. 8 at p. 5; Zodiac, No. 13 at
p. 2). In response, DOE clarifies that the
neither the load points proposed in the
September 2016 DPPP test procedure
NOPR nor the load points adopted in
this final rule for multi-speed and
variable-speed pool filter pumps require
exact speeds to be achieved. Instead, the
load points specify specific head or flow
values that must be achieved at the
lowest available speed for which the
pump can achieve the specified flow
rate and/or head value; a pump may
vary speed to achieve this load point.
DOE proposed and is adopting
thresholds on the specified head or flow
values to account for experimental
variability, which are discussed in
section III.E.2.d.
d. Load Point Weighting Factors
WEF is calculated as the weighted
average flow rate divided by the
weighted average input power to the
dedicated-purpose pool pump at various
load points, as described in equation (1).
For this reason, DOE also must assign
weights to the load points discussed
above for each self-priming or non-selfpriming pool filter pump. In the
September 2016 DPPP test procedure
NOPR, consistent with the DPPP
Working Group recommendations
(Docket No. EERE–2015–BT–STD–0008,
No. 51 Recommendation #7 at p. 5) as
well as DOE’s own analysis, DOE
proposed a weight of 1.0 for singlespeed self-priming and non-self-priming
pool filter pumps and weights of 0.20 at
the high flow point and 0.80 at the low
flow point for two-speed, multi-speed,
and variable-speed pool filter pumps, as
summarized in Table III.5. 81 FR 64580,
64610 (Sept. 20, 2016).
TABLE III.5—SUMMARY OF LOAD POINT WEIGHTS (wi) FOR SELF-PRIMING AND NON-SELF-PRIMING POOL FILTER PUMPS
RECOMMENDED BY THE DPPP WORKING GROUP
DPPP varieties
Load point(s)
i
Speed type
Low flow
mstockstill on DSK30JT082PROD with RULES2
Self-Priming Pool Filter Pumps and Non-Self-Priming Pool Filter Pumps .....
Single .................................................
Two/Multi/Variable ..............................
DOE requested comment on these
proposed weights. In response to DOE’s
proposed weights, APSP and Zodiac
stated that unbalanced weighting of the
economical single-speed pumps
negatively affects consumers who only
operate pools for a short seasonal
duration. (APSP, No. 8 at p. 5; Zodiac,
No. 13 at p. 2) DOE acknowledges that
pool pumps with more than one speed,
such as two-speed, multi-speed, and
variable-speed dedicated-purpose pool
pumps, will have a greater (i.e., more
efficient) WEF score than a single-speed
pump. However, this is consistent with
the intent of the DPPP Working Group
and the typical energy consumption of
such pumps in the field. That is, single-
speed pumps will use more energy than
comparable two-speed, multi-speed, or
variable-speed pumps. DOE also
disagrees with APSP and Zodiac that a
load point of 1.0 for single-speed pool
filter pumps is ‘‘unbalanced’’ because,
as recommended by the DPPP Working
Group, single-speed pool pump operate
at only one load point, which must be
fully weighted in order to accurately
and equitably account for the energy
performance of such pumps.
APSP and Hayward agreed with the
0.8 value for low flow for two-speed
pool filter pumps. (APSP, No. 8 at p. 5;
Hayward, No. 6 at p. 3) CEC, in written
comments, affirmed DOE’s proposal to
establish weighting factors for single-
28 The public meeting slides can be found in the
docket (www.regulations.gov/
20:57 Aug 04, 2017
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1.0
0.20
speed, two-speed, multi-speed, and
variable-speed pool filter pumps. (CEC,
No. 7 at p. 2) As such, DOE is adopting,
in this final rule, the weights proposed
in the September 2016 DPPP test
procedure NOPR.
#!docketDetail;D=EERE-2016-BT-TP-0002) No. 2 at
p. 31.
VerDate Sep<11>2014
....................
0.80
High flow
e. Applicability of Two-Speed, MultiSpeed, and Variable-Speed Pool Filter
Pump Test Methods
As discussed in section III.B.7, DOE
proposed in the September 2016 DPPP
test procedure NOPR to establish
specific definitions for two-speed,
multi-speed, and variable-speed
dedicated-purpose pool pumps that
would dictate which of the pool filter
pump test methods applies to a given
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pool filter pump. The specific test
methods for each of the DPPP speed
configurations are described in sections
III.D.1.a through III.D.1.c. The
definitions for two-speed, multi-speed,
and variable-speed dedicated-purpose
pool pumps establish specific criteria
that any given dedicated-purpose pool
pump must meet in order to be
considered such a pump and be eligible
to apply the test points for two-speed,
multi-speed, and variable-speed pool
filter pumps, respectively. If a
dedicated-purpose pool pump does not
meet the definition of a two-speed,
multi-speed, or variable-speed
dedicated-purpose pool pump discussed
in section III.B.7, DOE proposed in the
September 2016 DPPP test procedure
NOPR that such a pump would be tested
using the single-speed pool filter pump
test point, regardless of the number of
operating speeds the pump may have.
81 FR 64580, 64610 (Sept. 20, 2016).
In the September 2016 DPPP test
procedure NOPR, consistent with the
recommendations of the DPPP Working
Group (Docket No. EERE–2015–BT–
STD–0008, No. 82, Recommendation
#5B at p. 3), DOE also proposed that
two-speed self-priming pool filter
pumps that are greater than or equal to
0.711 rated hydraulic horsepower and
less than 2.5 rated hydraulic
horsepower must also be distributed in
commerce either: (1) With a pool pump
control (variable speed drive and user
interface or switch) that changes the
speed in response to pre-programmed
user preferences and allows the user to
select the duration of each speed and/
or the on/off times or (2) without a pool
pump control with such capability but
is unable to operate without the
presence of such a pool pump control.
Id. DOE also proposed that two-speed
self-priming pool filter pumps (in the
referenced size range) that do not meet
the proposed control requirements
would be tested as a single-speed pool
filter pump. Id.
Hayward commented, at the
September 2016 DPPP test procedure
NOPR public meeting, that two-speed
dedicated-purpose pool pumps should
be allowed to operate at low speed
without the requisite control, instead of
not able to operate at all. (Hayward,
Public Meeting Transcript, No. 3 at pp.
21, 26–27) DOE addressed this comment
in section III.B.7.a. In that section, DOE
noted that DOE believes the two-speed
DPPP test points are only applicable to
and representative of two-speed
dedicated-purpose pool pumps operated
with the appropriate controls. If a twospeed dedicated-purpose pool pump is
capable of operating, even at low speed,
without an applicable pool pump
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control, this significantly increases the
risk that two-speed pool filter pumps
would be installed and operated
without an appropriate control.
Similarly, with regard to the
applicability of the two-speed test
points, DOE believes that two-speed
dedicated-purpose pool pumps greater
than 0.711 rated hydraulic horsepower
must be distributed in commerce with
either an appropriate control or not able
to operate without the presence of such
a pool pump control in order to apply
the two-speed dedicated-purpose pool
pump test points. If the pump can
operate without an appropriate control,
even at low speed, the two-speed test
points would not be representative of
the pump’s energy performance in the
field. DOE did not receive any
comments on this proposal. Therefore,
DOE is adopting in this final rule the
requirements for applying the two-speed
dedicated-purpose pool pump test
points proposed in the September 2016
DPPP test procedure NOPR, which was
agreed to by all DPPP Working Group
members as part of the June 2016 DPPP
Working Group Recommendations.
2. Waterfall Pumps
DOE also proposed a unique test point
for waterfall pumps in the September
2016 DPPP test procedure NOPR. 81 FR
64580, 64610–64611 (Sept. 20, 2016).
Under the definition discussed in
section III.B.4.a, waterfall pumps are
pool filter pumps that have a maximum
head less than or equal to 30 feet and
a maximum speed less than or equal to
1,800 rpm. As discussed in the
September 2016 DPPP test procedure
NOPR, waterfall pumps are specialtypurpose single-speed, pool filter pumps
that typically operate waterfalls or other
water features in a pool. Id.
Because of these specific applications,
the DPPP Working Group recommended
a single unique test point at a fixed head
of 17 feet and the maximum operating
speed for waterfall pumps, which the
DPPP Working Group believed was
representative of typical applications.
Consistent with the single
recommended load point, the DPPP
Working Group also recommended fully
weighting that load point (i.e., assigning
it a weight of 1.0). (Docket No. EERE–
2015–BT–STD–0008, No. 51
Recommendation #6 at p. 5)
DOE agreed with the DPPP Working
Group recommendations; however, DOE
slightly modified the recommendation
by adding greater specificity to the head
value in DOE’s proposal. DOE proposed
to test waterfall pumps at a single load
point at maximum speed and a head of
17.0 feet and to fully weight that single
load point. 81 FR 64580, 64610–64611
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36885
(Sept. 20, 2016). DOE received no
comment on the proposal and, therefore,
is adopting the load point and weighting
for waterfall pumps proposed in the
September 2016 DPPP test procedure
NOPR.
3. Pressure Cleaner Booster Pumps
DOE also proposed a unique test point
for pressure cleaner booster pumps in
the September 2016 DPPP test
procedure NOPR. 81 FR 64580, 64611–
64612 (Sept. 20, 2016). Pressure cleaner
booster pumps, as defined in section
III.B.4.b, are dedicated-purpose pool
pumps that are specifically designed to
propel pressure-side pool cleaners along
the bottom of the pool in pressure-side
cleaner applications. These pressureside cleaner applications require a high
amount of head and a low flow. In the
December 2015 DPPP Working Group
recommendations, the DPPP Working
Group had recommended a single, fixed
load point of 90 feet of head at
maximum speed based on the fact that
any given pressure-side pool cleaner
application is typically a single, fixed
load point. (Docket No. EERE–2015–BT–
STD–0008, No. 51, Recommendations
#6) However, in the second round of
negotiations, the DPPP Working Group
reevaluated the recommended test
procedure for pressure cleaner booster
pumps and its ability to representatively
evaluate and differentiate the
potentially variable energy performance
of different pressure cleaner booster
pump technologies. Specifically, to
better capture the potential for variablespeed pressure cleaner booster pumps,
in the June 2016 DPPP Working Group
recommendations, the DPPP Working
Group revised the recommended test
point for pressure cleaner booster
pumps to be a flow rate of 10 gpm at the
minimum speed that results in a head
value at or above 60 feet. (Docket No.
EERE–2015–BT–STD–0008, No. 82,
Recommendation #8 at pp. 4–5)
In either case, as only a single load
point is required to adequately
characterize the efficiency of pressure
cleaner booster pumps, the DPPP
Working Group recommended a
weighting factor of 1.0 for measured
performance at that single load point
when calculating WEF. (Docket No.
EERE–2015–BT–STD–0008, No. 51,
Recommendation #6 and #7 at p. 5)
In the September 2016 DPPP test
procedure NOPR, DOE proposed to
adopt the load point and weighting
recommended in the June 2016 DPPP
Working Group recommendations;
however, DOE added specificity to the
flow and head values in the September
2016 DPPP test procedure NOPR.
Specifically, DOE proposed to test
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pressure cleaner booster pumps at a
single load point of 10.0 gpm at the
minimum speed that results in a head
value at or above 60.0 feet and to weight
the measured performance of the pump
at that load point with a weighting
factor of 1.0. 81 FR 64580, 64611–64612
(Sept. 20, 2016).
In response to DOE’s proposed test
method for pressure cleaner booster
pumps, APSP and Zodiac commented
that the proposed test point seemed
reasonable. (APSP, No. 8 at p. 5; Zodiac,
No. 13 at p. 2). DOE thanks APSP and
Zodiac for their supportive comments.
In written comments, Pentair stated
that it would be more appropriate to
base the load point for pressure cleaner
booster pump testing on a system
friction curve instead of a defined single
point. (Pentair, No. 11 at p. 3) In
response, DOE notes that the proposed
load point for pressure cleaner booster
pumps was developed based on input
from the DPPP Working Group and
available information regarding the
representative operating characteristics
for such pumps. Specifically, the DPPP
Working Group recommended a load
point of 10 gpm at the minimum speed
that results in a head value at or above
60 feet, because this scenario
accommodates all pressure cleaner
booster pumps on the market. At the
same time this scenario also accounts
for the potential improved energy
performance of pressure cleaner booster
pumps that could use variable speed
technology to precisely match the head
requirements of a pressure cleaner
system. (Docket No. EERE–2015–BT–
STD–0008, No. 82, Recommendation #8
at pp. 4–5; Docket No. EERE–2015–BT–
STD–0008, No. 101 at pp. 11–20) The
DPPP Working Group selected a value of
10 gpm based on the typical flow rate
that was required or recommended for
suction-side pressure cleaner apparatus
to function. (Docket No. EERE–2015–
BT–STD–0008, No. 100, CA IOUs, pp.
186–188; 197–198; Docket No. EERE–
2015–BT–STD–0008, No. 101, Various,
pp. 14–15, 49–50, 87–89). Although
DOE understands that a system curve
that includes both static and dynamic
friction head would theoretically
describe the relationship between head
and flow for pressure cleaner booster
pump applications, DOE believes that
such a system curve is not necessary or
representative in this case because: (1)
Pressure cleaner booster pumps operate
at only one load point and (2) the
specified flow point and head threshold
appropriately describe the required
operating parameters for pressure
cleaner booster pump applications. That
is, as noted by the DPPP Working
Group, suction-side pressure cleaner
apparatus typically recommend a
specific flow rate that will enable the
equipment to operate correctly. DOE
acknowledges that a certain amount of
pressure must be produced by the
pressure cleaner booster pump to
deliver the recommended flow rate.
However, once that flow and head value
are achieved, the pump will operate at
only that one load point. Therefore,
based on DOE’s understanding of
pressure cleaner booster pump
applications, DOE is requiring in this
final rule that a specific flow rate must
be achieved regardless of the
installation’s system curve.
DOE did not receive any other
comments related to this proposal.
Therefore in this final rule, DOE is
adopting the proposal that pressure
cleaner booster pumps to be tested at a
single load point of 10.0 gpm at the
minimum speed that results in a head
value at or above 60.0 feet and to weight
the measured performance of the pump
at that load point with a weighting
factor of 1.0.
4. Summary
In summary, DOE adopts, in this final
rule, unique load points for the different
varieties and speed configurations of
dedicated-purpose pool pumps. DOE’s
load points (i) and weights (wi) used in
determining WEF for each pump variety
are presented in Table III.6.
DOE requested comment on the highspeed and low-speed load points
proposed for all DPPP equipment
classes. 81 FR 64580, 64642–64643
(Sept. 20, 2016). Hayward requested
clarification regarding whether all of the
load points used to determine WEF
should be measured on system curve C.
(Hayward, No. 6 at p. 2) DOE refers
Hayward to Table III.6, which
summarizes the load points for all
dedicated-purpose pool pumps subject
to the test procedure adopted in this
final rule. As shown in Table III.6, all
of the load points for self-priming and
non-self-priming pool filter pumps are
specified with respect to curve C.
However, while many self-priming and
non-self-priming pool filter pumps
models will be evaluated directly on
curve C, certain models may have their
load points measured at head values
above curve C, if the load point cannot
be measured on curve C based on the
operating speeds available on the pump.
In addition, waterfall pumps and
pressure cleaner booster pumps have
load points that are specified with
respect to unique flow and/or head
values and do not reference curve C.
TABLE III.6—LOAD POINTS (i) AND WEIGHTS (wi) FOR EACH DPPP VARIETY AND SPEED CONFIGURATION
Test points
DPPP varieties
Speed type
Number
of points
(n)
Load
point
(i)
Flow rate
(Q)
Head
(H)
Speed
(n)
Weight
(wi)
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Single * .............................
1
High .......
Qhigh (gpm) =
Qmax_speed@C =
flow at maximum speed
on curve C
H = 0.0082 ×
Qhigh2
Maxspeed .........................
1.0
Two-Speed .......................
Self-Priming Pool Filter
Pumps And Non-SelfPriming Pool Filter
Pumps (with hydraulic
hp ≤2.5 hp).
2
Low .......
Qlow (gpm) = Flow rate
associated with specified head and speed
that is not below:
• 31.1 gpm if pump hydraulic hp at max speed
on curve C is >0.75 or
• 24.7 gpm if pump hydraulic hp at max speed
on curve C is ≤0.75 (a
pump may vary speed
to achieve this load
point)
H ≥ 0.0082 ×
Qlow2
Lowest speed capable of
meeting the specified
flow and head values, if
any.
0.8
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36887
TABLE III.6—LOAD POINTS (i) AND WEIGHTS (wi) FOR EACH DPPP VARIETY AND SPEED CONFIGURATION—Continued
Test points
Number
of points
(n)
Speed type
Weight
(wi)
Multi- and Variable-Speed
2
Load
point
(i)
Flow rate
(Q)
Head
(H)
Speed
(n)
High .......
DPPP varieties
Qhigh (gpm) =
Qmax_speed@C = flow at
max speed on curve C
Qlow(gpm)
• If pump hydraulic hp at
max speed on curve C
is >0.75, then Qlow
≥31.1 gpm
• If pump hydraulic hp at
max speed on curve C
is ≤0.75, then Qlow
≥24.7 gpm (a pump
may vary speed to
achieve this load point)
Qhigh (gpm) ≥0.8 ×
Qmax_speed@C ≥80% of
flow at maximum speed
on curve C (a pump
may vary speed to
achieve this load point)
Flow corresponding to
specified head (on max
speed pump curve)
10.0 gpm (a pump may
vary speed to achieve
this load point)
H = 0.0082 ×
Qhigh2
Max speed .......................
0.2
H = 0.0082 ×
Qlow2
Lowest speed capable of
meeting the specified
flow and head values.
0.8
H = 0.0082 ×
Qhigh2
Lowest speed capable of
meeting the specified
flow and head values.
0.2
17.0 ft
Max speed .......................
1.0
≥60.0 ft
Lowest speed capable of
meeting the specified
flow and head values, if
any.
1.0
Low .......
High .......
Waterfall Pumps ...............
Single ...............................
1
High .......
Pressure Cleaner Booster
Pumps.
All .....................................
1
High .......
* As discussed in section III.D.1.e, any pumps that do not meet DOE’s definitions of two-speed, multi-speed, or variable-speed pool filter pump, as applicable, and,
in the case of two-speed self-priming pool filter pumps that are greater than or equal to 0.711 rated hydraulic horsepower and less than 2.5 rated hydraulic horsepower and do not meet the requirements to apply the two-speed pool filter pump test method must be tested as a single-speed pool filter pump.
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E. Determination of Pump Performance
As part of DOE’s test procedure for
dedicated-purpose pool pumps, DOE is
specifying how to measure the
performance of the dedicated-purpose
pool pump at the applicable load points
consistently and unambiguously.
Specifically, to determine WEF for
applicable dedicated-purpose pool
pumps, the test procedure specifies
methods to measure the driver input
power to the motor or to the DPPP
controls (if any) and the flow rate at
each specified load point, as well as the
hydraulic output power at maximum
speed on system curve C (i.e., the rated
hydraulic horsepower, see section
III.G.1).
The following section III.E.1 discusses
the industry standard DOE is
incorporating by reference for
measuring the performance of
dedicated-purpose pool pumps. The
September 2016 DPPP test procedure
NOPR proposed several exceptions,
modifications, and additions to this base
test procedure that DOE deemed
necessary to ensure accuracy and
repeatability. These are presented in
sections III.E.2.a through III.E.2.f.
Finally, DOE is adopting specific
procedures for calculating the WEF from
the collected test data and rounding the
values to ensure that the test results are
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determined in a consistent manner
(section III.E.2.g).
1. Incorporation by Reference of HI
40.6–2014
In the September 2016 DPPP test
procedure NOPR, in accordance with
the DPPP Working Group
recommendations (Docket No. EERE–
2015–BT–STD–0008, No. 51,
Recommendation #8 at p. 6), DOE
proposed to incorporate by reference
certain sections of HI 40.6–2014 as part
of DOE’s test procedure for measuring
the energy consumption of dedicatedpurpose pool pumps, with the
exceptions, modifications, and
additions listed in III.E.2. DOE stated
that HI 40.6–2014 contains the relevant
test methods needed to accurately
characterize the performance of
dedicated-purpose pool pumps, with a
few exceptions, modifications, and
additions. Id. Specifically, HI 40.6–2014
defines and explains how to calculate
driver power input,29 volume per unit
29 The term ‘‘driver power input’’ in HI 40.6–2014
is defined as ‘‘the power absorbed by the pump
driver’’ and is synonymous with the term ‘‘driver
input power’’ and ‘‘input power to the motor and/
or controls,’’ as used in this document.
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time,30 pump total head,31 pump power
output,32 overall efficiency,33 and other
relevant quantities at the specified load
points necessary to determine the metric
(WEF), and contains appropriate
specifications regarding the test setup,
methodology, standard rating
conditions, equipment specifications,
uncertainty calculations, and tolerances.
DOE also noted that HI 40.6–2014,
with several exceptions, modifications,
and additions was adopted in the
January 2016 general pumps test
procedure final rule. 81 FR 4086, 4109–
4117 (Jan. 25, 2016). Therefore, HI 40.6–
2014, with certain exceptions, is already
incorporated by reference into appendix
30 The term ‘‘volume per unit time’’ in HI 40.6 is
defined as ‘‘the volume rate of flow in any given
section’’ and is used synonymously with ‘‘flow’’
and ‘‘flow rate’’ in this document.
31 The term ‘‘pump total head’’ is defined in HI
40.6–2014 as the difference between the outlet total
head and the inlet total head and is used
synonymously with the terms ‘‘total dynamic head’’
and ‘‘head’’ in this document.
32 The term ‘‘pump power output’’ in HI 40.6 is
defined as ‘‘the mechanical power transferred to the
liquid as it passes through the pump, also known
as pump hydraulic power.’’ It is used
synonymously with ‘‘hydraulic horsepower’’ in this
document. However, where hydraulic horsepower
is used to reference the capacity of a dedicatedpurpose pool pump, it refers to the rated hydraulic
horsepower, as defined in section III.G.1.
33 The term ‘‘overall efficiency’’ is defined in HI
40.6–2014 as a ratio of pump power output to driver
power input and describes the combined efficiency
of a pump and driver.
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Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
A to subpart Y of part 431. 10 CFR
431.463.
In response to DOE’s proposal to
incorporate by reference certain sections
of HI 40.6–2014, CEC expressed its
support of DOE’s proposal. (CEC, No. 7
at p. 2) Conversely, APSP and Hayward
suggested that DOE consider raising the
upper limit of the test fluid required in
HI 40.6–2014 from 86 °F to 107 °F to be
consistent with the requirements for
other test standards, including NSF–50
and ENERGY STAR. APSP and
Hayward added that this would allow
for manufacturers to establish and
maintain one temperature volume of
water for NSF, ENERGY STAR, and
DOE testing, allowing for more efficient
use of laboratory resources. (APSP, No.
8 at pp. 5–6; Hayward, No. 6 at p. 4)
In response to APSP and Hayward’s
suggestion that DOE allow the use of
warmer temperature water for use in
testing dedicated-purpose pool pumps,
DOE evaluated the impact of using
107 °F water as opposed to water
between 50 and 86 °F on the determined
WEF, rated hydraulic horsepower, or
other metrics. Based on DOE’s review,
testing with water up to 107 °F would
have an insignificant impact on the
resultant metrics and, therefore, to
reduce testing burden and allow DOE
testing to be streamlined with testing for
other programs, DOE is adopting
requirements for the test fluid that allow
testing with water up to 107 °F, as
requested by APSP and Hayward.
Similarly, in their comments, APSP
and Hayward also requested that DOE
use a nephelometric turbidity unit
(NTU) measurement to determine and
describe the appropriate test fluid for
testing dedicated-purpose pool pumps,
as opposed to the kinematic viscosity
and maximum density metrics used in
HI 40.6–2014 and proposed by DOE.
APSP and Hayward requested
clarification regarding whether test labs
would be required to measure the
kinematic viscosity and density of the
test water and whether these parameters
would need to be included in test
reports and data. APSP and Hayward
stated that test lab water is not currently
measured to determine kinematic
viscosity and density. APSP and
Hayward stated that it is not clear what
options test labs will have if incoming
municipal supply water does not meet
the proposed requirements for
kinematic viscosity and density. APSP
and Hayward believe that the NTU
measurement, which is currently
referenced in the NSF/ANSI 50–2015
test and was been used in the DPPP
industry for over 20 years, is a more
convenient and cost effective criteria to
use to specify the characteristics of the
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19:37 Aug 04, 2017
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test fluid. (APSP, No.8 at pp. 5–6;
Hayward, No. 6 at pp. 4–5).
In response to APSP’s and Hayward’s
suggestion regarding the characteristics
of the test fluid, DOE notes that it
reviewed the test fluid requirements for
NSF/ANSI 50–2015, the ENERGY STAR
Test Method for Pool Pumps,34 and HI
40.6–2014. As discussed in the
September 2016 DPPP test procedure
NOPR, section C.3.3, ‘‘Test conditions,’’
of NSF/ANSI 50–2015 specifies test
conditions for both swimming pools and
hot tubs/spas in terms of temperature
and NTU thresholds, as shown in Table
III.7. That section further states that all
pumps, except those labeled for
swimming pool applications only, are to
be tested at the hot tub/spa conditions.
81 FR 64580, 64625–64626 (Sept. 20,
2016).
TABLE III.7—TEST CONDITIONS
SPECIFIED IN NSF/ANSI 50–2015
Measurement
Swimming
pool
Water Temperature.
Turbidity ..........
75 ± 10 °F ..
102 ± 10 °F
≤15 NTU * ...
≤15 NTU
Hot tub/spa
* NTU = Nephelometric Turbidity Units; a
measure of how much light is scattered by the
particles contained in a water sample.
Section 40.6.5.5, ‘‘Test conditions,’’ of
HI 40.6–2014, which was proposed to be
incorporated by reference into the DPPP
test procedure in the September 2016
DPPP test procedure NOPR, specifies
that all testing must be conducted with
‘‘clear water’’ that is between 50 and
86 °F, where clear water means water
with a maximum kinematic viscosity of
1.6 × 10¥5 ft2/s and a maximum density
of 62.4 lb/ft3. 81 FR at 64614–64615.
The ENERGY STAR Test Method for
Pool Pumps 35 does not appear to
contain requirements regarding the
temperature of the test fluid.
In response to APSP’s and Hayward’s
concern regarding the availability of
‘‘clear water’’ as defined in HI 40.6–
2014, DOE notes that the characteristics
of clear water specified in HI 40.6–2014
are meant to be inclusive of any fresh
water in the temperature range of
interest, as well as sea water, and would
certainly be available from any tap. For
34 EPA. 2013. ‘‘ENERGY STAR Program
Requirements Product Specification for Pool
Pumps—Final Test Method.’’ Available at: https://
www.energystar.gov/sites/default/files/specs/Pool
%20Pump%20Final%20Test%20Method%200115-2013.pdf.
35 EPA. 2013. ‘‘ENERGY STAR Program
Requirements Product Specification for Pool
Pumps—Final Test Method.’’ Available at: https://
www.energystar.gov/sites/default/files/specs/Pool
%20Pump%20Final%20Test%20Method%200115-2013.pdf.
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reference, the kinematic viscosity of
fresh water between 50 and 107 °F
ranges from 1.4 × 10¥5 ft2/s to 0.69 ×
10¥5 ft2/s, respectively, while the
kinematic viscosity of sea water is
approximately 1.24 × 10¥5 ft2/s at
68 °F.36 However, DOE acknowledges
that DPPP manufacturers may be less
familiar with the measurement of
kinematic viscosity than NTU. As the
characterization of the test fluid is not
expected to greatly affect the resultant
WEF score, provided testing is done
with municipal water within a
reasonable temperature range, DOE
agrees with Hayward that the NTU
metric referenced by NSF/ANSI 50–
2015 is also an acceptable criteria to
describe water that is reasonably free
from impurities for the purposes of
testing.
As discussed in the September 2016
DPPP test procedure NOPR, DOE noted
that the viscosity and density
requirements adopted in HI 40.6–2014
are intended to accomplish the same
purpose as the turbidity limits in NSF/
ANSI 50–2015, to ensure the test is
conducted with water that does not
have contaminants or additives in such
concentrations that they would affect
the thermodynamic properties of the
water. Therefore, to better align with
NSF/ANSI 50–2015 and the existing
capabilities and experience of DPPP test
labs, in this final rule, DOE is adopting
requirements that testing be carried out
with water that is between 50 and
107 °F with less than or equal to 15
NTU, as opposed to the ‘‘clear water’’
defined in section 40.6.5.5 of HI 40.6–
2014. DOE will also exclude section
40.6.5.5 of HI 40.6–2014 from the
incorporation by reference into the DOE
test procedure, as that section will no
longer be necessary. As a result,
measurements of kinematic viscosity
and density of the test fluid will not be
required, minimizing burden on
manufacturers. However, measurements
of fluid temperature and NTU will be
required to be made and maintained as
part of the test records underlying
certification to DOE to ensure that the
test fluid is in accordance with the DOE
requirements.
With regard to DOE’s proposal to
incorporate by reference appendix D of
HI 40.6–2014, ‘‘Suitable Time Periods
for Calibration of Test Instruments,’’
APSP and Hayward noted that HI 40.6–
2014 does not explicitly provide an
option for historical data to be used as
a basis to support a longer recalibration
36 Engineering Toolbox. Liquids—Kinematic
Viscosity. Last accessed Nov. 15, 2016. Available at:
https://www.engineeringtoolbox.com/kinematicviscosity-d_397.html.
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interval than recommended by table D.1
of HI 40.6–2014. APSP and Hayward
stated that this provision used to be
available as an option in HI 14.6–2011.
APSP and Hayward added that it
currently calibrates all instruments
annually, in accordance with ISO
17025,37 which would not comply with
some of the required calibration
intervals in HI 40.6–2014, such as 0.33
years for pressure transducers. As such,
APSP and Hayward suggested DOE
include a provision to allow for
historical data to be used to determine
longer calibration intervals than
currently provided for in appendix D of
HI 40.6–2014 (APSP, No. 8 at pp. 5–6;
Hayward, No. 6 at p. 5).
In response to APSP’s and Hayward’s
suggestion regarding the allowance for
extended calibration intervals beyond
those specified in appendix D of HI
40.6–2014 based on historical data, DOE
agrees that such a provision used to be
available in ANSI/HI 14.6–2011, which
preceded HI 40.6–2014. DOE
understands that it is common practice
to extend the calibration interval of
some equipment that has demonstrated,
based on past calibration data, to
maintain calibration over several
calibration cycles. DOE also recognizes
that this can reduce the burden of
maintaining equipment within the
specifications required by the DOE test
procedure. As such, DOE believes it is
reasonable to allow the use of historical
test data to justify calibration intervals
longer than those specified in table D.1
of HI 40.6–2014 and that such a
provision does not compromise the
accuracy of the resultant test data.
However, DOE believes additional
specificity is required to ensure that
unreasonably long time periods between
calibration intervals are not permitted.
Therefore, DOE is adopting
requirements in this final rule that
historical calibration data may be used
to justify time periods up to three times
longer than those specified in table D.1
of HI 40.6–2014. In such a case, the
supporting historical data must show
maintenance of calibration of the given
instrument up to the selected extended
calibration interval on at least two
unique occasions, based on the interval
specified in HI 40.6–2014. For example,
in the case of the pressure transducers
discussed by Hayward, Hayward may
justify a calibration interval up to 1
year 38 (three times the calibration
interval of 0.33 years specified in HI
40.6–2014) based on calibration data
taken at least every 0.33 years that
demonstrates that the calibration has
been maintained for 1 year for at least
two different years.
China stated, in written comments, its
belief that the proposed test method did
not provide a test method for total head.
(China, No. 14 at p. 3) DOE disagrees
and clarifies that, as stated previously,
the proposed test procedure proposed to
incorporate by reference certain sections
of HI 40.6–2014, which contain relevant
specifications regarding test setup,
methodology, standard rating
conditions, equipment specifications,
uncertainty calculations, and tolerances
to measure pump total head, among
other pump performance metrics.
DOE did not receive any comments on
any of the other sections of HI 40.6–
2014 DOE proposed to incorporate by
reference. Therefore, in this final rule,
DOE incorporates by reference HI 40.6–
2014, with certain exceptions,
modifications, and additions, into the
new appendices B and C (see section
III.H) to subpart Y that will contain the
DPPP test procedure. DOE notes that
DOE is using the nomenclature ‘‘HI
40.6–2014–B’’ in the regulatory text to
refer to the incorporation by reference of
HI 40.6–2014 for the dedicated-purpose
36889
pool pumps test procedure in
appendices B and C and differentiate it
from the existing incorporation by
reference of HI 40.6–2014 to appendix A
established in the January 2016 general
pumps test procedure final rule. 81 FR
4086, 4109–4117 (Jan. 25, 2016).
2. Exceptions, Modifications and
Additions to HI 40.6–2014
In general, DOE finds the test methods
contained within HI 40.6–2014 are
sufficiently specific and reasonably
designed to produce test results
necessary to determine the WEF of
applicable dedicated-purpose pool
pumps. However, only certain sections
of HI 40.6–2014 are applicable to the
new DPPP test procedure. In addition,
DOE requires a few exceptions,
modifications, and additions to ensure
test results are as repeatable and
reproducible as possible. DOE’s
modifications and clarifications to HI
40.6–2014 are addressed in the
subsequent sections III.E.2.a through
III.E.2.g.
a. Applicability and Clarification of
Certain Sections of HI 40.6–2014
Although DOE is incorporating by
reference HI 40.6–2014 as the basis for
the DPPP test procedure, DOE noted in
the September 2016 DPPP test
procedure NOPR that some sections of
the standard are not applicable to the
DPPP test procedure and other sections
require clarification regarding their
applicability when conducting the DPPP
test procedure. 81 FR 64580, 64615–20
(Sept. 20, 2016). Table III.8 provides an
overview of the sections of HI 40.6–2014
that DOE proposed to exclude from the
DOE test procedure for dedicatedpurpose pool pumps, as well as those
that DOE proposed to only be optional
and not required for determination of
WEF. Id.
TABLE III.8—SECTIONS OF HI 40.6–2014 DOE PROPOSED TO EXCLUDE FROM INCORPORATION BY REFERENCE OR MAKE
OPTIONAL AS PART OF THE DPPP TEST PROCEDURE
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Section No.
Title
40.6.4.1 ............................
40.6.4.2 ............................
40.6.5.3 ............................
40.6.5.5.1 .........................
40.6.5.5.2 .........................
40.6.6.1 ............................
40.6.6.2 ............................
40.6.6.3 ............................
A.7 ....................................
Appendix B ......................
Vertically suspended pumps .............................................
Submersible pumps ...........................................................
Test report .........................................................................
Test procedure ..................................................................
Speed of rotation during test .............................................
Translation of test results to rated speed of rotation ........
Pump efficiency .................................................................
Performance curve ............................................................
Testing at temperatures exceeding 30 °C (86 °F) ............
Reporting of test results ....................................................
37 ISO/IEC 17025, ‘‘General requirements for the
competence of testing and calibration laboratories,’’
is an internationally recognized standard that
contains specifics on testing, calibration methods,
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19:37 Aug 04, 2017
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Applicability
Excluded.
Excluded.
Excluded.
Certain Portions Optional for Representations.
Excluded.
Excluded.
Optional for Representations.
Optional for Representations.
Excluded.
Excluded.
data quality management systems, and other general
requirements for test laboratories to carry out
testing or calibration. See www.iso.org for more
information.
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38 While DOE acknowledges that three times 0.33
is 0.99, 0.99 years can practically be treated as 1
year, as the calibration intervals are not precise to
the hundredths of a year (±3 days).
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In the September 2016 DPPP test
procedure NOPR, DOE discussed in
detail the specific rationale for
excluding or making optional certain
sections of HI 40.6–2014. 81 FR 64580,
64615 (Sept. 20, 2016).
In response to DOE’s proposal to
exclude certain sections from the
incorporation by reference of HI 40.6–
2014, while making other sections
optional for representations, Hayward
suggested DOE reconsider the exception
of section A.7 of HI 40.6–2017, ‘‘Testing
at temperatures exceeding 30 °C (86
°F),’’ in light of their other suggestions
related to elevated test fluid
temperatures discussed in section
III.E.1. Pentair commented that section
40.6.5.5.2, which requires the speed of
the pump to be within 80 to 120 percent
of the rated speed, should remain a
stipulation of testing and should not be
excluded, especially for single- and twospeed induction motor pumps, as
NEMA–MG requires only better than 7.5
percent of the regulated speed. (Pentair,
No. 11 at p. 3) China also commented
that the proposed test procedure did not
define a test method for rotating speed
and, similarly, suggested maintaining
speed between 80 and 110 percent of
rated rotating speed. (China, No. 14 at
p. 3)
In response to Hayward’s comment
regarding the proposed exclusion of
section A.7 of HI 40.6–2014, as
discussed in section III.E.1, DOE is
adopting alternative criteria to describe
the test fluid in lieu of the criteria
specified in HI 40.6–2014. Therefore, a
specific accommodation to test at higher
temperatures, as specified in appendix
A.7 of HI 40.6–2014, is not required. In
addition, DOE notes that the
instructions in section A.7 are not
currently very descriptive and could
introduce ambiguity to the test. As such,
DOE excludes section A.7 of HI 40.6–
2014 from incorporation by reference in
this final rule.
In response to Pentair and China’s
comments regarding the measurement of
and tolerances related to rotational
speed, DOE clarifies that the adopted
test procedure references specific load
points for different varieties and speed
configurations of dedicated-purpose
pool pumps, as described in section
III.D. These load points were
specifically recommended by the DPPP
Working Group and include
specifications regarding the flow, head,
and speed at each load point. For
example, single-speed pool filter pumps
must be evaluated on curve C at the
maximum speed, which is typically the
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only speed available.39 Two-speed pool
filter pumps must be evaluated at the
maximum and low speed, which are, by
definition, the only speeds available on
the pump. The load points for multispeed and variable-speed pool filter
pumps do not specify speed values, but
are described with respect to specific
head and flow requirements. In all
cases, tolerances around a given speed
value are not relevant since there is no
‘‘target’’ speed value that must be
attained. Instead, DOE describes
tolerances around the tested flow or
head values that must be achieved, as
those values have specified values or
thresholds that must be achieved and
drive the specification of the load point.
While the speed is integral to attaining
a given load point, the tested speed is
a dependent variable to satisfy the
required head and flow values based on
the capabilities of the pump. Therefore,
DOE does not believe that allowing
measurements at alternative speeds,
either those specified in section
40.6.5.5.2 or NEMA MG–1–2016, is
necessary or relevant to the DPPP test
procedure. In addition, DOE
understands the primary purpose of
section 40.6.5.5.2 is to accommodate
testing of very large pumps that may
overload the power supply of the test
lab when run at full speed. DOE does
not believe this is a concern for
dedicated-purpose pool pumps, most of
which are less than 2.5 rated hydraulic
horsepower. Therefore, this final rule
does not incorporate by reference
section 40.6.5.5.2, and requires all
testing to be conducted at the
appropriate load points specified in
section III.D for each DPPP variety and
speed configuration. Regarding
measurement of speed, DOE notes that
HI 40.6–2014, which is incorporated by
reference in the adopted test procedure,
includes specifications for measuring
rotating speed.
DOE did not receive any other
comments pertaining to the other
sections DOE proposed to exclude from
DOE’s incorporation by reference.
Therefore, in this final rule, DOE is not
incorporating by reference section
40.6.4.1, 40.6.4.2, 40.6.5.3, 40.6.5.5.2,
40.6.6.1, section A.7 of appendix A, and
appendix B of HI 40.6–2014 as part of
the DOE test procedure for dedicated39 As described in more detail in section III.D.1.e,
if a dedicated-purpose pool pump does not meet the
definition of a two-speed, multi-speed, or variablespeed dedicated-purpose pool pump discussed in
section III.B.7, or the necessary criteria to apply the
two-speed test method discussed in section
III.D.1.e, such a pump must be tested using the
single-speed pool filter pump test point, regardless
of the number of operating speeds the pump may
have.
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purpose pool pumps. In addition, as
discussed in section III.E.1, as DOE is
adopting alternative criteria to describe
the test fluid. For that reason, DOE is
also excluding section 40.6.5.5 from the
incorporation by reference of HI 40.6–
2014. To allow manufacturers to make
voluntary representations of other
metrics, in addition to WEF, DOE
incorporates by reference section
40.6.5.5.1, section 40.6.6.2, and section
40.6.6.3, of HI 40.6–2014 and clarifies
that these sections are not required for
determination of WEF, but may be
optionally conducted to determine and
make representations about other DPPP
performance parameters.
b. Calculation of Hydraulic Horsepower
In addition to the clarifications
regarding the applicability of certain
sections of HI 40.6–2014 to the DPPP
test procedure, DOE believes that
clarification is also required regarding
the calculation of hydraulic horsepower.
As discussed in the September 2016
DPPP test procedure NOPR, DOE
proposed that hydraulic horsepower
must be calculated with a unit
conversion factor of 3956, instead of
3960, which is specified in HI 40.6–
2014. 81 FR 64580, 64617 (Sept. 20,
2016). DOE explained that using a value
of 3956 is more accurate and precise
given the properties of the specified test
fluid. Also, as noted, in the September
2016 DPPP test procedure NOPR, the
conversion factor of 3956 was adopted
also in the January 2016 general pumps
test procedure final rule. 81 FR 4086,
4109 (Jan. 25, 2016).
In response to DOE’s proposal, during
the September 2016 DPPP test
procedure NOPR public meeting,
Hayward sought clarification from DOE,
as it believed that the value referred to
the rotating speed of the pump.
Hayward questioned whether this was
the same value used during the DPPP
Working Group meetings. (Hayward,
Public Meeting Transcript, No. 3 at pp.
62–63) In response, during the
September 2016 DPPP test procedure
NOPR public meeting, Pentair clarified
that the value was a unit conversion
(Pentair, Public Meeting Transcript, No.
3 at pp. 62–63) and DOE clarified that
the value of 3956 (as proposed in the
September 2016 DPPP test procedure
NOPR) was the one used throughout the
DPPP Working Group meetings. APSP
and Hayward later suggested, in their
written comments, that the DPPP test
procedure continue to rely on the 3960
value historically used in all hydraulic
power calculations. (APSP, No. 8 at p.
6)
While DOE believes that the value of
3956 proposed in the September 2016
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DPPP test procedure NOPR is more
precise and accurate given the specific
gravity of 1.0 assumed in the calculation
of hydraulic power, the value of the unit
conversion (3956 or 3960) does not
meaningfully impact the resultant rated
hydraulic horsepower within the
number of number of digits to which
rated hydraulic horsepower is to be
reported. Therefore, in this final rule,
DOE adopts a requirement that
hydraulic horsepower must be
calculated with a unit conversion factor
of 3960, consistent with Hayward’s
request.
c. Data Collection and Determination of
Stabilization
The DPPP test procedure must
provide instructions regarding how to
sample and collect data at each load
point. Such instructions must ensure
that the collected data are taken at
stabilized conditions that accurately and
precisely represent the performance of
the dedicated-purpose pool pump at the
designated load points, thus improving
repeatability of the test.
In the September 2016 DPPP test
procedure NOPR, DOE explained that
section 40.6.5.5.1 of HI 40.6–2014
provides that all measurements shall be
made under steady state conditions.
DOE stated that the requirements for
determining when the pump is
operating under steady state conditions
in HI 40.6–2014 were described as
follows: (1) There is no vortexing, (2)
the margins are as specified in ANSI/HI
9.6.1, ‘‘Rotodynamic Pumps Guideline
for NPSH Margin,’’ and (3) the mean
value of all measured quantities
required for the test data point remains
constant within the permissible
amplitudes of fluctuations defined in
Table 40.6.3.2.2 of HI 40.6–2014 over a
minimum period of 10 seconds before
performance data are collected. 81 FR
64580, 64617 (Sept. 20, 2016).
In addition to the requirements
specified in section 40.6.5.5.1 of HI
40.6–2014, in the September 2016 DPPP
test procedure NOPR, DOE proposed
requirements that at least two unique
measurements must be used to
determine stabilization when testing
pumps according to the DPPP test
procedure. 81 FR 64580, 64617 (Sept.
20, 2016). DOE explained within the
September 2016 test procedure NOPR,
that HI 40.6–2014 does not specify the
measurement interval for determination
of steady state operation. Id. DOE’s
proposal of two measurements is the
same as the requirement established in
the January 2016 general pumps test
procedure final rule. 81 FR 4086, 4011
(Jan. 25, 2016). This requirement
accommodates a longer period between
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the sampling of individual data points,
as compared to the ENERGY STAR
program. 81 FR 64580, 64617 (Sept. 20,
2016).
Section 40.6.3.2.2 of HI 40.6–2014,
‘‘Permissible fluctuations,’’ specifies
that permissible damping devices may
be used to minimize noise and large
fluctuations in the data in order to
achieve the specifications noted in
Table 40.6.3.2.2 of HI 40.6–2014. In the
September 2016 DPPP test procedure
NOPR, similar to the January 2016
general pumps test procedure final rule
(81 FR 4086, 4011 (Jan. 25, 2016)), DOE
proposed that damping devices are only
permitted to integrate up to the
measurement interval to ensure that
each stabilization data point is reflective
of a separate measurement. 81 FR
64580, 64617 (Sept. 20, 2016). DOE also
proposed in the September 2016 DPPP
test procedure NOPR that, for physical
dampening devices, the pressure
indicator/signal must register 99 percent
of a sudden change in pressure over the
measurement interval to satisfy the
requirement for unique measurements.
This requirement is consistent with
annex D of ISO 3966:2008(E),
‘‘Measurement of fluid flow in closed
conduits—Velocity area method using
Pitot static tubes,’’ which is referenced
in HI 40.6–2014 for measuring flow with
pitot tubes. 81 FR 64580, 64617 (Sept.
20, 2016).
In response to DOE’s proposed
stabilization requirements, particularly
those incorporated by reference in
section 40.6.5.5.1 of HI 40.6–2014,
APSP and Hayward requested
clarification of the definition of
‘‘vortexing’’ and an explanation of how
to specifically determine if vortices are,
or are not present. (APSP, No. 8 at pp.6–
7; Hayward, No. 6 at p. 6) In response,
DOE acknowledges that DOE did not
propose a definition for ‘‘vortexing’’ or
‘‘vortices,’’ and such definitions are not
contained in HI 40.6–2014. After
reviewing the context of section
40.6.5.5.1 of HI 40.6–2014, DOE
concludes that the language of ‘‘no
vortexing’’ is a redundant, but
informative statement, related to
defining steady state conditions. In
other words, vortexing is a specific
scenario, which would cause test
readings to fluctuate beyond the
permissible amplitudes of fluctuations
defined in Table 40.6.3.2.2 of HI 40.6–
2014 over a minimum period of 10
seconds before performance data are
collected. Accordingly, DOE will not
establish any further definitions or
verification procedures related to
vortexing or vortices. Under section
40.6.5.5.1 of HI 40.6–2014, as
incorporated by reference into the test
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36891
procedure, steady state is achieved
when the mean value of all measured
quantities required for the test data
point remain constant within the
permissible amplitudes of fluctuations
defined in Table 40.6.3.2.2 over a
minimum time of 10 seconds before
data are collected. No explicit
measurement or determination of
vortexing or vortices is required.
DOE did not receive any additional
comments on this proposal and,
therefore, is adopting, in this final rule,
the proposal that determination of
stabilization must be made based on at
least two unique measurements and any
damping devices are only permitted to
integrate up to the data collection
interval.
d. Test Tolerances
As discussed in section III.D, DOE
proposed in the September 2016 DPPP
test procedure NOPR to specify unique
load points for each DPPP variety and
speed configuration. As DOE noted in
the September 2016 DPPP test
procedure NOPR, HI 40.6–2014 does not
specify how close a measured data point
must be to the specified load point or
if that data point must be corrected in
any way for deviations from the
specified value. 81 FR 64580, 64617–18
(Sept. 20, 2016).
In the September 2016 DPPP test
procedure NOPR, consistent with the
tolerances adopted in the ENERGY
STAR test procedure, DOE proposed
tolerances of ±2.5 percent on flow rate
for self-priming and non-self-priming
pool filter pumps and pressure cleaner
booster pumps. However, due to the fact
that the load point for waterfall pumps
is specified as a fixed head value, DOE
proposed a tolerance of ±2.5 percent of
head for waterfall pumps. DOE did not
propose a tolerance on the tested speed,
as the tested maximum speeds are
specific to each dedicated-purpose pool
pump being tested. 81 FR 64580, 64617–
18 (Sept. 20, 2016).
In response to DOE’s proposal, APSP
and Hayward commented that
maintaining ±2.5 percent of the
specified flow rate or head value will be
difficult to achieve, particularly with
regards to the 10 gpm load point for
pressure cleaner booster pumps. APSP
and Hayward requested any exemplary
data that demonstrates stabilization can
be maintained within the specified
tolerance at low head or flows and that
DOE consider a larger tolerance for low
flow or head measurements (APSP, No.
8 at p. 7; Hayward, No. 6 at p. 6).
In response to APSP’s and Hayward’s
request for larger tolerances on low flow
and head values, DOE reiterates that
DOE based the proposal in the
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September 2016 DPPP test procedure
NOPR on the existing tolerance
requirements in the ENERGY STAR Test
Method for Pool Pumps.40 The ENERGY
STAR method applies to all load points
specified by the test method, including
the minimum speed test point for
variable-speed dedicated-purpose pool
pumps. DOE also notes that the flow
rates on Curves A, B, and C at minimum
flow rate for many variable-speed
dedicated-purpose pool pumps are at or
below 10 gpm, as demonstrated in
DOE’s Self-Priming Pool Filter Pump
Performance Database. (Docket No.
EERE–2015–BT–STD–0008, No. 102)
Specifically, 43 of the 83 total variablespeed self-priming pool filter pumps in
DOE’s database report flow rates less
than or equal to 10 gpm and at least 19
of those 43 models are from the
ENERGY STAR database.41 Based on the
fact that such requirements can be met
to certify pumps in accordance with
ENERGY STAR, DOE believes that such
a requirement can be met when
conducting the DOE DPPP test
procedure. Although the pumps in the
ENERGY STAR database should be
conforming to the flow and head
tolerances, DOE does not have access to
source data to confirm this. Therefore,
in light of Hayward’s comment, in this
final rule, DOE is adopting a broader
tolerance requirement for lower flow
scenarios. Specificity, the flow tolerance
will be ±2.5 percent of the specified
flow rate or ±0.5 gpm, whichever is
greater. DOE believes that a range of 1.0
gpm can reasonably be maintained with
typical lab testing equipment. DOE
notes that such an accommodation is
not necessary for waterfall pumps, since
the tolerance is a fixed 17.0 ± 0.425 feet.
In addition, based on the revised load
points for multi-speed and variablespeed pool filter pumps presented in
section III.D.1.c, DOE notes that the
multi-speed and variable-speed pool
filter pump load points are now
specified with respect to the head value
(i.e., H = 0.0082 × Q2), while the flow
point may vary based on the operating
speeds available on the pump.
Therefore, in this final rule, DOE is
revising the tolerances for the multispeed and variable-speed pool filter
pump test points to be achieved within
±2.5 percent of the specified head value,
40 EPA. 2013. ‘‘ENERGY STAR Program
Requirements Product Specification for Pool
Pumps—Final Test Method.’’ Available at: https://
www.energystar.gov/sites/default/files/specs/Pool
%20Pump%20Final%20Test%20Method%200115-2013.pdf.
41 ENERGY STAR maintains a database of
certified products, including pool pumps. See
https://www.energystar.gov/productfinder/product/
certified-pool-pumps/results.
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which is curve C. DOE is adopting all
other tolerances as proposed in the
September 2016 DPPP test procedure
NOPR.
e. Power Supply Characteristics
In the September 2016 DPPP test
procedure NOPR and consistent with
the January 2016 general pumps test
procedure final rule (81 FR 4086, 4112–
4115 (Jan. 25, 2016)), DOE proposed
tolerances for voltage, frequency,
voltage unbalance, and total harmonic
distortion that must be maintained at
the input terminals to the motor and/or
control, as applicable, when conducting
the DPPP test procedure. 81 FR 64580,
64618–19 (Sept. 20, 2016). DOE
discussed how the measurement of
input power to the driver is an
important element of the test, because
input power is a key component of
WEF. In addition, in the September
2016 DPPP test procedure NOPR, DOE
discussed how large differences in
voltage, frequency, voltage unbalance,
or total harmonic distortion can affect
the performance of the motor and/or
control under test. Id.
DOE believes that, because dedicatedpurpose pool pumps utilize electrical
equipment (i.e., motors and drives)
similar to that used by general pumps,
such requirements also apply when
testing dedicated-purpose pool pumps.
In the September 2016 DPPP test
procedure NOPR, DOE proposed that
when testing dedicated-purpose pool
pumps the following conditions would
apply to the main power supplied to the
motor or controls, if any:
• Voltage maintained within ±5
percent of the rated value of the motor.
• Frequency maintained within ±1
percent of the rated value of the motor.
• Voltage unbalance of the power
supply maintained within ±3 percent of
the rated value of the motor.
• Total harmonic distortion
maintained at or below 12 percent
throughout the test. 81 FR 64580, 64619
(Sept. 20, 2016).
APSP and Hayward submitted
comments regarding voltage unbalance
of the power supply. APSP and
Hayward were familiar with a voltage
unbalance in a three-phase power
supply, but were unclear about how it
applied to a single-phase power supply.
(APSP, No. 8 at p.7; Hayward, No. 4 at
p.1; Hayward, No. 6 at pp. 6–7) In
response, voltage unbalance or
imbalance is defined as the largest
difference between the average RMS
voltage and the RMS value of any single
voltage phase divided by the average
RMS voltage, usually expressed as a
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percentage.42 Voltage unbalance is a
function of multiple phase power
supplies and, by definition, does not
exist in single-phase power supplies. As
there is no voltage unbalance in a
single-phase power supply, the
requirement to maintain voltage
unbalance within ±3 percent of the rated
value of the motor only applies to
pumps with motors driven by a threephase power supply.
APSP and Hayward also requested
that DOE confirm that the voltage
unbalance specification of ‘‘±3 percent
of the rated value of the motor’’ applies
to the rated voltage of the motor. (APSP,
No. 8 at p. 7; Hayward, No. 6 at pp. 6–
7) In response, DOE agrees that the
proposal in the September DPPP 2016
test procedure NOPR could be clarified.
DOE understands that motors typically
do not have nominal rated voltage
unbalance values, similar to the
nominal rated frequency and voltage
values listed on many motor
nameplates. In this case ‘‘±3 percent of
the rated value of the motor’’ refers to
‘‘the value at which the motor was
rated.’’ That is, the value is referring to
the voltage unbalance associated with
the rated efficiency of the motor. DOE
also notes that, in IEEE Standard 112–
2004, ‘‘IEEE Standard Test Procedure for
Polyphase Induction Motors and
Generators,’’ (IEEE 112–2004) and the
Canadian Standards Association (CSA)
C390–10, ‘‘Test methods, marking
requirements, and energy efficiency
levels for three-phase induction
motors,’’ (CSA C390–10), which are the
test methods incorporated by reference
as the DOE test procedure for electric
motors, a voltage unbalance of ≤0.5
percent is required. Therefore, the
requirement of ‘‘±3 percent of the value
at which the motor was rated’’ can also
be interpreted as ≤3.5 percent for motors
rated in accordance with DOE’s electric
motor test procedure. In this final rule,
DOE will specify the voltage unbalance
requirement as ‘‘±3 percent of value
with which the motor was rated.’’
During the September 2016 DPPP test
procedure NOPR public meeting, CA
IOUs, DOE, and Hayward discussed
total harmonic distortion (THD).
Hayward inquired about differences
related to tolerances between the
September 2016 DPPP test procedure
NOPR and ENERGY STAR and
specifically sought indication of
whether the tolerances in DOE’s
proposal were more stringent than
ENERGY STAR. (Hayward, Public
42 An overview by DOE on voltage unbalance can
be found at: https://energy.gov/sites/prod/files/2014/
04/f15/eliminate_voltage_unbalanced_motor_
systemts7.pdf.
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Meeting Transcript, No. 3 at p. 58) DOE
responded during the September 2016
DPPP test procedure NOPR public
meeting that ENERGY STAR requires
THD to be less than 2 percent and DOE’s
proposal was less than 12 percent.
(DOE, Public Meeting Transcript, No. 3
at p. 59) CA IOUs noted that ENERGY
STAR’s THD requirements were much
more stringent than the proposed DOE
requirements and raised questions if
current test labs can comply with this
value. (CA IOUs, Public Meeting
Transcript, No. 3 at pp. 59–60) Hayward
responded that upon initial review, if a
manufacturer is already conducting
ENERGY STAR testing in-house, that
the DOE proposal does not seem more
stringent, nor did Hayward believe that
the DOE proposal would require any
more elaborate equipment. (Hayward,
Public Meeting Transcript, No. 3 at p.
60) CA IOUs responded that a different
THD value might be necessary in that
the DOE’s proposal of 12 percent seems
unreasonably high, but ENERGY STAR’s
36893
requirement of 2 percent seems
unreasonably low. (CA IOUs, Public
Meeting Transcript, No. 3 at p. 60)
Regarding Hayward’s inquiry as to the
relative stringency of DOE’s proposed
power supply characteristics as
compared to the ENERGY STAR 43 test
procedure for pool pumps,44 DOE notes
that all of DOE’s proposed power supply
characteristic requirements are
equivalent to or less stringent than the
existing ENERGY STAR requirements,
as shown in Table III.9.
TABLE III.9—COMPARISON OF POWER SUPPLY CHARACTERISTICS REQUIREMENTS PROPOSED IN DOE’S SEPTEMBER 2016
DPPP TEST PROCEDURE NOPR AND IN THE ENERGY STAR TEST METHOD FOR POOL PUMPS 45
Power supply characteristic
DOE September 2016 DPPP test procedure
NOPR proposal
Voltage .............................
Frequency ........................
Voltage Unbalance ..........
Total Harmonic Distortion
within ±5 percent of the rated value of the motor .............
within ±5 percent of the rated value of the motor .............
within ±3 percent of the rated value of the motor .............
≤12 percent .......................................................................
ENERGY STAR
within ±1.0 percent of the rated value of the motor.
within ±1.0 percent of the rated value of the motor.
N/A.
≤2.0 percent.
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With regard to CA IOUs comment
regarding DOE’s proposed tolerance on
THD perhaps being too large, DOE notes
that the THD tolerance of 12 percent
was developed based on reasonable
limits that motor systems should be
designed to handle. Further, a THD
tolerance of 12 percent is widely
available on the national electrical grid
and, therefore, is not unduly
burdensome to attain during testing.
DOE discussed this justification, at
length, in the January 2016 general
pumps test procedure final rule. 81 FR
4086, 4112–4118 (Jan. 25, 2016) For
example, regarding limitations on
harmonic distortion on the power
supply, the AMO publication,
‘‘Improving Motor and Drive System
Performance’’ (AMO motor sourcebook)
states that electrical equipment is often
rated to handle 5 percent THD (as
defined in IEEE 519–2014 46), and notes
that motors are typically much less
sensitive to harmonics than computers
or communication systems.47 In
addition, section 5.1 of IEEE 519–2014
recommends line-to-neutral harmonic
voltage limits of 5.0 percent individual
harmonic distortion and 8.0 percent
voltage THD for weekly 95th percentile
short time (10 min) values, measured to
the 50th harmonic. The IEEE standard
also indicates that daily 99th percentile
very short time (3 second) values should
be less than 1.5 times these values.
Hayward also submitted written
comments stating that DOE’s proposed
voltage, frequency, voltage unbalance,
and THD requirements are suitable for
testing dedicated-purpose pool pumps
and were reasonably achievable in
existing laboratory environments.
(Hayward, No. 6 at p. 7) Additionally,
Hayward submitted written comments
that the proposed power supply
requirements in the September 2016
DPPP test procedure NOPR are in
alignment with (or not as stringent as)
the power supply requirements for other
pool pump industry programs including
ENERGY STAR, NSF, and UL.
(Hayward, No. 6 at p. 7) Similarly, APSP
stated that DOE’s proposed power
supply requirements were less stringent
than the requirements used in DOE
motor efficiency testing. (APSP, No. 8 at
p. 7) Both APSP and Hayward felt that
existing equipment would be more than
capable of meeting the proposed
requirements. (APSP, No. 8 at p. 7;
Hayward, No. 6 at p. 7). Ultimately, for
the reasons discussed in this section,
DOE adopts requirements in this final
rule that when testing dedicatedpurpose pool pumps the main power
supplied to the motor or controls, if any,
must maintain voltage within ±5 percent
of the rated value of the motor,
frequency within ±1 percent of the rated
value of the motor, voltage unbalance of
the power supply maintained within ±3
percent of the value with which the
motor was rated, and total harmonic
distortion maintained at or below 12
percent throughout the test.
43 ENERGY STAR is a joint program of the U.S.
Environmental Protection Agency (EPA) and DOE
that establishes a voluntary rating, certification, and
labeling program for highly energy efficient
consumer products and commercial equipment.
Information on the program is available at
www.energystar.gov/index.cfm?c=home.index.
44 EPA. 2013. ‘‘ENERGY STAR Program
Requirements Product Specification for Pool
Pumps—Final Test Method. Rev. Jan–2013’’ https://
www.energystar.gov/sites/default/files/specs/Pool
%20Pump%20Final%20Test%20Method%200115-2013.pdf.
45 EPA. 2013. ‘‘ENERGY STAR Program
Requirements Product Specification for Pool
Pumps—Final Test Method. Rev. Jan-2013’’ https://
www.energystar.gov/sites/default/files/specs/Pool
%20Pump%20Final%20Test%20Method%200115-2013.pdf.
46 IEEE. 2014. Standard 519: ‘‘IEEE
Recommended Practice and Requirements for
Harmonic Control in Electric Power Systems.’’
Available at: https://standards.ieee.org/findstds/
standard/519-2014.html.
47 DOE EERE. Improving Motor and Drive System
Performance—A Sourcebook for Industry. February
2014. Available at www.energy.gov/eere/amo/
motor-systems.
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f. Measurement Equipment for Testing
Appendix C of HI 40.6–2014, which
DOE is incorporating by reference into
the DPPP test procedure, specifies the
required instrumentation to measure
head, speed, flow rate, torque,
temperature, and electrical input power
to the motor. In the September 2016
DPPP test procedure NOPR, DOE
proposes to refer to appendix C of HI
40.6–2014, as incorporated by reference
(see section III.E.1), to specify the
required instrumentation to measure
head, speed, flow rate, and temperature
in the DPPP test procedure. 81 FR
64580, 64619–64620 (Sept. 20, 2016).
However, DOE noted that for the
purposes of measuring input power to
the motor or control, as applicable, of
DPPP models, the equipment specified
in section C.4.3.1, ‘‘electric power input
to the motor,’’ of HI 40.6–2014 may not
be sufficient. Instead, DOE proposed
requirements that electrical
measurements for determining pump
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power input be taken using equipment
capable of measuring current, voltage,
and real power up to at least the 40th
harmonic of fundamental supply source
frequency 48 and have an accuracy level
of ±2.0 percent of the measured value
when measured at the fundamental
supply source frequency when rating
pumps using the testing-based methods
or with a calibrated motor. Id. These
proposed requirements are consistent
with other relevant industry
standards 49 for measurement of input
power to motor and drive systems and
the January 2016 general pumps test
procedure final rule. 81 FR 4086, 4118–
19 (Jan. 25, 2016) DOE notes that the
September 2016 DPPP test procedure
NOPR contained inconsistent
statements with regard to whether the
accuracy requirement was with respect
to full scale or the measured value.
Specifically, the preamble (81 FR
64619–64620) discussed the accuracy
requirement with respect to full scale,
while the proposed regulatory text
discussed accuracy requirements with
respect to the measured value (81 FR
64650). The proposed regulatory text
contained the correct proposal, which is
that electrical measurement equipment
must be accurate to ±2.0 percent of the
measured value. DOE notes that this is
consistent with the requirements
adopted in the January 2016 general
pumps test procedure final rule and is
less stringent than the requirements
contained in the ENERGY STAR Test
Method for Pool Pumps,50 which
requires accuracy of 1.5 percent of the
measured value for power measurement.
In response to DOE’s proposal,
Hayward commented that the
manufacturer of the power analyzer
within Hayward’s lab met the level of
accuracy proposed in the September
2016 DPPP test procedure NOPR.
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48 CSA
C838–13 requires measurement up to the
50th harmonic. However, DOE believes that
measurement up to the 40th harmonic is sufficient,
and the difference between the two types of
frequency measurement equipment will not be
appreciable.
49 Specifically, DOE identified AHRI 1210–2011,
‘‘2011 Standard for Performance Rating of Variable
Frequency Drives’’; the 2013 version of CSA
Standard C838, ‘‘Energy efficiency test methods for
three-phase variable frequency drive systems’’; CSA
C390–10, ‘‘Test methods, marking requirements,
and energy efficiency levels for three-phase
induction motors’’; and IEC 61000–4–7, ‘‘Testing
and measurement techniques—General guide on
harmonics and interharmonics measurements and
instrumentation, for power supply systems and
equipment connected thereto’’ as relevant to the
measurement of input power to the motor or
control.
50 EPA. 2013. ‘‘ENERGY STAR Program
Requirements Product Specification for Pool
Pumps—Final Test Method.’’ Available at: https://
www.energystar.gov/sites/default/files/specs/Pool
%20Pump%20Final%20Test%20Method%200115-2013.pdf.
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(Hayward, No. 6 at p. 11) APSP also
commented that currently existing
motor test data acquisition equipment is
adequate to meet the tolerance limits
proposed by DOE. (APSP, No. 8 at p. 7)
Therefore, for the reasons discussed
in this section, DOE adopts that
electrical measurement equipment must
be capable of measuring current,
voltage, and real power up to at least the
40th harmonic of fundamental supply
source frequency and having an
accuracy level of ±2.0 percent of the
measured value when measured at the
fundamental supply source frequency.
DOE also noted in the September
2016 DPPP test procedure NOPR that HI
40.6–2014 does not contain any
requirements for the instruments used
for measuring distance. Distance must
be measured when determining the selfpriming capability of self-priming and
non-self-priming pool filter pumps (see
section III.G.2). 81 FR 64580, 64620
(Sept. 20, 2016). As such, DOE proposed
in the September 2016 DPPP test
procedure NOPR to require instruments
for measuring distance that are accurate
to and have a resolution of at least ±0.1
inch to improve consistency and
repeatability of test results. Id. DOE
noted that, although this accuracy
requirement is generally applicable,
when used in combination with other
instruments to measure head, both the
accuracy requirements of distancemeasuring instruments and the
specified accuracies for measurement of
differential, suction, and discharge head
apply. Id.
DOE received no comments related to
this proposal. Therefore, in this final
rule, DOE requires instruments for
measuring distance that are accurate to
and have a resolution of at least ±0.1
inch.
g. Calculation and Rounding
Modifications and Additions
DOE notes HI 40.6–2014 does not
specify how to round values for
calculation and reporting purposes.
DOE recognizes that the manner in
which values are rounded can affect the
resulting WEF, and all WEF values
should be reported with the same
precision. Therefore, to improve the
accuracy and consistency of
calculations, DOE proposed in the
September 2016 DPPP test procedure
NOPR that raw measured data be used
to calculate WEF and the resultant value
be rounded to the nearest 0.1. 81 FR
64580, 64620 (Sept. 20, 2016). Similarly,
DOE proposed that all values of EF,
maximum head, vertical lift, and true
priming time be reported to the tenths
place and all other values be reported to
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the hundredths place. 81 FR 64580,
64650 (Sept. 20, 2016).
DOE received no comments related to
this proposal. However, DOE notes that
the June 2016 DPPP Working Group
Recommendations and January 2017
DPPP DFR specify separate standards
for self-priming pool filter pumps with
rated hydraulic horsepower greater than
or equal to 0.711 hp and less than 0.711
hp. (Docket No. EERE–2015–BT–STD–
0008, No. 82, Recommendation #1 at pp.
1–2; 86 FR 5650, 5743). As such, DOE
notes that rated hydraulic horsepower
must be reported to the thousandths
place, consistent with the precision
desired by the DPPP Working Group in
their equipment class specifications.
Therefore, in this final rule, DOE adopts
that all calculations shall be performed
with raw measured data; that WEF, EF,
maximum head, vertical lift, and true
priming time be rounded to the nearest
tenths place; that rated hydraulic
horsepower be reported to the nearest
thousandths place; and all other values
be rounded to the hundredths place.
F. Representations of Test Metrics
In the September 2016 DPPP test
procedure NOPR, DOE stated that
manufacturers of equipment that are
addressed by the proposed test
procedure would have 180 days after
the publication of the test procedure
final rule to begin using the DOE
procedure as the basis for
representations. However, DOE clarified
that manufacturers would not be
required to certify or otherwise make
representations regarding the
performance of applicable dedicatedpurpose pool pumps using the WEF
metric until the compliance date of any
potential energy conservation standards
that DOE might set for dedicatedpurpose pool pumps. However, if
manufacturers elect to make
representations of WEF prior to such
compliance date, they will be required
to do so using the DOE test procedure.
81 FR 64580, 64627–28 (Sept. 20, 2016).
In the September 2016 DPPP test
procedure NOPR, DOE also discussed
how other metrics that are outcomes of
the DPPP test procedure would also
need to be updated to be consistent with
the final DPPP test procedure 180 days
after publication of the final rule in the
Federal Register. Specifically, DOE also
proposed establishing standardized and
consistent methods for determining
several DPPP metrics, including DPPP
horsepower metrics, EF, pump
efficiency, overall efficiency, driver
power input, pump power output, and
power factor. One hundred and eighty
(180) days after the publication of this
final rule any representations of those
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metrics would also be required to be
based on values consistent with the
DOE test procedure. DOE notes that
some of these test methods and
representations were proposed as
optional to allow manufacturers to make
such representations if they chose to. Id.
DOE received many comments related
to the representation of efficiency
metrics, including use of alternative
metrics, the definition of a
representation, the impact on voluntary
programs, and the timing required to
transition to the new test procedure.
These comments and DOE’s responses
are discussed in the following sections
III.F.1, III.F.2, III.F.3, and III.F.4.
1. Representations of Primary Efficiency
Metrics
As discussed in section III.C, DOE is
adopting the WEF as the regulatory
metric for defining the energy efficiency
of dedicated-purpose pool pumps.
Typically, DOE only includes in the test
procedure the DOE metric (the metric
used for the energy conservation
standards), and EPCA requires
manufacturers to switch over to use of
the DOE metric for representations
beginning 180 days of publication of the
test procedure final rule. This helps
ensure standardization of efficiency
representations throughout the industry
and eliminates potential confusion in
the market place if multiple nonequivalent metrics are used to describe
the same piece of equipment. DOE
believes that requiring use of the single,
standardized DOE metric determined
through a public notice and comment
process is the most appropriate
approach. A single, standardized metric
that provides a comprehensive picture
of the equipment’s energy performance
will provide a clear and consistent basis
for consumers to compare and select
dedicated-purpose pool pumps.
As described in detail in the
September 2016 DPPP test procedure
NOPR, EF is the metric currently used
in the industry to describe the energy
performance of dedicated-purpose pool
pumps. 81 FR 64580, 64598–64600
(Sept. 20, 2016). EF describes the
efficiency of the dedicated-purpose pool
pump, in terms of gal/Wh, at a single
speed point and on a single system
curve. However, there are multiple
tested speeds and system curves that
can be used to determine EF, resulting
in multiple EF values. For example, a
single pump can have up to nine
different EF values, making selection
and comparison of equipment
confusing.
Conversely, WEF uses the same
measured input data as EF (flow in
gallons and input power in W), but
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weights the efficiency of the pump at
multiple speeds into one comprehensive
and consistent metric that better
represents the average efficiency of the
equipment during typical operation.
This makes product comparison and
selection more straightforward. During
the DPPP Working Group discussions,
the Working Group members agreed that
the weighted average approach was a
good approach to achieve a single
energy metric that would be
representative of the energy efficiency of
dedicated-purpose pool pumps, while
allowing for an equitable differentiation
and comparison of performance among
different DPPP models and technologies
and providing the necessary and
sufficient information for purchasers to
make informed decisions regarding
DPPP selection. (Docket No. EERE–
2015–BT–STD–0008, No. 38 at pp. 212–
213; Docket No. EERE–2015–BT–STD–
0008, No. 58 at pp. 170–171 and 178)
The DPPP Working Group also agreed
that, currently, comparing the multiple
EF values was confusing and made
equipment comparisons difficult. The
DPPP Working Group also stated that
some of the EF values did not
meaningfully represent the efficiency of
the equipment . (Docket No. EERE–
2015–BT–STD–0008, No. 38 at p. 133;
Docket No. EERE–2015–BT–STD–0008,
No. 58 at pp. 170–171)
However, the DPPP Working Group
also discussed the importance of the EF
metric for making product selections for
specific applications or making energy
saving calculations in support of utility
programs. (Docket No. EERE–2015–BT–
STD–0008, No. 38 at p. 133 and 213–
214; Docket No. EERE–2015–BT–STD–
0008, No. 58 at pp. 167–170 and 174–
175) Due to the interest expressed in the
use of the EF metric during the DPPP
Working Group negotiations, in contrast
to typical practice, DOE proposed to
allow the representation of two metrics,
EF and WEF. Specifically, DOE
proposed to include EF as an optional
alternative metric in addition to WEF.
81 FR 64580, 64627–64628 (Sept. 20,
2016). DOE notes that the use of this
optional additional metric is a unique
allowance in this case, a result of a
negotiated rulemaking where the
industry clearly represented the
importance of maintaining the use of the
EF metric. DOE provided the DPPP
Working Group with an opportunity
through the NOPR to formally express
their intent to continue using EF as an
alternative metric at multiple speeds
and/or system curves, in addition to
WEF, to describe the energy
performance of dedicated-purpose pool
pumps.
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36895
In the September 2016 DPPP test
procedure NOPR public meeting, the CA
IOUs expressed support for the ability to
test EF at different speeds, in addition
to the DOE metric. (CA IOUs, Public
Meeting Transcript, No. 3 at pp. 78–79)
However, other commenters requested
clarification regarding the allowance for
the representation of two metrics in
DOE’s proposal and described how the
use of multiple metrics may cause
confusion and complicate ratings with
other voluntary industry programs.
Specifically, during the public meeting
and subsequent written comments,
APSP, Pentair, and Hayward expressed
confusion and concern related to
representations of EF, coordination with
ENERGY STAR and other entities, and
standardization of reported metrics
across the industry. (Pentair, Public
Meeting Transcript, No. 3 at pp. 8–9,
Hayward, No. 6 at p. 1, APSP, No. 8 at
p. 2; Pentair, No. 11 at p. 5)
DOE notes that such representations
are governed by statute. EPCA requires
that, manufacturers of dedicatedpurpose pool pumps within the scope of
the DPPP test procedure will be
required to use the test procedure
established in this rulemaking when
making representations about the energy
efficiency or energy use of their
equipment. Specifically, 42 U.S.C.
6314(d) provides that, ‘‘[e]ffective 180
days after a test procedure rule
applicable to any covered equipment is
prescribed . . . , [n]o manufacturer . . .
may make any representation . . .
respecting the energy consumption of
such equipment or cost of energy
consumed by such equipment, unless
such equipment has been tested in
accordance with such test procedure
and such representation fairly discloses
the results of such testing.’’
Therefore, beginning 180 days after
publication of this final rule, any
representations made with respect to the
energy use or efficiency of dedicatedpurpose pool pumps subject to testing
pursuant to 10 CFR 431.464(b) must be
made in accordance with the results of
testing pursuant to appendix B.
Manufacturers will not be required to
certify or make or make other
representations regarding the
performance of applicable dedicatedpurpose pool pumps using the WEF
metric until July 19, 2021, the
compliance date of energy conservation
standards for dedicated-purpose pool
pumps. If, however, manufacturers elect
to make representations of efficiency
prior to July 19, 2021, they will be
required to do so using a measurement
of the WEF metric derived from use of
the DOE test procedure.
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Given the confusion regarding the use
of the optional metrics expressed by the
majority of interested parties, DOE is
adopting, in this final rule,
modifications to its proposal to ensure
consistency with DOE’s test procedure
in the long term. Specifically, DOE is
providing a test procedure to derive an
EF metric, but only for representations
made before July 19, 2021, the
compliance date of any energy
conservation standards for dedicatedpurpose pool pumps. Thus, in this final
rule, DOE is adopting two appendices.
The first (appendix B) must be used
beginning 180 days after publication of
the final rule until July 19, 2021, the
compliance date of energy conservation
standards and includes both WEF and
the optional EF method. However, DOE
notes that if appendix B is used to make
representations of the optional metric
EF, the manufacturer must also make
representations of the required metric
WEF, such that, as required by EPCA,
the representations ‘‘fairly disclose the
results of testing’’ under appendix B. (42
U.S.C. 6314(d)).
The second appendix (C) includes
only the WEF metric. Manufacturers
must make representations in
accordance with appendix C on or after
July 19, 2021, the compliance date of
the adopted energy conservation
standards, including when certifying
compliance with those standards. As
appendix C does not provide a
procedure to arrive at an EF metric, after
July 19, 2021, representations of EF will
no longer be allowed.
Through the use of these two
appendices, DOE is clarifying that the
industry has until July 19, 2021, the
compliance date of adopted energy
conservation standards to transition
completely to WEF. DOE believes that
the transition to use of this one,
standardized metric will reduce
confusion among manufacturers and in
the marketplace. However, prior to July
19, 2021, DOE is allowing manufactures
to continue to make representations
using the EF metric, if tested in
accordance with the appendix B, during
the transition to representations using
only the WEF metric derived from the
test procedures in appendix C. DOE is
allowing this optional continued use of
EF until July 19, 2021, to provide the
industry with increased time to
transition fully to the new WEF metric,
due to the interest in maintaining the EF
metric expressed by the DPPP Working
Group. DOE also notes that use of
appendix B is optional and
manufacturers may decline to make
representations of EF and WEF, or any
other DPPP metrics, until July 19, 2021,
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when representations must be based on
the results of testing under appendix C.
2. Definition of Representation
In response to the September 2016
DPPP test procedure NOPR, Hayward
requested a definition of the term
representation. (Hayward, No. 6 at p. 1)
During the NOPR public meeting
Hayward also requested that DOE
provide an example of what would be
a typical representation applied to other
regulated products. (Hayward, Public
Meeting Transcript, No. 3 at p. 9)
In response, DOE notes that there is
no formal definition of representation.
However, as noted previously, 42 U.S.C.
6314(d), which establishes the 180-day
representation requirements, states that
manufacturers, distributors, retailers,
and private labelers are prohibited from
making ‘‘any representation—in writing
(including any representation on a label)
or in any broadcast advertisement
respecting the energy consumption of
such equipment or cost of energy
consumed by such equipment, unless
such equipment has been tested in
accordance with such test procedure
and such representation fairly discloses
the results of such testing.’’ Therefore,
representations include any and all
values that are generated by the test
procedure, as well as any statement
regarding the energy consumption or
cost of energy consumed.
Representations include, for example,
any information included in operation
and installation manuals, in marketing
materials, on a Web site, or on the
equipment label, as well as verbal
statements made in broadcast
advertisements.
In response to Hayward’s request for
an example of what would be a typical
representation, potentially for a
different product or piece of equipment,
DOE provided the example at the
September 2016 DPPP test procedure
NOPR public meeting of a residential
refrigerator where any representation of
how much electricity the refrigerator
consumes made in a manufacturer’s
literature or on their Web site would
need to be made based on the
appropriate DOE test procedure for that
product. DOE stated that any metrics
that come out of the DOE test procedure
must be based on testing in accordance
with that test procedure. (DOE, Public
Meeting Transcript, No. 3 at pp. 9–10).
For dedicated-purpose pool pumps, the
relevant metrics as proposed were WEF,
EF, rated hydraulic horsepower, DPPP
nominal motor horsepower, DPPP total
horsepower, DPPP service factor, true
power factor, and maximum head, as
well as pump efficiency, overall (wireto-water) efficiency, driver power input,
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and pump power output (hydraulic
horsepower), graphically or in
numerical form, and potentially at a
variety of speeds or load points.
3. Impact on Voluntary and Other
Regulatory Programs
Hayward asked whether or not
current the current reporting of data
(e.g., EF, horsepower, service factor,
etc.) to EPA, CEC, and APSP are affected
by this rulemaking (and whether DOE
would work with those entities to
update their standards). (Hayward, No.
6 at p. 1) Pentair also requested
clarification regarding whether or not
the EF value displayed in the ENERGY
STAR database would be subject to DOE
test procedures and representation
requirements 180 days after publication
of the final rule. (Pentair, Public
Meeting Transcript, No. 3 at pp. 8–9) CA
IOUs were supportive of the DOE DPPP
test procedure being incorporated by
ENERGY STAR as well as if ENERGY
STAR or other organizations wanted to
test at different speeds, they could use
the DOE test procedure, but specify the
speed accordingly. (CA IOUs, Public
Meeting Transcript, No. 3 at pp. 78–79)
In response to Hayward and Pentair’s
comments regarding the reporting of EF,
DOE clarifies that, as discussed
previously, 180 days after publication of
the final rule in the Federal Register, all
representations of energy and efficiency
metrics, including EF, will need to be
updated to be consistent with the final
DPPP test procedure. This is a statutory
requirement of EPCA, not a timeframe
set by DOE. DOE understands that
manufacturers of pumps likely have
historical test data which were
developed with methods consistent
with the DOE test procedure being
adopted in this final rule. DOE notes
that it does not expect that
manufacturers will need to regenerate
all of the historical test data as long as
the tested units remain representative of
the basic model’s current design and the
rating remains valid under the adopted
method of test for dedicated-purpose
pool pumps. If the testing methods used
to generate historical ratings for DPPP
basic models are substantially different
from those adopted in this final rule or
the manufacturer has changed the
design of the basic model, the
representations resulting from the
historical methods would no longer be
valid.
APSP and Hayward noted that
because DOE proposes EF as kgal/kWh,
it is not consistent with other programs
that require reporting it as gal/Wh, and
therefore the same number would be
reported with different units. (APSP,
No. 8 at p. 9; Hayward, No. 6 at p. 8)
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In response, DOE notes that, although
the DOE test procedure for EF proposed
to use kgal/kWh instead of gal/Wh,
these values are numerically equivalent.
However, for consistency with previous
ratings, in this final rule, DOE is
adopting units of gal/Wh for the
optional EF test metric.
With regard to coordination with
voluntary and other regulatory programs
in general, DOE notes that during the
Working Group meetings and the NOPR
public meeting, it was made clear to
stakeholders that not only the industry,
but also ENERGY STAR and CEC,
would have to transition to the DOE test
procedure within 180 days of
publication of the test procedure final
rule. (Docket No. EERE–2015–BT–STD–
0008, No. 54 at pp. 42–43; Public
Meeting Transcript, No. 3 at pp. 9–11)
On or after this date, representations
must be made in accordance with the
adopted DOE test procedure.
Accordingly, DOE expects that both
ENERGY STAR and CEC will transition
to DOE’s WEF metric and test
procedure. DOE will work with
ENERGY STAR and CEC to make this
transition. However, during this period
of transition, manufacturers may still be
making representations of EF for other
programs and must determine whether
their historical test data is valid in
accordance with the DOE test procedure
or not. After 180 days, all
representations, including
representations of EF, must be made in
accordance with the DOE test
procedure. In the case any historical test
data is determined not to be valid, that
DPPP model must be retested in order
to continue making representations of
EF.
4. Request for Extension
Hayward requested an extension of
the 180 day timeframe for
representations to allow manufacturers
sufficient time to obtain the necessary
resources, equipment, and personnel to
respond to DOE’s request. (Hayward,
No. 6 at p. 1) Pentair and APSP stated
that it was impossible to comply with
the 180 day requirement for publishing
performance and labeling products
according to the DOE test procedure,
particularly due to the relationship with
ENERGY STAR requirements. They also
noted that introducing new terms into
the market so early would be disruptive.
Therefore, they requested that the 180
day requirement be changed to coincide
with the compliance date of energy
conservation standards. (APSP, No. 8 at
p. 2; Pentair, No. 11 at p. 5)
In response to Pentair and APSP’s
concerns about labeling and
introduction of new metrics, DOE did
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not propose that products be labeled
within the 180 day period (see section
III.I). Furthermore, DOE notes that
manufacturers may decline to make any
representations of WEF, or any other
DPPP metrics, until July 19, 2021,
meaning that no equipment is required
to be rated in accordance with the DOE
test procedure within 180 days. EPCA
does require, however, that any
representation that a manufacturer may
choose to make on a label or otherwise
must reflect testing under the applicable
DOE test procedure, beginning 180 days
after publication of this final rule. (42
U.S.C. 6314(d)) In this case, they must
make representations of WEF at a
minimum, but may choose to continue
making representations of EF, reflective
of the results of testing in accordance
with appendix B, until July 19, 2021.
DOE acknowledges that some DPPP
models currently participate in
voluntary industry programs, such as
ENERGY STAR, that rely on the EF
metric. As such, DOE is accommodating
the continued use of the EF metric until
July 19, 2021 to allow a smooth
transition in the industry, as requested
by Pentair and APSP. However, as
mentioned previously, both ENERGY
STAR and CEC are also required to
transition to DOE’s new WEF metric and
test procedure within 180 days. In
addition, after July 19, 2021, only
representations of WEF will be allowed,
as representation of EF would not be
reflective of testing under appendix C of
the DPPP test procedure. DOE believes
this should address Pentair and APSP’s
concern regarding market confusion
with new metrics.
DOE notes that 42 U.S.C. 6314(d)(2)
allows manufacturers to petition for an
extension of up to another 180 days in
the case of undue hardship to the
manufacturer. However, because a
finding as to undue hardship is
particular to a given manufacturer, the
petition must be filed by the
manufacturer within 60 days of the
publication of this final rule, specifying
the hardship to the manufacturer that
would result from the 180-day
requirement, and any extension will be
determined by the Secretary on a caseby-case basis. (42 U.S.C. 6314(d)(2))
G. Additional Test Methods
In addition to the measurements and
calculations necessary to determine
WEF, DOE also must establish
consistent terminology and
measurement methods to categorize the
capacity and maximum head of a given
dedicated-purpose pool pump, as well
as establish whether a given dedicatedpurpose pool pump is self-priming.
Specifically, as discussed in section
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III.D, DOE is establishing different load
points and reference curves based on
the rated hydraulic horsepower of a
given pool filter pump. DOE’s
standardized and consistent method for
determining DPPP capacity is discussed
in section III.G.1. As discussed in
section III.B.3.a, DOE also is
differentiating pool filter pumps based
on whether they are self-priming. DOE’s
test method for determining the selfpriming capability of dedicated-purpose
pool pumps is discussed in section
III.G.2. In addition, waterfall pumps are
categorized with respect to the
maximum head the pump can produce.
DOE’s test method for determining
maximum head is discussed in section
III.G.3.
1. Determination of DPPP Capacity
As discussed in detail in the
September 2016 DPPP test procedure
NOPR, industry currently uses several
terms to characterize the capacity of
dedicated-purpose pool pumps,
including total horsepower, DPPP motor
capacity, nameplate horsepower, rated
horsepower, max-rated horsepower, uprated horsepower, brake horsepower,
service factor horsepower, peak power,
and hydraulic horsepower. 81 FR 64580,
64620–64623 (Sept. 20, 2016). The
DPPP Working Group discussed these
terms and recommended standardizing
the terminology by referring to pump
capacity around the hydraulic
horsepower provided by the pump at a
specific load point. (Docket No., EERE–
2015–BT–STD–0008, No. 56 at pp. 148–
173) In addition, the DPPP Working
Group recommended that DOE assist in
standardizing the testing and rating of
dedicated-purpose pool pumps with
regard to other typical horsepower
metrics. (Docket No. EERE–2015–BT–
STD–0008, No. 92 at pp. 319–322)
Specifically, the June 2016 DPPP
Working Group recommended that DOE
should investigate a label that would
facilitate proper application and include
specified horsepower information.
(Docket No. EERE–2015–BT–STD–0008,
No. 82, Recommendation #9 at p. 5)
Section III.G.1.a and section III.G.1.b
contain DOE’s proposals and the
adopted provisions related to rated
hydraulic horsepower and other DPPP
motor horsepower metrics, respectively.
a. Rated Hydraulic Horsepower
In the September 2016 DPPP test
procedure NOPR, DOE proposed to
consistently refer to and categorize
dedicated-purpose pool pumps based on
the hydraulic horsepower they can
produce at a particular load point, as
measured in accordance with the new
DPPP test procedure. 81 FR 64580,
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64620–64623 (Sept. 20, 2016). In order
to have consistent and comparable
values of hydraulic horsepower, the
DPPP test procedure must also specify
a load point at which to determine the
hydraulic horsepower. DOE proposed to
categorize dedicated-purpose pool
pumps based on the hydraulic
horsepower determined at maximum
speed on the reference curve for each
DPPP variety and speed configuration
(section III.D) and at full impeller
diameter to result in consistent and
comparable ratings among DPPP
varieties and speed configurations. Id.
While hydraulic horsepower (termed
pump power output 51) is defined in HI
40.6–2014, in the September 2016 DPPP
test procedure NOPR, DOE proposed to
use the term ‘‘rated hydraulic
horsepower’’ to specifically identify the
measured hydraulic horsepower on the
reference curve (i.e., curve C for selfpriming and non-self-priming pool filter
pumps) or the specified load point (i.e.,
17.0 ft or 10.0 gpm for waterfall pumps
or pressure cleaner booster pumps,
respectively) at the maximum speed and
full impeller diameter for the rated
pump. 81 FR 64580, 64622 (Sept. 20,
2016). DOE’s goal in proposing this term
was to unambiguously specify the pump
power characteristic and differentiate it
from the general term ‘‘hydraulic
horsepower’’ that can be determined at
any location on the pump curve. Id. In
addition, DOE proposed in the
September 2016 DPPP test procedure
NOPR that the representative value of
rated horsepower, for each basic model
of dedicated-purpose pool pump, be
determined as the mean of the rated
hydraulic horsepower for each tested
unit measured in accordance with the
new DPPP test procedure. Id. The test
method for determining hydraulic
horsepower (pump power output) is
described in more detail in section
III.E.2.b.
DOE did not receive any comments
related to the proposed definition of
rated hydraulic horsepower, the
proposal to base the characterization of
DPPP capacity on rated hydraulic
horsepower, or the proposed method for
determining representative values of
rated hydraulic horsepower.
Consequently, DOE is adopting the
terminology and test methods proposed
51 The term ‘‘pump power output’’ in HI 40.6 is
defined as ‘‘the mechanical power transferred to the
liquid as it passes through the pump, also known
as pump hydraulic power.’’ It is used
synonymously with ‘‘hydraulic horsepower’’ in this
document. However, where hydraulic horsepower
is used to reference the capacity of a dedicatedpurpose pool pump, it refers to the rated hydraulic
horsepower.
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in the September 2016 DPPP test
procedure NOPR without modification.
b. Other DPPP Motor Horsepower
Metrics
DPPP Working Group suggested that
DOE assist in standardizing the testing
and rating of dedicated-purpose pool
pumps with regard to other typical
horsepower metrics (Docket No. EERE–
2015–BT–STD–0008, No. 92 at pp. 319–
322). In the September 2016 DPPP test
procedure NOPR, DOE reviewed the
terms typically used in the DPPP
industry to characterize motor
horsepower. 81 FR 64580, 64622 (Sept.
20, 2016). To alleviate any ambiguity
associated with rated horsepower, total
horsepower, and service factor, DOE
proposed, in the September 2016 DPPP
test procedure NOPR, the terms ‘‘DPPP
nominal motor horsepower,’’ ‘‘DPPP
motor total horsepower,’’ and ‘‘DPPP
service factor.’’ 81 64580, 64622–64623
(Sept. 20, 2016). The proposed
definitions for these terms are as
follows:
• Dedicated-purpose pool pump
nominal motor horsepower means the
nominal motor horsepower as
determined in accordance with the
applicable procedures in NEMA–MG–1–
2014.
• Dedicated-purpose pool pump
motor total horsepower (also known as
service factor horsepower) means the
product of the dedicated-purpose pool
pump nominal motor horsepower and
the dedicated-purpose pool pump
service factor of a motor used on a
dedicated-purpose pool pump based on
the maximum continuous duty motor
power output rating allowable for the
nameplate ambient rating and motor
insulation class.
• Dedicated-purpose pool pump
service factor means a multiplier
applied to the rated horsepower of a
pump motor to indicate the percent
above nameplate horsepower at which
the motor can operate continuously
without exceeding its allowable
insulation class temperature limit. 81
FR 64580, 64622–64623 (Sept. 20,
2016).
The definitions proposed in the NOPR
were developed based on the existing
industry definitions for these terms.
However, the term ‘‘dedicated-purpose
pool pump nominal motor horsepower’’
is defined slightly differently than the
terms ‘‘rated horsepower’’ or
‘‘nameplate horsepower,’’ which are
synonymous in the industry.
Specifically, DOE defines DPPP nominal
motor horsepower based on the nominal
horsepower of the motor with which the
dedicated-purpose pool pump is
distributed in commerce, as determined
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in accordance with the applicable
procedures in NEMA MG–1–2014,
‘‘Motors and Generators.’’ Id.
In response to DOE’s proposed
definitions, CA IOUs were generally
supportive of this approach and stated
that CEC has similar terms to those
proposed in the September 2016 DPPP
test procedure NOPR, but noted that
CEC uses the term ‘‘motor capacity’’ for
consistency with the motor industry,
which is synonymous with the total
horsepower and service factor
horsepower. (CA IOUs, Public Meeting
Transcript, No. 3 at p. 66).
DOE acknowledges CA IOUs’
comment and is aware that different
organizations use different terms to
describe similar quantities. Although
DOE is aware that CEC uses the term
motor capacity to refer to what DOE is
proposing to define as DPPP motor total
horsepower, DOE believes the proposed
term is more straightforward and widely
understood. DOE also notes that Title 20
of the California Code of Regulations
defines both the term ‘‘capacity of the
motor’’ and ‘‘total horsepower’’ (of an
AC motor) as the product of the rated
horsepower and the service factor of a
motor used on a dedicated-purpose pool
pump (also known as service factor
horsepower) based on the maximum
continuous duty motor power output
rating allowable for the nameplate
ambient rating and motor insulation
class. Cal. Code Regs., tit. 20 section
1602, subd. (g) However, to be
consistent with both CEC definitions for
the same term, this final rule will adopt
the definition with a parenthetical to
note that DPPP motor total horsepower
is also referred to as service factor
horsepower or motor capacity.
Regarding the definition of DPPP
nominal motor horsepower, based on
response to comment discussed further
in this section, DOE is not referencing
NEMA MG–1–2014 for the test method
to determine DPPP nominal motor
horsepower and is instead directly
referencing a more simplified method
with equivalent burden. As such, DOE’s
proposed definition is no longer
applicable. DOE believes specifying a
test method for determining this value
is sufficient and is not adopting a
definition of DPPP nominal motor
horsepower.
In the September 2016 DPPP test
procedure NOPR, DOE also proposed
test methods to consistently and
unambiguously determine the DPPP
nominal motor horsepower, DPPP
service factor, and DPPP motor total
horsepower. To determine the DPPP
nominal motor horsepower for singlephase and polyphase small and medium
AC motors, DOE proposed to reference
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the relevant sections of NEMA MG–1–
2014, as summarized in Table III.10.
DOE also proposed to incorporate by
reference these sections of NEMA MG–
1–2014 into the DPPP test procedure. 81
36899
FR 64580, 64622–64623 (Sept. 20,
2016).
TABLE III.10—SUMMARY OF RELEVANT NEMA MG–1–2014 SECTIONS APPLICABLE TO SMALL AND MEDIUM SINGLE- AND
THREE-PHASE AC MOTORS
Characteristic
Single-phase AC motors
Three-phase AC motors
Breakdown Torque ...............
Locked-Rotor Torque ...........
Pull-up Torque .....................
Locked-Rotor Current ..........
Slip .......................................
Section 10.34 of NEMA MG–1–2014.* ...........................
N/A ..................................................................................
N/A ..................................................................................
N/A ..................................................................................
N/A ..................................................................................
Section
Section
Section
Section
Section
12.39 of NEMA MG–1–2014.*
12.37 or 12.38 of NEMA MG–1–2014.*
12.40 of NEMA MG–1–2014.*
12.35.1 of NEMA MG–1–2014.*
1.19 of NEMA MG–1–2014.*
* Based on testing in accordance with section 12.30 of NEMA MG–1–2014.
DOE also proposed to base the
determination of DPPP service factor on
the standardized service factor values in
table 12–4 of section 12.51, ‘‘Service
Factor of Alternating-Current Motors.’’
For AC motors not covered by table 12–
4 of section 12.51 of NEMA MG–1–2014
and for DC motors, DOE proposed
assigning a service factor of 1.0,
consistent with section 12.51.2 of
NEMA MG–1–2014. Id.
Finally, DOE proposed that total
horsepower would be calculated as the
product of the DPPP nominal motor
horsepower and the DPPP service factor,
both determined in accordance with the
applicable provisions in the DPPP test
procedure. Id.
In response to DOE’s proposed test
methods for the proposed DPPP motor
horsepower metrics, Nidec commented
that section 10.34 of NEMA MG–1–
2014, which DOE proposed to
incorporate by reference, applies
specifically to general purpose motors,
while small electric motors designed for
use on dedicated-purpose pool pumps
are definite purpose motors that do not
follow the design criteria of NEMA MG–
1–2014. Instead, Nidec suggested that
DOE use equation (4) to determine
nominal motor horsepower:
Where:
Nidec noted that this is consistent with
the labeling requirements set forth in
ANSI/APSP/ICC 15a–2013. (Nidec, No.
10 at p. 3). Finally, Nidec commented
that three-phase motors utilized on
dedicated-purpose pool pumps are
energy efficient and already regulated
and, therefore, should not need further
testing nor reporting requirements.
(Nidec, No. 10 at p. 3).
APSP agreed with Nidec that DPPP
motors are typically definite-purpose
and do not always align with NEMA on
mechanical and electrical performance.
Similarly, APSP recommended using
equation (4) to calculate nominal motor
horsepower and assigning a service
factor of 1.0, such that nominal motor
horsepower was equivalent to motor
total horsepower. (APSP, No. 8 at p. 8).
During the September 2016 DPPP test
procedure NOPR public meeting, CA
IOUs stated that commercial and
industrial motors commonly have
service factors of 1.15, where the motor
is capable of performing at a higher
level than what the nameplate shows. In
contrast, in DOE’s proposal of 1.0, the
motor will do at best exactly what the
nameplate states. (CA IOUs, Public
Meeting Transcript, No. 3 at p. 68)
Pentair also commented that the
proposal would restrict a manufacturer’s
ability to use higher service factor
motors for purposes of improved motor
life and/or reduction of inventory/SKUs.
(Pentair, No. 11 at p. 3). However,
Pentair expressed, in its comments, the
importance of standardizing and
labeling regarding DPPP horsepower
metrics and described how the current
practice of up-rate and full-rate labeling
of similar products causes significant
confusion in the market. (Pentair, No. 11
at p. 5). In response to Nidec and
APSP’s suggestions regarding the
appropriate test methods for
determining motor horsepower and
service factor, DOE believes the method
suggested by Nidec and APSP is sound
and, as described by the commenters,
represents the methods currently used
by the motor industry to determine
motor total horsepower for DPPP
motors. DOE is also aware that equation
(4) is a common method for measuring
motor horsepower when speed and
torque are known. Specifically, equation
Pnm = the nominal total horsepower 52 at full
load (in hp),
T = output torque at full load (in lb-ft), and
RPM = the motor speed at full load (in rpm).
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Nidec believes that the calculation in
equation (4) is a better method for
calculation than using the NEMA
sections DOE proposed for DPPP motors
and stated that equation (4) is the
equation Nidec currently uses to rate
such motors, which it manufacturers.
(Nidec, No. 10 at p. 2). Nidec also
inquired as to the test methods DOE
proposed to use for DPPP motors.
(Nidec, No. 10 at p. 4).
Nidec also commented that the
service factor for small electric motors
used in the DPPP industry should not
follow NEMA section 12.51 of NEMA
MG–1–2014 but instead should be
established as 1.0 for all DPPP motors.
52 Nidec’s comment defined this term as the
‘‘nominal motor horsepower at full load.’’ However,
the rest of the comment describes the value as the
motor total horsepower. As Nidec also
recommended a service factor of 1.0 (Nidec, No. 10
at pp. 2–3), nominal motor horsepower is
equivalent to motor total horsepower and the
equation is applicable to both quantities.
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Similarly, for direct current (DC)
motors, including electrically
commutated motors, section 10.62 of
part 10 of NEMA MG–1–2014,
‘‘Horsepower, Speed, and Voltage
Ratings,’’ describes the requirements for
determining the nominal horsepower
based on the applicable rated load speed
and rated voltages for these motors. To
clearly specify how DPPP nominal
motor horsepower would be determined
for DC motors based on the procedures
in NEMA MG–1–2014, DOE also
proposed to include instructions in the
DPPP test procedure that reference the
relevant sections of NEMA MG–1–2014.
Id.
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(4) is described in NEMA MG–1–2014
(the standard DOE proposed to
incorporate by reference for this
determination), the IEEE Standard 114–
2010, ‘‘Test Procedure for Single-Phase
Induction Motors’’; IEEE Standard 113–
1985, ‘‘IEEE Guide: Test Procedures for
Direct-Current Machines’’; and
Canadian Standards Association (CSA)
C747–2009 (Reaffirmed (RA) 2014),
‘‘Energy Efficiency Test Methods for
Small Motors.’’ 53
DOE notes that this method provides
a direct measurement of the horsepower
provided by the motor at full load,
which is consistent with the term DPPP
motor total horsepower, as opposed to
DPPP nominal motor horsepower as
suggested by Nidec and APSP. However,
DOE acknowledges that, as Nidec and
APSP both suggested using a service
factor of 1.0 with this method, the DPPP
nominal motor horsepower and DPPP
motor total horsepower would be
equivalent and either could be
determined with the suggested method
shown in equation (4). Therefore,
determining nominal motor horsepower
using equation (4) is technically correct,
provided it is used with a service factor
of 1.0. Both Nidec and APSP
specifically suggested determining
DPPP nominal motor horsepower using
equation (4), setting DPPP service factor
to 1.0, and determining DPPP motor
total horsepower as the product of the
DPPP nominal motor horsepower and
DPPP service factor. (Nidec, No. 10 at p.
4; APSP, No. 8 at p. 8). As noted in the
NOPR, determining DPPP motor total
horsepower as the product of DPPP
nominal motor horsepower and DPPP
service factor is also consistent with
ANSI/APSP/ICC 15a–2013,54 ENERGY
STAR,55 and CA Title 20 56 definitions
for the term. 81 FR 64580, 64620–64622
(Sept. 20, 2016). As such, DOE is
adopting the method suggested by Nidec
and APSP as the test method for
determining DPPP nominal total
horsepower for dedicated-purpose pool
pumps subject to the adopted
53 DOE notes that the equation in section 6.4 of
CSA C&47–2009 (RA 2014) uses a conversion factor
of 5254, instead of the value 5252 suggested by
NEMA. However, based on DOE’s review, DOE
believes a conversion factor of 5252 is more
accurate and is more consistent with the value
listed in other standards.
54 ANSI/APSP/ICC–15a–2013, American National
Standard for Residential Swimming Pool and Spa
Energy Efficiency—section 3, ‘‘Definitions.’’
Includes Addenda A. ANSI Approved January 9,
2013. The Association of Pool and Spa
Professionals and the International Code Council.
55 ENERGY STAR Program Requirements for Pool
Pumps Eligibility Criteria (Version 1.1), section 1.4,
‘‘Product Ratings.’’
56 Cal. Code Regs., tit. 20 section 1602, subd. (g).
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procedure.57 As discussed further in
this section regarding incorporations by
reference, the burden and fundamental
procedure associated with the adopted
procedure for measuring motor
performance are not different from those
proposed in the NOPR, but the adopted
method provides a simpler, more direct
description.
Regarding service factor, DOE
appreciates Nidec and APSP’s
suggestions regarding service factor and
agrees that a service factor of 1.0 for all
DPPP motors that are subject to the
adopted motor horsepower provisions
would be more consistent and ensure
standardized rating across DPPP
models. It also enables to use of the
more direct determination of DPPP
nominal horsepower adopted in this
final rule. Although Pentair requested
more flexibility specifically with regard
to service factor, Pentair also requested
standardization in horsepower ratings.
As such, in this final rule, in order to
better standardize the motor horsepower
ratings as recommended by
commenters, DOE is adopting a service
factor of 1.0 for all dedicated-purpose
pool pumps to which the adopted motor
horsepower test methods apply.
Regarding Nidec’s statement that a
service factor of 1.0 was consistent with
ANSI/APSP/ICC 15a–2013, DOE
reviewed ANSI/APSP/ICC 15a–2013
and finds that ANSI/APSP/ICC 15a–
2013 does not appear to provide any
restriction with regard to the service
factor of DPPP motors. In fact, ANSI/
APSP/ICC 15a–2013 defines several
terms, including rated horsepower, total
horsepower, and service factor, that
indicate service factors greater than 1.0
are quiet common. For example, the
definition of service factor references a
pump with a rated horsepower of 1.5
hp, a service factor of 1.65, and a total
horsepower of 2.475 hp.58
In response to CA IOUs comments on
the proposed DPPP service factor for
DPPP motors, DOE notes that, consistent
with CA IOUs observation, the service
factor prescribed in table 12–4 of section
12.51, ‘‘Service Factor of AlternatingCurrent Motors,’’ is 1.15 for most AC
motors with a nominal horsepower
greater than 0.5 horsepower and typical
synchronous speeds. However,
consistent with section 12.51.2 of
NEMA MG–1–2014 and the comments
of Nidec and APSP, DOE believes that
57 As
discussed subsequently in this section, DOE
is adopting test methods for determining the motor
horsepower characteristics of dedicated-purpose
pool pumps that are only applicable to dedicatedpurpose pool pumps distributed in commerce with
single-phase AC or DC motors.
58 ANSI/APSP/ICC–15a–2013, section 3,
‘‘Definitions.’’
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a service factor of 1.0 for AC motors not
covered by table 12–4 is more
appropriate than a service factor of 1.15.
In addition, as discussed in the
September 2016 DPPP test procedure
NOPR, NEMA MG–1–2014 does not
provide information regarding service
factor for DC motors, as nominal
synchronous speeds are typically not
applicable to DC motors. Therefore,
DOE believes a DPPP service factor of
1.0 is appropriate for DC motors,
effectively making the nominal
horsepower equivalent to the total
horsepower of the dedicated-purpose
pool pump, which is consistent with the
convention for rating such motors in the
motor industry.
However, DOE notes that Nidec
recommended applying the suggested
methodology for single-phase DPPP
motors only. Nidec indicated that threephase motors sold with dedicatedpurpose pool pumps are already subject
to DOE’s energy conservation standards
for polyphase electric motors at 10 CFR
431.25 or 10 CFR 431.446, depending on
the size of the motor. (Nidec, No. 10 at
p. 3). DOE agrees with Nidec that any
polyphase induction motors currently
subject to DOE’s existing regulations for
electric motors or small electric motors
are already subject to test procedures
that describe how to determine relevant
motor performance parameters,
including nominal motor horsepower
and service factor, in a standardized and
consistent manner. Therefore,
additional specifications in the DPPP
test procedure are not required.59 For
these reasons, in this final rule, DOE is
limiting the applicability of the test
methods for determining DPPP nominal
motor horsepower and DPPP service
factor to dedicated-purpose pool pumps
that are distributed in commerce with
single-phase AC or DC motors, which
are not subject to DOE’s existing
regulations for electric motors or small
electric motors.
DOE notes that the test method for
determining DPPP motor total
horsepower is still applicable to all
dedicated-purpose pool pumps,
including those distributed in
commerce with polyphase AC motors,
as NEMA MG–1–2014 does directly
define or prescribe unambiguous
methods for determining motor total
horsepower. In addition, as discussed
59 DOE notes that the existing electric motor and
small electric motor regulations reference relevant
sections of NEMA MG–1–2014 and are consistent
with the test methods proposed in the September
2016 DPPP TP NOPR. As such, consistent with CA
IOUs observation, dedicated-purpose pool pumps
distributed in commerce with polyphase motors
will continue to apply table 12–4 in NEMA MG–
1–2014.
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further in section III.K.2 and III.I, all
dedicated-purpose pool pumps,
including dedicated-purpose pool
pumps distributed in commerce with
polyphase AC motors, are required to
report to DOE the DPPP motor total
horsepower and include such
information on the equipment
nameplate.
In adopting Nidec and APSP’s
recommended test method for
determining DPPP nominal motor
horsepower, DOE is not referencing
NEMA MG–1–2014 as the method for
determining DPPP motor total
horsepower. However DOE still must
adopt specific and standardized test
methods for measuring speed and
torque of DPPP motors at full load. IEEE
Standard 114–2010, ‘‘Test Procedure for
Single-Phase Induction Motors’’ (IEEE
114–2010) and IEEE Standard 113–1985,
‘‘Test Procedures for Direct-Current
Machines’’ (IEEE 113–1985) describe the
general test requirements and methods
for determining motor speed and torque
at full load for single-phase AC
induction motors and DC motors,
respectively. DOE notes that these are
the test methods referenced in NEMA
MG–1–2014, so the burden and
fundamental procedure associated with
measuring motor performance are not
different from those proposed in the
NOPR. However, as the method of
determining DPPP nominal motor
horsepower suggested by Nidec and
APSP and incorporated by DOE is more
direct, DOE is incorporating by
reference the relevant sections of IEEE
114–2010 and IEEE 113–1985 directly,
as opposed to through NEMA MG–1–
2014.
In addition, DOE notes that CSA
C747–2009 (RA 2014) is another
commonly referenced test method for
determining motor horsepower that is
treated as equivalent to IEEE 114–2010
in DOE’s existing small electric motor
test procedure. 10 CFR 431.444(b). In
DOE’s July 2009 small motors test
procedure final rule, DOE determined
that IEEE 114–2010 and CSA C747–2009
(RA 2014) would produce equivalent
ratings. 74 FR 32059, 32065 (July 7,
2009). DOE has reviewed CSA C7474–
2009 (RA 2014) as compared to IEEE
113–1985 and believes that the
standards will also produce equivalent
measurements of full load speed and
torque, which are the values relevant for
this test procedure. DOE understands
36901
that some manufacturers may currently
be using CSA C747–2009 (RA 2014) to
determine the performance of small
motors, including both single-phase AC
and DC motors. Therefore, to provide
flexibility to manufacturers and
consistency with DOE’s existing motor
regulations, DOE is adopting test
provisions that allow for testing in
accordance with either the applicable
IEEE standard (IEEE 114–2010 for
single-phase AC motors or IEEE 113–
1985 for DC motors) or CSA C747–2009
(RA 2014). DOE believes that these
standards provide the necessary and
sufficient methods to determine the
torque and rotating speed of the motor
at full load for single-phase AC
induction motors and DC motors,
respectively. Specifically, DOE is
adopting the sections specified in the
Table III.11 for each standard, which are
relevant to measuring speed and torque
at full load. In addition, section E.3.2 of
both appendix B and C, as adopted in
this final rule, states that full-load speed
and torque shall be determined based on
the maximum continuous duty motor
power output rating allowable for the
motor’s nameplate ambient rating and
insulation class.
TABLE III.11—SECTIONS OF IEEE 114–2010 AND IEEE 113–1985 THAT DOE INCORPORATES BY REFERENCE FOR
DETERMINING DPPP MOTOR TOTAL HORSEPOWER
Characteristic
IEEE 114–2010
IEEE 113–1985
Relevant Scope ...........
Single-phase AC Motors.
Section 4 ....................
DC Motors .......................................................
Single-phase AC and DC Motors
Section 3.5, 4.1.2, and 4.1.4 (and machine
temperature rise shall be some value between 50% and 100% of rated temperature
rise, as specified in 5.4.3).
Section 5.4.3.2 (except that curves of torque
versus electric power are not required, as
only measurement at full load is required).
Section 5.2, 5.3, 5.5. 6.1.
Test Conditions ...........
Section 3.2 and section 6.
Measurement Instruments.
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Test Requirements ......
Section 5.2 and 5.3 ....
In responses to Nidec’s inquiry
regarding the test methods for
determining DPPP motor horsepower
characteristics, the test methods
referenced in NEMA MG–1–2014 were,
by extension, proposed to be
incorporated by reference as the specific
testing requirements for determining
motor performance in the September
2016 DPPP test procedure NOPR.
Regarding the scope of the proposed
motor horsepower testing requirements,
Pentair commented that a loophole
could be introduced in replacement
DPPP motors are not also subject to
these requirements. (Pentair, No. 11 at
p. 3).
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Section 3.1, 3.4 ...............................................
In response to Pentair’s request, DOE
notes that the scope of the required DOE
test procedure recommended by the
DPPP Working Group and proposed by
DOE in the September 2016 DPPP test
procedure NOPR is limited to
dedicated-purpose pool pumps. DOE
acknowledges that, in the September
2016 DPPP test procedure NOPR, DOE
proposed an optional test method to
determine WEF for replacement DPPP
motors. 81 FR 64580, 64629 (Sept. 20,
2016). However, in the September 2016
DPPP test procedure NOPR, DOE also
described how DOE does not intend to
regulate replacement DPPP motors as
part of this rulemaking because they do
not (by themselves) meet the definition
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Section 6.3, 6.4 (except in section (b) the
conversion factor shall be 5252), 6.5 (except only measurements at full load are required), and 6.7.1.
Section 5.1, 5.4.6, 5.4.7, 5.6.4, 5.6.5, 5.6.6,
6.2.
of a dedicated-purpose pool pump. Id.
Similar to the optional testing
provisions for replacement DPPP motors
adopted in this final rule, manufacturers
of replacement DPPP motors may opt to
apply the provisions for determining
DPPP nominal motor horsepower, DPPP
service factor, and DPPP motor total
horsepower, as applicable, and make
representations of these quantities if
they so choose. However, as discussed
further in section III.J, replacement
DPPP motors are not dedicated-purpose
pool pumps, and requirements for such
equipment were not discussed or
recommended by the DPPP Working
Group. Therefore, DOE is declining to
adopt any required testing provisions or
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2. Determination of Self-Priming
Capability
As discussed in section III.B.3.a, DOE
proposed separate definitions for selfpriming and non-self-priming pool filter
pumps based on their capability to selfprime as determined based on testing in
accordance with NSF/ANSI 50–2015. In
the September 2016 DPPP test
procedure NOPR, DOE proposed to
incorporate by reference relevant
sections of the NSF/ANSI 50–2015
standard and also specify several
modifications and additions to improve
repeatability and consistency of the test
results. 81 FR 64580, 64623–27 (Sept.
20, 2016). Specifically, DOE proposed to
incorporate by reference section C.3 of
Annex C of NSF/ANSI 50–2015, which
contains the relevant test parameters,
test apparatus, and testing instructions
for determining the self-priming
capability of self-priming and non-selfpriming pool filter pumps. Id.
To determine the self-priming
capability of self-priming and non-selfpriming pool filter pumps, DOE
proposed in the September 2016 DPPP
test procedure NOPR to follow the test
method specified in section C.3 of
Annex C of NSF/ANSI 50–2015 with
several minor modifications to improve
test consistency and repeatability, as
well as conform with the new
definitions for self-priming and nonself-priming pool filter pumps presented
in section III.B.3.a. Id. First, where
section C.3.2, ‘‘Apparatus,’’ and section
C.3.4, ‘‘Self-priming capability test
method,’’ state that the ‘‘suction line
must be essentially as shown in annex
C, figure C.1’’ DOE notes that the
suction line refers to the riser pipe that
extends from the pump suction inlet to
the water surface. DOE also proposed in
the September 2016 DPPP test
procedure NOPR to clarify that
‘‘essentially as shown in Annex C,
figure C.1’’ means:
• The centerline of the pump
impeller shaft is situated a vertical
distance of 5.0 feet above the water level
of a water tank of sufficient volume as
to maintain a constant water surface
level for the duration of the test;
• the pump draws water from the
water tank with a riser pipe that extends
below the water level a distance of at
least 3 times the riser pipe diameter (i.e.,
3 pipe diameters); and
• the suction inlet of the pump is at
least 5 pipe diameters from any
obstructions, 90° bends, valves, or
fittings.
Id.
Further, DOE noted that NSF/ANSI
50–2015 does not specify where the
measurement instruments are to be
placed in the test set up. DOE
understands that instruments are
typically installed at the suction inlet of
the pump and therefore, DOE proposed
to specify that all measurements of
head, flow, and water temperature must
be taken at the pump suction inlet. Id.
It is also important that all
measurements are taken with respect to
a common reference plane, which DOE
proposed should be the centerline of the
pump impeller shaft. DOE also
proposed that such adjustments be
performed in accordance with section
A.3.1.3.1 of HI 40.6–2014. Id.
In addition, DOE proposed that
height, or vertical lift (VL), must be
determined from the height of the water
to the centerline of the pump impeller
shaft. Id. In addition to proposing
clarifications with regard to the
measurement of VL, DOE proposed
clarifications on how to correct the
value to a standard temperature of 68 °F,
a pressure of 14.7 psia, and a water
density of 62.4 lb/ft3, as shown in
equation (5). DOE notes that the
definitions proposed in the September
2016 DPPP test procedure NOPR
specifies a VL of 5.0 feet:
Where:
VL = vertical lift of the test apparatus from
the waterline to the centerline of the
pump impeller shaft, in ft;
rtest = density of test fluid, in lb/ft3; and
Patm,test = absolute barometric pressure of test
apparatus location at centerline of pump
impeller shaft, in psia.
81 FR 64580, 64624–25 (Sept. 20, 2016).
In addition, DOE also noted in the
September 2016 DPPP test procedure
NOPR that section C.3.2 of NSF/ANSI
50–2015 describes the instruments that
are required to perform the test, but,
with the exception of the time indicator,
does not specify their required accuracy.
Subsequently, DOE proposed to apply
the accuracy requirements contained in
HI 40.6–2014 to the measurement
devices noted in NSF/ANSI 50–2015, as
detailed in Table III.12. 81 FR 64580,
64625 (Sept. 20, 2016).
TABLE III.12—MEASUREMENT DEVICE ACCURACY REQUIREMENTS FOR MEASUREMENTS DEVICES SPECIFIED IN NSF/ANSI
50–2015
Measurement device
Accuracy requirement
Elapsed Time Indicator ...........................................................................
Gauge Pressure Indicating Device .........................................................
Temperature Indicating Device ...............................................................
±0.1 min .........................................
±2.5% of reading * .........................
±0.5 °F ...........................................
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Source
NSF/ANSI 50–2015.
HI 40.6–2014.
HI 40.6–2014.
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reporting requirements for replacement
DPPP motors in this rulemaking. DOE
may address requirements for
replacement DPPP motors in a future
rulemaking specifically addressing such
equipment.
In summary, based on the comments
received in response to the September
2016 DPPP test procedure NOPR, DOE
is adopting revised test methods for
DPPP nominal motor horsepower and
DPPP service factor, which are
applicable only to dedicated-purpose
pool pumps distributed in commerce
with single-phase AC motors and DC
motors. DOE is also adopting the test
method for DPPP motor total
horsepower proposed in the September
2016 DPPP test procedure NOPR
without modification, which is
applicable to all dedicated-purpose pool
pumps. DOE believes such standardized
rating methods are consistent with the
recommendations of the DPPP Working
Group, will be beneficial to consumers
in selecting and applying the
equipment, and are consistent with
existing methods used to rate motors
today. DOE notes that these
standardized horsepower metrics are
intended to support labeling provisions
for dedicated-purpose pool pumps,
which are discussed further in section
III.I.
Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
36903
TABLE III.12—MEASUREMENT DEVICE ACCURACY REQUIREMENTS FOR MEASUREMENTS DEVICES SPECIFIED IN NSF/ANSI
50–2015—Continued
Measurement device
Accuracy requirement
Source
Barometric Pressure Indicating Device ...................................................
Height ......................................................................................................
±2.5% of reading * .........................
±0.1 inch ........................................
HI 40.6–2014.
N/A.
* The ±2.5 percent requirement applies to discharge, suction, and differential head measurements, as indicated in table 40.6.3.2.3, for values
taken between 40 and 120 percent of BEP flow.
same thing and result in similar water
characteristics. Therefore, to simplify
testing requirements and be consistent
with the other portions of the DPPP test
procedure, in the September 2016 DPPP
test procedure NOPR, DOE proposed to
require testing of the self-priming
capability of pool filter pumps with
clear water that is between 50 and 86 °F,
as opposed to the existing water
temperature and turbidity requirements
contained in section C.3.3 of the NSF/
ANSI 50–2015 test method. 81 FR
64580, 64625–64626 (Sept. 20, 2016).
Section C.3.4, ‘‘Self-priming
capability test method,’’ of NSF/ANSI
50–2015 specifies that ‘‘the elapsed time
to steady discharge gauge reading or full
discharge flow’’ is to be recorded as the
measured priming time (MPT).
However, NSF/ANSI 50–2015 does not
specify how to determine ‘‘steady
discharge gauge reading or full
discharge flow.’’ In the September 2016
DPPP test procedure NOPR, DOE
proposed to determine steady discharge
gauge and full discharge flow as when
the changes in head and flow,
respectively, are within the tolerance
values specified in table 40.6.3.2.2,
‘‘Permissible amplitude of fluctuation as
a percentage of mean value of quantity
being measured at any test point,’’ of HI
40.6–2014. 81 FR 64580, 64626 (Sept.
20, 2016). Based on this criteria for
stabilization, DOE also proposed that
the elapsed time should be recorded
when both steady state pressure and
flow readings have been achieved. Id.
Section C.3.4 of NSF/ANSI 50–2015
then specifies that the true priming time
(TPT) is calculated by scaling the MPT
based on the relative diameter of the
riser pipe and the pump suction inlet
according to the following equation (6):
As discussed in the September 2016
DPPP test procedure NOPR, DOE noted
that, although theoretically correct,
testing with different riser pipe
diameters could affect the accuracy and
repeatability of the results, especially if
pipes that are substantially larger or
smaller than the pump suction inlet are
used. 81 FR 64580, 64626 (Sept. 20,
2016). As a result, DOE proposed that
testing of self-priming capability of pool
filter pumps that are not already
certified with NSF/ANSI 50–2015 be
performed with riser pipe that is of the
same pipe diameter as the pump suction
inlet. As a result, no adjustment of MPT
would be required and TPT would be
measured directly. Id.
Section C.3.4 of NSF/ANSI 50–2015
also specifies that the complete test
method must be repeated, such that two
TPT values are generated. In addition,
section C.3.5 of NSF/ANSI 50–2015
requires that both measurements must
be less than 6 minutes or the
manufacturer’s specified TPT,
whichever is greater. However, as the
criteria for TPT established in DOE’s
definitions (see section III.B.3.a) instead
reference a TPT of 10.0 minutes, DOE
proposed to specify that both test runs
result in TPT values that are less than
or equal to 10.0 minutes. 81 FR 64580,
64626 (Sept. 20, 2016).
Similarly, section C.3.5 of NSF/ANSI
50–2015 describes the TPT criteria that
pumps must meet in order to certify as
self-priming under NSF/ANSI 50–2015
and the caption of figure C.1 specifies
the VL criteria applicable to the NSF/
ANSI 50–2015 test. As noted previously,
DOE’s definitions proposed in the
September 2016 DPPP test procedure
NOPR reference a specific TPT of 10.0
minutes and VL of 5.0 feet. Therefore,
DOE proposed to exclude section C.3.5
and the relevant portions of the VL
definition in the caption of C.1 to be
consistent with DOE’s definition. 81 FR
64580, 64626 (Sept. 20, 2016).
In the September 2016 DPPP test
procedure NOPR public meeting, DOE
presented the general procedure for the
self-priming test. (Public Meeting
Presentation, No. 2 at p. 44) During the
September 2016 public meeting,
Hayward sought clarification regarding
the second step in the overview of the
self-priming test procedure DOE
provided in the preamble to the
September 2016 DPPP test procedure
NOPR. Specifically, Hayward sought
confirmation that the terminology ‘‘shut
off and allow pump to drain’’ did not
mean open the pump to atmosphere.
(Hayward, Public Meeting Transcript,
No. 3 at pp. 73–74)
In response to Hayward’s inquiry,
DOE notes that the statement in the
September 2016 DPPP test procedure
NOPR meant only to shut off the pump
and allow all lines to be drained of
water, without opening the pump to the
atmosphere, as would typically be the
case during the NSF/ANSI 50–2015 test.
Specifically, in the DPPP test procedure,
DOE is incorporating by reference
section C.3 of Annex C of NSF/ANSI
50–2015 with the minor modifications
discussed above as the test method for
determining the self-priming capability
of pool filter pumps and all testing must
be conducted in accordance with the
instructions in those sections.
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DOE also noted in the September
2016 DPPP test procedure NOPR that
NSF/ANSI 50–2015 does not specify an
instrument for measuring distance and
proposed that instruments for
measuring distance are accurate to ±0.1
inch, consistent with other requirements
for distance-measuring instruments
(section III.E.2.f). 81 FR 64580, 64625
(Sept. 20, 2016).
In section C.3.3, ‘‘Test conditions,’’
NSF/ANSI 50–2015 specifies test
conditions for both swimming pools and
hot tubs/spas. NSF/ANSI 50–2015
specifies test conditions in terms of
water temperature and turbidity
requirements. DOE notes that the
remainder of the DPPP test procedure is
to be conducted with ‘‘clear water,’’ as
required by HI 40.6–2014. While NSF/
ANSI 50–2015 and HI 40.6–2014
contain different requirements, DOE
believes they are intended to do the
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CEC, in written comments, supported
DOE’s proposal to use NSF/ANSI 50–
2015 to differentiate between selfpriming and non-self-priming pool filter
pumps. (CEC, No.7 at p. 2) DOE did not
receive any other comments suggesting
changes to DOE’s proposed test method
to determine the self-priming capability
of pool filter pumps.
Therefore, in this final rule, DOE is
adopting the self-priming test method
proposed in the September 2016 DPPP
test procedure NOPR without
modification. This method relies on
section C.3 of NSF/ANSI 50–2015 with
several minor clarifications and
modifications. However, DOE notes
that, as discussed in section III.E.1, in
this final rule, DOE is adopting
alternative requirements for the test
fluid instead of testing with ‘‘clear
water’’ as specified in HI 40.6–2014. As
such, to be consistent with the
remainder of the DPPP test procedure,
in this final rule DOE is adopting
provisions that testing for self-priming
capability be performed with the same
test fluid used for all other testing,
instead of testing with ‘‘clear water’’ as
proposed in the September 2016 DPPP
test procedure NOPR. DOE notes that
the characteristics of the test fluid
adopted in this final rule are now more
consistent with those in NSF/ANSI 50–
2015 as well.
Table III.13 provides a summary of
DOE’s modifications and additions to
NSF/ANSI 50–2015 to remove
ambiguity from the NSF/ANSI 50–2015
test method, improve the repeatability
of the test, and harmonize the test
requirements with the other DPPP test
procedure requirements contained in
this final rule.
TABLE III.13—SUMMARY OF MODIFICATIONS AND ADDITIONS TO NSF/ANSI 50–2015 SELF-PRIMING CAPABILITY TEST
NSF/ANSI 50–2015 section
NSF/ANSI 50–2015 specification
DOE modification/addition
Section C.3.2, ‘‘Apparatus,’’ and Section C.3.4,
‘‘Self-priming capability test method’’.
‘‘Essentially as shown in Annex C, figure C.1’’
Section C.3.2, ‘‘Apparatus’’ ................................
Measurement Instruments (no accuracy requirements).
Water temperature and turbidity requirements;
all measurements at hot tub/spa temperatures unless for swimming pool applications
only.
Measure MPT at steady discharge gauge or
full discharge flow.
More clearly specify the test setup requirements, where VL = 5.0 feet, adjusted to
nominal conditions of 14.7 psia and a water
density of 62.4 lb/ft3.
Accuracy requirements contained in HI 40.6–
2014, table 40.6.3.2.3, as applicable.
Test with clear water between 50 and 107 °F
with ≤15 NTU.
Section C.3.3, ‘‘Test conditions’’ ........................
Section C.3.4, ‘‘Self-priming capability test
method’’.
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Section C.3.4, ‘‘Self-priming capability test
method’’.
Section C.3.5, ‘‘Acceptance criteria,’’ and caption of figure C.1.
3. Determination of Maximum Head
As noted in section III.B.4.a, waterfall
pumps are, by definition, pool filter
pumps with maximum head less than or
equal to 30 feet, and a maximum speed
less than or equal to 1,800 rpm.
Therefore, in order to unambiguously
distinguish waterfall pumps from other
varieties of pool filter pumps, DOE must
establish a specific and repeatable
method for determining maximum head
of pool filter pumps. Based on the
demonstrated relationship between flow
and head, DOE understands the
maximum head to be associated with
the minimum flow of the pump.
However, DOE also understands that
pumps cannot always be operated safely
or reliable at zero or very low flow
conditions. Therefore, in the September
2016 DPPP test procedure NOPR, DOE
proposed that for the purposes of
differentiating waterfall pumps from
other varieties of pool filter pumps, the
maximum head of pool filter pumps be
determined based on the measured head
value associated with the maximum
speed and the minimum flow rate at
which the pump is designed to operate
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Adjust MPT to TPT based on relative diameter of suction inlet and pipe diameter.
TPT of 6 minutes or the manufacturer’s specified recommended time, whichever is greater and VL of 5.0 feet or the manufacturer’s
specified lift, whichever is greater.
continuously or safely. 81 FR 64580,
64627 (Sept. 20, 2016). DOE notes that
the minimum flow rate will be assumed
to be zero unless otherwise specified in
the manufacturer literature. Id.
DOE did not receive any comments in
response to the proposed test method
for determining maximum head.
Therefore, in this final rule, DOE is
adopting the proposal to determine the
maximum head of dedicated-purpose
pool pumps as the head associated with
the maximum speed and the minimum
flow rate at which the pump is designed
to operate continuously or safely, which
is assumed to be zero unless otherwise
specified in the manufacturer literature.
As discussed previously, in section
III.F, in the September 2016 DPPP test
procedure NOPR, DOE’s proposed test
procedure contained an optional test
method for determining EF at any
desired speed on any of the specified
optional system curves (i.e., Curve A, B,
C, or D), along with the tested speed and
the system curve associated with each
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energy factor value. 81 FR 64580,
64627–64628 (Sept. 20, 2016).
Regarding the test method for EF,
Pentair and APSP both commented that
table III.21 in the September 2016 DPPP
test procedure NOPR (81 FR 64580,
64628; Sept. 20, 2016) used inconsistent
terminology to specify the flow terms
for system curves A, B, C, and D and
recommended that the terms be reported
consistently as shown in table 4 of the
September 2016 DPPP test procedure
NOPR (Id. at 64653). (Pentair, No. 11 at
p. 6; APSP, No. 8 at p. 2) DOE has made
the correction in this final rule and
incorporated the correct table into
appendix B.
I. Labeling Requirements
H. Energy Factor Test Method
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Measure elapsed time at steady state pressure and temperature conditions; MPT is
when those conditions were first achieved.
Use pipe of the same diameter as the suction
inlet (MPT = TPT).
Excluded; TPT = 10 minutes and VL = 5.0
feet adjusted to nominal conditions of 14.7
psia and a water density of 62.4 lb/ft3.
In the June 2016 DPPP Working
Group recommendations, the DPPP
Working Group recommended that DOE
consider whether to require a label that
would facilitate proper application and
include specified horsepower
information. (Docket No. EERE–2015–
BT–STD–0008, No. 82,
Recommendation #9 at p. 5) To
implement the recommendations of the
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DPPP Working Group, DOE proposed in
the September 2016 DPPP test
procedure NOPR to require labeling of
all dedicated-purpose pool pumps for
which the DPPP Working Group
recommended test procedures. 81 FR
64580, 64628–29 (Sept. 20, 2016). That
is, DOE proposed that the labeling
requirements be applicable to:
• Self-priming pool filter pumps less
than 2.5 rated hydraulic horsepower,60
• non-self-priming pool filter pumps
less than 2.5 rated hydraulic
horsepower,
• pressure cleaner booster pumps,
and
• waterfall pumps.
Id.
For self-priming pool filter pumps,
non-self-priming pool filter pumps,
pressure cleaner booster pumps, and
waterfall pumps, DOE proposed that
each DPPP unit clearly display on the
permanent nameplate the following
information:
• WEF, in kgal/kWh,
• rated hydraulic horsepower,
• DPPP nominal motor horsepower,
• DPPP motor total horsepower, and
• service factor.
Id.
DOE also proposed specific
requirements regarding the formatting of
required information on the nameplate
and the specific terminology that is
required to be displayed. DOE proposed
that these labeling requirements would
be applicable to all units manufactured,
including imported, on the compliance
date of any potential energy
conservation standards that may be set
for dedicated-purpose pool pumps. Id.
ASAP and NRDC submitted a joint
written comment supporting the
labeling requirements proposed in the
September 2016 DPPP test procedure
NOPR. (ASAP and NRDC, No. 12 at p.
2)
Regarding the proposed formatting of
the label, Hayward requested
clarification regarding the specific
details of the label (e.g., font size, etc.).
(Hayward, Public Meeting Transcript.
No. 3 at pp. 93–94; Hayward, No. 6 at
p. 9) APSP also recommended that all
labeling details, including font size and
label material, comply with UL1081–
2016. (APSP, No. 8 at p. 10) Pentair
requested that the pool industry be
integrally involved in the labeling
60 DOE notes that the DPPP Working Group only
recommended standards for single-phase selfpriming pool filter pumps less than 2.5 rated
hydraulic horsepower. However, the DPPP Working
Group recommended that the test procedure and
reporting requirements would still be applicable to
single- and three-phase self-priming pool filter
pumps. Therefore, DOE believes it is appropriate to
apply the proposed labeling requirements to threephase pumps.
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efforts, pointing out that details
associated with label formatting and
sizing can be critical due to other
required safety and compliance labeling
requirements combined with limited
available space. (Pentair, No. 11, at p. 4)
Hayward similarly encouraged DOE to
allow use of standard industry
nomenclature (i.e., ‘‘HP’’ for horsepower
and ‘‘THP’’ for total horsepower) due to
limited space available on the product
for labels. (Hayward, No. 6 at p. 9)
Hayward also sought confirmation that
the information required may be
provided on separate labels/data plates
and is not required to be co-located on
one label or data plate. (Hayward, No.
6 at p. 9)
Hayward also objected to listing three
separate horsepower values saying it
will cause confusion and not support
the goal of having the correctly sized,
most energy efficient pump used in all
applications. As an alternative,
Hayward support listing only the total
horsepower on any DPPP label.
(Hayward, No. 6 at p. 9) Similarly, APSP
requested that, based on its
recommendations regarding horsepower
(see section III.G.1.b), only total
horsepower and not nominal motor
horsepower or service factor be listed on
the label, consistent with requirements
in ANSI/APSP/ICC 15a–2013. (APSP,
No. 8 at pp. 9–10) Nidec commented
similarly. (Nidec, No. 10 at p. 5)
APSP and Pentair commented that
while use of hydraulic horsepower for
the purposes of sizing is acceptable, use
of this value on a label would cause
significant confusion in the marketplace
and recommended it not be included on
the pump label.61 (APSP, No. 8 at pp.
7–8; Pentair, No. 11 at p. 3) Zodiac
similarly commented that so much
information on the label my cause
confusion during field installation and
may compromise proper installation of
the pump. (Zodiac, No. 13 at p. 3)
However, Zodiac did not provide a
suggested alternative.
Hayward, APSP, and Zodiac
expressed opposition to a requirement
that labeling include a specific WEF
result, stating that such designation may
disadvantage some manufacturers and
cause confusion in the marketplace
when dissimilar pumps are incorrectly
compared. (Hayward, No. 6 at p. 9;
APSP, No. 8 at pp. 9–10; Zodiac, No. 13
at p. 3) Zodiac also stated that the WEF
result may confuse or contradict
ENERGY STAR ratings. (Zodiac, No. 13
at p. 3) Hayward and APSP also
61 Note that separately APSP presented a
recommendation for required nameplate
information that did include rated hydraulic
horsepower. (APSP, No. 8 at pp. 9–10)
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36905
commented that the required label
should only state ‘‘meets DOE WEF
requirement.’’ (Hayward, No. 6 at p. 9;
APSP, No. 8 at p. 9)
APSP and Hayward recommended
that all labeling requirements be
removed for three-phase products, as
they are out of scope of the final ASRAC
working group term sheet. (APSP, No. 8
at p. 10; Hayward, No. 6 at p. 9)
As discussed previously, DOE’s
proposal in the September 2016 DPPP
test procedure NOPR contained details
regarding the font size, spacing, and
formatting of the required label, as well
as when such label would be required
to be applied. As proposed in the
September 2016 DPPP test procedure
NOPR, all orientation, spacing, type
sizes, typefaces, and line widths to
display this required information must
be the same as or similar to the display
of the other performance data on the
pump’s permanent nameplate. For this
reason, DOE believes that it is not
necessary to specify that the labeling
requirements comply with UL1081–
2016, as requested by APSP, or to have
additional industry involvement beyond
the comment period on the NOPR, as
requested by Pentair, given that the
manufacturers already have the option
to individually determine the details of
the label formatting. In response to
Hayward’s suggestion regarding use of
common industry abbreviations, DOE
notes that the use of ‘‘hp’’ for
horsepower was already allowed in
DOE’s proposed labeling requirements.
However, in light of Hayward’s
comments, DOE has modified its
proposal to also allow for the
abbreviation of total horsepower as
THP.
Given the modified requirements for
service factor and motor total
horsepower discussed in section
III.G.1.b, DOE agrees with Hayward,
APSP, and Nidec, that DPPP nominal
motor horsepower and DPPP service
factor do not need to be on the label. In
addition, DOE agrees with APSP and
Pentair that, while hydraulic
horsepower is necessary in certification
reporting and for compliance with
standards, this information is not used
by consumers and does not need to be
on the label.
With regard to Hayward, APSP,
Zodiac’s opposition to including the
WEF value on the label, DOE believes
that it is especially important to clearly
and consistently communicate the
performance of dedicated-purpose pool
pumps using the DOE metric in order to
provide customers with standardized,
comparable information to inform
purchasing decisions and is retaining
the requirement to include the WEF
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value on the DPPP label. With regard to
Zodiac’s comment regarding the
consistency of WEF and ENERGY STAR
EF information, DOE responds that, as
discussed in section III.H, as of 180 days
after the publication of this final rule all
representations of WEF, EF, and other
representations of dedicated-pool pump
performance must be made in
accordance with the adopted DOE test
procedure and, therefore, any EF values
will be consistent with the tested WEF
result for that pool pump in that they
will be based on the same test data.
However, regarding the confusion
between EF and WEF values, DOE is
clarifying in this final rule that, as of the
compliance date of any energy
conservation standard for dedicatedpurpose pool pumps, all manufacturers
and rating programs must transition to
the new WEF metric and
representations of EF will no longer be
allowed. DOE believes this will resolve
the confusion Zodiac is concerned with.
Representations of EF and WEF are
discussed in more detail in section III.H.
Therefore, in this final rule DOE is
adopting labeling provisions that
require dedicated-purpose pool pumps
subject to the test procedure to be
labeled only with WEF and DPPP motor
total horsepower. In response to
Hayward’s request that the required
information not be required to be colocated on one label or data plate, DOE
believes, given the reduced labeling
requirements adopted in this final rule
as compared to the NOPR proposal, that
it is entirely reasonable to require that
these values appear on the pump’s
permanent nameplate.
In response to APSP and Hayward’s
recommendation that labeling
requirements not apply to three-phase
products, DOE notes that this proposal
is not consistent with the
recommendations of the DPPP Working
Group. The June 2016 DPPP Working
Group recommendations only specified
that standards should not apply to
three-phase self-priming pool filter
pumps. (Docket No. EERE–2015–BT–
STD–0008, No. 82 Recommendations #3
at p. 2) Therefore, DOE believes that
requiring labels for three-phase pumps
is consistent with requiring them to be
subject to the test procedure and
reporting requirements, as
recommended by the DPPP Working
Group.
J. Replacement DPPP Motors
DOE understands that DPPP motors
typically require replacement more
frequently than DPPP bare pumps and,
thus, replacement DPPP motors are
often distributed in commerce to be
paired with an existing, appropriate
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DPPP bare pump in the field. DOE does
not intend to regulate replacement DPPP
motors, because they do not (by
themselves) meet the definition of a
dedicated-purpose pool pump.
However, DOE believes that end-users
and manufacturers may benefit from
having a method to determine an
applicable WEF for replacement DPPP
motors. This method could allow
replacement motor manufacturers to
label their products and/or utilities or
efficiency programs to encourage the
sale of replacement DPPP motors, which
could maintain or increase the savings
of the dedicated-purpose pool pump, as
installed in the field.
For those reasons, DOE proposed in
the September 2016 DPPP test
procedure NOPR an optional method to
determine the WEF for replacement
DPPP motors. 81 FR 64580, 64629 (Sept.
20, 2016). Specifically, under this
method, the replacement motor would
be paired with an appropriate DPPP
bare pump and the combination would
be subject to the DOE test procedure for
that dedicated-purpose pool pump,
based on the DPPP variety and speed
configuration. Id.
In the September 2016 DPPP test
procedure NOPR, DOE recognized that
replacement DPPP motors may be
offered for sale or advertised to be
paired with multiple DPPP bare pumps.
Furthermore, each combination of a
DPPP motor and a DPPP bare pump may
have a different WEF, as each bare
pump may affect the WEF rating.
Therefore, DOE proposed in the
September 2016 DPPP test procedure
NOPR that the WEF for each
replacement DPPP motor and bare
pump pairing be determined separately.
However, consistent with DOE’s
treatment of all equipment, DOE would
allow manufacturers to group similar
replacement motor-bare pump pairings
within a given replacement DPPP motor
rating to minimize testing burden, while
still ensuring that the rating is
representative of minimum efficiency or
maximum energy consumption of the
group. DOE also proposed that
replacement DPPP motor manufacturers
would be required to make a statement,
along with any advertised WEF value,
regarding the specific DPPP bare pump
to which the WEF value applies. If no
specific DPPP bare pumps were listed in
the manufacturer literature or otherwise
along with any WEF representation,
then the WEF value would be assumed
to be applicable to any and all possible
DPPP bare pumps. Id.
During the September 2016 DPPP test
procedure NOPR public meeting, CA
IOUs stated that if the worst performing
pump method were to be utilized for
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replacement motors, the bare pumps
considered would have to be specified
in order to determine which was the
worst performing. (CA IOUs, Public
Meeting Transcript, No. 3 at p. 80) As
such, CA IOUS proposed that if
manufacturers test the replacement
motors, the test report or result include
the range of products that were included
in the test. (CA IOUs, Public Meeting
Transcript, No. 3 at pp. 82–84)
DOE acknowledges CA IOUs’ concern
in unambiguously identifying the
replacement DPPP motor and bare
pump combination on which any WEF
value was based. However, as DOE is
proposing this as an optional procedure,
DOE did not propose any standard or
reporting requirements for replacement
DPPP motors. In addition, the
manufacturer of the replacement DPPP
motor may be different than the
manufacturer of the dedicated-purpose
pool pump. For this reason, DOE does
not believe that including such
information in the list of optional
information DPPP manufacturers may
submit when certifying products to DOE
would be appropriate. As reporting of
replacement DPPP motor WEF
information would have to be done as
a separate certification report and is not
based on compliance with any standard,
DOE does not believe collecting such
information is warranted at this time.
The purpose of the procedure is simply
to provide a standardized way to
determine WEF for replacement DPPP
motors.
ASAP, CA IOUs, CEC, and NRDC
commented to support the inclusion of
this optional test method for DPPP
replacement motors. (ASAP and NRDC,
No. 12 at p. 2; CA IOUs, No. 9 at p. 2;
CEC, No. 7 at p. 2) ASAP and NRDC and
CEC stated that the test method could
provide data to guide consumers and
support utility and efficiency programs
that seek to improve the efficiency of
dedicated-purpose pool pumps already
in use. (ASAP and NRDC, No. 12 at p.
2; CEC, No. 7 at p. 2)
In written comments, Pentair also
supported the optional test method for
DPPP replacement motors. However,
Pentair stated its belief that the DPPP
replacement motor testing should be
mandatory, to protect against pool
owners pairing low efficiency
replacement motors with kit pumps.
(Pentair, No. 11 at p. 4) CA IOUs also
believe that a national standard is
needed for DPPP replacement motors.
(CA IOUs, No. 9 at p. 2)
Conversely, in written comments,
APSP, Hayward, and Nidec opposed
DOE’s proposed optional test method
for replacement DPPP motors. (APSP,
No. 8 at pp. 10–11; Hayward, No. 6 at
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p. 9; Nidec, No. 10 at p. 6) Hayward
noted that such motors were not
discussed by the DPPP Working Group.
(Hayward, No. 6 at p. 9) Hayward and
Nidec also believe that the methodology
presented by DOE is not practical and
does not ensure compliance. (Hayward,
No. 6 at p. 9; Nidec, No. 10 at p. 6)
Nidec suggested that replacement DPPP
motors be regulated through an
expansion in small motor regulations.
(Nidec, No. 10 at p. 6)
DOE appreciates the support of ASAP,
CA IOUs, CEC, and NRDC. In response
to Pentair and CA IOU’s request to
adopt requirements for replacement
DPPP motors, DOE understands that
there is a potential for pool owners or
installation contractors to purchase and
pair a pump wet end with a lowefficiency replacement motor. However,
DOE notes that mandatory requirements
for DPPP replacement motors are
outside the scope of this rulemaking, as
this rulemaking pertains only to pumps
as defined in 10 CFR 431.462. DOE
proposed an optional test method for
replacement motors because of this
limitation on rulemaking scope. DOE
notes that in the future it could consider
mandatory requirements for
replacement DPPP motors as part of a
rulemaking specifically addressing such
motors.
DOE understands Hayward’s and
Nidec’s concerns and agrees that this
specific proposal was not discussed at
length by the DPPP Working Group.
However, DOE reiterates that the test
method contained in the September
2016 DPPP test procedure NOPR is an
optional test method that manufacturers
of DPPP motors may use at their
discretion; there is no associated
certification or compliance criteria for
replacement DPPP motors. That is,
replacement DPPP motors would not be
required to meet any energy
conservation standard set for dedicatedpurpose pool pumps. The purpose of
the test method is solely to provide
standardized information to consumers
regarding the efficiency and
performance of replacement DPPP
motors and provide an opportunity for
efficiency programs to incentivize the
application of more efficient
replacement DPPP motors. In response
to Hayward’s and Nidec’s concern that
the test method is impractical, DOE
believes that the proposed test method
presents a reasonable path to determine
the representative WEF score for
replacement DPPP motors and notes
that Hayward did not provide an
alternative suggestion. In response to
Nidec’s suggestion that replacement
DPPP motors be regulated through rules
crafted specifically for small motors,
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DOE notes that, as stated previously,
there are no regulatory requirements
pertaining to the optional motor test
method. Rather, the optional test
method proposed for DPPP motors is
intended to provide information to
consumers and efficiency incentive
programs regarding which motors will
conserve energy in a DPPP-specific
application, and DOE believes this
information would not be made
available through small motor
regulations. As noted previously, this
does not preclude DOE from
considering mandatory requirements for
replacement DPPP motors as part of a
rulemaking specifically addressing such
motors.
Hayward also recommended
clarifying that replacement motors
identical to the original motor that was
used to test and qualify the DPPP model
(only varying in nomenclature for
marketing purposes, such as service part
number) should be permitted to make
representations of WEF when sold for
use with the specific bare pump,
without the need for additional testing.
(Hayward, No. 6 at p. 9) DOE agrees
with Hayward’s suggestion. DOE
believes that so long as the testing of a
given DPPP motor and bare pump pair
was performed consistent with DOE’s
test procedure for replacement DPPP
motors, the rating will be accurate. As
such, the resultant WEF score can be
applied to the tested replacement DPPP
motor when offered for sale with the
tested DPPP bare pump and would be
identical to that applied to the DPPP
model comprised of that DPPP motor
and bare pump.
K. Certification and Enforcement
Provisions for Dedicated-Purpose Pool
Pumps
DOE must provide uniform methods
for manufacturers to determine
representative values of energy- and
non-energy-related metrics, for each
basic model. See 42 U.S.C. 6314(a)(2).
These values are used when making
public representations and when
determining compliance with
prescribed energy conservation
standards. DOE proposed in the
September 2016 DPPP test procedure
NOPR that DPPP manufacturers use a
statistical sampling plan consistent with
the sampling plan for pumps that is
currently specified at 10 CFR 429.59 to
determine representative values of WEF
and other energy-related metrics. 81 FR
64580, 64629 (Sept. 20 2016).
Manufacturers would use these
sampling plans to determine the
representative values of WEF and other
metrics necessary to demonstrate
compliance with the adopted energy
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36907
conservation standards for dedicatedpurpose pool pumps. In addition, DOE
commonly specifies enforcement
procedures that DOE uses to verify
compliance of a basic model. Sections,
III.K.1, III.K.2, and III.K.3 discuss DOE’s
sampling plan, certification
requirements, and enforcement
provisions for dedicated-purpose pool
pumps, respectively.
1. Sampling Plan
DOE provides, in subpart B to 10 CFR
part 429, sampling plans for all covered
equipment. For dedicated-purpose pool
pumps, DOE proposed in the September
2016 DPPP test procedure NOPR to
adopt statistical sampling plans for
WEF, EF, and other energy-related
metrics similar to those adopted for
pumps. 81 FR 64580, 64630 (Sept. 20,
2016). These sampling plans generally
require a sample of sufficient size such
that the representative value of WEF,
EF, or any other energy consumption
metric of a DPPP basic model is less
than or equal to the lower of: (A) The
lower 95 percent confidence limit
divided by 1.05 or (B) the mean of the
sample. DOE also proposed similar
provisions for quantities, such as pump
input power, for which consumers
would favor lower values. See 10 CFR
429.59(a)(1)(ii).
In addition to energy-related metrics,
DOE also noted that the rated hydraulic
horsepower, DPPP nominal motor
horsepower, DPPP motor total
horsepower, service factor, and true
power factor are important
characteristics for dedicated-purpose
pool pumps that must be reported for
each DPPP basic model based on the
sampling plan discussed above.
Therefore, DOE also proposed that DPPP
nominal motor horsepower, DPPP motor
total horsepower, service factor, and
true power factor for each DPPP basic
model be determined based on the mean
of the applicable test results, for each
metric, from all the tested units that
serve as the basis for the rating for that
basic model. 81 FR 64580, 64630 (Sept.
20, 2016).
In written comments, Hayward and
APSP requested clarification of
sampling plan and record keeping
requirements for certain motor
characteristics. Specifically, APSP and
Hayward asked if DOE expects DPPP
manufacturers to establish, maintain,
and retain underlying test data for
nominal motor horsepower, motor total
horsepower, and motor service factor for
2 years from the date on which the
model is no longer distributed in
commerce or if this information would
be the responsibility of the individual
motor manufacturers. (APSP, No. 8 at p.
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9; Hayward, No. 6 at pp. 7–8) In
addition, as noted in section III.H,
Hayward expressed concern over DOE’s
requirements being in conflict with
other industry programs, especially
those regarding determination of EF.
(Hayward, No. 6 at p. 1)
In response to Hayward, DOE notes
that while motor manufacturers may
conduct testing of motors, it is the
responsibility of the DPPP manufacturer
to retain the underlying test data. As
discussed in section III.G.1.b, DOE is
adopting test methods for determination
of motor horsepower characteristics
consistent with those currently used in
the industry. However, given the
suggestion from interested parties that
DOE only require listing DPPP motor
total horsepower on the label (see
section III.I), DOE is withdrawing the
proposal to establish sampling plans for
DPPP nominal motor horsepower and
DPPP service factor and adopting a
sampling plan for DPPP motor total
horsepower only.
Regarding potential conflict with
industry programs, which DOE believes
relates primarily to the sampling plan
(as other provisions are quantitatively
consistent), in this final rule, DOE limits
the sampling plan to only metrics
necessary for DOE’s test procedure,
standard, and labeling requirements
(i.e., WEF, rated hydraulic horsepower,
and DPPP motor total horsepower). DOE
has removed the sampling plan
requirements for EF and other motor
horsepower metrics. DOE is adopting
the other sampling provisions proposed
in the September 2016 DPPP test
procedure NOPR without modification.
In written comments, APSP asked
whether small modifications to the
‘‘basic model’’ require new samples to
be tested, and if so, if there is a defined
threshold regarding what change would
require a new sample to be tested.
(APSP, No. 8 at pp. 10–11) DOE believes
that APSP is asking about how changes
to an individual model’s design impact
the represented value for a basic model.
If any design changes to an individual
model that is part of a basic model
result in a more consumptive or less
efficient represented value, then the
individual model must be retested and
the represented value must be revised
based on the results of the retesting.
2. Certification Requirements
Paragraph (b) of 10 CFR 429.59
contains the certification requirements
for certain styles of pumps for which
DOE adopted test procedures and
standards in the January 2016 general
pumps test procedure and ECS final
rules. 81 FR 4086 (Jan. 25, 2016); 81 FR
4368 (Jan. 26, 2016). Because dedicated-
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purpose pool pumps are a style of
pump, DOE proposed in the September
2016 DPPP test procedure NOPR to
amend 10 CFR 429.59 to include the
reporting requirements for dedicatedpurpose pool pumps. 81 FR 64580,
64630–64632 (Sep. 20, 2016).
Specifically, DOE proposed that the
general certification report requirements
contained in 10 CFR 429.12 would
apply to dedicated-purpose pool pumps
as they do to other styles of pumps,
including general pumps. However,
because dedicated-purpose pool pumps
have a unique test procedure and metric
from general pumps, DOE proposed
unique certification requirements for
dedicated-purpose pool pumps that
require manufacturers to supply certain
additional information to DOE in
certification reports to demonstrate
compliance with any energy
conservation standards that DOE may
set. Id.
Specifically, DOE proposed that the
following items be included in
certification reports and made public on
DOE’s Web site:
• WEF in kilogallons per kilowatthour (kgal/kWh);
• rated hydraulic horsepower in
horsepower (hp);
• maximum speed of rotation in
revolutions per minute (rpm);
• dedicated-purpose pool pump
nominal motor horsepower in
horsepower (hp);
• dedicated-purpose pool pump
motor total horsepower in horsepower
(hp);
• dedicated-purpose pool pump
service factor (dimensionless);
• the speed configuration for which
the pump is being rated (i.e., singlespeed, two-speed, multi-speed, or
variable-speed);
• for self-priming pool filter pumps,
non-self-priming pool filter pumps, and
waterfall pumps, the maximum head in
feet; and
• for self-priming and non-selfpriming pool filter pumps: The vertical
lift and true priming time for the DPPP
model and a statement regarding
whether the pump is certified with
NSF/ANSI 50–2015. Id.
In the June 2016 DPPP Working
Group recommendations, the DPPP
Working Group also recommended that
DOE require reporting of true power
factor at all applicable test procedure
load points in the public information
provided in the certification report for
all dedicated-purpose pool pumps to
which the test procedure is applicable
(i.e., self-priming and non-self-priming
pool filter pumps, waterfall pumps, and
pressure cleaner booster pumps).
(Docket No. EERE–2015–BT–STD–0008,
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No. 82, Recommendation #7 at p. 4) As
such, DOE proposed that, for all
dedicated-purpose pool pumps to which
the test procedure is applicable, true
power factor be reported at all
applicable test procedure load points in
the certification report and be made
public on DOE’s Web site. 81 FR 64580,
64630–64632 (Sep. 20, 2016).
In addition, as discussed in section
III.B.7, the DPPP Working Group
recommended specific prescriptive
requirements for dedicated-purpose
pool pumps distributed in commerce
with freeze protection controls to ensure
freeze protection controls on dedicatedpurpose pool pumps only operate when
necessary and do not result in
unnecessary, wasted energy use.
Specifically, the DPPP Working Group
recommended that all dedicatedpurpose pool pumps distributed in
commerce with freeze protection
controls be shipped either:
(1) With freeze protection disabled or
(2) with the following default, useradjustable settings:
a. The default dry-bulb air
temperature setting is no greater than 40
°F; and
b. The default run time setting shall
be no greater than 1 hour (before the
temperature is rechecked); and
c. The default motor speed shall not
be more than 1⁄2 of the maximum
available speed.
(Docket No. EERE–2015–BT–STD–
0008, No. 82, Recommendation #6A at
p. 4)
Relatedly, the DPPP Working Group
recommended that, in order to certify
compliance with such a requirement,
DPPP manufacturers be required to
make a statement certifying compliance
to the applicable design requirement
and make available publicly as part of
their literature the details by which they
have met the applicable design
standard. (Docket No. EERE–2015–BT–
STD–0008, No. 82, Recommendation
#6B at p. 4) The DPPP Working Group
specifically recommended that, as part
of certification reporting, manufacturers
must include the default dry-bulb air
temperature setting (in °F), default run
time setting (in minutes), and default
motor speed (in rpm). (Docket No.
EERE–2015–BT–STD–0008, No. 82,
Recommendation #6A at p. 4) Therefore,
consistent with recommendations of the
DPPP Working Group, DOE proposed
that, for dedicated-purpose pool pumps
distributed in commerce with freeze
protection controls enabled, the
certification report also include the
default dry-bulb air temperature setting
(in °F), default run time setting (in
minutes), and default motor speed (in
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rpm). 81 FR 64580, 64630–64632 (Sep.
20, 2016).
The DPPP Working Group also
recommended that DOE include a
verification procedure in case there was
ever an issue regarding whether a
product distributed in commerce
actually had such features. (Docket No.
EERE–2015–BT–STD–0008, No. 82,
Recommendation #6A at p. 4) The
verification test is discussed in more
detail in section III.K.3.
Finally, for integral cartridge-filter
and sand-filter pool pumps, the DPPP
Working Group recommended DOE
consider only a prescriptive standard,
which requires such pumps be
distributed in commerce with pool
pump timers. (Docket No. EERE–2015–
BT–STD–0008, No. 51,
Recommendation #2B at pp. 1–2)
Relatedly, the DPPP Working Group also
recommended a definition for pool
pump timer that describes the specific
features and operational characteristics
that applicable pool pump timers must
contain in order to comply with the
prescriptive standard. The
recommended definition defines pool
pump timer as a pool pump control that
automatically turns off a dedicatedpurpose pool pump after a run-time of
no longer than 10 hours. As such, for
these DPPP varieties, DOE proposed that
the certification report must contain the
maximum run-time of the pool pump
control with which the integral
cartridge-filter or sand-filter pump is
distributed in commerce. 81 FR 64580,
64630–64632 (Sep. 20, 2016).
In addition to the required elements,
DOE recognizes that other DPPP
characteristics may provide useful
information to inform consumers or
support programs related to dedicatedpurpose pool pumps. To provide
additional information to consumers
and the market place, DOE proposed in
the September 2016 DPPP test
procedure NOPR that the following
information may optionally be included
in certification reports and, if included,
would be made public:
• Calculated driver power input and
flow rate at each load point i (Pi and Qi),
in horsepower (hp) and gallons per
minute (gpm), respectively; and/or
• Energy factor at any desired speed
on any of the specified optional system
curves (i.e., Curve A, B, C, or D), along
with the tested speed and the system
curve associated with each energy factor
value. 81 FR 64580, 64631–32 (Sept. 20,
2016).
Although useful to consumers and the
public, DOE recognizes that
manufacturers may incur additional
burden conducting the testing for and
reporting of these additional metrics.
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DOE reiterates that the reporting of
these additional metrics will be optional
and at the discretion of the
manufacturer.
In response to DOE’s proposed
reporting requirements, ASAP and
NRDC submitted written comments in
support of the certification requirements
proposed in the September 2016 DPPP
test procedure NOPR. (ASAP and
NRDC, No. 12 at p. 2) DOE appreciates
the support of ASAP and NRDC.
During the September 2016 DPPP test
procedure NOPR public meeting,
Hayward inquired if they have a pump
that meets acceptable NSF priming
criteria, how this should be reported
along with the WEF value. (Hayward,
Public Meeting Transcript, No. 3 at p.
74) Additionally, in written comments,
Hayward and APSP commented that the
vertical lift and true priming time fields
should only be applicable to selfpriming pool filter pumps that are not
certified with NSF/ANSI 50–2015.
(Hayward, No. 6 at p. 10; APSP, No. 8
at p. 11)
As noted in the September 2016 DPPP
test procedure NOPR, for self-priming
and non-self-priming pool filter pumps,
the certification report is required to
include the vertical lift and true priming
time for the DPPP model and a
statement regarding whether the pump
is certified with NSF/ANSI 50–2015.
However, in light of Hayward and
APSP’s concern, DOE recognizes that
these requirements are only necessary
and relevant for self-priming pool filter
pumps. In addition, consistent with
Hayward and APSP’s request, DOE
agrees that a statement that the selfpriming pool filter pump is certified
with NSF/ANSI 50–2015 is sufficient to
demonstrate compliance with DOE’s
definition for self-priming pool filter
pump. Therefore, in this final rule, DOE
is modifying the certification reporting
requirements such that only selfpriming pool filter pumps that are not
certified with NSF/ANSI 50–2015 need
provide the vertical lift and true priming
time for the DPPP model.
In written comments, Hayward and
APSP requested that DOE explain why
maximum head (‘‘dead head’’) is listed
and recommended removing it, as they
did not see the need to list it. (Hayward,
No. 6 at p. 10; APSP, No. 10 at p. 11)
In response, DOE clarifies that
maximum head is necessary to
differentiate waterfall pumps from selfpriming and non-self-priming pool filter
pumps. As described in section III.B.4.a,
section III.G.3, and the September 2016
DPPP test procedure NOPR, waterfall
pumps are, by definition, pool filter
pumps with maximum head less than or
equal to 30 feet, and a maximum speed
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less than or equal to 1,800 rpm.
Therefore, in order to unambiguously
distinguish waterfall pumps from other
varieties of pool filter pumps, DOE
established a specific and repeatable
method for determining maximum head
of pool filter pumps (discussed in
section III.G.3). DOE requires reporting
of the maximum head, determined in
accordance with the test procedure for
self-priming pool filter pumps, non-selfpriming pool filter pumps, and waterfall
pumps, to ensure that such pumps are
appropriately categorized into the
correct equipment class.
Hayward and APSP also
recommended that, for dedicatedpurpose pool pumps with freeze
protection controls shipped disabled,
the default dry-bulb air temperature
setting, default run time setting, and
default motor speed setting should not
have to be reported. (Hayward, No. 6 at
p. 10; APSP, No. 10 at p. 11) In
response, DOE notes that Hayward and
APSP’s suggestion is consistent with the
proposal in the September 2016 DPPP
test procedure NOPR. 81 FR 64580,
64645 (Sept. 20, 2016). As such, in this
final rule, DOE is adopting the proposal
in the September 2016 DPPP test
procedure NOPR that in the certification
report all dedicated-purpose pool
pumps must provide a statement
regarding if freeze protection is shipped
enabled or disabled, but only dedicatedpurpose pool pumps distributed in
commerce with freeze protection
controls enabled must provide the
default dry-bulb air temperature setting
(in °F), default run time setting (in
minutes), and default motor speed (in
rpm).
During the September 2016 DPPP test
procedure NOPR public meeting, CA
IOUs recommended clarifying that the
maximum run time for integrated
cartridge-filter and sand-filter pumps
referred to the maximum run time
without resetting the timer. (CA IOUs,
Public Meeting Transcript, No. 3 at p.
90) In response, DOE acknowledges CA
IOUs concern that the maximum run
time in the field could be extended by
resetting the timer. However, DOE
believes that the maximum run time of
the model is the maximum time interval
for which the timer can be set to run and
that it is implied that such does not
account for resetting of the timer, as it
is a physical and unambiguous
characteristic of the equipment.
Therefore, DOE agrees with CA IOUs
regarding the intent of the statement,
but does not believe such clarification is
necessary.
APSP and Hayward also requested
confirmation that the test procedure to
determine EF is optional and neither it
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nor data relating to it will be required
to be provided or certified to DOE.
(APSP, No. 8 at p. 9; Hayward, No. 6 at
p. 8) Similarly, Zodiac also commented
that optional items, such as EF, pump
efficiency, overall efficiency, driver
power input, and/or pump power
output, should remain optional and up
to the manufacturer to present. (Zodiac,
No. 13 at p. 3)
Regarding APSP, Hayward, and
Zodiac’s comments with respect to EF
and other optional tested values (i.e.,
pump efficiency, overall efficiency,
driver power input, and/or pump power
output), DOE reiterates that the EF test
procedure proposed was optional in that
manufacturers may decline to make any
representations of EF, but that if made,
all representations of relevant metrics,
including EF, would need to be based
on the DOE test procedure 180 days
after publication of this final rule in the
Federal Register. However, EF, pump
efficiency, overall efficiency, driver
power input, and/or pump power
output are not required to be reported to
DOE.
In addition, as discussed in section
III.F, DOE received several comments
from interested parties regarding the
testing and representation of energy
factor and consistency with other
programs. To respond to the concerns of
interested parties and clarify the
applicability of DPPP metrics, DOE, in
this final rule, is adopting two
appendices that are applicable before
(appendix B) and on or after (appendix
C) July 19, 2021, the compliance date of
the adopted energy conservation
standards for this equipment. As a result
of the confusion regarding
representations of energy factor and the
lack of comments supporting the
optional reporting of energy factor to
DOE, DOE is not adopting the proposal
to optionally list any tested energy
factor values in the certification report
submitted to DOE. Specifically, DOE is
not including EF at any desired speed
on any of the specified optional system
curves (i.e., Curve A, B, C, or D), along
with the tested speed and the system
curve associated with each energy factor
value in the certification report.
DOE did not receive any other
comments or suggestions regarding the
certification reporting requirements for
dedicated-purpose pool pumps. As
such, DOE is adopting, in this final rule,
the certification reporting requirements
as proposed in the September 2016
DPPP test procedure NOPR, with the
exception of the optional listing of
energy factor as discussed above. DOE is
also clarifying the applicability of the
certification requirements that are only
applicable to certain styles of pumps for
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which DOE adopted test procedures and
standards in the January 2016 general
pumps test procedure and ECS final
rules. 81 FR 4086 (Jan. 25, 2016); 81 FR
4368 (Jan. 26, 2016). DOE notes that, as
specified in paragraph (a) of 10 CFR
429.12, the certification requirements
for covered products and equipment,
including those discussed in this final
rule, are only applicable to equipment
subject to an applicable energy
conservation standard set forth in 10
CFR part 430 or 431. Therefore, the
certification requirements established in
this final rule will only be required on
and after July 19, 2021, the compliance
date for energy conservation standards
for dedicated-purpose pool pumps.
3. Enforcement Provisions
Enforcement provisions govern the
process DOE will follow when
performing its own assessment of basic
model compliance with standards, as
described under subpart C of 10 CFR
part 429. Specifically, subpart C
describes the notification requirements,
legal processes, penalties, specific
prohibited acts, and testing protocols
related to testing covered equipment to
determine or verify compliance with
standards. 10 CFR 429.102–429.134.
DOE notes that the same general
enforcement provisions contained in
subpart C of 10 CFR part 429 will be
applicable to dedicated-purpose pool
pumps.
Related to enforcement testing of
dedicated-purpose pool pumps, as
specified in 10 CFR 429.110(e), DOE
proposed in the September 2016 DPPP
test procedure NOPR to conduct the
applicable DPPP test procedure, to
determine the WEF for tested DPPP
models. 81 FR 64580, 64632 (Sept. 20,
2016). In addition, DOE proposed to
use, when determining performance for
a specific basic model, the enforcement
testing sample size, calculations, and
procedures laid out in appendix A to
subpart C of 10 CFR part 429 for
consumer products and certain highvolume commercial equipment. These
procedures, in general, provide that
DOE will test an initial sample of at
least 4 units and determine the mean
WEF value and standard error of the
sample. DOE will then compare these
values to the WEF standard level, once
adopted, to determine the compliance of
the basic model or if additional testing
(up to a total of 21 units) is required to
make a compliance determination with
sufficient confidence. DOE also
proposed to clarify that the provisions at
10 CFR 429.110(e)(5), which are
applicable to general pumps subject to
the January 2016 general pumps test
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procedure final rule, are not applicable
to dedicated-purpose pool pumps. Id.
In addition, when determining
compliance of any units tested for
enforcement purposes, DOE proposed in
the September 2016 DPPP test
procedure NOPR to adopt provisions
that specify how DOE would determine
the rated hydraulic horsepower at
maximum speed on the reference curve
for determining the appropriate test
method and standard level for any
tested equipment (if applicable).
Specifically, DOE proposed to perform
the same test procedure for determining
the rated hydraulic horsepower at
maximum speed on the reference curve
specified by the test procedure for each
DPPP variety (see section III.D) on one
or more units of each model selected for
testing. DOE proposed that, if the rated
hydraulic horsepower determined
through DOE’s testing (either the
measured rated hydraulic horsepower
for a single unit sample or the average
of the measured rated hydraulic
horsepower values for a multiple unit
sample) is within 5 percent of the
certified value of rated hydraulic
horsepower, then DOE will use the
certified value of rated hydraulic
horsepower as the basis for determining
the standard level for tested equipment.
However, if DOE’s tested value of rated
hydraulic horsepower is not within 5
percent of the certified value of rated
hydraulic horsepower, DOE will use the
arithmetic mean of all the rated
hydraulic horsepower values resulting
from DOE’s testing when determining
the standard level for tested equipment.
81 FR 64580, 64632 (Sept. 20, 2016).
In addition, DOE proposed to
establish similar procedures for relevant
quantities necessary to differentiate the
varieties of pool filter pumps: Selfpriming pool filter pumps, non-selfpriming pool filter pumps, and waterfall
pumps. Specifically, to differentiate
waterfall pumps, DOE proposed an
enforcement testing procedure for the
maximum head value. Similarly, to
differentiate self-priming and non-selfpriming pool filter pumps, DOE
proposed performing the self-priming
capability test and determine the
vertical lift and true priming time of one
or more tested units. DOE proposed
tolerances of 5 percent on the certified
values in both of these instances as well.
Id.
Pentair responded that without audit
and enforcement, the economic effect
from the potential costs related to
testing (see section IV.B) could be low
as manufacturers will not feel
compelled to re-test dedicated-purpose
pool pumps. (Pentair, No. 11 at p. 4)
DOE responds that DOE does conduct
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enforcement testing, as discussed in this
section. If a product is suspected of not
meeting the minimum energy
conservation standard, DOE has
enforcement mechanisms to verify the
equipment performance in relation to
the standard. DOE’s burden assessment
contained in section IV.B reflects the
assumption that manufacturers will
conduct testing and certify equipment
in accordance with the test procedure
adopted in this final rule.
DOE did not receive any other
comments related to DOE’s proposal
related to enforcement testing
provisions for WEF, rated hydraulic
horsepower, maximum head, or selfpriming capability. As such, DOE is
adopting the enforcement testing
provisions for WEF, rated hydraulic
horsepower, and maximum head, as
proposed in the September 2016 DPPP
test procedure NOPR. However, with
regard to the enforcement provisions to
verify the self-priming capability of nonself-priming pool filter pumps and selfpriming pool filter pumps not certified
with NSF/ANSI 50–2015, DOE notes
that, in response to comments from
interested parties, DOE is removing the
requirement to report the vertical lift
and true priming time of non-selfpriming pool filter pumps, as discussed
in section III.K.2. As DOE’s proposed
enforcement testing provisions included
comparing the tested values to the
values of vertical lift and true priming
time certified by the manufacturer to
determine the validity of the certified
values, DOE must adopt different
criteria for non-self-priming pool filter
pumps, as they will not have certified
values to which DOE can compare the
test results. Instead, DOE is adopting
validity criteria for non-self-priming
pool filter pumps based on the values of
vertical lift and true priming time
referenced in the definition of non-selfpriming pool filter pump. That is, DOE
will compare the values of vertical lift
and true priming time obtained from the
tested unit(s) to the values of vertical lift
and true priming time referenced in the
definition of non-self-priming pool filter
pump (i.e., 5.0 feet and 10.0 minutes,
respectively). DOE will continue to
apply the same tolerance of 5 percent so
that any non-self-priming pool filter
pump that is not capable of priming to
a vertical lift of 5.0 feet with a true
priming time of less than or equal to 9.5
minutes (10.0 minutes—5 percent) will
continue to be treated as a non-selfpriming pool filter pump, as certified by
the manufacturer. DOE notes that
vertical lift and true priming time are
related variables, such that the 5 percent
tolerance need only be applied to true
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priming time as the independent
variable.
In addition, based on DPPP Working
Group recommendations (Docket No.
EERE–2015–BT–STD–0008, No. 82,
Recommendation #6B at p. 4), DOE also
proposed in the September 2016 DPPP
test procedure NOPR a procedure to
verify the presence and operation of any
freeze protection controls distributed in
commerce with any applicable
dedicated-purpose pool pump. The
proposed procedure starts by installing
the DPPP unit in a test stand in
accordance with HI 40.6–2014 with the
pump powered on but not circulating
water (i.e., the controls are active and
the flow or speed are set to zero). The
temperature measured by the freeze
protection temperature control would
then be gradually decreased by 1 ± 0.5
°F every 5.0 minutes, starting at 42 ± 0.5
°F until the pump freeze protection
controls initiate water circulation or 38
± 0.5 °F, whichever occurs first. The
freeze protection ambient temperature
reading and DPPP rotating speed, if any,
would be recorded after each reduction
in temperature and subsequent
stabilization. 81 FR 64580, 64633 (Sept.
20, 2016).
Under DOE’s proposed test procedure,
if the DPPP freeze protection controls do
not initiate water circulation at a
temperature of 38 ± 0.5 °F, as measured
by the freeze protection ambient
temperature sensor, the test would
conclude and the dedicated-purpose
pool pump would be deemed
compliant. If the freeze protection
controls initiate water circulation, the
temperature would be increased to 42 ±
0.5 °F and the dedicated-purpose pool
pump would be allowed to run for at
least 30.0 minutes. After 30.0 minutes,
the freeze protection ambient
temperature and rotating speed, if any,
would be recorded again. If the
dedicated-purpose pool pump initiated
water circulation at a temperature
greater than 40 °F, if the dedicatedpurpose pool pump is still circulating
water after 30.0 minutes of operation at
42 ± 0.5 °F, or if rotating speed for freeze
protection is greater than one-half of the
maximum rotating speed of the DPPP
model, as certified by the manufacturer,
that DPPP model would be deemed to
not comply with the stated design
requirement for freeze protection
controls. Id.
In written comments, ASAP and
NRDC expressed appreciation that DOE
developed a verification procedure that
can be used to verify whether a DPPP
shipped with freeze protection controls
meets the freeze protection certification
requirements promulgated in this rule.
(ASAP and NRDC, No. 12 at pp. 2–3)
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36911
DOE appreciates the support of ASAP
and NRDC.
During the September 2016 DPPP test
procedure NOPR public meeting,
Pentair raised a concern that the default
run-time setting in the freeze protection
requirements recommended by the
DPPP Working Group is no greater than
an hour, but the test procedure stops
after 30.0 minutes. (Pentair, Public
Meeting Transcript, No. 3 at p. 101)
In response, DOE agrees with Pentair
that the time requirement in the freeze
protection enforcement testing
procedure should be 60.0 minutes,
rather than the 30.0 minutes proposed
in the September 2016 DPPP test
procedure NOPR, consistent with the
recommendations of the DPPP Working
Group. Therefore, in this final rule, DOE
is updating the procedure to allow 60.0
minutes of operation before the freeze
protection ambient temperature and
rotating speed, if any, will be recorded
again.
In written comments, APSP and
Pentair questioned why the dry-bulb
temperature was selected as the
measurement to determine temperature.
APSP and Pentair commented that few
if any of the products in the market use
dry-bulb temperature sensors to initiate
freeze protection controls. (APSP, No. 8
at p. 4; Pentair, No. 11 at p. 2) DOE
responds that DOE researched the
typical controls and sensing
mechanisms of freeze protection
controls when developing the test
method. Based on DOE’s research, the
three largest pool pump manufacturers
produce freeze protection systems that
sense the ambient air temperature and
(if freeze protection is enabled) activate
the freeze protection mode when the
ambient air temperature falls below a
certain threshold.62 On May 19, 2016,
the DPPP Working Group discussed
using the dry-bulb air temperature as
one of the key metrics for specifying the
characteristics of freeze protection
controls, and no members of the group
opposed the use of dry-bulb
temperature. (Docket No. EERE–2015–
BT–STD–0008, No. 101 at pp. 105–107)
Then, the DPPP Working Group
recommended that manufacturers
include dry-bulb air temperature in
their certification reports. (Docket No.
EERE–2015–BT–STD–0008, No. 82
Recommendation #6A at p. 4) DOE
62 Several operation manuals for pool control
systems note that freeze protection is triggered by
air temperature. See, for example: Pentair.
Intellitouch Quick-Start Manual. 2004.
www.pentairpool.com/pdfs/
IntelliTouchQuickStartIG.pdf. Hayward. Pro Logic
Operation Manual. 2010. www.hayward-pool.com/
pdf/manuals/PLTPM-PL-PS-x&PL-PS-xVOperationsOct08&Later.pdf.
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believes that the manufacturers’
installation and operation manuals, the
DPPP Working Group discussions, and
the DPPP Working Group
recommendations provide ample
justification for using dry-bulb air
temperature as a certification
requirement for dedicated-purpose pool
pumps distributed in commerce with
freeze protection controls enabled.
Further, DOE is not aware of other
temperature-based criteria that are
relevant to the activation of freeze
protection controls at this time and
Pentair did not provide an alternative
recommendation in their comments. If
freeze protection controls are developed
that activate based on alternative
temperature criteria (other than dry-bulb
air temperature), DOE may consider
modifying the enforcement test and any
prescriptive freeze protection control
requirements at that time.
CA IOUs also raised questions related
to the temperature measurement
apparatus and whether the
measurement would be impacted by
heat created by the DPPP motor. (CA
IOUs, Public Meeting Transcript, No. 3
at pp. 101–102)
In response, DOE notes that, as
described in the September 2016 DPPP
test procedure NOPR, several methods
are allowed to control and record the
temperature registered by the freeze
protection ambient temperature sensor.
This can be accomplished, depending
on the specific location and
configuration of the temperature sensor,
by exposing the freeze protection
thermocouple to a specific temperature
by, for example, submerging the
thermocouple in a water bath of known
temperature, adjusting the ambient air
temperature of the test chamber and
measuring the temperature directly at
the freeze protection ambient
temperature sensor location, or other
means to simulate and vary the ambient
temperature registered by the freeze
protection temperature sensor(s). While
DOE acknowledges that, as noted by CA
IOUs, the temperature measured by the
freeze protection ambient temperature
sensor may be slightly higher than the
bulk ambient temperature due to
localized heating of the sensor from the
DPPP motor and controls, DOE believes
this is representative of operation in the
field and the test procedure is designed
to accommodate this. Based on the
recommendations of the DPPP Working
Group, the freeze protection
enforcement test is designed to identify
DPPP freeze protection controls that
initiate water circulation when the
freeze protection ambient temperature
sensor registers 40.0 °F or higher,
regardless of the bulk ambient
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temperature (which may be slightly
cooler than 40.0 °F). DOE notes that this
is accomplished regardless of the
method used to measure and control the
freeze protection ambient temperature
sensor and enables the variety of
methods discussed previously. If only
the bulk ambient temperature were
measured, the pump would need to be
placed in an environmental chamber
and the temperature of the chamber
controlled in order to test the freeze
protection controls operation. In
summary, DOE believes that the
proposed temperature measurement
methods provide a representative
measure of the ambient temperature
measured by the freeze protection
controls and minimizes burden
associated with the test by providing a
variety of options for measuring and
controlling the temperature registered
by the freeze protection ambient
temperature sensor. DOE also believes
the proposal is consistent with the
intent of the DPPP Working Group
recommendations. Therefore, while
DOE acknowledges CA IOUs concern,
DOE is adopting the specifications
regarding measurement of the
temperature registered by the freeze
protection ambient temperature sensor
as proposed in the September 2016
DPPP test procedure NOPR.
APSP and Hayward, in written
comments, recommended clarifying that
enforcement testing of freeze protection
is not applicable for units shipped with
the freeze protection disabled. (APSP,
No. 8 at p. 11; Hayward, No. 6 at p. 10)
In response, DOE clarifies that the
provisions are primarily intended to
verify that the default settings for
dedicated-purpose pool pumps shipped
with freeze protection control enabled
are within the thresholds recommended
by the DPPP Working Group. However,
DOE notes that the freeze protection
control enforcement test could also be
applied to dedicated-purpose pool
pumps shipped with freeze protection
control disabled to verify the fact that
the controls were, in fact, disabled. In
either case, any dedicated-purpose pool
pumps tested under the freeze
protection control enforcement test
provisions should not be altered from
their as-shipped settings. DOE is
clarifying, in this final rule, that
dedicated-purpose pool pumps must be
tested in the ‘‘as-shipped control
settings’’ when applying the freeze
protection control enforcement test.
DOE notes that the actual design
requirements would be established in
any ECS rulemaking for dedicatedpurpose pool pumps and that this
verification procedure would only be
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necessary if and when any such
requirements are established.
APSP and Hayward also
recommended clarifying that the
vertical lift and true priming time for
enforcement testing of the self-priming
capability test should be 6 minutes or
the manufacturers recommended prime
time, as permitted by NSF/ANSI 50–
2015. (APSP, No. 8 at p.11; Hayward,
No. 6 at p. 10)
In response, DOE acknowledges that,
as defined, self-priming pool filter
pumps that are certified with NSF/ANSI
50–2015 would have been tested based
on the criteria in NSF/ANSI 50–2015
that allow for some amount of
manufacturer discretion with regard to
the tested vertical lift and true priming
time. Specifically, NSF/ANSI 50–2015
allows a vertical lift of 5 feet or the
manufacturers specified lift, whichever
is greater, and a true priming time not
to exceed 6 minutes or the
manufacturers recommended time,
whichever is greater. However, DOE
notes that DOE’s self-priming capability
enforcement testing provisions are
fundamentally designed to evaluate the
self-priming capability of a pool filter
pump not certified to NSF/ANSI 50–
2015 as self-priming to verify the
appropriate equipment class is applied
to each DPPP model. As such, the
criteria adopted in the definitions of
self-priming and non-self-priming pool
filter pump (see section III.B.3.a) are
most applicable.
In addition, DOE notes that, as
discussed in the DPPP Working Group,
DOE’s specified criteria of a vertical lift
of 5.0 feet and true priming time of 10.0
minutes were meant to ensure that any
pump certified to NSF/ANSI 50–2015 as
a self-priming pump would inherently
meet DOE’s criteria for self-priming
pumps. That is, based on NSF/ANSI
criteria, any pump that was certified as
self-priming would have a vertical lift of
at least 5.0 feet, which would also
comply with DOE’s requirement.
Regarding the true priming time, as
NSF/ANSI 50–2015 allows for a true
priming time of 6 minutes or the
manufacturers specified time,
whichever is greater, it is possible that
a pump could be certified to NSF/ANSI
50–2015 with a priming time greater
than 10.0 minutes and still be qualified
as a self-priming pump. However, the
DPPP Working Group noted on several
occasions that the majority of existing
self-priming pool filter pumps have true
priming times less than 10.0 minutes.
(Docket No. EERE–2015–BT–STD–0008,
No. 95 at pp. 20–38, 110–113, and 119–
128; Docket No. EERE–2015–BT–STD–
0008, No. 79 at pp. 154–192) However,
DOE would only apply the self-priming
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capability enforcement test to pool filter
pumps that are not certified as selfpriming with NSF/ANSI 50–2015 and,
therefore, DOE’s requirements of 5.0 feet
and 10.0 minutes are the applicable
thresholds.
IV. Procedural Issues and Regulatory
Review
A. Review Under Executive Order 12866
The Office of Management and Budget
(OMB) has determined that test
procedure rulemakings do not constitute
‘‘significant regulatory actions’’ under
section 3(f) of Executive Order 12866,
Regulatory Planning and Review, 58 FR
51735 (Oct. 4, 1993). Accordingly, this
action was not subject to review under
the Executive Order by the Office of
Information and Regulatory Affairs
(OIRA) in the Office of Management and
Budget (OMB).
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B. Review Under the Regulatory
Flexibility Act
The Regulatory Flexibility Act (5
U.S.C. 601 et seq.) requires preparation
of a regulatory flexibility analysis for
any rule that by law must be proposed
for public comment, unless the agency
certifies that the rule, if promulgated,
will not have a significant economic
impact on a substantial number of small
entities. As required by Executive Order
13272, ‘‘Proper Consideration of Small
Entities in Agency Rulemaking,’’ 67 FR
53461 (August 16, 2002), DOE
published procedures and policies on
February 19, 2003 to ensure that the
potential impacts of its rules on small
entities are properly considered during
the DOE rulemaking process. 68 FR
7990. DOE has made its procedures and
policies available on the Office of the
General Counsel’s Web site: https://
energy.gov/gc/office-general-counsel.
DOE reviewed this final rule, which
establishes a new test procedure for
dedicated-purpose pool pumps, under
the provisions of the Regulatory
Flexibility Act and the procedures and
policies published on February 19,
2003. DOE concludes that this final rule
will not result in a significant impact on
a substantial number of small entities,
as it would not, in and of itself, require
the use of the adopted test procedure.
That is, any burden associated with
testing dedicated-purpose pool pumps
in accordance with the requirements of
this test procedure is accounted for in
the related January 2017 DPPP DFR, as
promulgation of energy conservation
standards is what ultimately requires
use of the adopted test procedure. 82 FR
5650, 5738–40. On this basis, DOE
certifies that this test procedure final
rule would not have a ‘‘significant
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economic impact on a substantial
number of small entities,’’ and the
preparation of a regulatory flexibility
analysis is not warranted. DOE will
transmit the certification and supporting
statement of factual basis to the Chief
Counsel for Advocacy of the Small
Business Administration (SBA) for
review under 5 U.S.C. 605(b).
1. Review of DPPP Manufacturers
As presented in the September 2016
DPPP test procedure NOPR, DOE
conducted a focused inquiry into
manufacturers of equipment covered by
this rulemaking. During its market
survey, DOE used available public
information to identify potential small
manufacturers. DOE’s research involved
the review of individual company Web
sites and marketing research tools (e.g.,
Dun and Bradstreet reports, Manta,
Hoovers) to create a list of companies
that manufacture pumps covered by this
rulemaking. Using these sources, DOE
identified 21 distinct manufacturers of
dedicated-purpose pool pumps. 81 FR
64580, 64637.
DOE notes that the Regulatory
Flexibility Act requires analysis of, in
particular, ‘‘small entities’’ that might be
affected by the rule. For the DPPP
manufacturing industry, the SBA has set
a size threshold, which defines those
entities classified as ‘‘small businesses’’
for the purpose of the statute. DOE used
the SBA’s size standards to determine
whether any small entities would be
required to comply with the rule. The
size standards are codified at 13 CFR
part 121. The standards are listed by
North American Industry Classification
System (NAICS) code and industry
description and are available at https://
www.sba.gov/sites/default/files/files/
Size_Standards_Table.pdf.
DPPP manufacturers are classified
under NAICS 333911, ‘‘Pump and
Pumping Equipment Manufacturing.’’
The SBA sets a threshold of 750
employees or less for an entity to be
considered as a small business for this
category. To determine the number of
DPPP manufacturers that are small
businesses and might be differentially
affected by the rule, DOE reviewed these
data to determine whether the entities
met the SBA’s definition of a small
business manufacturer of dedicatedpurpose pool pumps and then screened
out companies that do not offer
equipment covered by this rulemaking,
do not meet the definition of a ‘‘small
business,’’ are foreign-owned and
operated, or are owned by another
company. Based on this review, DOE
identified five companies that would be
considered small manufacturers by the
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36913
SBA definition in terms of the number
of employees.
DOE requested comment on this
estimate in the September 2016 DPPP
test procedure NOPR. 81 FR 64580,
64637 (Sept. 20, 2016). Hayward
commented that they had no means to
confirm the accuracy of this value.
(Hayward, No. 10 at pp. 10–11) Further
analysis of small businesses was
conducted as part of the Manufacturer
Impact Analysis discussed in the
January 2017 DPPP DFR. 82 FR 5650,
5726.
2. Burden of Conducting the DOE DPPP
Test Procedure
Although DOE maintains that this test
procedure has no incremental burden
associated with it when viewed as a
stand-alone rulemaking, DOE recognizes
that DPPP energy conservation
standards were adopted in the January
2017 DPPP DFR. 86 FR 5650, 5743.
Given the DPPP ECS rulemaking and the
potential testing manufacturers may
elect to undertake prior to July 19, 2021,
the compliance date of adopted
standards, DOE estimated the cost of
developing certified ratings for covered
DPPP models.
In the September 2016 DPPP test
procedure NOPR, DOE estimated the
cost to test and certify a DPPP basic
model, and the total certification cost
for each manufacturer, based on input
from manufacturers and independent
research. DOE estimated the cost for
both (a) testing units in house and (b)
testing units at a third-party testing
facility. Using the assumption that each
manufacturer rates 15 basic models on
average, DOE developed testing costs for
manufacturers that perform in-house
testing ranging from $1,000 to $1,350
per basic model. This included up to
$1,000 in capital costs, and up to $350
in labor costs to perform the DPPP tests
to comply with DOE’s testing
requirements. For testing units at third
party test labs, DOE estimated the cost
to be $11,000 per basic model. 81 FR
64580, 64635–64637 (Sept. 20, 2016).
In response to the September 2016
DPPP test procedure NOPR, APSP,
Hayward, and Pentair commented that
DOE’s estimated capital cost for inhouse testing is too low. APSP,
Hayward, Pentair, and Zodiac stated
that a manufacturer starting out should
expect to spend between $50,000 and
$100,000 for equipment suitable for
testing. (APSP, No. 8 at p. 11; Hayward,
No. 6 at p. 10; Pentair, No. 11, at p. 4;
Zodiac, No. 13 at p. 3) In addition,
Hayward, APSP, and Zodiac stated that
the estimated time to complete a test of
a DPPP basic model is between 12 and
14 hours. (APSP, No. 8 at p. 11;
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Hayward, No. 6 at p. 10; Zodiac, No. 13
at p. 3)
DOE notes that APSP, Hayward,
Pentair, and Zodiac did not provide
additional detail regarding the basis for
their estimates or why they are higher
than DOE’s estimates. However, DOE
recognizes that the assumptions in the
September 2016 DPPP test procedure
NOPR only accounted for the capital
cost of acquiring the necessary
equipment and did not account for the
additional labor associated with setting
up and commissioning any new testing
facility. DOE believes that, including the
additional labor estimates, a figure of
$50,000 to $100,000 may be appropriate.
Therefore, DOE has revised the worstcase burden estimate, which was
previously estimated as $43,800, using
the information provided by
manufacturers. Using the same
assumption from the September 2016
DPPP test procedure NOPR that each
manufacturer will rate 15 basic models
on average and the estimated capital
costs provided by Hayward, APSP,
Pentair, and Zodiac, the worst-case
burden estimate ranges from $3,333 to
$6,666 per basic model. In addition,
adjusting the testing time to 14 hours
and using a labor rate with fringe
benefits of $56.42 per hour,63 the total
labor costs are $790 per basic model. In
total, using estimates from Hayward,
APSP, Pentair, and Zodiac, the per basic
model testing costs range from $4,123 to
$7,456.
However, as discussed in the
September 2016 DPPP test procedure
NOPR, many DPPP manufacturers
already have existing testing capabilities
and likely would not incur the full
burden on constructing completely new
test facilities. Specifically, DOE
estimated a more representative burden
estimate of $15,000 for manufacturers
that may be required to acquire new
power measurement equipment and
power conditioning equipment to
comply with the proposed test
procedure requirements. However, DOE
noted that the costs could be as low as
$0. 81 FR 64580, 64635–64637 (Sept. 20,
2016). DOE notes that these
representative burden estimates are
consistent with the comments of APSP,
Hayward, and Pentair that many of the
requirements regarding test equipment
and test conditions adopted in the DOE
test procedure are consistent with (or
less stringent than) those already in use
in manufacturer’s test labs (see section
III.E.2.e and III.E.2.f). (APSP, No. 8 at p.
63 U.S. Department of Labor, Bureau of Labor
Statistics. 2015. Employer Costs for Employee
Compensation—Management, Professional, and
Related Employees. Washington, DC. www.bls.gov/
news.release/pdf/ecec.pdf.
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7; Hayward, No. 6 at pp. 7, 11; Pentair,
No. 11 at p. 4) In addition, in response
to comments from interested parties,
DOE is making several modifications in
this test procedure final rule to further
align testing requirements with existing
industry programs and, therefore,
reduce testing burden for manufacturers
(see section III.E.2, III.H, and III.K.1).
However, Pentair pointed out that
manufacturers may need to upgrade
capacity to certify all applicable DPPP
models in accordance with the
regulation. (Pentair, No. 11 at p. 4)
While DOE understands that
manufacturers may incur cost to certify
DPPP models in accordance with any
energy conservation standard that may
be set, there is no requirement to certify
any or all models associated with this
test procedure final rule. As such, DOE
is assessing the burden associated with
certifying DPPP models in accordance
with this test procedure and the impact
on manufacturers in the Manufacturer
Impact Analysis in the associated
energy conservation standard (Docket
No. EERE–2015–BT–STD–0008).
Specifically, in the Manufacturer Impact
Analysis in the energy conservation
standard, DOE is including the highest
cost per basic model testing cost
estimate to prevent underestimating
testing burden to the industry. DOE
determined that the per basic model test
cost at third-party test labs ($11,000 per
model, as estimated in the September
2016 DPPP test procedure NOPR) is
greater than the per basic model test
cost estimate from Hayward, Pentair,
and APSP. Therefore, in the ECS
Manufacturer Impact Assessment, DOE
assumes that all manufacturers test 15
basic models at third-party test labs at
a cost of $11,000 per basic model.
In the September 2016 DPPP test
procedure NOPR, DOE also estimated
that manufacturers incur testing burden
every time a new basic model is
introduced. DOE estimated that
manufacturers introduce or significantly
modify the basic model every 5 years.
Pentair APSP, and Zodiac responded
that significant changes in basic models
are not common and the 5 year estimate
is low. APSP commented that 5 years is
the minimum time for a manufacturer to
make changes to basic models, but it
could be as much as 10 years. (Pentair,
No. 11 at p. 4; APSP, No. 8 at p. 12;
Zodiac, No. 13 at p. 3) DOE appreciates
the comments from the interested
parties and concludes that, based on the
updated testing time of 14 hours
discussed previously, ongoing testing
costs would be approximately $790 per
manufacturer to certify new models.
However, DOE reiterates that this cost
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would not be required until the
compliance date of any energy
conservation standard that may be
adopted for such equipment.
C. Review Under the Paperwork
Reduction Act of 1995
All collections of information from
the public by a Federal agency must
receive prior approval from OMB. DOE
has established regulations for the
certification and recordkeeping
requirements for covered consumer
products and industrial equipment. 10
CFR part 429, subpart B. In an
application to renew the OMB
information collection approval for
DOE’s certification and recordkeeping
requirements filed in January 2015, DOE
included an estimated burden for
manufacturers of pumps in case DOE
ultimately sets energy conservation
standards for this equipment, and OMB
approved the revised information
collection for DOE’s certification and
recordkeeping requirements. 80 FR 5099
(Jan. 30, 2015). In the January 2016
general pumps ECS final rule, DOE
established energy conservation
standards and reporting requirements
for certain categories of pumps and
estimated that public reporting burden
for the certification for pumps, similar
to other covered consumer products and
commercial equipment, would average
30 hours per response, including the
time for reviewing instructions,
searching existing data sources,
gathering and maintaining the data
needed, and completing and reviewing
the collection of information. 81 FR
4368, 4428 (Jan. 26, 2016). As
dedicated-purpose pool pumps are a
specific style of pump and the testing
and certification requirements adopted
in this final rule are similar to those
established for general pumps in the
January 2016 general pumps test
procedure final rule, DOE believes that
the estimated reporting burden of 30
hours would also be applicable for
dedicated-purpose pool pumps. 81 FR
4086 (Jan. 25, 2016). DOE notes that,
although this test procedure rulemaking
discusses recordkeeping requirements
that are associated with executing and
maintaining the test data for this
equipment (see section III.K.1),
certification requirements would not
need to be performed until July 19,
2021, the compliance date of adopted
energy conservation standards for
dedicated-purpose pool pumps.
Notwithstanding any other provision
of the law, no person is required to
respond to, nor shall any person be
subject to a penalty for failure to comply
with, a collection of information subject
to the requirements of the PRA, unless
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that collection of information displays a
currently valid OMB Control Number.
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D. Review Under the National
Environmental Policy Act of 1969
In this final rule, DOE is adopting
new definitions; a new test procedure;
and new certification, enforcement, and
labeling requirements for dedicatedpurpose pool pumps. DOE has
determined that this rule falls into a
class of actions that are categorically
excluded from review under the
National Environmental Policy Act of
1969 (42 U.S.C. 4321 et seq.) and DOE’s
implementing regulations at 10 CFR part
1021. Specifically, this rule considers a
test procedure for dedicated-purpose
pool pumps that is largely based upon
industry test procedures and
methodologies resulting from a
negotiated rulemaking without affecting
the amount, quality, or distribution of
energy usage, and, therefore, will not
result in any environmental impacts.
Thus, this rulemaking is covered by
Categorical Exclusion A5 under 10 CFR
part 1021, subpart D, which applies to
any rulemaking that interprets or
amends an existing rule without
changing the environmental effect of
that rule. Accordingly, neither an
environmental assessment nor an
environmental impact statement is
required.
E. Review Under Executive Order 13132
Executive Order 13132, ‘‘Federalism,’’
64 FR 43255 (August 4, 1999), imposes
certain requirements on agencies
formulating and implementing policies
or regulations that preempt State law or
that have Federalism implications. The
Executive Order requires agencies to
examine the constitutional and statutory
authority supporting any action that
would limit the policymaking discretion
of the States and to carefully assess the
necessity for such actions. The
Executive Order also requires agencies
to have an accountable process to
ensure meaningful and timely input by
State and local officials in the
development of regulatory policies that
have Federalism implications. On
March 14, 2000, DOE published a
statement of policy describing the
intergovernmental consultation process
it will follow in the development of
such regulations. 65 FR 13735. DOE
examined this final rule and determined
that it will not have a substantial direct
effect on the States, on the relationship
between the national government and
the States, or on the distribution of
power and responsibilities among the
various levels of government. EPCA
governs and prescribes Federal
preemption of State regulations as to
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energy conservation for the products
that are the subject of this final rule.
States can petition DOE for exemption
from such preemption to the extent, and
based on criteria, set forth in EPCA. (42
U.S.C. 6297(d)) No further action is
required by Executive Order 13132.
F. Review Under Executive Order 12988
Regarding the review of existing
regulations and the promulgation of
new regulations, section 3(a) of
Executive Order 12988, ‘‘Civil Justice
Reform,’’ 61 FR 4729 (Feb. 7, 1996),
imposes on Federal agencies the general
duty to adhere to the following
requirements: (1) Eliminate drafting
errors and ambiguity; (2) write
regulations to minimize litigation; (3)
provide a clear legal standard for
affected conduct rather than a general
standard; and (4) promote simplification
and burden reduction. Section 3(b) of
Executive Order 12988 specifically
requires that Executive agencies make
every reasonable effort to ensure that the
regulation (1) clearly specifies the
preemptive effect, if any; (2) clearly
specifies any effect on existing Federal
law or regulation; (3) provides a clear
legal standard for affected conduct
while promoting simplification and
burden reduction; (4) specifies the
retroactive effect, if any; (5) adequately
defines key terms; and (6) addresses
other important issues affecting clarity
and general draftsmanship under any
guidelines issued by the Attorney
General. Section 3(c) of Executive Order
12988 requires Executive agencies to
review regulations in light of applicable
standards in sections 3(a) and 3(b) to
determine whether they are met or it is
unreasonable to meet one or more of
them. DOE has completed the required
review and determined that, to the
extent permitted by law, this final rule
meets the relevant standards of
Executive Order 12988.
G. Review Under the Unfunded
Mandates Reform Act of 1995
Title II of the Unfunded Mandates
Reform Act of 1995 (UMRA) requires
each Federal agency to assess the effects
of Federal regulatory actions on State,
local, and Tribal governments and the
private sector. Public Law 104–4, sec.
201 (codified at 2 U.S.C. 1531). For a
regulatory action resulting in a rule that
may cause the expenditure by State,
local, and Tribal governments, in the
aggregate, or by the private sector of
$100 million or more in any one year
(adjusted annually for inflation), section
202 of UMRA requires a Federal agency
to publish a written statement that
estimates the resulting costs, benefits,
and other effects on the national
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36915
economy. (2 U.S.C. 1532(a), (b)) The
UMRA also requires a Federal agency to
develop an effective process to permit
timely input by elected officers of State,
local, and Tribal governments on a
proposed ‘‘significant intergovernmental
mandate,’’ and requires an agency plan
for giving notice and opportunity for
timely input to potentially affected
small governments before establishing
any requirements that might
significantly or uniquely affect small
governments. On March 18, 1997, DOE
published a statement of policy on its
process for intergovernmental
consultation under UMRA. 62 FR
12820; also available at https://
energy.gov/gc/office-general-counsel.
DOE examined this final rule according
to UMRA and its statement of policy
and determined that the rule contains
neither an intergovernmental mandate,
nor a mandate that may result in the
expenditure of $100 million or more in
any year, so these requirements do not
apply.
H. Review Under the Treasury and
General Government Appropriations
Act, 1999
Section 654 of the Treasury and
General Government Appropriations
Act, 1999 (Pub. L. 105–277) requires
Federal agencies to issue a Family
Policymaking Assessment for any rule
that may affect family well-being. This
final rule will not have any impact on
the autonomy or integrity of the family
as an institution. Accordingly, DOE has
concluded that it is not necessary to
prepare a Family Policymaking
Assessment.
I. Review Under Executive Order 12630
DOE has determined, under Executive
Order 12630, ‘‘Governmental Actions
and Interference with Constitutionally
Protected Property Rights,’’ 53 FR 8859
(March 18, 1988), that this regulation
will not result in any takings that might
require compensation under the Fifth
Amendment to the U.S. Constitution.
J. Review Under Treasury and General
Government Appropriations Act, 2001
Section 515 of the Treasury and
General Government Appropriations
Act, 2001 (44 U.S.C. 3516 note) provides
for agencies to review most
disseminations of information to the
public under guidelines established by
each agency pursuant to general
guidelines issued by OMB. OMB’s
guidelines were published at 67 FR
8452 (Feb. 22, 2002), and DOE’s
guidelines were published at 67 FR
62446 (Oct. 7, 2002). DOE has reviewed
this final rule under the OMB and DOE
guidelines and has concluded that it is
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consistent with applicable policies in
those guidelines.
K. Review Under Executive Order 13211
Executive Order 13211, ‘‘Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use,’’ 66 FR 28355 (May
22, 2001), requires Federal agencies to
prepare and submit to OMB, a
Statement of Energy Effects for any
significant energy action. A ‘‘significant
energy action’’ is defined as any action
by an agency that promulgated or is
expected to lead to promulgation of a
final rule, and that (1) is a significant
regulatory action under Executive Order
12866, or any successor order; and (2)
is likely to have a significant adverse
effect on the supply, distribution, or use
of energy; or (3) is designated by the
Administrator of OIRA as a significant
energy action. For any significant energy
action, the agency must give a detailed
statement of any adverse effects on
energy supply, distribution, or use if the
regulation is implemented, and of
reasonable alternatives to the action and
their expected benefits on energy
supply, distribution, and use.
This regulatory action is not a
significant regulatory action under
Executive Order 12866. Moreover, it
would not have a significant adverse
effect on the supply, distribution, or use
of energy, nor has it been designated as
a significant energy action by the
Administrator of OIRA. Therefore, it is
not a significant energy action, and,
accordingly, DOE has not prepared a
Statement of Energy Effects.
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L. Review Under Section 32 of the
Federal Energy Administration Act of
1974
Under section 301 of the Department
of Energy Organization Act (Pub. L. 95–
91; 42 U.S.C. 7101), DOE must comply
with section 32 of the Federal Energy
Administration Act of 1974, as amended
by the Federal Energy Administration
Authorization Act of 1977. (15 U.S.C.
788; FEAA) Section 32 essentially
provides in relevant part that, where a
proposed rule authorizes or requires use
of commercial standards, the NOPR
must inform the public of the use and
background of such standards. In
addition, section 32(c) requires DOE to
consult with the Attorney General and
the Chairman of the Federal Trade
Commission (FTC) concerning the
impact of the commercial or industry
standards on competition.
The modifications to the test
procedure for dedicated-purpose pool
pumps adopted in this final rule
incorporates testing methods contained
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in certain sections of the following
commercial standards:
(1) UL 1081, (‘‘ANSI/UL 1081–2016’’),
‘‘Standard for Swimming Pool Pumps,
Filters, and Chlorinators,’’ 7th Edition,
ANSI approved October 21, 2016.
(2) Canadian Standards Association
(CSA) C747–2009 (Reaffirmed 2014),
‘‘Energy Efficiency Test Methods for
Small Motors,’’ CSA reaffirmed 2014,
section 1, ‘‘Scope’’; section 3,
‘‘Definitions’’; section 5, ‘‘General Test
Requirements’’; and section 6, ‘‘Test
Method.’’
(3) Institute of Electrical and
Electronics Engineers (IEEE) Standard
114–2010, ‘‘Test Procedure for SinglePhase Induction Motors,’’ Approved
September 30, 2010, section 3.2, ‘‘Tests
with load’’; section 4 ‘‘Testing
facilities’’; section 5.2 ‘‘Mechanical
measurements’’; section 5.3
‘‘Temperature measurements’’; and
section 6 ‘‘Tests.’’
(4) Institute of Electrical and
Electronics Engineers (IEEE) Standard
113–1985, ‘‘IEEE Guide: Test Procedures
for Direct-Current Machines,’’ 1985,
section 3.1, ‘‘Instrument Selection
Factors’’; section 3.4 ‘‘Power
Measurement’’: section 3.5 ‘‘Power
Sources’’; section 4.1.2 ‘‘Ambient Air’’;
section 4.1.4 ‘‘Direction of Rotation’’;
section 5.4.1 ‘‘Reference Conditions’’;
and section 5.4.3.2 ‘‘Dynomometer or
Torquemeter Method.’’
(5) NSF International Standard (NSF)/
American National Standards Institute
(ANSI) 50–2015, (‘‘NSF/ANSI 50–
2015’’), ‘‘Equipment for Swimming
Pools, Spas, Hot Tubs and Other
Recreational Water Facilities,’’ approved
January 26, 2015, section C.3, ‘‘selfpriming capability,’’ of Annex C, ‘‘Test
methods for the evaluation of
centrifugal pumps.’’
In addition, the rule expands the
incorporation by reference of Hydraulic
Institute (HI) 40.6–2014, (‘‘HI 40.6–
2014’’) ‘‘Methods for Rotodynamic
Pump Efficiency Testing,’’ (except for
section 40.6.4.1, ‘‘Vertically suspended
pumps‘‘; section 40.6.4.2, ‘‘Submersible
pumps’’; section 40.6.5.3, ‘‘Test report’’;
section 40.6.5.5, ‘‘Test conditions’’;
section 40.6.5.5.2, ‘‘Speed of rotation
during testing’’; section 40.6.6.1,
‘‘Translation of test results to rated
speed of rotation’’; Appendix A, section
A.7, ‘‘Testing at temperatures exceeding
30 °C (86 °F)’’; and Appendix B,
‘‘Reporting of test results (normative)’’;)
copyright 2014. HI 40.6–2014 is already
IBR approved for § 431.464, and
appendix A to subpart Y of part 431. 10
CFR 431.463. As such, DOE is only
modifying the existing incorporation by
reference to extend the applicability of
certain sections to the new appendices
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B and C to subpart Y that will contain
the DPPP test procedure.
Although the DPPP test procedure is
not exclusively based on these industry
testing standards, some components of
the test procedure will adopt
definitions, test parameters,
measurement techniques, and
additional calculations from them
without amendment. DOE has evaluated
these standards and is unable to
conclude whether it fully complies with
the requirements of section 32(b) of the
FEAA (i.e., whether it was developed in
a manner that fully provides for public
participation, comment, and review).
DOE has consulted with both the
Attorney General and the Chairman of
the FTC about the impact on
competition of using the methods
contained in these standards and has
received no comments objecting to their
use.
M. Congressional Notification
As required by 5 U.S.C. 801, DOE will
report to Congress on the promulgation
of this rule before its effective date. The
report will state that it has been
determined that the rule is not a ‘‘major
rule’’ as defined by 5 U.S.C. 804(2).
N. Description of Materials Incorporated
by Reference
In this final rule, DOE incorporates by
reference six industry standards related
to pump nomenclature, definitions, and
test specifications, which DOE has
referenced in its proposed definitions
and test procedure.
Specifically, the definitions in this
final rule, as well as relevant testing
procedures to determine self-priming
capability, incorporate by reference the
following sections of the following
standards:
(1) UL 1081, (‘‘ANSI/UL 1081–2016’’),
‘‘Standard for Swimming Pool Pumps,
Filters, and Chlorinators,’’ 7th Edition,
ANSI approved October 21, 2016.
(2) Canadian Standards Association
(CSA) C747–2009 (Reaffirmed 2014),
‘‘Energy Efficiency Test Methods for
Small Motors,’’ CSA reaffirmed 2014,
section 1, ‘‘Scope’’; section 3,
‘‘Definitions’’; section 5, ‘‘General Test
Requirements’’; and section 6, ‘‘Test
Method.’’
(3) Institute of Electrical and
Electronics Engineers (IEEE) Standard
114–2010, ‘‘Test Procedure for SinglePhase Induction Motors,’’ Approved
September 30, 2010, section 3.2, ‘‘Tests
with load’’; section 4 ‘‘Testing
facilities’’; section 5.2 ‘‘Mechanical
measurements’’; section 5.3
‘‘Temperature measurements’’; and
section 6 ‘‘Tests.’’
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(4) Institute of Electrical and
Electronics Engineers (IEEE) Standard
113–1985, ‘‘IEEE Guide: Test Procedures
for Direct-Current Machines,’’ 1985,
section 3.1, ‘‘Instrument Selection
Factors’’; section 3.4 ‘‘Power
Measurement’’: section 3.5 ‘‘Power
Sources’’; section 4.1.2 ‘‘Ambient Air’’;
section 4.1.4 ‘‘Direction of Rotation’’;
section 5.4.1 ‘‘Reference Conditions’’;
and section 5.4.3.2 ‘‘Dynomometer or
Torquemeter Method.’’
(5) NSF International Standard (NSF)/
American National Standards Institute
(ANSI) 50–2015, (‘‘NSF/ANSI 50–
2015’’), ‘‘Equipment for Swimming
Pools, Spas, Hot Tubs and Other
Recreational Water Facilities,’’ approved
January 26, 2015, section C.3, ‘‘selfpriming capability,’’ of Annex C, ‘‘Test
methods for the evaluation of
centrifugal pumps.’’
(6) Hydraulic Institute (HI) 40.6–2014,
(‘‘HI 40.6–2014–B’’) ‘‘Methods for
Rotodynamic Pump Efficiency Testing,’’
(except for section 40.6.4.1, ‘‘Vertically
suspended pumps’’; section 40.6.4.2,
‘‘Submersible pumps’’; section 40.6.5.3,
‘‘Test report’’; section 40.6.5.5, ‘‘Test
conditions’’; section 40.6.5.5.2, ‘‘Speed
of rotation during testing’’; section
40.6.6.1, ‘‘Translation of test results to
rated speed of rotation’’; Appendix A,
section A.7, ‘‘Testing at temperatures
exceeding 30 °C (86 °F)’’; and Appendix
B, ‘‘Reporting of test results
(normative)’’;) to establish procedures
for measuring relevant pump
performance parameters.
DOE incorporates by reference UL
1081–2016 into 10 CFR 431.462 and
NSF/ANSI 50–2015 into 10 CFR 429.59,
10 CFR 429.134, 10 CFR 431.462, and
appendices B and C of subpart Y. UL
1081–2016 describes, among other
things, the safety-related performance
and construction requirements for rating
dedicated-purpose pool pumps under
the UL 1081 standard. Section C.3 of
annex C of the NSF/ANSI 50–2015
standard describes the test methods and
criteria for establishing the self-priming
capability of dedicated-purpose pool
pumps.
DOE incorporates by reference CSA
C747–2009 (RA 2014) into appendices B
and C of part 431 to describe the
standardized methods for determining
certain DPPP motor horsepower
characteristics. CSA C747–2009 (RA
2014) contains standardized methods
for evaluating and categorizing AC and
DC electric motors that are
internationally recognized and are
harmonized with IEEE 114–2010 and
IEEE 113–1985.
DOE also incorporates by reference
IEEE 114–2010 into appendices B and C
of part 431 to describe the standardized
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methods for determining certain DPPP
motor horsepower characteristics for
dedicated-purpose pool pumps with
single-phase AC motors. IEEE 114–2010
contains standardized methods for
evaluating and categorizing single-phase
induction motors. These methods are
consistent with those in CSA C742–
2009 (RA 2014).
DOE also incorporates by reference
IEEE 113–1985 into appendices B and C
of part 431 to describe the standardized
methods for determining certain DPPP
motor horsepower characteristics for
dedicated-purpose pool pumps with DC
motors. IEEE 113–1985 contains
standardized methods for evaluating
and categorizing DC motors. These
methods are consistent with those in
CSA C742–2009 (RA 2014).
In addition, the test procedure
adopted in this final rule incorporates
by reference the Hydraulic Institute (HI)
40.6–2014, (‘‘HI 40.6–2014–B’’)
‘‘Methods for Rotodynamic Pump
Efficiency Testing,’’ (except for section
40.6.4.1, ‘‘Vertically suspended
pumps’’; section 40.6.4.2, ‘‘Submersible
pumps’’; section 40.6.5.3, ‘‘Test report’’;
section 40.6.5.5, ‘‘Test conditions’’;
section 40.6.5.5.2, ‘‘Speed of rotation
during testing’’; section 40.6.6.1,
‘‘Translation of test results to rated
speed of rotation’’; Appendix A, section
A.7, ‘‘Testing at temperatures exceeding
30 °C (86 °F)’’; and Appendix B,
‘‘Reporting of test results (normative)’’;)
to establish procedures for measuring
relevant pump performance parameters.
HI 40.6–2014–B, with certain
exceptions, is already IBR approved for
appendix A to subpart Y of part 431. 10
CFR 431.463. DOE proposes to
incorporate by reference HI 40.6–2014–
B, with certain additional exceptions,
into the new appendices B and C to
subpart Y that would contain the DPPP
test procedure, as well as 10 CFR
429.134 to support DOE’s enforcement
testing. HI 40.6–2014–B is an industryaccepted standard used to specify
methods of testing for determining the
head, flow rate, pump power input,
driver power input, pump power
output, and other relevant parameters
necessary to determine the WEF of
applicable pumps, as well as other
voluntary metrics, adopted in this final
rule (see sections III.C and III.H).
Additionally, these standards can be
obtained from the organizations directly
at the following addresses:
(1) UL, 333 Pfingsten Road,
Northbrook, IL 60062, (847) 272–8800,
or by visiting https://ul.com.
(2) CSA, 5060 Spectrum Way, Suite
100, Mississauga, Ontario, L4W 5N6,
Canada, (800) 463–6727, or by visiting
www.csagroup.org.
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(3) IEEE, 45 Hoes Lane, P.O. Box
1331, Piscataway, NJ 08855–1331, (732)
981–0060, or by visiting https://
www.ieee.org.
(4) NSF International, 789 N. Dixboro
Road, Ann Arbor, MI 48105, (743) 769–
8010, or by visiting www.nsf.org.
(5) Hydraulic Institute, located at 6
Campus Drive, First Floor North,
Parsippany, NJ, 07054, (973) 267–9700,
or by visiting www.pumps.org.
V. Approval of the Office of the
Secretary
The Secretary of Energy has approved
publication of this final rule.
List of Subjects
10 CFR Part 429
Administrative practice and
procedure, Confidential business
information, Energy conservation,
Imports, Incorporation by reference,
Intergovernmental relations, Small
businesses.
10 CFR Part 431
Administrative practice and
procedure, Confidential business
information, Energy conservation,
Imports, Incorporation by reference,
Intergovernmental relations, Small
businesses.
Issued in Washington, DC, on December
22, 2016.
Kathleen B. Hogan,
Deputy Assistant Secretary for Energy
Efficiency, Energy Efficiency and Renewable
Energy.
For the reasons stated in the
preamble, DOE amends parts 429 and
431 of chapter II, subchapter D of title
10, Code of Federal Regulations as set
forth below:
PART 429—CERTIFICATION,
COMPLIANCE, AND ENFORCEMENT
FOR CONSUMER PRODUCTS AND
COMMERCIAL AND INDUSTRIAL
EQUIPMENT
1. The authority citation for part 429
continues to read as follows:
■
Authority: 42 U.S.C. 6291–6317; 28 U.S.C.
2461 note.
2. Section 429.4 is amended by:
a. Redesignating paragraph (d) as (e);
and
■ b. Adding new paragraphs (d) and (f).
The additions read as follows:
■
■
§ 429.4 Materials incorporated by
reference.
*
*
*
*
*
(d) HI. Hydraulic Institute, 6 Campus
Drive, First Floor North, Parsippany, NJ
07054–4406, 973–267–9700.
www.Pumps.org.
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(1) HI 40.6–2014, (‘‘HI 40.6–2014–B’’),
‘‘Methods for Rotodynamic Pump
Efficiency Testing,’’, (except for sections
40.6.4.1 ‘‘Vertically suspended pumps’’,
40.6.4.2 ‘‘Submersible pumps’’,40.6.5.3
‘‘Test report’’, 40.6.5.5 ‘‘Test
conditions’’, 40.6.5.5.2 ‘‘Speed of
rotation during testing’’, and 40.6.6.1
‘‘Translation of test results to rated
speed of rotation’’, and Appendix A
‘‘Testing arrangements (normative)’’:
A.7 ‘‘Testing at temperatures exceeding
30 °C (86 °F)’’, and Appendix B
‘‘Reporting of test results (normative)’’),
copyright 2014, IBR approved for
§ 429.134.
(2) [Reserved]
*
*
*
*
*
(f) NSF. NSF International. 789 N.
Dixboro Road, Ann Arbor, MI 48105,
(743) 769–8010. www.nsf.org.
(1) NSF/ANSI 50–2015, ‘‘Equipment
for Swimming Pools, Spas, Hot Tubs
and Other Recreational Water
Facilities,’’ Annex C—‘‘Test methods for
the evaluation of centrifugal pumps,’’
Section C.3, ‘‘self-priming capability,’’
ANSI approved January 26, 2015, IBR
approved for §§ 429.59 and 429.134.
(2) [Reserved]
■ 3. Section 429.59 is amended by:
■ a. Revising paragraph (a)(1)(ii);
■ b. Adding paragraphs (a)(2), (b)(2)(iv)
and (v), and (b)(3)(iv); and
■ c. Revising paragraph (c).
The revisions and additions read as
follows:
§ 429.59
Pumps.
(a) * * *
(1) * * *
(ii) Any representation of weighted
energy factor of a basic model must be
less than or equal to the lower of:
(A) The mean of the sample, where:
¯
And x is the sample mean; n is the
number of samples; and xi is the
maximum of the ith sample; or,
¯
And x is the sample mean; s is the
sample standard deviation; n is the
number of samples; and t0.95 is the t
statistic for a 95 percent one-tailed
confidence interval with n-1 degrees of
freedom (from appendix A of this
subpart).
(2) Other representations—(i) Rated
hydraulic horsepower. The
representative value of rated hydraulic
horsepower of a basic model of
dedicated-purpose pool pump must be
the mean of the rated hydraulic
horsepower for each tested unit.
(ii) Dedicated-purpose pool pump
motor total horsepower. The
representative value of dedicatedpurpose pool pump motor total
horsepower of a basic model of
dedicated-purpose pool pump must be
the mean of the dedicated-purpose pool
pump motor total horsepower for each
tested unit.
(iii) True power factor (PFi). The
representative value of true power factor
at each load point i of a basic model of
dedicated-purpose pool pump must be
the mean of the true power factors at
that load point for each tested unit of
dedicated-purpose pool pump.
(b) * * *
(2) * * *
(iv) For a dedicated-purpose pool
pump subject to the test methods
prescribed in § 431.464(b) of this
chapter: weighted energy factor (WEF)
in kilogallons per kilowatt-hour (kgal/
kWh); rated hydraulic horsepower in
horsepower (hp); the speed
configuration for which the pump is
being rated (i.e., single-speed, twospeed, multi-speed, or variable-speed);
true power factor at all applicable test
procedure load points i (dimensionless),
as specified in Table 1 of appendix B or
Individual model number(s)
Basic model number
Number unique to the basic model ..........
Number unique to the basic model ..........
Number unique to the basic model ..........
(2) Or must otherwise provide
sufficient information to identify the
specific driver model and/or controls
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2
Bare pump .........
Bare pump .........
Bare pump .........
N/A ....................
Driver .................
Driver .................
model(s) with which a bare pump is
distributed.
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3
N/A.
N/A.
Controls.
4. Section 429.110 is amended by
revising paragraphs (e)(1) and (5) to read
as follows:
■
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ER07AU17.009
Bare pump ................................................
Bare pump with driver ..............................
Bare pump with driver and controls .........
1
ER07AU17.008
Equipment configuration
(as distributed in commerce)
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C to subpart Y of part 431 of this
chapter, as applicable; dedicatedpurpose pool pump nominal motor
horsepower in horsepower (hp);
dedicated-purpose pool pump motor
total horsepower in horsepower (hp);
dedicated-purpose pool pump service
factor (dimensionless); for self-priming
pool filter pumps, non-self-priming pool
filter pumps, and waterfall pumps: The
maximum head (in feet) which is based
on the mean of the units in the tested
sample; a statement regarding whether
freeze protection is shipped enabled or
disabled; for dedicated-purpose pool
pumps distributed in commerce with
freeze protection controls enabled: The
default dry-bulb air temperature setting
(in °F), default run time setting (in
minutes), and default motor speed (in
rpm); for self-priming pool filter pumps
a statement regarding whether the pump
is certified with NSF/ANSI 50–2015
(incorporated by reference, see § 429.4)
as self-priming; and, for self-priming
pool filter pumps that are not certified
with NSF/ANSI 50–2015 as selfpriming: The vertical lift (in feet) and
true priming time (in minutes) for the
DPPP model.
(v) For integral cartridge-filter and
sand-filter pool pumps, the maximum
run-time (in hours) of the pool pump
control with which the integral
cartridge-filter or sand-filter pump is
distributed in commerce.
(3) * * *
(iv) For a dedicated-purpose pool
pump subject to the test methods
prescribed in § 431.464(b) of this
chapter: Calculated driver power input
and flow rate at each load point i (Pi and
Qi), in horsepower (hp) and gallons per
minute (gpm), respectively.
*
*
*
*
*
(c) Individual model numbers. (1) For
a pump subject to the test methods
prescribed in appendix A to subpart Y
of part 431 of this chapter, each
individual model number required to be
reported pursuant to § 429.12(b)(6) must
consist of the following:
(B) The lower 95 percent confidence
limit (LCL) of the true mean divided by
0.95, where:
Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
§ 429.110
Enforcement testing.
*
*
*
*
*
(e) * * *
(1) For products with applicable
energy conservation standard(s) in
§ 430.32 of this chapter, and commercial
prerinse spray valves, illuminated exit
signs, traffic signal modules and
pedestrian modules, commercial clothes
washers, dedicated-purpose pool
pumps, and metal halide lamp ballasts,
DOE will use a sample size of not more
than 21 units and follow the sampling
plans in appendix A of this subpart
(Sampling for Enforcement Testing of
Covered Consumer Products and Certain
High-Volume Commercial Equipment).
*
*
*
*
*
(5) For pumps subject to the standards
specified in § 431.465(a) of this chapter,
DOE will use an initial sample size of
not more than four units and will
determine compliance based on the
arithmetic mean of the sample.
*
*
*
*
*
■ 5. Section 429.134 is amended by
revising paragraph (i) to read as follows:
§ 429.134 Product-specific enforcement
provisions.
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*
*
*
*
*
(i) Pumps—(1) General purpose
pumps. (i) The volume rate of flow (flow
rate) at BEP and nominal speed of
rotation of each tested unit of the basic
model will be measured pursuant to the
test requirements of § 431.464 of this
chapter, where the value of volume rate
of flow (flow rate) at BEP and nominal
speed of rotation certified by the
manufacturer will be treated as the
expected BEP flow rate. The results of
the measurement(s) will be compared to
the value of volume rate of flow (flow
rate) at BEP and nominal speed of
rotation certified by the manufacturer.
The certified volume rate of flow (flow
rate) at BEP and nominal speed of
rotation will be considered valid only if
the measurement(s) (either the
measured volume rate of flow (flow rate)
at BEP and nominal speed of rotation for
a single unit sample or the average of
the measured flow rates for a multiple
unit sample) is within five percent of
the certified volume rate of flow (flow
rate) at BEP and nominal speed of
rotation.
(A) If the representative value of
volume rate of flow (flow rate) at BEP
and nominal speed of rotation is found
to be valid, the measured volume rate of
flow (flow rate) at BEP and nominal
speed of rotation will be used in
subsequent calculations of constant load
pump energy rating (PERCL) and
constant load pump energy index
(PEICL) or variable load pump energy
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rating (PERVL) and variable load pump
energy index (PEIVL) for that basic
model.
(B) If the representative value of
volume rate of flow (flow rate) at BEP
and nominal speed of rotation is found
to be invalid, the mean of all the
measured volume rate of flow (flow rate)
at BEP and nominal speed of rotation
values determined from the tested
unit(s) will serve as the new expected
BEP flow rate and the unit(s) will be
retested until such time as the measured
rate of flow (flow rate) at BEP and
nominal speed of rotation is within 5
percent of the expected BEP flow rate.
(ii) DOE will test each pump unit
according to the test method specified
by the manufacturer in the certification
report submitted pursuant to
§ 429.59(b).
(2) Dedicated-purpose pool pumps. (i)
The rated hydraulic horsepower of each
tested unit of the basic model of
dedicated-purpose pool pump will be
measured pursuant to the test
requirements of § 431.464(b) of this
chapter and the result of the
measurement(s) will be compared to the
value of rated hydraulic horsepower
certified by the manufacturer. The
certified rated hydraulic horsepower
will be considered valid only if the
measurement(s) (either the measured
rated hydraulic horsepower for a single
unit sample or the average of the
measured rated hydraulic horsepower
values for a multiple unit sample) is
within 5 percent of the certified rated
hydraulic horsepower.
(A) If the representative value of rated
hydraulic horsepower is found to be
valid, the value of rated hydraulic
horsepower certified by the
manufacturer will be used to determine
the standard level for that basic model.
(B) If the representative value of rated
hydraulic horsepower is found to be
invalid, the mean of all the measured
rated hydraulic horsepower values
determined from the tested unit(s) will
be used to determine the standard level
for that basic model.
(ii) To verify the self-priming
capability of non-self-priming pool filter
pumps and of self-priming pool filter
pumps that are not certified with NSF/
ANSI 50–2015 (incorporated by
reference, see § 429.4) as self-priming,
the vertical lift and true priming time of
each tested unit of the basic model of
self-priming or non-self-priming pool
filter pump will be measured pursuant
to the test requirements of § 431.464(b)
of this chapter.
(A) For self-priming pool filter pumps
that are not certified with NSF/ANSI
50–2015 as self-priming, at a vertical lift
of 5.0 feet, the result of the true priming
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36919
time measurement(s) will be compared
to the value of true priming time
certified by the manufacturer. The
certified value of true priming time will
be considered valid only if the
measurement(s) (either the measured
true priming time for a single unit
sample or the average of true priming
time values for a multiple unit sample)
is within 5 percent of the certified value
of true priming time.
(1) If the representative value of true
priming time is found to be valid, the
value of true priming time certified by
the manufacturer will be used to
determine the appropriate equipment
class and standard level for that basic
model.
(2) If the representative value of true
priming time is found to be invalid, the
mean of the values of true priming time
determined from the tested unit(s) will
be used to determine the appropriate
equipment class and standard level for
that basic model.
(B) For non-self-priming pool filter
pumps, at a vertical lift of 5.0 feet, the
result of the true priming time
measurement(s) (either the measured
true priming time for a single unit
sample or the average of true priming
time values, for a multiple unit sample)
will be compared to the value of true
priming time referenced in the
definition of non-self-priming pool filter
pump at § 431.462 (10.0 minutes).
(1) If the measurement(s) of true
priming time are greater than 95 percent
of the value of true priming time
referenced in the definition of non-selfpriming pool filter pump at § 431.462
with a vertical lift of 5.0 feet, the DPPP
model will be considered a non-selfpriming pool filter pump for the
purposes of determining the appropriate
equipment class and standard level for
that basic model.
(2) If the conditions specified in
paragraph (i)(2)(ii)(B)(1) of this section
are not satisfied, then the DPPP model
will be considered a self-priming pool
filter pump for the purposes of
determining the appropriate equipment
class and standard level for that basic
model.
(iii) To verify the maximum head of
self-priming pool filter pump, non-selfpriming pool filter pumps, and waterfall
pumps, the maximum head of each
tested unit of the basic model of selfpriming pool filter pump, non-selfpriming pool filter pump, or waterfall
pump will be measured pursuant to the
test requirements of § 431.464(b) of this
chapter and the result of the
measurement(s) will be compared to the
value of maximum head certified by the
manufacturer. The certified value of
maximum head will be considered valid
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only if the measurement(s) (either the
measured maximum head for a single
unit sample or the average of the
maximum head values for a multiple
unit sample) is within 5 percent of the
certified values of maximum head.
(A) If the representative value of
maximum head is found to be valid, the
value of maximum head certified by the
manufacturer will be used to determine
the appropriate equipment class and
standard level for that basic model.
(B) If the representative value of
maximum head is found to be invalid,
the measured value(s) of maximum head
determined from the tested unit(s) will
be used to determine the appropriate
equipment class and standard level for
that basic model.
(iv) To verify that a DPPP model
complies with the applicable freeze
protection control design requirements,
the initiation temperature, run-time, and
speed of rotation of the default control
configuration of each tested unit of the
basic model of dedicated-purpose pool
pump will be evaluated according to the
procedure specified in paragraph
(i)(2)(iv)(A) of this section:
(A)(1) Set up and configure the
dedicated-purpose pool pump under
test according to the manufacturer
instructions, including any necessary
initial priming, in a test apparatus as
described in appendix A of HI 40.6–
2014–B (incorporated by reference, see
§ 429.4), except that the ambient
temperature registered by the freeze
protection ambient temperature sensor
will be able to be measured and
controlled by, for example, exposing the
freeze protection temperature sensor to
a specific temperature by submerging
the sensor in a water bath of known
temperature, by adjusting the actual
ambient air temperature of the test
chamber and measuring the temperature
at the freeze protection ambient
temperature sensor location, or by other
means that allows the ambient
temperature registered by the freeze
protection temperature sensor to be
reliably simulated, varied, and
measured. Do not adjust the default
freeze protection control settings or
enable the freeze protection control if it
is shipped disabled.
(2) Activate power to the pump with
the flow rate set to zero (i.e., the pump
is energized but not circulating water).
Set the ambient temperature to 42.0 ±
0.5 °F and allow the temperature to
stabilize, where stability is determined
in accordance with section 40.6.3.2.2 of
HI 40.6–2014–B. After 5 minutes,
decrease the temperature measured by
the freeze protection temperature sensor
by 1.0 ± 0.5 °F and allow the
temperature to stabilize. After each
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reduction in ambient temperature and
subsequent stabilization, record the
DPPP rotating speed, if any, and freeze
protection ambient temperature reading,
where the ‘‘freeze protection ambient
temperature reading’’ is representative
of the temperature measured by the
freeze protection ambient temperature
sensor, which may be recorded by a
variety of means depending on how the
temperature is being simulated and
controlled. If no flow is initiated, record
zero rpm or no flow. Continue
decreasing the temperature measured by
the freeze protection temperature sensor
by 1.0 ± 0.5 °F after 5.0 minutes of stable
operation at the previous temperature
reading until the pump freeze protection
initiates water circulation or until the
ambient temperature of 38.0 ± 0.5 °F has
been evaluated (i.e., the end of the 5.0
minute interval of 38.0 °F), whichever
occurs first.
(3) If and when the DPPP freeze
protection controls initiate water
circulation, increase the ambient
temperature reading registered by the
freeze protection temperature sensor to
a temperature of 42.0 ± 0.5 °F and
maintain that temperature for 60.0
minutes. Do not modify or interfere with
the operation of the DPPP freeze
protection operating cycle. After 60.0
minutes, record the freeze protection
ambient temperature and rotating speed,
if any, of the dedicated-purpose pool
pump under test.
(B) If the dedicated-purpose pool
pump initiates water circulation at a
temperature greater than 40.0 °F; if the
dedicated-purpose pool pump was still
circulating water after 60.0 minutes of
operation at 42.0 ± 0.5 °F; or if rotating
speed measured at any point during the
DPPP freeze protection control test in
paragraph (i)(2)(iii)(A) of this section
was greater than one-half of the
maximum rotating speed of the DPPP
model certified by the manufacturer,
that DPPP model is deemed to not
comply with the design requirement for
freeze protection controls.
(C) If none of the conditions specified
in paragraph (i)(2)(iv)(B) of this section
are met, including if the DPPP freeze
protection control does not initiate
water circulation at all during the test,
the dedicated-purpose pool pump under
test is deemed compliant with the
design requirement for freeze protection
controls.
*
*
*
*
*
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PART 431—ENERGY EFFICIENCY
PROGRAM FOR CERTAIN
COMMERCIAL AND INDUSTRIAL
EQUIPMENT
6. The authority citation for part 431
continues to read as follows:
■
Authority: 42 U.S.C. 6291–6317; 28 U.S.C.
2461 note.
7. Section 431.462 is amended by:
a. Revising the introductory text; and
b. Revising the definition of ‘‘Basic
model;’’
■ c. Adding, in alphabetical order,
definitions for ‘‘Basket strainer,’’
‘‘Dedicated-purpose pool pump,’’
‘‘Dedicated-purpose pool pump motor
total horsepower,’’ ‘‘Dedicated-purpose
pool pump service factor,’’ ‘‘Designed
and marketed,’’ ‘‘Freeze protection
control,’’ ‘‘Integral,’’ ‘‘Integral cartridgefilter pool pump,’’ ‘‘Integral sand-filter
pool pump,’’ ‘‘Multi-speed dedicatedpurpose pool pump,’’ ‘‘Non-self-priming
pool filter pump,’’ ‘‘Pool filter pump,’’
‘‘Pressure cleaner booster pump,’’
‘‘Removable cartridge filter,’’ ‘‘Rigid
electric spa pump,’’ ‘‘Sand filter,’’ and
‘‘Self-priming pool filter pump;’’
■ d. Revising the definition of ‘‘Selfpriming pump;’’ and
■ e. Adding, in alphabetical order,
definitions for ‘‘Single-speed dedicatedpurpose pool pump,’’ ‘‘Storable electric
spa pump,’’ ‘‘Submersible pump,’’
‘‘Two-speed dedicated-purpose pool
pump,’’ ‘‘Variable-speed dedicatedpurpose pool pump,’’ ‘‘Variable speed
drive,’’ and ‘‘Waterfall pump.’’
The additions and revisions read as
follows:
■
■
■
§ 431.462
Definitions.
The following definitions are
applicable to this subpart, including
appendices A and B. In cases where
there is a conflict, the language of the
definitions adopted in this section takes
precedence over any descriptions or
definitions found in the 2014 version of
ANSI/HI Standard 1.1–1.2,
‘‘Rotodynamic (Centrifugal) Pumps For
Nomenclature And Definitions’’ (ANSI/
HI 1.1–1.2–2014; incorporated by
reference, see § 431.463), or the 2014
version of ANSI/HI Standard 2.1–2.2,
‘‘Rotodynamic (Vertical) Pumps For
Nomenclature And Definitions’’ (ANSI/
HI 2.1–2.2–2014; incorporated by
reference, see § 431.463). In cases where
definitions reference design intent, DOE
will consider marketing materials, labels
and certifications, and equipment
design to determine design intent.
*
*
*
*
*
Basic model means all units of a given
class of pump manufactured by one
manufacturer, having the same primary
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energy source, and having essentially
identical electrical, physical, and
functional (or hydraulic) characteristics
that affect energy consumption, energy
efficiency, water consumption, or water
efficiency; and, in addition, for pumps
that are subject to the standards
specified in § 431.465(b), the following
provisions also apply:
(1) All variations in numbers of stages
of bare RSV and ST pumps must be
considered a single basic model;
(2) Pump models for which the bare
pump differs in impeller diameter, or
impeller trim, may be considered a
single basic model; and
(3) Pump models for which the bare
pump differs in number of stages or
impeller diameter and which are sold
with motors (or motors and controls) of
varying horsepower may only be
considered a single basic model if:
(i) For ESCC, ESFM, IL, and RSV
pumps, each motor offered in the basic
model has a nominal full load motor
efficiency rated at the Federal minimum
(see the current table for NEMA Design
B motors at § 431.25) or the same
number of bands above the Federal
minimum for each respective motor
horsepower (see Table 3 of appendix A
to subpart Y of this part); or
(ii) For ST pumps, each motor offered
in the basic model has a full load motor
efficiency at the default nominal full
load submersible motor efficiency
shown in Table 2 of appendix A to
subpart Y of this part or the same
number of bands above the default
nominal full load submersible motor
efficiency for each respective motor
horsepower (see Table 3 of appendix A
to subpart Y of this part).
Basket strainer means a perforated or
otherwise porous receptacle, mounted
within a housing on the suction side of
a pump, that prevents solid debris from
entering a pump. The basket strainer
receptacle is capable of passing
spherical solids of 1 mm in diameter,
and can be removed by hand or using
only simple tools (e.g., screwdriver,
pliers, open-ended wrench).
*
*
*
*
*
Dedicated-purpose pool pump
comprises self-priming pool filter
pumps, non-self-priming pool filter
pumps, waterfall pumps, pressure
cleaner booster pumps, integral sandfilter pool pumps, integral-cartridge
filter pool pumps, storable electric spa
pumps, and rigid electric spa pumps.
Dedicated-purpose pool pump motor
total horsepower means the product of
the dedicated-purpose pool pump
nominal motor horsepower and the
dedicated-purpose pool pump service
factor of a motor used on a dedicated-
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purpose pool pump based on the
maximum continuous duty motor power
output rating allowable for the motor’s
nameplate ambient rating and insulation
class. (Dedicated-purpose pool pump
motor total horsepower is also referred
to in the industry as service factor
horsepower or motor capacity.)
Dedicated-purpose pool pump service
factor means a multiplier applied to the
rated horsepower of a pump motor to
indicate the percent above nameplate
horsepower at which the motor can
operate continuously without exceeding
its allowable insulation class
temperature limit.
Designed and marketed means that
the equipment is designed to fulfill the
indicated application and, when
distributed in commerce, is designated
and marketed for that application, with
the designation on the packaging and
any publicly available documents (e.g.,
product literature, catalogs, and
packaging labels).
*
*
*
*
*
Freeze protection control means a
pool pump control that, at a certain
ambient temperature, turns on the
dedicated-purpose pool pump to
circulate water for a period of time to
prevent the pool and water in plumbing
from freezing.
*
*
*
*
*
Integral means a part of the device
that cannot be removed without
compromising the device’s function or
destroying the physical integrity of the
unit.
Integral cartridge-filter pool pump
means a pump that requires a removable
cartridge filter, installed on the suction
side of the pump, for operation; and the
cartridge filter cannot be bypassed.
Integral sand-filter pool pump means
a pump distributed in commerce with a
sand filter that cannot be bypassed.
*
*
*
*
*
Multi-speed dedicated-purpose pool
pump means a dedicated-purpose pool
pump that is capable of operating at
more than two discrete, pre-determined
operating speeds separated by speed
increments greater than 100 rpm, where
the lowest speed is less than or equal to
half of the maximum operating speed
and greater than zero, and must be
distributed in commerce with an onboard pool pump control (i.e., variable
speed drive and user interface or
programmable switch) that changes the
speed in response to pre-programmed
user preferences and allows the user to
select the duration of each speed and/
or the on/off times.
*
*
*
*
*
Non-self-priming pool filter pump
means a pool filter pump that is not
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certified under NSF/ANSI 50–2015
(incorporated by reference, see
§ 431.463) to be self-priming and is not
capable of re-priming to a vertical lift of
at least 5.0 feet with a true priming time
less than or equal to 10.0 minutes, when
tested in accordance with section F of
appendix B or C of this subpart, and is
not a waterfall pump.
Pool filter pump means an end
suction pump that:
(1) Either:
(i) Includes an integrated basket
strainer; or
(ii) Does not include an integrated
basket strainer, but requires a basket
strainer for operation, as stated in
manufacturer literature provided with
the pump; and
(2) May be distributed in commerce
connected to, or packaged with, a sand
filter, removable cartridge filter, or other
filtration accessory, so long as the
filtration accessory are connected with
consumer-removable connections that
allow the filtration accessory to be
bypassed.
*
*
*
*
*
Pressure cleaner booster pump means
an end suction, dry rotor pump
designed and marketed for pressure-side
pool cleaner applications, and which
may be UL listed under ANSI/UL 1081–
2016 (incorporated by reference, see
§ 431.463).
*
*
*
*
*
Removable cartridge filter means a
filter component with fixed dimensions
that captures and removes suspended
particles from water flowing through the
unit. The removable cartridge filter is
not capable of passing spherical solids
of 1 mm in diameter or greater, and can
be removed from the filter housing by
hand or using only simple tools (e.g.,
screwdrivers, pliers, open-ended
wrench).
Rigid electric spa pump means an end
suction pump that does not contain an
integrated basket strainer or require a
basket strainer for operation as stated in
manufacturer literature provided with
the pump and that meets the following
three criteria:
(1) Is assembled with four through
bolts that hold the motor rear endplate,
rear bearing, rotor, front bearing, front
endplate, and the bare pump together as
an integral unit;
(2) Is constructed with buttress
threads at the inlet and discharge of the
bare pump; and
(3) Uses a casing or volute and
connections constructed of a nonmetallic material.
*
*
*
*
*
Sand filter means a device designed to
filter water through sand or an alternate
sand-type media.
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Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
Self-priming pool filter pump means a
pool filter pump that is certified under
NSF/ANSI 50–2015 (incorporated by
reference, see § 431.463) to be selfpriming or is capable of re-priming to a
vertical lift of at least 5.0 feet with a true
priming time less than or equal to 10.0
minutes, when tested in accordance
with section F of appendix B or C of this
subpart, and is not a waterfall pump.
Self-priming pump means a pump
that either is a self-priming pool filter
pump or a pump that:
(1) Is designed to lift liquid that
originates below the centerline of the
pump inlet;
(2) Contains at least one internal
recirculation passage; and
(3) Requires a manual filling of the
pump casing prior to initial start-up, but
is able to re-prime after the initial startup without the use of external vacuum
sources, manual filling, or a foot valve.
*
*
*
*
*
Single-speed dedicated-purpose pool
pump means a dedicated-purpose pool
pump that is capable of operating at
only one speed.
Storable electric spa pump means a
pump that is distributed in commerce
with one or more of the following:
(1) An integral heater; and
(2) An integral air pump.
Submersible pump means a pump
that is designed to be operated with the
motor and bare pump fully submerged
in the pumped liquid.
*
*
*
*
*
Two-speed dedicated-purpose pool
pump means a dedicated-purpose pool
pump that is capable of operating at
only two different pre-determined
operating speeds, where the low
operating speed is less than or equal to
half of the maximum operating speed
and greater than zero, and must be
distributed in commerce either:
(1) With a pool pump control (e.g.,
variable speed drive and user interface
or switch) that is capable of changing
the speed in response to user
preferences; or
(2) Without a pool pump control that
has the capability to change speed in
response to user preferences, but is
unable to operate without the presence
of such a pool pump control.
Variable-speed dedicated-purpose
pool pump means a dedicated-purpose
pool pump that is capable of operating
at a variety of user-determined speeds,
where all the speeds are separated by at
most 100 rpm increments over the
operating range and the lowest
operating speed is less than or equal to
one-third of the maximum operating
speed and greater than zero. Such a
pump must include a variable speed
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drive and be distributed in commerce
either:
(1) With a user interface that changes
the speed in response to preprogrammed user preferences and
allows the user to select the duration of
each speed and/or the on/off times; or
(2) Without a user interface that
changes the speed in response to preprogrammed user preferences and
allows the user to select the duration of
each speed and/or the on/off times, but
is unable to operate without the
presence of a user interface.
Variable speed drive means
equipment capable of varying the speed
of the motor.
Waterfall pump means a pool filter
pump with a certified maximum head
less than or equal to 30.0 feet, and a
maximum speed less than or equal to
1,800 rpm.
■ 8. Section 431.463 is amended by:
■ a. Revising paragraph (a);
■ b. Redesignating paragraphs (b)
through (d) and (e) as paragraphs (c)
through (f) and (h), respectively;
■ c. Adding new paragraph (b);
■ d. In newly redesignated paragraph
(d), adding paragraph (d)(4);
■ e. Adding new paragraphs (e) and (g);
and
■ f. In newly redesignated paragraph (h),
adding paragraph (h)(2).
The revisions and additions read as
follows:
call 202–741–6030, or go to:
www.archives.gov/federal_register/
code_of_federal_regulations/ibr_
locations.html.
(b) CSA. Canadian Standards
Association, 5060 Spectrum Way, Suite
100, Mississauga, Ontario, L4W 5N6,
Canada, (800) 463–6727.
www.csagroup.org.
(1) CSA C747–2009 (Reaffirmed
2014), (‘‘CSA C747–2009 (RA 2014)’’),
‘‘Energy efficiency test methods for
small motors,’’ CSA reaffirmed 2014,
IBR approved for appendices B and C to
this subpart, as follows:
(i) Section 1, ‘‘Scope’’;
(ii) Section 3, ‘‘Definitions’’;
(iii) Section 5, ‘‘General Test
Requirements’’; and
(iv) Section 6, ‘‘Test Method.’’
(2) [Reserved]
*
*
*
*
*
(d) * * *
(4) HI 40.6–2014, (‘‘HI 40.6–2014–B’’),
‘‘Methods for Rotodynamic Pump
Efficiency Testing’’ (except sections
40.6.4.1 ‘‘Vertically suspended pumps’’,
40.6.4.2 ‘‘Submersible pumps’’, 40.6.5.3
‘‘Test report’’, 40.6.5.5 ‘‘Test
conditions’’, 40.6.5.5.2 ‘‘Speed of
rotation during test’’, and 40.6.6.1
‘‘Translation of test results to rated
speed of rotation’’, Appendix A ‘‘Test
arrangements (normative)’’: A.7
‘‘Testing at temperatures exceeding 30
°C (86 °F)’’, and Appendix B, ‘‘Reporting
of test results (normative)’’), copyright
§ 431.463 Materials incorporated by
2014, IBR approved for appendices B
reference.
and C to this subpart.
(a) General. DOE incorporates by
(e) IEEE. Institute of Electrical and
reference the following standards into
Electronics Engineers, Inc., 45 Hoes
subpart Y of this part. The material
Lane, P.O. Box 1331, Piscataway, NJ
listed has been approved for
08855–1331, (732) 981–0060. https://
incorporation by reference by the
www.ieee.org.
Director of the Federal Register in
(1) IEEE Std 113–1985, (‘‘IEEE 113–
accordance with 5 U.S.C. 552(a) and 1
1985’’), ‘‘IEEE Guide: Test Procedures
CFR part 51. Any subsequent
for Direct-Current Machines,’’ copyright
amendment to a standard by the
1985, IBR approved for appendices B
standard-setting organization will not
and C to this subpart, as follows:
affect the DOE test procedures unless
(i) Section 3, Electrical Measurements
and until amended by DOE. Material is
and Power Sources for all Test
incorporated as it exists on the date of
Procedures:
the approval, and notification of any
(A) Section 3.1, ‘‘Instrument Selection
change in the material will be published Factors’’;
in the Federal Register. All approved
(B) Section 3.4 ‘‘Power
material can be obtained from the
Measurement’’; and
sources listed in this section and is
(C) Section 3.5 ‘‘Power Sources’’;
available for inspection at the U.S.
(ii) Section 4, Preliminary Tests:
Department of Energy, Office of Energy
(A) Section 4.1, Reference Conditions,
Efficiency and Renewable Energy,
Section 4.1.2, ‘‘Ambient Air’’; and
Building Technologies Program, Sixth
(B) Section 4.1, Reference Conditions,
Floor, 950 L’Enfant Plaza SW.,
Section 4.1.4 ‘‘Direction of Rotation’’;
Washington, DC 20024, (202) 586–2945, and
or go to: https://www1.eere.energy.gov/
(iii) Section 5, Performance
buildings/appliance_standards. It is also Determination:
available for inspection at the National
(A) Section 5.4, Efficiency, Section
Archives and Records Administration
5.4.1, ‘‘Reference Conditions’’; and
(NARA). For information on the
(B) Section 5.4.3, Direct
availability of this material at NARA,
Measurements of Input and Output,
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Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
Section 5.4.3.2 ‘‘Dynomometer or
Torquemeter Method.’’
(2) IEEE Std 114–2010, (‘‘IEEE 114–
2010’’), ‘‘IEEE Standard Test Procedure
for Single-Phase Induction Motors,’’
approved September 30, 2010, IBR
approved for appendices B and C to this
subpart, as follows:
(i) Section 3, ‘‘General tests’’, Section
3.2, ‘‘Tests with load’’;
(ii) Section 4 ‘‘Testing facilities’’; and
(iii) Section 5, ‘‘Measurements’’:
(A) Section 5.2 ‘‘Mechanical
measurements’’;
(B) Section 5.3 ‘‘Temperature
measurements’’; and
(iv) Section 6 ‘‘Tests.’’
*
*
*
*
*
(g) NSF. NSF International. 789 N.
Dixboro Road, Ann Arbor, MI 48105,
(743) 769–8010. www.nsf.org.
(1) NSF/ANSI 50–2015, ‘‘Equipment
for Swimming Pools, Spas, Hot Tubs
and Other Recreational Water
Facilities,’’ Annex C, ‘‘(normative Test
methods for the evaluation of
centrifugal pumps,’’ Section C.3, ‘‘Selfpriming capability,’’ ANSI approved
January 26, 2015, IBR approved for
§ 431.462 and appendices B and C to
this subpart.
(2) [Reserved]
(h) * * *
(2) UL 1081, (‘‘ANSI/UL 1081–2016’’),
‘‘Standard for Swimming Pool Pumps,
Filters, and Chlorinators,’’ 7th Edition,
ANSI approved October 21, 2016, IBR
approved for § 431.462.
■ 9. Section 431.464 is revised to read
as follows:
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§ 431.464 Test procedure for the
measurement of energy efficiency, energy
consumption, and other performance
factors of pumps.
(a) General pumps—(1) Scope. This
paragraph (a) provides the test
procedures for determining the constant
and variable load pump energy index
for:
(i) The following categories of clean
water pumps:
(A) End suction close-coupled (ESCC);
(B) End suction frame mounted/own
bearings (ESFM);
(C) In-line (IL);
(D) Radially split, multi-stage,
vertical, in-line casing diffuser (RSV);
and
(E) Submersible turbine (ST) pumps.
(ii) With the following characteristics:
(A) Flow rate of 25 gpm or greater at
BEP and full impeller diameter;
(B) Maximum head of 459 feet at BEP
and full impeller diameter and the
number of stages required for testing
(see section 1.2.2 of appendix A of this
subpart);
(C) Design temperature range from 14
to 248 °F;
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(D) Designed to operate with either:
(1) A 2- or 4-pole induction motor; or
(2) A non-induction motor with a
speed of rotation operating range that
includes speeds of rotation between
2,880 and 4,320 revolutions per minute
(rpm) and/or 1,440 and 2,160 rpm, and
in either case, the driver and impeller
must rotate at the same speed;
(E) For ST pumps, a 6-inch or smaller
bowl diameter; and
(F) For ESCC and ESFM pumps, a
specific speed less than or equal to
5,000 when calculated using U.S.
customary units.
(iii) Except for the following pumps:
(A) Fire pumps;
(B) Self-priming pumps;
(C) Prime-assist pumps;
(D) Magnet driven pumps;
(E) Pumps designed to be used in a
nuclear facility subject to 10 CFR part
50, ‘‘Domestic Licensing of Production
and Utilization Facilities’’; and
(F) Pumps meeting the design and
construction requirements set forth in
Military Specifications: MIL–P–17639F,
‘‘Pumps, Centrifugal, Miscellaneous
Service, Naval Shipboard Use’’ (as
amended); MIL–P–17881D, ‘‘Pumps,
Centrifugal, Boiler Feed, (Multi-Stage)’’
(as amended); MIL–P–17840C, ‘‘Pumps,
Centrifugal, Close-Coupled, Navy
Standard (For Surface Ship
Application)’’ (as amended); MIL–P–
18682D, ‘‘Pump, Centrifugal, Main
Condenser Circulating, Naval
Shipboard’’ (as amended); and MIL–P–
18472G, ‘‘Pumps, Centrifugal,
Condensate, Feed Booster, Waste Heat
Boiler, And Distilling Plant’’ (as
amended). Military specifications and
standards are available for review at
https://everyspec.com/MIL-SPECS.
(2) Testing and calculations.
Determine the applicable constant load
pump energy index (PEICL) or variable
load pump energy index (PEIVL) using
the test procedure set forth in appendix
A of this subpart.
(b) Dedicated-purpose pool pumps—
(1) Scope. This paragraph (b) provides
the test procedures for determining the
weighted energy factor (WEF), rated
hydraulic horsepower, dedicatedpurpose pool pump nominal motor
horsepower, dedicated-purpose pool
pump motor total horsepower,
dedicated-purpose pool pump service
factor, and other pump performance
parameters for:
(i) The following varieties of
dedicated-purpose pool pumps:
(A) Self-priming pool filter pumps;
(B) Non-self-priming pool filter
pumps;
(C) Waterfall pumps; and
(D) Pressure cleaner booster pumps;
(ii) Served by single-phase or
polyphase input power;
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(iii) Except for:
(A) Submersible pumps; and
(B) Self-priming and non-self-priming
pool filter pumps with hydraulic output
power greater than or equal to 2.5
horsepower.
(2) Testing and calculations.
Determine the weighted energy factor
(WEF) using the test procedure set forth
in appendix B or appendix C of this
subpart, as applicable.
■ 10. Section 431.466 is revised to read
as follows:
§ 431.466
Pumps labeling requirements.
(a) General pumps. For the pumps
described in § 431.464(a), the following
requirements apply to units
manufactured on the same date that
compliance is required with any
applicable standards prescribed in
§ 431.465.
(1) Pump nameplate—(i) Required
information. The permanent nameplate
must be marked clearly with the
following information:
(A) For bare pumps and pumps sold
with electric motors but not continuous
or non-continuous controls, the rated
pump energy index—constant load
(PEICL), and for pumps sold with motors
and continuous or non-continuous
controls, the rated pump energy index—
variable load (PEIVL);
(B) The bare pump model number;
and
(C) If transferred directly to an enduser, the unit’s impeller diameter, as
distributed in commerce. Otherwise, a
space must be provided for the impeller
diameter to be filled in.
(ii) Display of required information.
All orientation, spacing, type sizes,
typefaces, and line widths to display
this required information must be the
same as or similar to the display of the
other performance data on the pump’s
permanent nameplate. The PEICL or
PEIVL, as appropriate to a given pump
model, must be identified in the form
‘‘PEICL ____’’ or ‘‘PEIVL ____.’’ The
model number must be in one of the
following forms: ‘‘Model ____’’ or
‘‘Model number ____’’ or ‘‘Model No. _
___.’’ The unit’s impeller diameter must
be in the form ‘‘Imp. Dia. ____(in.).’’
(2) Disclosure of efficiency
information in marketing materials. (i)
The same information that must appear
on a pump’s permanent nameplate
pursuant to paragraph (a)(1)(i) of this
section, must also be prominently
displayed:
(A) On each page of a catalog that lists
the pump; and
(B) In other materials used to market
the pump.
(ii) [Reserved]
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(b) Dedicated-purpose pool pumps.
For the pumps described in
§ 431.464(b), the following requirements
apply on the same date that compliance
is required with any applicable
standards prescribed in § 431.465.
(1) Pump nameplate—(i) Required
information. The permanent nameplate
must be marked clearly with the
following information:
(A) The weighted energy factor (WEF);
and
(B) The dedicated-purpose pool pump
motor total horsepower.
(ii) Display of required information.
All orientation, spacing, type sizes,
typefaces, and line widths to display
this required information must be the
same as or similar to the display of the
other performance data on the pump’s
permanent nameplate.
(A) The WEF must be identified in the
form ‘‘WEF ____.’’
(B) The dedicated-purpose pool pump
motor total horsepower must be
identified in one of the following forms:
‘‘Dedicated-purpose pool pump motor
total horsepower _____,’’ ‘‘DPPP motor
total horsepower _____,’’ ‘‘motor total
horsepower _____,’’ ‘‘motor THP _____,’’
or ‘‘THP _____.’’
(2) [Reserved]
Appendix A to Subpart Y of Part 431
[Amended]
11. In the introductory note to
appendix A of subpart Y of part 431,
remove the reference ‘‘10 CFR 431.464’’
and add in its place ‘‘10 CFR
431.464(a)’’.
■ 12. Add appendices B and C to
subpart Y of part 431 to read as follows:
■
Appendix B to Subpart Y of Part 431—
Uniform Test Method for the
Measurement of Energy Efficiency of
Dedicated-Purpose Pool Pumps
Note: On February 5, 2018 but before July
19, 2021, any representations made with
respect to the energy use or efficiency of
dedicated-purpose pool pumps subject to
testing pursuant to 10 CFR 431.464(b) must
be made in accordance with the results of
testing pursuant to this appendix. Any
optional representations of energy factor (EF)
must be accompanied by a representation of
weighted energy factor (WEF).
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I. Test Procedure for Dedicated-Purpose Pool
Pumps
A. General
A.1 Test Method. To determine the
weighted energy factor (WEF) for dedicatedpurpose pool pumps, perform ‘‘wire-towater’’ testing in accordance with HI 40.6–
2014–B, except section 40.6.4.1, ‘‘Vertically
suspended pumps’’; section 40.6.4.2,
‘‘Submersible pumps’’; section 40.6.5.3,
‘‘Test report’’; section 40.6.5.5, ‘‘Test
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conditions’’; section 40.6.5.5.2, ‘‘Speed of
rotation during testing’’; section 40.6.6.1,
‘‘Translation of test results to rated speed of
rotation’’; section 40.6.6.2, ‘‘Pump
efficiency’’; section 40.6.6.3, ‘‘Performance
curve’’; section A.7, ‘‘Testing at temperatures
exceeding 30 °C (86 °F)’’; and appendix B,
‘‘Reporting of test results’’; (incorporated by
reference, see § 431.463) with the
modifications and additions as noted
throughout the provisions below. Do not use
the test points specified in section 40.6.5.5.1,
‘‘Test procedure’’ of HI 40.6–2014–B and
instead use those test points specified in
section D.3 of this appendix for the
applicable dedicated-purpose pool pump
variety and speed configuration. When
determining overall efficiency, best efficiency
point, or other applicable pump energy
performance information, section 40.6.5.5.1,
‘‘Test procedure’’; section 40.6.6.2, ‘‘Pump
efficiency’’; and section 40.6.6.3,
‘‘Performance curve’’ must be used, as
applicable. For the purposes of applying this
appendix, the term ‘‘volume per unit time,’’
as defined in section 40.6.2, ‘‘Terms and
definitions,’’ of HI 40.6–2014–B shall be
deemed to be synonymous with the term
‘‘flow rate’’ used throughout that standard
and this appendix.
A.2. Calculations and Rounding. All
terms and quantities refer to values
determined in accordance with the
procedures set forth in this appendix for the
rated pump. Perform all calculations using
raw measured values without rounding.
Round WEF, EF, maximum head, vertical lift,
and true priming time values to the tenths
place (i.e., 0.1) and rated hydraulic
horsepower to the thousandths place (i.e.,
0.001). Round all other reported values to the
hundredths place unless otherwise specified.
B. Measurement Equipment
B.1 For the purposes of measuring flow
rate, speed of rotation, temperature, and
pump power output, the equipment specified
in HI 40.6–2014–B Appendix C (incorporated
by reference, see § 431.463) necessary to
measure head, speed of rotation, flow rate,
and temperature must be used and must
comply with the stated accuracy
requirements in HI 40.6–2014–B Table
40.6.3.2.3, except as specified in section
B.1.1 and B.1.2 of this appendix. When more
than one instrument is used to measure a
given parameter, the combined accuracy,
calculated as the root sum of squares of
individual instrument accuracies, must meet
the specified accuracy requirements.
B.1.1 Electrical measurement equipment
for determining the driver power input to the
motor or controls must be capable of
measuring true root mean squared (RMS)
current, true RMS voltage, and real power up
to the 40th harmonic of fundamental supply
source frequency, and have a combined
accuracy of ±2.0 percent of the measured
value at the fundamental supply source
frequency.
B.1.2 Instruments for measuring distance
(e.g., height above the reference plane or
water level) must be accurate to and have a
resolution of at least ±0.1 inch.
B.2 Calibration. Calibration requirements
for instrumentation are specified in appendix
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D of HI 40.6–2014–B (incorporated by
reference, see § 431.463). Historical
calibration data may be used to justify time
periods up to three times longer than those
specified in table D.1 of HI 40.6–2014–B
provided the supporting historical data
shows maintenance of calibration of the
given instrument up to the selected extended
calibration interval on at least two unique
occasions, based on the interval specified in
HI 40.6–2014–B.
C. Test Conditions and Tolerances
C.1 Pump Specifications. Conduct testing
at full impeller diameter in accordance with
the test conditions, stabilization
requirements, and specifications of HI 40.6–
2014–B section 40.6.3, ‘‘Pump efficiency
testing’’; section 40.6.4, ‘‘Considerations
when determining the efficiency of a pump’’;
section 40.6.5.4 (including appendix A),
‘‘Test arrangements’’; and section 40.6.5.5,
‘‘Test conditions’’ (incorporated by reference,
see § 431.463).
C.2 Power Supply Requirements. The
following conditions also apply to the mains
power supplied to the DPPP motor or
controls, if any:
(1) Maintain the voltage within ±5 percent
of the rated value of the motor,
(2) Maintain the frequency within ±1
percent of the rated value of the motor,
(3) Maintain the voltage unbalance of the
power supply within ±3 percent of the value
with which the motor was rated, and
(4) Maintain total harmonic distortion
below 12 percent throughout the test.
C.3 Test Conditions. Testing must be
carried out with water that is between 50 and
107 °F with less than or equal to 15
nephelometric turbidity units (NTU).
C.4 Tolerances. For waterfall pumps,
multi-speed self-priming and non-selfpriming pool filter pumps, and variablespeed self-priming and non-self-priming pool
filter pumps all measured load points must
be within ±2.5 percent of the specified head
value and comply with any specified flow
values or thresholds. For all other dedicatedpurpose pool pumps, all measured load
points must be within the greater of ±2.5
percent of the specified flow rate values or
±0.5 gpm and comply with any specified
head values or thresholds.
D. Data Collection and Stabilization
D.1 Damping Devices. Use of damping
devices, as described in section 40.6.3.2.2 of
HI 40.6–2014–B (incorporated by reference,
see § 431.463), are only permitted to integrate
up to the data collection interval used during
testing.
D.2 Stabilization. Record data at any
tested load point only under stabilized
conditions, as defined in HI 40.6–2014–B
section 40.6.5.5.1 (incorporated by reference,
see § 431.463), where a minimum of two
measurements are used to determine
stabilization.
D.3 Test Points. Measure the flow rate in
gpm, pump total head in ft, the driver power
input in W, and the speed of rotation in rpm
at each load point specified in Table 1 of this
appendix for each DPPP variety and speed
configuration:
E:\FR\FM\07AUR2.SGM
07AUR2
36925
Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
TABLE 1—LOAD POINTS (i) AND WEIGHTS (wi) FOR EACH DPPP VARIETY AND SPEED CONFIGURATION
DPPP varieties
Self-Priming Pool Filter
Pumps And Non-SelfPriming Pool Filter Pumps.
Number
of load
points
(n)
Speed configuration(s)
Single-speed dedicated-purpose pool pumps and all
self-priming and non-selfpriming pool filter pumps
not meeting the definition
of two-*, multi-, or variable-speed dedicated-purpose pool pump.
Two-speed dedicated-purpose pool pumps *.
Test points
Load
point
(i)
Flow rate
(Q) (GPM)
Head
(H) (ft)
Speed
(rpm)
1
High .......
Qhigh (gpm) =
Qmax_speed@C **
H = 0.0082 ×
Qhigh2
Maximum speed
2
Low .......
Qlow (gpm) = Flow rate associated with specified head
and speed that is not
below:
• 31.1 gpm if rated hydraulic
horsepower is >0.75 or
• 24.7 gpm if rated hydraulic
horsepower is ≤0.75
Qhigh (gpm) =
Qmax_speed@C **
Qlow (gpm) =
• If rated hydraulic horsepower is >0.75, then Qlow
≥ 31.1 gpm
• If rated hydraulic horsepower is ≤0.75, then Qlow
≥24.7 gpm
Qhigh (gpm) ≥0.8 ×
Qmax_speed@C **
H = 0.0082 ×
Qlow2
Lowest speed capable of
meeting the specified flow
and head values, if
any ***.
H = 0.0082 ×
Qhigh2
H = 0.0082 ×
Qlow2
Maximum speed.
H = 0.0082 ×
Qhigh2
Lowest speed capable of
meeting the specified flow
and head values.
Maximum speed.
High .......
Multi-speed and variablespeed dedicated-purpose
pool pumps.
2
Low .......
High .......
Waterfall Pumps .....................
Single-speed dedicated-purpose pool pumps.
1
High .......
Pressure Cleaner Booster
Pumps.
Any .......................................
1
High .......
Qlow (gpm) = Flow corresponding to specified
head
10.0 gpm
17.0 ft
≥60.0 ft
Lowest speed capable of
meeting the specified flow
and head values.
Lowest speed capable of
meeting the specified flow
and head values.
* In order to apply the test points for two-speed self-priming and non-self-priming pool filter pumps, self-priming pool filter pumps that are greater than or equal to
0.711 rated hydraulic horsepower that are two-speed dedicated-purpose pool pumps must also be distributed in commerce either: (1) With a pool pump control (variable speed drive and user interface or switch) that changes the speed in response to pre-programmed user preferences and allows the user to select the duration of
each speed and/or the on/off times or (2) without a pool pump control that has such capability, but without which the pump is unable to operate. Two-speed selfpriming pool filter pumps greater than or equal to 0.711 rated hydraulic horsepower that do not meet these requirements must be tested using the load point for single-speed self-priming or non-self-priming pool filter pumps, as appropriate.
** Qmax_speed@C = Flow at max speed on curve C (gpm)
*** If a two-speed pump has a low speed that results in a flow rate below the specified values, the low speed of that pump shall not be tested.
E. Calculations
E.1 Determination of Weighted Energy
Factor. Determine the WEF as a ratio of the
measured flow and driver power input to the
dedicated-purpose pool pump in accordance
with the following equation:
Where:
WEF = Weighted Energy Factor in kgal/kWh;
wi = weighting factor at each load point i, as
specified in section E.2 of this appendix;
Qi = flow at each load point i, in gpm;
Pi = driver power input to the motor (or
controls, if present) at each load point i,
in watts;
i = load point(s), defined uniquely for each
DPPP variety and speed configuration as
specified in section D.3 of this appendix;
and
n = number of load point(s), defined
uniquely for each DPPP variety and
speed configuration as specified in
section D.3 of this appendix.
E.2 Weights. When determining WEF,
apply the weights specified in Table 2 of this
appendix for the applicable load points,
DPPP varieties, and speed configurations:
TABLE 2—LOAD POINT WEIGHTS (wi)
Load point(s) i
Speed configuration(s)
Low flow
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Self-Priming Pool Filter Pumps and Non-Self-Priming
Pool Filter Pumps.
Waterfall Pumps ...........................................................
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Single-speed dedicated-purpose pool pumps and all
self-priming and non-self-priming pool filter pumps
not meeting the definition of two-,* multi-, or variable-speed dedicated-purpose pool pump.
Two-speed dedicated-purpose pool pumps * ...............
Multi-speed and variable-speed dedicated-purpose
pool pumps.
Single-speed dedicated-purpose pool pumps ..............
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07AUR2
High flow
........................
1.0
0.80
0.80
0.20
0.20
........................
1.0
ER07AU17.010
DPPP varieties
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TABLE 2—LOAD POINT WEIGHTS (wi)—Continued
Load point(s) i
DPPP varieties
Speed configuration(s)
Low flow
Pressure Cleaner Booster Pump .................................
Any ................................................................................
........................
High flow
1.0
* In order to apply the test points for two-speed self-priming and non-self-priming pool filter pumps, self-priming pool filter pumps that are greater than or equal to 0.711 rated hydraulic horsepower that are two-speed dedicated-purpose pool pumps must also be distributed in commerce either: (1) With a pool pump control (variable speed drive and user interface or switch) that changes the speed in response to pre-programmed
user preferences and allows the user to select the duration of each speed and/or the on/off times or (2) without a pool pump control that has
such capability, but without which the pump is unable to operate. Two-speed self-priming pool filter pumps greater than or equal to 0.711 rated
hydraulic horsepower that do not meet these requirements must be tested using the load point for single-speed self-priming or non-self-priming
pool filter pumps, as appropriate.
Full-load speed and torque shall be
determined based on the maximum
continuous duty motor power output rating
allowable for the motor’s nameplate ambient
rating and insulation class.
E.3.2.1 For single-phase AC motors,
determine the measured speed and torque at
full load according to either section E.3.2.1.1
or E.3.2.1.2 of this appendix.
E.3.2.1.1 Use the procedures in section
3.2, ‘‘Tests with load’’; section 4 ‘‘Testing
facilities’’; section 5.2 ‘‘Mechanical
measurements’’; section 5.3 ‘‘Temperature
measurements’’; and section 6 ‘‘Tests’’ of
IEEE 114–2010 (incorporated by reference,
see § 431.463), or
E.3.2.1.2 Use the applicable procedures
in section 5, ‘‘General test requirements’’ and
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Where:
PFi = true power factor at each load point i,
dimensionless;
Pi = driver power input to the motor (or
controls, if present) at each load point i,
in watts;
Vi = voltage at each load point i, in volts;
Ii = current at each load point i, in amps; and
i = load point(s), defined uniquely for each
DPPP variety and speed configuration as
specified in section D.3 of this appendix.
E.4 Determination of Maximum Head.
Determine the maximum head for selfpriming pool filter pumps, non-self-priming
pool filter pumps, and waterfall pumps by
measuring the head at maximum speed and
the minimum flow rate at which the pump
is designed to operate continuously or safely,
where the minimum flow rate is assumed to
be zero unless stated otherwise in the
manufacturer literature.
F. Determination of Self-Priming Capability
F.1 Test Method. Determine the vertical
lift and true priming time of non-self-priming
pool filter pumps and self-priming pool filter
pumps that are not already certified as selfpriming under NSF/ANSI 50–2015
(incorporated by reference, see § 431.463) by
testing such pumps pursuant to section C.3
of appendix C of NSF/ANSI 50–2015, except
for the modifications and exceptions listed in
the following sections F.1.1 through F.1.5 of
this appendix:
F.1.1 Where section C.3.2, ‘‘Apparatus,’’
and section C.3.4, ‘‘Self-priming capability
test method,’’ of NSF/ANSI 50–2015
(incorporated by reference, see § 431.463)
state that the ‘‘suction line must be
essentially as shown in annex C, figure C.1;’’
the phrase ‘‘essentially as shown in Annex C,
figure C.1’’ means:
• The centerline of the pump impeller
shaft is situated a vertical distance equivalent
to the specified vertical lift (VL), calculated
in accordance with section F.1.1.1. of this
appendix, above the water level of a water
tank of sufficient volume as to maintain a
constant water surface level for the duration
of the test;
E:\FR\FM\07AUR2.SGM
07AUR2
ER07AU17.013
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Where:
Pnm = the dedicated-purpose pool pump
nominal total horsepower at full load, in
hp;
T = output torque at full load, in lb-ft; and
n = the motor speed at full load, in rpm.
input to the motor (or controls, if present)
(Pi), in watts, divided by the product of the
voltage in volts and the current in amps at
each load point i, as shown in the following
equation:
ER07AU17.012
Where:
Pu,i = the measured pump power output at
load point i of the tested pump, in hp;
Qi = the measured flow rate at load point i
of the tested pump, in gpm;
Hi = pump total head at load point i of the
tested pump, in ft; and
SG = the specific gravity of water at specified
test conditions, which is equivalent to
1.00.
E.3.1.1 Determine the rated hydraulic
horsepower as the pump power output
measured on the reference curve at maximum
rotating speed and full impeller diameter for
the rated pump.
E.3.2 For dedicated-purpose pool pumps
with single-phase AC motors or DC motors,
determine the dedicated-purpose pool pump
nominal motor horsepower as the product of
the measured full load speed and torque,
adjusted to the appropriate units, as shown
in the following equation:
section 6, ‘‘Tests’’ of CSA C747–2009 (RA
2014); except in section 6.4(b) the conversion
factor shall be 5252, only measurements at
full load are required in section 6.5, and
section 6.6 shall be disregarded (incorporated
by reference, see § 431.463).
E.3.2.2 For DC motors, determine the
measured speed and torque at full load
according to either section E.3.2.2.1 or
E.3.2.2.2 of this appendix.
E.3.2.2.1 Use the procedures in section
3.1, ‘‘Instrument Selection Factors’’; section
3.4 ‘‘Power Measurement’’: Section 3.5
‘‘Power Sources’’; section 4.1.2 ‘‘Ambient
Air’’; section 4.1.4 ‘‘Direction of Rotation’’;
section 5.4.1 ‘‘Reference Conditions’’; and
section 5.4.3.2 ‘‘Dynomometer or
Torquemeter Method’’ of IEEE 113–1985
(incorporated by reference, see § 431.463), or
E.3.2.2.2 Use the applicable procedures
in section 5, ‘‘General test requirements’’ and
section 6, ‘‘Tests’’ of CSA C747–2009 (RA
2014); except in section 6.4(b) the conversion
factor shall be 5252, only measurements at
full load are required in section 6.5, and
section 6.6 shall be disregarded (incorporated
by reference, see § 431.463).
E.3.3 For dedicated-purpose pool pumps
with single-phase AC motors or DC motors,
the dedicated-purpose pool pump service
factor is equal to 1.0.
E.3.4 Determine the dedicated-purpose
pool pump motor total horsepower according
to section E.3.4.1 of this appendix for
dedicated-purpose pool pumps with singlephase AC motors or DC motors and section
E.3.4.2 of this appendix for dedicatedpurpose pool pumps with polyphase AC
motors.
E.3.4.1 For dedicated-purpose pool
pumps with single-phase AC motors or DC
motors, determine the dedicated-purpose
pool pump motor total horsepower as the
product of the dedicated-purpose pool pump
nominal motor horsepower, determined in
accordance with section E.3.2 of this
appendix, and the dedicated-purpose pool
pump service factor, determined in
accordance with section E.3.3 of this
appendix.
E.3.4.2 For dedicated-purpose pool
pumps with polyphase AC induction motors,
determine the dedicated-purpose pool pump
motor total horsepower as the product of the
rated nominal motor horsepower and the
rated service factor of the motor.
E.3.5 Determine the true power factor at
each applicable load point specified in Table
1 of this appendix for each DPPP variety and
speed configuration as a ratio of driver power
ER07AU17.011
E.3 Determination of Horsepower and
True Power Factor Metrics
E.3.1 Determine the pump power output
at any load point i using the following
equation:
Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
36927
• The pump draws water from the water
tank with a riser pipe that extends below the
water level a distance of at least 3 times the
riser pipe diameter (i.e., 3 pipe diameters);
• The suction inlet of the pump is at least
5 pipe diameters from any obstructions, 90°
bends, valves, or fittings; and
• The riser pipe is of the same pipe
diameter as the pump suction inlet.
F.1.1.1 The vertical lift (VL) must be
normalized to 5.0 feet at an atmospheric
pressure of 14.7 psia and a water density of
62.4 lb/ft3 in accordance with the following
equation:
Where:
VL = vertical lift of the test apparatus from
the waterline to the centerline of the
pump impeller shaft, in ft;
rtest = density of test fluid, in lb/ft3; and
Pabs,test = absolute barometric pressure of test
apparatus location at centerline of pump
impeller shaft, in psia.
40.6–2014–B (incorporated by reference, see
§ 431.463).
F.1.3 All tests must be conducted with
clear water that meets the requirements
adopted in section C.3 of this appendix.
F.1.4 In section C.3.4, ‘‘Self-priming
capability test method,’’ of NSF/ANSI 50–
2015 (incorporated by reference, see
§ 431.463), ‘‘the elapsed time to steady
discharge gauge reading or full discharge
flow’’ is determined when the changes in
head and flow, respectively, are within the
tolerance values specified in table 40.6.3.2.2,
‘‘Permissible amplitude of fluctuation as a
percentage of mean value of quantity being
measured at any test point,’’ of HI 40.6–
2014–B (incorporated by reference, see
§ 431.463). The measured priming time
(MPT) is determined as the point in time
when the stabilized load point is first
achieved, not when stabilization is
determined. In addition, the true priming
time (TPT) is equivalent to the MPT.
F.1.5 The maximum true priming time for
each test run must not exceed 10.0 minutes.
Disregard section C.3.5 of NSF/ANSI 50–
2015 (incorporated by reference, see
§ 431.463).
replacement DPPP motor paired with each
dedicated-purpose pool pump bare pump for
which the replacement DPPP motor is
advertised to be paired, as stated in the
manufacturer’s literature for that replacement
DPPP motor model, according to the testing
and calculations described in sections A, B,
C, D, and E of this appendix. Alternatively,
each replacement DPPP motor may be tested
with the most consumptive dedicatedpurpose pool pump bare pump for which it
is advertised to be paired, as stated in the
manufacturer’s literature for that replacement
DPPP motor model. If a replacement DPPP
motor is not advertised to be paired with any
specific dedicated-purpose pool pump bare
pumps, test with the most consumptive
dedicated-purpose pool pump bare pump
available.
I. Test Procedure for Dedicated-Purpose Pool
Pumps
G.1.1 System Curves. The energy factor
may be determined at any speed (s) and on
any of the four system curves A, B, C, and/
or D specified in the Table 3:
TABLE 3—SYSTEMS CURVES FOR
OPTIONAL EF TEST PROCEDURE
mstockstill on DSK30JT082PROD with RULES2
System curve
A
B
C
D
....................
....................
....................
....................
System curve equation *
H
H
H
H
=
=
=
=
0.0167
0.0500
0.0082
0.0044
×
×
×
×
Q2
Q2
Q2
Q2
* In the above table, Q refers to the flow rate
in gpm and H refers to head in ft.
G.2 Replacement Dedicated-Purpose Pool
Pump Motors. To determine the WEF for
replacement DPPP motors, test each
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Appendix C to Subpart Y of Part 431—
Uniform Test Method for the
Measurement of Energy Efficiency of
Dedicated-Purpose Pool Pumps
Note: Any representations made on or after
July 19, 2021, with respect to the energy use
or efficiency of dedicated-purpose pool
pumps subject to testing pursuant to 10 CFR
431.464(b) must be made in accordance with
the results of testing pursuant to this
appendix.
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G.1 Energy Factor. When making
representations regarding the EF of
dedicated-purpose pool pumps, determine
EF on one of four system curves (A, B, C, or
D) and at any given speed (s) according to the
following equation:
A. General
A.1 Test Method. To determine the
weighted energy factor (WEF) for dedicatedpurpose pool pumps, perform ‘‘wire-towater’’ testing in accordance with HI 40.6–
2014–B, except section 40.6.4.1, ‘‘Vertically
suspended pumps’’; section 40.6.4.2,
‘‘Submersible pumps’’; section 40.6.5.3,
‘‘Test report’’; section 40.6.5.5, ‘‘Test
conditions’’; section 40.6.5.5.2, ‘‘Speed of
rotation during testing’’; section 40.6.6.1,
‘‘Translation of test results to rated speed of
rotation’’; section 40.6.6.2, ‘‘Pump
efficiency’’; section 40.6.6.3, ‘‘Performance
curve’’; section A.7, ‘‘Testing at temperatures
exceeding 30 °C (86 °F)’’; and appendix B,
‘‘Reporting of test results’’; (incorporated by
reference, see § 431.463) with the
modifications and additions as noted
throughout the provisions below. Do not use
the test points specified in section 40.6.5.5.1,
‘‘Test procedure’’ of HI 40.6–2014–B and
instead use those test points specified in
section D.3 of this appendix for the
applicable dedicated-purpose pool pump
variety and speed configuration. When
determining overall efficiency, best efficiency
point, or other applicable pump energy
performance information, section 40.6.5.5.1,
‘‘Test procedure’’; section 40.6.6.2, ‘‘Pump
efficiency’’; and section 40.6.6.3,
E:\FR\FM\07AUR2.SGM
07AUR2
ER07AU17.015
Where:
EFX,s = the energy factor on system curve X
at speed s in gal/Wh;
X = one of four possible system curves (A,
B, C, or D), as defined in section G.1.1
of this appendix;
s = the tested speed, in rpm;
QX,s = flow rate measured on system curve X
at speed s in gpm; and
PX,s = driver power input to the motor (or
controls, if present) on system curve X at
speed s in watts.
G. Optional Testing and Calculations
ER07AU17.014
F.1.2 The equipment accuracy
requirements specified in section B,
‘‘Measurement Equipment,’’ of this appendix
also apply to this section F, as applicable.
F.1.2.1 All measurements of head (gauge
pressure), flow, and water temperature must
be taken at the pump suction inlet and all
head measurements must be normalized back
to the centerline of the pump impeller shaft
in accordance with section A.3.1.3.1 of HI
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‘‘Performance curve’’ must be used, as
applicable. For the purposes of applying this
appendix, the term ‘‘volume per unit time,’’
as defined in section 40.6.2, ‘‘Terms and
definitions,’’ of HI 40.6–2014–B shall be
deemed to be synonymous with the term
‘‘flow rate’’ used throughout that standard
and this appendix .
A.2 Calculations and Rounding. All terms
and quantities refer to values determined in
accordance with the procedures set forth in
this appendix for the rated pump. Perform all
calculations using raw measured values
without rounding. Round WEF, maximum
head, vertical lift, and true priming time
values to the tenths place (i.e., 0.1) and rated
hydraulic horsepower to the thousandths
place (i.e., 0.001). Round all other reported
values to the hundredths place unless
otherwise specified.
B. Measurement Equipment
B.1 For the purposes of measuring flow
rate, speed of rotation, temperature, and
pump power output, the equipment specified
in HI 40.6–2014–B Appendix C (incorporated
by reference, see § 431.463) necessary to
measure head, speed of rotation, flow rate,
and temperature must be used and must
comply with the stated accuracy
requirements in HI 40.6–2014–B Table
40.6.3.2.3, except as specified in sections
B.1.1 and B.1.2 of this appendix. When more
than one instrument is used to measure a
given parameter, the combined accuracy,
calculated as the root sum of squares of
individual instrument accuracies, must meet
the specified accuracy requirements.
B.1.1 Electrical measurement equipment
for determining the driver power input to the
motor or controls must be capable of
measuring true root mean squared (RMS)
current, true RMS voltage, and real power up
to the 40th harmonic of fundamental supply
source frequency, and have a combined
accuracy of ±2.0 percent of the measured
value at the fundamental supply source
frequency.
B.1.2 Instruments for measuring distance
(e.g., height above the reference plane or
water level) must be accurate to and have a
resolution of at least ±0.1 inch.
B.2 Calibration. Calibration requirements
for instrumentation are specified in appendix
D of HI 40.6–2014–B (incorporated by
reference, see § 431.463). Historical
calibration data may be used to justify time
periods up to three times longer than those
specified in table D.1 of HI 40.6–2014–B
provided the supporting historical data
shows maintenance of calibration of the
given instrument up to the selected extended
calibration interval on at least two unique
occasions, based on the interval specified in
HI 40.6–2014–B.
(3) Maintain the voltage unbalance of the
power supply within ±3 percent of the value
with which the motor was rated, and
(4) Maintain total harmonic distortion
below 12 percent throughout the test.
C.3 Test Conditions. Testing must be
carried out with water that is between 50 and
107 °F with less than or equal to 15
nephelometric turbidity units (NTU).
C.4 Tolerances. For waterfall pumps,
multi-speed self-priming and non-selfpriming pool filter pumps, and variablespeed self-priming and non-self-priming pool
filter pumps all measured load points must
be within ±2.5 percent of the specified head
value and comply with any specified flow
values or thresholds. For all other dedicatedpurpose pool pumps, all measured load
points must be within the greater of ±2.5
percent of the specified flow rate values or
±0.5 gpm and comply with any specified
head values or thresholds.
C. Test Conditions and Tolerances
C.1 Pump Specifications. Conduct testing
at full impeller diameter in accordance with
the test conditions, stabilization
requirements, and specifications of HI 40.6–
2014–B section 40.6.3, ‘‘Pump efficiency
testing’’; section 40.6.4, ‘‘Considerations
when determining the efficiency of a pump’’;
section 40.6.5.4 (including appendix A),
‘‘Test arrangements’’; and section 40.6.5.5,
‘‘Test conditions’’ (incorporated by reference,
see § 431.463).
C.2 Power Supply Requirements. The
following conditions also apply to the mains
power supplied to the DPPP motor or
controls, if any:
(1) Maintain the voltage within ±5 percent
of the rated value of the motor,
(2) Maintain the frequency within ±1
percent of the rated value of the motor,
D. Data Collection and Stabilization
D.1 Damping Devices. Use of damping
devices, as described in section 40.6.3.2.2 of
HI 40.6–2014–B (incorporated by reference,
see § 431.463), are only permitted to integrate
up to the data collection interval used during
testing.
D.2 Stabilization. Record data at any
tested load point only under stabilized
conditions, as defined in HI 40.6–2014–B
section 40.6.5.5.1 (incorporated by reference,
see § 431.463), where a minimum of two
measurements are used to determine
stabilization.
D.3 Test Points. Measure the flow rate in
gpm, pump total head in ft, the driver power
input in W, and the speed of rotation in rpm
at each load point specified in Table 1 of this
appendix for each DPPP variety and speed
configuration:
TABLE 1—LOAD POINTS (i) AND WEIGHTS (wi) FOR EACH DPPP VARIETY AND SPEED CONFIGURATION
DPPP varieties
Speed configuration(s)
Self-Priming Pool Filter
Pumps And Non-SelfPriming Pool Filter Pumps.
Number
of load
points
(n)
Single-speed dedicated-purpose pool pumps and all
self-priming and non-selfpriming pool filter pumps
not meeting the definition
of two-*, multi-, or variable-speed dedicated-purpose pool pump.
Two-speed dedicated-purpose pool pumps *.
Test points
Load
point
(i)
Flow rate
(Q) (GPM)
High .......
Qhigh (gpm) =
Qmax_speed@C **
H = 0.0082 ×
Qhigh2
Maximum speed.
2
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Multi-speed and variablespeed dedicated-purpose
pool pumps.
Low .......
Qlow (gpm) = Flow rate associated with specified head
and speed that is not
below:
• 31.1 gpm if rated hydraulic
horsepower is >0.75 or
• 24.7 gpm if rated hydraulic
horsepower is ≤0.75
Qhigh (gpm) =
Qmax_speed@C **
Qlow (gpm) =
• If rated hydraulic horsepower is >0.75, then Qlow
≥31.1 gpm
• If rated hydraulic horsepower is ≤0.75, then Qlow
≥24.7 gpm
Qhigh (gpm) ≥0.8 ×
Qmax_speed@C **
H = 0.0082 ×
Qlow2
Lowest speed capable of
meeting the specified flow
and head values, if
any. ***
H = 0.0082 ×
Qlow2
H = 0.0082 ×
Qlow2
Maximum speed.
H = 0.0082 ×
Qhigh2
Lowest speed capable of
meeting the specified flow
and head values.
2
Low .......
High .......
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Speed
(rpm)
1
High .......
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Head
(H) (ft)
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Lowest speed capable of
meeting the specified flow
and head values.
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TABLE 1—LOAD POINTS (i) AND WEIGHTS (wi) FOR EACH DPPP VARIETY AND SPEED CONFIGURATION—Continued
Number
of load
points
(n)
Test points
Load
point
(i)
DPPP varieties
Speed configuration(s)
Waterfall Pumps .....................
Single-speed dedicated-purpose pool pumps.
1
High .......
Pressure Cleaner Booster
Pumps.
Any .......................................
1
High .......
Flow rate
(Q) (GPM)
Head
(H) (ft)
Qlow (gpm) = Flow corresponding to specified
head
10.0 gpm
Speed
(rpm)
17.0 ft
Maximum speed.
≥60.0 ft
Lowest speed capable of
meeting the specified flow
and head values.
* In order to apply the test points for two-speed self-priming and non-self-priming pool filter pumps, self-priming pool filter pumps that are greater than or equal to
0.711 rated hydraulic horsepower that are two-speed dedicated-purpose pool pumps must also be distributed in commerce either: (1) With a pool pump control (variable speed drive and user interface or switch) that changes the speed in response to pre-programmed user preferences and allows the user to select the duration of
each speed and/or the on/off times or (2) without a pool pump control that has such capability, but without which the pump is unable to operate. Two-speed selfpriming pool filter pumps greater than or equal to 0.711 rated hydraulic horsepower that do not meet these requirements must be tested using the load point for single-speed self-priming or non-self-priming pool filter pumps, as appropriate.
** Qmax_speed@C = Flow at max speed on curve C (gpm).
*** If a two-speed pump has a low speed that results in a flow rate below the specified values, the low speed of that pump shall not be tested.
E. Calculations
E.1 Determination of Weighted Energy
Factor. Determine the WEF as a ratio of the
measured flow and driver power input to the
dedicated-purpose pool pump in accordance
with the following equation:
Where:
WEF = Weighted Energy Factor in kgal/kWh;
Wi = weighting factor at each load point i, as
specified in section E.2 of this appendix;
Qi = flow at each load point i, in gpm;
Pi = driver power input to the motor (or
controls, if present) at each load point i,
in watts;
i = load point(s), defined uniquely for each
DPPP variety and speed configuration as
specified in section D.3 of this appendix;
and
n = number of load point(s), defined
uniquely for each DPPP variety and
speed configuration as specified in
section D.3 of this appendix.
E.2 Weights. When determining WEF,
apply the weights specified in Table 2 of this
appendix for the applicable load points,
DPPP varieties, and speed configurations:
TABLE 2—LOAD POINT WEIGHTS (wi)
DPPP varieties
Load point(s)
i
Speed configuration(s)
Low flow
Self-Priming Pool Filter Pumps and Non-Self-Priming
Pool Filter Pumps.
Waterfall Pumps ...........................................................
Pressure Cleaner Booster Pump .................................
Single-speed dedicated-purpose pool pumps and all
self-priming and non-self-priming pool filter pumps
not meeting the definition of two-*, multi-, or variable-speed dedicated-purpose pool pump.
Two-speed dedicated-purpose pool pumps * ...............
Multi-speed and variable-speed dedicated-purpose
pool pumps.
Single-speed dedicated-purpose pool pumps ..............
Any ................................................................................
High flow
........................
1.0
0.80
0.80
0.20
0.20
........................
........................
1.0
1.0
* In order to apply the test points for two-speed self-priming and non-self-priming pool filter pumps, self-priming pool filter pumps that are greater than or equal to 0.711 rated hydraulic horsepower that are two-speed dedicated-purpose pool pumps must also be distributed in commerce either: (1) With a pool pump control (variable speed drive and user interface or switch) that changes the speed in response to pre-programmed
user preferences and allows the user to select the duration of each speed and/or the on/off times or (2) without a pool pump control that has
such capability, but without which the pump is unable to operate. Two-speed self-priming pool filter pumps greater than or equal to 0.711 rated
hydraulic horsepower that do not meet these requirements must be tested using the load point for single-speed self-priming or non-self-priming
pool filter pumps, as appropriate.
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Where:
Pnm = the dedicated-purpose pool pump
nominal total horsepower at full load, in
hp;
T = output torque at full load, in lb-ft; and
n = the motor speed at full load, in rpm.
Full-load speed and torque shall be
determined based on the maximum
continuous duty motor power output rating
allowable for the motor’s nameplate ambient
rating and insulation class.
E.3.2.1 For single-phase AC motors,
determine the measured speed and torque at
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07AUR2
ER07AU17.018
E.3.1.1 Determine the rated hydraulic
horsepower as the pump power output
measured on the reference curve at maximum
rotating speed and full impeller diameter for
the rated pump.
E.3.2 For dedicated-purpose pool pumps
with single-phase AC motors or DC motors,
determine the dedicated-purpose pool pump
nominal motor horsepower as the product of
the measured full load speed and torque,
adjusted to the appropriate units, as shown
in the following equation:
ER07AU17.017
Where:
Pu,i = the measured pump power output at
load point i of the tested pump, in hp;
Qi = the measured flow rate at load point i
of the tested pump, in gpm;
Hi = pump total head at load point i of the
tested pump, in ft; and
SG = the specific gravity of water at specified
test conditions, which is equivalent to
1.00.
ER07AU17.016
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E.3 Determination of Horsepower and
True Power Factor Metrics
E.3.1 Determine the pump power output
at any load point i using the following
equation:
Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
head measurements must be normalized back
to the centerline of the pump impeller shaft
in accordance with section A.3.1.3.1 of HI
40.6–2014–B (incorporated by reference, see
§ 431.463).
F.1.3 All tests must be conducted with
clear water that meets the requirements
adopted in section C.3 of this appendix.
F.1.4 In section C.3.4, ‘‘Self-priming
capability test method,’’ of NSF/ANSI 50–
2015 (incorporated by reference, see
§ 431.463), ‘‘the elapsed time to steady
discharge gauge reading or full discharge
flow’’ is determined when the changes in
head and flow, respectively, are within the
tolerance values specified in table 40.6.3.2.2,
F.1.2 The equipment accuracy
requirements specified in section B,
‘‘Measurement Equipment,’’ of this appendix
also apply to this section F, as applicable.
F.1.2.1 All measurements of head (gauge
pressure), flow, and water temperature must
be taken at the pump suction inlet and all
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Where:
PFi = true power factor at each load point i,
dimensionless;
Pi = driver power input to the motor (or
controls, if present) at each load point i,
in watts;
Vi = voltage at each load point i, in volts;
Ii = current at each load point i, in amps; and
i = load point(s), defined uniquely for each
DPPP variety and speed configuration as
specified in section D.3 of this appendix.
E.4 Determination of Maximum Head.
Determine the maximum head for selfpriming pool filter pumps, non-self-priming
pool filter pumps, and waterfall pumps by
measuring the head at maximum speed and
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the minimum flow rate at which the pump
is designed to operate continuously or safely,
where the minimum flow rate is assumed to
be zero unless stated otherwise in the
manufacturer literature.
F. Determination of Self-Priming Capability
F.1 Test Method. Determine the vertical
lift and true priming time of non-self-priming
pool filter pumps and self-priming pool filter
pumps that are not already certified as selfpriming under NSF/ANSI 50–2015
(incorporated by reference, see § 431.463) by
testing such pumps pursuant to section C.3
of appendix C of NSF/ANSI 50–2015, except
for the modifications and exceptions listed in
the following sections F.1.1 through F.1.5 of
this appendix:
F.1.1 Where section C.3.2, ‘‘Apparatus,’’
and section C.3.4, ‘‘Self-priming capability
test method,’’ of NSF/ANSI 50–2015
(incorporated by reference, see § 431.463)
state that the ‘‘suction line must be
essentially as shown in annex C, figure C.1;’’
the phrase ‘‘essentially as shown in Annex C,
figure C.1’’ means:
(1) The centerline of the pump impeller
shaft is situated a vertical distance equivalent
to the specified vertical lift (VL), calculated
in accordance with section F.1.1.1. of this
appendix, above the water level of a water
tank of sufficient volume as to maintain a
constant water surface level for the duration
of the test;
(2) The pump draws water from the water
tank with a riser pipe that extends below the
water level a distance of at least 3 times the
riser pipe diameter (i.e., 3 pipe diameters);
(3) The suction inlet of the pump is at least
5 pipe diameters from any obstructions, 90°
bends, valves, or fittings; and
(4) The riser pipe is of the same pipe
diameter as the pump suction inlet.
F.1.1.1 The vertical lift (VL) must be
normalized to 5.0 feet at an atmospheric
pressure of 14.7 psia and a water density of
62.4 lb/ft3 in accordance with the following
equation:
‘‘Permissible amplitude of fluctuation as a
percentage of mean value of quantity being
measured at any test point,’’ of HI 40.6–
2014–B (incorporated by reference, see
§ 431.463). The measured priming time
(MPT) is determined as the point in time
when the stabilized load point is first
achieved, not when stabilization is
determined. In addition, the true priming
time (TPT) is equivalent to the MPT.
F.1.5 The maximum true priming time for
each test run must not exceed 10.0 minutes.
Disregard section C.3.5 of NSF/ANSI 50–
2015 (incorporated by reference, see
§ 431.463).
E:\FR\FM\07AUR2.SGM
07AUR2
ER07AU17.020
purpose pool pumps with polyphase AC
motors.
E.3.4.1 For dedicated-purpose pool
pumps with single-phase AC motors or DC
motors, determine the dedicated-purpose
pool pump motor total horsepower as the
product of the dedicated-purpose pool pump
nominal motor horsepower, determined in
accordance with section E.3.2 of this
appendix, and the dedicated-purpose pool
pump service factor, determined in
accordance with section E.3.3 of this
appendix.
E.3.4.2 For dedicated-purpose pool
pumps with polyphase AC induction motors,
determine the dedicated-purpose pool pump
motor total horsepower as the product of the
rated nominal motor horsepower and the
rated service factor of the motor.
E.3.5 Determine the true power factor at
each applicable load point specified in Table
1 of this appendix for each DPPP variety and
speed configuration as a ratio of driver power
input to the motor (or controls, if present)
(Pi), in watts, divided by the product of the
voltage in volts and the current in amps at
each load point i, as shown in the following
equation:
Where:
VL = vertical lift of the test apparatus from
the waterline to the centerline of the
pump impeller shaft, in ft;
rtest = density of test fluid, in lb/ft3; and
Pabs,test = absolute barometric pressure of test
apparatus location at centerline of pump
impeller shaft, in psia.
mstockstill on DSK30JT082PROD with RULES2
full load according to either section E.3.2.1.1
or E.3.2.1.2 of this appendix.
E.3.2.1.1 Use the procedures in section
3.2, ‘‘Tests with load’’; section 4 ‘‘Testing
facilities’’; section 5.2 ‘‘Mechanical
measurements’’; section 5.3 ‘‘Temperature
measurements’’; and section 6 ‘‘Tests’’ of
IEEE 114–2010 (incorporated by reference,
see § 431.463), or
E.3.2.1.2 Use the applicable procedures
in section 5, ‘‘General test requirements’’ and
section 6, ‘‘Tests’’ of CSA C747–2009 (RA
2014); except in section 6.4(b) the conversion
factor shall be 5252, only measurements at
full load are required in section 6.5, and
section 6.6 shall be disregarded (incorporated
by reference, see § 431.463).
E.3.2.2 For DC motors, determine the
measured speed and torque at full load
according to either section E.3.2.2.1 or
E.3.2.2.2 of this appendix.
E.3.2.2.1 Use the procedures in section
3.1, ‘‘Instrument Selection Factors’’; section
3.4 ‘‘Power Measurement’’: Section 3.5
‘‘Power Sources’’; section 4.1.2 ‘‘Ambient
Air’’; section 4.1.4 ‘‘Direction of Rotation’’;
section 5.4.1 ‘‘Reference Conditions’’; and
section 5.4.3.2 ‘‘Dynomometer or
Torquemeter Method’’ of IEEE 113–1985
(incorporated by reference, see § 431.463), or
E.3.2.2.2 Use the applicable procedures
in section 5, ‘‘General test requirements’’ and
section 6, ‘‘Tests’’ of CSA C747–2009 (RA
2014); except in section 6.4(b) the conversion
factor shall be 5252, only measurements at
full load are required in section 6.5, and
section 6.6 shall be disregarded (incorporated
by reference, see § 431.463).
E.3.3 For dedicated-purpose pool pumps
with single-phase AC motors or DC motors,
the dedicated-purpose pool pump service
factor is equal to 1.0.
E.3.4 Determine the dedicated-purpose
pool pump motor total horsepower according
to section E.3.4.1 of this appendix for
dedicated-purpose pool pumps with singlephase AC motors or DC motors and section
E.3.4.2 of this appendix for dedicated-
ER07AU17.019
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Federal Register / Vol. 82, No. 150 / Monday, August 7, 2017 / Rules and Regulations
G. Optional Testing and Calculations
mstockstill on DSK30JT082PROD with RULES2
G.1 Replacement Dedicated-Purpose Pool
Pump Motors. To determine the WEF for
replacement DPPP motors, test each
replacement DPPP motor paired with each
dedicated-purpose pool pump bare pump for
which the replacement DPPP motor is
advertised to be paired, as stated in the
manufacturer’s literature for that replacement
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19:37 Aug 04, 2017
Jkt 241001
DPPP motor model, according to the testing
and calculations described in sections A, B,
C, D, and E of this appendix. Alternatively,
each replacement DPPP motor may be tested
with the most consumptive dedicatedpurpose pool pump bare pump for which it
is advertised to be paired, as stated in the
manufacturer’s literature for that replacement
DPPP motor model. If a replacement DPPP
motor is not advertised to be paired with any
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36931
specific dedicated-purpose pool pump bare
pumps, test with the most consumptive
dedicated-purpose pool pump bare pump
available.
Editorial note: This document was
received for publication by the Office of the
Federal Register on July 19, 2017.
[FR Doc. 2017–15464 Filed 8–4–17; 8:45 am]
BILLING CODE 6450–01–P
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Agencies
[Federal Register Volume 82, Number 150 (Monday, August 7, 2017)]
[Rules and Regulations]
[Pages 36858-36931]
From the Federal Register Online via the Government Publishing Office [www.gpo.gov]
[FR Doc No: 2017-15464]
[[Page 36857]]
Vol. 82
Monday,
No. 150
August 7, 2017
Part II
Department of Energy
-----------------------------------------------------------------------
10 CFR Parts 429 and 431
Energy Conservation Program: Test Procedure for Dedicated-Purpose Pool
Pumps; Final Rule
Federal Register / Vol. 82 , No. 150 / Monday, August 7, 2017 / Rules
and Regulations
[[Page 36858]]
-----------------------------------------------------------------------
DEPARTMENT OF ENERGY
10 CFR Parts 429 and 431
[EERE-2016-BT-TP-0002]
RIN 1904-AD66
Energy Conservation Program: Test Procedure for Dedicated-Purpose
Pool Pumps
AGENCY: Office of Energy Efficiency and Renewable Energy, Department of
Energy.
ACTION: Final rule.
-----------------------------------------------------------------------
SUMMARY: On September 20, 2016, the U.S. Department of Energy (DOE)
issued a notice of proposed rulemaking (NOPR) to establish a new
metric, as well as new definitions, test procedures, certification
requirements, enforcement testing procedures, and labeling provisions
for dedicated-purpose pool pumps (DPPPs). That proposed rulemaking
serves as the basis for the final rule. Specifically, DOE is adopting a
test procedure for measuring the weighted energy factor (WEF) for
certain varieties of dedicated-purpose pool pumps. This final rule
incorporates by reference certain sections of the industry test
standard Hydraulic Institute (HI) 40.6-2014, ``Methods for Rotodynamic
Pump Efficiency Testing'' as the basis of the adopted test procedure.
The definitions, test procedures, certification requirements,
enforcement testing procedures, and labeling provisions are based on
the recommendations of the DPPP Working Group, which was established
under the Appliance Standards Rulemaking Federal Advisory Committee
(ASRAC).
DATES: The effective date of this rule is September 6, 2017. Compliance
with the final rule will be mandatory for representations of WEF and
other metrics addressed by the adopted test procedure made on or after
February 5, 2018. The incorporation by reference of certain
publications listed in this rule is approved by the Director of the
Federal Register on September 6, 2017.
ADDRESSES: The docket, which includes Federal Register notices, public
meeting attendee lists and transcripts, comments, and other supporting
documents/materials, is available for review at www.regulations.gov.
All documents in the docket are listed in the www.regulations.gov
index. However, some documents listed in the index, such as those
containing information that is exempt from public disclosure, may not
be publicly available.
A link to the docket Web page can be found at https://www.regulations.gov/docket?D=EERE-2016-BT-TP-0002. The docket Web page
will contain simple instructions on how to access all documents,
including public comments, in the docket.
For further information on how to review the docket, contact the
Appliance and Equipment Standards Program staff at (202) 586-6636 or by
email: ApplianceStandardsQuestions@ee.doe.gov.
FOR FURTHER INFORMATION CONTACT:
Ms. Ashley Armstrong, U.S. Department of Energy, Office of Energy
Efficiency and Renewable Energy, Building Technologies Office, EE-5B,
1000 Independence Avenue SW., Washington, DC 20585-0121. Telephone:
(202) 586-6590. Email: Ashley.Armstrong@ee.doe.gov.
Ms. Mary Greene, U.S. Department of Energy, Office of the General
Counsel, GC-33, 1000 Independence Avenue SW., Washington, DC 20585-
0121. Telephone: (202) 586-1817. Email: Mary.Greene@hq.doe.gov.
SUPPLEMENTARY INFORMATION: This final rule incorporates by reference
into 10 CFR parts 429 and 431 the following industry standards:
(1) Hydraulic Institute (HI) 40.6-2014, (``HI 40.6-2014-B'')
``Methods for Rotodynamic Pump Efficiency Testing,'' except for section
40.6.4.1, ``Vertically suspended pumps''; section 40.6.4.2,
``Submersible pumps''; section 40.6.5.3, ``Test report''; section
40.6.5.5, ``Test conditions''; section 40.6.5.5.2, ``Speed of rotation
during testing''; and section 40.6.6.1, ``Translation of test results
to rated speed of rotation''; and Appendix A, Testing arrangements
(normative): A.7, ``Testing at temperatures exceeding 30 [deg]C
(86[emsp14][deg]F)''; and Appendix B, ``Reporting of test results
(normative)''), copyright 2014.
Copies of HI 40.6-2014 can be obtained from: The Hydraulic
Institute at 6 Campus Drive, First Floor North, Parsippany, NJ 07054-
4406, (973) 267-9700, or by visiting www.pumps.org.
(2) Canadian Standards Association (CSA) C747-2009 (Reaffirmed
2014), ``Energy Efficiency Test Methods for Small Motors,'' CSA
reaffirmed 2014, section 1, ``Scope''; section 3, ``Definitions'';
section 5, ``General Test Requirements''; and section 6, ``Test
Method.''
Copies of CSA C747-2009 (RA 2014) can be obtained from: 5060
Spectrum Way, Suite 100, Mississauga, Ontario, L4W 5N6, Canada, (800)
463-6727, or by visiting www.csagroup.org.
(3) IEEE Std 113-1985, ``IEEE Guide: Test Procedures for Direct-
Current Machines,'' copyright 1985, section 3.1, ``Instrument Selection
Factors''; section 3.4 ``Power Measurement'': section 3.5 ``Power
Sources''; section 4.1.2 ``Ambient Air''; section 4.1.4 ``Direction of
Rotation''; section 5.4.1 ``Reference Conditions''; and section 5.4.3.2
``Dynomometer or Torquemeter Method.''
(4) IEEE Std 114-2010, ``IEEE Standard Test Procedure for Single-
Phase Induction Motors,'' approved September 30, 2010, section 3.2,
``Tests with load''; section 4 ``Testing facilities''; section 5.2
``Mechanical measurements''; section 5.3 ``Temperature measurements'';
and section 6 ``Tests.''
Copies of IEEE 113-1985 and IEEE 114-2010 and can be obtained from:
IEEE, 45 Hoes Lane, P.O. Box 1331, Piscataway, NJ 08855-1331, (732)
981-0060, or by visiting www.ieee.org.
(5) NSF International (NSF)/American National Standards Institute
(ANSI) Standard 50-2015, (``NSF/ANSI 50-2015''), ``Equipment for
Swimming Pools, Spas, Hot Tubs and Other Recreational Water
Facilities,'' Annex C, ``(normative) Test methods for the evaluation of
centrifugal pumps,'' section C.3, ``Self-priming capability,'' ANSI
approved January 26, 2015.
Copies of NSF/ANSI 50-2015 can be obtained from: NSF International,
789 N. Dixboro Road, Ann Arbor, MI 48105, (743) 769-8010, or by
visiting www.nsf.org.
(6) UL 1081, (``ANSI/UL 1081-2016''), ``Standard for Swimming Pool
Pumps, Filters, and Chlorinators,'' 7th Edition, ANSI approved October
21, 2016.
Copies of ANSI/UL 1081-2016 can be obtained from: UL, 333 Pfingsten
Road, Northbrook, IL 60062, (847) 272-8800, or by visiting https://ul.com.
See section IV.N for additional information on these standards.
Table of Contents
I. Authority and Background
A. Authority
B. Background
II. Synopsis of the Final Rule
III. Discussion
A. General Comments
B. Definitions
1. Existing Pump Definitions
2. Definition of Dedicated-Purpose Pool Pump
3. Pool Filter Pumps
4. Other Varieties of Dedicated-Purpose Pool Pumps
5. Storable and Rigid Electric Spa Pumps
6. Applicability of Test Procedure Based on Pump Configuration
7. Definitions Related to Dedicated-Purpose Pool Pump Speed
Configurations and Controls
8. Basic Model
C. Rating Metric
D. Test Methods for Different DPPP Categories and Configurations
[[Page 36859]]
1. Self-Priming and Non-Self-Priming Pool Filter Pumps
2. Waterfall Pumps
3. Pressure Cleaner Booster Pumps
4. Summary
E. Determination of Pump Performance
1. Incorporation by Reference of HI 40.6-2014
2. Exceptions, Modifications and Additions to HI 40.6-2014
F. Representations of Test Metrics
1. Representations of Primary Efficiency Metrics
2. Definition of Representation
3. Impact on Voluntary and Other Regulatory Programs
4. Request for Extension
G. Additional Test Methods
1. Determination of DPPP Capacity
2. Determination of Self-Priming Capability
3. Determination of Maximum Head
H. Energy Factor Test Method
I. Labeling Requirements
J. Replacement DPPP Motors
K. Certification and Enforcement Provisions for Dedicated-
Purpose Pool Pumps
1. Sampling Plan
2. Certification Requirements
3. Enforcement Provisions
IV. Procedural Issues and Regulatory Review
A. Review Under Executive Order 12866
B. Review Under the Regulatory Flexibility Act
1. Review of DPPP Manufacturers
2. Burden of Conducting the DOE DPPP Test Procedure
C. Review Under the Paperwork Reduction Act of 1995
D. Review Under the National Environmental Policy Act of 1969
E. Review Under Executive Order 13132
F. Review Under Executive Order 12988
G. Review Under the Unfunded Mandates Reform Act of 1995
H. Review Under the Treasury and General Government
Appropriations Act, 1999
I. Review Under Executive Order 12630
J. Review Under Treasury and General Government Appropriations
Act, 2001
K. Review Under Executive Order 13211
L. Review Under Section 32 of the Federal Energy Administration
Act of 1974
M. Congressional Notification
N. Description of Materials Incorporated by Reference
V. Approval of the Office of the Secretary
I. Authority and Background
Pumps are included in the list of ``covered equipment'' for which
the U.S. Department of Energy (DOE) is authorized to establish and
amend energy conservation standards (ECSs) and test procedures (TPs).
(42 U.S.C. 6311(1)(A)) Dedicated-purpose pool pumps (DPPPs), which are
the subject of this rulemaking, are a kind of pump for which DOE is
authorized to establish test procedures and energy conservation
standards. In 2016, DOE published in the Federal Register two final
rules establishing energy conservation standards and a test procedure
for commercial and industrial pumps. 81 FR 4368 (Jan. 26, 2016) and 81
FR 4086 (January 25, 2016), respectively. However, dedicated-purpose
pool pumps were specifically excluded from those final rules. Based on
recommendations of the industry and DOE's own analysis, DOE determined
that dedicated-purpose pool pumps have a unique application and
equipment characteristics that merit a separate analysis. As a result,
DOE initiated separate rulemakings to establish energy conservation
standards and test procedures for dedicated-purpose pool pumps. The
following sections discuss DOE's authority to establish test procedures
for dedicated-purpose pool pumps and relevant background information
regarding DOE's consideration of establishing Federal regulations for
this equipment.
A. Authority
Title III of the Energy Policy and Conservation Act of 1975, as
amended, (42 U.S.C. 6291, et seq.; ``EPCA'' or, ``the Act'') sets forth
a variety of provisions designed to improve energy efficiency.\1\ Part
C of Title III, which for editorial reasons was codified as Part A-1
upon incorporation into the U.S. Code (42 U.S.C. 6311-6317),
establishes the Energy Conservation Program for Certain Industrial
Equipment. ``Pumps'' are listed as a type of industrial equipment
covered by EPCA, although EPCA does not define the term ``pump.'' (42
U.S.C. 6311(1)(A)) DOE defined ``pump'' in a test procedure final rule
(January 2016 general pumps test procedure final rule) as equipment
designed to move liquids (which may include entrained gases, free
solids, and totally dissolved solids) by physical or mechanical action,
and includes a bare pump and, if included by the manufacturer at the
time of sale, mechanical equipment, driver, and controls. 81 FR 4086
(Jan. 25, 2016). Dedicated-purpose pool pumps, which are the subject of
this final rule, meet this definition of a pump and are covered under
the pump equipment type.
---------------------------------------------------------------------------
\1\ All references to EPCA in this document refer to the statute
as amended through the Energy Efficiency Improvement Act of 2015,
Public Law 114-11 (Apr. 30, 2015).
---------------------------------------------------------------------------
Under EPCA, the energy conservation program consists essentially of
four parts: (1) Testing, (2) labeling, (3) Federal energy conservation
standards, and (4) certification and enforcement procedures. The
testing requirements consist of test procedures that manufacturers of
covered products must use as the basis for (1) certifying to DOE that
their products comply with the applicable energy conservation standards
adopted under EPCA, and (2) making representations about the efficiency
of those products. Similarly, DOE must use these test procedures to
determine whether the products comply with any relevant standards
promulgated under EPCA.
Under 42 U.S.C. 6293, EPCA sets forth the criteria and procedures
DOE must follow when prescribing or amending test procedures for
covered products. EPCA provides that any test procedures prescribed or
amended under this section shall be reasonably designed to produce test
results that measure energy efficiency, energy use, or estimated annual
operating cost of a covered product during a representative average use
cycle or period of use and shall not be unduly burdensome to conduct.
(42 U.S.C. 6293(b)(3))
In addition, if DOE determines that a test procedure amendment is
warranted, DOE must publish a proposed test procedure and offer the
public an opportunity to present oral and written comments on it. (42
U.S.C. 6293(b)(2)) Finally, in any rulemaking to amend a test
procedure, DOE must determine to what extent, if any, the proposed test
procedure would alter the measured energy efficiency of any covered
product as determined under the existing test procedure. (42 U.S.C.
6293(e)(1))
B. Background
Dedicated-purpose pool pumps are a style of pump for which DOE has
not yet established a test procedure. Although in 2016 DOE completed
final rules establishing energy conservation standards (81 FR 4368
(Jan. 26, 2016); January 2016 general pumps ECS final rule) and a test
procedure (81 FR 4086 (Jan. 25, 2016); January 2016 general pumps test
procedure final rule) for certain categories and configurations of
pumps, DOE declined in those rules to establish any requirements
applicable to dedicated-purpose pool pumps because of their different
equipment characteristics and applications. 81 FR 4086, 4094 (Jan. 25,
2016).
To begin a separate rulemaking for dedicated-purpose pool pumps, on
May 8, 2015, DOE issued a Request for Information (RFI), hereafter
referred to as the ``May 2015 DPPP RFI.'' The May 2015 DPPP RFI
presented information and requested public comment about any
definitions, metrics, test procedures, equipment characteristics, and
typical applications relevant to DPPP equipment. 80 FR 26475. Following
the publication of the May 2015 DPPP RFI, DOE began a process
[[Page 36860]]
through the Appliance Standards Rulemaking Federal Advisory Committee
(ASRAC) to discuss conducting a negotiated rulemaking to develop
standards and a test procedure for dedicated-purpose pool pumps as an
alternative to the traditional notice and comment route that DOE had
already begun. (Docket No. EERE-2015-BT-STD-0008) On August 25, 2015,
DOE published a notice of intent to establish a negotiated rulemaking
working group for dedicated-purpose pool pumps (as previously defined,
the ``DPPP Working Group'') to negotiate, if possible, Federal
standards for the energy efficiency of dedicated-purpose pool pumps and
to announce the first public meeting. 80 FR 51483.
The DPPP Working Group met four times between September and
December 2015 \2\ and concluded its negotiations on December 8, 2015,
with a consensus vote to approve a term sheet containing
recommendations to DOE on scope, metric, and the basis of the test
procedure (``December 2015 DPPP Working Group recommendations'').\3\
The term sheet containing these recommendations is available in the
DPPP Working Group docket. (Docket No. EERE-2015-BT-STD-0008, No. 51)
ASRAC subsequently voted unanimously to approve the December 2015 DPPP
Working Group recommendations during a January 20, 2016, meeting.
(Docket No. EERE-2015-BT-STD-0008, No. 0052)
---------------------------------------------------------------------------
\2\ Details of the negotiations sessions can be found in the
public meeting transcripts that are posted to the docket for the
DPPP Working Group (https://www.regulations.gov/docket?D=EERE-2015-BT-STD-0008).
\3\ The ground rules of the DPPP Working Group define consensus
as no more than three negative votes. (Docket No. EERE-2015-BT-0008-
0016 at p. 3) Concurrence was assumed absent overt dissent,
evidenced by a negative vote. Abstention was not construed as a
negative vote.
---------------------------------------------------------------------------
The DPPP Working Group also requested, and was ultimately granted,
more time to discuss possible energy conservation standards for this
equipment. (Docket No. EERE-2013-BT-NOC-0005, No. 71 at pp. 20-52) The
meetings to discuss energy conservation standards commenced on March
21, 2016, (81 FR 10152, 10153) and concluded on June 23, 2016, with
approval of a second term sheet (June 2016 DPPP Working Group
recommendations). This term sheet contained Working Group
recommendations related to scope, definitions, energy conservation
standards, performance standards or design requirements for various
styles of pumps, applicable test procedure, and labeling for dedicated-
purpose pool pumps. (Docket No. EERE-2015-BT-STD-0008, No. 82) The
definitions, DPPP test procedure, sampling provisions, enforcement
requirements, and labeling requirements contained in this final rule
reflect the recommendations of the DPPP Working Group contained in both
the December 2015 and June 2016 DPPP Working Group recommendations.
On September 20, 2016, DOE published a proposed test procedure
rulemaking for dedicated-purpose pool pumps (September 2016 DPPP test
procedure NOPR), which proposed to implement the recommendations of the
DPPP Working Group. 81 FR 64580. On September 26, 2016, DOE held a
public meeting to discuss and request comment on the September 2016
DPPP test procedure NOPR (September 2016 DPPP test procedure NOPR
public meeting).
The test procedure adopted in this final rule reflects certain
recommendations of the DPPP Working Group, as well as input from
interested parties received in response to the September 2016 DPPP test
procedure NOPR. Provisions of this final rule that are directly
pertinent to any of the approved DPPP Working Group recommendations are
specified with a citation to the December 2015 or June 2016 DPPP
Working Group recommendations and are noted with the recommendation
number (e.g., Docket No. EERE-2015-BT-STD-0008, No. #, Recommendation
#X at p. Y). Additionally, in developing the provisions of this final
rule, DOE also has referenced discussions from the DPPP Working Group
meetings regarding potential actions or comments that may not have been
formally approved as part of the DPPP Working Group recommendations.
These references to discussions or suggestions of the DPPP Working
Group not found in the DPPP Working Group recommendations will have a
citation to meeting transcripts and the commenter, if applicable (e.g.,
Docket No. EERE-2015-BT-STD-0008, [Organization], No. X at p. Y).
Finally, in this final rule, DOE responds to all comments received
from interested parties in response to the proposals presented in the
September 2016 DPPP test procedure NOPR, either during the September
2016 DPPP test procedure NOPR public meeting or in subsequent written
comments. In response to the September 2016 DPPP test procedure NOPR,
DOE received 11 written comments in addition to the verbal comments
made by interested parties during the September 2016 DPPP test
procedure NOPR public meeting. The commenters included: The Southern
California Gas Company (SCG), Southern California Edison (SCE), and San
Diego Gas and Electric Company (SDG&E), collectively referred to herein
as the California Investor-Owned Utilities (CA IOUs); a joint comment
by the Appliance Standards Awareness Project (ASAP) and the Natural
Resources Defense Council (NRDC); \4\ Pentair Aquatic Systems
(Pentair); Hayward Industries, Inc. (Hayward); Waterway; Davey Water
Products Pty Ltd. (Davey); the California Energy Commission (CEC); the
Association of Pool & Spa Professionals (APSP); Nidec Motor Corporation
(Nidec); Zodiac Pool Systems, Inc. (Zodiac); and the People's Republic
of China (China). DOE identifies comments received in response to the
September 2016 DPPP test procedure NOPR by the commenter, the number of
document as listed in the docket maintained at www.regulations.gov
(Docket No. EERE-2016-BT-TP-0002), and the page number of that document
where the comment appears (for example: Hayward, No. 4 at p. 1). If a
comment was made verbally during the September 2016 DPPP test procedure
NOPR public meeting, DOE will also specifically identify those as being
located in the NOPR public meeting transcript (for example: CA IOUs,
public meeting transcript, No. 3 at p. 66).
---------------------------------------------------------------------------
\4\ ASAP was present at the September 2016 DPPP TP NOPR public
meeting. When ASAP commented at the public meeting, comments will be
indicated as ASAP. ASAP and NRDC submitted a joint written comment
and written comments will be indicated as ASAP and NRDC.
---------------------------------------------------------------------------
Regarding comments, during the September 2016 DPPP test procedure
public meeting, Hayward inquired if it was appropriate to suggest any
modifications to previously negotiated language, if Hayward believed it
could be helpful. (Hayward, Public Meeting Transcript, No. 3 at p. 20)
DOE requested feedback on a number of items in the September 2016 DPPP
test procedure NOPR and welcomed comment from interested parties on any
of the proposals contained in the NOPR. DOE notes that DPPP Working
Group ground rules stipulate that each party, except individuals that
have previously voted negatively on the final term sheet, agrees not to
file negative comments or speak negatively on the proposed rule or its
preamble to the extent they have the same substance and effect as the
term sheet. (Docket No. EERE-2015-BT-STD-0008, No. 16 at p. 5) However,
these rules are not legally binding, but instead are good-faith
principles to govern Working Group's negotiations. Under the
Administrative Procedure Act, DOE must consider all relevant comments
submitted concerning the
[[Page 36861]]
September 2016 DPPP test procedure NOPR, and make modifications to the
proposals, as necessary, in this final rule. (5 U.S.C. 553(c)) Specific
required modifications are discussed in their relevant sections.
On January 18, 2017, DOE published a direct final rule containing
energy conservation standards for dedicated-purpose pool pumps (e.g.,
the January 2017 DPPP DFR), based on the recommendations of the DPPP
Working Group, with a compliance date of July 19, 2021. 82 FR 5650.
After reviewing comments submitted during the 110-day comment period,
on May 26, 2017, DOE published a confirmation of effective date and
compliance date for the DFR. 82 FR 24218.
II. Synopsis of the Final Rule
In this final rule, DOE is amending subpart Y to 10 CFR part 431 to
include definitions and a test procedure applicable to dedicated-
purpose pool pumps. However, DOE is establishing a test procedure for
only a specific subset of dedicated-purpose pool pumps. Specifically,
this test procedure applies only to self-priming and non-self-priming
pool filter pumps, waterfall pumps, and pressure cleaner booster pumps.
The test procedure does not apply to integral cartridge-filter pool
pumps, integral sand-filter pool pumps, storable electric spa pumps, or
rigid electric spa pumps. The test procedure is applicable to those
varieties of pool pumps for which DOE established performance-based
standards in the January 2017 DPPP DFR (82 FR 5650, 5743), as well as
additional categories of dedicated-purpose pool pumps for which the
DPPP Working Group did not propose standards. (See section III.B.6 for
more information on the applicability of the new test procedure to
different DPPP varieties).
In this final rule, DOE defines a new metric, the weighted energy
factor (WEF), to characterize the energy performance of dedicated-
purpose pool pumps within the scope of this test procedure. As
described further in section III.C, WEF is determined as a weighted
average of water volumetric flow rate divided by the input power to the
dedicated-purpose pool pump at different load points. The specific load
points and weights depend on the variety of the dedicated-purpose pool
pump and the number of operating speeds with which it is distributed in
commerce. In addition, the DPPP test procedure includes a test method
to determine the self-priming capability of pool filter pumps to
effectively differentiate self-priming and non-self-priming pool filter
pumps. Finally, the DPPP test procedure provides optional methods for
determining the WEF for replacement DPPP motors.
DOE's new test method includes measurements of volumetric flow rate
and input power, both of which are required to calculate WEF, as well
as other quantities to effectively characterize the rated DPPP
performance (e.g., head, hydraulic output power, rotating speed). For
consistent and uniform measurement of these values, DOE is
incorporating by reference the test methods established in HI 40.6-
2014, ``Methods for Rotodynamic Pump Efficiency Testing,'' with certain
exceptions. DOE reviewed the relevant sections of HI 40.6-2014 and
determined that HI 40.6-2014, in conjunction with the additional test
methods and calculations adopted in this test procedure, will produce
test results that reflect the energy efficiency, energy use, or
estimated operating costs of a dedicated-purpose pool pump during a
representative average use cycle. (42 U.S.C. 6314(a)(2)) DOE also
reviewed the burdens associated with conducting the test procedure,
including HI 40.6-2014, and, based on the results of such analysis,
found that the test procedure is not unduly burdensome to conduct. (42
U.S.C. 6314(a)(2)) DOE's analysis of the burdens associated with the
test procedure is presented in section IV.B.
This final rule also establishes requirements regarding the
sampling plan, certification requirements, and representations for
dedicated-purpose pool pumps at subpart B of part 429 of title 10 of
the Code of Federal Regulations. The sampling plan requirements are
similar to those for several other types of commercial equipment and
are appropriate for dedicated-purpose pool pumps based on the expected
range of measurement uncertainty and manufacturing tolerances for this
equipment (see section III.K.1 for more detailed information). As DOE's
DPPP test procedure contains methods for calculating the energy factor
(EF),\5\ overall (wire-to-water) efficiency, driver power input, DPPP
nominal motor horsepower,\6\ DPPP motor total horsepower, DPPP service
factor, pump power output (hydraulic horsepower), and true power factor
(PF), DOE also is adopting provisions regarding allowable
representations of energy consumption, energy efficiency, and other
relevant metrics manufacturers may make regarding DPPP performance
(section III.H). DOE is also clarifying the appropriate use of such
metrics through the use of two appendices: Appendix B, which contains
metrics and test methods applicable to testing dedicated-purpose pool
pumps prior to the compliance date of the established energy
conservation standards for such equipment (i.e., prior to July 19,
2021), and appendix C, which contains metrics and test methods
applicable to testing dedicated-purpose pool pumps on or after the
compliance date of any applicable energy conservation standards (i.e.,
on and after July 19, 2021).
---------------------------------------------------------------------------
\5\ EF is a metric that is common in the DPPP industry and which
describes the volume of water provided by a dedicated-purpose pool
pump divided by the input power required to pump that amount of
water in units of gallons per watt-hour (gal/Wh). The relevant test
methods for determining EF are described in section III.F.
\6\ In this final rule, DOE is adopting specific test methods
and metrics applicable to DPPP nominal motor horsepower, DPPP total
horsepower, DPPP service factor, and rated hydraulic horsepower of
dedicated-purpose pool pumps. See section III.G.1 for a discussion
of the different horsepower metrics applicable to dedicated-purpose
pool pumps and the adopted testing requirements applicable to these
metrics.
---------------------------------------------------------------------------
Starting on July 19, 2021, the compliance date for the energy
conservation standards that DOE established for dedicated-purpose pool
pumps, all dedicated-purpose pool pumps within the scope of those
standards must be certified in accordance with the amended subpart Y of
part 431 and the applicable sampling requirements in 10 CFR 429.59. DOE
is also requiring that, beginning on July 19, 2021, certain
certification and compliance information must be reported to DOE on an
annual basis (section III.K.2). Similarly, all representations
regarding the energy efficiency or energy use of dedicated-purpose pool
pumps within the scope of this DPPP test procedure should be made by
testing in accordance with the adopted DPPP test procedure (appendix B)
beginning 180 days after the publication date of this test procedure
final rule in the Federal Register. (42 U.S.C. 6314(d)(1)) DOE
understands that manufacturers of dedicated-purpose pool pumps likely
have historical test data (e.g., existing pump curves) that were
developed with methods consistent with the new DOE test procedure. DOE
also understands that the DPPP test procedure is based on the same
testing methodology used to generate most existing pump performance
information. Consequently, DOE does not expect that manufacturers will
need to regenerate all of the historical test data, as long as the
original rating method is consistent with the methods adopted in this
final rule, and the original tested units remain
[[Page 36862]]
representative of the basic model's current design. If the testing
methods used to generate historical ratings for DPPP basic models are
substantially different from those adopted in this final rule or the
manufacturer has changed the design of the basic model, the
representations resulting from the historical methods would no longer
be valid. This is discussed in more detail in section III.F.
III. Discussion
In this final rule, DOE amends subpart Y of 10 CFR part 431 to add
a new DPPP test procedure and related definitions, amends 10 CFR 429.59
to add a new sampling plan for dedicated-purpose pool pumps, and amends
10 CFR 429.110 and 429.134 to add new enforcement provisions for this
equipment. The amendments are shown in Table III.1.
Table III.1--Summary of Amendments in This Final Rule, Their Location Within the Code of Federal Regulations,
and the Applicable Preamble Discussion
----------------------------------------------------------------------------------------------------------------
Applicable preamble
Location Amendment Summary of additions discussion
----------------------------------------------------------------------------------------------------------------
10 CFR 429.59...................... Test Procedure Minimum number of dedicated- Section III.K and
Sampling Plan and purpose pool pumps to be III.H.
Certification tested to rate a DPPP
Requirements. basic model, determination
of representative values,
and certification
reporting requirements.
10 CFR 429.110 & 429.134........... Enforcement Provisions Method for DOE Section III.K.
determination of
compliance of DPPP basic
models.
10 CFR 431.462..................... Definitions........... Definitions pertinent to Section III.B.
categorizing and testing
of dedicated-purpose pool
pumps.
10 CFR 431.464, Appendix B, & Test Procedure........ Instructions for Sections III.C, III.D,
Appendix C. determining the WEF (and III.E, III.H, III.F,
other applicable and III.J.
performance
characteristics) for
applicable varieties of
dedicated-purpose pool
pumps and replacement DPPP
motors.
10 CFR 431.466..................... Labeling.............. Requirements for labeling Section III.I.
dedicated-purpose pool
pumps.
----------------------------------------------------------------------------------------------------------------
The following sections discuss comments received from interested
parties and DOE's final adopted provisions regarding (A) the scope of
this rulemaking; (B) definitions related to the categorizing and
testing of dedicated-purpose pool pumps; (C) the metric used to
describe the energy performance of dedicated-purpose pool pumps; (D)
the test procedure for different varieties of dedicated-purpose pool
pumps; (E) the incorporation of HI 40.6-2014 as the test method for
determining pump performance; (F) representations of energy use and
energy efficiency; (G) additional test methods necessary to determine
rated hydraulic horsepower,\7\ other DPPP horsepower metrics,\8\ and
the self-priming capability of dedicated-purpose pool pumps; (H)
labeling requirements for dedicated-purpose pool pumps; (I) an optional
test method for replacement DPPP motors; and (J) certification and
enforcement provisions for tested DPPP models.
---------------------------------------------------------------------------
\7\ Rated hydraulic horsepower refers to the hydraulic
horsepower at maximum speed and full impeller diameter on the
reference curve for the rated pump and is the metric DOE is
referencing to describe the capacity of dedicated-purpose pool
pumps. (See section III.G.1.)
\8\ DOE is adopting, based on the June 2016 DPPP Working Group
recommendations, standardized methods for determining nominal motor
horsepower, total horsepower, and service factor of a dedicated-
purpose pool pump to support labeling provisions. The adopted test
methods are discussed in section III.F and the labeling requirements
are discussed in section III.I.
---------------------------------------------------------------------------
A. General Comments
CA IOUs submitted a general comment expressing their support of the
test procedure proposed in the September 2016 DPPP test procedure NOPR
and stating that the proposal reflected issues negotiated in the DPPP
Working Group in 2015 and 2016. CA IOUs also encouraged DOE to publish
a final rule for both the test procedure and energy conservation
standards by the end of 2016 so that the standards can take effect as
soon as possible. (CA IOUs, No. 9 at pp. 1-2) DOE appreciates the
support of CA IOUs and has finalized this test procedure final rule in
2016. DOE addressed the energy conservation standards recommended by
the DPPP Working Group in the January 2017 DPPP DFR. 82 FR 5650.
In response to the September 2016 DPPP test procedure NOPR, Hayward
raised concerns on the number of requests for comment and new items
outside the DPPP Working Group discussions and the possible need for a
supplemental NOPR (SNOPR). (Hayward, Public Meeting Transcript, No. 3
at pp. 5-6) DOE acknowledges that in the September 2016 DPPP test
procedure NOPR, DOE proposed a new DPPP test procedure, as well as
several items recommended by the DPPP Working Group related to DPPP
test procedure, such as definitions and test methods. In addition, the
September 2016 DPPP test procedure NOPR contained several items
recommended by the DPPP Working Group that are not directly related to
the DPPP test procedure, such as labeling and certification
requirements. Finally, the September 2016 DPPP test procedure NOPR
contained a number of items that were not directly discussed or
recommended by the DPPP Working Group, but are necessary to fully
implement DOE's regulatory framework, such as a sampling plan for the
determination of representative values and enforcement requirements.
While DOE recognizes that the number and breadth of the proposals
contained in the September 2016 DPPP test procedure NOPR was
significant, DOE maintains that many of the items are necessary to
ensure DOE's DPPP regulations, once adopted, are comprehensive and
robust. For example, the sampling plan provisions are necessary to
describe how to determine uniform and consistent representative values
from the test procedure results.
In addition, as discussed at length in the DPPP Working Group
negotiations, the energy conservation standard recommended by the DPPP
Working Group contains both performance and prescriptive requirements
for different varieties of dedicated-purpose pool pumps, which must be
implemented in a direct final rule. However, such a direct final rule
can only contain the explicit consensus recommendations of the DPPP
Working Group, since any additional provisions would not have the
opportunity for public comment
[[Page 36863]]
through the direct final rule process. Therefore, some items typically
implemented in standards rulemakings, such as certification reporting
requirements and labeling provisions, were included in the September
2016 DPPP test procedure NOPR, because, while they implemented the
recommendations of the DPPP Working Group, they contained additional
details and minor provisions not explicitly recommended by the DPPP
Working Group (see section III.I and III.K.2 for more information on
the labeling and certification provisions, respectively).
Therefore, while DOE understands that the breadth of the proposals
contained in the September 2016 DPPP test procedure NOPR may be greater
than typical test procedure NOPRs, DOE believes that all the proposals
are necessary to fully implement the recommendations of the DPPP
Working Group and ensure comprehensive and robust DPPP regulations. In
addition, DOE notes that interested parties had the opportunity to
comment on all DOE's proposals in response to the September 2016 DPPP
test procedure NOPR and DOE has provided answers to all comments, and,
where appropriate, has amended its proposal in response to the
comments. Therefore, DOE believes that an SNOPR is not necessary.
In written comments, APSP and Pentair noted that DOE based the
various efficiency levels considered for energy conservation standards
during the DPPP Working Group negotiations on the WEF scores estimated
for individual pump models using data from the ENERGY STAR Qualified
Products List database. Pentair commented, and APSP agreed, that
analysis they conducted using actual test data generated WEF scores
that were different from DOE's estimates, sometimes by up to 20
percent. APSP and Pentair recommended that DOE reevaluate the various
efficiency levels using actual test data instead of estimates based on
ENERGY STAR data points. (APSP, No. 8 at p. 2; Pentair, No. 11 at p. 6)
DOE interprets APSP and Pentair's comments to be specific to self-
priming pool filter pumps, which are the only variety of pool pump that
are listed in the ENERGY STAR Qualified Products List database.\9\
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\9\ ENERGY STAR maintains a database of certified products,
including pool pumps. See https://www.energystar.gov/productfinder/product/certified-pool-pumps/results.
---------------------------------------------------------------------------
In response to APSP and Pentair, DOE notes that the tested data
points for all self-priming pool filter pumps were based on
certification data from the ENERGY STAR Qualified Products List
database, as well as other entities besides ENERGY STAR. DOE
incorporated certification data from the CEC (including current and
historical data), APSP, and ENERGY STAR, and included other data
provided by DPPP manufacturers in DOE's Self-Priming Pool Filter Pump
database.\10\ (Docket No. EERE-2015-BT-STD-0008, No. 94 at pp. 24-30)
DOE presumes the data in these databases to be accurate and determined
in accordance with the appropriate test procedures. As discussed
further in section III.H, these test procedures are consistent with the
test procedure recommended by the DPPP Working Group and adopted by DOE
in this final rule. Therefore, the data in the ENERGY STAR, CEC, and
APSP databases are deemed to be consistent with data generated in
accordance with the adopted DPPP test procedure.
---------------------------------------------------------------------------
\10\ Docket No. EERE-2015-BT-STD-0008, No. 102.
---------------------------------------------------------------------------
DOE notes that WEF scores used to establish efficiency levels for
single-speed and two-speed self-priming pool filter pumps were directly
calculated from actual known test data points at appropriate load
points, and no mathematical estimations were employed. However, as
discussed in the DPPP Working Group, DOE acknowledges that, for
variable-speed self-priming pool filter pumps, the WEF scores used to
establish efficiency levels considered for energy conservation
standards were mathematically estimated from certain known test data
points contained in DOE's database. (Docket No. EERE-2015-BT-STD-0008,
No. 94 at pp. 26-31)
DOE pursued the mathematical estimation of WEF scores because the
variable-speed self-priming pool filter pump performance data contained
in above-mentioned databases does not always align with the load points
(i.e., speed settings) needed to evaluate each pump against the WEF
metric. Specifically, DOE's mathematical estimations were derived from
a regression analyses of known variable-speed self-priming pool filter
pump data points. Furthermore, as DOE described during the DPPP Working
Group meetings, DOE used actual test stand data provided by DPPP
manufacturers to validate the estimation methodology. (Docket No. EERE-
2015-BT-STD-0008, No. 94 at pp. 28-34) Ultimately, DOE publically
presented its regression methodology to the DPPP Working Group for
input and no members of the DPPP Working Group offered sustained
objections to the methodology or results during the Working Group
meetings.\11\ (Docket No. EERE-2015-BT-STD-0008, No. 94 at pp. 24-34)
---------------------------------------------------------------------------
\11\ The CA IOUs initially objected to the results of the
regression methodology, saying that previous CA IOU efforts had
gathered data that did not fit the regression trend presented by
DOE. (Docket No. EERE-2015-BT-STD-0008, CA IOUs, No. 94 at pp. 30-
31) In a subsequent meeting the CA IOUs rescinded their objection
and stated that previous CA IOUs analysis shows the same results as
DOE's regression methodology. (Docket No. EERE-2015-BT-STD-0008, CA
IOUs, No. 95 at pp. 4-5).
---------------------------------------------------------------------------
In addition, and as discussed in the DPPP Working Group, DOE
acknowledges that the estimated WEF scores for variable-speed pumps are
subject to mathematically uncertainty. As a part of the DPPP Working
Group meetings, DOE mathematically quantified this uncertainty and
provided the DPPP Working Group with a revised variable-speed
efficiency level option that would conservatively account for this
uncertainty. (Docket No. EERE-2015-BT-STD-0008, No. 100 at pp. 118-121)
Ultimately, as a part of their energy conservation standard
negotiations, the DPPP Working Group decided not to account for such
uncertainty in the variable-speed efficiency level. (Docket No. EERE-
2015-BT-STD-0008, No. 92 at pp. 281-283) Consequently, DOE believes
that the concept of WEF score uncertainty for variable-speed pumps was
well understood by the DPPP Working Group, including the commenters.
In general, DOE developed efficiency level options for the DPPP
Working Group based on the best data and analytical methods that were
available at the time. In light of the concerns raised by APSP and
Pentair, DOE reevaluated its variable-speed WEF estimation methodology,
but found no technical inaccuracies. In the absence of new data (noting
that APSP and Pentair did not submit to DOE any test data to
substantiate their claims), DOE has no means to adjust its variable-
speed WEF estimation methodology at this time. Furthermore, DOE
believes that data uncertainty concerns raised by APSP and Pentair were
sufficiently considered by the DPPP Working Group, and adjustment to
DOE's analysis, based on new test data (if made available), would not
materially impact the recommendations of the DPPP Working Group.
Therefore, DOE will not reevaluate self-priming pool filter pump
efficiency levels using new test data, as recommended by APSP and
Pentair. DOE notes that DOE established energy conservation standards
as part of the January 2017 DPPP DFR. 82 FR 5650, 5743.
In written comments, Nidec stated that it believed that there
should be a
[[Page 36864]]
public comment period for the related energy conservation standards and
requested information on the timing of the ECS rulemaking as well as
the opportunity for public review and comment. (Nidec, No. 10 at p. 4)
DOE notes that the related energy conservation standards were
negotiated through the DPPP Working Group and approved by ASRAC,\12\
and that notice of all meetings were published in the Federal
Register.\13\ All meetings were open and provided opportunity for
public comment. In addition, the public had 110 days to submit public
comments on the DFR, which were considered by DOE prior to confirming
the effective date and compliance date for the energy conservation
standards. 82 FR 24218; May 26, 2017.
---------------------------------------------------------------------------
\12\ Docket No. EERE-2013-BT-NOC-0005, No. 87.
\13\ See https://www1.eere.energy.gov/buildings/appliance_standards/standards.aspx?productid=67 and https://www.regulations.gov/docket?D=EERE-2015-BT-STD-0008.
---------------------------------------------------------------------------
B. Definitions
In this final rule, DOE is adopting definitions for the term
dedicated-purpose pool pump, several sub-varieties of dedicated-purpose
pool pumps, and the variations of DPPP operating speed configurations.
DOE is also adopting definitions pertinent to categorizing and testing
dedicated-purpose pool pumps in accordance with the DOE test procedure.
In general, ASAP and NRDC commented that they agreed with DOE's
proposed definitions. (ASAP and NRDC, No. 12 at p. 1) DOE appreciates
the support of ASAP and NRDC. DOE presents these definitions in the
subsequent sections. In addition, DOE is adopting definitions and
methods for determining several terms related to describing DPPP
capacity, including ``rated hydraulic horsepower,'' ``dedicated-purpose
pool pump nominal motor horsepower,'' ``dedicated-purpose pool pump
service factor,'' and ``dedicated-purpose pool pump motor total
horsepower.'' These terms are discussed in detail in section III.G.1.
1. Existing Pump Definitions
DOE notes that because dedicated-purpose pool pumps are a style of
pump, some terms defined at 10 CFR 431.462, as adopted in the January
2016 general pumps test procedure final rule, also apply to dedicated-
purpose pool pumps, including bare pump, mechanical equipment, driver,
and control. 81 FR 4086, 4090-4091 (Jan. 25, 2016). In addition, as
dedicated-purpose pool pumps are end suction pumps, DOE believes the
definition for end suction pump established in the January 2016 general
pumps test procedure final rule also applies to dedicated-purpose pool
pumps. In the January 2016 general pumps test procedure final rule, DOE
defined ``end suction pump'' as a single-stage, rotodynamic pump in
which the liquid enters the bare pump in a direction parallel to the
impeller shaft and on the side opposite the bare pump's driver-end. The
liquid is discharged through a volute in a plane perpendicular to the
shaft. 81 FR 4086, 4146 (Jan. 25, 2016). DOE notes that, as it is
referenced in the definition for end suction pump, the definition for
rotodynamic pump established in the January 2016 general pumps test
procedure final rule also applies to dedicated-purpose pool pumps. Id.
at 4147.
In the September 2016 DPPP test procedure NOPR, DOE used the term
``dry rotor'' as a part of the definition of pressure cleaner booster
pumps. 81 FR 64580, 64591 (Sept. 20, 2016). DOE also discussed how the
term ``dry rotor pump'' applies to dedicated-purpose pool pumps and
asserted that, to DOE's knowledge, all dedicated-purpose pool pumps are
dry rotor (as defined in the January 2016 general pumps final rule
\14\). 81 FR 64580, 64587 (Sept. 20, 2016) DOE requested comment on the
assertion that all dedicated-purpose pool pumps are dry rotor pumps.
---------------------------------------------------------------------------
\14\ DOE defines ``dry rotor pump'' as a pump in which the motor
rotor is not immersed in the pumped fluid. 10 CFR 431.462.
---------------------------------------------------------------------------
In written comments, APSP, Hayward, and Zodiac commented that all
of the dedicated-purpose pool pumps covered by this rule are typically
dry rotor pumps. (APSP, No. 8 at p.3; Hayward, No. 6 at p. 1; Zodiac,
No. 13 at p. 1) However, APSP and Zodiac also requested a clearer
definition of dry rotor and wet rotor style pumps. APSP, No. 8 at p. 3;
Zodiac, No. 13 at p. 1) APSP, Hayward, and Zodiac also inquired how a
wet rotor pump (such as a pump with a water-cooled motor) may be
impacted by the dry rotor definition. (APSP, No. 8 at p.3; Hayward, No.
6 at p. 1; Zodiac, No. 13 at p. 1)
In response to APSP and Zodiac's request for clarification
regarding the terms dry rotor and wet rotor, DOE defined dry rotor and
wet rotor pumps in the January 2016 general pumps test procedure final
rule. 81 FR 4086, 4146 (Jan. 25, 2016). Dry rotor pump means a pump in
which the motor rotor is not immersed in the pumped fluid. Conversely,
a wet rotor pump is one in which the motor rotor is immersed in the
pumped liquid. Id. at 4101 (Jan. 25, 2016) The rotor is the portion of
the motor that rotates and provides torque to output shaft (which may
be integral to the rotor). For most motors varieties, including all
known dedicated-purpose pool pump motors, the rotor is an internal
component of the motor, which resides inside the motor stator. If any
significant amount of liquid is present in-between the stator and rotor
during operation, the rotation of the motor rotor will cause the liquid
to surround or cover the rotor (i.e., immerse it). Consequently, such a
configuration would be considered a wet rotor pump. Alternatively, if a
dedicated-purpose pool pump has no significant amount of liquid between
stator and rotor, the rotation of the rotation will not cause the
liquid to surround or cover the rotor (i.e., immerse it), and thus such
a configuration would not be considered a dry rotor pump. DOE notes
that the water-resistance of, or ability to immerse, the exterior
casing of a motor has no relation to the definition of wet rotor and
dry rotor pump.
DOE believes these definitions are clear and unambiguous and do not
require further clarification.
Regarding how a wet rotor pump would be treated under DOE's new
dedicated-purpose pool pump regulations, DOE understands that pressure
cleaner booster pumps are the only variety of dedicated-purpose pool
pump that use the term ``dry rotor'' within the definition (i.e., a
pressure cleaner booster pump is a dry rotor pump). Consequently, the
test procedure will only be applicable to dry rotor pressure cleaner
booster pumps, as non-dry rotor variants would not meet the definition
of a pressure cleaner booster pump. The remaining varieties of
dedicated purpose pool pumps make no specification to whether the pump
is, or is not, dry rotor. Consequently, both dry rotor and non-dry
rotor pumps will meet certain definitions established in this final
rule, and would thus be subject to the test procedure.
DOE received no other comments regarding the use of dry rotor,
within the definition of pressure cleaner booster pump. Therefore, the
term dry rotor pump will remain a part of the definition of pressure
cleaner booster pump.
Additional definitions from the January 2016 general pumps test
procedure final rule that apply to dedicated-purpose pool pumps,
include the definition of basic model (discussed further in section
III.B.8), the definitions incorporated by reference from HI 40.6-2014
(discussed further in section III.E.1), and the definition of self-
priming pump (discussed further in section III.B.3.a). While other
terms may be applicable to the description of
[[Page 36865]]
dedicated-purpose pool pumps, they are not referenced in any of the
DPPP definitions or specifications of the DPPP test procedure.
2. Definition of Dedicated-Purpose Pool Pump
Consistent with the recommendations of the DPPP Working Group, DOE
proposed in the September 2016 DPPP test procedure NOPR to define
dedicated-purpose pool pump as follows:
Dedicated-purpose pool pump comprises self-priming pool filter
pumps, non-self-priming pool filter pumps, waterfall pumps, pressure
cleaner booster pumps, integral sand-filter pool pumps, integral-
cartridge filter pool pumps, storable electric spa pumps, and rigid
electric spa pumps. 81 FR 64580, 64587 (Sept. 20, 2016).
DOE received no comments in response to the proposed definition of
dedicated-purpose pool pump. Therefore, DOE is adopting the definition
of dedicated-purpose pool pump as proposed in the September 2016 DPPP
test procedure NOPR.
In the September 2016 DPPP test procedure NOPR, DOE also proposed
definitions for each DPPP variety based on DPPP Working Group
recommendations. These definitions are discussed in more detail in
sections III.B.3, III.B.4, and III.B.5.
3. Pool Filter Pumps
Pool filter pumps are the most common style of dedicated-purpose
pool pump. A ``pool filter pump'' or ``pool circulation pump'' is
typically used to refer to an end suction style pump that circulates
water through a pool and filtration system and removes large debris
using a basket strainer or other device. Consistent with the
recommendations of the DPPP Working Group, in the September 2016 DPPP
test procedure NOPR, DOE proposed to define pool filter pump as an end
suction pump that
(a) either:
(1) Includes an integrated basket strainer, or
(2) does not include an integrated basket strainer, but requires a
basket strainer for operation, as stated in manufacturer literature
provided with the pump; and
(b) may be distributed in commerce connected to, or packaged with,
a sand filter, removable cartridge filter, or other filtration
accessory, so long as the filtration accessory is connected with
consumer-removable connections that allow the pump to be plumbed to
bypass the filtration accessory. (Docket No. EERE-2015-BT-STD-0008, No.
51 Recommendation #4 at pp. 2-3); 81 FR 64580, 64587 (Sept. 20, 2016).
In the September 2016 DPPP test procedure NOPR, DOE requested
comment on the proposed definition of pool filter pump. No comments,
negative or positive, were received regarding the proposed definition
of pool filter pump. Therefore, in this final rule, DOE adopts the
definition of pool filter pump as proposed in the September 2016 DPPP
test procedure NOPR.
a. Definition of a Basket Strainer and Filtration Accessories
The definition of pool filter pump includes the use of a basket
strainer to differentiate pool filter pumps from other varieties of end
suction pumps. To clearly and unambiguously establish what would be
considered a basket strainer when applying the pool filter pump
definition, the DPPP Working Group recommended to define ``basket
strainer'' as ``a perforated or otherwise porous receptacle that
prevents solid debris from entering a pump, when mounted within a
housing on the suction side of a pump. The basket strainer receptacle
is capable of passing spherical solids of 1 mm in diameter, and can be
removed by hand or using only simple tools. Simple tools include but
are not limited to a screwdriver, pliers, and an open-ended wrench.''
(Docket No. EERE-2015-BT-STD-0008, No. 51 Recommendation #4 at pp. 2-3)
To establish what would be considered a ``removable cartridge
filter'' and to differentiate removable cartridge filters from basket
strainers, the DPPP Working Group recommended that the definitions of
basket strainer and removable cartridge filter include a specification
for the diameter of spherical solid that the basket strainer or filter
component is capable of passing. The DPPP Working Group recommended a
definition for ``removable cartridge filter'' as ``a filter component
with fixed dimensions that captures and removes suspended particles
from water flowing through the unit. The removable cartridge filter is
not capable of passing spherical solids of 1 mm in diameter, can be
removed from the filter housing by hand or using only simple tools, and
is not a sand filter. Simple tools include but are not limited to a
screwdriver, pliers, and an open-ended wrench.'' (Docket No. EERE-2015-
BT-STD-0008, No. 51 Recommendation #4 at pp. 2-3)
Similarly, to clearly differentiate sand filters from other
filtration apparatuses, such as basket strainers and removable
cartridge filters, the DPPP Working Group recommended defining ``sand
filter'' as ``a device designed to filter water through sand or an
alternate sand-type media.'' The definition for sand filter is intended
to include all depth filters that allow fluid to pass through while
retaining particulates and debris in a porous filtration medium. In the
DPPP equipment industry, such a filter is most commonly made with sand,
but could also be made with other media such as diatomaceous earth.
(Docket No. EERE-2015-BT-STD-0008, No. 58 at pp. 91-96)
In the September 2016 DPPP test procedure NOPR, DOE noted that
these definitions are useful in clearly differentiating different
styles of pool filter pumps, including integral cartridge-filter and
sand-filter pool pumps, from those that have non-integral filtration
accessories. As such, DOE proposed adopting the definitions for basket
strainer, removable cartridge filter, and sand filter, as recommended
by the DPPP Working Group. 81 FR 64580; 64587-88 (Sept. 20, 2016).
In response to the proposed definition of basket strainer, Pentair
submitted a written comment stating that there is a possibility of
manufacturers using the 1mm size restriction as a loophole to create a
strainer basket with very small openings, which would not meet DOE's
definition for pool filter pumps. Pentair acknowledged that doing so
would significantly limit the utility of the pump in pool filtration
applications. However, Pentair noted that consumers could throw away
the original basket strainer and replace it with one that has more
reasonable opening size. (Pentair, No. 11 at p. 1)
In response, DOE acknowledges Pentair's concern regarding the
potential for manufacturers to circumvent the regulation through
adjusting the opening size on the basket strainer. In the DPPP Working
Group negotiations, the DPPP Working Group discussed the opening size
as the clearest and most unambiguous way to differentiate between
basket strainers and removable cartridge filters. During that
discussion, Hayward raised the possibility that the filter basket
opening size may limit future design flexibility. DOE responded that
DOE definitions and analysis are developed around filter basket designs
that are currently available on the market. DOE also noted that a
filtration apparatus that does not meet the definition established in
this rule could be considered in a future rulemakings, if such designs
are developed. (Docket No. EERE-2015-BT-STD-0008, CA IOUs, DOE,
Waterway, and Zodiac, No. 53 at pp. 13-19) Also, as noted by Pentair,
the opening size of the basket filter directly impacts its utility as a
[[Page 36866]]
filtration device. Therefore, DOE believes that the market will
effectively discourage manufacturers from producing pool filter pumps
with ineffective basket filters. However, DOE will monitor the market
as this test procedure and associated energy conservation standards
take effect and, if DOE observes any such circumvention, DOE may
reconsider the definition of basket strainer as necessary.
DOE received no other comments related to the proposed definitions
of basket strainer, removable cartridge filter, or sand filter.
Therefore, DOE is adopting the definitions of these terms as proposed
in the September 2016 DPPP test procedure NOPR.
b. Self-Priming and Non-Self-Priming Pool Filter Pumps
All pool filter pumps on the market are either self-priming or non-
self-priming. Self-priming pumps are able to lift liquid that
originates below the centerline of the pump inlet and, after initial
manual priming, are able to subsequently re-prime without the use of
external vacuum sources, manual filling, or a foot valve. In contrast,
non-self-priming pumps must be manually primed prior to start up each
time. Accordingly, self-priming pumps are constructed in a different
manner than non-self-priming pumps and have different energy use
characteristics. Specifically, self-priming pool filter pumps typically
incorporate a diffuser that maintains the prime on the pump between
periods of operation. The diffuser affects the energy performance of
the pump because it can decrease the maximum achievable energy
efficiency.
In addition, whether a pool filter pump is self-priming or not also
impacts the typical applications for self-priming versus non-self-
priming pool filter pumps. Specifically, in the DPPP equipment
industry, self-priming pool filter pumps are often referred to as
``inground pool pumps'' and non-self-priming pool filter pumps are
often referred to as ``aboveground pool pumps.'' Accordingly, the DPPP
Working Group proposed to analyze self-priming and non-self-priming
pool filter pumps separately. (Docket No. EERE-2015-BT-STD-0008, No. 51
Recommendation #2A at p. 2)
In the September 2016 DPPP test procedure NOPR, based on feedback
from the DPPP Working Group, DOE proposed definitions for self-priming
and non-self-priming pool filter pumps, as well as a method to
differentiate the two. Specifically, in the September 2016 DPPP test
procedure NOPR, DOE proposed the following definitions for self-priming
and non-self-priming pool filter pumps:
Self-priming pool filter pump means a pool filter pump that is
certified under NSF/ANSI 50-2015 \15\ to be self-priming or is capable
of re-priming to a vertical lift of at least 5.0 feet with a true
priming time less than or equal to 10.0 minutes, when tested in
accordance with NSF/ANSI 50-2015, and is not a waterfall pump.
---------------------------------------------------------------------------
\15\ NSF International (NSF)/ANSI Standard 50-2015, (``NSF/ANSI
50-2015''), ``Equipment for Swimming Pools, Spas, hot Tubs and Other
Recreational Water Facilities.''
---------------------------------------------------------------------------
Non-self-priming pool filter pump means a pool filter pump that is
not certified under NSF/ANSI 50-2015 to be self-priming and is not
capable of re-priming to a vertical lift of at least 5.0 feet with a
true priming time less than or equal to 10.0 minutes, when tested in
accordance with NSF/ANSI 50-2015, and is not a waterfall pump. 81 FR
64580, 64647-68 (Sept. 20, 2016).
The definitions are consistent with the NSF/ANSI 50-2015 self-
priming designation such that any pumps certified as self-priming under
NSF/ANSI 50-2015 would be treated as self-priming pool filter pumps
under the DOE regulations, even if such a pump was certified based on
manufacturer's specified or recommended vertical lift and/or true
priming time. However, as certification with NSF/ANSI 50-2015 is
voluntary, the definitions also adopt specific criteria in terms of
vertical lift and true priming time that are applicable to any pool
filter pumps not certified as self-priming under NSF/ANSI 50-2015. The
criterion for vertical lift is specified as 5.0 feet, consistent with
the NSF/ANSI 50-2015 requirement. This ensures that all pool filter
pumps that can achieve a vertical lift of 5.0 feet (within the required
true priming time), whether they are certified with NSF/ANSI or not,
would be considered a self-priming pool filter pump under DOE's
regulations.
The criterion for true priming time recommended by the DPPP Working
Group and proposed in the September 2016 DPPP test procedure NOPR is
10.0 minutes, as opposed to the 6 minutes specified in NSF/ANSI 50-
2015. 81 FR 64580, 64589 and 64647 (Sept. 20, 2016). This is because
the 6 minute threshold is a minimum, and manufacturers believed that
some pool filter pumps that are currently considered self-priming pool
filter pumps in the industry have true priming times greater than 6
minutes. Thus, the DPPP Working Group believed that 10.0 minutes was
more appropriate and comprehensive. 81 FR 64580, 64589 (Sept. 20,
2016). DOE proposed a vertical lift and true priming time of 5.0 feet
and 10.0 minutes in order to clearly specify the appropriate and
required level of precision in the definitions and test method. Id.
DOE notes that these definitions rely on the NSF/ANSI 50-2015 test
method to determine self-priming capability. DOE's test procedure for
determining self-priming capability, including the incorporation by
reference of the NSF/ANSI 50-2015 test method, is discussed further in
section III.G.2.
The definitions proposed for self-priming and non-self-priming pool
filter pumps in the September 2016 DPPP test procedure NOPR also
explicitly exclude waterfall pumps. As discussed in section III.B.4.a,
waterfall pumps are pool filter pumps and could meet a definition of
either self-priming or non-self-priming, unless explicitly excluded
from those definitions. Because DOE intended for these pumps to be
treated specifically as waterfall pumps, the proposed definitions for
self-priming and non-self-priming pool filter pumps both specifically
excluded waterfall pumps.
DOE notes that, in the January 2016 general pumps test procedure
final rule, DOE already defined the term ``self-priming pump'' as a
pump that (1) is designed to lift liquid that originates below the
centerline of the pump inlet; (2) contains at least one internal
recirculation passage; and (3) requires a manual filling of the pump
casing prior to initial start-up, but is able to re-prime after the
initial start-up without the use of external vacuum sources, manual
filling, or a foot valve. 81 FR 4086, 4147 (Jan. 25, 2016). However, in
the September 2016 DPPP test procedure NOPR, DOE discussed how this
definition is not applicable to dedicated-purpose pool pumps because
pool filter pumps typically do not contain a recirculation passage to
accomplish the self-priming function. Therefore, DOE proposed to revise
the definition of self-priming pump to ensure the definition of self-
priming is comprehensive and consistent with the new definitions for
self-priming and non-self-priming pool filter pump. Specifically, DOE
proposed in the September 2016 DPPP test procedure NOPR to modify the
existing definition of self-priming pump to also include self-priming
pool filter pumps, in addition to the other referenced criteria. 81 FR
64580, 64648 (Sept. 20, 2016).
In response to DOE's proposal, CEC commented in support of DOE's
proposal to differentiate self-priming from non-self-priming pool pumps
[[Page 36867]]
using the NSF/ANSI 50-2015. (CEC, No. 7 at p.2)
During the September 2016 public meeting, Hayward requested
clarification of the reference to NSF/ANSI 50-2015 asking if changes
are made to that standard, would manufacturers be bound to those
changes. (Hayward, Public Meeting Transcript, No. 3 at p. 20) As stated
during the September 2016 public meeting, DOE incorporates by reference
a specific edition of a specific standard. If that standard is updated,
DOE would need to update the reference within their test procedure.
Until such an update is made, manufacturers are held to the standard
adopted in the DOE test procedure.
Hayward also submitted a written comment in response to DOE's
proposed definition of self-priming and non-self-priming pool filter
pumps. Hayward recommended that DOE remove the requirement to test
whether a non-self-priming pump is capable of self-priming. Hayward
stated that requiring pumps not marketed or sold as self-priming pumps
to be tested for self-priming capability would be unnecessarily
burdensome. Hayward recommended that the definition of non-self-priming
pumps be revised to designate pumps that are ``not marketed or sold as
self-priming,'' rather than pumps that are not capable of self-priming.
(Hayward, No. 6 at p.1)
In response to Hayward's inquiry, DOE clarifies that manufacturers
may certify their pump models to DOE as non-self-priming without
testing, so long as manufacturers are certain that the non-self-priming
pump model has vertical lift (of lack thereof) and true priming time
characteristics consistent with DOE's definition of non-self-priming
pool filter pump. That is, the non-self-priming pump would meet the
definition of non-self-priming, if it were to be tested in accordance
with DOE's test method for verifying self-priming capability (see
section III.G.2). Consequently, manufacturers are not required to
actually test each non-self-priming pump model to prove that such a
pump is non-self-priming. However, DOE will use the definition of non-
self-priming pool filter pump and the additional test method described
in section III.G.2 to ensure that manufacturers are properly
categorizing their pool filter pumps as either self-priming or non-
self-priming in accordance with the adopted definitions. Consequently,
DOE believes that the definition of non-self-priming pool filter pumps
does not introduce any additional testing burden, as DOE believes that
manufacturers already know whether their pumps currently marketed as
``non-self-priming'' would meet the definition established in this
final rule. With no additional burden, DOE believes that amending the
definition of non-self-priming pool filter pumps is not warranted. In
addition, DOE notes that establishing a clear, quantitative threshold
to differentiate self-priming and non-self-priming pool filter pumps is
important to confirm that the pumps are appropriately differentiated
based on the utility (i.e., self-priming capability) they are able to
provide.
Hayward also requested clarification regarding the definition of
self-priming pool filter pumps. APSP and Hayward asked if 10 minutes is
the maximum time allowed to reach prime and meet the self-priming
requirement. (APSP, No. 8 at p. 3; Hayward, No. 6 at p.1)
The proposed definition for a self-priming pool filter pump allows
manufacturers to meet the definition of self-priming pool filter pump
in one of two ways. Manufacturers may show that a pool filter pump is
self-priming by certifying the pool filter pump as self-priming in
accordance with NSF/ANSI 50-2015. Alternatively, manufacturers may show
that a pool filter pump is a self-priming pool filter pump by
demonstrating that a pump is capable of re-priming to a vertical lift
of at least 5.0 feet with a true priming time of less than or equal to
10.0 minutes, without certifying the pump to NSF/ANSI 50-2015. 81 FR
64580, 64589. The NSF/ANSI 50-2015 standard does not specify a maximum
true priming time. Section C.3.5 of NSF/ANSI 50-2015 states that, ``if
a pump is to be designated as self-priming, the true priming time for
each run shall not exceed 6 min or the manufacturer's recommended time,
whichever is greater.'' To certify a pump's self-priming capability
under NSF/ANSI 50-2015, a manufacturer could recommend a true priming
time greater than 10.0 minutes. Under the proposed definition of self-
priming pool filter pump, if a pool filter pump has true priming time
greater than 10.0 minutes but is certified as self-priming under NSF/
ANSI 50-2015, that pump would qualify as a self-priming pool filter
pump. However, if the pump is not certified under NSF/ANSI 50-2015, the
pump must be capable of re-priming to a vertical lift of 5.0 feet with
a true priming time of less than or equal to 10.0 minutes in order to
be classified as a self-priming pump.
In written comments, Pentair pointed out that NSF requires pumps to
prime to 10 feet in order to be classified as ``self-priming'' without
listing a qualifying height, but allows a product to be certified as
self-priming in the 5 to 10 foot range if accompanied by a qualifying
height and time to prime. Pentair added that DOE's proposal does not
require the listing of the qualifying height and suggested that the
definition of self-priming pump should reflect the non-qualified
definition of 10 feet. (Pentair, No. 11 at p. 1)
Pentair also disagreed with DOE's attempt to separate dedicated-
purpose pool pumps intended for aboveground and inground applications
by using non-self-priming and self-priming characteristics,
respectively. Specifically, Pentair argued that there are many self-
priming aboveground pumps currently in the market that would become
non-viable under DOE's proposed definitions. Pentair further notes that
while modifications could be made to these existing aboveground pumps
to prevent them from priming, such changes would negatively impact pump
efficiency and reduce energy savings for this category of non-self-
priming pumps. (Pentair, No. 11 at p. 2)
In response to Pentair's comments regarding DOE's specified
vertical lift of 5.0 feet, DOE recommended the vertical lift of 5.0
feet based on the discussions and recommendation of the DPPP Working
Group. (Docket No. EERE-2015-BT-STD-0008, Hayward, No. 79 at pp. 160;
Zodiac, No. 79 at pp. 161-162) DOE notes that, as mentioned previously,
this ensures that all pool filter pumps that can achieve a vertical
lift of 5.0 feet (within the required true priming time), whether they
are certified with NSF/ANSI or not, would be considered a self-priming
pool filter pump under DOE's regulations. DOE reviewed NSF/ANSI 50-2015
and notes that, contrary to Pentair's comment, section 6.9.1 of NSF/
ANSI 50-2015 requires that the maximum vertical lift be specified if
the pump is designated as self-priming, as determined in accordance
with section C.3 of NSF/ANSI 50-2015. NSF/ANSI 50-2015 does not appear
to provide the discretion indicated by Pentair if the vertical lift is
10 feet. In this final rule, DOE is adopting a definition specifying a
vertical lift of 5.0 feet, as proposed in the September 2016 DPPP test
procedure NOPR, to maintain consistency with NSF/ANSI 50-2015.
In response to Pentair's comments regarding the differentiation of
self-priming and non-self-priming pool filter pumps, DOE proposed to
differentiate these two styles of pool filter pumps based on the
recommendations of the DPPP Working Group. (Docket No. EERE-2015-BT-
STD-0008, No. 51 Recommendation #2A at p. 2) DOE acknowledges that one
factor associated
[[Page 36868]]
with the differentiation of self-priming and non-self-priming pool
filter pumps is their ability to service inground pools. That is, the
capability of a pump to self-prime is a fundamental utility associated
with the ability of a pump to service an inground pool, as the pump is
typically installed on the ground next to the pool, above the water
line of the pool. Therefore, the pump must be self-priming in order to
reliably circulate water on a continual basis. Conversely, pumps
serving aboveground pools are typically installed below the water line
and, therefore, gravity can serve to maintain the prime in the pump.
Although pumps serving aboveground pools could be self-priming or non-
self-priming, self-priming pumps do not provide the same utility to
aboveground pools because they require modifications that reduce the
energy efficiency benefits that self-priming pumps provide. Non-self-
priming pumps do not require those modifications, which benefits the
consumer and provides a distinct utility to the end user. This utility
is a feature that allows DOE to separate the two styles of pumps into
distinct equipment classes. In addition, self-priming pumps are more
efficient than non-self-priming pumps, and merging the product classes
could result in the unavailability of the feature that non-self-priming
pumps provide. For these reasons, consistent with the recommendations
of the DPPP Working Group, in this final rule DOE adopts definitions of
non-self-priming and self-priming pool filter pumps based on their
capability to self-prime.
DOE received no other comments related to the proposed definitions
for self-priming and non-self-priming pool filter pumps or the revision
to the definition of self-priming pump established in the January 2016
general pumps test procedure final rule. However, in reviewing the
definitions, DOE notes that the vertical lift and true priming time
should refer to the DOE test method to verifying self-priming
capability, which DOE is adopting in this final rule (see section
III.G.2) as opposed to the test method in NSF/ANSI 50-2015. As
discussed in section III.G.2, DOE's test method for verifying self-
priming capability incorporates by reference the test method in section
C.3 of NSF/ANSI 50-2015, but also adds several clarifications and
additions to improve the repeatability and consistency of the test. DOE
believes this is consistent with the DPPP Working Group's intent,
whereby a self-priming pool filter pump would either be certified with
NSF/ANSI 50-2015 or have the specified vertical lift and true priming
time. DOE's self-priming capability test method is designed to verify
the criteria established by the DPPP Working Group. Therefore, in this
final rule, DOE is adopting definitions for self-priming and non-self-
priming pool filter pumps based on certification with NSF/ANSI 50-2015
and the criteria recommended by the DPPP Working Group, as tested
pursuant to the DOE test procedure, with minor modifications regarding
the level of precision required by the criteria. DOE is also adopting
the changes proposed to the definition of self-priming pump to align
with the new definitions for self-priming and non-self-priming pool
filter pumps.
c. Integral Cartridge-Filter and Integral Sand-Filter Pool Pumps
Most self-priming and non-self-priming filter pumps are installed
in permanent inground or aboveground pools. However, a significant
market also exists for temporary pools; e.g., inflatable or collapsible
pools that can be deflated or collapsed when not in use. Although
temporary pools also require dedicated-purpose pool pumps to circulate
and filter the water, these pools are typically served by a unique
style of dedicated-purpose pool pump that is exclusively distributed in
commerce with a temporary pool or as a replacement pump for such a
pool. Some of these pumps are integrally and permanently mounted to a
filtration accessory such as an integral cartridge-filter or sand-
filter. These particular pumps can only be operated with the integral
filtration accessory inline--the filtration accessory cannot be plumbed
out for the purposes of testing. The DPPP Working Group recommended
establishing prescriptive requirements for these pumps, which requires
that timers be distributed in commerce with the pumps. (Docket No.
EERE-2015-BT-STD-0008, No. 51, Recommendation #2B at pp. 1-2) With a
prescriptive standard, the performance-related metric (i.e., WEF) and
test procedure would not be necessary and, therefore, not applicable.
To clearly differentiate integral cartridge-filter and integral
sand-filter pool pumps from other varieties of dedicated-purpose pool
pumps, the DPPP Working Group recommended definitions for integral
cartridge-filter pool pump and integral sand-filter pool pump. The
recommended definitions create differentiation based on the physical
construction of the pump. (Docket No. EERE-2015-BT-STD-0008, No. 51
Recommendation #4 at pp. 2-3) In the September 2016 DPPP test procedure
NOPR, DOE proposed to adopt the definitions for integral cartridge-
filter pool pump and integral sand-filter pool pump recommended by the
DPPP Working Group, with a few minor changes to use consistent
terminology in both definitions. Specifically, DOE proposed the
following definitions for integral cartridge-filter pool pump and
integral sand-filter pool pump:
Integral cartridge-filter pool pump means a pump that requires a
removable cartridge filter, installed on the suction side of the pump,
for operation; and the cartridge filter cannot be bypassed.
Integral sand-filter pool pump means a pump distributed in commerce
with a sand filter that cannot be bypassed. 81 FR 64580, 64590 (Sept.
20, 2016).
APSP stated that the proposed definitions for integral cartridge-
filter pool pump and integral sand-filter pool pump are acceptable and
consistent with DPPP Working Group meetings. (APSP, No. 8 at p. 3) DOE
appreciates APSP's comment. DOE received no other comments related to
the proposed definitions for integral cartridge-filter pool pump and
integral sand-filter pool pump. Therefore, DOE is adopting the
definitions as proposed in the September 2016 DPPP test procedure NOPR.
4. Other Varieties of Dedicated-Purpose Pool Pumps
In addition to pool filter pumps, DOE identified varieties of
dedicated-purpose pool pumps that are used to drive auxiliary pool
equipment such as pool cleaners and water features. These pumps, which
include waterfall pumps and pressure cleaner booster pumps, are
discussed in greater detail in the following sections.
a. Waterfall Pumps
Within the pool pump industry, a certain variety of pump exists,
which is specifically intended to pump water for water features, such
as waterfalls. These pumps are similar in construction to pool filter
pumps, except that they only have limited head and speed operating
ranges. DOE refers to these pumps as waterfall pumps. Waterfall pumps
meet the definition of pool filter pump discussed in section III.B.3.a,
but are always equipped with a lower speed motor (approximately 1,800
rpm) in order to provide the specific high flow, low head
characteristics required for typical water feature applications. Based
on this unique construction and end user utility, the DPPP Working
Group recommended to differentiate waterfall pumps from self-priming
and non-self-priming pool filter pumps. (Docket No. EERE-2015-BT-STD-
0008, No. 51
[[Page 36869]]
Recommendation #4 at pp. 2-4) In accordance with the intent of the
December 2015 DPPP Working Group's recommendation, DOE proposed in the
September 2016 DPPP test procedure NOPR to define waterfall pump as ``a
pool filter pump with maximum head less than or equal to 30 feet, and a
maximum speed less than or equal to 1,800 rpm.'' 81 FR 64580, 64590
(Sept. 20, 2016). This definition uses maximum head and a specific
maximum speed to distinguish waterfall pumps from other varieties of
pool filter pumps.
During the September 2016 DPPP test procedure NOPR public meeting,
Pentair pointed out that there was a minor typo on page 81 FR 64590
regarding the description of waterfall pumps. Pentair noted that the
text read ``the DPPP Working Group agreed that all currently available
waterfall pumps utilize 4-pole motors, as their low flow requirements
do not necessitate the use of a higher speed 2-pole motor'' where it
should actually refer to their low head requirements, not low flow
requirements. (Pentair, Public Meeting Transcript, No. 3 at p. 74) APSP
and Pentair reiterated this point in their written comments, pointing
out that it is the low head requirements that make use of a higher
speed 2-pole motor unnecessary. (APSP, No. 8 at p. 2; Pentair, No. 11
at p. 5) DOE agrees with APSP and Pentair that the statement should
refer to the low head requirements of waterfall pumps and that the
preamble text in the NOPR was in error.
DOE received no other comments related to the proposed definition
of waterfall pump. Therefore, DOE is adopting the definition of
waterfall pump as proposed in the September 2016 DPPP test procedure
NOPR, with the clarification that the maximum head value is the value
certified to DOE.
b. Pressure Cleaner Booster Pumps
Pressure cleaner booster pumps provide water pressure that is used
to propel pressure-side pool cleaners along the bottom of the pool and
remove debris as the cleaner moves. To perform this task, a pressure
cleaner booster pump must provide high head (i.e., pressure) at a low
flow.
The DPPP Working Group recommended that pressure cleaner booster
pumps be included as a variety of dedicated-purpose pool pump, subject
to the test procedure, and specifically considered in the analysis to
support potential energy conservation standards. (Docket No. EERE-2015-
BT-STD-0008, No. 51, Recommendation #1 at p. 1, #2A at p. 2, and #6 at
p. 5) However, the DPPP Working Group did not recommend a definition of
pressure cleaner booster pump due to the difficulty of effectively
differentiating pressure cleaner booster pumps from other DPPP
varieties. (Docket No. EERE-2015-BT-STD-0008, No. 51 Recommendation #4
at p. 3) Instead, the DPPP Working Group recommended that DOE develop
an appropriate definition.
After considering the design, construction, and performance of
pressure cleaner booster pumps, DOE determined that the most effective
differentiator for pressure cleaner booster pumps is the fact that they
are designed and marketed for a specific pressure-side cleaning
application. Therefore, to effectively differentiate pressure cleaner
booster pumps from other pump varieties, DOE proposed in the September
2016 DPPP test procedure NOPR to define ``pressure cleaner booster
pump'' as an end suction, dry rotor pump designed and marketed for
pressure-side pool cleaner applications, and which may be UL listed
under ANSI/UL 1081-2014, ``Standard for Swimming Pool Pumps, Filters,
and Chlorinators.'' 81 FR 64580, 65491-92 (Sept. 20, 2016).
In response to definition of pressure cleaner booster pump proposed
in the September 2016 DPPP test procedure NOPR, the CA IOUs suggested
that DOE should include the UL listing as a requirement rather than an
illustrative characteristic. CA IOUs justified this suggestion, by
reasoning that in order to be used on pools, most local inspection
authorities would want to see the UL label. (CA IOUs, Public Meeting
Transcript, No. 3 at pp. 18-19) Conversely, in written comments,
Hayward, APSP, and Zodiac asserted that the phrase ``be UL listed''
should not be included in the definition of pressure cleaner booster
pump as it would require a manufacturer to work solely with UL and that
DOE should not seek to require manufacturers to list pressure cleaner
booster pumps in accordance with a 3rd party, voluntary standard.
(Hayward, No. 6, at p. 2; APSP, No. 8 at p. 3; Zodiac, No. 13 at pp. 1-
2) Hayward, APSP, and Zodiac further questioned the benefit of adding a
statement referencing the UL standard since, while UL 1081 is the de
facto standard and is applicable to all DPPP, it is not a requirement
in the United States to certify products to the standard and it does
not necessarily distinguish a pressure cleaner booster pump from a non-
pressure cleaner booster pump. (Id.)
As noted during the September 2016 DPPP test procedure NOPR public
meeting, DOE does not wish to narrow or restrict the definition of
pressure cleaner booster pump to only those pumps UL listed under ANSI/
UL 1081, because DOE is not fully confident that all pressure cleaner
booster pumps require such a listing in order to be installed in all
pools in the United States. This understanding is consistent with
Hayward, APSP, and Zodiac's written comments suggesting removing the
reference to ANSI/UL 1081 certification. Therefore, because it is
possible that some jurisdictions may not require such a listing, DOE
does not wish to limit the definition of pressure cleaner booster pump
to pumps with a UL listing if the pump is in fact designed and marketed
for pressure-side pool cleaner applications. However, DOE agrees with
CA IOUs that the majority of jurisdictions require UL listing for
installation of dedicated-purpose pool pumps, including pressure
cleaner booster pumps, in pools. This is why DOE believes that such
listing is a useful characteristic to use for distinguishing pressure
cleaner booster pumps from other end suction pumps not intended for
pools. While helpful, this reference does not require pressure cleaner
booster pumps to be certified with UL or any other 3rd party entity.
The controlling criteria for determining whether a pump meets DOE's
definition of pressure cleaner booster pump is whether that pump is
designed and marketed for pressure-side cleaner applications. As such,
DOE believes that referencing ANSI/UL 1081 certification continues to
be a useful, illustrative indicator for identifying pressure cleaner
booster pumps, although it is not mandatory and pressure cleaner
booster pumps may still meet the definition regardless of whether they
are certified under ANSI/UL 1081 or not. That is, DOE believes the
intended application of the pump, as indicated by the pump's own
marketing literature, is the best indication of whether or not that
pump is a pressure cleaner booster pump, regardless of whether the pump
is UL listed under ANSI/UL 1081.
APSP, Hayward, and Zodiac also pointed out in their written
comments that the current edition of ANSI/UL 1081 is the 2016 version
of the standard, not the 2014 version proposed to be incorporated by
reference in the September 2016 DPPP test procedure NOPR. (APSP, No. 8
at p.3; Hayward, No. 6 at pp. 1-2; Zodiac, No. 13 at pp. 1-2) DOE has
reviewed ANSI/UL 1081-2016 and finds it to be similar in content and
intent to the 2014 edition of the standard. Therefore, in order to
reference the most recent and relevant version, DOE is incorporating by
[[Page 36870]]
reference ANSI/UL 1081-2016 in this final rule.
No other comments were received related to the proposed definition
of pressure cleaner booster pump. Therefore, for the reasons discussed
in this section and the September 2016 DPPP test procedure NOPR, DOE is
adopting the definition of pressure cleaner booster pump as proposed in
the September 2016 DPPP test procedure NOPR, except the adopted
definition references ANSI/UL 1081-2016 instead of ANSI/UL 1081-2014.
To provide clarity and remove ambiguity when applying the
definition for pressure cleaner booster pump, DOE also proposed a
definition for ``designed and marketed'' that DOE would use when
determining the applicability of any DPPP test procedure or energy
conservation standards to such pumps. Specifically, DOE proposed to
define ``designed and marketed'' as meaning that the equipment is
specifically designed to fulfill the indicated application and, when
distributed in commerce, is designated and marketed for that
application, with the designation on the packaging and all publicly
available documents (e.g., product literature, catalogs, and packaging
labels). 81 FR 64580, 64647 (Sept. 20, 2016).
In response to this proposal, CA IOUs expressed concern that the
inclusion of ``designed and marketed'' in the definition of pressure
cleaner booster pump could create a loophole where products could be
used as pressure cleaner booster pumps even if not specifically
marketed for that purpose and, in turn, avoid regulation. (CA IOUs,
Public Meeting Transcript, No. 3 at pp. 23-24) ASAP also commented that
the proposed definition for designed and marketed seemed to be narrow,
pointing to a scenario where a pump is designed as a booster pump for
pool applications but is also marketed by the manufacturer for another
application. ASAP requested clarification if in this scenario the pump
in question would be required to meet the standard. (ASAP, Public
Meeting Transcript, No. 3 at pp. 22-23) In written comments, ASAP and
NRDC also encouraged DOE to attempt to ensure that the definition for
``designed and marketed'' does not contain any loopholes. Specifically,
ASAP and NRDC supported the definition of designed and marketed
presented in the regulatory text portion of the September 2016 DPPP
test procedure NOPR over the one presented in the preamble.\16\
Additionally, ASAP and NRDC encouraged DOE to consider whether removing
the word ``specifically'' may further reduce the possibility for
potential loopholes and suggested removing the word ``all'' from ``all
publicly available documents'' to ensure pumps are considered pressure
cleaner booster pumps in cases where the designation is on some
publicly available documents, but not others. (ASAP and NRDC, No. 12 at
pp. 1-2) Similarly, CA IOUs recommended that DOE remove the word
``specifically,'' in order to address pumps designed for both pressure
cleaner and domestic water booster pump applications, and change
``all'' to ``any'' publicly available documents. (CA IOUs, No. 9 at pp.
2-3)
---------------------------------------------------------------------------
\16\ The definition of designed and marketed contained in the
preamble (81 FR 64580, 6464592; Sept. 20, 2016) did not exactly
match the definition of designed and marketed proposed in the
regulatory text (Id. at 64647). Specifically, the preamble
definition contained the words ``exclusively'' and ``solely.''
---------------------------------------------------------------------------
In response to CA IOUs' concern about pumps used as pressure
cleaner booster pumps but not marketed as such, DOE acknowledges that
some individuals may attempt to use inappropriate pumps to run
pressure-side cleaner applications. However, it is DOE's understanding
that pressure-side pool cleaners are designed to be paired with pumps
with specific characteristics (e.g., high head and low flow) and that
manufacturers all design and market specific pumps intended for this
application. DOE also notes that pumps without these specific
characteristics would not provide adequate utility in the pressure-side
pool application and manufacturers would recommend against the use of
such pumps with their pressure-side cleaners. Therefore, while DOE
acknowledges the concern of CA IOUs, DOE cannot control the actions of
installers who may select inappropriate pumps for pressure-side cleaner
applications, and DOE believes that all pumps appropriate for pressure-
side pool cleaner applications are currently specifically designed and
marketed as such. DOE will continue to monitor the market to ensure
that this continues to be the case and that all pumps appropriate for
pressure-side pool cleaner applications continue to be characterized as
pressure cleaner booster pumps in the future.
In response to the concerns of ASAP, NRDC, and CA IOUs regarding
the applicability of the designed and marketed definition to pumps that
may be marketed for a variety of applications, in addition to pressure-
side pool cleaner applications, DOE agrees with the commenters.
Specifically, all pumps designed and marketed for pressure-cleaner
booster applications should be treated as pressure cleaner booster
pumps, regardless of any other applications for which they may be
designed and marketed. DOE acknowledges that the definition of designed
and marketed that was presented in the preamble of the September 2016
DPPP test procedure NOPR (81 FR 64580, 64592) was slightly different
than that contained in the proposed regulatory text (Id. at 64647) and
may have created confusion regarding the applicability of the designed
and marketed definition. Specifically, in the preamble, DOE discussed
defining the term designed and marketed as meaning that the equipment
is exclusively designed to fulfill the indicated application and, when
distributed in commerce, is designated and marketed solely for that
application, with the designation on the packaging and all publicly
available documents (e.g., product literature, catalogs, and packaging
labels). Id. DOE notes that the definition presented in the preamble
was incorrect and the definition presented in the regulatory text on
page 64647 of the NOPR was the intended definition. DOE believes that
the definition contained in the regulatory text, which does not refer
to the exclusivity of the design or that the equipment would be solely
marketed for a specific purpose, is broader and inclusive of pumps that
would be designed and marketed for pressure-side cleaner applications
in addition to other applications. However, DOE agrees with ASAP, NRDC,
and CA IOUs, that removal of the term ``specifically'' would help
clarify this aspect of the definition. In addition, DOE agrees that
changing from ``all publicly available documents'' to ``any publicly
available documents'' best fulfills the intent of the definition, as
any marketing of a pump as a pressure cleaner booster pump would show
that the pump is intended to be treated as a pressure cleaner booster
pump.
Therefore, DOE is defining the term ``designed and marketed'' as
set forth in the regulatory text of this rule.
5. Storable and Rigid Electric Spa Pumps
In addition to swimming pools, dedicated-purpose pool pumps are
also used in spas to circulate and filter the water and operate water
jets. Similar to swimming pools, spas can range in size and
construction style. Specifically, spas can be portable or permanent
installations and can be constructed out of a variety of materials
depending on the installation.
[[Page 36871]]
Permanent, inground spas are typically constructed similar to small
inground pools and use the same pumps (i.e., self-priming pool filter
pumps described in section III.B.3.a) to operate the spa. Conversely,
for portable spas, a specific-purpose pump is typically distributed in
commerce with the portable spa that is specifically designed and
marketed for portable electric spa applications only. Such portable
electric spa applications can be further differentiated into two
general categories: Storable electric spas and rigid electric spas. A
storable electric spa refers to an inflatable or otherwise temporary
spa that can be collapsed or compacted into a storable unit. In
contrast, a rigid electric spa is constructed with rigid, typically
more durable, materials and cannot be collapsed or compacted for
storage.
In the September 2016 DPPP test procedure NOPR, consistent with the
recommendations of the DPPP Working Group (Docket No. EERE-2015-BT-STD-
0008, No. 51 Recommendation #4 at p. 3), DOE proposed definitions for
``storable electric spa pump'' and ``rigid electric spa pump'' to
effectively differentiate them from other varieties of pumps.
Specifically, DOE proposed to define ``storable electric spa pump'' as
a pump that is distributed in commerce with one or more of the
following: (1) An integral heater and (2) an integral air pump. DOE
also proposed to define ``rigid electric spa pump'' as an end suction
pump that does not contain an integrated basket strainer or require a
basket strainer for operation as stated in the manufacturer literature
provided with the pump, and meets the following three criteria: (1) Is
assembled with four through bolts that hold the motor rear endplate,
rear bearing, rotor, front bearing, front endplate, and the bare pump
together as an integral unit; (2) is constructed with buttress threads
at the inlet and discharge of the bare pump; and (3) uses a casing or
volute and connections constructed of a non-metallic material. 81 FR
64580, 64592-93 (Sept. 20, 2016).
DOE received no comments negative or positive related to the
proposed definitions for storable electric spa pump and rigid electric
spa pump. Therefore, DOE is adopting the definitions for these terms as
proposed in the September 2016 DPPP test procedure NOPR.
In addition, DOE notes that the definitions for storable electric
spa pump, as well as the definitions for integral cartridge-filter pool
pump and integral sand-filter pool pump (see section III.B.3.c), all
utilize the term ``integral'' as part of the definition. In support of
these definitions, the DPPP Working Group recommended a definition for
integral. (Docket No. EERE-2015-BT-STD-0008, No. 51 Recommendation #4
at p. 7) In the September 2016 DPPP test procedure NOPR, DOE proposed
the definition recommended by the DPPP Working Group and proposed
defining the term ``integral'' as a part of the device that cannot be
removed without compromising the device's function or destroying the
physical integrity of the unit. 81 FR 64580, 64592-93 (Sept. 20, 2016).
DOE received no comments related to the proposed definition of the
term ``integral.'' Therefore, DOE is adopting the definition for
integral as proposed in the September 2016 DPPP test procedure NOPR.
6. Applicability of Test Procedure Based on Pump Configuration
In addition to specific definitions, the DPPP Working Group also
discussed and provided recommendations pertinent to the scope of
applicability of the DPPP test procedure. Ultimately, the DPPP Working
Group recommended that the scope of the test procedure be limited to
only the following specific varieties of dedicated-purpose pool pumps:
Self-priming pool filter pumps,
non-self-priming pool filter pumps,
waterfall pumps, and
pressure cleaner booster pumps.
(Docket No. EERE-2015-BT-STD-0008, No. 51, Recommendations #1, #2A,
and #2B at pp. 1-2; Recommendation #6 at p. 5)
In addition, although not included in the December 2015 DPPP
Working Group recommendations, the DPPP Working Group discussed and
ultimately recommended not considering a test procedure or standards
for self-priming and non-self-priming pool filter pumps with a rated
hydraulic horsepower \17\ greater than 2.5 hp. (Docket No. EERE-2015-
BT-STD-0008, No. 79 at pp. 33-54)
---------------------------------------------------------------------------
\17\ See section III.G.1 for a discussion of determination of
rated hydraulic horsepower.
---------------------------------------------------------------------------
The DPPP Working Group also recommended that the test procedure and
reporting requirements be applicable to all self-priming pool filter
pumps--both those served by single-phase power and those served by
three-phase power.\18\ (Docket No. EERE-2015-BT-STD-0008, No. 82
Recommendations #3 at p. 2) Consistent with the DPPP Working Group
recommendations, DOE proposed in the September 2016 DPPP test procedure
NOPR that the test procedure, sampling requirements, labeling, and
related provisions for dedicated-purpose pool pumps apply to all self-
priming pool filter pumps and non-self-priming pool filter pumps less
than 2.5 rated hydraulic horsepower, as well as waterfall pumps and
pressure cleaner booster pumps, regardless of the phase of the supplied
power with which they are intended to be used. 81 FR 64580, 64593
(Sept. 20, 2016).
---------------------------------------------------------------------------
\18\ The Working Group recommended that the scope of standards
for self-priming pool filter pumps only apply to self-priming pool
filter pumps served by single-phase power, while the recommended
test procedure and reporting requirements would still be applicable
to all self-priming pool filter pumps--both those served by single-
phase power and those served by three-phase power.
---------------------------------------------------------------------------
Consistent with the December 2015 DPPP Working Group
recommendations, in the September 2016 DPPP test procedure NOPR, DOE
also proposed definitions for rigid-electric and storable-electric spa
pumps as a variety of dedicated-purpose pool pump in this test
procedure final rule, but DOE did not propose test procedures or
reporting requirements for them.
In the September 2016 DPPP test procedure NOPR, DOE also
specifically proposed to exclude submersible pumps from the scope of
the DPPP test procedure and proposed defining a ``submersible pump'' as
a pump that is designed to be operated with the motor and bare pump
fully submerged in the pumped liquid. 81 FR 64580, 64594 (Sept. 20,
2016).
In written comments, CEC expressed support of DOE's proposal to set
the scope of the test procedure rulemaking to include self-priming and
non-self-priming pool filter pumps, waterfall pool pumps, and pressure
cleaner booster pumps. (CEC, No. 7 at p. 2) DOE appreciates CEC's
support.
In response to DOE's proposal regarding the applicability of the
proposed test procedure to dedicated-purpose pool pumps served by both
single- and three-phase power, Hayward and APSP requested clarification
as to the scope of the rule and specifically if it included three-phase
dedicated-purpose pool pumps. (Hayward, No. 6 at p. 4; APSP, No. 8 at
p. 5) Nidec supported the DPPP Working Group's recommendation that any
potential energy conservation standards would only apply to dedicated-
purpose pool pumps served by single-phase power. However, Nidec
recommended that the test procedure and reporting requirements only
apply to dedicated-purpose pool pumps served by single-phase power.
Nidec stated that three-
[[Page 36872]]
phase motors used with dedicated-purpose pool pumps are very energy
efficient and are already regulated. Nidec suggested that three-phase
dedicated-purpose pool pumps and related motors should not need further
testing nor reporting requirements. (Nidec, No. 10 at p. 3)
In response to Hayward and APSP's request for clarification, DOE
clarifies that, as noted previously and discussed in the September 2016
DPPP test procedure NOPR, DOE's proposed test procedure would apply to
self-priming pool filter pumps and non-self-priming pool filter pumps
less than 2.5 rated hydraulic horsepower, as well as waterfall pumps
and pressure cleaner booster pumps, served by both single-phase power
or three-phase power. In response to Nidec's comments regarding the
applicability of the proposed DOE test procedure to three-phase
equipment, DOE believes that the applicability of the DPPP test
procedure proposed in the September 2016 DPPP test procedure NOPR is
consistent with the intent of the DPPP Working Group exhibited in the
June 2016 DPPP Working Group recommendations, where the Working Group
recommended that the test procedure and reporting requirements would be
applicable to all self-priming pool filter pumps served by single- and
three-phase power. (Docket No. EERE-2015-BT-STD-0008, No. 82,
Recommendation #3 at p. 2) Although the June 2016 DPPP Working Group
recommendations reference only self-priming pool filter pumps, there is
no reason why DOE's proposed DPPP test procedure would not be
applicable to other varieties of dedicated-purpose pool pumps served by
single- or three-phase power. In addition, the DPPP Working Group did
not recommend restricting the scope of standards for any of the other
DPPP varieties based on the phase of power with which it is intended to
be used. However, DOE agrees with Nidec that three-phase motors may
already be regulated under existing DOE test procedures and energy
conservation standards for electric motors and small electric motors.
As discussed further in section III.G.1.b, in this final rule, DOE is
limiting the test methods for motor horsepower metrics (i.e., DPPP
nominal motor horsepower, DPPP service factor, and DPPP motor total
horsepower) to single-phase motors because testing and rating of three-
phase motors is already regulated by DOE.
DOE agrees that, as stated by Nidec, the applicability of the DPPP
test procedure and standards recommended by the DPPP Working Group
differ slightly with respect to dedicated-purpose pool pumps that are
supplied by single-phase versus three-phase power. Specifically, the
DPPP Working Group recommended that the scope of standards for self-
priming pool filter pumps only apply to self-priming pool filter pumps
served by single-phase power, while the recommended test procedure and
reporting requirements would still be applicable to all self-priming
pool filter pumps--both those served by single-phase power and those
served by three-phase power. (Docket No. EERE-2015-BT-STD-0008, No. 82
Recommendations #3 at p. 2)
In response to the scope of test procedure and metric applicability
proposed by DOE in the September 2016 DPPP test procedure NOPR, Pentair
and APSP commented that some form of differentiation or exclusion
should be established for dedicated-purpose pool pumps with nominal
motor horsepower greater than 3 hp. Pentair suggested that the metric,
as proposed in the NOPR, potentially limits a manufacturer's ability to
develop an optimal solution for these lower head hydraulic systems,
because these pumps are typically applied to pools with larger plumbing
and do not typically operate on curve C. Pentair claimed that as a
result, these larger pumps will be eliminated from the market.
(Pentair, No. 11, at p. 2; APSP, No 8 at pp. 3-4)
As discussed previously in this section, the DPPP Working Group, of
which Pentair was a member, recommended that the scope of the test
procedure be limited to self- and non-self-priming pool filter pumps,
waterfall pumps, and pressure cleaner booster pumps. (Docket No. EERE-
2015-BT-STD-0008, No. 51, Recommendations #1, #2A, and #2B at pp. 1-2;
Recommendation #6 at p. 5) In the December 2015 DPPP Working Group
recommendations, the DPPP Working Group discussed and ultimately
recommended not considering a test procedure or standards for self-
priming and non-self-priming pool filter pumps with a rated hydraulic
horsepower greater than 2.5 hp. (Docket No. EERE-2015-BT-STD-0008, No.
79 at pp. 33-54) However, the DPPP Working Group did not recommend any
other test procedure differentiation or exclusions based on nominal
motor horsepower, nor did the DPPP Working Group ask DOE to pursue such
action. Therefore, the test procedure and standards recommended by the
DPPP Working Group were intended to be applicable to self-priming and
non-self-priming pool filter pumps with rated hydraulic horsepower less
than or equal to 2.5 hp, which include some pool filter pumps with a
nominal motor horsepower greater than 3 hp,\19\ which are typically
installed into applications with larger plumbing, for which the test
procedure would not be representative. (Docket No. EERE-2015-BT-STD-
0008, No. 94 at pp. 38-53; Docket No. EERE-2015-BT-STD-0008, No. 95 at
pp. 176-194; Docket No. EERE-2015-BT-STD-0008, No. 79 at pp. 39-40, 47-
48) In response to Pentair and APSP, DOE notes that Pentair and APSP
did not introduce any new data indicating that the cutoff should
actually be a nominal motor horsepower of 3 hp; rather they simply
indicated this was due to larger plumbing systems not on curve C, which
the Working Group already considered in making its cutoff selection.
Finally, the introduction of an exclusion for pumps with greater than 3
nominal motor horsepower opens a significant circumvention loophole
risk. For example, manufacturers of pumps with 3 nominal motor
horsepower could decide to slightly increase the capacity of the motor
(with no change to the bare pump), in order to avoid being subject the
test procedure and energy conservation standards. Such a change on
nominal horsepower would have little impact on the utility or
production cost of such a pump. Alternatively, any change to a pump's
hydraulic horsepower rating will directly impact end-user utility
(i.e., flow and head). Consequently, DOE reaffirms its conclusion that
hydraulic horsepower, rather than motor horsepower, should be used to
define the upper scope limit, as hydraulic horsepower is more directly
tied to end-user utility (i.e., flow and head) than motor horsepower.
For these reasons, DOE is not adopting an alternative scope limitation
in this final rule.
---------------------------------------------------------------------------
\19\ Nominal motor horsepower is approximately equivalent to the
rated hydraulic horsepower divided by the pump efficiency and the
motor efficiency of the dedicated-purpose pool pump.
---------------------------------------------------------------------------
DOE did not receive any other comments regarding the definition of
submersible pump, or the general scope of applicability of the
September 2016 DPPP test procedure NOPR. Consequently, in this final
rule, DOE is adopting test methods for all self-priming pool filter
pumps and non-self-priming pool filter pumps less than 2.5 rated
hydraulic horsepower, as well as waterfall pumps and pressure cleaner
booster pumps, including pumps served by both single- and three-phase
power, with the exclusion of submersible pumps. The specific test
methods for each of the applicable DPPP varieties are discussed in more
detail in section III.D.
[[Page 36873]]
7. Definitions Related to Dedicated-Purpose Pool Pump Speed
Configurations and Controls
In addition to definitions of dedicated-purpose pool pump and the
specific DPPP varieties, DOE also proposed in the September 2016 DPPP
test procedure NOPR to establish definitions to further differentiate
certain varieties of dedicated-purpose pool pumps, based on the speed
configuration of the motor and/or the presence of controls on the DPPP
model as distributed in commerce. These definitions are discussed in
section III.B.7.a. For dedicated-purpose pool pumps distributed in
commerce with applicable pool pump controls, DOE also proposed a
definition for ``freeze protection controls.'' This is discussed in
section III.B.7.b.
a. DPPP Speed Configurations
In the June 2016 DPPP Working Group recommendations, the DPPP
Working Group recommended definitions for the following DPPP speed
configurations: Single-speed, two-speed, multi-speed, and variable-
speed. (Docket No. EERE-2015-BT-STD-0008, No. 82, Recommendation #5A at
p. 3) In the September 2016 DPPP test procedure NOPR, DOE proposed
adopting the DPPP Working Group's recommended definitions with a few
minor modifications for clarity and consistency. 81 FR 64580, 64594-97
(Sept. 20, 2016). Specifically, DOE proposed the following definitions
for single-speed, two-speed, multi-speed, and variable-speed dedicated-
purpose pool pump:
Single-speed dedicated-purpose pool pump means a
dedicated-purpose pool pump that is capable of operating at only one
speed.
Two-speed dedicated-purpose pool pump means a dedicated-
purpose pool pump that is capable of operating at only two different
pre-determined operating speeds, where the low operating speed is less
than or equal to half of the maximum operating speed and greater than
zero, and must be distributed in commerce either: (1) With a pool pump
control (i.e., variable speed drive and user interface or switch) that
is capable of changing the speed in response to user preferences; or
(2) Without a pool pump control that has the capability to change speed
in response to user preferences, but without which the pump is unable
to operate without the presence of such a pool pump control.
Multi-speed dedicated-purpose pool pump means a dedicated-
purpose pool pump that is capable of operating at more than two
discrete pre-determined operating speeds separated by speed increments
greater than 100 rpm, where the lowest speed is less than or equal to
half of the maximum operating speed and greater than zero, and must be
distributed in commerce with an on-board pool pump control (i.e.,
variable speed drive and user interface or programmable switch) that
changes the speed in response to pre-programmed user preferences and
allows the user to select the duration of each speed and/or the on/off
times.
Variable-speed dedicated-purpose pool pump means a
dedicated-purpose pool pump that is capable of operating at a variety
of user-determined speeds, where all the speeds are separated by at
most 100 rpm increments over the operating range and the lowest
operating speed is less than or equal to one-third of the maximum
operating speed and greater than zero. Such a pump must include a
variable speed drive and be distributed in commerce either: (1) With a
user interface that changes the speed in response to pre-programmed
user preferences and allows the user to select the duration of each
speed and/or the on/off times; or (2) without a user interface but be
unable to operate without the presence of a user interface.
81 FR 64580, 64647-48 (Sept. 20, 2016).
DOE's proposed definitions enable each speed configuration to be
identified based on (1) the number of operating speeds available to the
pump; (2) the minimum operating speed, or turn-down ratio,\20\ of the
pump; (3) the pump's ability to connect to a pool pump control; and/or
(4) the characteristics of that pool pump control. The pool pump
control varieties, pool pump control operating characteristics, and
requirements regarding the inclusion of pool pump controls applicable
to each DPPP speed configuration, as proposed in the September 2016
DPPP test procedure NOPR, are summarized in Table III.2.
---------------------------------------------------------------------------
\20\ The turn-down ratio for multi-speed pumps, including two-
speed pumps, describes the ability of the pump to decrease speed
relative to the maximum operating speed and is calculated as the
maximum operating speed over the minimum operating speed of the
pump.
Table III.2--Summary of Applicable Pool Pump Control Varieties and Related Proposed Requirements for Each DPPP
Speed Configuration
----------------------------------------------------------------------------------------------------------------
Inclusion of pool pump
DPPP speed configuration definition Applicable pool pump Pool pump control must controls as distributed
control varieties be pre-programmable in commerce
----------------------------------------------------------------------------------------------------------------
Two-Speed............................ Variable speed No..................... Included.
drive and user
interface or
Switch........
Multi-Speed.......................... Variable speed Yes.................... Included and on-board.
drive and user
interface or
Switch........
Variable-Speed....................... Variable speed Yes.................... Included or DPPP model
drive and user cannot operate without
interface being installed with
such controls.
----------------------------------------------------------------------------------------------------------------
CEC, in written comments, supported DOE's proposal to establish
definitions for single-speed, two-speed, multi-speed, and variable
speed pool filter pumps. (CEC, No. 7 at p. 2) DOE appreciates the
support of CEC.
In response to DOE's proposed definitions for two-speed dedicated-
purpose pool pump, Hayward suggested a modification to the definitional
requirement that two-speed dedicated-purpose pool pumps not be able to
operate at high speed without the requisite control, instead of not
able to operate at all. That is, instead of being unable to operate
entirely, two-speed dedicated-purpose pool pumps could be allowed to
function at a default low-speed if they are operated without an
appropriate pool pump control.
[[Page 36874]]
(Hayward, Public Meeting Transcript, No. 3 at pp. 21, 26-27) In
response to Hayward's suggestion, CA IOUs stated their support for
DOE's originally proposed provision that does not allow a two-speed
dedicated-purpose pool pump be considered a two-speed pump unless it is
unable to operate without an appropriate pool pump control. (CA IOUs,
Public Meeting Transcript, No. 3 at p. 26-27)
In response to Hayward's suggestion regarding the definition of
two-speed dedicated-purpose pool pump, DOE agrees with CA IOUs that the
proposed modification is not consistent with the recommendations of the
DPPP Working Group. (Docket No. EERE-2015-BT-STD-0008, No. 82,
Recommendation #5A at p. 3) The specific wording of the DPPP speed
configuration definitions were discussed at length and in significant
detail during the DPPP Working Group negotiations and, if fact, were
part of the final negotiation of standard levels. (Docket No. EERE-
2015-BT-STD-0008, No. 91 at pp. 141-183; Docket No. EERE-2015-BT-STD-
0008, No. 92 at pp. 215-222) Specifically, certain members of the DPPP
Working Group voiced concern that if two-speed dedicated-purpose pool
pumps were distributed in commerce without any form of control and were
capable of being operated without such a control, there would be a
significant risk that such pumps would not be paired with an applicable
pool pump control in the field and would not achieve the performance
and potential energy savings represented by the WEF metric. (Docket No.
EERE-2015-BT-STD-0008, No. 91 at pp. 141-183) DOE believes that if a
two-speed dedicated-purpose pool pump is capable of operating, even at
low speed, without an applicable pool pump control, this significantly
increases the risk that two-speed pool filter pumps would be installed
and operated without an appropriate control. As the two-speed
dedicated-purpose pool pump test points presume a low flow and high
flow test point, the two-speed dedicated-purpose pool pump test
procedure is only appropriate and representative of two-speed
dedicated-purpose pool pumps with controls that enable operation at
both speeds. Therefore, to ensure that the test points and resultant
WEF metric for two-speed dedicated-purpose pool pumps is representative
of actual performance of the equipment in the field, DOE is adopting
the definition for two-speed dedicated-purpose pool pump proposed in
the September 2016 DPPP test procedure NOPR. Furthermore, DOE notes
that the two-speed dedicated-purpose pool pump definition does not
restrict DPPP manufacturers from producing a pump that has two
operating speeds and can only be operated at low speed without an
appropriate control, as described by Hayward. However, in such a case
the pump would not meet the definition of two-speed dedicated-purpose
pool pump and, therefore, would be tested and subject to standards
based on the single-speed dedicated-purpose pool pump test points. See
section D.1 for more discussion regarding the specific test points for
the different DPPP speed configurations.
In response to DOE's definition of a two-speed dedicated-purpose
pool pump, Hayward and APSP also requested clarification regarding the
meaning of the phrase ``unable to operate.'' (Hayward, No. 6 at pp. 2;
APSP, No. 8 at p. 3) DOE clarifies that the phrase ``unable to
operate'' means that the pump is non-operational and could not be used
to circulate water in a pool. That is, the pump is unable to provide
any flow or head, and consumes no energy.
Hayward and APSP also requested a better definition of the term
``pool pump control.'' Hayward and APSP both commented that the two-
speed dedicated-purpose pool pump definition includes a parenthetical
``(i.e., variable speed drive and user interface or switch)'' that
implies the only two options for a pool pump control are a switch or a
variable speed drive and user interface. (Hayward, No. 6 at pp. 2;
APSP, No. 8 at p. 3)
DOE recognizes that the use of the abbreviation ``i.e.'' \21\ was
used in error, and may have caused confusion. DOE's intent was to use
the abbreviation ``e.g.,'' \22\ which would signify that a variable
speed drive and a user interface or switch were just two examples of
possible technologies. That said, the phrase ``pool pump control'' is
not explicitly defined in this final rule and a pool pump control is
not limited to the two options used as examples. DOE interprets the
phrase ``pool pump control'' as a general term that encompasses any
technology that is capable of changing the speed in response to user
preferences. To clarify DOE's original intent, DOE has modified the
definition of two-speed dedicated-purpose pool pump to replace ``i.e.''
with ``e.g.''
---------------------------------------------------------------------------
\21\ Latin for ``id est.'' Meaning ``that is.'' https://www.merriam-webster.com/dictionary/i.e.
\22\ Latin for ``exempli gratia.'' Meaning ``for example.''
https://www.merriam-webster.com/dictionary/e.g.
---------------------------------------------------------------------------
Similarly, Davey commented that the proposed definition for
variable-speed dedicated purpose pool pumps may hinder innovation of
pump products that do not require additional controllers. For example,
Davey suggested that a dedicated-purpose pool pump, with no pool pump
control, but which enables the user to set a duration of operation at
high speed and then default to low speed operation might improve
efficiency. Davey also noted that, under the proposed definition of
variable-speed dedicated-purpose pool pump, a user could program the
pump to run at the highest speed all the time. (Davey, No. 5 at pp. 2-
3)
DOE notes that Davey's comment describes a configuration where a
pump is capable of operating at a high speed and a low speed and is
capable of programming the duration of each speed in response to user
preferences. Such a configuration would meet the proposed definition of
a two-speed dedicated-purpose pool pump. As described above, DOE
proposed that a two-speed dedicated-purpose pool pump be defined as a
dedicated-purpose pool pump that is capable of operating at only two
different, pre-determined operating speeds, where the low operating
speed is less than or equal to half of the maximum operating speed and
greater than zero, and must be distributed in commerce either: (1) With
a pool pump control (i.e., variable speed drive and user interface or
switch) that sets the speed in response to user preferences or (2)
without a pool pump control that has such capability but is unable to
operate without the presence of such a pool pump control. 81 FR 64580,
64594 (Sept. 20, 2016). As noted previously, DOE, in this final rule,
is altering the definition to refer to the variable speed drive and
user interface or switch as illustrative examples with the term
``e.g.'' and any pool pump control capable of operating in the manner
described in the definition would meet DOE's definition of two-speed
dedicated-purpose pool pump, regardless of the control's technology.
The DPPP Working Group discussed the definition of variable-speed
dedicated-purpose pool filter pumps, and took care to craft a
definition that is sufficiently broad so as to not restrict innovation.
Working Group members agreed that the definition should not specify
whether the pool pump controller is attached to or detached from the
motor, and the definition should not specify whether the control is
sold with the pump or sold separately from the pump. (Docket No. EERE-
2015-BT-STD-008, No. 91 at pp. 164-166) Based on recommendations from
[[Page 36875]]
the DPPP Working Group, DOE proposed that a variable-speed drive be
defined as equipment capable of varying the speed of the motor. 81 FR
64580, 64596 (Sept. 20, 2016) This definition is very broad, and it
only limits the available technologies to the extent that is required
to describe the utility inherent in a variable-speed dedicated purpose
pool pump. Similarly, the September 2016 DPPP test procedure NOPR
implicitly defines a user interface as a device that changes the speed
in response to pre-programmed user preferences and allows the user to
select the duration of each speed and/or the on/off times. 81 FR 64580,
64595 (Sept. 20, 2016) This definition is also broad, and is only
limited to the extent necessary to capture the required functionality
of variable-speed dedicated-purpose pool pumps. Based on these points,
DOE believes that the definition of a variable-speed dedicated-purpose
pool filter pump is sufficiently broad to allow a range of technologies
and innovative approaches, while ensuring that any such technologies
would still provide the utility of a variable-speed dedicated-purpose
pool pump consistent with the intent of the DPPP Working Group.
DOE understands that equipment covered by standards change as
manufacturers add new features to their products and update their
designs. DOE will monitor the DPPP market for changes in equipment and
technology. In the future, DOE may amend the definitions of any of DPPP
varieties or speed configurations, or include new varieties of
dedicated-purpose pool pumps, if necessary. In the meantime,
manufacturers may apply for a test procedure waiver if they develop a
pump that meets the intent of the variable-speed DPPP definition but
does not meet all of the definition's criteria. In general, any
interested party may submit a petition for a test procedure waiver for
a basic model of a covered product if the basic model's design prevents
it from being tested according to the test procedures or cause the
prescribed test procedures to evaluate the basic model in a manner so
unrepresentative of its true energy consumption characteristics as to
provide materially inaccurate comparative data. Additional details on
the petition for waiver process are available at 10 CFR 431.401 and at
https://energy.gov/eere/buildings/test-procedure-waivers.
In addition, in reviewing the proposed definitions, DOE also
noticed that the proposed definition for two-speed dedicated-purpose
pool pump was grammatically incorrect. In this final rule, DOE is
correcting the grammatical error, which does not affect the intent or
substance of the definition. Specifically, the proposed definition
contained the final clause ``but without which the pump is unable to
operate without the presence of such a pool pump control,'' which this
final rule adopts as modified to read ``but is unable to operate
without the presence of such a pool pump control'' in this final rule.
Similarly, in reviewing the variable-speed DPPP definition, DOE
noticed that the last phrase refers generically to a ``user interface''
when it is intended to refer to a user interface with specific
characteristics and capabilities, as referenced in the previous clause
in the definition. Therefore, in this final rule, DOE is modifying the
definition to clarify that the definition is, in all places, referring
to a user interface that changes the speed in response to pre-
programmed user preferences and allows the user to select the duration
of each speed and/or the on/off times. This ensures that the two
clauses in the definition are mutually exclusive. DOE is also updated
the terminology in the second clause to be grammatically correct,
consistent with the definition of two-speed dedicated-purpose pool
pump. That is, DOE adopts a definition with the final clause in the
definition to read ``without a user interface that changes the speed in
response to pre-programmed user preferences and allows the user to
select the duration of each speed and/or the on/off times, but is
unable to operate without the presence of a user interface.''
In addition to proposing definitions of the various DPPP speed
configurations, in the September 2016 DPPP test procedure NOPR, DOE
proposed to define variable-speed drive to mean equipment capable of
varying the speed of the motor. 81 FR 64580, 64594-64597 (Sept. 20,
2016). This definition was intended to clarify and support the proposed
definitions for two-speed, multi-speed, and variable-speed dedicated-
purpose pool pump.
DOE received no comments regarding the proposed definition of
variable-speed drive. Therefore, DOE is adopting the definition for
variable speed drive as proposed in the September 2016 DPPP test
procedure NOPR.
b. Freeze Protection Controls
DPPP Working Group recommended additional prescriptive requirements
for dedicated-purpose pool pumps distributed in commerce with ``freeze
protection controls.'' (Docket No. EERE-2015-BT-STD-0008, No. 82,
Recommendation #6A at p. 4). Freeze protection controls are controls
that, at a certain ambient temperature, turn on the dedicated-purpose
pool pump to circulate water for a period of time to prevent the pool
and water in plumbing from freezing. These prescriptive freeze control
requirements are discussed in section III.H.
To identify dedicated-purpose pool pumps with freeze protection
controls, DOE proposed in the September 2016 DPPP test procedure NOPR
to define freeze protection controls as pool pump controls that, at a
certain ambient temperature, turn on the dedicated-purpose pool pump to
circulate water for a period of time to prevent the pool and water in
plumbing from freezing. 81 FR 64580, 64597 (Sept. 20, 2016).
DOE received no comments related to the proposed definition of
freeze protection controls. Therefore, DOE is adopting the definition
of freeze protection controls as proposed in the September 2016 DPPP
test procedure NOPR. DOE did receive comments related to the proposed
test method for verifying the presence and operation of freeze
protection controls, which are discussed in section III.K.3.
8. Basic Model
For purposes of certification, compliance, and enforcement, DOE
generally applies its energy conservation standards to ``basic models''
of consumer products and commercial and industrial equipment. For the
purposes of applying the DPPP regulations, DOE proposed in the
September 2016 DPPP test procedure NOPR to define what constitutes a
``basic model'' of a dedicated-purpose pool pump. 81 FR 64580, 64597
(Sept. 20, 2016). Applying this basic model concept allows
manufacturers to group similar models within a basic model to minimize
testing burden, while ensuring that key variables that differentiate
DPPP energy performance and/or utility are maintained as separate basic
models.
In the September 2016 DPPP test procedure NOPR, DOE proposed
adopting only the provisions of the current pump basic model definition
that are applicable to dedicated-purpose pool pumps, which includes all
units of a given product or equipment type (or class thereof)
manufactured by one manufacturer, having the same primary energy
source, and having essentially identical electrical, physical, and
functional (or hydraulic) characteristics that affect energy
consumption, energy efficiency, water consumption, or water efficiency.
81 FR 64580, 64597 (Sept. 20, 2016). Procedurally, to apply the basic
model concept to dedicated-
[[Page 36876]]
purpose pool pumps, DOE proposed to amend the definition of ``basic
model'' for pumps that currently exists at 10 CFR 431.462, as
established in the January 2016 general pumps test procedure final rule
to also accommodate dedicated-purpose pool pumps. 81 FR 4086 (Jan. 25,
2016). The current pumps basic model definition contains several
specific accommodations regarding number of stages for multistage pumps
and trimmed impellers and is applicable only to those general pumps
that were the subject of the January 2016 general pumps test procedure
final rule. Consequently, DOE proposed amending the definition to
clarify that the multistage pump and trimmed impeller provisions were
only applicable to pumps subject to the test procedure established in
the January 2016 general pumps test procedure final rule. 81 FR 64580,
64597 (Sept. 20, 2016).
In response to DOE's proposed definition of basic model for
dedicated-purpose pool pumps, DOE received several comments regarding
how different individual models could be grouped under the basic model
provisions. Waterway commented that sometimes a single individual model
has identical functional characteristics to several other individual
models, and asked whether such individual models may be grouped within
the basic model. (Waterway, Public Meeting Transcript, No. 3 at p. 95)
In response to Waterway's comment, as discussed in the September
2016 DPPP test procedure NOPR public meeting, models that have
identical electrical, physical, and functional (or hydraulic)
characteristics that affect energy consumption, energy efficiency,
water consumption, or water efficiency, fall within the same basic
model for the purposes of DOE certification, even if they have
different unique model numbers in the manufacturer's catalogue. In such
a case, a manufacturer would just list all the unique individual model
numbers to which a given basic model certification applied in the
certification report submitted to DOE. (See section III.K.2 for more
information on certification reporting requirements.)
Pentair expressed concern regarding using a basic model in
certifying products to DOE, stating that, in the ENERGY STAR database,
when models are grouped under a single certification, utilities often
do not recognize models that do not appear in the main column listing
the basic models. Pentair stated that this makes it necessary to list
each unit separately in the ENERGY STAR database, even if the
performance is similar. (Pentair, Public Meeting Transcript, No. 3 at
pp. 32-33)
In response to Pentair's comment, DOE notes that it is at the
manufacturer's discretion to group individual models into a single
basic model to reduce testing and certification burden or to test and
certify each individual model as a unique basic model. Regardless of
whether a manufacturer chooses to group individual models into a basic
model for purposes of certification, the manufacturer would still be
required to specify in its certification the individual model numbers
that fall within the basic model certified, and any representations
regarding an individual model made in a certification report must be
consistent with representation as to that individual model made to
ENERGY STAR.
Hayward inquired if the same wet end is used within a family, but
the horsepower of the motor and impeller size changes, such individual
models could be grouped within the same basic model. (Hayward, Public
Meeting Transcript, No. 3 at pp. 31-32) Hayward and APSP also requested
clarity on the verbiage of the definition as well as examples from
other products. Hayward and APSP asked whether the same product but
with a different name or label for specific customers would be the same
``basic model.'' Finally, Hayward and APSP requested elaboration on
whether a single or multi-stage pump within the same performance
category and WEF criteria are considered within the same basic model.
(Hayward, No. 6 at p. 2; APSP, No.8 at p. 4)
In response to Hayward and APSP's inquiry, DOE notes that,
consistent with DOE's practice with other products and equipment, DPPP
manufacturers may elect to group individual pump models that are
similar, but not identical, into the same basic model to reduce testing
burden, provided all representations regarding the energy use of pumps
within that basic model are identical and based on the most consumptive
unit. See 76 FR 12422, 12423 (March 7, 2011).\23\ However, all
individual models represented by the same basic model must be in the
same equipment class.\24\ DOE notes that because standards recommended
by the DPPP Working Group in the June 2016 DPPP Working Group
recommendations and adopted by DOE in the January 2017 DPPP DFR
differentiate and assign different standards to dedicated-purpose pool
pumps based on their rated hydraulic horsepower, this limits the
ability of manufacturers to group individual DPPP models that vary in
capacity. (Docket No. EERE-2015-BT-STD-0008, Recommendation #1, No. 82
at p. 1; 82 FR 5650, 5743) DOE agrees with Hayward and APSP that a
product with different names or labels that is otherwise the same could
be grouped within a basic model. Examples from other products and
equipment include appliances with varying finishes grouped into one
basic model; refrigerators with varying door opening sides grouped into
one basic model, or air conditioners of varying voltages grouped into
one basic model. DOE notes that the example related to all stage
versions of a multi-stage pump being required to be in the same basic
model is a specific requirement for general pumps that DOE does not
apply to dedicated-purpose pool pumps.
---------------------------------------------------------------------------
\23\ These provisions allow manufacturers to group individual
models with essentially identical, but not exactly the same, energy
performance characteristics into a basic model to reduce testing
burden. Under DOE's certification requirements, all the individual
models within a basic model identified in a certification report as
being the same basic model must have the same certified efficiency
rating and use the same test data underlying the certified rating.
The compliance, certification, and enforcement (CCE) final rule also
establishes that the efficiency rating of a basic model must be
based on the least efficient or most energy consuming individual
model (i.e., put another way, all individual models within a basic
model must be at least as energy efficient as the certified rating).
76 FR at 12428-29 (March 7, 2011).
\24\ DOE believes this is what Hayward is referring to in their
comment when they refer to ``performance category and WEF
criteria.''
---------------------------------------------------------------------------
No additional comments were received pertaining to DOE's proposal
to adopt the general provisions of the general pumps basic model
definition. Therefore, DOE is adopting the changes to the definition of
basic model in 10 CFR 431.462, as proposed in the September 2016 DPPP
test procedure NOPR.
C. Rating Metric
Overall, the key objectives of any DPPP metric are that it (1) be
objectively measurable, (2) be representative of the energy use or
energy efficiency of dedicated-purpose pool pumps, (3) provide an
equitable differentiation of performance among different DPPP models
and technologies, (4) be able to compare the energy efficiency of a
given DPPP model to a minimum standard level, and (5) provide the
necessary and sufficient information for purchasers to make informed
decisions regarding DPPP selection.
As described in the September 2016 DPPP test procedure NOPR, the
DPPP Working Group focused on defining a performance-based metric that
is similar to the energy factor (EF) metric currently used to describe
DPPP
[[Page 36877]]
performance by many existing programs,\25\ but that also accounts for
the potential energy savings of equipment with multiple operating
speeds. 81 FR 64580, 64597-64601 (Sept. 20, 2016). Ultimately, the DPPP
Working Group recommended using the WEF, which is defined as the ratio
of the volumetric flow provided by the pump, divided by the input power
to the pump, at one or more load points, where these load points are
selected depending on the specific DPPP variety and speed
configuration, as shown in equation (1). The specific load points and
weights for each DPPP variety are discussed in section III.D.
---------------------------------------------------------------------------
\25\ As described in the September 2016 DPPP TP NOPR, EF is used
by California Title 20, APSP, and ENERGY STAR to describe DPPP
performance. 81 FR 64580, 64598-64600 (Sept. 20, 2016).
[GRAPHIC] [TIFF OMITTED] TR07AU17.000
---------------------------------------------------------------------------
Where:
WEF = weighted energy factor in kgal/kWh;
wi = weighting factor at each load point i;
Qi = flow at each load point i in gpm;
Pi = input power to the motor (or controls, if present)
at each load point i in W;
i = load point(s), defined uniquely for each DPPP variety; and
n = number of load point(s), defined uniquely for each speed
configuration.
(Docket No. EERE-2015-BT-STD-0008, No. 51 Recommendation #5 at p. 4)
DOE agrees with the DPPP Working Group that the recommended WEF
metric, as shown in equation (1), provides a representative, objective,
and informative characterization of DPPP performance. Consequently, in
the September 2016 DPPP test procedure NOPR, DOE proposed to adopt the
WEF metric as the performance-based metric for representing the energy
performance of certain styles of dedicated-purpose pool pumps.
In the September 2016 DPPP test procedure NOPR, DOE requested
feedback on the proposed metric. CEC stated in written comments that
CEC supported DOE's proposal to establish a weighted energy factor
metric. (CEC, No. 7 at p. 2)
APSP and Hayward commented that they believe that equation (1) in
the September 2016 DPPP test procedure NOPR (81 FR 64580, 64600),\26\
which is used to determine WEF, does not correctly result in the
weighting of energy factors at the specified load points. (APSP, No. 8
at p. 4; Hayward, No. 6 at pp. 2-3) Instead, APSP and Hayward proposed
using the following equation (2), with all variables as defined
previously:
---------------------------------------------------------------------------
\26\ Equation (1) in the September 2016 DPPP TP NOPR is
identical to equation (1) in this document.
[GRAPHIC] [TIFF OMITTED] TR07AU17.001
DOE responds that equation (1), as published in the September 2016
DPPP test procedure NOPR, correctly describes the efficiency of DPPP
equipment and aligns with the recommendation of the DPPP Working Group.
(Docket No. EERE-2015-BT-STD-0008, No. 51, Recommendation #5 at p. 4)
DOE notes that the DPPP Working Group evaluated both methods of
calculating WEF, both the proposed equation (1) and equation (2), as
recommended by APSP and Hayward. (Docket No. EERE-2015-BT-STD-0008 No.
49 at pp. 6-9; Docket No. EERE-2015-BT-STD-0008 No. 56 at pp. 24-60)
The DPPP Working Group ultimately chose to use equation (1) because it
is more representative of the energy savings to the customer. (Docket
No. EERE-2015-STD-0008 No. 50 at p. 3) Equation (2) is a weighting of
the EF values, which results in an exaggeration of the benefits of
multi-speed and variable-speed technologies, while equation (1) is a
ratio of the amount of water pumped over the amount of energy consumed
over a given period of time in real-world applications. (Docket No.
EERE-2015-BT-STD-0008 No. 56 at pp. 29, 38, 60) That is,
mathematically, weighting the EF values directly, as shown in equation
(2), results in a weighted average of the flow values in the numerator,
but equal weighting of the denominator values, meaning the flow at high
speed is given more weight than the associated power value at high
speed. To illustrate this, the calculation of WEF, with both equations,
for a two-speed, multi-speed, or variable-speed dedicated-purpose pool
pump with both a low speed and high speed test point is shown in
equation (3).
[[Page 36878]]
[GRAPHIC] [TIFF OMITTED] TR07AU17.002
Conversely, equation (1) correctly accounts for the amount of power
it takes to provide a given amount of flow. That is, equation (1)
reflects the more realistic case where a pump provides a low flow rate
for an associated amount of power during a portion of the day and a
high flow rate for an associate amount of power during another portion
of the day. If one were to calculate the ``total daily WEF,'' one would
sum the flow rates throughout the day and the power consumption
throughout the day and take a ratio of the two; both power and flow
values would be weighted according to their proportional use during the
day. Therefore, equation (1) is more representative of the energy
efficiency of dedicated-purpose pool pumps over a typical cycle of use.
During the September 2016 DPPP test procedure NOPR public meeting,
CA IOUs inquired about including standby power as part of the metric
for dedicated-purpose pool pumps. (CA IOUs, Public Meeting Transcript,
No. 3 at pp. 91-92) In response to CA IOUs inquiry, DOE explained that
standby power was discussed during the DPPP Working Group meetings and,
ultimately, the DPPP Working Group decided not to include standby power
in the WEF metric due to the negligible impact any standby power
measurements would have on the final WEF value. (Docket No. EERE-2015-
BT-STD-0008, No. 95 at pp. 229-30) Consistent with the DPPP Working
Group recommendations, DOE did not propose to include standby power
measurements nor reporting in the September 2016 DPPP test procedure
NOPR. While DOE appreciates that some dedicated-purpose pool pumps with
controls will consume standby power in their idle state and the desire
to minimize this energy consumption, DOE does not believe the
additional burden associated with dedicated testing and reporting
requirements would be justified. Specifically, testing of standby power
for dedicated-purpose pool pumps would require an additional test
method and may require different or more specialized power measurement
equipment to accurately capture the low power during standby operation.
Furthermore, as the DPPP Working Group did not recommend specific
requirements for standby energy consumption, such testing would only be
informative and would not be necessary to determine compliance of
dedicated-purpose pool pumps. DOE does not believe the additional
burden associated with establishing test requirements to measure
standby energy use of dedicated-purpose pool pumps is justified at this
time. Therefore, in this final rule, DOE is not adopting testing or
reporting requirements for standby power of dedicated-purpose pool
pumps.
In addition to WEF, in the September 2016 DPPP test procedure NOPR,
DOE also proposed an optional test method for EF at multiple speeds
and/or system curves and to allow manufacturers and industry to
continue to describe the energy performance of dedicated-purpose pool
pumps using the EF metric. 81 FR 64580, 64627-64628 (Sept. 20, 2016).
DOE typically only includes one primary energy metric, the DOE metric
that is used for the energy conservation standards, in the test
procedure to ensure standardization of efficiency representations
throughout the industry and eliminates potential confusion in the
market place if multiple non-equivalent metrics are used to describe
the same piece of equipment. However, in this specific case, DOE
departed from typical practice due to the interest expressed in the use
of the EF metric during the DPPP Working Group negotiations. DOE notes
that, as discussed in more detail in section III.F, representations of
EF will only be allowed until July 19, 2021, the compliance date of
standards for dedicated-purpose pool pumps and, if made, must be
accompanied by a representation of the DOE metric, WEF.
D. Test Methods for Different DPPP Categories and Configurations
As discussed in section III.C, DOE will characterize the
performance of dedicated-purpose pool pumps according to the WEF. Due
to differences in equipment design and typical use profiles, the DPPP
Working Group recommended that unique weights and load points be
specified for each DPPP variety and pump speed configuration. Based on
the recommendations of the DPPP Working Group, in the September 2016
DPPP test procedure NOPR, DOE proposed unique load points for the
various speed configurations (e.g., single-speed, two-speed, multi-
speed, or variable-speed dedicated-purpose pool pumps) of self-priming
and non-self-priming pool filter pumps with a rated hydraulic
horsepower less than 2.5 hp (section III.D.1). DOE also proposed unique
load points for waterfall pumps (section 0) and pressure cleaner
booster pumps (section III.D.3), each of which reference only a single
load point. 81 FR 64580, 64601-64602 (Sept. 20, 2016). The load points
for self-priming and non-self-priming pool filter pumps, waterfall
pumps, and pressure cleaner booster pumps are discussed in the
subsequent sections.
1. Self-Priming and Non-Self-Priming Pool Filter Pumps
As noted in section III.B.3.a, self-priming and non-self-priming
pool filter pumps have different construction characteristics and
potentially different applications. However, during the Working Group
meetings, the DPPP Working Group discussed how the performance of these
two different varieties of pumps is comparable in most instances.
(Docket No. EERE-2015-BT-STD-0008, No. 57 at pp. 329-331) Therefore, to
provide comparable ratings between self-priming and non-self-priming
pool filter pumps, the DPPP Working Group recommended the same
reference curve, curve C, for self-
[[Page 36879]]
priming and non-self-priming filter pumps. (Docket No. EERE-2015-BT-
STD-0008, No. 51 Recommendation #6 at p. 5) Consistent with the DPPP
Working Group recommendations, in the September 2016 test procedure
NOPR, DOE proposed that both self-priming and non-self-priming pool
filter pumps be tested at specific load points along curve C. 81 FR
64580, 64602-64603 (Sept. 20, 2016).
During the September 2016 DPPP test procedure NOPR public meeting,
CA IOUs did not object to the recommendation, but noted that the
typical pipe size associated with these curves is a generalization and
the overall plumbing system can affect the curves as much as the pump
size in response to DOE's assertion that curve C was representative of
2.5-inch plumbing. (CA IOUs, Public Meeting Transcript, No. 3 at p. 37)
In response to CA IOUs observation, DOE agrees with CA IOUs that many
factors may impact system head. DOE was simply referring to the fact
that curve C was initially developed to be representative of 2.5-inch
plumbing,\27\ as is acknowledged in section 4.1.2.1.3 of ANSI/APSP/ICC-
15a-2013.
---------------------------------------------------------------------------
\27\ PG&E developed curves A, B, and C based data from an
exercise by ADM Associates, Inc. in 2002, EVALUATION OF YEAR 2001
SUMMER INITIATIVES POOL PUMP PROGRAM and contractor input. However,
the actual data for the curves are not contained in the ADM report
(the ADM report can be found at www.calmac.org/publications/SI_Pool_Pump.pdf; Last accessed April 4, 2016). Curves A and B are
first formally mentioned in a subsequent report by PG&E in Codes and
Standards Enhancement Initiative for FY 2004. However, this report
does not discuss the derivation of the curves. (https://consensus.fsu.edu/FBC/Pool-Efficiency/CASE_Pool_Pump.pdf; Last
accessed April 29, 2016).
---------------------------------------------------------------------------
Beyond the proposed system curve, DOE also proposed specific load
points for each variety of self-priming and non-self-priming pool
filter pump. The specific load points for single-speed, two-speed,
multi-speed, and variable-speed pool filter pumps are discussed in
sections III.D.1.a, III.D.1.b, and III.D.1.c, respectively.
a. Single-Speed Pool Filter Pumps
Single-speed pool filter pumps, by definition and design, are only
capable of operating at one speed. In the September 2016 DPPP test
procedure NOPR, consistent with the DPPP Working Group recommendations
(Docket No. EERE-2015-BT-STD-0008, No. 51 Recommendation #6 at p. 5),
DOE proposed testing single-speed pool filter pumps at the pump's
maximum speed of rotation on curve C. 81 FR 64580, 64603 (Sept. 20,
2016). That is, the load point for single-speed pool filter pumps would
be specified as the point of intersection between the pump's
performance curve at its maximum speed (which is its only speed) and
the system curve C, as shown in Figure III.1. Id.
[GRAPHIC] [TIFF OMITTED] TR07AU17.003
CEC, in written comments, supported DOE's proposal to establish a
load point for single-speed filter pumps. (CEC, No. 7 at p. 2) DOE
received no other comments related to the proposal to test single-speed
pool filter pumps at a single load point based on the maximum speed on
curve C. Therefore, DOE is adopting in this final rule the proposed
single load point for single-speed pool filter pumps.
b. Two-Speed Pool Filter Pumps
Two-speed pumps, by definition and design, are capable of operating
at two discrete speeds. In two-speed pool filter pumps, the low speed
setting is designed to handle filtration and provide an adequate
turnover-rate, while the high speed setting operation is designed to be
used intermittently for short duration periods to operate suction-side
pool cleaners and ensure proper mixing of the water. Consistent with
typical two-speed pool filter pump design and the requirements of
existing regulatory programs, the DPPP Working Group recommended
testing two-speed pool filter pumps (1) at the load point corresponding
to the pump's maximum speed of rotation on curve C and (2) at the load
point corresponding to half of the maximum-speed flow rate with total
dynamic head at or above curve C.
[[Page 36880]]
(Docket No. EERE-2015-BT-STD-0008, No. 51, Recommendation #6, at p. 5)
However, in the September 2016 DPPP test procedure NOPR, DOE proposed
load points that were slightly modified from those recommended by the
DPPP Working Group. Specifically, DOE proposed the following two load
points for two-speed pool filter pumps: (1) A high flow point at the
maximum speed on curve C and (2) a low flow point at the low-speed
setting on curve C. 81 FR 64580, 64604-64606 (Sept. 20, 2016). As
explained in the September 2016 DPPP test procedure NOPR, the load
points recommended by the DPPP Working Group are only possible for
pumps with the low-speed setting equivalent to one-half of the rotating
speed of the maximum speed setting. DOE proposed the modification
because DOE believed the DPPP Working Group recommendation, as written,
would not provide equitable or representative ratings for any two-speed
pool filter pumps with a low speed that was less than one-half the
maximum speed setting. Id.
DOE also proposed certain criteria for the low flow point to
prevent manufacturers from producing pumps with unrepresentatively high
(i.e., advantageous) WEF scores by designing pumps with an extremely
low speed setting. Id. Specifically, DOE proposed minimum flow rates
for two-speed pumps of 24.7 gpm for two-speed pool filter pumps that
have a rated hydraulic horsepower less than or equal to 0.75 hp (small
pool filter pumps) and 31.1 gpm for two-speed pool filter pumps that
have a rated hydraulic horsepower greater than 0.75 (large pool filter
pumps). DOE's proposed minimum flow rates are consistent with the DPPP
Working Group's recommended low flow rates for multi-speed and
variable-speed pool filter pumps. (Docket No. EERE-2015-BT-STD-0008,
No. 51, Recommendation #6 at p. 5); 81 FR 64580, 64604-06 (Sept. 20,
2016). The DPPP Working Group developed these low flow rates based on
the minimum effective flow rates for typical pool sizes. DOE believes
these flow rates are also representative of minimum flow rates for two-
speed pool filter pumps and they will effectively prevent the inclusion
of unreasonably low speeds on two-speed pool filter pumps for the sole
purpose of inflating WEF ratings. 81 FR 64580, 64604-06 (Sept. 20,
2016).
DOE believes that the proposed load points for two-speed pool
filter pumps are representative of typical pool filter pump operation
and energy performance, and the load points characterize the efficiency
of the pump speeds and flow points in typical applications (i.e.,
cleaning/mixing and filtration). In addition, DOE believes that the
proposal is consistent with the intent of the DPPP Working Group.
During the September 2016 DPPP test procedure NOPR public meeting,
CA IOUs confirmed that two-speed pool filter pumps with low speed below
one-half of maximum speed are a reasonable scenario and supported DOE's
proposed load points to address this scenario. (CA IOUs, Public Meeting
Transcript, No. 3 at pp. 39-41) ASAP, NRDC, and CEC, in written
comments, supported DOE's proposal to establish load points for two-
speed pool filter pumps and did not articulate any different
suggestions to the proposed test procedure. (ASAP and NRDC, No. 12 at
p. 2; CEC, No. 7 at p. 2) ASAP and NRDC also commented that proposed
load points would provide consistent and comparable ratings among two-
speed filter pumps. (ASAP and NRDC, No. 12 at p. 2)
DOE appreciates the support of CA IOUs, ASAP, NRDC, and CEC. DOE
received no other comments related to the proposed test procedure for
two-speed pool filter pumps. Therefore, DOE is adopting in this final
rule the proposed load points at low and high speed for two-speed pool
filter pumps, as well as the minimum flow rate thresholds of 24.7 gpm
for two-speed pool filter pumps that have a hydraulic output power less
than or equal to 0.75 hp (small pool filter pumps) and a low flow rate
of 31.1 gpm for two-speed pool filter pumps that have a hydraulic
output power greater than 0.75 and less than 2.5 hp (large pool filter
pumps).
c. Variable-Speed and Multi-Speed Pool Filter Pumps
In accordance with the DPPP Working Group recommendations, in the
September 2016 DPPP test procedure NOPR, DOE proposed different
definitions for variable-speed and multi-speed pool filter pumps (see
section III.B.7.a), but proposed the same test procedure be applied to
both speed configurations. (Docket No. EERE-2015-BT-STD-0008, No. 51,
Recommendation #6, at p. 5); 81 FR 64580, 64606-64610 (Sept. 20, 2016).
For variable- and multi-speed pool filter pumps, DOE proposed two load
points that are generally representative of a high-speed mixing/
cleaning flow rate and a low-speed filtration flow rate, similar to
two-speed pool filter pumps (as discussed in section III.D.1.b).
However, the high-speed and low-speed load points for variable- and
multi-speed equipment are specified in a slightly different manner than
for two-speed equipment. 81 FR 64580, 64606-64610 (Sept. 20, 2016).
As DOE discussed in the September 2016 DPPP test procedure NOPR,
the DPPP Working Group recommended (Docket No. EERE-2015-BT-STD-0008,
No. 51, Recommendation #6 at p. 5), and DOE subsequently proposed,
testing multi- and variable-speed pool filter pumps at two load points.
These points are (1) a high-flow load point that is achieved by running
the pump at 80 percent of flow rate at maximum speed on or above curve
C and (2) a low-flow load point that is representative of a specific,
typical filtration flow rate, as opposed to a specific speed setting or
relative reduction from maximum speed (also on or above curve C), as
summarized in Table III.3. 81 FR 64580, 64606-64610 (Sept. 20, 2016).
Table III.3--Variable- and Multi-Speed Load Points Recommended by DPPP Working Group and Proposed by DOE in
September 2016 DPPP Test Procedure NOPR
----------------------------------------------------------------------------------------------------------------
Load point Flow rate (gpm) Head (ft) Speed (rpm)
----------------------------------------------------------------------------------------------------------------
High Speed..................... Qhigh (gpm) = 0.8xQmax\speed@C * H >=0.0082 x Lowest available speed
Low Speed...................... Qlow (gpm) = Qhigh\2\ for which the pump
If pump hydraulic hp at H >=0.0082 x can achieve the
max speed on curve C is >0.75, Qlow\2\ specified flow rate
then Qlow = 31.1 gpm (a pump may vary
If pump hydraulic hp at speed to achieve this
max speed on curve C is <=0.75, load point).
then Qlow = 24.7 gpm
----------------------------------------------------------------------------------------------------------------
* Qmax\speed@C = flow at maximum speed on curve C.
[[Page 36881]]
The high speed load point corresponding to a flow rate of 80
percent of the flow at maximum speed on curve C was recommended by the
DPPP Working Group to reflect that multi- and variable-speed pool
filter pumps can be optimized to account for the oversizing the
typically occurs in the field and provide a specific desired amount of
flow that may be less than the flow rate at maximum speed. Id. In the
September 2016 DPPP test procedure NOPR, DOE discussed that, for multi-
speed pumps without a speed setting at 80 percent of the maximum speed
setting, the high flow point would be determined at the maximum
operating speed of the pump and may not be on curve C. 81 FR 64580,
64607 (Sept. 20, 2016). Such a pump would need to be tested at a speed
setting higher than 80 percent of maximum and throttled to a head
pressure higher than curve C to achieve a flow rate of 80 percent of
the flow rate at maximum flow on curve C, as shown in Figure III.2.
[GRAPHIC] [TIFF OMITTED] TR07AU17.004
To specify the low flow points for multi-speed and variable-speed
pool filter pumps, the DPPP Working Group developed specific, discrete
flow rates that are representative of the typical flow rates observed
in the field. (Docket No. EERE-2015-BT-STD-0008, No. 51, Recommendation
#6 at p. 5) That is, as discussed in the September 2016 DPPP test
procedure NOPR, the DPPP Working Group recommended that ``small pool
filter pumps'' with rated hydraulic horsepower values of less than or
equal 0.75 would be assigned a flow rate of 24.7 gpm, which is
representative of the flow rate necessary for filtration in smaller
pools. The DPPP Working Group also recommended that ``large pool filter
pumps'' with rated hydraulic horsepower values greater than 0.75 and
less than or equal to 2.5 would be assigned a flow rate of 31.1 gpm,
which is representative of the flow rate necessary for filtration in
large pools. The selected low flow rates for small and large multi-
speed and variable-speed pool filter pumps are intended to be
representative of the applications such pumps would typically serve.
The methodology for developing the specific flow rates for small and
large multi-speed and variable-speed pool filter pumps is discussed at
length in the September 2016 DPPP test procedure NOPR. 81 FR 64580,
64606-64610 (Sept. 20, 2016).
DOE's proposal for the high flow and low flow points for multi-
speed and variable-speed pumps does not explicitly specify the speed at
which the pump operates at the high or low flow points. Instead, DOE
determined that the low and high flow rates would be achieved at the
lowest available speed while operating on or above curve C to
accommodate multi-speed pumps that may not be capable of operating at
the exact speed that allows the pump to achieve the required flow rate
exactly on curve C. For such a pump, DOE established that the pump be
tested at the lowest available speed that can meet the specified flow
with a head point that is at or above curve C. Id.
In the September 2016 DPPP test procedure NOPR, DOE requested
comment on the treatment of multi-speed pumps and the necessity to
throttle multi-speed pumps on the maximum speed performance curve if
appropriate lower discrete operating speeds are not available to
achieve 80 percent of the flow rate at maximum speed on curve C while
still maintaining head at or above curve C. 81 FR 64580, 64608 (Sept.
20, 2016).
In response, CEC supported DOE's proposal to establish load points
for multi-speed and variable-speed pool filter pumps. However, CEC did
not advocate for any different values compared to DOE's proposal. (CEC,
No.
[[Page 36882]]
7 at p. 2). Pentair requested clarification during the September 2016
DPPP test procedure NOPR public meeting and in written comments
regarding whether the high flow load point for multi-speed and
variable-speed pool filter pumps was specified with respect to 80
percent flow or 80 percent speed. (Pentair, Public Meeting Transcript,
No. 3 at p. 48; Pentair, No. 11 at p. 4) APSP reiterated Pentair's
comments that flow and speed were used interchangeably in the September
2016 DPPP test procedure NOPR and recommended that the test procedure
be standardized on a percentage of flow requirements (APSP, No. 8 at p.
2). Consistent with APSP's recommendation, in this final rule, DOE
clarifies that the high flow load point for multi-speed and variable-
speed pool filter pumps is specified with respect to at 80 percent of
the flow rate at maximum speed on curve C.
APSP and Pentair also commented that throttling multi-speed pumps
to obtain 80 percent flow moves the pump off of curve C, which is
otherwise the standardized performance curve proposed by DOE in the
test procedure NOPR. Pentair commented that throttling and testing off
of curve C makes direct product performance comparisons impossible, and
has the potential to overstate the performance of less efficient and
less capable pumps. (APSP, No. 8 at pp. 4-5; Pentair, No. 11, at p. 2)
Pentair similarly expressed concern over the low flow load points.
Pentair agreed that 24.7 gpm and 31.1 gpm are reasonable minimum flow
rates for typical swimming pool applications. However, Pentair stated
that fixing the low-speed load point at one of these two values would
create an unfair bias against higher capacity pumps that are designed
for high-flow, low-head systems. (Pentair, No. 11 at p. 2) At the test
procedure NOPR public meeting, Pentair suggested that multi-speed pumps
that cannot be tested at 80 percent of the flow rate at maximum speed
on curve C be tested at their maximum speed on curve C. (Pentair,
Public Meeting Transcript, No. 3 at pp. 42-43) Pentair did not provide
a specific recommendation for the low flow load points.
In response to Pentair and APSP's dissatisfaction with DOE's
proposal to allow throttling multi-speed pumps, DOE agrees with Pentair
and APSP's concerns that throttling and testing off of curve C may
result in WEF values that are not directly representative of the
typical energy performance of the pump in the field, as users are
unlikely to throttle pumps to compensate for oversizing. In assessing
Pentair and APSP's concerns, DOE recognized that the multi-speed pump
load points specified in the December 2015 DPPP Working Group
recommendations did not explicitly mention or require throttling.
Specifically, for flow, the term sheet stated ``same method as variable
speed, but testing at closest available speed that can meet the
specified flow (while at or above Qlow or Qhigh,
respectively).'' For head, the term sheet stated: ``H >= 0.0082 x
Qhigh\2\.'' (Docket No. EERE-2015-BT-STD-0008, No. 51,
Recommendation #6 at p. 5) Allowing flow to be ``at or above''
Qhigh and ``at or above'' 0.0082 x Qhigh\2\ means
that a multi-speed pump that does not have an 80 percent speed setting
could test exactly on curve C with a flow rate at or above 80 percent
of the flow rate at maximum speed on curve C, as suggested by Pentair,
and still meet the load point requirements laid out by the DPPP Working
Group in the December 2015 term sheet. Id.
Consequently, DOE acknowledges that its proposal in the September
2016 DPPP test procedure NOPR to require throttling of multi-speed
pumps was based on one possible interpretation of the December 2015
DPPP Working Group recommendations, while Pentair's proposal to test on
curve C as the lowest speed that resulted in a flow rate at or above 80
percent of the flow rate at maximum speed on curve C is based on
another possible interpretation. That is, as written, the December 2015
DPPP Working Group recommendations allow multiple interpretations of
the appropriate load points for multi-speed pool filter pumps. In the
September 2016 DPPP test procedure NOPR, DOE proposed the test method
that required fixing the flow point at 80 percent of the flow rate at
maximum speed on curve C (i.e., Qhigh = 0.8 x
Qmax_speed@C) because DOE's test procedure must be precise
and repeatable and, therefore, must provide additional specificity
beyond that specified by the DPPP Working Group. However, DOE
acknowledges that Pentair's suggestion of fixing the head value on
curve C (H = 0.0082 x Qhigh\2\) and allowing flow rates
above 80 percent of the flow rate at maximum speed on curve C is
another viable method to provide the requisite additional specificity
and precision in the multi-speed test method. DOE also acknowledges
that, as mentioned by Pentair and APSP, that throttling off of curve C
would be a departure from the standardized system curve and would
result in WEF values that are less representative of the typical energy
performance of such multi-speed pumps. Instead, multi-speed pumps would
more likely be operated on the standardized system curve (i.e., curve
C) at the lowest speed available at or above 80 percent of the flow
rate at maximum speed on curve C (i.e., the flow rate the DPPP Working
Group believed was ``required'' for high flow mixing in pumps that are
oversized). Therefore, in this final rule, DOE is revising the load
points for multi-speed pumps to require the head value to be on curve
C, as suggested by Pentair, but allow the flow value to be greater than
or equal to 80 percent of the flow rate at maximum speed on curve C. As
noted previously, this test method is consistent with that recommended
by the DPPP Working Group.
With regard to the low flow load points, DOE responds that the DPPP
Working Group recommended that the low-speed load point for variable-
and multi-speed pumps be measured at either 24.7 gpm or 31.1 gpm,
depending on the pump hydraulic horsepower at maximum speed on curve C.
(Docket No. EERE-2015-BT-STD-0008, No. 51, Recommendation #6 at p. 5)
As discussed at length in the September 2016 DPPP test procedure NOPR,
the DPPP Working Group recommended these values to allow for more
comparable WEF values among pool filter pumps intended to serve the
same size pools. 81 FR 64580, 64606-64610 (Sept. 20, 2016). While
Pentair noted in its comments that this construct may bias higher
capacity (high flow, low head) pumps, DOE notes that in general, higher
capacity pumps have been excluded from the scope of this rulemaking. In
addition, as discussed previously, these low flow points were chosen
specifically to represent typical filtration flow rates that would be
experienced in the majority of pools, regardless of the size of the
pump. That is, the required filtration flow rate is dictated more by
the size of the pool than the size of the pump. Converse to Pentair's
observation, the ability of larger pumps to reduce their speed to
achieve these low flow rates will potentially result in higher (i.e.,
better) WEF scores than slightly small dedicated-purpose pool pumps
serving the same load.
For these reasons, DOE is adopting in this final rule the low speed
load points of 24.7 gpm and 31.1 gpm, as proposed, in the September
2016 DPPP TP NOPR. However, for multi-speed pumps, DOE acknowledges
that the low speed may not result in a flow rate that is exactly 24.7
or 31.1 gpm while on curve C and throttling may be required to achieve
the flow points proposed in the NOPR. As discussed previously, DOE
agrees with Pentair and APSP that throttling
[[Page 36883]]
may not be representative of the performance of multi-speed dedicated-
purpose pool pumps in the field. Therefore, based on the same reasoning
as the high flow point, DOE is revising the low flow point for multi-
speed dedicated-purpose pool pumps to also require testing along curve
C, but allow flow rates at or above the specified values. Specifically,
the adopted load points are presented in Table III.4.
Table III.4--Multi-Speed and Variable-Speed Load Points Adopted in This Final Rule
----------------------------------------------------------------------------------------------------------------
Load point Flow rate (gpm) Head (ft) Speed (rpm)
----------------------------------------------------------------------------------------------------------------
High Speed......................... Qhigh (gpm) >=0.8 x H = 0.0082 x Qhigh\2\ Lowest available speed
Low Speed.......................... Qmax\speed@C * (i.e., on Curve C) for which the pump
Qlow (gpm) =............... H = 0.0082 x Qlow\2\ can achieve the
If pump hydraulic (i.e., on Curve C). specified head value
hp at max speed on curve C and flow rate
is >0.75, then Qlow >=31.1 threshold (a pump may
gpm. vary speed to achieve
If pump hydraulic this load point).
hp at max speed on curve C
is <=0.75, then Qlow
>=24.7 gpm.
----------------------------------------------------------------------------------------------------------------
* Qmax\speed@C = flow at maximum speed on curve C.
DOE believes that the load points shown in Table III.4 are
consistent with the intent of the DPPP Working Group while addressing
the concerns brought by Pentair and APSP for multi-speed pool filter
pumps.
With regard to the variable-speed load points, DOE notes that the
load points recommended by the DPPP Working Group were specified
clearly as exactly equivalent to 24.7 or 31.1 gpm for the low flow load
point and 80 percent of the flow rate at maximum speed on curve C for
the high flow load point. (Docket No. EERE-2015-BT-STD-0008, No. 51,
Recommendation #6 at p. 5) The DPPP Working Group discussed and
recommended these load points based on the understanding that a
variable-speed dedicated purpose pool pump would be equipped with a
continuously variable control that could exactly achieve the load
points specified in the test procedure or desired by a user in the
field. However, DOE notes that the definition for variable-speed
dedicated-purpose pool pump recommended by the DPPP Working Group and
adopted by DOE references a maximum increment between available
operating speeds of 100 rpm. Based on the adopted definition it is
possible that a variable-speed dedicated-purpose pool pump with
extremely wide speed increments (e.g., 95 rpm) will not be able to
exactly achieve the flow points specified by the DPPP Working Group.
DOE notes that the definition for variable-speed dedicated-purpose pool
pump was not finalized by the DPPP Working Group until after the load
points for variable-speed dedicated-purpose pool pump had already by
been established and approved. Therefore, the DPPP Working Group did
not explicitly consider a scenario where a variable-speed dedicated-
purpose pool pump would not be able to exactly achieve the specified
flow points.
DOE believes that, similar to multi-speed pool filter pumps, it is
unlikely that a user would throttle the pump in the field to achieve a
specific flow rate. Instead, DOE believes it would be more
representative and consistent to also require variable-speed pool
filter pumps to be tested on curve C at the lowest speed that results
in a flow rate at or above the flow rate specified by the DPPP Working
Group, similar to the load points specified for multi-speed pool filter
pumps. Therefore, DOE is adopting, in this final rule, the same load
points for multi-speed and variable-speed pool filter pumps, as
summarized in Table III.4.
In response to the multi-speed load points proposed in the
September 2016 DPPP test procedure NOPR, Hayward commented that the
proposed criteria for multi-speed pumps would severely penalize less
capable multispeed pumps [without a discrete operating speed at 80
percent of flow rate at maximum speed on curve C]. (Hayward, No. 6 at
p. 3) In response to Hayward's concerns regarding the penalization of
multi-speed pumps, DOE acknowledges that the test procedure (both as
proposed in the NOPR and as adopted in this final rule) will indeed
``penalize'' (i.e., generate less advantageous WEF score for) less
capable multi-speed pumps that cannot exactly achieve 80 percent of the
flow rate at maximum speed on curve C. This is by-design and in
agreement with the recommendations of DPPP Working Group, because such
pumps provide the end-user less utility and are more likely to be run
at higher-speeds and consume more energy than pumps that can reach 80
percent of the flow rate at maximum speed on curve C. Furthermore, the
disadvantage in WEF score is commensurate with the reduced speed
capability of the pump--the closer the pump can get to the 80 percent
load point (with speed reduction), the better the pump's WEF score will
be. For this reason, DOE is adopting its proposals as to the treatment
of multi-speed pumps in this final rule, except as noted in this
section.
Pentair raised a concern that an unintended consequence of
specifying the high flow load point based on 80 percent flow was that
manufacturers may start designing pool filter pumps with an 80 percent
speed setting, even if it is not the best optimization for the pump for
specific applications. (Pentair, Public Meeting Transcript. No. 3 at p.
46) In response, DOE acknowledges Pentair's concern, but notes that the
80 percent load point was selected by the DPPP Working Group to be
representative of the amount of ``right-sizing'' that would be possible
in typical applications. (EERE-2015-BT-STD-0008, No. 57 at pp. 388-405;
CA IOUs, No. 53 at pp. 142-143; Waterway, No. 54 at p. 51) As such, DOE
believes the 80 percent setting is representative of a speed setting
that would reliably result in energy savings in the field for typical
applications. However, DOE acknowledges that for some applications the
80 percent speed setting may not be the most appropriate choice. DOE
notes that, if specific applications necessitate different speed
settings, manufacturers may continue to produce such equipment to serve
the market need for equipment with specific speed settings. The DOE
test procedure does not affect the flexibility of manufacturers to
produce equipment that is demanded by the market; it just describes how
to rate such equipment.
Additionally, Hayward and APSP pointed out a discrepancy between
Table 1 in the regulatory text of the September 2016 DPPP test
procedure NOPR and the language presented in the rest of the NOPR.
Specifically, Hayward noted that the required head for the variable-
speed and multi-speed high flow load point should be ``H >= 0.0082 x
Qlow\2\,'' rather than ``H = 0.0082 x
[[Page 36884]]
Qlow\2\,'' which was printed in Table 1 of the September
2016 DPPP test procedure NOPR. (Hayward, No. 6 at p. 3; APSP, No. 8 at
p. 4) DOE agrees with Hayward and APSP. A typographical error occurred
in Table 1 in the September 2016 DPPP test procedure NOPR and the
equation should have read ``H >= 0.0082 x Qlow\2\'' based on
the proposed load points for multi-speed dedicated purpose pool pumps.
However, based on the adopted load points, DOE is specifying the load
points as depicted in Table III.4, which have the appropriate
mathematical operators.
During the September 2016 DPPP test procedure NOPR public meeting,
Pentair also requested verification regarding Figure III.5 in the
September 2016 DPPP test procedure NOPR and a similar figure in the
September 2016 DPPP test procedure NOPR public meeting presentation.
(Pentair, Public Meeting Transcript, No, 3, p. 54) DOE acknowledged
during the September 2016 DPPP test procedure NOPR public meeting that
the public meeting presentation slide was correct and Figure III.5 in
the September 2016 DPPP test procedure NOPR was incorrect.\28\
Accordingly, in this final rule, DOE includes the corrected and
clarified version of the figure, which is labeled Figure III.2 in this
final rule.
---------------------------------------------------------------------------
\28\ The public meeting slides can be found in the docket
(www.regulations.gov/#!docketDetail;D=EERE-2016-BT-TP-0002) No. 2 at
p. 31.
---------------------------------------------------------------------------
APSP and Zodiac also requested clarification regarding how the
high-speed flow point is based on a flow rate of 80 percent of the flow
rate at maximum speed on curve C and head at or above curve C. (APSP,
No. 8 at p. 4; Zodiac, No. 13 at p. 2) DOE responds that, as discussed
in the September 2016 DPPP test procedure NOPR, the DPPP Working Group
recommended the high speed load point corresponding to a flow rate of
80 percent of the flow at maximum speed on curve C to reflect that
multi- and variable-speed pool filter pumps can be optimized to account
for the oversizing the typically occurs in the field and provide a
specific desired amount of flow that may be less than the flow rate at
maximum speed. 81 FR 64580, 64606-64610 (Sept. 20, 2016).
Finally, APSP and Zodiac commented that they would like to see a
tolerance for the 80 percent load point for multi-speed and variable-
speed pool filter pumps, as a speed of 80.00 percent exactly would be
difficult to achieve. (APSP, No. 8 at p. 5; Zodiac, No. 13 at p. 2). In
response, DOE clarifies that the neither the load points proposed in
the September 2016 DPPP test procedure NOPR nor the load points adopted
in this final rule for multi-speed and variable-speed pool filter pumps
require exact speeds to be achieved. Instead, the load points specify
specific head or flow values that must be achieved at the lowest
available speed for which the pump can achieve the specified flow rate
and/or head value; a pump may vary speed to achieve this load point.
DOE proposed and is adopting thresholds on the specified head or flow
values to account for experimental variability, which are discussed in
section III.E.2.d.
d. Load Point Weighting Factors
WEF is calculated as the weighted average flow rate divided by the
weighted average input power to the dedicated-purpose pool pump at
various load points, as described in equation (1). For this reason, DOE
also must assign weights to the load points discussed above for each
self-priming or non-self-priming pool filter pump. In the September
2016 DPPP test procedure NOPR, consistent with the DPPP Working Group
recommendations (Docket No. EERE-2015-BT-STD-0008, No. 51
Recommendation #7 at p. 5) as well as DOE's own analysis, DOE proposed
a weight of 1.0 for single-speed self-priming and non-self-priming pool
filter pumps and weights of 0.20 at the high flow point and 0.80 at the
low flow point for two-speed, multi-speed, and variable-speed pool
filter pumps, as summarized in Table III.5. 81 FR 64580, 64610 (Sept.
20, 2016).
Table III.5--Summary of Load Point Weights (wi) for Self-Priming and Non-
Self-Priming Pool Filter Pumps Recommended by the DPPP Working Group
------------------------------------------------------------------------
Load point(s) i
DPPP varieties Speed type -------------------------
Low flow High flow
------------------------------------------------------------------------
Self-Priming Pool Filter Single......... ........... 1.0
Pumps and Non-Self-Priming Two/Multi/ 0.80 0.20
Pool Filter Pumps. Variable.
------------------------------------------------------------------------
DOE requested comment on these proposed weights. In response to
DOE's proposed weights, APSP and Zodiac stated that unbalanced
weighting of the economical single-speed pumps negatively affects
consumers who only operate pools for a short seasonal duration. (APSP,
No. 8 at p. 5; Zodiac, No. 13 at p. 2) DOE acknowledges that pool pumps
with more than one speed, such as two-speed, multi-speed, and variable-
speed dedicated-purpose pool pumps, will have a greater (i.e., more
efficient) WEF score than a single-speed pump. However, this is
consistent with the intent of the DPPP Working Group and the typical
energy consumption of such pumps in the field. That is, single-speed
pumps will use more energy than comparable two-speed, multi-speed, or
variable-speed pumps. DOE also disagrees with APSP and Zodiac that a
load point of 1.0 for single-speed pool filter pumps is ``unbalanced''
because, as recommended by the DPPP Working Group, single-speed pool
pump operate at only one load point, which must be fully weighted in
order to accurately and equitably account for the energy performance of
such pumps.
APSP and Hayward agreed with the 0.8 value for low flow for two-
speed pool filter pumps. (APSP, No. 8 at p. 5; Hayward, No. 6 at p. 3)
CEC, in written comments, affirmed DOE's proposal to establish
weighting factors for single-speed, two-speed, multi-speed, and
variable-speed pool filter pumps. (CEC, No. 7 at p. 2) As such, DOE is
adopting, in this final rule, the weights proposed in the September
2016 DPPP test procedure NOPR.
e. Applicability of Two-Speed, Multi-Speed, and Variable-Speed Pool
Filter Pump Test Methods
As discussed in section III.B.7, DOE proposed in the September 2016
DPPP test procedure NOPR to establish specific definitions for two-
speed, multi-speed, and variable-speed dedicated-purpose pool pumps
that would dictate which of the pool filter pump test methods applies
to a given
[[Page 36885]]
pool filter pump. The specific test methods for each of the DPPP speed
configurations are described in sections III.D.1.a through III.D.1.c.
The definitions for two-speed, multi-speed, and variable-speed
dedicated-purpose pool pumps establish specific criteria that any given
dedicated-purpose pool pump must meet in order to be considered such a
pump and be eligible to apply the test points for two-speed, multi-
speed, and variable-speed pool filter pumps, respectively. If a
dedicated-purpose pool pump does not meet the definition of a two-
speed, multi-speed, or variable-speed dedicated-purpose pool pump
discussed in section III.B.7, DOE proposed in the September 2016 DPPP
test procedure NOPR that such a pump would be tested using the single-
speed pool filter pump test point, regardless of the number of
operating speeds the pump may have. 81 FR 64580, 64610 (Sept. 20,
2016).
In the September 2016 DPPP test procedure NOPR, consistent with the
recommendations of the DPPP Working Group (Docket No. EERE-2015-BT-STD-
0008, No. 82, Recommendation #5B at p. 3), DOE also proposed that two-
speed self-priming pool filter pumps that are greater than or equal to
0.711 rated hydraulic horsepower and less than 2.5 rated hydraulic
horsepower must also be distributed in commerce either: (1) With a pool
pump control (variable speed drive and user interface or switch) that
changes the speed in response to pre-programmed user preferences and
allows the user to select the duration of each speed and/or the on/off
times or (2) without a pool pump control with such capability but is
unable to operate without the presence of such a pool pump control. Id.
DOE also proposed that two-speed self-priming pool filter pumps (in the
referenced size range) that do not meet the proposed control
requirements would be tested as a single-speed pool filter pump. Id.
Hayward commented, at the September 2016 DPPP test procedure NOPR
public meeting, that two-speed dedicated-purpose pool pumps should be
allowed to operate at low speed without the requisite control, instead
of not able to operate at all. (Hayward, Public Meeting Transcript, No.
3 at pp. 21, 26-27) DOE addressed this comment in section III.B.7.a. In
that section, DOE noted that DOE believes the two-speed DPPP test
points are only applicable to and representative of two-speed
dedicated-purpose pool pumps operated with the appropriate controls. If
a two-speed dedicated-purpose pool pump is capable of operating, even
at low speed, without an applicable pool pump control, this
significantly increases the risk that two-speed pool filter pumps would
be installed and operated without an appropriate control. Similarly,
with regard to the applicability of the two-speed test points, DOE
believes that two-speed dedicated-purpose pool pumps greater than 0.711
rated hydraulic horsepower must be distributed in commerce with either
an appropriate control or not able to operate without the presence of
such a pool pump control in order to apply the two-speed dedicated-
purpose pool pump test points. If the pump can operate without an
appropriate control, even at low speed, the two-speed test points would
not be representative of the pump's energy performance in the field.
DOE did not receive any comments on this proposal. Therefore, DOE is
adopting in this final rule the requirements for applying the two-speed
dedicated-purpose pool pump test points proposed in the September 2016
DPPP test procedure NOPR, which was agreed to by all DPPP Working Group
members as part of the June 2016 DPPP Working Group Recommendations.
2. Waterfall Pumps
DOE also proposed a unique test point for waterfall pumps in the
September 2016 DPPP test procedure NOPR. 81 FR 64580, 64610-64611
(Sept. 20, 2016). Under the definition discussed in section III.B.4.a,
waterfall pumps are pool filter pumps that have a maximum head less
than or equal to 30 feet and a maximum speed less than or equal to
1,800 rpm. As discussed in the September 2016 DPPP test procedure NOPR,
waterfall pumps are specialty-purpose single-speed, pool filter pumps
that typically operate waterfalls or other water features in a pool.
Id.
Because of these specific applications, the DPPP Working Group
recommended a single unique test point at a fixed head of 17 feet and
the maximum operating speed for waterfall pumps, which the DPPP Working
Group believed was representative of typical applications. Consistent
with the single recommended load point, the DPPP Working Group also
recommended fully weighting that load point (i.e., assigning it a
weight of 1.0). (Docket No. EERE-2015-BT-STD-0008, No. 51
Recommendation #6 at p. 5)
DOE agreed with the DPPP Working Group recommendations; however,
DOE slightly modified the recommendation by adding greater specificity
to the head value in DOE's proposal. DOE proposed to test waterfall
pumps at a single load point at maximum speed and a head of 17.0 feet
and to fully weight that single load point. 81 FR 64580, 64610-64611
(Sept. 20, 2016). DOE received no comment on the proposal and,
therefore, is adopting the load point and weighting for waterfall pumps
proposed in the September 2016 DPPP test procedure NOPR.
3. Pressure Cleaner Booster Pumps
DOE also proposed a unique test point for pressure cleaner booster
pumps in the September 2016 DPPP test procedure NOPR. 81 FR 64580,
64611-64612 (Sept. 20, 2016). Pressure cleaner booster pumps, as
defined in section III.B.4.b, are dedicated-purpose pool pumps that are
specifically designed to propel pressure-side pool cleaners along the
bottom of the pool in pressure-side cleaner applications. These
pressure-side cleaner applications require a high amount of head and a
low flow. In the December 2015 DPPP Working Group recommendations, the
DPPP Working Group had recommended a single, fixed load point of 90
feet of head at maximum speed based on the fact that any given
pressure-side pool cleaner application is typically a single, fixed
load point. (Docket No. EERE-2015-BT-STD-0008, No. 51, Recommendations
#6) However, in the second round of negotiations, the DPPP Working
Group reevaluated the recommended test procedure for pressure cleaner
booster pumps and its ability to representatively evaluate and
differentiate the potentially variable energy performance of different
pressure cleaner booster pump technologies. Specifically, to better
capture the potential for variable-speed pressure cleaner booster
pumps, in the June 2016 DPPP Working Group recommendations, the DPPP
Working Group revised the recommended test point for pressure cleaner
booster pumps to be a flow rate of 10 gpm at the minimum speed that
results in a head value at or above 60 feet. (Docket No. EERE-2015-BT-
STD-0008, No. 82, Recommendation #8 at pp. 4-5)
In either case, as only a single load point is required to
adequately characterize the efficiency of pressure cleaner booster
pumps, the DPPP Working Group recommended a weighting factor of 1.0 for
measured performance at that single load point when calculating WEF.
(Docket No. EERE-2015-BT-STD-0008, No. 51, Recommendation #6 and #7 at
p. 5)
In the September 2016 DPPP test procedure NOPR, DOE proposed to
adopt the load point and weighting recommended in the June 2016 DPPP
Working Group recommendations; however, DOE added specificity to the
flow and head values in the September 2016 DPPP test procedure NOPR.
Specifically, DOE proposed to test
[[Page 36886]]
pressure cleaner booster pumps at a single load point of 10.0 gpm at
the minimum speed that results in a head value at or above 60.0 feet
and to weight the measured performance of the pump at that load point
with a weighting factor of 1.0. 81 FR 64580, 64611-64612 (Sept. 20,
2016).
In response to DOE's proposed test method for pressure cleaner
booster pumps, APSP and Zodiac commented that the proposed test point
seemed reasonable. (APSP, No. 8 at p. 5; Zodiac, No. 13 at p. 2). DOE
thanks APSP and Zodiac for their supportive comments.
In written comments, Pentair stated that it would be more
appropriate to base the load point for pressure cleaner booster pump
testing on a system friction curve instead of a defined single point.
(Pentair, No. 11 at p. 3) In response, DOE notes that the proposed load
point for pressure cleaner booster pumps was developed based on input
from the DPPP Working Group and available information regarding the
representative operating characteristics for such pumps. Specifically,
the DPPP Working Group recommended a load point of 10 gpm at the
minimum speed that results in a head value at or above 60 feet, because
this scenario accommodates all pressure cleaner booster pumps on the
market. At the same time this scenario also accounts for the potential
improved energy performance of pressure cleaner booster pumps that
could use variable speed technology to precisely match the head
requirements of a pressure cleaner system. (Docket No. EERE-2015-BT-
STD-0008, No. 82, Recommendation #8 at pp. 4-5; Docket No. EERE-2015-
BT-STD-0008, No. 101 at pp. 11-20) The DPPP Working Group selected a
value of 10 gpm based on the typical flow rate that was required or
recommended for suction-side pressure cleaner apparatus to function.
(Docket No. EERE-2015-BT-STD-0008, No. 100, CA IOUs, pp. 186-188; 197-
198; Docket No. EERE-2015-BT-STD-0008, No. 101, Various, pp. 14-15, 49-
50, 87-89). Although DOE understands that a system curve that includes
both static and dynamic friction head would theoretically describe the
relationship between head and flow for pressure cleaner booster pump
applications, DOE believes that such a system curve is not necessary or
representative in this case because: (1) Pressure cleaner booster pumps
operate at only one load point and (2) the specified flow point and
head threshold appropriately describe the required operating parameters
for pressure cleaner booster pump applications. That is, as noted by
the DPPP Working Group, suction-side pressure cleaner apparatus
typically recommend a specific flow rate that will enable the equipment
to operate correctly. DOE acknowledges that a certain amount of
pressure must be produced by the pressure cleaner booster pump to
deliver the recommended flow rate. However, once that flow and head
value are achieved, the pump will operate at only that one load point.
Therefore, based on DOE's understanding of pressure cleaner booster
pump applications, DOE is requiring in this final rule that a specific
flow rate must be achieved regardless of the installation's system
curve.
DOE did not receive any other comments related to this proposal.
Therefore in this final rule, DOE is adopting the proposal that
pressure cleaner booster pumps to be tested at a single load point of
10.0 gpm at the minimum speed that results in a head value at or above
60.0 feet and to weight the measured performance of the pump at that
load point with a weighting factor of 1.0.
4. Summary
In summary, DOE adopts, in this final rule, unique load points for
the different varieties and speed configurations of dedicated-purpose
pool pumps. DOE's load points (i) and weights (wi) used in determining
WEF for each pump variety are presented in Table III.6.
DOE requested comment on the high-speed and low-speed load points
proposed for all DPPP equipment classes. 81 FR 64580, 64642-64643
(Sept. 20, 2016). Hayward requested clarification regarding whether all
of the load points used to determine WEF should be measured on system
curve C. (Hayward, No. 6 at p. 2) DOE refers Hayward to Table III.6,
which summarizes the load points for all dedicated-purpose pool pumps
subject to the test procedure adopted in this final rule. As shown in
Table III.6, all of the load points for self-priming and non-self-
priming pool filter pumps are specified with respect to curve C.
However, while many self-priming and non-self-priming pool filter pumps
models will be evaluated directly on curve C, certain models may have
their load points measured at head values above curve C, if the load
point cannot be measured on curve C based on the operating speeds
available on the pump. In addition, waterfall pumps and pressure
cleaner booster pumps have load points that are specified with respect
to unique flow and/or head values and do not reference curve C.
Table III.6--Load Points (i) and Weights (wi) for Each DPPP Variety and Speed Configuration
--------------------------------------------------------------------------------------------------------------------------------------------------------
Test points
--------------------------------------------------------------------------------------
DPPP varieties Speed type Number of Weight
points Load point (i) Flow rate (Q) Head (H) Speed (n) (wi)
(n)
--------------------------------------------------------------------------------------------------------------------------------------------------------
Self-Priming Pool Filter Pumps Single *............ 1 High........... Qhigh (gpm) = H = 0.0082 x Maxspeed........... 1.0
And Non-Self-Priming Pool Filter Qmax_speed@C = Qhigh\2\
Pumps (with hydraulic hp <=2.5 flow at maximum speed
hp). on curve C
Two-Speed........... 2 Low............ Qlow (gpm) = Flow H >= 0.0082 Lowest speed 0.8
rate associated with x Qlow\2\ capable of meeting
specified head and the specified flow
speed that is not and head values,
below: if any.
31.1 gpm if
pump hydraulic hp at
max speed on curve C
is >0.75 or
24.7 gpm if
pump hydraulic hp at
max speed on curve C
is <=0.75 (a pump
may vary speed to
achieve this load
point)
[[Page 36887]]
High........... Qhigh (gpm) = H = 0.0082 x Max speed.......... 0.2
Qmax_speed@C = flow Qhigh\2\
at max speed on
curve C
Multi- and Variable- 2 Low............ Qlow(gpm) H = 0.0082 x Lowest speed 0.8
Speed. If pump Qlow\2\ capable of meeting
hydraulic hp at max the specified flow
speed on curve C is and head values.
>0.75, then Qlow
>=31.1 gpm
If pump
hydraulic hp at max
speed on curve C is
<=0.75, then Qlow
>=24.7 gpm (a pump
may vary speed to
achieve this load
point)
High........... Qhigh (gpm) >=0.8 x H = 0.0082 x Lowest speed 0.2
Qmax_speed@C >=80% Qhigh\2\ capable of meeting
of flow at maximum the specified flow
speed on curve C (a and head values.
pump may vary speed
to achieve this load
point)
Waterfall Pumps.................. Single.............. 1 High........... Flow corresponding to 17.0 ft Max speed.......... 1.0
specified head (on
max speed pump
curve)
Pressure Cleaner Booster Pumps... All................. 1 High........... 10.0 gpm (a pump may >=60.0 ft Lowest speed 1.0
vary speed to capable of meeting
achieve this load the specified flow
point) and head values,
if any.
--------------------------------------------------------------------------------------------------------------------------------------------------------
* As discussed in section III.D.1.e, any pumps that do not meet DOE's definitions of two-speed, multi-speed, or variable-speed pool filter pump, as
applicable, and, in the case of two-speed self-priming pool filter pumps that are greater than or equal to 0.711 rated hydraulic horsepower and less
than 2.5 rated hydraulic horsepower and do not meet the requirements to apply the two-speed pool filter pump test method must be tested as a single-
speed pool filter pump.
E. Determination of Pump Performance
As part of DOE's test procedure for dedicated-purpose pool pumps,
DOE is specifying how to measure the performance of the dedicated-
purpose pool pump at the applicable load points consistently and
unambiguously. Specifically, to determine WEF for applicable dedicated-
purpose pool pumps, the test procedure specifies methods to measure the
driver input power to the motor or to the DPPP controls (if any) and
the flow rate at each specified load point, as well as the hydraulic
output power at maximum speed on system curve C (i.e., the rated
hydraulic horsepower, see section III.G.1).
The following section III.E.1 discusses the industry standard DOE
is incorporating by reference for measuring the performance of
dedicated-purpose pool pumps. The September 2016 DPPP test procedure
NOPR proposed several exceptions, modifications, and additions to this
base test procedure that DOE deemed necessary to ensure accuracy and
repeatability. These are presented in sections III.E.2.a through
III.E.2.f. Finally, DOE is adopting specific procedures for calculating
the WEF from the collected test data and rounding the values to ensure
that the test results are determined in a consistent manner (section
III.E.2.g).
1. Incorporation by Reference of HI 40.6-2014
In the September 2016 DPPP test procedure NOPR, in accordance with
the DPPP Working Group recommendations (Docket No. EERE-2015-BT-STD-
0008, No. 51, Recommendation #8 at p. 6), DOE proposed to incorporate
by reference certain sections of HI 40.6-2014 as part of DOE's test
procedure for measuring the energy consumption of dedicated-purpose
pool pumps, with the exceptions, modifications, and additions listed in
III.E.2. DOE stated that HI 40.6-2014 contains the relevant test
methods needed to accurately characterize the performance of dedicated-
purpose pool pumps, with a few exceptions, modifications, and
additions. Id. Specifically, HI 40.6-2014 defines and explains how to
calculate driver power input,\29\ volume per unit time,\30\ pump total
head,\31\ pump power output,\32\ overall efficiency,\33\ and other
relevant quantities at the specified load points necessary to determine
the metric (WEF), and contains appropriate specifications regarding the
test setup, methodology, standard rating conditions, equipment
specifications, uncertainty calculations, and tolerances.
---------------------------------------------------------------------------
\29\ The term ``driver power input'' in HI 40.6-2014 is defined
as ``the power absorbed by the pump driver'' and is synonymous with
the term ``driver input power'' and ``input power to the motor and/
or controls,'' as used in this document.
\30\ The term ``volume per unit time'' in HI 40.6 is defined as
``the volume rate of flow in any given section'' and is used
synonymously with ``flow'' and ``flow rate'' in this document.
\31\ The term ``pump total head'' is defined in HI 40.6-2014 as
the difference between the outlet total head and the inlet total
head and is used synonymously with the terms ``total dynamic head''
and ``head'' in this document.
\32\ The term ``pump power output'' in HI 40.6 is defined as
``the mechanical power transferred to the liquid as it passes
through the pump, also known as pump hydraulic power.'' It is used
synonymously with ``hydraulic horsepower'' in this document.
However, where hydraulic horsepower is used to reference the
capacity of a dedicated-purpose pool pump, it refers to the rated
hydraulic horsepower, as defined in section III.G.1.
\33\ The term ``overall efficiency'' is defined in HI 40.6-2014
as a ratio of pump power output to driver power input and describes
the combined efficiency of a pump and driver.
---------------------------------------------------------------------------
DOE also noted that HI 40.6-2014, with several exceptions,
modifications, and additions was adopted in the January 2016 general
pumps test procedure final rule. 81 FR 4086, 4109-4117 (Jan. 25, 2016).
Therefore, HI 40.6-2014, with certain exceptions, is already
incorporated by reference into appendix
[[Page 36888]]
A to subpart Y of part 431. 10 CFR 431.463.
In response to DOE's proposal to incorporate by reference certain
sections of HI 40.6-2014, CEC expressed its support of DOE's proposal.
(CEC, No. 7 at p. 2) Conversely, APSP and Hayward suggested that DOE
consider raising the upper limit of the test fluid required in HI 40.6-
2014 from 86[emsp14][deg]F to 107[emsp14][deg]F to be consistent with
the requirements for other test standards, including NSF-50 and ENERGY
STAR. APSP and Hayward added that this would allow for manufacturers to
establish and maintain one temperature volume of water for NSF, ENERGY
STAR, and DOE testing, allowing for more efficient use of laboratory
resources. (APSP, No. 8 at pp. 5-6; Hayward, No. 6 at p. 4)
In response to APSP and Hayward's suggestion that DOE allow the use
of warmer temperature water for use in testing dedicated-purpose pool
pumps, DOE evaluated the impact of using 107[emsp14][deg]F water as
opposed to water between 50 and 86[emsp14][deg]F on the determined WEF,
rated hydraulic horsepower, or other metrics. Based on DOE's review,
testing with water up to 107[emsp14][deg]F would have an insignificant
impact on the resultant metrics and, therefore, to reduce testing
burden and allow DOE testing to be streamlined with testing for other
programs, DOE is adopting requirements for the test fluid that allow
testing with water up to 107[emsp14][deg]F, as requested by APSP and
Hayward.
Similarly, in their comments, APSP and Hayward also requested that
DOE use a nephelometric turbidity unit (NTU) measurement to determine
and describe the appropriate test fluid for testing dedicated-purpose
pool pumps, as opposed to the kinematic viscosity and maximum density
metrics used in HI 40.6-2014 and proposed by DOE. APSP and Hayward
requested clarification regarding whether test labs would be required
to measure the kinematic viscosity and density of the test water and
whether these parameters would need to be included in test reports and
data. APSP and Hayward stated that test lab water is not currently
measured to determine kinematic viscosity and density. APSP and Hayward
stated that it is not clear what options test labs will have if
incoming municipal supply water does not meet the proposed requirements
for kinematic viscosity and density. APSP and Hayward believe that the
NTU measurement, which is currently referenced in the NSF/ANSI 50-2015
test and was been used in the DPPP industry for over 20 years, is a
more convenient and cost effective criteria to use to specify the
characteristics of the test fluid. (APSP, No.8 at pp. 5-6; Hayward, No.
6 at pp. 4-5).
In response to APSP's and Hayward's suggestion regarding the
characteristics of the test fluid, DOE notes that it reviewed the test
fluid requirements for NSF/ANSI 50-2015, the ENERGY STAR Test Method
for Pool Pumps,\34\ and HI 40.6-2014. As discussed in the September
2016 DPPP test procedure NOPR, section C.3.3, ``Test conditions,'' of
NSF/ANSI 50-2015 specifies test conditions for both swimming pools and
hot tubs/spas in terms of temperature and NTU thresholds, as shown in
Table III.7. That section further states that all pumps, except those
labeled for swimming pool applications only, are to be tested at the
hot tub/spa conditions. 81 FR 64580, 64625-64626 (Sept. 20, 2016).
---------------------------------------------------------------------------
\34\ EPA. 2013. ``ENERGY STAR Program Requirements Product
Specification for Pool Pumps--Final Test Method.'' Available at:
https://www.energystar.gov/sites/default/files/specs/Pool%20Pump%20Final%20Test%20Method%2001-15-2013.pdf.
Table III.7--Test Conditions Specified in NSF/ANSI 50-2015
------------------------------------------------------------------------
Measurement Swimming pool Hot tub/spa
------------------------------------------------------------------------
Water Temperature............... 75 10 102
[deg]F. 10 [deg]F
Turbidity....................... <=15 NTU *........ <=15 NTU
------------------------------------------------------------------------
* NTU = Nephelometric Turbidity Units; a measure of how much light is
scattered by the particles contained in a water sample.
Section 40.6.5.5, ``Test conditions,'' of HI 40.6-2014, which was
proposed to be incorporated by reference into the DPPP test procedure
in the September 2016 DPPP test procedure NOPR, specifies that all
testing must be conducted with ``clear water'' that is between 50 and
86[emsp14][deg]F, where clear water means water with a maximum
kinematic viscosity of 1.6 x 10-5 ft\2\/s and a maximum
density of 62.4 lb/ft\3\. 81 FR at 64614-64615. The ENERGY STAR Test
Method for Pool Pumps \35\ does not appear to contain requirements
regarding the temperature of the test fluid.
---------------------------------------------------------------------------
\35\ EPA. 2013. ``ENERGY STAR Program Requirements Product
Specification for Pool Pumps--Final Test Method.'' Available at:
https://www.energystar.gov/sites/default/files/specs/Pool%20Pump%20Final%20Test%20Method%2001-15-2013.pdf.
---------------------------------------------------------------------------
In response to APSP's and Hayward's concern regarding the
availability of ``clear water'' as defined in HI 40.6-2014, DOE notes
that the characteristics of clear water specified in HI 40.6-2014 are
meant to be inclusive of any fresh water in the temperature range of
interest, as well as sea water, and would certainly be available from
any tap. For reference, the kinematic viscosity of fresh water between
50 and 107[emsp14][deg]F ranges from 1.4 x 10-5 ft\2\/s to
0.69 x 10-5 ft\2\/s, respectively, while the kinematic
viscosity of sea water is approximately 1.24 x 10-5 ft\2\/s
at 68[emsp14][deg]F.\36\ However, DOE acknowledges that DPPP
manufacturers may be less familiar with the measurement of kinematic
viscosity than NTU. As the characterization of the test fluid is not
expected to greatly affect the resultant WEF score, provided testing is
done with municipal water within a reasonable temperature range, DOE
agrees with Hayward that the NTU metric referenced by NSF/ANSI 50-2015
is also an acceptable criteria to describe water that is reasonably
free from impurities for the purposes of testing.
---------------------------------------------------------------------------
\36\ Engineering Toolbox. Liquids--Kinematic Viscosity. Last
accessed Nov. 15, 2016. Available at: https://www.engineeringtoolbox.com/kinematic-viscosity-d_397.html.
---------------------------------------------------------------------------
As discussed in the September 2016 DPPP test procedure NOPR, DOE
noted that the viscosity and density requirements adopted in HI 40.6-
2014 are intended to accomplish the same purpose as the turbidity
limits in NSF/ANSI 50-2015, to ensure the test is conducted with water
that does not have contaminants or additives in such concentrations
that they would affect the thermodynamic properties of the water.
Therefore, to better align with NSF/ANSI 50-2015 and the existing
capabilities and experience of DPPP test labs, in this final rule, DOE
is adopting requirements that testing be carried out with water that is
between 50 and 107[emsp14][deg]F with less than or equal to 15 NTU, as
opposed to the ``clear water'' defined in section 40.6.5.5 of HI 40.6-
2014. DOE will also exclude section 40.6.5.5 of HI 40.6-2014 from the
incorporation by reference into the DOE test procedure, as that section
will no longer be necessary. As a result, measurements of kinematic
viscosity and density of the test fluid will not be required,
minimizing burden on manufacturers. However, measurements of fluid
temperature and NTU will be required to be made and maintained as part
of the test records underlying certification to DOE to ensure that the
test fluid is in accordance with the DOE requirements.
With regard to DOE's proposal to incorporate by reference appendix
D of HI 40.6-2014, ``Suitable Time Periods for Calibration of Test
Instruments,'' APSP and Hayward noted that HI 40.6-2014 does not
explicitly provide an option for historical data to be used as a basis
to support a longer recalibration
[[Page 36889]]
interval than recommended by table D.1 of HI 40.6-2014. APSP and
Hayward stated that this provision used to be available as an option in
HI 14.6-2011. APSP and Hayward added that it currently calibrates all
instruments annually, in accordance with ISO 17025,\37\ which would not
comply with some of the required calibration intervals in HI 40.6-2014,
such as 0.33 years for pressure transducers. As such, APSP and Hayward
suggested DOE include a provision to allow for historical data to be
used to determine longer calibration intervals than currently provided
for in appendix D of HI 40.6-2014 (APSP, No. 8 at pp. 5-6; Hayward, No.
6 at p. 5).
---------------------------------------------------------------------------
\37\ ISO/IEC 17025, ``General requirements for the competence of
testing and calibration laboratories,'' is an internationally
recognized standard that contains specifics on testing, calibration
methods, data quality management systems, and other general
requirements for test laboratories to carry out testing or
calibration. See www.iso.org for more information.
---------------------------------------------------------------------------
In response to APSP's and Hayward's suggestion regarding the
allowance for extended calibration intervals beyond those specified in
appendix D of HI 40.6-2014 based on historical data, DOE agrees that
such a provision used to be available in ANSI/HI 14.6-2011, which
preceded HI 40.6-2014. DOE understands that it is common practice to
extend the calibration interval of some equipment that has
demonstrated, based on past calibration data, to maintain calibration
over several calibration cycles. DOE also recognizes that this can
reduce the burden of maintaining equipment within the specifications
required by the DOE test procedure. As such, DOE believes it is
reasonable to allow the use of historical test data to justify
calibration intervals longer than those specified in table D.1 of HI
40.6-2014 and that such a provision does not compromise the accuracy of
the resultant test data. However, DOE believes additional specificity
is required to ensure that unreasonably long time periods between
calibration intervals are not permitted. Therefore, DOE is adopting
requirements in this final rule that historical calibration data may be
used to justify time periods up to three times longer than those
specified in table D.1 of HI 40.6-2014. In such a case, the supporting
historical data must show maintenance of calibration of the given
instrument up to the selected extended calibration interval on at least
two unique occasions, based on the interval specified in HI 40.6-2014.
For example, in the case of the pressure transducers discussed by
Hayward, Hayward may justify a calibration interval up to 1 year \38\
(three times the calibration interval of 0.33 years specified in HI
40.6-2014) based on calibration data taken at least every 0.33 years
that demonstrates that the calibration has been maintained for 1 year
for at least two different years.
---------------------------------------------------------------------------
\38\ While DOE acknowledges that three times 0.33 is 0.99, 0.99
years can practically be treated as 1 year, as the calibration
intervals are not precise to the hundredths of a year (3
days).
---------------------------------------------------------------------------
China stated, in written comments, its belief that the proposed
test method did not provide a test method for total head. (China, No.
14 at p. 3) DOE disagrees and clarifies that, as stated previously, the
proposed test procedure proposed to incorporate by reference certain
sections of HI 40.6-2014, which contain relevant specifications
regarding test setup, methodology, standard rating conditions,
equipment specifications, uncertainty calculations, and tolerances to
measure pump total head, among other pump performance metrics.
DOE did not receive any comments on any of the other sections of HI
40.6-2014 DOE proposed to incorporate by reference. Therefore, in this
final rule, DOE incorporates by reference HI 40.6-2014, with certain
exceptions, modifications, and additions, into the new appendices B and
C (see section III.H) to subpart Y that will contain the DPPP test
procedure. DOE notes that DOE is using the nomenclature ``HI 40.6-2014-
B'' in the regulatory text to refer to the incorporation by reference
of HI 40.6-2014 for the dedicated-purpose pool pumps test procedure in
appendices B and C and differentiate it from the existing incorporation
by reference of HI 40.6-2014 to appendix A established in the January
2016 general pumps test procedure final rule. 81 FR 4086, 4109-4117
(Jan. 25, 2016).
2. Exceptions, Modifications and Additions to HI 40.6-2014
In general, DOE finds the test methods contained within HI 40.6-
2014 are sufficiently specific and reasonably designed to produce test
results necessary to determine the WEF of applicable dedicated-purpose
pool pumps. However, only certain sections of HI 40.6-2014 are
applicable to the new DPPP test procedure. In addition, DOE requires a
few exceptions, modifications, and additions to ensure test results are
as repeatable and reproducible as possible. DOE's modifications and
clarifications to HI 40.6-2014 are addressed in the subsequent sections
III.E.2.a through III.E.2.g.
a. Applicability and Clarification of Certain Sections of HI 40.6-2014
Although DOE is incorporating by reference HI 40.6-2014 as the
basis for the DPPP test procedure, DOE noted in the September 2016 DPPP
test procedure NOPR that some sections of the standard are not
applicable to the DPPP test procedure and other sections require
clarification regarding their applicability when conducting the DPPP
test procedure. 81 FR 64580, 64615-20 (Sept. 20, 2016). Table III.8
provides an overview of the sections of HI 40.6-2014 that DOE proposed
to exclude from the DOE test procedure for dedicated-purpose pool
pumps, as well as those that DOE proposed to only be optional and not
required for determination of WEF. Id.
Table III.8--Sections of HI 40.6-2014 DOE Proposed To Exclude From Incorporation by Reference or Make Optional
as Part of the DPPP Test Procedure
----------------------------------------------------------------------------------------------------------------
Section No. Title Applicability
----------------------------------------------------------------------------------------------------------------
40.6.4.1................................ Vertically suspended pumps........ Excluded.
40.6.4.2................................ Submersible pumps................. Excluded.
40.6.5.3................................ Test report....................... Excluded.
40.6.5.5.1.............................. Test procedure.................... Certain Portions Optional for
Representations.
40.6.5.5.2.............................. Speed of rotation during test..... Excluded.
40.6.6.1................................ Translation of test results to Excluded.
rated speed of rotation.
40.6.6.2................................ Pump efficiency................... Optional for Representations.
40.6.6.3................................ Performance curve................. Optional for Representations.
A.7..................................... Testing at temperatures exceeding Excluded.
30 [deg]C (86 [deg]F).
Appendix B.............................. Reporting of test results......... Excluded.
----------------------------------------------------------------------------------------------------------------
[[Page 36890]]
In the September 2016 DPPP test procedure NOPR, DOE discussed in
detail the specific rationale for excluding or making optional certain
sections of HI 40.6-2014. 81 FR 64580, 64615 (Sept. 20, 2016).
In response to DOE's proposal to exclude certain sections from the
incorporation by reference of HI 40.6-2014, while making other sections
optional for representations, Hayward suggested DOE reconsider the
exception of section A.7 of HI 40.6-2017, ``Testing at temperatures
exceeding 30 [deg]C (86 [deg]F),'' in light of their other suggestions
related to elevated test fluid temperatures discussed in section
III.E.1. Pentair commented that section 40.6.5.5.2, which requires the
speed of the pump to be within 80 to 120 percent of the rated speed,
should remain a stipulation of testing and should not be excluded,
especially for single- and two-speed induction motor pumps, as NEMA-MG
requires only better than 7.5 percent of the regulated speed. (Pentair,
No. 11 at p. 3) China also commented that the proposed test procedure
did not define a test method for rotating speed and, similarly,
suggested maintaining speed between 80 and 110 percent of rated
rotating speed. (China, No. 14 at p. 3)
In response to Hayward's comment regarding the proposed exclusion
of section A.7 of HI 40.6-2014, as discussed in section III.E.1, DOE is
adopting alternative criteria to describe the test fluid in lieu of the
criteria specified in HI 40.6-2014. Therefore, a specific accommodation
to test at higher temperatures, as specified in appendix A.7 of HI
40.6-2014, is not required. In addition, DOE notes that the
instructions in section A.7 are not currently very descriptive and
could introduce ambiguity to the test. As such, DOE excludes section
A.7 of HI 40.6-2014 from incorporation by reference in this final rule.
In response to Pentair and China's comments regarding the
measurement of and tolerances related to rotational speed, DOE
clarifies that the adopted test procedure references specific load
points for different varieties and speed configurations of dedicated-
purpose pool pumps, as described in section III.D. These load points
were specifically recommended by the DPPP Working Group and include
specifications regarding the flow, head, and speed at each load point.
For example, single-speed pool filter pumps must be evaluated on curve
C at the maximum speed, which is typically the only speed
available.\39\ Two-speed pool filter pumps must be evaluated at the
maximum and low speed, which are, by definition, the only speeds
available on the pump. The load points for multi-speed and variable-
speed pool filter pumps do not specify speed values, but are described
with respect to specific head and flow requirements. In all cases,
tolerances around a given speed value are not relevant since there is
no ``target'' speed value that must be attained. Instead, DOE describes
tolerances around the tested flow or head values that must be achieved,
as those values have specified values or thresholds that must be
achieved and drive the specification of the load point. While the speed
is integral to attaining a given load point, the tested speed is a
dependent variable to satisfy the required head and flow values based
on the capabilities of the pump. Therefore, DOE does not believe that
allowing measurements at alternative speeds, either those specified in
section 40.6.5.5.2 or NEMA MG-1-2016, is necessary or relevant to the
DPPP test procedure. In addition, DOE understands the primary purpose
of section 40.6.5.5.2 is to accommodate testing of very large pumps
that may overload the power supply of the test lab when run at full
speed. DOE does not believe this is a concern for dedicated-purpose
pool pumps, most of which are less than 2.5 rated hydraulic horsepower.
Therefore, this final rule does not incorporate by reference section
40.6.5.5.2, and requires all testing to be conducted at the appropriate
load points specified in section III.D for each DPPP variety and speed
configuration. Regarding measurement of speed, DOE notes that HI 40.6-
2014, which is incorporated by reference in the adopted test procedure,
includes specifications for measuring rotating speed.
---------------------------------------------------------------------------
\39\ As described in more detail in section III.D.1.e, if a
dedicated-purpose pool pump does not meet the definition of a two-
speed, multi-speed, or variable-speed dedicated-purpose pool pump
discussed in section III.B.7, or the necessary criteria to apply the
two-speed test method discussed in section III.D.1.e, such a pump
must be tested using the single-speed pool filter pump test point,
regardless of the number of operating speeds the pump may have.
---------------------------------------------------------------------------
DOE did not receive any other comments pertaining to the other
sections DOE proposed to exclude from DOE's incorporation by reference.
Therefore, in this final rule, DOE is not incorporating by reference
section 40.6.4.1, 40.6.4.2, 40.6.5.3, 40.6.5.5.2, 40.6.6.1, section A.7
of appendix A, and appendix B of HI 40.6-2014 as part of the DOE test
procedure for dedicated-purpose pool pumps. In addition, as discussed
in section III.E.1, as DOE is adopting alternative criteria to describe
the test fluid. For that reason, DOE is also excluding section 40.6.5.5
from the incorporation by reference of HI 40.6-2014. To allow
manufacturers to make voluntary representations of other metrics, in
addition to WEF, DOE incorporates by reference section 40.6.5.5.1,
section 40.6.6.2, and section 40.6.6.3, of HI 40.6-2014 and clarifies
that these sections are not required for determination of WEF, but may
be optionally conducted to determine and make representations about
other DPPP performance parameters.
b. Calculation of Hydraulic Horsepower
In addition to the clarifications regarding the applicability of
certain sections of HI 40.6-2014 to the DPPP test procedure, DOE
believes that clarification is also required regarding the calculation
of hydraulic horsepower. As discussed in the September 2016 DPPP test
procedure NOPR, DOE proposed that hydraulic horsepower must be
calculated with a unit conversion factor of 3956, instead of 3960,
which is specified in HI 40.6-2014. 81 FR 64580, 64617 (Sept. 20,
2016). DOE explained that using a value of 3956 is more accurate and
precise given the properties of the specified test fluid. Also, as
noted, in the September 2016 DPPP test procedure NOPR, the conversion
factor of 3956 was adopted also in the January 2016 general pumps test
procedure final rule. 81 FR 4086, 4109 (Jan. 25, 2016).
In response to DOE's proposal, during the September 2016 DPPP test
procedure NOPR public meeting, Hayward sought clarification from DOE,
as it believed that the value referred to the rotating speed of the
pump. Hayward questioned whether this was the same value used during
the DPPP Working Group meetings. (Hayward, Public Meeting Transcript,
No. 3 at pp. 62-63) In response, during the September 2016 DPPP test
procedure NOPR public meeting, Pentair clarified that the value was a
unit conversion (Pentair, Public Meeting Transcript, No. 3 at pp. 62-
63) and DOE clarified that the value of 3956 (as proposed in the
September 2016 DPPP test procedure NOPR) was the one used throughout
the DPPP Working Group meetings. APSP and Hayward later suggested, in
their written comments, that the DPPP test procedure continue to rely
on the 3960 value historically used in all hydraulic power
calculations. (APSP, No. 8 at p. 6)
While DOE believes that the value of 3956 proposed in the September
2016
[[Page 36891]]
DPPP test procedure NOPR is more precise and accurate given the
specific gravity of 1.0 assumed in the calculation of hydraulic power,
the value of the unit conversion (3956 or 3960) does not meaningfully
impact the resultant rated hydraulic horsepower within the number of
number of digits to which rated hydraulic horsepower is to be reported.
Therefore, in this final rule, DOE adopts a requirement that hydraulic
horsepower must be calculated with a unit conversion factor of 3960,
consistent with Hayward's request.
c. Data Collection and Determination of Stabilization
The DPPP test procedure must provide instructions regarding how to
sample and collect data at each load point. Such instructions must
ensure that the collected data are taken at stabilized conditions that
accurately and precisely represent the performance of the dedicated-
purpose pool pump at the designated load points, thus improving
repeatability of the test.
In the September 2016 DPPP test procedure NOPR, DOE explained that
section 40.6.5.5.1 of HI 40.6-2014 provides that all measurements shall
be made under steady state conditions. DOE stated that the requirements
for determining when the pump is operating under steady state
conditions in HI 40.6-2014 were described as follows: (1) There is no
vortexing, (2) the margins are as specified in ANSI/HI 9.6.1,
``Rotodynamic Pumps Guideline for NPSH Margin,'' and (3) the mean value
of all measured quantities required for the test data point remains
constant within the permissible amplitudes of fluctuations defined in
Table 40.6.3.2.2 of HI 40.6-2014 over a minimum period of 10 seconds
before performance data are collected. 81 FR 64580, 64617 (Sept. 20,
2016).
In addition to the requirements specified in section 40.6.5.5.1 of
HI 40.6-2014, in the September 2016 DPPP test procedure NOPR, DOE
proposed requirements that at least two unique measurements must be
used to determine stabilization when testing pumps according to the
DPPP test procedure. 81 FR 64580, 64617 (Sept. 20, 2016). DOE explained
within the September 2016 test procedure NOPR, that HI 40.6-2014 does
not specify the measurement interval for determination of steady state
operation. Id. DOE's proposal of two measurements is the same as the
requirement established in the January 2016 general pumps test
procedure final rule. 81 FR 4086, 4011 (Jan. 25, 2016). This
requirement accommodates a longer period between the sampling of
individual data points, as compared to the ENERGY STAR program. 81 FR
64580, 64617 (Sept. 20, 2016).
Section 40.6.3.2.2 of HI 40.6-2014, ``Permissible fluctuations,''
specifies that permissible damping devices may be used to minimize
noise and large fluctuations in the data in order to achieve the
specifications noted in Table 40.6.3.2.2 of HI 40.6-2014. In the
September 2016 DPPP test procedure NOPR, similar to the January 2016
general pumps test procedure final rule (81 FR 4086, 4011 (Jan. 25,
2016)), DOE proposed that damping devices are only permitted to
integrate up to the measurement interval to ensure that each
stabilization data point is reflective of a separate measurement. 81 FR
64580, 64617 (Sept. 20, 2016). DOE also proposed in the September 2016
DPPP test procedure NOPR that, for physical dampening devices, the
pressure indicator/signal must register 99 percent of a sudden change
in pressure over the measurement interval to satisfy the requirement
for unique measurements. This requirement is consistent with annex D of
ISO 3966:2008(E), ``Measurement of fluid flow in closed conduits--
Velocity area method using Pitot static tubes,'' which is referenced in
HI 40.6-2014 for measuring flow with pitot tubes. 81 FR 64580, 64617
(Sept. 20, 2016).
In response to DOE's proposed stabilization requirements,
particularly those incorporated by reference in section 40.6.5.5.1 of
HI 40.6-2014, APSP and Hayward requested clarification of the
definition of ``vortexing'' and an explanation of how to specifically
determine if vortices are, or are not present. (APSP, No. 8 at pp.6-7;
Hayward, No. 6 at p. 6) In response, DOE acknowledges that DOE did not
propose a definition for ``vortexing'' or ``vortices,'' and such
definitions are not contained in HI 40.6-2014. After reviewing the
context of section 40.6.5.5.1 of HI 40.6-2014, DOE concludes that the
language of ``no vortexing'' is a redundant, but informative statement,
related to defining steady state conditions. In other words, vortexing
is a specific scenario, which would cause test readings to fluctuate
beyond the permissible amplitudes of fluctuations defined in Table
40.6.3.2.2 of HI 40.6-2014 over a minimum period of 10 seconds before
performance data are collected. Accordingly, DOE will not establish any
further definitions or verification procedures related to vortexing or
vortices. Under section 40.6.5.5.1 of HI 40.6-2014, as incorporated by
reference into the test procedure, steady state is achieved when the
mean value of all measured quantities required for the test data point
remain constant within the permissible amplitudes of fluctuations
defined in Table 40.6.3.2.2 over a minimum time of 10 seconds before
data are collected. No explicit measurement or determination of
vortexing or vortices is required.
DOE did not receive any additional comments on this proposal and,
therefore, is adopting, in this final rule, the proposal that
determination of stabilization must be made based on at least two
unique measurements and any damping devices are only permitted to
integrate up to the data collection interval.
d. Test Tolerances
As discussed in section III.D, DOE proposed in the September 2016
DPPP test procedure NOPR to specify unique load points for each DPPP
variety and speed configuration. As DOE noted in the September 2016
DPPP test procedure NOPR, HI 40.6-2014 does not specify how close a
measured data point must be to the specified load point or if that data
point must be corrected in any way for deviations from the specified
value. 81 FR 64580, 64617-18 (Sept. 20, 2016).
In the September 2016 DPPP test procedure NOPR, consistent with the
tolerances adopted in the ENERGY STAR test procedure, DOE proposed
tolerances of 2.5 percent on flow rate for self-priming and
non-self-priming pool filter pumps and pressure cleaner booster pumps.
However, due to the fact that the load point for waterfall pumps is
specified as a fixed head value, DOE proposed a tolerance of 2.5 percent of head for waterfall pumps. DOE did not propose a
tolerance on the tested speed, as the tested maximum speeds are
specific to each dedicated-purpose pool pump being tested. 81 FR 64580,
64617-18 (Sept. 20, 2016).
In response to DOE's proposal, APSP and Hayward commented that
maintaining 2.5 percent of the specified flow rate or head
value will be difficult to achieve, particularly with regards to the 10
gpm load point for pressure cleaner booster pumps. APSP and Hayward
requested any exemplary data that demonstrates stabilization can be
maintained within the specified tolerance at low head or flows and that
DOE consider a larger tolerance for low flow or head measurements
(APSP, No. 8 at p. 7; Hayward, No. 6 at p. 6).
In response to APSP's and Hayward's request for larger tolerances
on low flow and head values, DOE reiterates that DOE based the proposal
in the
[[Page 36892]]
September 2016 DPPP test procedure NOPR on the existing tolerance
requirements in the ENERGY STAR Test Method for Pool Pumps.\40\ The
ENERGY STAR method applies to all load points specified by the test
method, including the minimum speed test point for variable-speed
dedicated-purpose pool pumps. DOE also notes that the flow rates on
Curves A, B, and C at minimum flow rate for many variable-speed
dedicated-purpose pool pumps are at or below 10 gpm, as demonstrated in
DOE's Self-Priming Pool Filter Pump Performance Database. (Docket No.
EERE-2015-BT-STD-0008, No. 102) Specifically, 43 of the 83 total
variable-speed self-priming pool filter pumps in DOE's database report
flow rates less than or equal to 10 gpm and at least 19 of those 43
models are from the ENERGY STAR database.\41\ Based on the fact that
such requirements can be met to certify pumps in accordance with ENERGY
STAR, DOE believes that such a requirement can be met when conducting
the DOE DPPP test procedure. Although the pumps in the ENERGY STAR
database should be conforming to the flow and head tolerances, DOE does
not have access to source data to confirm this. Therefore, in light of
Hayward's comment, in this final rule, DOE is adopting a broader
tolerance requirement for lower flow scenarios. Specificity, the flow
tolerance will be 2.5 percent of the specified flow rate or
0.5 gpm, whichever is greater. DOE believes that a range of
1.0 gpm can reasonably be maintained with typical lab testing
equipment. DOE notes that such an accommodation is not necessary for
waterfall pumps, since the tolerance is a fixed 17.0 0.425
feet.
---------------------------------------------------------------------------
\40\ EPA. 2013. ``ENERGY STAR Program Requirements Product
Specification for Pool Pumps--Final Test Method.'' Available at:
https://www.energystar.gov/sites/default/files/specs/Pool%20Pump%20Final%20Test%20Method%2001-15-2013.pdf.
\41\ ENERGY STAR maintains a database of certified products,
including pool pumps. See https://www.energystar.gov/productfinder/product/certified-pool-pumps/results.
---------------------------------------------------------------------------
In addition, based on the revised load points for multi-speed and
variable-speed pool filter pumps presented in section III.D.1.c, DOE
notes that the multi-speed and variable-speed pool filter pump load
points are now specified with respect to the head value (i.e., H =
0.0082 x Q\2\), while the flow point may vary based on the operating
speeds available on the pump. Therefore, in this final rule, DOE is
revising the tolerances for the multi-speed and variable-speed pool
filter pump test points to be achieved within 2.5 percent
of the specified head value, which is curve C. DOE is adopting all
other tolerances as proposed in the September 2016 DPPP test procedure
NOPR.
e. Power Supply Characteristics
In the September 2016 DPPP test procedure NOPR and consistent with
the January 2016 general pumps test procedure final rule (81 FR 4086,
4112-4115 (Jan. 25, 2016)), DOE proposed tolerances for voltage,
frequency, voltage unbalance, and total harmonic distortion that must
be maintained at the input terminals to the motor and/or control, as
applicable, when conducting the DPPP test procedure. 81 FR 64580,
64618-19 (Sept. 20, 2016). DOE discussed how the measurement of input
power to the driver is an important element of the test, because input
power is a key component of WEF. In addition, in the September 2016
DPPP test procedure NOPR, DOE discussed how large differences in
voltage, frequency, voltage unbalance, or total harmonic distortion can
affect the performance of the motor and/or control under test. Id.
DOE believes that, because dedicated-purpose pool pumps utilize
electrical equipment (i.e., motors and drives) similar to that used by
general pumps, such requirements also apply when testing dedicated-
purpose pool pumps. In the September 2016 DPPP test procedure NOPR, DOE
proposed that when testing dedicated-purpose pool pumps the following
conditions would apply to the main power supplied to the motor or
controls, if any:
Voltage maintained within 5 percent of the
rated value of the motor.
Frequency maintained within 1 percent of the
rated value of the motor.
Voltage unbalance of the power supply maintained within
3 percent of the rated value of the motor.
Total harmonic distortion maintained at or below 12
percent throughout the test. 81 FR 64580, 64619 (Sept. 20, 2016).
APSP and Hayward submitted comments regarding voltage unbalance of
the power supply. APSP and Hayward were familiar with a voltage
unbalance in a three-phase power supply, but were unclear about how it
applied to a single-phase power supply. (APSP, No. 8 at p.7; Hayward,
No. 4 at p.1; Hayward, No. 6 at pp. 6-7) In response, voltage unbalance
or imbalance is defined as the largest difference between the average
RMS voltage and the RMS value of any single voltage phase divided by
the average RMS voltage, usually expressed as a percentage.\42\ Voltage
unbalance is a function of multiple phase power supplies and, by
definition, does not exist in single-phase power supplies. As there is
no voltage unbalance in a single-phase power supply, the requirement to
maintain voltage unbalance within 3 percent of the rated
value of the motor only applies to pumps with motors driven by a three-
phase power supply.
---------------------------------------------------------------------------
\42\ An overview by DOE on voltage unbalance can be found at:
https://energy.gov/sites/prod/files/2014/04/f15/eliminate_voltage_unbalanced_motor_systemts7.pdf.
---------------------------------------------------------------------------
APSP and Hayward also requested that DOE confirm that the voltage
unbalance specification of ``3 percent of the rated value
of the motor'' applies to the rated voltage of the motor. (APSP, No. 8
at p. 7; Hayward, No. 6 at pp. 6-7) In response, DOE agrees that the
proposal in the September DPPP 2016 test procedure NOPR could be
clarified. DOE understands that motors typically do not have nominal
rated voltage unbalance values, similar to the nominal rated frequency
and voltage values listed on many motor nameplates. In this case
``3 percent of the rated value of the motor'' refers to
``the value at which the motor was rated.'' That is, the value is
referring to the voltage unbalance associated with the rated efficiency
of the motor. DOE also notes that, in IEEE Standard 112-2004, ``IEEE
Standard Test Procedure for Polyphase Induction Motors and
Generators,'' (IEEE 112-2004) and the Canadian Standards Association
(CSA) C390-10, ``Test methods, marking requirements, and energy
efficiency levels for three-phase induction motors,'' (CSA C390-10),
which are the test methods incorporated by reference as the DOE test
procedure for electric motors, a voltage unbalance of <=0.5 percent is
required. Therefore, the requirement of ``3 percent of the
value at which the motor was rated'' can also be interpreted as <=3.5
percent for motors rated in accordance with DOE's electric motor test
procedure. In this final rule, DOE will specify the voltage unbalance
requirement as ``3 percent of value with which the motor
was rated.''
During the September 2016 DPPP test procedure NOPR public meeting,
CA IOUs, DOE, and Hayward discussed total harmonic distortion (THD).
Hayward inquired about differences related to tolerances between the
September 2016 DPPP test procedure NOPR and ENERGY STAR and
specifically sought indication of whether the tolerances in DOE's
proposal were more stringent than ENERGY STAR. (Hayward, Public
[[Page 36893]]
Meeting Transcript, No. 3 at p. 58) DOE responded during the September
2016 DPPP test procedure NOPR public meeting that ENERGY STAR requires
THD to be less than 2 percent and DOE's proposal was less than 12
percent. (DOE, Public Meeting Transcript, No. 3 at p. 59) CA IOUs noted
that ENERGY STAR's THD requirements were much more stringent than the
proposed DOE requirements and raised questions if current test labs can
comply with this value. (CA IOUs, Public Meeting Transcript, No. 3 at
pp. 59-60) Hayward responded that upon initial review, if a
manufacturer is already conducting ENERGY STAR testing in-house, that
the DOE proposal does not seem more stringent, nor did Hayward believe
that the DOE proposal would require any more elaborate equipment.
(Hayward, Public Meeting Transcript, No. 3 at p. 60) CA IOUs responded
that a different THD value might be necessary in that the DOE's
proposal of 12 percent seems unreasonably high, but ENERGY STAR's
requirement of 2 percent seems unreasonably low. (CA IOUs, Public
Meeting Transcript, No. 3 at p. 60)
Regarding Hayward's inquiry as to the relative stringency of DOE's
proposed power supply characteristics as compared to the ENERGY STAR
\43\ test procedure for pool pumps,\44\ DOE notes that all of DOE's
proposed power supply characteristic requirements are equivalent to or
less stringent than the existing ENERGY STAR requirements, as shown in
Table III.9.
---------------------------------------------------------------------------
\43\ ENERGY STAR is a joint program of the U.S. Environmental
Protection Agency (EPA) and DOE that establishes a voluntary rating,
certification, and labeling program for highly energy efficient
consumer products and commercial equipment. Information on the
program is available at www.energystar.gov/index.cfm?c=home.index.
\44\ EPA. 2013. ``ENERGY STAR Program Requirements Product
Specification for Pool Pumps--Final Test Method. Rev. Jan-2013''
https://www.energystar.gov/sites/default/files/specs/Pool%20Pump%20Final%20Test%20Method%2001-15-2013.pdf.
Table III.9--Comparison of Power Supply Characteristics Requirements Proposed in DOE's September 2016 DPPP Test
Procedure NOPR and in the ENERGY STAR Test Method for Pool Pumps \45\
----------------------------------------------------------------------------------------------------------------
DOE September 2016 DPPP test
Power supply characteristic procedure NOPR proposal ENERGY STAR
----------------------------------------------------------------------------------------------------------------
Voltage................................. within 5 percent of within 1.0 percent of
the rated value of the motor. the rated value of the motor.
Frequency............................... within 5 percent of within 1.0 percent of
the rated value of the motor. the rated value of the motor.
Voltage Unbalance....................... within 3 percent of N/A.
the rated value of the motor.
Total Harmonic Distortion............... <=12 percent...................... <=2.0 percent.
----------------------------------------------------------------------------------------------------------------
With regard to CA IOUs comment regarding DOE's proposed tolerance
on THD perhaps being too large, DOE notes that the THD tolerance of 12
percent was developed based on reasonable limits that motor systems
should be designed to handle. Further, a THD tolerance of 12 percent is
widely available on the national electrical grid and, therefore, is not
unduly burdensome to attain during testing. DOE discussed this
justification, at length, in the January 2016 general pumps test
procedure final rule. 81 FR 4086, 4112-4118 (Jan. 25, 2016) For
example, regarding limitations on harmonic distortion on the power
supply, the AMO publication, ``Improving Motor and Drive System
Performance'' (AMO motor sourcebook) states that electrical equipment
is often rated to handle 5 percent THD (as defined in IEEE 519-2014
\46\), and notes that motors are typically much less sensitive to
harmonics than computers or communication systems.\47\ In addition,
section 5.1 of IEEE 519-2014 recommends line-to-neutral harmonic
voltage limits of 5.0 percent individual harmonic distortion and 8.0
percent voltage THD for weekly 95th percentile short time (10 min)
values, measured to the 50th harmonic. The IEEE standard also indicates
that daily 99th percentile very short time (3 second) values should be
less than 1.5 times these values.
---------------------------------------------------------------------------
\45\ EPA. 2013. ``ENERGY STAR Program Requirements Product
Specification for Pool Pumps--Final Test Method. Rev. Jan-2013''
https://www.energystar.gov/sites/default/files/specs/Pool%20Pump%20Final%20Test%20Method%2001-15-2013.pdf.
\46\ IEEE. 2014. Standard 519: ``IEEE Recommended Practice and
Requirements for Harmonic Control in Electric Power Systems.''
Available at: https://standards.ieee.org/findstds/standard/519-2014.html.
\47\ DOE EERE. Improving Motor and Drive System Performance--A
Sourcebook for Industry. February 2014. Available at www.energy.gov/eere/amo/motor-systems.
---------------------------------------------------------------------------
Hayward also submitted written comments stating that DOE's proposed
voltage, frequency, voltage unbalance, and THD requirements are
suitable for testing dedicated-purpose pool pumps and were reasonably
achievable in existing laboratory environments. (Hayward, No. 6 at p.
7) Additionally, Hayward submitted written comments that the proposed
power supply requirements in the September 2016 DPPP test procedure
NOPR are in alignment with (or not as stringent as) the power supply
requirements for other pool pump industry programs including ENERGY
STAR, NSF, and UL. (Hayward, No. 6 at p. 7) Similarly, APSP stated that
DOE's proposed power supply requirements were less stringent than the
requirements used in DOE motor efficiency testing. (APSP, No. 8 at p.
7) Both APSP and Hayward felt that existing equipment would be more
than capable of meeting the proposed requirements. (APSP, No. 8 at p.
7; Hayward, No. 6 at p. 7). Ultimately, for the reasons discussed in
this section, DOE adopts requirements in this final rule that when
testing dedicated-purpose pool pumps the main power supplied to the
motor or controls, if any, must maintain voltage within 5
percent of the rated value of the motor, frequency within 1
percent of the rated value of the motor, voltage unbalance of the power
supply maintained within 3 percent of the value with which
the motor was rated, and total harmonic distortion maintained at or
below 12 percent throughout the test.
f. Measurement Equipment for Testing
Appendix C of HI 40.6-2014, which DOE is incorporating by reference
into the DPPP test procedure, specifies the required instrumentation to
measure head, speed, flow rate, torque, temperature, and electrical
input power to the motor. In the September 2016 DPPP test procedure
NOPR, DOE proposes to refer to appendix C of HI 40.6-2014, as
incorporated by reference (see section III.E.1), to specify the
required instrumentation to measure head, speed, flow rate, and
temperature in the DPPP test procedure. 81 FR 64580, 64619-64620 (Sept.
20, 2016). However, DOE noted that for the purposes of measuring input
power to the motor or control, as applicable, of DPPP models, the
equipment specified in section C.4.3.1, ``electric power input to the
motor,'' of HI 40.6-2014 may not be sufficient. Instead, DOE proposed
requirements that electrical measurements for determining pump
[[Page 36894]]
power input be taken using equipment capable of measuring current,
voltage, and real power up to at least the 40th harmonic of fundamental
supply source frequency \48\ and have an accuracy level of 2.0 percent of the measured value when measured at the
fundamental supply source frequency when rating pumps using the
testing-based methods or with a calibrated motor. Id. These proposed
requirements are consistent with other relevant industry standards \49\
for measurement of input power to motor and drive systems and the
January 2016 general pumps test procedure final rule. 81 FR 4086, 4118-
19 (Jan. 25, 2016) DOE notes that the September 2016 DPPP test
procedure NOPR contained inconsistent statements with regard to whether
the accuracy requirement was with respect to full scale or the measured
value. Specifically, the preamble (81 FR 64619-64620) discussed the
accuracy requirement with respect to full scale, while the proposed
regulatory text discussed accuracy requirements with respect to the
measured value (81 FR 64650). The proposed regulatory text contained
the correct proposal, which is that electrical measurement equipment
must be accurate to 2.0 percent of the measured value. DOE
notes that this is consistent with the requirements adopted in the
January 2016 general pumps test procedure final rule and is less
stringent than the requirements contained in the ENERGY STAR Test
Method for Pool Pumps,\50\ which requires accuracy of 1.5 percent of
the measured value for power measurement.
---------------------------------------------------------------------------
\48\ CSA C838-13 requires measurement up to the 50th harmonic.
However, DOE believes that measurement up to the 40th harmonic is
sufficient, and the difference between the two types of frequency
measurement equipment will not be appreciable.
\49\ Specifically, DOE identified AHRI 1210-2011, ``2011
Standard for Performance Rating of Variable Frequency Drives''; the
2013 version of CSA Standard C838, ``Energy efficiency test methods
for three-phase variable frequency drive systems''; CSA C390-10,
``Test methods, marking requirements, and energy efficiency levels
for three-phase induction motors''; and IEC 61000-4-7, ``Testing and
measurement techniques--General guide on harmonics and
interharmonics measurements and instrumentation, for power supply
systems and equipment connected thereto'' as relevant to the
measurement of input power to the motor or control.
\50\ EPA. 2013. ``ENERGY STAR Program Requirements Product
Specification for Pool Pumps--Final Test Method.'' Available at:
https://www.energystar.gov/sites/default/files/specs/Pool%20Pump%20Final%20Test%20Method%2001-15-2013.pdf.
---------------------------------------------------------------------------
In response to DOE's proposal, Hayward commented that the
manufacturer of the power analyzer within Hayward's lab met the level
of accuracy proposed in the September 2016 DPPP test procedure NOPR.
(Hayward, No. 6 at p. 11) APSP also commented that currently existing
motor test data acquisition equipment is adequate to meet the tolerance
limits proposed by DOE. (APSP, No. 8 at p. 7)
Therefore, for the reasons discussed in this section, DOE adopts
that electrical measurement equipment must be capable of measuring
current, voltage, and real power up to at least the 40th harmonic of
fundamental supply source frequency and having an accuracy level of
2.0 percent of the measured value when measured at the
fundamental supply source frequency.
DOE also noted in the September 2016 DPPP test procedure NOPR that
HI 40.6-2014 does not contain any requirements for the instruments used
for measuring distance. Distance must be measured when determining the
self-priming capability of self-priming and non-self-priming pool
filter pumps (see section III.G.2). 81 FR 64580, 64620 (Sept. 20,
2016). As such, DOE proposed in the September 2016 DPPP test procedure
NOPR to require instruments for measuring distance that are accurate to
and have a resolution of at least 0.1 inch to improve
consistency and repeatability of test results. Id. DOE noted that,
although this accuracy requirement is generally applicable, when used
in combination with other instruments to measure head, both the
accuracy requirements of distance-measuring instruments and the
specified accuracies for measurement of differential, suction, and
discharge head apply. Id.
DOE received no comments related to this proposal. Therefore, in
this final rule, DOE requires instruments for measuring distance that
are accurate to and have a resolution of at least 0.1 inch.
g. Calculation and Rounding Modifications and Additions
DOE notes HI 40.6-2014 does not specify how to round values for
calculation and reporting purposes. DOE recognizes that the manner in
which values are rounded can affect the resulting WEF, and all WEF
values should be reported with the same precision. Therefore, to
improve the accuracy and consistency of calculations, DOE proposed in
the September 2016 DPPP test procedure NOPR that raw measured data be
used to calculate WEF and the resultant value be rounded to the nearest
0.1. 81 FR 64580, 64620 (Sept. 20, 2016). Similarly, DOE proposed that
all values of EF, maximum head, vertical lift, and true priming time be
reported to the tenths place and all other values be reported to the
hundredths place. 81 FR 64580, 64650 (Sept. 20, 2016).
DOE received no comments related to this proposal. However, DOE
notes that the June 2016 DPPP Working Group Recommendations and January
2017 DPPP DFR specify separate standards for self-priming pool filter
pumps with rated hydraulic horsepower greater than or equal to 0.711 hp
and less than 0.711 hp. (Docket No. EERE-2015-BT-STD-0008, No. 82,
Recommendation #1 at pp. 1-2; 86 FR 5650, 5743). As such, DOE notes
that rated hydraulic horsepower must be reported to the thousandths
place, consistent with the precision desired by the DPPP Working Group
in their equipment class specifications. Therefore, in this final rule,
DOE adopts that all calculations shall be performed with raw measured
data; that WEF, EF, maximum head, vertical lift, and true priming time
be rounded to the nearest tenths place; that rated hydraulic horsepower
be reported to the nearest thousandths place; and all other values be
rounded to the hundredths place.
F. Representations of Test Metrics
In the September 2016 DPPP test procedure NOPR, DOE stated that
manufacturers of equipment that are addressed by the proposed test
procedure would have 180 days after the publication of the test
procedure final rule to begin using the DOE procedure as the basis for
representations. However, DOE clarified that manufacturers would not be
required to certify or otherwise make representations regarding the
performance of applicable dedicated-purpose pool pumps using the WEF
metric until the compliance date of any potential energy conservation
standards that DOE might set for dedicated-purpose pool pumps. However,
if manufacturers elect to make representations of WEF prior to such
compliance date, they will be required to do so using the DOE test
procedure. 81 FR 64580, 64627-28 (Sept. 20, 2016).
In the September 2016 DPPP test procedure NOPR, DOE also discussed
how other metrics that are outcomes of the DPPP test procedure would
also need to be updated to be consistent with the final DPPP test
procedure 180 days after publication of the final rule in the Federal
Register. Specifically, DOE also proposed establishing standardized and
consistent methods for determining several DPPP metrics, including DPPP
horsepower metrics, EF, pump efficiency, overall efficiency, driver
power input, pump power output, and power factor. One hundred and
eighty (180) days after the publication of this final rule any
representations of those
[[Page 36895]]
metrics would also be required to be based on values consistent with
the DOE test procedure. DOE notes that some of these test methods and
representations were proposed as optional to allow manufacturers to
make such representations if they chose to. Id.
DOE received many comments related to the representation of
efficiency metrics, including use of alternative metrics, the
definition of a representation, the impact on voluntary programs, and
the timing required to transition to the new test procedure. These
comments and DOE's responses are discussed in the following sections
III.F.1, III.F.2, III.F.3, and III.F.4.
1. Representations of Primary Efficiency Metrics
As discussed in section III.C, DOE is adopting the WEF as the
regulatory metric for defining the energy efficiency of dedicated-
purpose pool pumps. Typically, DOE only includes in the test procedure
the DOE metric (the metric used for the energy conservation standards),
and EPCA requires manufacturers to switch over to use of the DOE metric
for representations beginning 180 days of publication of the test
procedure final rule. This helps ensure standardization of efficiency
representations throughout the industry and eliminates potential
confusion in the market place if multiple non-equivalent metrics are
used to describe the same piece of equipment. DOE believes that
requiring use of the single, standardized DOE metric determined through
a public notice and comment process is the most appropriate approach. A
single, standardized metric that provides a comprehensive picture of
the equipment's energy performance will provide a clear and consistent
basis for consumers to compare and select dedicated-purpose pool pumps.
As described in detail in the September 2016 DPPP test procedure
NOPR, EF is the metric currently used in the industry to describe the
energy performance of dedicated-purpose pool pumps. 81 FR 64580, 64598-
64600 (Sept. 20, 2016). EF describes the efficiency of the dedicated-
purpose pool pump, in terms of gal/Wh, at a single speed point and on a
single system curve. However, there are multiple tested speeds and
system curves that can be used to determine EF, resulting in multiple
EF values. For example, a single pump can have up to nine different EF
values, making selection and comparison of equipment confusing.
Conversely, WEF uses the same measured input data as EF (flow in
gallons and input power in W), but weights the efficiency of the pump
at multiple speeds into one comprehensive and consistent metric that
better represents the average efficiency of the equipment during
typical operation. This makes product comparison and selection more
straightforward. During the DPPP Working Group discussions, the Working
Group members agreed that the weighted average approach was a good
approach to achieve a single energy metric that would be representative
of the energy efficiency of dedicated-purpose pool pumps, while
allowing for an equitable differentiation and comparison of performance
among different DPPP models and technologies and providing the
necessary and sufficient information for purchasers to make informed
decisions regarding DPPP selection. (Docket No. EERE-2015-BT-STD-0008,
No. 38 at pp. 212-213; Docket No. EERE-2015-BT-STD-0008, No. 58 at pp.
170-171 and 178) The DPPP Working Group also agreed that, currently,
comparing the multiple EF values was confusing and made equipment
comparisons difficult. The DPPP Working Group also stated that some of
the EF values did not meaningfully represent the efficiency of the
equipment . (Docket No. EERE-2015-BT-STD-0008, No. 38 at p. 133; Docket
No. EERE-2015-BT-STD-0008, No. 58 at pp. 170-171)
However, the DPPP Working Group also discussed the importance of
the EF metric for making product selections for specific applications
or making energy saving calculations in support of utility programs.
(Docket No. EERE-2015-BT-STD-0008, No. 38 at p. 133 and 213-214; Docket
No. EERE-2015-BT-STD-0008, No. 58 at pp. 167-170 and 174-175) Due to
the interest expressed in the use of the EF metric during the DPPP
Working Group negotiations, in contrast to typical practice, DOE
proposed to allow the representation of two metrics, EF and WEF.
Specifically, DOE proposed to include EF as an optional alternative
metric in addition to WEF. 81 FR 64580, 64627-64628 (Sept. 20, 2016).
DOE notes that the use of this optional additional metric is a unique
allowance in this case, a result of a negotiated rulemaking where the
industry clearly represented the importance of maintaining the use of
the EF metric. DOE provided the DPPP Working Group with an opportunity
through the NOPR to formally express their intent to continue using EF
as an alternative metric at multiple speeds and/or system curves, in
addition to WEF, to describe the energy performance of dedicated-
purpose pool pumps.
In the September 2016 DPPP test procedure NOPR public meeting, the
CA IOUs expressed support for the ability to test EF at different
speeds, in addition to the DOE metric. (CA IOUs, Public Meeting
Transcript, No. 3 at pp. 78-79) However, other commenters requested
clarification regarding the allowance for the representation of two
metrics in DOE's proposal and described how the use of multiple metrics
may cause confusion and complicate ratings with other voluntary
industry programs. Specifically, during the public meeting and
subsequent written comments, APSP, Pentair, and Hayward expressed
confusion and concern related to representations of EF, coordination
with ENERGY STAR and other entities, and standardization of reported
metrics across the industry. (Pentair, Public Meeting Transcript, No. 3
at pp. 8-9, Hayward, No. 6 at p. 1, APSP, No. 8 at p. 2; Pentair, No.
11 at p. 5)
DOE notes that such representations are governed by statute. EPCA
requires that, manufacturers of dedicated-purpose pool pumps within the
scope of the DPPP test procedure will be required to use the test
procedure established in this rulemaking when making representations
about the energy efficiency or energy use of their equipment.
Specifically, 42 U.S.C. 6314(d) provides that, ``[e]ffective 180 days
after a test procedure rule applicable to any covered equipment is
prescribed . . . , [n]o manufacturer . . . may make any representation
. . . respecting the energy consumption of such equipment or cost of
energy consumed by such equipment, unless such equipment has been
tested in accordance with such test procedure and such representation
fairly discloses the results of such testing.''
Therefore, beginning 180 days after publication of this final rule,
any representations made with respect to the energy use or efficiency
of dedicated-purpose pool pumps subject to testing pursuant to 10 CFR
431.464(b) must be made in accordance with the results of testing
pursuant to appendix B. Manufacturers will not be required to certify
or make or make other representations regarding the performance of
applicable dedicated-purpose pool pumps using the WEF metric until July
19, 2021, the compliance date of energy conservation standards for
dedicated-purpose pool pumps. If, however, manufacturers elect to make
representations of efficiency prior to July 19, 2021, they will be
required to do so using a measurement of the WEF metric derived from
use of the DOE test procedure.
[[Page 36896]]
Given the confusion regarding the use of the optional metrics
expressed by the majority of interested parties, DOE is adopting, in
this final rule, modifications to its proposal to ensure consistency
with DOE's test procedure in the long term. Specifically, DOE is
providing a test procedure to derive an EF metric, but only for
representations made before July 19, 2021, the compliance date of any
energy conservation standards for dedicated-purpose pool pumps. Thus,
in this final rule, DOE is adopting two appendices. The first (appendix
B) must be used beginning 180 days after publication of the final rule
until July 19, 2021, the compliance date of energy conservation
standards and includes both WEF and the optional EF method. However,
DOE notes that if appendix B is used to make representations of the
optional metric EF, the manufacturer must also make representations of
the required metric WEF, such that, as required by EPCA, the
representations ``fairly disclose the results of testing'' under
appendix B. (42 U.S.C. 6314(d)).
The second appendix (C) includes only the WEF metric. Manufacturers
must make representations in accordance with appendix C on or after
July 19, 2021, the compliance date of the adopted energy conservation
standards, including when certifying compliance with those standards.
As appendix C does not provide a procedure to arrive at an EF metric,
after July 19, 2021, representations of EF will no longer be allowed.
Through the use of these two appendices, DOE is clarifying that the
industry has until July 19, 2021, the compliance date of adopted energy
conservation standards to transition completely to WEF. DOE believes
that the transition to use of this one, standardized metric will reduce
confusion among manufacturers and in the marketplace. However, prior to
July 19, 2021, DOE is allowing manufactures to continue to make
representations using the EF metric, if tested in accordance with the
appendix B, during the transition to representations using only the WEF
metric derived from the test procedures in appendix C. DOE is allowing
this optional continued use of EF until July 19, 2021, to provide the
industry with increased time to transition fully to the new WEF metric,
due to the interest in maintaining the EF metric expressed by the DPPP
Working Group. DOE also notes that use of appendix B is optional and
manufacturers may decline to make representations of EF and WEF, or any
other DPPP metrics, until July 19, 2021, when representations must be
based on the results of testing under appendix C.
2. Definition of Representation
In response to the September 2016 DPPP test procedure NOPR, Hayward
requested a definition of the term representation. (Hayward, No. 6 at
p. 1) During the NOPR public meeting Hayward also requested that DOE
provide an example of what would be a typical representation applied to
other regulated products. (Hayward, Public Meeting Transcript, No. 3 at
p. 9)
In response, DOE notes that there is no formal definition of
representation. However, as noted previously, 42 U.S.C. 6314(d), which
establishes the 180-day representation requirements, states that
manufacturers, distributors, retailers, and private labelers are
prohibited from making ``any representation--in writing (including any
representation on a label) or in any broadcast advertisement respecting
the energy consumption of such equipment or cost of energy consumed by
such equipment, unless such equipment has been tested in accordance
with such test procedure and such representation fairly discloses the
results of such testing.'' Therefore, representations include any and
all values that are generated by the test procedure, as well as any
statement regarding the energy consumption or cost of energy consumed.
Representations include, for example, any information included in
operation and installation manuals, in marketing materials, on a Web
site, or on the equipment label, as well as verbal statements made in
broadcast advertisements.
In response to Hayward's request for an example of what would be a
typical representation, potentially for a different product or piece of
equipment, DOE provided the example at the September 2016 DPPP test
procedure NOPR public meeting of a residential refrigerator where any
representation of how much electricity the refrigerator consumes made
in a manufacturer's literature or on their Web site would need to be
made based on the appropriate DOE test procedure for that product. DOE
stated that any metrics that come out of the DOE test procedure must be
based on testing in accordance with that test procedure. (DOE, Public
Meeting Transcript, No. 3 at pp. 9-10). For dedicated-purpose pool
pumps, the relevant metrics as proposed were WEF, EF, rated hydraulic
horsepower, DPPP nominal motor horsepower, DPPP total horsepower, DPPP
service factor, true power factor, and maximum head, as well as pump
efficiency, overall (wire-to-water) efficiency, driver power input, and
pump power output (hydraulic horsepower), graphically or in numerical
form, and potentially at a variety of speeds or load points.
3. Impact on Voluntary and Other Regulatory Programs
Hayward asked whether or not current the current reporting of data
(e.g., EF, horsepower, service factor, etc.) to EPA, CEC, and APSP are
affected by this rulemaking (and whether DOE would work with those
entities to update their standards). (Hayward, No. 6 at p. 1) Pentair
also requested clarification regarding whether or not the EF value
displayed in the ENERGY STAR database would be subject to DOE test
procedures and representation requirements 180 days after publication
of the final rule. (Pentair, Public Meeting Transcript, No. 3 at pp. 8-
9) CA IOUs were supportive of the DOE DPPP test procedure being
incorporated by ENERGY STAR as well as if ENERGY STAR or other
organizations wanted to test at different speeds, they could use the
DOE test procedure, but specify the speed accordingly. (CA IOUs, Public
Meeting Transcript, No. 3 at pp. 78-79)
In response to Hayward and Pentair's comments regarding the
reporting of EF, DOE clarifies that, as discussed previously, 180 days
after publication of the final rule in the Federal Register, all
representations of energy and efficiency metrics, including EF, will
need to be updated to be consistent with the final DPPP test procedure.
This is a statutory requirement of EPCA, not a timeframe set by DOE.
DOE understands that manufacturers of pumps likely have historical test
data which were developed with methods consistent with the DOE test
procedure being adopted in this final rule. DOE notes that it does not
expect that manufacturers will need to regenerate all of the historical
test data as long as the tested units remain representative of the
basic model's current design and the rating remains valid under the
adopted method of test for dedicated-purpose pool pumps. If the testing
methods used to generate historical ratings for DPPP basic models are
substantially different from those adopted in this final rule or the
manufacturer has changed the design of the basic model, the
representations resulting from the historical methods would no longer
be valid.
APSP and Hayward noted that because DOE proposes EF as kgal/kWh, it
is not consistent with other programs that require reporting it as gal/
Wh, and therefore the same number would be reported with different
units. (APSP, No. 8 at p. 9; Hayward, No. 6 at p. 8)
[[Page 36897]]
In response, DOE notes that, although the DOE test procedure for EF
proposed to use kgal/kWh instead of gal/Wh, these values are
numerically equivalent. However, for consistency with previous ratings,
in this final rule, DOE is adopting units of gal/Wh for the optional EF
test metric.
With regard to coordination with voluntary and other regulatory
programs in general, DOE notes that during the Working Group meetings
and the NOPR public meeting, it was made clear to stakeholders that not
only the industry, but also ENERGY STAR and CEC, would have to
transition to the DOE test procedure within 180 days of publication of
the test procedure final rule. (Docket No. EERE-2015-BT-STD-0008, No.
54 at pp. 42-43; Public Meeting Transcript, No. 3 at pp. 9-11) On or
after this date, representations must be made in accordance with the
adopted DOE test procedure. Accordingly, DOE expects that both ENERGY
STAR and CEC will transition to DOE's WEF metric and test procedure.
DOE will work with ENERGY STAR and CEC to make this transition.
However, during this period of transition, manufacturers may still be
making representations of EF for other programs and must determine
whether their historical test data is valid in accordance with the DOE
test procedure or not. After 180 days, all representations, including
representations of EF, must be made in accordance with the DOE test
procedure. In the case any historical test data is determined not to be
valid, that DPPP model must be retested in order to continue making
representations of EF.
4. Request for Extension
Hayward requested an extension of the 180 day timeframe for
representations to allow manufacturers sufficient time to obtain the
necessary resources, equipment, and personnel to respond to DOE's
request. (Hayward, No. 6 at p. 1) Pentair and APSP stated that it was
impossible to comply with the 180 day requirement for publishing
performance and labeling products according to the DOE test procedure,
particularly due to the relationship with ENERGY STAR requirements.
They also noted that introducing new terms into the market so early
would be disruptive. Therefore, they requested that the 180 day
requirement be changed to coincide with the compliance date of energy
conservation standards. (APSP, No. 8 at p. 2; Pentair, No. 11 at p. 5)
In response to Pentair and APSP's concerns about labeling and
introduction of new metrics, DOE did not propose that products be
labeled within the 180 day period (see section III.I). Furthermore, DOE
notes that manufacturers may decline to make any representations of
WEF, or any other DPPP metrics, until July 19, 2021, meaning that no
equipment is required to be rated in accordance with the DOE test
procedure within 180 days. EPCA does require, however, that any
representation that a manufacturer may choose to make on a label or
otherwise must reflect testing under the applicable DOE test procedure,
beginning 180 days after publication of this final rule. (42 U.S.C.
6314(d)) In this case, they must make representations of WEF at a
minimum, but may choose to continue making representations of EF,
reflective of the results of testing in accordance with appendix B,
until July 19, 2021.
DOE acknowledges that some DPPP models currently participate in
voluntary industry programs, such as ENERGY STAR, that rely on the EF
metric. As such, DOE is accommodating the continued use of the EF
metric until July 19, 2021 to allow a smooth transition in the
industry, as requested by Pentair and APSP. However, as mentioned
previously, both ENERGY STAR and CEC are also required to transition to
DOE's new WEF metric and test procedure within 180 days. In addition,
after July 19, 2021, only representations of WEF will be allowed, as
representation of EF would not be reflective of testing under appendix
C of the DPPP test procedure. DOE believes this should address Pentair
and APSP's concern regarding market confusion with new metrics.
DOE notes that 42 U.S.C. 6314(d)(2) allows manufacturers to
petition for an extension of up to another 180 days in the case of
undue hardship to the manufacturer. However, because a finding as to
undue hardship is particular to a given manufacturer, the petition must
be filed by the manufacturer within 60 days of the publication of this
final rule, specifying the hardship to the manufacturer that would
result from the 180-day requirement, and any extension will be
determined by the Secretary on a case-by-case basis. (42 U.S.C.
6314(d)(2))
G. Additional Test Methods
In addition to the measurements and calculations necessary to
determine WEF, DOE also must establish consistent terminology and
measurement methods to categorize the capacity and maximum head of a
given dedicated-purpose pool pump, as well as establish whether a given
dedicated-purpose pool pump is self-priming. Specifically, as discussed
in section III.D, DOE is establishing different load points and
reference curves based on the rated hydraulic horsepower of a given
pool filter pump. DOE's standardized and consistent method for
determining DPPP capacity is discussed in section III.G.1. As discussed
in section III.B.3.a, DOE also is differentiating pool filter pumps
based on whether they are self-priming. DOE's test method for
determining the self-priming capability of dedicated-purpose pool pumps
is discussed in section III.G.2. In addition, waterfall pumps are
categorized with respect to the maximum head the pump can produce.
DOE's test method for determining maximum head is discussed in section
III.G.3.
1. Determination of DPPP Capacity
As discussed in detail in the September 2016 DPPP test procedure
NOPR, industry currently uses several terms to characterize the
capacity of dedicated-purpose pool pumps, including total horsepower,
DPPP motor capacity, nameplate horsepower, rated horsepower, max-rated
horsepower, up-rated horsepower, brake horsepower, service factor
horsepower, peak power, and hydraulic horsepower. 81 FR 64580, 64620-
64623 (Sept. 20, 2016). The DPPP Working Group discussed these terms
and recommended standardizing the terminology by referring to pump
capacity around the hydraulic horsepower provided by the pump at a
specific load point. (Docket No., EERE-2015-BT-STD-0008, No. 56 at pp.
148-173) In addition, the DPPP Working Group recommended that DOE
assist in standardizing the testing and rating of dedicated-purpose
pool pumps with regard to other typical horsepower metrics. (Docket No.
EERE-2015-BT-STD-0008, No. 92 at pp. 319-322) Specifically, the June
2016 DPPP Working Group recommended that DOE should investigate a label
that would facilitate proper application and include specified
horsepower information. (Docket No. EERE-2015-BT-STD-0008, No. 82,
Recommendation #9 at p. 5) Section III.G.1.a and section III.G.1.b
contain DOE's proposals and the adopted provisions related to rated
hydraulic horsepower and other DPPP motor horsepower metrics,
respectively.
a. Rated Hydraulic Horsepower
In the September 2016 DPPP test procedure NOPR, DOE proposed to
consistently refer to and categorize dedicated-purpose pool pumps based
on the hydraulic horsepower they can produce at a particular load
point, as measured in accordance with the new DPPP test procedure. 81
FR 64580,
[[Page 36898]]
64620-64623 (Sept. 20, 2016). In order to have consistent and
comparable values of hydraulic horsepower, the DPPP test procedure must
also specify a load point at which to determine the hydraulic
horsepower. DOE proposed to categorize dedicated-purpose pool pumps
based on the hydraulic horsepower determined at maximum speed on the
reference curve for each DPPP variety and speed configuration (section
III.D) and at full impeller diameter to result in consistent and
comparable ratings among DPPP varieties and speed configurations. Id.
While hydraulic horsepower (termed pump power output \51\) is
defined in HI 40.6-2014, in the September 2016 DPPP test procedure
NOPR, DOE proposed to use the term ``rated hydraulic horsepower'' to
specifically identify the measured hydraulic horsepower on the
reference curve (i.e., curve C for self-priming and non-self-priming
pool filter pumps) or the specified load point (i.e., 17.0 ft or 10.0
gpm for waterfall pumps or pressure cleaner booster pumps,
respectively) at the maximum speed and full impeller diameter for the
rated pump. 81 FR 64580, 64622 (Sept. 20, 2016). DOE's goal in
proposing this term was to unambiguously specify the pump power
characteristic and differentiate it from the general term ``hydraulic
horsepower'' that can be determined at any location on the pump curve.
Id. In addition, DOE proposed in the September 2016 DPPP test procedure
NOPR that the representative value of rated horsepower, for each basic
model of dedicated-purpose pool pump, be determined as the mean of the
rated hydraulic horsepower for each tested unit measured in accordance
with the new DPPP test procedure. Id. The test method for determining
hydraulic horsepower (pump power output) is described in more detail in
section III.E.2.b.
---------------------------------------------------------------------------
\51\ The term ``pump power output'' in HI 40.6 is defined as
``the mechanical power transferred to the liquid as it passes
through the pump, also known as pump hydraulic power.'' It is used
synonymously with ``hydraulic horsepower'' in this document.
However, where hydraulic horsepower is used to reference the
capacity of a dedicated-purpose pool pump, it refers to the rated
hydraulic horsepower.
---------------------------------------------------------------------------
DOE did not receive any comments related to the proposed definition
of rated hydraulic horsepower, the proposal to base the
characterization of DPPP capacity on rated hydraulic horsepower, or the
proposed method for determining representative values of rated
hydraulic horsepower. Consequently, DOE is adopting the terminology and
test methods proposed in the September 2016 DPPP test procedure NOPR
without modification.
b. Other DPPP Motor Horsepower Metrics
DPPP Working Group suggested that DOE assist in standardizing the
testing and rating of dedicated-purpose pool pumps with regard to other
typical horsepower metrics (Docket No. EERE-2015-BT-STD-0008, No. 92 at
pp. 319-322). In the September 2016 DPPP test procedure NOPR, DOE
reviewed the terms typically used in the DPPP industry to characterize
motor horsepower. 81 FR 64580, 64622 (Sept. 20, 2016). To alleviate any
ambiguity associated with rated horsepower, total horsepower, and
service factor, DOE proposed, in the September 2016 DPPP test procedure
NOPR, the terms ``DPPP nominal motor horsepower,'' ``DPPP motor total
horsepower,'' and ``DPPP service factor.'' 81 64580, 64622-64623 (Sept.
20, 2016). The proposed definitions for these terms are as follows:
Dedicated-purpose pool pump nominal motor horsepower means
the nominal motor horsepower as determined in accordance with the
applicable procedures in NEMA-MG-1-2014.
Dedicated-purpose pool pump motor total horsepower (also
known as service factor horsepower) means the product of the dedicated-
purpose pool pump nominal motor horsepower and the dedicated-purpose
pool pump service factor of a motor used on a dedicated-purpose pool
pump based on the maximum continuous duty motor power output rating
allowable for the nameplate ambient rating and motor insulation class.
Dedicated-purpose pool pump service factor means a
multiplier applied to the rated horsepower of a pump motor to indicate
the percent above nameplate horsepower at which the motor can operate
continuously without exceeding its allowable insulation class
temperature limit. 81 FR 64580, 64622-64623 (Sept. 20, 2016).
The definitions proposed in the NOPR were developed based on the
existing industry definitions for these terms. However, the term
``dedicated-purpose pool pump nominal motor horsepower'' is defined
slightly differently than the terms ``rated horsepower'' or ``nameplate
horsepower,'' which are synonymous in the industry. Specifically, DOE
defines DPPP nominal motor horsepower based on the nominal horsepower
of the motor with which the dedicated-purpose pool pump is distributed
in commerce, as determined in accordance with the applicable procedures
in NEMA MG-1-2014, ``Motors and Generators.'' Id.
In response to DOE's proposed definitions, CA IOUs were generally
supportive of this approach and stated that CEC has similar terms to
those proposed in the September 2016 DPPP test procedure NOPR, but
noted that CEC uses the term ``motor capacity'' for consistency with
the motor industry, which is synonymous with the total horsepower and
service factor horsepower. (CA IOUs, Public Meeting Transcript, No. 3
at p. 66).
DOE acknowledges CA IOUs' comment and is aware that different
organizations use different terms to describe similar quantities.
Although DOE is aware that CEC uses the term motor capacity to refer to
what DOE is proposing to define as DPPP motor total horsepower, DOE
believes the proposed term is more straightforward and widely
understood. DOE also notes that Title 20 of the California Code of
Regulations defines both the term ``capacity of the motor'' and ``total
horsepower'' (of an AC motor) as the product of the rated horsepower
and the service factor of a motor used on a dedicated-purpose pool pump
(also known as service factor horsepower) based on the maximum
continuous duty motor power output rating allowable for the nameplate
ambient rating and motor insulation class. Cal. Code Regs., tit. 20
section 1602, subd. (g) However, to be consistent with both CEC
definitions for the same term, this final rule will adopt the
definition with a parenthetical to note that DPPP motor total
horsepower is also referred to as service factor horsepower or motor
capacity.
Regarding the definition of DPPP nominal motor horsepower, based on
response to comment discussed further in this section, DOE is not
referencing NEMA MG-1-2014 for the test method to determine DPPP
nominal motor horsepower and is instead directly referencing a more
simplified method with equivalent burden. As such, DOE's proposed
definition is no longer applicable. DOE believes specifying a test
method for determining this value is sufficient and is not adopting a
definition of DPPP nominal motor horsepower.
In the September 2016 DPPP test procedure NOPR, DOE also proposed
test methods to consistently and unambiguously determine the DPPP
nominal motor horsepower, DPPP service factor, and DPPP motor total
horsepower. To determine the DPPP nominal motor horsepower for single-
phase and polyphase small and medium AC motors, DOE proposed to
reference
[[Page 36899]]
the relevant sections of NEMA MG-1-2014, as summarized in Table III.10.
DOE also proposed to incorporate by reference these sections of NEMA
MG-1-2014 into the DPPP test procedure. 81 FR 64580, 64622-64623 (Sept.
20, 2016).
Table III.10--Summary of Relevant NEMA MG-1-2014 Sections Applicable to
Small and Medium Single- and Three-Phase AC Motors
------------------------------------------------------------------------
Single-phase AC Three-phase AC
Characteristic motors motors
------------------------------------------------------------------------
Breakdown Torque............ Section 10.34 of Section 12.39 of
NEMA MG-1-2014.*. NEMA MG-1-2014.*
Locked-Rotor Torque......... N/A................. Section 12.37 or
12.38 of NEMA MG-1-
2014.*
Pull-up Torque.............. N/A................. Section 12.40 of
NEMA MG-1-2014.*
Locked-Rotor Current........ N/A................. Section 12.35.1 of
NEMA MG-1-2014.*
Slip........................ N/A................. Section 1.19 of NEMA
MG-1-2014.*
------------------------------------------------------------------------
* Based on testing in accordance with section 12.30 of NEMA MG-1-2014.
Similarly, for direct current (DC) motors, including electrically
commutated motors, section 10.62 of part 10 of NEMA MG-1-2014,
``Horsepower, Speed, and Voltage Ratings,'' describes the requirements
for determining the nominal horsepower based on the applicable rated
load speed and rated voltages for these motors. To clearly specify how
DPPP nominal motor horsepower would be determined for DC motors based
on the procedures in NEMA MG-1-2014, DOE also proposed to include
instructions in the DPPP test procedure that reference the relevant
sections of NEMA MG-1-2014. Id.
DOE also proposed to base the determination of DPPP service factor
on the standardized service factor values in table 12-4 of section
12.51, ``Service Factor of Alternating-Current Motors.'' For AC motors
not covered by table 12-4 of section 12.51 of NEMA MG-1-2014 and for DC
motors, DOE proposed assigning a service factor of 1.0, consistent with
section 12.51.2 of NEMA MG-1-2014. Id.
Finally, DOE proposed that total horsepower would be calculated as
the product of the DPPP nominal motor horsepower and the DPPP service
factor, both determined in accordance with the applicable provisions in
the DPPP test procedure. Id.
In response to DOE's proposed test methods for the proposed DPPP
motor horsepower metrics, Nidec commented that section 10.34 of NEMA
MG-1-2014, which DOE proposed to incorporate by reference, applies
specifically to general purpose motors, while small electric motors
designed for use on dedicated-purpose pool pumps are definite purpose
motors that do not follow the design criteria of NEMA MG-1-2014.
Instead, Nidec suggested that DOE use equation (4) to determine nominal
motor horsepower:
[GRAPHIC] [TIFF OMITTED] TR07AU17.005
Where:
Pnm = the nominal total horsepower \52\ at full load (in
hp),
---------------------------------------------------------------------------
\52\ Nidec's comment defined this term as the ``nominal motor
horsepower at full load.'' However, the rest of the comment
describes the value as the motor total horsepower. As Nidec also
recommended a service factor of 1.0 (Nidec, No. 10 at pp. 2-3),
nominal motor horsepower is equivalent to motor total horsepower and
the equation is applicable to both quantities.
---------------------------------------------------------------------------
T = output torque at full load (in lb-ft), and
RPM = the motor speed at full load (in rpm).
Nidec believes that the calculation in equation (4) is a better
method for calculation than using the NEMA sections DOE proposed for
DPPP motors and stated that equation (4) is the equation Nidec
currently uses to rate such motors, which it manufacturers. (Nidec, No.
10 at p. 2). Nidec also inquired as to the test methods DOE proposed to
use for DPPP motors. (Nidec, No. 10 at p. 4).
Nidec also commented that the service factor for small electric
motors used in the DPPP industry should not follow NEMA section 12.51
of NEMA MG-1-2014 but instead should be established as 1.0 for all DPPP
motors. Nidec noted that this is consistent with the labeling
requirements set forth in ANSI/APSP/ICC 15a-2013. (Nidec, No. 10 at p.
3). Finally, Nidec commented that three-phase motors utilized on
dedicated-purpose pool pumps are energy efficient and already regulated
and, therefore, should not need further testing nor reporting
requirements. (Nidec, No. 10 at p. 3).
APSP agreed with Nidec that DPPP motors are typically definite-
purpose and do not always align with NEMA on mechanical and electrical
performance. Similarly, APSP recommended using equation (4) to
calculate nominal motor horsepower and assigning a service factor of
1.0, such that nominal motor horsepower was equivalent to motor total
horsepower. (APSP, No. 8 at p. 8).
During the September 2016 DPPP test procedure NOPR public meeting,
CA IOUs stated that commercial and industrial motors commonly have
service factors of 1.15, where the motor is capable of performing at a
higher level than what the nameplate shows. In contrast, in DOE's
proposal of 1.0, the motor will do at best exactly what the nameplate
states. (CA IOUs, Public Meeting Transcript, No. 3 at p. 68) Pentair
also commented that the proposal would restrict a manufacturer's
ability to use higher service factor motors for purposes of improved
motor life and/or reduction of inventory/SKUs. (Pentair, No. 11 at p.
3). However, Pentair expressed, in its comments, the importance of
standardizing and labeling regarding DPPP horsepower metrics and
described how the current practice of up-rate and full-rate labeling of
similar products causes significant confusion in the market. (Pentair,
No. 11 at p. 5). In response to Nidec and APSP's suggestions regarding
the appropriate test methods for determining motor horsepower and
service factor, DOE believes the method suggested by Nidec and APSP is
sound and, as described by the commenters, represents the methods
currently used by the motor industry to determine motor total
horsepower for DPPP motors. DOE is also aware that equation (4) is a
common method for measuring motor horsepower when speed and torque are
known. Specifically, equation
[[Page 36900]]
(4) is described in NEMA MG-1-2014 (the standard DOE proposed to
incorporate by reference for this determination), the IEEE Standard
114-2010, ``Test Procedure for Single-Phase Induction Motors''; IEEE
Standard 113-1985, ``IEEE Guide: Test Procedures for Direct-Current
Machines''; and Canadian Standards Association (CSA) C747-2009
(Reaffirmed (RA) 2014), ``Energy Efficiency Test Methods for Small
Motors.'' \53\
---------------------------------------------------------------------------
\53\ DOE notes that the equation in section 6.4 of CSA C&47-2009
(RA 2014) uses a conversion factor of 5254, instead of the value
5252 suggested by NEMA. However, based on DOE's review, DOE believes
a conversion factor of 5252 is more accurate and is more consistent
with the value listed in other standards.
---------------------------------------------------------------------------
DOE notes that this method provides a direct measurement of the
horsepower provided by the motor at full load, which is consistent with
the term DPPP motor total horsepower, as opposed to DPPP nominal motor
horsepower as suggested by Nidec and APSP. However, DOE acknowledges
that, as Nidec and APSP both suggested using a service factor of 1.0
with this method, the DPPP nominal motor horsepower and DPPP motor
total horsepower would be equivalent and either could be determined
with the suggested method shown in equation (4). Therefore, determining
nominal motor horsepower using equation (4) is technically correct,
provided it is used with a service factor of 1.0. Both Nidec and APSP
specifically suggested determining DPPP nominal motor horsepower using
equation (4), setting DPPP service factor to 1.0, and determining DPPP
motor total horsepower as the product of the DPPP nominal motor
horsepower and DPPP service factor. (Nidec, No. 10 at p. 4; APSP, No. 8
at p. 8). As noted in the NOPR, determining DPPP motor total horsepower
as the product of DPPP nominal motor horsepower and DPPP service factor
is also consistent with ANSI/APSP/ICC 15a-2013,\54\ ENERGY STAR,\55\
and CA Title 20 \56\ definitions for the term. 81 FR 64580, 64620-64622
(Sept. 20, 2016). As such, DOE is adopting the method suggested by
Nidec and APSP as the test method for determining DPPP nominal total
horsepower for dedicated-purpose pool pumps subject to the adopted
procedure.\57\ As discussed further in this section regarding
incorporations by reference, the burden and fundamental procedure
associated with the adopted procedure for measuring motor performance
are not different from those proposed in the NOPR, but the adopted
method provides a simpler, more direct description.
---------------------------------------------------------------------------
\54\ ANSI/APSP/ICC-15a-2013, American National Standard for
Residential Swimming Pool and Spa Energy Efficiency--section 3,
``Definitions.'' Includes Addenda A. ANSI Approved January 9, 2013.
The Association of Pool and Spa Professionals and the International
Code Council.
\55\ ENERGY STAR Program Requirements for Pool Pumps Eligibility
Criteria (Version 1.1), section 1.4, ``Product Ratings.''
\56\ Cal. Code Regs., tit. 20 section 1602, subd. (g).
\57\ As discussed subsequently in this section, DOE is adopting
test methods for determining the motor horsepower characteristics of
dedicated-purpose pool pumps that are only applicable to dedicated-
purpose pool pumps distributed in commerce with single-phase AC or
DC motors.
---------------------------------------------------------------------------
Regarding service factor, DOE appreciates Nidec and APSP's
suggestions regarding service factor and agrees that a service factor
of 1.0 for all DPPP motors that are subject to the adopted motor
horsepower provisions would be more consistent and ensure standardized
rating across DPPP models. It also enables to use of the more direct
determination of DPPP nominal horsepower adopted in this final rule.
Although Pentair requested more flexibility specifically with regard to
service factor, Pentair also requested standardization in horsepower
ratings. As such, in this final rule, in order to better standardize
the motor horsepower ratings as recommended by commenters, DOE is
adopting a service factor of 1.0 for all dedicated-purpose pool pumps
to which the adopted motor horsepower test methods apply.
Regarding Nidec's statement that a service factor of 1.0 was
consistent with ANSI/APSP/ICC 15a-2013, DOE reviewed ANSI/APSP/ICC 15a-
2013 and finds that ANSI/APSP/ICC 15a-2013 does not appear to provide
any restriction with regard to the service factor of DPPP motors. In
fact, ANSI/APSP/ICC 15a-2013 defines several terms, including rated
horsepower, total horsepower, and service factor, that indicate service
factors greater than 1.0 are quiet common. For example, the definition
of service factor references a pump with a rated horsepower of 1.5 hp,
a service factor of 1.65, and a total horsepower of 2.475 hp.\58\
---------------------------------------------------------------------------
\58\ ANSI/APSP/ICC-15a-2013, section 3, ``Definitions.''
---------------------------------------------------------------------------
In response to CA IOUs comments on the proposed DPPP service factor
for DPPP motors, DOE notes that, consistent with CA IOUs observation,
the service factor prescribed in table 12-4 of section 12.51, ``Service
Factor of Alternating-Current Motors,'' is 1.15 for most AC motors with
a nominal horsepower greater than 0.5 horsepower and typical
synchronous speeds. However, consistent with section 12.51.2 of NEMA
MG-1-2014 and the comments of Nidec and APSP, DOE believes that a
service factor of 1.0 for AC motors not covered by table 12-4 is more
appropriate than a service factor of 1.15. In addition, as discussed in
the September 2016 DPPP test procedure NOPR, NEMA MG-1-2014 does not
provide information regarding service factor for DC motors, as nominal
synchronous speeds are typically not applicable to DC motors.
Therefore, DOE believes a DPPP service factor of 1.0 is appropriate for
DC motors, effectively making the nominal horsepower equivalent to the
total horsepower of the dedicated-purpose pool pump, which is
consistent with the convention for rating such motors in the motor
industry.
However, DOE notes that Nidec recommended applying the suggested
methodology for single-phase DPPP motors only. Nidec indicated that
three-phase motors sold with dedicated-purpose pool pumps are already
subject to DOE's energy conservation standards for polyphase electric
motors at 10 CFR 431.25 or 10 CFR 431.446, depending on the size of the
motor. (Nidec, No. 10 at p. 3). DOE agrees with Nidec that any
polyphase induction motors currently subject to DOE's existing
regulations for electric motors or small electric motors are already
subject to test procedures that describe how to determine relevant
motor performance parameters, including nominal motor horsepower and
service factor, in a standardized and consistent manner. Therefore,
additional specifications in the DPPP test procedure are not
required.\59\ For these reasons, in this final rule, DOE is limiting
the applicability of the test methods for determining DPPP nominal
motor horsepower and DPPP service factor to dedicated-purpose pool
pumps that are distributed in commerce with single-phase AC or DC
motors, which are not subject to DOE's existing regulations for
electric motors or small electric motors.
---------------------------------------------------------------------------
\59\ DOE notes that the existing electric motor and small
electric motor regulations reference relevant sections of NEMA MG-1-
2014 and are consistent with the test methods proposed in the
September 2016 DPPP TP NOPR. As such, consistent with CA IOUs
observation, dedicated-purpose pool pumps distributed in commerce
with polyphase motors will continue to apply table 12-4 in NEMA MG-
1-2014.
---------------------------------------------------------------------------
DOE notes that the test method for determining DPPP motor total
horsepower is still applicable to all dedicated-purpose pool pumps,
including those distributed in commerce with polyphase AC motors, as
NEMA MG-1-2014 does directly define or prescribe unambiguous methods
for determining motor total horsepower. In addition, as discussed
[[Page 36901]]
further in section III.K.2 and III.I, all dedicated-purpose pool pumps,
including dedicated-purpose pool pumps distributed in commerce with
polyphase AC motors, are required to report to DOE the DPPP motor total
horsepower and include such information on the equipment nameplate.
In adopting Nidec and APSP's recommended test method for
determining DPPP nominal motor horsepower, DOE is not referencing NEMA
MG-1-2014 as the method for determining DPPP motor total horsepower.
However DOE still must adopt specific and standardized test methods for
measuring speed and torque of DPPP motors at full load. IEEE Standard
114-2010, ``Test Procedure for Single-Phase Induction Motors'' (IEEE
114-2010) and IEEE Standard 113-1985, ``Test Procedures for Direct-
Current Machines'' (IEEE 113-1985) describe the general test
requirements and methods for determining motor speed and torque at full
load for single-phase AC induction motors and DC motors, respectively.
DOE notes that these are the test methods referenced in NEMA MG-1-2014,
so the burden and fundamental procedure associated with measuring motor
performance are not different from those proposed in the NOPR. However,
as the method of determining DPPP nominal motor horsepower suggested by
Nidec and APSP and incorporated by DOE is more direct, DOE is
incorporating by reference the relevant sections of IEEE 114-2010 and
IEEE 113-1985 directly, as opposed to through NEMA MG-1-2014.
In addition, DOE notes that CSA C747-2009 (RA 2014) is another
commonly referenced test method for determining motor horsepower that
is treated as equivalent to IEEE 114-2010 in DOE's existing small
electric motor test procedure. 10 CFR 431.444(b). In DOE's July 2009
small motors test procedure final rule, DOE determined that IEEE 114-
2010 and CSA C747-2009 (RA 2014) would produce equivalent ratings. 74
FR 32059, 32065 (July 7, 2009). DOE has reviewed CSA C7474-2009 (RA
2014) as compared to IEEE 113-1985 and believes that the standards will
also produce equivalent measurements of full load speed and torque,
which are the values relevant for this test procedure. DOE understands
that some manufacturers may currently be using CSA C747-2009 (RA 2014)
to determine the performance of small motors, including both single-
phase AC and DC motors. Therefore, to provide flexibility to
manufacturers and consistency with DOE's existing motor regulations,
DOE is adopting test provisions that allow for testing in accordance
with either the applicable IEEE standard (IEEE 114-2010 for single-
phase AC motors or IEEE 113-1985 for DC motors) or CSA C747-2009 (RA
2014). DOE believes that these standards provide the necessary and
sufficient methods to determine the torque and rotating speed of the
motor at full load for single-phase AC induction motors and DC motors,
respectively. Specifically, DOE is adopting the sections specified in
the Table III.11 for each standard, which are relevant to measuring
speed and torque at full load. In addition, section E.3.2 of both
appendix B and C, as adopted in this final rule, states that full-load
speed and torque shall be determined based on the maximum continuous
duty motor power output rating allowable for the motor's nameplate
ambient rating and insulation class.
Table III.11--Sections of IEEE 114-2010 and IEEE 113-1985 That DOE Incorporates by Reference for Determining
DPPP Motor Total Horsepower
----------------------------------------------------------------------------------------------------------------
Characteristic IEEE 114-2010 IEEE 113-1985 CSA C747-2009 (RA 2014)
----------------------------------------------------------------------------------------------------------------
Relevant Scope.................... Single-phase AC DC Motors................. Single-phase AC and DC
Motors. Motors
Test Conditions................... Section 4............ Section 3.5, 4.1.2, and Section 5.2, 5.3, 5.5.
4.1.4 (and machine 6.1.
temperature rise shall be
some value between 50%
and 100% of rated
temperature rise, as
specified in 5.4.3).
Test Requirements................. Section 3.2 and Section 5.4.3.2 (except Section 6.3, 6.4 (except
section 6. that curves of torque in section (b) the
versus electric power are conversion factor shall
not required, as only be 5252), 6.5 (except
measurement at full load only measurements at
is required). full load are required),
and 6.7.1.
Measurement Instruments........... Section 5.2 and 5.3.. Section 3.1, 3.4.......... Section 5.1, 5.4.6,
5.4.7, 5.6.4, 5.6.5,
5.6.6, 6.2.
----------------------------------------------------------------------------------------------------------------
In responses to Nidec's inquiry regarding the test methods for
determining DPPP motor horsepower characteristics, the test methods
referenced in NEMA MG-1-2014 were, by extension, proposed to be
incorporated by reference as the specific testing requirements for
determining motor performance in the September 2016 DPPP test procedure
NOPR.
Regarding the scope of the proposed motor horsepower testing
requirements, Pentair commented that a loophole could be introduced in
replacement DPPP motors are not also subject to these requirements.
(Pentair, No. 11 at p. 3).
In response to Pentair's request, DOE notes that the scope of the
required DOE test procedure recommended by the DPPP Working Group and
proposed by DOE in the September 2016 DPPP test procedure NOPR is
limited to dedicated-purpose pool pumps. DOE acknowledges that, in the
September 2016 DPPP test procedure NOPR, DOE proposed an optional test
method to determine WEF for replacement DPPP motors. 81 FR 64580, 64629
(Sept. 20, 2016). However, in the September 2016 DPPP test procedure
NOPR, DOE also described how DOE does not intend to regulate
replacement DPPP motors as part of this rulemaking because they do not
(by themselves) meet the definition of a dedicated-purpose pool pump.
Id. Similar to the optional testing provisions for replacement DPPP
motors adopted in this final rule, manufacturers of replacement DPPP
motors may opt to apply the provisions for determining DPPP nominal
motor horsepower, DPPP service factor, and DPPP motor total horsepower,
as applicable, and make representations of these quantities if they so
choose. However, as discussed further in section III.J, replacement
DPPP motors are not dedicated-purpose pool pumps, and requirements for
such equipment were not discussed or recommended by the DPPP Working
Group. Therefore, DOE is declining to adopt any required testing
provisions or
[[Page 36902]]
reporting requirements for replacement DPPP motors in this rulemaking.
DOE may address requirements for replacement DPPP motors in a future
rulemaking specifically addressing such equipment.
In summary, based on the comments received in response to the
September 2016 DPPP test procedure NOPR, DOE is adopting revised test
methods for DPPP nominal motor horsepower and DPPP service factor,
which are applicable only to dedicated-purpose pool pumps distributed
in commerce with single-phase AC motors and DC motors. DOE is also
adopting the test method for DPPP motor total horsepower proposed in
the September 2016 DPPP test procedure NOPR without modification, which
is applicable to all dedicated-purpose pool pumps. DOE believes such
standardized rating methods are consistent with the recommendations of
the DPPP Working Group, will be beneficial to consumers in selecting
and applying the equipment, and are consistent with existing methods
used to rate motors today. DOE notes that these standardized horsepower
metrics are intended to support labeling provisions for dedicated-
purpose pool pumps, which are discussed further in section III.I.
2. Determination of Self-Priming Capability
As discussed in section III.B.3.a, DOE proposed separate
definitions for self-priming and non-self-priming pool filter pumps
based on their capability to self-prime as determined based on testing
in accordance with NSF/ANSI 50-2015. In the September 2016 DPPP test
procedure NOPR, DOE proposed to incorporate by reference relevant
sections of the NSF/ANSI 50-2015 standard and also specify several
modifications and additions to improve repeatability and consistency of
the test results. 81 FR 64580, 64623-27 (Sept. 20, 2016). Specifically,
DOE proposed to incorporate by reference section C.3 of Annex C of NSF/
ANSI 50-2015, which contains the relevant test parameters, test
apparatus, and testing instructions for determining the self-priming
capability of self-priming and non-self-priming pool filter pumps. Id.
To determine the self-priming capability of self-priming and non-
self-priming pool filter pumps, DOE proposed in the September 2016 DPPP
test procedure NOPR to follow the test method specified in section C.3
of Annex C of NSF/ANSI 50-2015 with several minor modifications to
improve test consistency and repeatability, as well as conform with the
new definitions for self-priming and non-self-priming pool filter pumps
presented in section III.B.3.a. Id. First, where section C.3.2,
``Apparatus,'' and section C.3.4, ``Self-priming capability test
method,'' state that the ``suction line must be essentially as shown in
annex C, figure C.1'' DOE notes that the suction line refers to the
riser pipe that extends from the pump suction inlet to the water
surface. DOE also proposed in the September 2016 DPPP test procedure
NOPR to clarify that ``essentially as shown in Annex C, figure C.1''
means:
The centerline of the pump impeller shaft is situated a
vertical distance of 5.0 feet above the water level of a water tank of
sufficient volume as to maintain a constant water surface level for the
duration of the test;
the pump draws water from the water tank with a riser pipe
that extends below the water level a distance of at least 3 times the
riser pipe diameter (i.e., 3 pipe diameters); and
the suction inlet of the pump is at least 5 pipe diameters
from any obstructions, 90[deg] bends, valves, or fittings.
Id.
Further, DOE noted that NSF/ANSI 50-2015 does not specify where the
measurement instruments are to be placed in the test set up. DOE
understands that instruments are typically installed at the suction
inlet of the pump and therefore, DOE proposed to specify that all
measurements of head, flow, and water temperature must be taken at the
pump suction inlet. Id. It is also important that all measurements are
taken with respect to a common reference plane, which DOE proposed
should be the centerline of the pump impeller shaft. DOE also proposed
that such adjustments be performed in accordance with section A.3.1.3.1
of HI 40.6-2014. Id.
In addition, DOE proposed that height, or vertical lift (VL), must
be determined from the height of the water to the centerline of the
pump impeller shaft. Id. In addition to proposing clarifications with
regard to the measurement of VL, DOE proposed clarifications on how to
correct the value to a standard temperature of 68 [deg]F, a pressure of
14.7 psia, and a water density of 62.4 lb/ft\3\, as shown in equation
(5). DOE notes that the definitions proposed in the September 2016 DPPP
test procedure NOPR specifies a VL of 5.0 feet:
[GRAPHIC] [TIFF OMITTED] TR07AU17.006
Where:
VL = vertical lift of the test apparatus from the waterline to the
centerline of the pump impeller shaft, in ft;
[rho]test = density of test fluid, in lb/ft\3\; and
Patm,test = absolute barometric pressure of test apparatus location
at centerline of pump impeller shaft, in psia.
81 FR 64580, 64624-25 (Sept. 20, 2016).
In addition, DOE also noted in the September 2016 DPPP test
procedure NOPR that section C.3.2 of NSF/ANSI 50-2015 describes the
instruments that are required to perform the test, but, with the
exception of the time indicator, does not specify their required
accuracy. Subsequently, DOE proposed to apply the accuracy requirements
contained in HI 40.6-2014 to the measurement devices noted in NSF/ANSI
50-2015, as detailed in Table III.12. 81 FR 64580, 64625 (Sept. 20,
2016).
Table III.12--Measurement Device Accuracy Requirements for Measurements
Devices Specified in NSF/ANSI 50-2015
------------------------------------------------------------------------
Accuracy
Measurement device requirement Source
------------------------------------------------------------------------
Elapsed Time Indicator.......... 0.1 NSF/ANSI 50-2015.
min.
Gauge Pressure Indicating Device 2.5% HI 40.6-2014.
of reading *.
Temperature Indicating Device... 0.5 HI 40.6-2014.
[deg]F.
[[Page 36903]]
Barometric Pressure Indicating 2.5% HI 40.6-2014.
Device. of reading *.
Height.......................... 0.1 N/A.
inch.
------------------------------------------------------------------------
* The 2.5 percent requirement applies to discharge, suction,
and differential head measurements, as indicated in table 40.6.3.2.3,
for values taken between 40 and 120 percent of BEP flow.
DOE also noted in the September 2016 DPPP test procedure NOPR that
NSF/ANSI 50-2015 does not specify an instrument for measuring distance
and proposed that instruments for measuring distance are accurate to
0.1 inch, consistent with other requirements for distance-
measuring instruments (section III.E.2.f). 81 FR 64580, 64625 (Sept.
20, 2016).
In section C.3.3, ``Test conditions,'' NSF/ANSI 50-2015 specifies
test conditions for both swimming pools and hot tubs/spas. NSF/ANSI 50-
2015 specifies test conditions in terms of water temperature and
turbidity requirements. DOE notes that the remainder of the DPPP test
procedure is to be conducted with ``clear water,'' as required by HI
40.6-2014. While NSF/ANSI 50-2015 and HI 40.6-2014 contain different
requirements, DOE believes they are intended to do the same thing and
result in similar water characteristics. Therefore, to simplify testing
requirements and be consistent with the other portions of the DPPP test
procedure, in the September 2016 DPPP test procedure NOPR, DOE proposed
to require testing of the self-priming capability of pool filter pumps
with clear water that is between 50 and 86 [deg]F, as opposed to the
existing water temperature and turbidity requirements contained in
section C.3.3 of the NSF/ANSI 50-2015 test method. 81 FR 64580, 64625-
64626 (Sept. 20, 2016).
Section C.3.4, ``Self-priming capability test method,'' of NSF/ANSI
50-2015 specifies that ``the elapsed time to steady discharge gauge
reading or full discharge flow'' is to be recorded as the measured
priming time (MPT). However, NSF/ANSI 50-2015 does not specify how to
determine ``steady discharge gauge reading or full discharge flow.'' In
the September 2016 DPPP test procedure NOPR, DOE proposed to determine
steady discharge gauge and full discharge flow as when the changes in
head and flow, respectively, are within the tolerance values specified
in table 40.6.3.2.2, ``Permissible amplitude of fluctuation as a
percentage of mean value of quantity being measured at any test
point,'' of HI 40.6-2014. 81 FR 64580, 64626 (Sept. 20, 2016). Based on
this criteria for stabilization, DOE also proposed that the elapsed
time should be recorded when both steady state pressure and flow
readings have been achieved. Id.
Section C.3.4 of NSF/ANSI 50-2015 then specifies that the true
priming time (TPT) is calculated by scaling the MPT based on the
relative diameter of the riser pipe and the pump suction inlet
according to the following equation (6):
[GRAPHIC] [TIFF OMITTED] TR07AU17.007
As discussed in the September 2016 DPPP test procedure NOPR, DOE
noted that, although theoretically correct, testing with different
riser pipe diameters could affect the accuracy and repeatability of the
results, especially if pipes that are substantially larger or smaller
than the pump suction inlet are used. 81 FR 64580, 64626 (Sept. 20,
2016). As a result, DOE proposed that testing of self-priming
capability of pool filter pumps that are not already certified with
NSF/ANSI 50-2015 be performed with riser pipe that is of the same pipe
diameter as the pump suction inlet. As a result, no adjustment of MPT
would be required and TPT would be measured directly. Id.
Section C.3.4 of NSF/ANSI 50-2015 also specifies that the complete
test method must be repeated, such that two TPT values are generated.
In addition, section C.3.5 of NSF/ANSI 50-2015 requires that both
measurements must be less than 6 minutes or the manufacturer's
specified TPT, whichever is greater. However, as the criteria for TPT
established in DOE's definitions (see section III.B.3.a) instead
reference a TPT of 10.0 minutes, DOE proposed to specify that both test
runs result in TPT values that are less than or equal to 10.0 minutes.
81 FR 64580, 64626 (Sept. 20, 2016).
Similarly, section C.3.5 of NSF/ANSI 50-2015 describes the TPT
criteria that pumps must meet in order to certify as self-priming under
NSF/ANSI 50-2015 and the caption of figure C.1 specifies the VL
criteria applicable to the NSF/ANSI 50-2015 test. As noted previously,
DOE's definitions proposed in the September 2016 DPPP test procedure
NOPR reference a specific TPT of 10.0 minutes and VL of 5.0 feet.
Therefore, DOE proposed to exclude section C.3.5 and the relevant
portions of the VL definition in the caption of C.1 to be consistent
with DOE's definition. 81 FR 64580, 64626 (Sept. 20, 2016).
In the September 2016 DPPP test procedure NOPR public meeting, DOE
presented the general procedure for the self-priming test. (Public
Meeting Presentation, No. 2 at p. 44) During the September 2016 public
meeting, Hayward sought clarification regarding the second step in the
overview of the self-priming test procedure DOE provided in the
preamble to the September 2016 DPPP test procedure NOPR. Specifically,
Hayward sought confirmation that the terminology ``shut off and allow
pump to drain'' did not mean open the pump to atmosphere. (Hayward,
Public Meeting Transcript, No. 3 at pp. 73-74)
In response to Hayward's inquiry, DOE notes that the statement in
the September 2016 DPPP test procedure NOPR meant only to shut off the
pump and allow all lines to be drained of water, without opening the
pump to the atmosphere, as would typically be the case during the NSF/
ANSI 50-2015 test. Specifically, in the DPPP test procedure, DOE is
incorporating by reference section C.3 of Annex C of NSF/ANSI 50-2015
with the minor modifications discussed above as the test method for
determining the self-priming capability of pool filter pumps and all
testing must be conducted in accordance with the instructions in those
sections.
[[Page 36904]]
CEC, in written comments, supported DOE's proposal to use NSF/ANSI
50-2015 to differentiate between self-priming and non-self-priming pool
filter pumps. (CEC, No.7 at p. 2) DOE did not receive any other
comments suggesting changes to DOE's proposed test method to determine
the self-priming capability of pool filter pumps.
Therefore, in this final rule, DOE is adopting the self-priming
test method proposed in the September 2016 DPPP test procedure NOPR
without modification. This method relies on section C.3 of NSF/ANSI 50-
2015 with several minor clarifications and modifications. However, DOE
notes that, as discussed in section III.E.1, in this final rule, DOE is
adopting alternative requirements for the test fluid instead of testing
with ``clear water'' as specified in HI 40.6-2014. As such, to be
consistent with the remainder of the DPPP test procedure, in this final
rule DOE is adopting provisions that testing for self-priming
capability be performed with the same test fluid used for all other
testing, instead of testing with ``clear water'' as proposed in the
September 2016 DPPP test procedure NOPR. DOE notes that the
characteristics of the test fluid adopted in this final rule are now
more consistent with those in NSF/ANSI 50-2015 as well.
Table III.13 provides a summary of DOE's modifications and
additions to NSF/ANSI 50-2015 to remove ambiguity from the NSF/ANSI 50-
2015 test method, improve the repeatability of the test, and harmonize
the test requirements with the other DPPP test procedure requirements
contained in this final rule.
Table III.13--Summary of Modifications and Additions to NSF/ANSI 50-2015
Self-Priming Capability Test
------------------------------------------------------------------------
NSF/ANSI 50-2015 DOE modification/
NSF/ANSI 50-2015 section specification addition
------------------------------------------------------------------------
Section C.3.2, ``Apparatus,'' ``Essentially as More clearly
and Section C.3.4, ``Self- shown in Annex C, specify the test
priming capability test figure C.1''. setup
method''. requirements,
where VL = 5.0
feet, adjusted to
nominal
conditions of
14.7 psia and a
water density of
62.4 lb/ft\3\.
Section C.3.2, ``Apparatus''.... Measurement Accuracy
Instruments (no requirements
accuracy contained in HI
requirements). 40.6-2014, table
40.6.3.2.3, as
applicable.
Section C.3.3, ``Test Water temperature Test with clear
conditions''. and turbidity water between 50
requirements; all and 107 [deg]F
measurements at with <=15 NTU.
hot tub/spa
temperatures
unless for
swimming pool
applications only.
Section C.3.4, ``Self-priming Measure MPT at Measure elapsed
capability test method''. steady discharge time at steady
gauge or full state pressure
discharge flow. and temperature
conditions; MPT
is when those
conditions were
first achieved.
Section C.3.4, ``Self-priming Adjust MPT to TPT Use pipe of the
capability test method''. based on relative same diameter as
diameter of the suction inlet
suction inlet and (MPT = TPT).
pipe diameter.
Section C.3.5, ``Acceptance TPT of 6 minutes Excluded; TPT = 10
criteria,'' and caption of or the minutes and VL =
figure C.1. manufacturer's 5.0 feet adjusted
specified to nominal
recommended time, conditions of
whichever is 14.7 psia and a
greater and VL of water density of
5.0 feet or the 62.4 lb/ft\3\.
manufacturer's
specified lift,
whichever is
greater.
------------------------------------------------------------------------
3. Determination of Maximum Head
As noted in section III.B.4.a, waterfall pumps are, by definition,
pool filter pumps with maximum head less than or equal to 30 feet, and
a maximum speed less than or equal to 1,800 rpm. Therefore, in order to
unambiguously distinguish waterfall pumps from other varieties of pool
filter pumps, DOE must establish a specific and repeatable method for
determining maximum head of pool filter pumps. Based on the
demonstrated relationship between flow and head, DOE understands the
maximum head to be associated with the minimum flow of the pump.
However, DOE also understands that pumps cannot always be operated
safely or reliable at zero or very low flow conditions. Therefore, in
the September 2016 DPPP test procedure NOPR, DOE proposed that for the
purposes of differentiating waterfall pumps from other varieties of
pool filter pumps, the maximum head of pool filter pumps be determined
based on the measured head value associated with the maximum speed and
the minimum flow rate at which the pump is designed to operate
continuously or safely. 81 FR 64580, 64627 (Sept. 20, 2016). DOE notes
that the minimum flow rate will be assumed to be zero unless otherwise
specified in the manufacturer literature. Id.
DOE did not receive any comments in response to the proposed test
method for determining maximum head. Therefore, in this final rule, DOE
is adopting the proposal to determine the maximum head of dedicated-
purpose pool pumps as the head associated with the maximum speed and
the minimum flow rate at which the pump is designed to operate
continuously or safely, which is assumed to be zero unless otherwise
specified in the manufacturer literature.
H. Energy Factor Test Method
As discussed previously, in section III.F, in the September 2016
DPPP test procedure NOPR, DOE's proposed test procedure contained an
optional test method for determining EF at any desired speed on any of
the specified optional system curves (i.e., Curve A, B, C, or D), along
with the tested speed and the system curve associated with each energy
factor value. 81 FR 64580, 64627-64628 (Sept. 20, 2016).
Regarding the test method for EF, Pentair and APSP both commented
that table III.21 in the September 2016 DPPP test procedure NOPR (81 FR
64580, 64628; Sept. 20, 2016) used inconsistent terminology to specify
the flow terms for system curves A, B, C, and D and recommended that
the terms be reported consistently as shown in table 4 of the September
2016 DPPP test procedure NOPR (Id. at 64653). (Pentair, No. 11 at p. 6;
APSP, No. 8 at p. 2) DOE has made the correction in this final rule and
incorporated the correct table into appendix B.
I. Labeling Requirements
In the June 2016 DPPP Working Group recommendations, the DPPP
Working Group recommended that DOE consider whether to require a label
that would facilitate proper application and include specified
horsepower information. (Docket No. EERE-2015-BT-STD-0008, No. 82,
Recommendation #9 at p. 5) To implement the recommendations of the
[[Page 36905]]
DPPP Working Group, DOE proposed in the September 2016 DPPP test
procedure NOPR to require labeling of all dedicated-purpose pool pumps
for which the DPPP Working Group recommended test procedures. 81 FR
64580, 64628-29 (Sept. 20, 2016). That is, DOE proposed that the
labeling requirements be applicable to:
Self-priming pool filter pumps less than 2.5 rated
hydraulic horsepower,\60\
---------------------------------------------------------------------------
\60\ DOE notes that the DPPP Working Group only recommended
standards for single-phase self-priming pool filter pumps less than
2.5 rated hydraulic horsepower. However, the DPPP Working Group
recommended that the test procedure and reporting requirements would
still be applicable to single- and three-phase self-priming pool
filter pumps. Therefore, DOE believes it is appropriate to apply the
proposed labeling requirements to three-phase pumps.
---------------------------------------------------------------------------
non-self-priming pool filter pumps less than 2.5 rated
hydraulic horsepower,
pressure cleaner booster pumps, and
waterfall pumps.
Id.
For self-priming pool filter pumps, non-self-priming pool filter
pumps, pressure cleaner booster pumps, and waterfall pumps, DOE
proposed that each DPPP unit clearly display on the permanent nameplate
the following information:
WEF, in kgal/kWh,
rated hydraulic horsepower,
DPPP nominal motor horsepower,
DPPP motor total horsepower, and
service factor.
Id.
DOE also proposed specific requirements regarding the formatting of
required information on the nameplate and the specific terminology that
is required to be displayed. DOE proposed that these labeling
requirements would be applicable to all units manufactured, including
imported, on the compliance date of any potential energy conservation
standards that may be set for dedicated-purpose pool pumps. Id.
ASAP and NRDC submitted a joint written comment supporting the
labeling requirements proposed in the September 2016 DPPP test
procedure NOPR. (ASAP and NRDC, No. 12 at p. 2)
Regarding the proposed formatting of the label, Hayward requested
clarification regarding the specific details of the label (e.g., font
size, etc.). (Hayward, Public Meeting Transcript. No. 3 at pp. 93-94;
Hayward, No. 6 at p. 9) APSP also recommended that all labeling
details, including font size and label material, comply with UL1081-
2016. (APSP, No. 8 at p. 10) Pentair requested that the pool industry
be integrally involved in the labeling efforts, pointing out that
details associated with label formatting and sizing can be critical due
to other required safety and compliance labeling requirements combined
with limited available space. (Pentair, No. 11, at p. 4) Hayward
similarly encouraged DOE to allow use of standard industry nomenclature
(i.e., ``HP'' for horsepower and ``THP'' for total horsepower) due to
limited space available on the product for labels. (Hayward, No. 6 at
p. 9) Hayward also sought confirmation that the information required
may be provided on separate labels/data plates and is not required to
be co-located on one label or data plate. (Hayward, No. 6 at p. 9)
Hayward also objected to listing three separate horsepower values
saying it will cause confusion and not support the goal of having the
correctly sized, most energy efficient pump used in all applications.
As an alternative, Hayward support listing only the total horsepower on
any DPPP label. (Hayward, No. 6 at p. 9) Similarly, APSP requested
that, based on its recommendations regarding horsepower (see section
III.G.1.b), only total horsepower and not nominal motor horsepower or
service factor be listed on the label, consistent with requirements in
ANSI/APSP/ICC 15a-2013. (APSP, No. 8 at pp. 9-10) Nidec commented
similarly. (Nidec, No. 10 at p. 5)
APSP and Pentair commented that while use of hydraulic horsepower
for the purposes of sizing is acceptable, use of this value on a label
would cause significant confusion in the marketplace and recommended it
not be included on the pump label.\61\ (APSP, No. 8 at pp. 7-8;
Pentair, No. 11 at p. 3) Zodiac similarly commented that so much
information on the label my cause confusion during field installation
and may compromise proper installation of the pump. (Zodiac, No. 13 at
p. 3) However, Zodiac did not provide a suggested alternative.
---------------------------------------------------------------------------
\61\ Note that separately APSP presented a recommendation for
required nameplate information that did include rated hydraulic
horsepower. (APSP, No. 8 at pp. 9-10)
---------------------------------------------------------------------------
Hayward, APSP, and Zodiac expressed opposition to a requirement
that labeling include a specific WEF result, stating that such
designation may disadvantage some manufacturers and cause confusion in
the marketplace when dissimilar pumps are incorrectly compared.
(Hayward, No. 6 at p. 9; APSP, No. 8 at pp. 9-10; Zodiac, No. 13 at p.
3) Zodiac also stated that the WEF result may confuse or contradict
ENERGY STAR ratings. (Zodiac, No. 13 at p. 3) Hayward and APSP also
commented that the required label should only state ``meets DOE WEF
requirement.'' (Hayward, No. 6 at p. 9; APSP, No. 8 at p. 9)
APSP and Hayward recommended that all labeling requirements be
removed for three-phase products, as they are out of scope of the final
ASRAC working group term sheet. (APSP, No. 8 at p. 10; Hayward, No. 6
at p. 9)
As discussed previously, DOE's proposal in the September 2016 DPPP
test procedure NOPR contained details regarding the font size, spacing,
and formatting of the required label, as well as when such label would
be required to be applied. As proposed in the September 2016 DPPP test
procedure NOPR, all orientation, spacing, type sizes, typefaces, and
line widths to display this required information must be the same as or
similar to the display of the other performance data on the pump's
permanent nameplate. For this reason, DOE believes that it is not
necessary to specify that the labeling requirements comply with UL1081-
2016, as requested by APSP, or to have additional industry involvement
beyond the comment period on the NOPR, as requested by Pentair, given
that the manufacturers already have the option to individually
determine the details of the label formatting. In response to Hayward's
suggestion regarding use of common industry abbreviations, DOE notes
that the use of ``hp'' for horsepower was already allowed in DOE's
proposed labeling requirements. However, in light of Hayward's
comments, DOE has modified its proposal to also allow for the
abbreviation of total horsepower as THP.
Given the modified requirements for service factor and motor total
horsepower discussed in section III.G.1.b, DOE agrees with Hayward,
APSP, and Nidec, that DPPP nominal motor horsepower and DPPP service
factor do not need to be on the label. In addition, DOE agrees with
APSP and Pentair that, while hydraulic horsepower is necessary in
certification reporting and for compliance with standards, this
information is not used by consumers and does not need to be on the
label.
With regard to Hayward, APSP, Zodiac's opposition to including the
WEF value on the label, DOE believes that it is especially important to
clearly and consistently communicate the performance of dedicated-
purpose pool pumps using the DOE metric in order to provide customers
with standardized, comparable information to inform purchasing
decisions and is retaining the requirement to include the WEF
[[Page 36906]]
value on the DPPP label. With regard to Zodiac's comment regarding the
consistency of WEF and ENERGY STAR EF information, DOE responds that,
as discussed in section III.H, as of 180 days after the publication of
this final rule all representations of WEF, EF, and other
representations of dedicated-pool pump performance must be made in
accordance with the adopted DOE test procedure and, therefore, any EF
values will be consistent with the tested WEF result for that pool pump
in that they will be based on the same test data. However, regarding
the confusion between EF and WEF values, DOE is clarifying in this
final rule that, as of the compliance date of any energy conservation
standard for dedicated-purpose pool pumps, all manufacturers and rating
programs must transition to the new WEF metric and representations of
EF will no longer be allowed. DOE believes this will resolve the
confusion Zodiac is concerned with. Representations of EF and WEF are
discussed in more detail in section III.H.
Therefore, in this final rule DOE is adopting labeling provisions
that require dedicated-purpose pool pumps subject to the test procedure
to be labeled only with WEF and DPPP motor total horsepower. In
response to Hayward's request that the required information not be
required to be co-located on one label or data plate, DOE believes,
given the reduced labeling requirements adopted in this final rule as
compared to the NOPR proposal, that it is entirely reasonable to
require that these values appear on the pump's permanent nameplate.
In response to APSP and Hayward's recommendation that labeling
requirements not apply to three-phase products, DOE notes that this
proposal is not consistent with the recommendations of the DPPP Working
Group. The June 2016 DPPP Working Group recommendations only specified
that standards should not apply to three-phase self-priming pool filter
pumps. (Docket No. EERE-2015-BT-STD-0008, No. 82 Recommendations #3 at
p. 2) Therefore, DOE believes that requiring labels for three-phase
pumps is consistent with requiring them to be subject to the test
procedure and reporting requirements, as recommended by the DPPP
Working Group.
J. Replacement DPPP Motors
DOE understands that DPPP motors typically require replacement more
frequently than DPPP bare pumps and, thus, replacement DPPP motors are
often distributed in commerce to be paired with an existing,
appropriate DPPP bare pump in the field. DOE does not intend to
regulate replacement DPPP motors, because they do not (by themselves)
meet the definition of a dedicated-purpose pool pump. However, DOE
believes that end-users and manufacturers may benefit from having a
method to determine an applicable WEF for replacement DPPP motors. This
method could allow replacement motor manufacturers to label their
products and/or utilities or efficiency programs to encourage the sale
of replacement DPPP motors, which could maintain or increase the
savings of the dedicated-purpose pool pump, as installed in the field.
For those reasons, DOE proposed in the September 2016 DPPP test
procedure NOPR an optional method to determine the WEF for replacement
DPPP motors. 81 FR 64580, 64629 (Sept. 20, 2016). Specifically, under
this method, the replacement motor would be paired with an appropriate
DPPP bare pump and the combination would be subject to the DOE test
procedure for that dedicated-purpose pool pump, based on the DPPP
variety and speed configuration. Id.
In the September 2016 DPPP test procedure NOPR, DOE recognized that
replacement DPPP motors may be offered for sale or advertised to be
paired with multiple DPPP bare pumps. Furthermore, each combination of
a DPPP motor and a DPPP bare pump may have a different WEF, as each
bare pump may affect the WEF rating. Therefore, DOE proposed in the
September 2016 DPPP test procedure NOPR that the WEF for each
replacement DPPP motor and bare pump pairing be determined separately.
However, consistent with DOE's treatment of all equipment, DOE would
allow manufacturers to group similar replacement motor-bare pump
pairings within a given replacement DPPP motor rating to minimize
testing burden, while still ensuring that the rating is representative
of minimum efficiency or maximum energy consumption of the group. DOE
also proposed that replacement DPPP motor manufacturers would be
required to make a statement, along with any advertised WEF value,
regarding the specific DPPP bare pump to which the WEF value applies.
If no specific DPPP bare pumps were listed in the manufacturer
literature or otherwise along with any WEF representation, then the WEF
value would be assumed to be applicable to any and all possible DPPP
bare pumps. Id.
During the September 2016 DPPP test procedure NOPR public meeting,
CA IOUs stated that if the worst performing pump method were to be
utilized for replacement motors, the bare pumps considered would have
to be specified in order to determine which was the worst performing.
(CA IOUs, Public Meeting Transcript, No. 3 at p. 80) As such, CA IOUS
proposed that if manufacturers test the replacement motors, the test
report or result include the range of products that were included in
the test. (CA IOUs, Public Meeting Transcript, No. 3 at pp. 82-84)
DOE acknowledges CA IOUs' concern in unambiguously identifying the
replacement DPPP motor and bare pump combination on which any WEF value
was based. However, as DOE is proposing this as an optional procedure,
DOE did not propose any standard or reporting requirements for
replacement DPPP motors. In addition, the manufacturer of the
replacement DPPP motor may be different than the manufacturer of the
dedicated-purpose pool pump. For this reason, DOE does not believe that
including such information in the list of optional information DPPP
manufacturers may submit when certifying products to DOE would be
appropriate. As reporting of replacement DPPP motor WEF information
would have to be done as a separate certification report and is not
based on compliance with any standard, DOE does not believe collecting
such information is warranted at this time. The purpose of the
procedure is simply to provide a standardized way to determine WEF for
replacement DPPP motors.
ASAP, CA IOUs, CEC, and NRDC commented to support the inclusion of
this optional test method for DPPP replacement motors. (ASAP and NRDC,
No. 12 at p. 2; CA IOUs, No. 9 at p. 2; CEC, No. 7 at p. 2) ASAP and
NRDC and CEC stated that the test method could provide data to guide
consumers and support utility and efficiency programs that seek to
improve the efficiency of dedicated-purpose pool pumps already in use.
(ASAP and NRDC, No. 12 at p. 2; CEC, No. 7 at p. 2)
In written comments, Pentair also supported the optional test
method for DPPP replacement motors. However, Pentair stated its belief
that the DPPP replacement motor testing should be mandatory, to protect
against pool owners pairing low efficiency replacement motors with kit
pumps. (Pentair, No. 11 at p. 4) CA IOUs also believe that a national
standard is needed for DPPP replacement motors. (CA IOUs, No. 9 at p.
2)
Conversely, in written comments, APSP, Hayward, and Nidec opposed
DOE's proposed optional test method for replacement DPPP motors. (APSP,
No. 8 at pp. 10-11; Hayward, No. 6 at
[[Page 36907]]
p. 9; Nidec, No. 10 at p. 6) Hayward noted that such motors were not
discussed by the DPPP Working Group. (Hayward, No. 6 at p. 9) Hayward
and Nidec also believe that the methodology presented by DOE is not
practical and does not ensure compliance. (Hayward, No. 6 at p. 9;
Nidec, No. 10 at p. 6) Nidec suggested that replacement DPPP motors be
regulated through an expansion in small motor regulations. (Nidec, No.
10 at p. 6)
DOE appreciates the support of ASAP, CA IOUs, CEC, and NRDC. In
response to Pentair and CA IOU's request to adopt requirements for
replacement DPPP motors, DOE understands that there is a potential for
pool owners or installation contractors to purchase and pair a pump wet
end with a low-efficiency replacement motor. However, DOE notes that
mandatory requirements for DPPP replacement motors are outside the
scope of this rulemaking, as this rulemaking pertains only to pumps as
defined in 10 CFR 431.462. DOE proposed an optional test method for
replacement motors because of this limitation on rulemaking scope. DOE
notes that in the future it could consider mandatory requirements for
replacement DPPP motors as part of a rulemaking specifically addressing
such motors.
DOE understands Hayward's and Nidec's concerns and agrees that this
specific proposal was not discussed at length by the DPPP Working
Group. However, DOE reiterates that the test method contained in the
September 2016 DPPP test procedure NOPR is an optional test method that
manufacturers of DPPP motors may use at their discretion; there is no
associated certification or compliance criteria for replacement DPPP
motors. That is, replacement DPPP motors would not be required to meet
any energy conservation standard set for dedicated-purpose pool pumps.
The purpose of the test method is solely to provide standardized
information to consumers regarding the efficiency and performance of
replacement DPPP motors and provide an opportunity for efficiency
programs to incentivize the application of more efficient replacement
DPPP motors. In response to Hayward's and Nidec's concern that the test
method is impractical, DOE believes that the proposed test method
presents a reasonable path to determine the representative WEF score
for replacement DPPP motors and notes that Hayward did not provide an
alternative suggestion. In response to Nidec's suggestion that
replacement DPPP motors be regulated through rules crafted specifically
for small motors, DOE notes that, as stated previously, there are no
regulatory requirements pertaining to the optional motor test method.
Rather, the optional test method proposed for DPPP motors is intended
to provide information to consumers and efficiency incentive programs
regarding which motors will conserve energy in a DPPP-specific
application, and DOE believes this information would not be made
available through small motor regulations. As noted previously, this
does not preclude DOE from considering mandatory requirements for
replacement DPPP motors as part of a rulemaking specifically addressing
such motors.
Hayward also recommended clarifying that replacement motors
identical to the original motor that was used to test and qualify the
DPPP model (only varying in nomenclature for marketing purposes, such
as service part number) should be permitted to make representations of
WEF when sold for use with the specific bare pump, without the need for
additional testing. (Hayward, No. 6 at p. 9) DOE agrees with Hayward's
suggestion. DOE believes that so long as the testing of a given DPPP
motor and bare pump pair was performed consistent with DOE's test
procedure for replacement DPPP motors, the rating will be accurate. As
such, the resultant WEF score can be applied to the tested replacement
DPPP motor when offered for sale with the tested DPPP bare pump and
would be identical to that applied to the DPPP model comprised of that
DPPP motor and bare pump.
K. Certification and Enforcement Provisions for Dedicated-Purpose Pool
Pumps
DOE must provide uniform methods for manufacturers to determine
representative values of energy- and non-energy-related metrics, for
each basic model. See 42 U.S.C. 6314(a)(2). These values are used when
making public representations and when determining compliance with
prescribed energy conservation standards. DOE proposed in the September
2016 DPPP test procedure NOPR that DPPP manufacturers use a statistical
sampling plan consistent with the sampling plan for pumps that is
currently specified at 10 CFR 429.59 to determine representative values
of WEF and other energy-related metrics. 81 FR 64580, 64629 (Sept. 20
2016). Manufacturers would use these sampling plans to determine the
representative values of WEF and other metrics necessary to demonstrate
compliance with the adopted energy conservation standards for
dedicated-purpose pool pumps. In addition, DOE commonly specifies
enforcement procedures that DOE uses to verify compliance of a basic
model. Sections, III.K.1, III.K.2, and III.K.3 discuss DOE's sampling
plan, certification requirements, and enforcement provisions for
dedicated-purpose pool pumps, respectively.
1. Sampling Plan
DOE provides, in subpart B to 10 CFR part 429, sampling plans for
all covered equipment. For dedicated-purpose pool pumps, DOE proposed
in the September 2016 DPPP test procedure NOPR to adopt statistical
sampling plans for WEF, EF, and other energy-related metrics similar to
those adopted for pumps. 81 FR 64580, 64630 (Sept. 20, 2016). These
sampling plans generally require a sample of sufficient size such that
the representative value of WEF, EF, or any other energy consumption
metric of a DPPP basic model is less than or equal to the lower of: (A)
The lower 95 percent confidence limit divided by 1.05 or (B) the mean
of the sample. DOE also proposed similar provisions for quantities,
such as pump input power, for which consumers would favor lower values.
See 10 CFR 429.59(a)(1)(ii).
In addition to energy-related metrics, DOE also noted that the
rated hydraulic horsepower, DPPP nominal motor horsepower, DPPP motor
total horsepower, service factor, and true power factor are important
characteristics for dedicated-purpose pool pumps that must be reported
for each DPPP basic model based on the sampling plan discussed above.
Therefore, DOE also proposed that DPPP nominal motor horsepower, DPPP
motor total horsepower, service factor, and true power factor for each
DPPP basic model be determined based on the mean of the applicable test
results, for each metric, from all the tested units that serve as the
basis for the rating for that basic model. 81 FR 64580, 64630 (Sept.
20, 2016).
In written comments, Hayward and APSP requested clarification of
sampling plan and record keeping requirements for certain motor
characteristics. Specifically, APSP and Hayward asked if DOE expects
DPPP manufacturers to establish, maintain, and retain underlying test
data for nominal motor horsepower, motor total horsepower, and motor
service factor for 2 years from the date on which the model is no
longer distributed in commerce or if this information would be the
responsibility of the individual motor manufacturers. (APSP, No. 8 at
p.
[[Page 36908]]
9; Hayward, No. 6 at pp. 7-8) In addition, as noted in section III.H,
Hayward expressed concern over DOE's requirements being in conflict
with other industry programs, especially those regarding determination
of EF. (Hayward, No. 6 at p. 1)
In response to Hayward, DOE notes that while motor manufacturers
may conduct testing of motors, it is the responsibility of the DPPP
manufacturer to retain the underlying test data. As discussed in
section III.G.1.b, DOE is adopting test methods for determination of
motor horsepower characteristics consistent with those currently used
in the industry. However, given the suggestion from interested parties
that DOE only require listing DPPP motor total horsepower on the label
(see section III.I), DOE is withdrawing the proposal to establish
sampling plans for DPPP nominal motor horsepower and DPPP service
factor and adopting a sampling plan for DPPP motor total horsepower
only.
Regarding potential conflict with industry programs, which DOE
believes relates primarily to the sampling plan (as other provisions
are quantitatively consistent), in this final rule, DOE limits the
sampling plan to only metrics necessary for DOE's test procedure,
standard, and labeling requirements (i.e., WEF, rated hydraulic
horsepower, and DPPP motor total horsepower). DOE has removed the
sampling plan requirements for EF and other motor horsepower metrics.
DOE is adopting the other sampling provisions proposed in the September
2016 DPPP test procedure NOPR without modification.
In written comments, APSP asked whether small modifications to the
``basic model'' require new samples to be tested, and if so, if there
is a defined threshold regarding what change would require a new sample
to be tested. (APSP, No. 8 at pp. 10-11) DOE believes that APSP is
asking about how changes to an individual model's design impact the
represented value for a basic model. If any design changes to an
individual model that is part of a basic model result in a more
consumptive or less efficient represented value, then the individual
model must be retested and the represented value must be revised based
on the results of the retesting.
2. Certification Requirements
Paragraph (b) of 10 CFR 429.59 contains the certification
requirements for certain styles of pumps for which DOE adopted test
procedures and standards in the January 2016 general pumps test
procedure and ECS final rules. 81 FR 4086 (Jan. 25, 2016); 81 FR 4368
(Jan. 26, 2016). Because dedicated-purpose pool pumps are a style of
pump, DOE proposed in the September 2016 DPPP test procedure NOPR to
amend 10 CFR 429.59 to include the reporting requirements for
dedicated-purpose pool pumps. 81 FR 64580, 64630-64632 (Sep. 20, 2016).
Specifically, DOE proposed that the general certification report
requirements contained in 10 CFR 429.12 would apply to dedicated-
purpose pool pumps as they do to other styles of pumps, including
general pumps. However, because dedicated-purpose pool pumps have a
unique test procedure and metric from general pumps, DOE proposed
unique certification requirements for dedicated-purpose pool pumps that
require manufacturers to supply certain additional information to DOE
in certification reports to demonstrate compliance with any energy
conservation standards that DOE may set. Id.
Specifically, DOE proposed that the following items be included in
certification reports and made public on DOE's Web site:
WEF in kilogallons per kilowatt-hour (kgal/kWh);
rated hydraulic horsepower in horsepower (hp);
maximum speed of rotation in revolutions per minute (rpm);
dedicated-purpose pool pump nominal motor horsepower in
horsepower (hp);
dedicated-purpose pool pump motor total horsepower in
horsepower (hp);
dedicated-purpose pool pump service factor
(dimensionless);
the speed configuration for which the pump is being rated
(i.e., single-speed, two-speed, multi-speed, or variable-speed);
for self-priming pool filter pumps, non-self-priming pool
filter pumps, and waterfall pumps, the maximum head in feet; and
for self-priming and non-self-priming pool filter pumps:
The vertical lift and true priming time for the DPPP model and a
statement regarding whether the pump is certified with NSF/ANSI 50-
2015. Id.
In the June 2016 DPPP Working Group recommendations, the DPPP
Working Group also recommended that DOE require reporting of true power
factor at all applicable test procedure load points in the public
information provided in the certification report for all dedicated-
purpose pool pumps to which the test procedure is applicable (i.e.,
self-priming and non-self-priming pool filter pumps, waterfall pumps,
and pressure cleaner booster pumps). (Docket No. EERE-2015-BT-STD-0008,
No. 82, Recommendation #7 at p. 4) As such, DOE proposed that, for all
dedicated-purpose pool pumps to which the test procedure is applicable,
true power factor be reported at all applicable test procedure load
points in the certification report and be made public on DOE's Web
site. 81 FR 64580, 64630-64632 (Sep. 20, 2016).
In addition, as discussed in section III.B.7, the DPPP Working
Group recommended specific prescriptive requirements for dedicated-
purpose pool pumps distributed in commerce with freeze protection
controls to ensure freeze protection controls on dedicated-purpose pool
pumps only operate when necessary and do not result in unnecessary,
wasted energy use. Specifically, the DPPP Working Group recommended
that all dedicated-purpose pool pumps distributed in commerce with
freeze protection controls be shipped either:
(1) With freeze protection disabled or
(2) with the following default, user-adjustable settings:
a. The default dry-bulb air temperature setting is no greater than
40 [deg]F; and
b. The default run time setting shall be no greater than 1 hour
(before the temperature is rechecked); and
c. The default motor speed shall not be more than \1/2\ of the
maximum available speed.
(Docket No. EERE-2015-BT-STD-0008, No. 82, Recommendation #6A at p.
4)
Relatedly, the DPPP Working Group recommended that, in order to
certify compliance with such a requirement, DPPP manufacturers be
required to make a statement certifying compliance to the applicable
design requirement and make available publicly as part of their
literature the details by which they have met the applicable design
standard. (Docket No. EERE-2015-BT-STD-0008, No. 82, Recommendation #6B
at p. 4) The DPPP Working Group specifically recommended that, as part
of certification reporting, manufacturers must include the default dry-
bulb air temperature setting (in [deg]F), default run time setting (in
minutes), and default motor speed (in rpm). (Docket No. EERE-2015-BT-
STD-0008, No. 82, Recommendation #6A at p. 4) Therefore, consistent
with recommendations of the DPPP Working Group, DOE proposed that, for
dedicated-purpose pool pumps distributed in commerce with freeze
protection controls enabled, the certification report also include the
default dry-bulb air temperature setting (in [deg]F), default run time
setting (in minutes), and default motor speed (in
[[Page 36909]]
rpm). 81 FR 64580, 64630-64632 (Sep. 20, 2016).
The DPPP Working Group also recommended that DOE include a
verification procedure in case there was ever an issue regarding
whether a product distributed in commerce actually had such features.
(Docket No. EERE-2015-BT-STD-0008, No. 82, Recommendation #6A at p. 4)
The verification test is discussed in more detail in section III.K.3.
Finally, for integral cartridge-filter and sand-filter pool pumps,
the DPPP Working Group recommended DOE consider only a prescriptive
standard, which requires such pumps be distributed in commerce with
pool pump timers. (Docket No. EERE-2015-BT-STD-0008, No. 51,
Recommendation #2B at pp. 1-2) Relatedly, the DPPP Working Group also
recommended a definition for pool pump timer that describes the
specific features and operational characteristics that applicable pool
pump timers must contain in order to comply with the prescriptive
standard. The recommended definition defines pool pump timer as a pool
pump control that automatically turns off a dedicated-purpose pool pump
after a run-time of no longer than 10 hours. As such, for these DPPP
varieties, DOE proposed that the certification report must contain the
maximum run-time of the pool pump control with which the integral
cartridge-filter or sand-filter pump is distributed in commerce. 81 FR
64580, 64630-64632 (Sep. 20, 2016).
In addition to the required elements, DOE recognizes that other
DPPP characteristics may provide useful information to inform consumers
or support programs related to dedicated-purpose pool pumps. To provide
additional information to consumers and the market place, DOE proposed
in the September 2016 DPPP test procedure NOPR that the following
information may optionally be included in certification reports and, if
included, would be made public:
Calculated driver power input and flow rate at each load
point i (Pi and Qi), in horsepower (hp) and gallons per minute (gpm),
respectively; and/or
Energy factor at any desired speed on any of the specified
optional system curves (i.e., Curve A, B, C, or D), along with the
tested speed and the system curve associated with each energy factor
value. 81 FR 64580, 64631-32 (Sept. 20, 2016).
Although useful to consumers and the public, DOE recognizes that
manufacturers may incur additional burden conducting the testing for
and reporting of these additional metrics. DOE reiterates that the
reporting of these additional metrics will be optional and at the
discretion of the manufacturer.
In response to DOE's proposed reporting requirements, ASAP and NRDC
submitted written comments in support of the certification requirements
proposed in the September 2016 DPPP test procedure NOPR. (ASAP and
NRDC, No. 12 at p. 2) DOE appreciates the support of ASAP and NRDC.
During the September 2016 DPPP test procedure NOPR public meeting,
Hayward inquired if they have a pump that meets acceptable NSF priming
criteria, how this should be reported along with the WEF value.
(Hayward, Public Meeting Transcript, No. 3 at p. 74) Additionally, in
written comments, Hayward and APSP commented that the vertical lift and
true priming time fields should only be applicable to self-priming pool
filter pumps that are not certified with NSF/ANSI 50-2015. (Hayward,
No. 6 at p. 10; APSP, No. 8 at p. 11)
As noted in the September 2016 DPPP test procedure NOPR, for self-
priming and non-self-priming pool filter pumps, the certification
report is required to include the vertical lift and true priming time
for the DPPP model and a statement regarding whether the pump is
certified with NSF/ANSI 50-2015. However, in light of Hayward and
APSP's concern, DOE recognizes that these requirements are only
necessary and relevant for self-priming pool filter pumps. In addition,
consistent with Hayward and APSP's request, DOE agrees that a statement
that the self-priming pool filter pump is certified with NSF/ANSI 50-
2015 is sufficient to demonstrate compliance with DOE's definition for
self-priming pool filter pump. Therefore, in this final rule, DOE is
modifying the certification reporting requirements such that only self-
priming pool filter pumps that are not certified with NSF/ANSI 50-2015
need provide the vertical lift and true priming time for the DPPP
model.
In written comments, Hayward and APSP requested that DOE explain
why maximum head (``dead head'') is listed and recommended removing it,
as they did not see the need to list it. (Hayward, No. 6 at p. 10;
APSP, No. 10 at p. 11) In response, DOE clarifies that maximum head is
necessary to differentiate waterfall pumps from self-priming and non-
self-priming pool filter pumps. As described in section III.B.4.a,
section III.G.3, and the September 2016 DPPP test procedure NOPR,
waterfall pumps are, by definition, pool filter pumps with maximum head
less than or equal to 30 feet, and a maximum speed less than or equal
to 1,800 rpm. Therefore, in order to unambiguously distinguish
waterfall pumps from other varieties of pool filter pumps, DOE
established a specific and repeatable method for determining maximum
head of pool filter pumps (discussed in section III.G.3). DOE requires
reporting of the maximum head, determined in accordance with the test
procedure for self-priming pool filter pumps, non-self-priming pool
filter pumps, and waterfall pumps, to ensure that such pumps are
appropriately categorized into the correct equipment class.
Hayward and APSP also recommended that, for dedicated-purpose pool
pumps with freeze protection controls shipped disabled, the default
dry-bulb air temperature setting, default run time setting, and default
motor speed setting should not have to be reported. (Hayward, No. 6 at
p. 10; APSP, No. 10 at p. 11) In response, DOE notes that Hayward and
APSP's suggestion is consistent with the proposal in the September 2016
DPPP test procedure NOPR. 81 FR 64580, 64645 (Sept. 20, 2016). As such,
in this final rule, DOE is adopting the proposal in the September 2016
DPPP test procedure NOPR that in the certification report all
dedicated-purpose pool pumps must provide a statement regarding if
freeze protection is shipped enabled or disabled, but only dedicated-
purpose pool pumps distributed in commerce with freeze protection
controls enabled must provide the default dry-bulb air temperature
setting (in [deg]F), default run time setting (in minutes), and default
motor speed (in rpm).
During the September 2016 DPPP test procedure NOPR public meeting,
CA IOUs recommended clarifying that the maximum run time for integrated
cartridge-filter and sand-filter pumps referred to the maximum run time
without resetting the timer. (CA IOUs, Public Meeting Transcript, No. 3
at p. 90) In response, DOE acknowledges CA IOUs concern that the
maximum run time in the field could be extended by resetting the timer.
However, DOE believes that the maximum run time of the model is the
maximum time interval for which the timer can be set to run and that it
is implied that such does not account for resetting of the timer, as it
is a physical and unambiguous characteristic of the equipment.
Therefore, DOE agrees with CA IOUs regarding the intent of the
statement, but does not believe such clarification is necessary.
APSP and Hayward also requested confirmation that the test
procedure to determine EF is optional and neither it
[[Page 36910]]
nor data relating to it will be required to be provided or certified to
DOE. (APSP, No. 8 at p. 9; Hayward, No. 6 at p. 8) Similarly, Zodiac
also commented that optional items, such as EF, pump efficiency,
overall efficiency, driver power input, and/or pump power output,
should remain optional and up to the manufacturer to present. (Zodiac,
No. 13 at p. 3)
Regarding APSP, Hayward, and Zodiac's comments with respect to EF
and other optional tested values (i.e., pump efficiency, overall
efficiency, driver power input, and/or pump power output), DOE
reiterates that the EF test procedure proposed was optional in that
manufacturers may decline to make any representations of EF, but that
if made, all representations of relevant metrics, including EF, would
need to be based on the DOE test procedure 180 days after publication
of this final rule in the Federal Register. However, EF, pump
efficiency, overall efficiency, driver power input, and/or pump power
output are not required to be reported to DOE.
In addition, as discussed in section III.F, DOE received several
comments from interested parties regarding the testing and
representation of energy factor and consistency with other programs. To
respond to the concerns of interested parties and clarify the
applicability of DPPP metrics, DOE, in this final rule, is adopting two
appendices that are applicable before (appendix B) and on or after
(appendix C) July 19, 2021, the compliance date of the adopted energy
conservation standards for this equipment. As a result of the confusion
regarding representations of energy factor and the lack of comments
supporting the optional reporting of energy factor to DOE, DOE is not
adopting the proposal to optionally list any tested energy factor
values in the certification report submitted to DOE. Specifically, DOE
is not including EF at any desired speed on any of the specified
optional system curves (i.e., Curve A, B, C, or D), along with the
tested speed and the system curve associated with each energy factor
value in the certification report.
DOE did not receive any other comments or suggestions regarding the
certification reporting requirements for dedicated-purpose pool pumps.
As such, DOE is adopting, in this final rule, the certification
reporting requirements as proposed in the September 2016 DPPP test
procedure NOPR, with the exception of the optional listing of energy
factor as discussed above. DOE is also clarifying the applicability of
the certification requirements that are only applicable to certain
styles of pumps for which DOE adopted test procedures and standards in
the January 2016 general pumps test procedure and ECS final rules. 81
FR 4086 (Jan. 25, 2016); 81 FR 4368 (Jan. 26, 2016). DOE notes that, as
specified in paragraph (a) of 10 CFR 429.12, the certification
requirements for covered products and equipment, including those
discussed in this final rule, are only applicable to equipment subject
to an applicable energy conservation standard set forth in 10 CFR part
430 or 431. Therefore, the certification requirements established in
this final rule will only be required on and after July 19, 2021, the
compliance date for energy conservation standards for dedicated-purpose
pool pumps.
3. Enforcement Provisions
Enforcement provisions govern the process DOE will follow when
performing its own assessment of basic model compliance with standards,
as described under subpart C of 10 CFR part 429. Specifically, subpart
C describes the notification requirements, legal processes, penalties,
specific prohibited acts, and testing protocols related to testing
covered equipment to determine or verify compliance with standards. 10
CFR 429.102-429.134. DOE notes that the same general enforcement
provisions contained in subpart C of 10 CFR part 429 will be applicable
to dedicated-purpose pool pumps.
Related to enforcement testing of dedicated-purpose pool pumps, as
specified in 10 CFR 429.110(e), DOE proposed in the September 2016 DPPP
test procedure NOPR to conduct the applicable DPPP test procedure, to
determine the WEF for tested DPPP models. 81 FR 64580, 64632 (Sept. 20,
2016). In addition, DOE proposed to use, when determining performance
for a specific basic model, the enforcement testing sample size,
calculations, and procedures laid out in appendix A to subpart C of 10
CFR part 429 for consumer products and certain high-volume commercial
equipment. These procedures, in general, provide that DOE will test an
initial sample of at least 4 units and determine the mean WEF value and
standard error of the sample. DOE will then compare these values to the
WEF standard level, once adopted, to determine the compliance of the
basic model or if additional testing (up to a total of 21 units) is
required to make a compliance determination with sufficient confidence.
DOE also proposed to clarify that the provisions at 10 CFR
429.110(e)(5), which are applicable to general pumps subject to the
January 2016 general pumps test procedure final rule, are not
applicable to dedicated-purpose pool pumps. Id.
In addition, when determining compliance of any units tested for
enforcement purposes, DOE proposed in the September 2016 DPPP test
procedure NOPR to adopt provisions that specify how DOE would determine
the rated hydraulic horsepower at maximum speed on the reference curve
for determining the appropriate test method and standard level for any
tested equipment (if applicable). Specifically, DOE proposed to perform
the same test procedure for determining the rated hydraulic horsepower
at maximum speed on the reference curve specified by the test procedure
for each DPPP variety (see section III.D) on one or more units of each
model selected for testing. DOE proposed that, if the rated hydraulic
horsepower determined through DOE's testing (either the measured rated
hydraulic horsepower for a single unit sample or the average of the
measured rated hydraulic horsepower values for a multiple unit sample)
is within 5 percent of the certified value of rated hydraulic
horsepower, then DOE will use the certified value of rated hydraulic
horsepower as the basis for determining the standard level for tested
equipment. However, if DOE's tested value of rated hydraulic horsepower
is not within 5 percent of the certified value of rated hydraulic
horsepower, DOE will use the arithmetic mean of all the rated hydraulic
horsepower values resulting from DOE's testing when determining the
standard level for tested equipment. 81 FR 64580, 64632 (Sept. 20,
2016).
In addition, DOE proposed to establish similar procedures for
relevant quantities necessary to differentiate the varieties of pool
filter pumps: Self-priming pool filter pumps, non-self-priming pool
filter pumps, and waterfall pumps. Specifically, to differentiate
waterfall pumps, DOE proposed an enforcement testing procedure for the
maximum head value. Similarly, to differentiate self-priming and non-
self-priming pool filter pumps, DOE proposed performing the self-
priming capability test and determine the vertical lift and true
priming time of one or more tested units. DOE proposed tolerances of 5
percent on the certified values in both of these instances as well. Id.
Pentair responded that without audit and enforcement, the economic
effect from the potential costs related to testing (see section IV.B)
could be low as manufacturers will not feel compelled to re-test
dedicated-purpose pool pumps. (Pentair, No. 11 at p. 4) DOE responds
that DOE does conduct
[[Page 36911]]
enforcement testing, as discussed in this section. If a product is
suspected of not meeting the minimum energy conservation standard, DOE
has enforcement mechanisms to verify the equipment performance in
relation to the standard. DOE's burden assessment contained in section
IV.B reflects the assumption that manufacturers will conduct testing
and certify equipment in accordance with the test procedure adopted in
this final rule.
DOE did not receive any other comments related to DOE's proposal
related to enforcement testing provisions for WEF, rated hydraulic
horsepower, maximum head, or self-priming capability. As such, DOE is
adopting the enforcement testing provisions for WEF, rated hydraulic
horsepower, and maximum head, as proposed in the September 2016 DPPP
test procedure NOPR. However, with regard to the enforcement provisions
to verify the self-priming capability of non-self-priming pool filter
pumps and self-priming pool filter pumps not certified with NSF/ANSI
50-2015, DOE notes that, in response to comments from interested
parties, DOE is removing the requirement to report the vertical lift
and true priming time of non-self-priming pool filter pumps, as
discussed in section III.K.2. As DOE's proposed enforcement testing
provisions included comparing the tested values to the values of
vertical lift and true priming time certified by the manufacturer to
determine the validity of the certified values, DOE must adopt
different criteria for non-self-priming pool filter pumps, as they will
not have certified values to which DOE can compare the test results.
Instead, DOE is adopting validity criteria for non-self-priming pool
filter pumps based on the values of vertical lift and true priming time
referenced in the definition of non-self-priming pool filter pump. That
is, DOE will compare the values of vertical lift and true priming time
obtained from the tested unit(s) to the values of vertical lift and
true priming time referenced in the definition of non-self-priming pool
filter pump (i.e., 5.0 feet and 10.0 minutes, respectively). DOE will
continue to apply the same tolerance of 5 percent so that any non-self-
priming pool filter pump that is not capable of priming to a vertical
lift of 5.0 feet with a true priming time of less than or equal to 9.5
minutes (10.0 minutes--5 percent) will continue to be treated as a non-
self-priming pool filter pump, as certified by the manufacturer. DOE
notes that vertical lift and true priming time are related variables,
such that the 5 percent tolerance need only be applied to true priming
time as the independent variable.
In addition, based on DPPP Working Group recommendations (Docket
No. EERE-2015-BT-STD-0008, No. 82, Recommendation #6B at p. 4), DOE
also proposed in the September 2016 DPPP test procedure NOPR a
procedure to verify the presence and operation of any freeze protection
controls distributed in commerce with any applicable dedicated-purpose
pool pump. The proposed procedure starts by installing the DPPP unit in
a test stand in accordance with HI 40.6-2014 with the pump powered on
but not circulating water (i.e., the controls are active and the flow
or speed are set to zero). The temperature measured by the freeze
protection temperature control would then be gradually decreased by 1
0.5 [deg]F every 5.0 minutes, starting at 42
0.5 [deg]F until the pump freeze protection controls initiate water
circulation or 38 0.5 [deg]F, whichever occurs first. The
freeze protection ambient temperature reading and DPPP rotating speed,
if any, would be recorded after each reduction in temperature and
subsequent stabilization. 81 FR 64580, 64633 (Sept. 20, 2016).
Under DOE's proposed test procedure, if the DPPP freeze protection
controls do not initiate water circulation at a temperature of 38
0.5 [deg]F, as measured by the freeze protection ambient
temperature sensor, the test would conclude and the dedicated-purpose
pool pump would be deemed compliant. If the freeze protection controls
initiate water circulation, the temperature would be increased to 42
0.5 [deg]F and the dedicated-purpose pool pump would be
allowed to run for at least 30.0 minutes. After 30.0 minutes, the
freeze protection ambient temperature and rotating speed, if any, would
be recorded again. If the dedicated-purpose pool pump initiated water
circulation at a temperature greater than 40 [deg]F, if the dedicated-
purpose pool pump is still circulating water after 30.0 minutes of
operation at 42 0.5 [deg]F, or if rotating speed for
freeze protection is greater than one-half of the maximum rotating
speed of the DPPP model, as certified by the manufacturer, that DPPP
model would be deemed to not comply with the stated design requirement
for freeze protection controls. Id.
In written comments, ASAP and NRDC expressed appreciation that DOE
developed a verification procedure that can be used to verify whether a
DPPP shipped with freeze protection controls meets the freeze
protection certification requirements promulgated in this rule. (ASAP
and NRDC, No. 12 at pp. 2-3) DOE appreciates the support of ASAP and
NRDC.
During the September 2016 DPPP test procedure NOPR public meeting,
Pentair raised a concern that the default run-time setting in the
freeze protection requirements recommended by the DPPP Working Group is
no greater than an hour, but the test procedure stops after 30.0
minutes. (Pentair, Public Meeting Transcript, No. 3 at p. 101)
In response, DOE agrees with Pentair that the time requirement in
the freeze protection enforcement testing procedure should be 60.0
minutes, rather than the 30.0 minutes proposed in the September 2016
DPPP test procedure NOPR, consistent with the recommendations of the
DPPP Working Group. Therefore, in this final rule, DOE is updating the
procedure to allow 60.0 minutes of operation before the freeze
protection ambient temperature and rotating speed, if any, will be
recorded again.
In written comments, APSP and Pentair questioned why the dry-bulb
temperature was selected as the measurement to determine temperature.
APSP and Pentair commented that few if any of the products in the
market use dry-bulb temperature sensors to initiate freeze protection
controls. (APSP, No. 8 at p. 4; Pentair, No. 11 at p. 2) DOE responds
that DOE researched the typical controls and sensing mechanisms of
freeze protection controls when developing the test method. Based on
DOE's research, the three largest pool pump manufacturers produce
freeze protection systems that sense the ambient air temperature and
(if freeze protection is enabled) activate the freeze protection mode
when the ambient air temperature falls below a certain threshold.\62\
On May 19, 2016, the DPPP Working Group discussed using the dry-bulb
air temperature as one of the key metrics for specifying the
characteristics of freeze protection controls, and no members of the
group opposed the use of dry-bulb temperature. (Docket No. EERE-2015-
BT-STD-0008, No. 101 at pp. 105-107) Then, the DPPP Working Group
recommended that manufacturers include dry-bulb air temperature in
their certification reports. (Docket No. EERE-2015-BT-STD-0008, No. 82
Recommendation #6A at p. 4) DOE
[[Page 36912]]
believes that the manufacturers' installation and operation manuals,
the DPPP Working Group discussions, and the DPPP Working Group
recommendations provide ample justification for using dry-bulb air
temperature as a certification requirement for dedicated-purpose pool
pumps distributed in commerce with freeze protection controls enabled.
Further, DOE is not aware of other temperature-based criteria that are
relevant to the activation of freeze protection controls at this time
and Pentair did not provide an alternative recommendation in their
comments. If freeze protection controls are developed that activate
based on alternative temperature criteria (other than dry-bulb air
temperature), DOE may consider modifying the enforcement test and any
prescriptive freeze protection control requirements at that time.
---------------------------------------------------------------------------
\62\ Several operation manuals for pool control systems note
that freeze protection is triggered by air temperature. See, for
example: Pentair. Intellitouch Quick-Start Manual. 2004.
www.pentairpool.com/pdfs/IntelliTouchQuickStartIG.pdf. Hayward. Pro
Logic Operation Manual. 2010. www.hayward-pool.com/pdf/manuals/PLTPM-PL-PS-x&PL-PS-x-VOperationsOct08&Later.pdf.
---------------------------------------------------------------------------
CA IOUs also raised questions related to the temperature
measurement apparatus and whether the measurement would be impacted by
heat created by the DPPP motor. (CA IOUs, Public Meeting Transcript,
No. 3 at pp. 101-102)
In response, DOE notes that, as described in the September 2016
DPPP test procedure NOPR, several methods are allowed to control and
record the temperature registered by the freeze protection ambient
temperature sensor. This can be accomplished, depending on the specific
location and configuration of the temperature sensor, by exposing the
freeze protection thermocouple to a specific temperature by, for
example, submerging the thermocouple in a water bath of known
temperature, adjusting the ambient air temperature of the test chamber
and measuring the temperature directly at the freeze protection ambient
temperature sensor location, or other means to simulate and vary the
ambient temperature registered by the freeze protection temperature
sensor(s). While DOE acknowledges that, as noted by CA IOUs, the
temperature measured by the freeze protection ambient temperature
sensor may be slightly higher than the bulk ambient temperature due to
localized heating of the sensor from the DPPP motor and controls, DOE
believes this is representative of operation in the field and the test
procedure is designed to accommodate this. Based on the recommendations
of the DPPP Working Group, the freeze protection enforcement test is
designed to identify DPPP freeze protection controls that initiate
water circulation when the freeze protection ambient temperature sensor
registers 40.0 [deg]F or higher, regardless of the bulk ambient
temperature (which may be slightly cooler than 40.0 [deg]F). DOE notes
that this is accomplished regardless of the method used to measure and
control the freeze protection ambient temperature sensor and enables
the variety of methods discussed previously. If only the bulk ambient
temperature were measured, the pump would need to be placed in an
environmental chamber and the temperature of the chamber controlled in
order to test the freeze protection controls operation. In summary, DOE
believes that the proposed temperature measurement methods provide a
representative measure of the ambient temperature measured by the
freeze protection controls and minimizes burden associated with the
test by providing a variety of options for measuring and controlling
the temperature registered by the freeze protection ambient temperature
sensor. DOE also believes the proposal is consistent with the intent of
the DPPP Working Group recommendations. Therefore, while DOE
acknowledges CA IOUs concern, DOE is adopting the specifications
regarding measurement of the temperature registered by the freeze
protection ambient temperature sensor as proposed in the September 2016
DPPP test procedure NOPR.
APSP and Hayward, in written comments, recommended clarifying that
enforcement testing of freeze protection is not applicable for units
shipped with the freeze protection disabled. (APSP, No. 8 at p. 11;
Hayward, No. 6 at p. 10) In response, DOE clarifies that the provisions
are primarily intended to verify that the default settings for
dedicated-purpose pool pumps shipped with freeze protection control
enabled are within the thresholds recommended by the DPPP Working
Group. However, DOE notes that the freeze protection control
enforcement test could also be applied to dedicated-purpose pool pumps
shipped with freeze protection control disabled to verify the fact that
the controls were, in fact, disabled. In either case, any dedicated-
purpose pool pumps tested under the freeze protection control
enforcement test provisions should not be altered from their as-shipped
settings. DOE is clarifying, in this final rule, that dedicated-purpose
pool pumps must be tested in the ``as-shipped control settings'' when
applying the freeze protection control enforcement test. DOE notes that
the actual design requirements would be established in any ECS
rulemaking for dedicated-purpose pool pumps and that this verification
procedure would only be necessary if and when any such requirements are
established.
APSP and Hayward also recommended clarifying that the vertical lift
and true priming time for enforcement testing of the self-priming
capability test should be 6 minutes or the manufacturers recommended
prime time, as permitted by NSF/ANSI 50-2015. (APSP, No. 8 at p.11;
Hayward, No. 6 at p. 10)
In response, DOE acknowledges that, as defined, self-priming pool
filter pumps that are certified with NSF/ANSI 50-2015 would have been
tested based on the criteria in NSF/ANSI 50-2015 that allow for some
amount of manufacturer discretion with regard to the tested vertical
lift and true priming time. Specifically, NSF/ANSI 50-2015 allows a
vertical lift of 5 feet or the manufacturers specified lift, whichever
is greater, and a true priming time not to exceed 6 minutes or the
manufacturers recommended time, whichever is greater. However, DOE
notes that DOE's self-priming capability enforcement testing provisions
are fundamentally designed to evaluate the self-priming capability of a
pool filter pump not certified to NSF/ANSI 50-2015 as self-priming to
verify the appropriate equipment class is applied to each DPPP model.
As such, the criteria adopted in the definitions of self-priming and
non-self-priming pool filter pump (see section III.B.3.a) are most
applicable.
In addition, DOE notes that, as discussed in the DPPP Working
Group, DOE's specified criteria of a vertical lift of 5.0 feet and true
priming time of 10.0 minutes were meant to ensure that any pump
certified to NSF/ANSI 50-2015 as a self-priming pump would inherently
meet DOE's criteria for self-priming pumps. That is, based on NSF/ANSI
criteria, any pump that was certified as self-priming would have a
vertical lift of at least 5.0 feet, which would also comply with DOE's
requirement. Regarding the true priming time, as NSF/ANSI 50-2015
allows for a true priming time of 6 minutes or the manufacturers
specified time, whichever is greater, it is possible that a pump could
be certified to NSF/ANSI 50-2015 with a priming time greater than 10.0
minutes and still be qualified as a self-priming pump. However, the
DPPP Working Group noted on several occasions that the majority of
existing self-priming pool filter pumps have true priming times less
than 10.0 minutes. (Docket No. EERE-2015-BT-STD-0008, No. 95 at pp. 20-
38, 110-113, and 119-128; Docket No. EERE-2015-BT-STD-0008, No. 79 at
pp. 154-192) However, DOE would only apply the self-priming
[[Page 36913]]
capability enforcement test to pool filter pumps that are not certified
as self-priming with NSF/ANSI 50-2015 and, therefore, DOE's
requirements of 5.0 feet and 10.0 minutes are the applicable
thresholds.
IV. Procedural Issues and Regulatory Review
A. Review Under Executive Order 12866
The Office of Management and Budget (OMB) has determined that test
procedure rulemakings do not constitute ``significant regulatory
actions'' under section 3(f) of Executive Order 12866, Regulatory
Planning and Review, 58 FR 51735 (Oct. 4, 1993). Accordingly, this
action was not subject to review under the Executive Order by the
Office of Information and Regulatory Affairs (OIRA) in the Office of
Management and Budget (OMB).
B. Review Under the Regulatory Flexibility Act
The Regulatory Flexibility Act (5 U.S.C. 601 et seq.) requires
preparation of a regulatory flexibility analysis for any rule that by
law must be proposed for public comment, unless the agency certifies
that the rule, if promulgated, will not have a significant economic
impact on a substantial number of small entities. As required by
Executive Order 13272, ``Proper Consideration of Small Entities in
Agency Rulemaking,'' 67 FR 53461 (August 16, 2002), DOE published
procedures and policies on February 19, 2003 to ensure that the
potential impacts of its rules on small entities are properly
considered during the DOE rulemaking process. 68 FR 7990. DOE has made
its procedures and policies available on the Office of the General
Counsel's Web site: https://energy.gov/gc/office-general-counsel.
DOE reviewed this final rule, which establishes a new test
procedure for dedicated-purpose pool pumps, under the provisions of the
Regulatory Flexibility Act and the procedures and policies published on
February 19, 2003. DOE concludes that this final rule will not result
in a significant impact on a substantial number of small entities, as
it would not, in and of itself, require the use of the adopted test
procedure. That is, any burden associated with testing dedicated-
purpose pool pumps in accordance with the requirements of this test
procedure is accounted for in the related January 2017 DPPP DFR, as
promulgation of energy conservation standards is what ultimately
requires use of the adopted test procedure. 82 FR 5650, 5738-40. On
this basis, DOE certifies that this test procedure final rule would not
have a ``significant economic impact on a substantial number of small
entities,'' and the preparation of a regulatory flexibility analysis is
not warranted. DOE will transmit the certification and supporting
statement of factual basis to the Chief Counsel for Advocacy of the
Small Business Administration (SBA) for review under 5 U.S.C. 605(b).
1. Review of DPPP Manufacturers
As presented in the September 2016 DPPP test procedure NOPR, DOE
conducted a focused inquiry into manufacturers of equipment covered by
this rulemaking. During its market survey, DOE used available public
information to identify potential small manufacturers. DOE's research
involved the review of individual company Web sites and marketing
research tools (e.g., Dun and Bradstreet reports, Manta, Hoovers) to
create a list of companies that manufacture pumps covered by this
rulemaking. Using these sources, DOE identified 21 distinct
manufacturers of dedicated-purpose pool pumps. 81 FR 64580, 64637.
DOE notes that the Regulatory Flexibility Act requires analysis of,
in particular, ``small entities'' that might be affected by the rule.
For the DPPP manufacturing industry, the SBA has set a size threshold,
which defines those entities classified as ``small businesses'' for the
purpose of the statute. DOE used the SBA's size standards to determine
whether any small entities would be required to comply with the rule.
The size standards are codified at 13 CFR part 121. The standards are
listed by North American Industry Classification System (NAICS) code
and industry description and are available at https://www.sba.gov/sites/default/files/files/Size_Standards_Table.pdf.
DPPP manufacturers are classified under NAICS 333911, ``Pump and
Pumping Equipment Manufacturing.'' The SBA sets a threshold of 750
employees or less for an entity to be considered as a small business
for this category. To determine the number of DPPP manufacturers that
are small businesses and might be differentially affected by the rule,
DOE reviewed these data to determine whether the entities met the SBA's
definition of a small business manufacturer of dedicated-purpose pool
pumps and then screened out companies that do not offer equipment
covered by this rulemaking, do not meet the definition of a ``small
business,'' are foreign-owned and operated, or are owned by another
company. Based on this review, DOE identified five companies that would
be considered small manufacturers by the SBA definition in terms of the
number of employees.
DOE requested comment on this estimate in the September 2016 DPPP
test procedure NOPR. 81 FR 64580, 64637 (Sept. 20, 2016). Hayward
commented that they had no means to confirm the accuracy of this value.
(Hayward, No. 10 at pp. 10-11) Further analysis of small businesses was
conducted as part of the Manufacturer Impact Analysis discussed in the
January 2017 DPPP DFR. 82 FR 5650, 5726.
2. Burden of Conducting the DOE DPPP Test Procedure
Although DOE maintains that this test procedure has no incremental
burden associated with it when viewed as a stand-alone rulemaking, DOE
recognizes that DPPP energy conservation standards were adopted in the
January 2017 DPPP DFR. 86 FR 5650, 5743. Given the DPPP ECS rulemaking
and the potential testing manufacturers may elect to undertake prior to
July 19, 2021, the compliance date of adopted standards, DOE estimated
the cost of developing certified ratings for covered DPPP models.
In the September 2016 DPPP test procedure NOPR, DOE estimated the
cost to test and certify a DPPP basic model, and the total
certification cost for each manufacturer, based on input from
manufacturers and independent research. DOE estimated the cost for both
(a) testing units in house and (b) testing units at a third-party
testing facility. Using the assumption that each manufacturer rates 15
basic models on average, DOE developed testing costs for manufacturers
that perform in-house testing ranging from $1,000 to $1,350 per basic
model. This included up to $1,000 in capital costs, and up to $350 in
labor costs to perform the DPPP tests to comply with DOE's testing
requirements. For testing units at third party test labs, DOE estimated
the cost to be $11,000 per basic model. 81 FR 64580, 64635-64637 (Sept.
20, 2016).
In response to the September 2016 DPPP test procedure NOPR, APSP,
Hayward, and Pentair commented that DOE's estimated capital cost for
in-house testing is too low. APSP, Hayward, Pentair, and Zodiac stated
that a manufacturer starting out should expect to spend between $50,000
and $100,000 for equipment suitable for testing. (APSP, No. 8 at p. 11;
Hayward, No. 6 at p. 10; Pentair, No. 11, at p. 4; Zodiac, No. 13 at p.
3) In addition, Hayward, APSP, and Zodiac stated that the estimated
time to complete a test of a DPPP basic model is between 12 and 14
hours. (APSP, No. 8 at p. 11;
[[Page 36914]]
Hayward, No. 6 at p. 10; Zodiac, No. 13 at p. 3)
DOE notes that APSP, Hayward, Pentair, and Zodiac did not provide
additional detail regarding the basis for their estimates or why they
are higher than DOE's estimates. However, DOE recognizes that the
assumptions in the September 2016 DPPP test procedure NOPR only
accounted for the capital cost of acquiring the necessary equipment and
did not account for the additional labor associated with setting up and
commissioning any new testing facility. DOE believes that, including
the additional labor estimates, a figure of $50,000 to $100,000 may be
appropriate. Therefore, DOE has revised the worst-case burden estimate,
which was previously estimated as $43,800, using the information
provided by manufacturers. Using the same assumption from the September
2016 DPPP test procedure NOPR that each manufacturer will rate 15 basic
models on average and the estimated capital costs provided by Hayward,
APSP, Pentair, and Zodiac, the worst-case burden estimate ranges from
$3,333 to $6,666 per basic model. In addition, adjusting the testing
time to 14 hours and using a labor rate with fringe benefits of $56.42
per hour,\63\ the total labor costs are $790 per basic model. In total,
using estimates from Hayward, APSP, Pentair, and Zodiac, the per basic
model testing costs range from $4,123 to $7,456.
---------------------------------------------------------------------------
\63\ U.S. Department of Labor, Bureau of Labor Statistics. 2015.
Employer Costs for Employee Compensation--Management, Professional,
and Related Employees. Washington, DC. www.bls.gov/news.release/pdf/ecec.pdf.
---------------------------------------------------------------------------
However, as discussed in the September 2016 DPPP test procedure
NOPR, many DPPP manufacturers already have existing testing
capabilities and likely would not incur the full burden on constructing
completely new test facilities. Specifically, DOE estimated a more
representative burden estimate of $15,000 for manufacturers that may be
required to acquire new power measurement equipment and power
conditioning equipment to comply with the proposed test procedure
requirements. However, DOE noted that the costs could be as low as $0.
81 FR 64580, 64635-64637 (Sept. 20, 2016). DOE notes that these
representative burden estimates are consistent with the comments of
APSP, Hayward, and Pentair that many of the requirements regarding test
equipment and test conditions adopted in the DOE test procedure are
consistent with (or less stringent than) those already in use in
manufacturer's test labs (see section III.E.2.e and III.E.2.f). (APSP,
No. 8 at p. 7; Hayward, No. 6 at pp. 7, 11; Pentair, No. 11 at p. 4) In
addition, in response to comments from interested parties, DOE is
making several modifications in this test procedure final rule to
further align testing requirements with existing industry programs and,
therefore, reduce testing burden for manufacturers (see section
III.E.2, III.H, and III.K.1). However, Pentair pointed out that
manufacturers may need to upgrade capacity to certify all applicable
DPPP models in accordance with the regulation. (Pentair, No. 11 at p.
4) While DOE understands that manufacturers may incur cost to certify
DPPP models in accordance with any energy conservation standard that
may be set, there is no requirement to certify any or all models
associated with this test procedure final rule. As such, DOE is
assessing the burden associated with certifying DPPP models in
accordance with this test procedure and the impact on manufacturers in
the Manufacturer Impact Analysis in the associated energy conservation
standard (Docket No. EERE-2015-BT-STD-0008). Specifically, in the
Manufacturer Impact Analysis in the energy conservation standard, DOE
is including the highest cost per basic model testing cost estimate to
prevent underestimating testing burden to the industry. DOE determined
that the per basic model test cost at third-party test labs ($11,000
per model, as estimated in the September 2016 DPPP test procedure NOPR)
is greater than the per basic model test cost estimate from Hayward,
Pentair, and APSP. Therefore, in the ECS Manufacturer Impact
Assessment, DOE assumes that all manufacturers test 15 basic models at
third-party test labs at a cost of $11,000 per basic model.
In the September 2016 DPPP test procedure NOPR, DOE also estimated
that manufacturers incur testing burden every time a new basic model is
introduced. DOE estimated that manufacturers introduce or significantly
modify the basic model every 5 years. Pentair APSP, and Zodiac
responded that significant changes in basic models are not common and
the 5 year estimate is low. APSP commented that 5 years is the minimum
time for a manufacturer to make changes to basic models, but it could
be as much as 10 years. (Pentair, No. 11 at p. 4; APSP, No. 8 at p. 12;
Zodiac, No. 13 at p. 3) DOE appreciates the comments from the
interested parties and concludes that, based on the updated testing
time of 14 hours discussed previously, ongoing testing costs would be
approximately $790 per manufacturer to certify new models. However, DOE
reiterates that this cost would not be required until the compliance
date of any energy conservation standard that may be adopted for such
equipment.
C. Review Under the Paperwork Reduction Act of 1995
All collections of information from the public by a Federal agency
must receive prior approval from OMB. DOE has established regulations
for the certification and recordkeeping requirements for covered
consumer products and industrial equipment. 10 CFR part 429, subpart B.
In an application to renew the OMB information collection approval for
DOE's certification and recordkeeping requirements filed in January
2015, DOE included an estimated burden for manufacturers of pumps in
case DOE ultimately sets energy conservation standards for this
equipment, and OMB approved the revised information collection for
DOE's certification and recordkeeping requirements. 80 FR 5099 (Jan.
30, 2015). In the January 2016 general pumps ECS final rule, DOE
established energy conservation standards and reporting requirements
for certain categories of pumps and estimated that public reporting
burden for the certification for pumps, similar to other covered
consumer products and commercial equipment, would average 30 hours per
response, including the time for reviewing instructions, searching
existing data sources, gathering and maintaining the data needed, and
completing and reviewing the collection of information. 81 FR 4368,
4428 (Jan. 26, 2016). As dedicated-purpose pool pumps are a specific
style of pump and the testing and certification requirements adopted in
this final rule are similar to those established for general pumps in
the January 2016 general pumps test procedure final rule, DOE believes
that the estimated reporting burden of 30 hours would also be
applicable for dedicated-purpose pool pumps. 81 FR 4086 (Jan. 25,
2016). DOE notes that, although this test procedure rulemaking
discusses recordkeeping requirements that are associated with executing
and maintaining the test data for this equipment (see section III.K.1),
certification requirements would not need to be performed until July
19, 2021, the compliance date of adopted energy conservation standards
for dedicated-purpose pool pumps.
Notwithstanding any other provision of the law, no person is
required to respond to, nor shall any person be subject to a penalty
for failure to comply with, a collection of information subject to the
requirements of the PRA, unless
[[Page 36915]]
that collection of information displays a currently valid OMB Control
Number.
D. Review Under the National Environmental Policy Act of 1969
In this final rule, DOE is adopting new definitions; a new test
procedure; and new certification, enforcement, and labeling
requirements for dedicated-purpose pool pumps. DOE has determined that
this rule falls into a class of actions that are categorically excluded
from review under the National Environmental Policy Act of 1969 (42
U.S.C. 4321 et seq.) and DOE's implementing regulations at 10 CFR part
1021. Specifically, this rule considers a test procedure for dedicated-
purpose pool pumps that is largely based upon industry test procedures
and methodologies resulting from a negotiated rulemaking without
affecting the amount, quality, or distribution of energy usage, and,
therefore, will not result in any environmental impacts. Thus, this
rulemaking is covered by Categorical Exclusion A5 under 10 CFR part
1021, subpart D, which applies to any rulemaking that interprets or
amends an existing rule without changing the environmental effect of
that rule. Accordingly, neither an environmental assessment nor an
environmental impact statement is required.
E. Review Under Executive Order 13132
Executive Order 13132, ``Federalism,'' 64 FR 43255 (August 4,
1999), imposes certain requirements on agencies formulating and
implementing policies or regulations that preempt State law or that
have Federalism implications. The Executive Order requires agencies to
examine the constitutional and statutory authority supporting any
action that would limit the policymaking discretion of the States and
to carefully assess the necessity for such actions. The Executive Order
also requires agencies to have an accountable process to ensure
meaningful and timely input by State and local officials in the
development of regulatory policies that have Federalism implications.
On March 14, 2000, DOE published a statement of policy describing the
intergovernmental consultation process it will follow in the
development of such regulations. 65 FR 13735. DOE examined this final
rule and determined that it will not have a substantial direct effect
on the States, on the relationship between the national government and
the States, or on the distribution of power and responsibilities among
the various levels of government. EPCA governs and prescribes Federal
preemption of State regulations as to energy conservation for the
products that are the subject of this final rule. States can petition
DOE for exemption from such preemption to the extent, and based on
criteria, set forth in EPCA. (42 U.S.C. 6297(d)) No further action is
required by Executive Order 13132.
F. Review Under Executive Order 12988
Regarding the review of existing regulations and the promulgation
of new regulations, section 3(a) of Executive Order 12988, ``Civil
Justice Reform,'' 61 FR 4729 (Feb. 7, 1996), imposes on Federal
agencies the general duty to adhere to the following requirements: (1)
Eliminate drafting errors and ambiguity; (2) write regulations to
minimize litigation; (3) provide a clear legal standard for affected
conduct rather than a general standard; and (4) promote simplification
and burden reduction. Section 3(b) of Executive Order 12988
specifically requires that Executive agencies make every reasonable
effort to ensure that the regulation (1) clearly specifies the
preemptive effect, if any; (2) clearly specifies any effect on existing
Federal law or regulation; (3) provides a clear legal standard for
affected conduct while promoting simplification and burden reduction;
(4) specifies the retroactive effect, if any; (5) adequately defines
key terms; and (6) addresses other important issues affecting clarity
and general draftsmanship under any guidelines issued by the Attorney
General. Section 3(c) of Executive Order 12988 requires Executive
agencies to review regulations in light of applicable standards in
sections 3(a) and 3(b) to determine whether they are met or it is
unreasonable to meet one or more of them. DOE has completed the
required review and determined that, to the extent permitted by law,
this final rule meets the relevant standards of Executive Order 12988.
G. Review Under the Unfunded Mandates Reform Act of 1995
Title II of the Unfunded Mandates Reform Act of 1995 (UMRA)
requires each Federal agency to assess the effects of Federal
regulatory actions on State, local, and Tribal governments and the
private sector. Public Law 104-4, sec. 201 (codified at 2 U.S.C. 1531).
For a regulatory action resulting in a rule that may cause the
expenditure by State, local, and Tribal governments, in the aggregate,
or by the private sector of $100 million or more in any one year
(adjusted annually for inflation), section 202 of UMRA requires a
Federal agency to publish a written statement that estimates the
resulting costs, benefits, and other effects on the national economy.
(2 U.S.C. 1532(a), (b)) The UMRA also requires a Federal agency to
develop an effective process to permit timely input by elected officers
of State, local, and Tribal governments on a proposed ``significant
intergovernmental mandate,'' and requires an agency plan for giving
notice and opportunity for timely input to potentially affected small
governments before establishing any requirements that might
significantly or uniquely affect small governments. On March 18, 1997,
DOE published a statement of policy on its process for
intergovernmental consultation under UMRA. 62 FR 12820; also available
at https://energy.gov/gc/office-general-counsel. DOE examined this final
rule according to UMRA and its statement of policy and determined that
the rule contains neither an intergovernmental mandate, nor a mandate
that may result in the expenditure of $100 million or more in any year,
so these requirements do not apply.
H. Review Under the Treasury and General Government Appropriations Act,
1999
Section 654 of the Treasury and General Government Appropriations
Act, 1999 (Pub. L. 105-277) requires Federal agencies to issue a Family
Policymaking Assessment for any rule that may affect family well-being.
This final rule will not have any impact on the autonomy or integrity
of the family as an institution. Accordingly, DOE has concluded that it
is not necessary to prepare a Family Policymaking Assessment.
I. Review Under Executive Order 12630
DOE has determined, under Executive Order 12630, ``Governmental
Actions and Interference with Constitutionally Protected Property
Rights,'' 53 FR 8859 (March 18, 1988), that this regulation will not
result in any takings that might require compensation under the Fifth
Amendment to the U.S. Constitution.
J. Review Under Treasury and General Government Appropriations Act,
2001
Section 515 of the Treasury and General Government Appropriations
Act, 2001 (44 U.S.C. 3516 note) provides for agencies to review most
disseminations of information to the public under guidelines
established by each agency pursuant to general guidelines issued by
OMB. OMB's guidelines were published at 67 FR 8452 (Feb. 22, 2002), and
DOE's guidelines were published at 67 FR 62446 (Oct. 7, 2002). DOE has
reviewed this final rule under the OMB and DOE guidelines and has
concluded that it is
[[Page 36916]]
consistent with applicable policies in those guidelines.
K. Review Under Executive Order 13211
Executive Order 13211, ``Actions Concerning Regulations That
Significantly Affect Energy Supply, Distribution, or Use,'' 66 FR 28355
(May 22, 2001), requires Federal agencies to prepare and submit to OMB,
a Statement of Energy Effects for any significant energy action. A
``significant energy action'' is defined as any action by an agency
that promulgated or is expected to lead to promulgation of a final
rule, and that (1) is a significant regulatory action under Executive
Order 12866, or any successor order; and (2) is likely to have a
significant adverse effect on the supply, distribution, or use of
energy; or (3) is designated by the Administrator of OIRA as a
significant energy action. For any significant energy action, the
agency must give a detailed statement of any adverse effects on energy
supply, distribution, or use if the regulation is implemented, and of
reasonable alternatives to the action and their expected benefits on
energy supply, distribution, and use.
This regulatory action is not a significant regulatory action under
Executive Order 12866. Moreover, it would not have a significant
adverse effect on the supply, distribution, or use of energy, nor has
it been designated as a significant energy action by the Administrator
of OIRA. Therefore, it is not a significant energy action, and,
accordingly, DOE has not prepared a Statement of Energy Effects.
L. Review Under Section 32 of the Federal Energy Administration Act of
1974
Under section 301 of the Department of Energy Organization Act
(Pub. L. 95-91; 42 U.S.C. 7101), DOE must comply with section 32 of the
Federal Energy Administration Act of 1974, as amended by the Federal
Energy Administration Authorization Act of 1977. (15 U.S.C. 788; FEAA)
Section 32 essentially provides in relevant part that, where a proposed
rule authorizes or requires use of commercial standards, the NOPR must
inform the public of the use and background of such standards. In
addition, section 32(c) requires DOE to consult with the Attorney
General and the Chairman of the Federal Trade Commission (FTC)
concerning the impact of the commercial or industry standards on
competition.
The modifications to the test procedure for dedicated-purpose pool
pumps adopted in this final rule incorporates testing methods contained
in certain sections of the following commercial standards:
(1) UL 1081, (``ANSI/UL 1081-2016''), ``Standard for Swimming Pool
Pumps, Filters, and Chlorinators,'' 7th Edition, ANSI approved October
21, 2016.
(2) Canadian Standards Association (CSA) C747-2009 (Reaffirmed
2014), ``Energy Efficiency Test Methods for Small Motors,'' CSA
reaffirmed 2014, section 1, ``Scope''; section 3, ``Definitions'';
section 5, ``General Test Requirements''; and section 6, ``Test
Method.''
(3) Institute of Electrical and Electronics Engineers (IEEE)
Standard 114-2010, ``Test Procedure for Single-Phase Induction
Motors,'' Approved September 30, 2010, section 3.2, ``Tests with
load''; section 4 ``Testing facilities''; section 5.2 ``Mechanical
measurements''; section 5.3 ``Temperature measurements''; and section 6
``Tests.''
(4) Institute of Electrical and Electronics Engineers (IEEE)
Standard 113-1985, ``IEEE Guide: Test Procedures for Direct-Current
Machines,'' 1985, section 3.1, ``Instrument Selection Factors'';
section 3.4 ``Power Measurement'': section 3.5 ``Power Sources'';
section 4.1.2 ``Ambient Air''; section 4.1.4 ``Direction of Rotation'';
section 5.4.1 ``Reference Conditions''; and section 5.4.3.2
``Dynomometer or Torquemeter Method.''
(5) NSF International Standard (NSF)/American National Standards
Institute (ANSI) 50-2015, (``NSF/ANSI 50-2015''), ``Equipment for
Swimming Pools, Spas, Hot Tubs and Other Recreational Water
Facilities,'' approved January 26, 2015, section C.3, ``self-priming
capability,'' of Annex C, ``Test methods for the evaluation of
centrifugal pumps.''
In addition, the rule expands the incorporation by reference of
Hydraulic Institute (HI) 40.6-2014, (``HI 40.6-2014'') ``Methods for
Rotodynamic Pump Efficiency Testing,'' (except for section 40.6.4.1,
``Vertically suspended pumps``; section 40.6.4.2, ``Submersible
pumps''; section 40.6.5.3, ``Test report''; section 40.6.5.5, ``Test
conditions''; section 40.6.5.5.2, ``Speed of rotation during testing'';
section 40.6.6.1, ``Translation of test results to rated speed of
rotation''; Appendix A, section A.7, ``Testing at temperatures
exceeding 30 [deg]C (86[emsp14][deg]F)''; and Appendix B, ``Reporting
of test results (normative)'';) copyright 2014. HI 40.6-2014 is already
IBR approved for Sec. 431.464, and appendix A to subpart Y of part
431. 10 CFR 431.463. As such, DOE is only modifying the existing
incorporation by reference to extend the applicability of certain
sections to the new appendices B and C to subpart Y that will contain
the DPPP test procedure.
Although the DPPP test procedure is not exclusively based on these
industry testing standards, some components of the test procedure will
adopt definitions, test parameters, measurement techniques, and
additional calculations from them without amendment. DOE has evaluated
these standards and is unable to conclude whether it fully complies
with the requirements of section 32(b) of the FEAA (i.e., whether it
was developed in a manner that fully provides for public participation,
comment, and review). DOE has consulted with both the Attorney General
and the Chairman of the FTC about the impact on competition of using
the methods contained in these standards and has received no comments
objecting to their use.
M. Congressional Notification
As required by 5 U.S.C. 801, DOE will report to Congress on the
promulgation of this rule before its effective date. The report will
state that it has been determined that the rule is not a ``major rule''
as defined by 5 U.S.C. 804(2).
N. Description of Materials Incorporated by Reference
In this final rule, DOE incorporates by reference six industry
standards related to pump nomenclature, definitions, and test
specifications, which DOE has referenced in its proposed definitions
and test procedure.
Specifically, the definitions in this final rule, as well as
relevant testing procedures to determine self-priming capability,
incorporate by reference the following sections of the following
standards:
(1) UL 1081, (``ANSI/UL 1081-2016''), ``Standard for Swimming Pool
Pumps, Filters, and Chlorinators,'' 7th Edition, ANSI approved October
21, 2016.
(2) Canadian Standards Association (CSA) C747-2009 (Reaffirmed
2014), ``Energy Efficiency Test Methods for Small Motors,'' CSA
reaffirmed 2014, section 1, ``Scope''; section 3, ``Definitions'';
section 5, ``General Test Requirements''; and section 6, ``Test
Method.''
(3) Institute of Electrical and Electronics Engineers (IEEE)
Standard 114-2010, ``Test Procedure for Single-Phase Induction
Motors,'' Approved September 30, 2010, section 3.2, ``Tests with
load''; section 4 ``Testing facilities''; section 5.2 ``Mechanical
measurements''; section 5.3 ``Temperature measurements''; and section 6
``Tests.''
[[Page 36917]]
(4) Institute of Electrical and Electronics Engineers (IEEE)
Standard 113-1985, ``IEEE Guide: Test Procedures for Direct-Current
Machines,'' 1985, section 3.1, ``Instrument Selection Factors'';
section 3.4 ``Power Measurement'': section 3.5 ``Power Sources'';
section 4.1.2 ``Ambient Air''; section 4.1.4 ``Direction of Rotation'';
section 5.4.1 ``Reference Conditions''; and section 5.4.3.2
``Dynomometer or Torquemeter Method.''
(5) NSF International Standard (NSF)/American National Standards
Institute (ANSI) 50-2015, (``NSF/ANSI 50-2015''), ``Equipment for
Swimming Pools, Spas, Hot Tubs and Other Recreational Water
Facilities,'' approved January 26, 2015, section C.3, ``self-priming
capability,'' of Annex C, ``Test methods for the evaluation of
centrifugal pumps.''
(6) Hydraulic Institute (HI) 40.6-2014, (``HI 40.6-2014-B'')
``Methods for Rotodynamic Pump Efficiency Testing,'' (except for
section 40.6.4.1, ``Vertically suspended pumps''; section 40.6.4.2,
``Submersible pumps''; section 40.6.5.3, ``Test report''; section
40.6.5.5, ``Test conditions''; section 40.6.5.5.2, ``Speed of rotation
during testing''; section 40.6.6.1, ``Translation of test results to
rated speed of rotation''; Appendix A, section A.7, ``Testing at
temperatures exceeding 30 [deg]C (86[emsp14][deg]F)''; and Appendix B,
``Reporting of test results (normative)'';) to establish procedures for
measuring relevant pump performance parameters.
DOE incorporates by reference UL 1081-2016 into 10 CFR 431.462 and
NSF/ANSI 50-2015 into 10 CFR 429.59, 10 CFR 429.134, 10 CFR 431.462,
and appendices B and C of subpart Y. UL 1081-2016 describes, among
other things, the safety-related performance and construction
requirements for rating dedicated-purpose pool pumps under the UL 1081
standard. Section C.3 of annex C of the NSF/ANSI 50-2015 standard
describes the test methods and criteria for establishing the self-
priming capability of dedicated-purpose pool pumps.
DOE incorporates by reference CSA C747-2009 (RA 2014) into
appendices B and C of part 431 to describe the standardized methods for
determining certain DPPP motor horsepower characteristics. CSA C747-
2009 (RA 2014) contains standardized methods for evaluating and
categorizing AC and DC electric motors that are internationally
recognized and are harmonized with IEEE 114-2010 and IEEE 113-1985.
DOE also incorporates by reference IEEE 114-2010 into appendices B
and C of part 431 to describe the standardized methods for determining
certain DPPP motor horsepower characteristics for dedicated-purpose
pool pumps with single-phase AC motors. IEEE 114-2010 contains
standardized methods for evaluating and categorizing single-phase
induction motors. These methods are consistent with those in CSA C742-
2009 (RA 2014).
DOE also incorporates by reference IEEE 113-1985 into appendices B
and C of part 431 to describe the standardized methods for determining
certain DPPP motor horsepower characteristics for dedicated-purpose
pool pumps with DC motors. IEEE 113-1985 contains standardized methods
for evaluating and categorizing DC motors. These methods are consistent
with those in CSA C742-2009 (RA 2014).
In addition, the test procedure adopted in this final rule
incorporates by reference the Hydraulic Institute (HI) 40.6-2014, (``HI
40.6-2014-B'') ``Methods for Rotodynamic Pump Efficiency Testing,''
(except for section 40.6.4.1, ``Vertically suspended pumps''; section
40.6.4.2, ``Submersible pumps''; section 40.6.5.3, ``Test report'';
section 40.6.5.5, ``Test conditions''; section 40.6.5.5.2, ``Speed of
rotation during testing''; section 40.6.6.1, ``Translation of test
results to rated speed of rotation''; Appendix A, section A.7,
``Testing at temperatures exceeding 30 [deg]C (86[emsp14][deg]F)''; and
Appendix B, ``Reporting of test results (normative)'';) to establish
procedures for measuring relevant pump performance parameters. HI 40.6-
2014-B, with certain exceptions, is already IBR approved for appendix A
to subpart Y of part 431. 10 CFR 431.463. DOE proposes to incorporate
by reference HI 40.6-2014-B, with certain additional exceptions, into
the new appendices B and C to subpart Y that would contain the DPPP
test procedure, as well as 10 CFR 429.134 to support DOE's enforcement
testing. HI 40.6-2014-B is an industry-accepted standard used to
specify methods of testing for determining the head, flow rate, pump
power input, driver power input, pump power output, and other relevant
parameters necessary to determine the WEF of applicable pumps, as well
as other voluntary metrics, adopted in this final rule (see sections
III.C and III.H).
Additionally, these standards can be obtained from the
organizations directly at the following addresses:
(1) UL, 333 Pfingsten Road, Northbrook, IL 60062, (847) 272-8800,
or by visiting https://ul.com.
(2) CSA, 5060 Spectrum Way, Suite 100, Mississauga, Ontario, L4W
5N6, Canada, (800) 463-6727, or by visiting www.csagroup.org.
(3) IEEE, 45 Hoes Lane, P.O. Box 1331, Piscataway, NJ 08855-1331,
(732) 981-0060, or by visiting https://www.ieee.org.
(4) NSF International, 789 N. Dixboro Road, Ann Arbor, MI 48105,
(743) 769-8010, or by visiting www.nsf.org.
(5) Hydraulic Institute, located at 6 Campus Drive, First Floor
North, Parsippany, NJ, 07054, (973) 267-9700, or by visiting
www.pumps.org.
V. Approval of the Office of the Secretary
The Secretary of Energy has approved publication of this final
rule.
List of Subjects
10 CFR Part 429
Administrative practice and procedure, Confidential business
information, Energy conservation, Imports, Incorporation by reference,
Intergovernmental relations, Small businesses.
10 CFR Part 431
Administrative practice and procedure, Confidential business
information, Energy conservation, Imports, Incorporation by reference,
Intergovernmental relations, Small businesses.
Issued in Washington, DC, on December 22, 2016.
Kathleen B. Hogan,
Deputy Assistant Secretary for Energy Efficiency, Energy Efficiency and
Renewable Energy.
For the reasons stated in the preamble, DOE amends parts 429 and
431 of chapter II, subchapter D of title 10, Code of Federal
Regulations as set forth below:
PART 429--CERTIFICATION, COMPLIANCE, AND ENFORCEMENT FOR CONSUMER
PRODUCTS AND COMMERCIAL AND INDUSTRIAL EQUIPMENT
0
1. The authority citation for part 429 continues to read as follows:
Authority: 42 U.S.C. 6291-6317; 28 U.S.C. 2461 note.
0
2. Section 429.4 is amended by:
0
a. Redesignating paragraph (d) as (e); and
0
b. Adding new paragraphs (d) and (f).
The additions read as follows:
Sec. 429.4 Materials incorporated by reference.
* * * * *
(d) HI. Hydraulic Institute, 6 Campus Drive, First Floor North,
Parsippany, NJ 07054-4406, 973-267-9700. www.Pumps.org.
[[Page 36918]]
(1) HI 40.6-2014, (``HI 40.6-2014-B''), ``Methods for Rotodynamic
Pump Efficiency Testing,'', (except for sections 40.6.4.1 ``Vertically
suspended pumps'', 40.6.4.2 ``Submersible pumps'',40.6.5.3 ``Test
report'', 40.6.5.5 ``Test conditions'', 40.6.5.5.2 ``Speed of rotation
during testing'', and 40.6.6.1 ``Translation of test results to rated
speed of rotation'', and Appendix A ``Testing arrangements
(normative)'': A.7 ``Testing at temperatures exceeding 30 [deg]C
(86[emsp14][deg]F)'', and Appendix B ``Reporting of test results
(normative)''), copyright 2014, IBR approved for Sec. 429.134.
(2) [Reserved]
* * * * *
(f) NSF. NSF International. 789 N. Dixboro Road, Ann Arbor, MI
48105, (743) 769-8010. www.nsf.org.
(1) NSF/ANSI 50-2015, ``Equipment for Swimming Pools, Spas, Hot
Tubs and Other Recreational Water Facilities,'' Annex C--``Test methods
for the evaluation of centrifugal pumps,'' Section C.3, ``self-priming
capability,'' ANSI approved January 26, 2015, IBR approved for
Sec. Sec. 429.59 and 429.134.
(2) [Reserved]
0
3. Section 429.59 is amended by:
0
a. Revising paragraph (a)(1)(ii);
0
b. Adding paragraphs (a)(2), (b)(2)(iv) and (v), and (b)(3)(iv); and
0
c. Revising paragraph (c).
The revisions and additions read as follows:
Sec. 429.59 Pumps.
(a) * * *
(1) * * *
(ii) Any representation of weighted energy factor of a basic model
must be less than or equal to the lower of:
(A) The mean of the sample, where:
[GRAPHIC] [TIFF OMITTED] TR07AU17.008
And x is the sample mean; n is the number of samples; and
xi is the maximum of the ith sample; or,
(B) The lower 95 percent confidence limit (LCL) of the true mean
divided by 0.95, where:
[GRAPHIC] [TIFF OMITTED] TR07AU17.009
And x is the sample mean; s is the sample standard deviation; n is
the number of samples; and t0.95 is the t statistic for a 95
percent one-tailed confidence interval with n-1 degrees of freedom
(from appendix A of this subpart).
(2) Other representations--(i) Rated hydraulic horsepower. The
representative value of rated hydraulic horsepower of a basic model of
dedicated-purpose pool pump must be the mean of the rated hydraulic
horsepower for each tested unit.
(ii) Dedicated-purpose pool pump motor total horsepower. The
representative value of dedicated-purpose pool pump motor total
horsepower of a basic model of dedicated-purpose pool pump must be the
mean of the dedicated-purpose pool pump motor total horsepower for each
tested unit.
(iii) True power factor (PFi). The representative value
of true power factor at each load point i of a basic model of
dedicated-purpose pool pump must be the mean of the true power factors
at that load point for each tested unit of dedicated-purpose pool pump.
(b) * * *
(2) * * *
(iv) For a dedicated-purpose pool pump subject to the test methods
prescribed in Sec. 431.464(b) of this chapter: weighted energy factor
(WEF) in kilogallons per kilowatt-hour (kgal/kWh); rated hydraulic
horsepower in horsepower (hp); the speed configuration for which the
pump is being rated (i.e., single-speed, two-speed, multi-speed, or
variable-speed); true power factor at all applicable test procedure
load points i (dimensionless), as specified in Table 1 of appendix B or
C to subpart Y of part 431 of this chapter, as applicable; dedicated-
purpose pool pump nominal motor horsepower in horsepower (hp);
dedicated-purpose pool pump motor total horsepower in horsepower (hp);
dedicated-purpose pool pump service factor (dimensionless); for self-
priming pool filter pumps, non-self-priming pool filter pumps, and
waterfall pumps: The maximum head (in feet) which is based on the mean
of the units in the tested sample; a statement regarding whether freeze
protection is shipped enabled or disabled; for dedicated-purpose pool
pumps distributed in commerce with freeze protection controls enabled:
The default dry-bulb air temperature setting (in [deg]F), default run
time setting (in minutes), and default motor speed (in rpm); for self-
priming pool filter pumps a statement regarding whether the pump is
certified with NSF/ANSI 50-2015 (incorporated by reference, see Sec.
429.4) as self-priming; and, for self-priming pool filter pumps that
are not certified with NSF/ANSI 50-2015 as self-priming: The vertical
lift (in feet) and true priming time (in minutes) for the DPPP model.
(v) For integral cartridge-filter and sand-filter pool pumps, the
maximum run-time (in hours) of the pool pump control with which the
integral cartridge-filter or sand-filter pump is distributed in
commerce.
(3) * * *
(iv) For a dedicated-purpose pool pump subject to the test methods
prescribed in Sec. 431.464(b) of this chapter: Calculated driver power
input and flow rate at each load point i (Pi and
Qi), in horsepower (hp) and gallons per minute (gpm),
respectively.
* * * * *
(c) Individual model numbers. (1) For a pump subject to the test
methods prescribed in appendix A to subpart Y of part 431 of this
chapter, each individual model number required to be reported pursuant
to Sec. 429.12(b)(6) must consist of the following:
----------------------------------------------------------------------------------------------------------------
Individual model number(s)
Equipment configuration (as Basic model -----------------------------------------------------------------
distributed in commerce) number 1 2 3
----------------------------------------------------------------------------------------------------------------
Bare pump.................... Number unique Bare pump........... N/A................. N/A.
to the basic
model.
Bare pump with driver........ Number unique Bare pump........... Driver.............. N/A.
to the basic
model.
Bare pump with driver and Number unique Bare pump........... Driver.............. Controls.
controls. to the basic
model.
----------------------------------------------------------------------------------------------------------------
(2) Or must otherwise provide sufficient information to identify
the specific driver model and/or controls model(s) with which a bare
pump is distributed.
0
4. Section 429.110 is amended by revising paragraphs (e)(1) and (5) to
read as follows:
[[Page 36919]]
Sec. 429.110 Enforcement testing.
* * * * *
(e) * * *
(1) For products with applicable energy conservation standard(s) in
Sec. 430.32 of this chapter, and commercial prerinse spray valves,
illuminated exit signs, traffic signal modules and pedestrian modules,
commercial clothes washers, dedicated-purpose pool pumps, and metal
halide lamp ballasts, DOE will use a sample size of not more than 21
units and follow the sampling plans in appendix A of this subpart
(Sampling for Enforcement Testing of Covered Consumer Products and
Certain High-Volume Commercial Equipment).
* * * * *
(5) For pumps subject to the standards specified in Sec.
431.465(a) of this chapter, DOE will use an initial sample size of not
more than four units and will determine compliance based on the
arithmetic mean of the sample.
* * * * *
0
5. Section 429.134 is amended by revising paragraph (i) to read as
follows:
Sec. 429.134 Product-specific enforcement provisions.
* * * * *
(i) Pumps--(1) General purpose pumps. (i) The volume rate of flow
(flow rate) at BEP and nominal speed of rotation of each tested unit of
the basic model will be measured pursuant to the test requirements of
Sec. 431.464 of this chapter, where the value of volume rate of flow
(flow rate) at BEP and nominal speed of rotation certified by the
manufacturer will be treated as the expected BEP flow rate. The results
of the measurement(s) will be compared to the value of volume rate of
flow (flow rate) at BEP and nominal speed of rotation certified by the
manufacturer. The certified volume rate of flow (flow rate) at BEP and
nominal speed of rotation will be considered valid only if the
measurement(s) (either the measured volume rate of flow (flow rate) at
BEP and nominal speed of rotation for a single unit sample or the
average of the measured flow rates for a multiple unit sample) is
within five percent of the certified volume rate of flow (flow rate) at
BEP and nominal speed of rotation.
(A) If the representative value of volume rate of flow (flow rate)
at BEP and nominal speed of rotation is found to be valid, the measured
volume rate of flow (flow rate) at BEP and nominal speed of rotation
will be used in subsequent calculations of constant load pump energy
rating (PERCL) and constant load pump energy index
(PEICL) or variable load pump energy rating
(PERVL) and variable load pump energy index
(PEIVL) for that basic model.
(B) If the representative value of volume rate of flow (flow rate)
at BEP and nominal speed of rotation is found to be invalid, the mean
of all the measured volume rate of flow (flow rate) at BEP and nominal
speed of rotation values determined from the tested unit(s) will serve
as the new expected BEP flow rate and the unit(s) will be retested
until such time as the measured rate of flow (flow rate) at BEP and
nominal speed of rotation is within 5 percent of the expected BEP flow
rate.
(ii) DOE will test each pump unit according to the test method
specified by the manufacturer in the certification report submitted
pursuant to Sec. 429.59(b).
(2) Dedicated-purpose pool pumps. (i) The rated hydraulic
horsepower of each tested unit of the basic model of dedicated-purpose
pool pump will be measured pursuant to the test requirements of Sec.
431.464(b) of this chapter and the result of the measurement(s) will be
compared to the value of rated hydraulic horsepower certified by the
manufacturer. The certified rated hydraulic horsepower will be
considered valid only if the measurement(s) (either the measured rated
hydraulic horsepower for a single unit sample or the average of the
measured rated hydraulic horsepower values for a multiple unit sample)
is within 5 percent of the certified rated hydraulic horsepower.
(A) If the representative value of rated hydraulic horsepower is
found to be valid, the value of rated hydraulic horsepower certified by
the manufacturer will be used to determine the standard level for that
basic model.
(B) If the representative value of rated hydraulic horsepower is
found to be invalid, the mean of all the measured rated hydraulic
horsepower values determined from the tested unit(s) will be used to
determine the standard level for that basic model.
(ii) To verify the self-priming capability of non-self-priming pool
filter pumps and of self-priming pool filter pumps that are not
certified with NSF/ANSI 50-2015 (incorporated by reference, see Sec.
429.4) as self-priming, the vertical lift and true priming time of each
tested unit of the basic model of self-priming or non-self-priming pool
filter pump will be measured pursuant to the test requirements of Sec.
431.464(b) of this chapter.
(A) For self-priming pool filter pumps that are not certified with
NSF/ANSI 50-2015 as self-priming, at a vertical lift of 5.0 feet, the
result of the true priming time measurement(s) will be compared to the
value of true priming time certified by the manufacturer. The certified
value of true priming time will be considered valid only if the
measurement(s) (either the measured true priming time for a single unit
sample or the average of true priming time values for a multiple unit
sample) is within 5 percent of the certified value of true priming
time.
(1) If the representative value of true priming time is found to be
valid, the value of true priming time certified by the manufacturer
will be used to determine the appropriate equipment class and standard
level for that basic model.
(2) If the representative value of true priming time is found to be
invalid, the mean of the values of true priming time determined from
the tested unit(s) will be used to determine the appropriate equipment
class and standard level for that basic model.
(B) For non-self-priming pool filter pumps, at a vertical lift of
5.0 feet, the result of the true priming time measurement(s) (either
the measured true priming time for a single unit sample or the average
of true priming time values, for a multiple unit sample) will be
compared to the value of true priming time referenced in the definition
of non-self-priming pool filter pump at Sec. 431.462 (10.0 minutes).
(1) If the measurement(s) of true priming time are greater than 95
percent of the value of true priming time referenced in the definition
of non-self-priming pool filter pump at Sec. 431.462 with a vertical
lift of 5.0 feet, the DPPP model will be considered a non-self-priming
pool filter pump for the purposes of determining the appropriate
equipment class and standard level for that basic model.
(2) If the conditions specified in paragraph (i)(2)(ii)(B)(1) of
this section are not satisfied, then the DPPP model will be considered
a self-priming pool filter pump for the purposes of determining the
appropriate equipment class and standard level for that basic model.
(iii) To verify the maximum head of self-priming pool filter pump,
non-self-priming pool filter pumps, and waterfall pumps, the maximum
head of each tested unit of the basic model of self-priming pool filter
pump, non-self-priming pool filter pump, or waterfall pump will be
measured pursuant to the test requirements of Sec. 431.464(b) of this
chapter and the result of the measurement(s) will be compared to the
value of maximum head certified by the manufacturer. The certified
value of maximum head will be considered valid
[[Page 36920]]
only if the measurement(s) (either the measured maximum head for a
single unit sample or the average of the maximum head values for a
multiple unit sample) is within 5 percent of the certified values of
maximum head.
(A) If the representative value of maximum head is found to be
valid, the value of maximum head certified by the manufacturer will be
used to determine the appropriate equipment class and standard level
for that basic model.
(B) If the representative value of maximum head is found to be
invalid, the measured value(s) of maximum head determined from the
tested unit(s) will be used to determine the appropriate equipment
class and standard level for that basic model.
(iv) To verify that a DPPP model complies with the applicable
freeze protection control design requirements, the initiation
temperature, run-time, and speed of rotation of the default control
configuration of each tested unit of the basic model of dedicated-
purpose pool pump will be evaluated according to the procedure
specified in paragraph (i)(2)(iv)(A) of this section:
(A)(1) Set up and configure the dedicated-purpose pool pump under
test according to the manufacturer instructions, including any
necessary initial priming, in a test apparatus as described in appendix
A of HI 40.6-2014-B (incorporated by reference, see Sec. 429.4),
except that the ambient temperature registered by the freeze protection
ambient temperature sensor will be able to be measured and controlled
by, for example, exposing the freeze protection temperature sensor to a
specific temperature by submerging the sensor in a water bath of known
temperature, by adjusting the actual ambient air temperature of the
test chamber and measuring the temperature at the freeze protection
ambient temperature sensor location, or by other means that allows the
ambient temperature registered by the freeze protection temperature
sensor to be reliably simulated, varied, and measured. Do not adjust
the default freeze protection control settings or enable the freeze
protection control if it is shipped disabled.
(2) Activate power to the pump with the flow rate set to zero
(i.e., the pump is energized but not circulating water). Set the
ambient temperature to 42.0 0.5[emsp14][deg]F and allow
the temperature to stabilize, where stability is determined in
accordance with section 40.6.3.2.2 of HI 40.6-2014-B. After 5 minutes,
decrease the temperature measured by the freeze protection temperature
sensor by 1.0 0.5[emsp14][deg]F and allow the temperature
to stabilize. After each reduction in ambient temperature and
subsequent stabilization, record the DPPP rotating speed, if any, and
freeze protection ambient temperature reading, where the ``freeze
protection ambient temperature reading'' is representative of the
temperature measured by the freeze protection ambient temperature
sensor, which may be recorded by a variety of means depending on how
the temperature is being simulated and controlled. If no flow is
initiated, record zero rpm or no flow. Continue decreasing the
temperature measured by the freeze protection temperature sensor by 1.0
0.5[emsp14][deg]F after 5.0 minutes of stable operation at
the previous temperature reading until the pump freeze protection
initiates water circulation or until the ambient temperature of 38.0
0.5[emsp14][deg]F has been evaluated (i.e., the end of the
5.0 minute interval of 38.0[emsp14][deg]F), whichever occurs first.
(3) If and when the DPPP freeze protection controls initiate water
circulation, increase the ambient temperature reading registered by the
freeze protection temperature sensor to a temperature of 42.0 0.5[emsp14][deg]F and maintain that temperature for 60.0
minutes. Do not modify or interfere with the operation of the DPPP
freeze protection operating cycle. After 60.0 minutes, record the
freeze protection ambient temperature and rotating speed, if any, of
the dedicated-purpose pool pump under test.
(B) If the dedicated-purpose pool pump initiates water circulation
at a temperature greater than 40.0[emsp14][deg]F; if the dedicated-
purpose pool pump was still circulating water after 60.0 minutes of
operation at 42.0 0.5[emsp14][deg]F; or if rotating speed
measured at any point during the DPPP freeze protection control test in
paragraph (i)(2)(iii)(A) of this section was greater than one-half of
the maximum rotating speed of the DPPP model certified by the
manufacturer, that DPPP model is deemed to not comply with the design
requirement for freeze protection controls.
(C) If none of the conditions specified in paragraph (i)(2)(iv)(B)
of this section are met, including if the DPPP freeze protection
control does not initiate water circulation at all during the test, the
dedicated-purpose pool pump under test is deemed compliant with the
design requirement for freeze protection controls.
* * * * *
PART 431--ENERGY EFFICIENCY PROGRAM FOR CERTAIN COMMERCIAL AND
INDUSTRIAL EQUIPMENT
0
6. The authority citation for part 431 continues to read as follows:
Authority: 42 U.S.C. 6291-6317; 28 U.S.C. 2461 note.
0
7. Section 431.462 is amended by:
0
a. Revising the introductory text; and
0
b. Revising the definition of ``Basic model;''
0
c. Adding, in alphabetical order, definitions for ``Basket strainer,''
``Dedicated-purpose pool pump,'' ``Dedicated-purpose pool pump motor
total horsepower,'' ``Dedicated-purpose pool pump service factor,''
``Designed and marketed,'' ``Freeze protection control,'' ``Integral,''
``Integral cartridge-filter pool pump,'' ``Integral sand-filter pool
pump,'' ``Multi-speed dedicated-purpose pool pump,'' ``Non-self-priming
pool filter pump,'' ``Pool filter pump,'' ``Pressure cleaner booster
pump,'' ``Removable cartridge filter,'' ``Rigid electric spa pump,''
``Sand filter,'' and ``Self-priming pool filter pump;''
0
d. Revising the definition of ``Self-priming pump;'' and
0
e. Adding, in alphabetical order, definitions for ``Single-speed
dedicated-purpose pool pump,'' ``Storable electric spa pump,''
``Submersible pump,'' ``Two-speed dedicated-purpose pool pump,''
``Variable-speed dedicated-purpose pool pump,'' ``Variable speed
drive,'' and ``Waterfall pump.''
The additions and revisions read as follows:
Sec. 431.462 Definitions.
The following definitions are applicable to this subpart, including
appendices A and B. In cases where there is a conflict, the language of
the definitions adopted in this section takes precedence over any
descriptions or definitions found in the 2014 version of ANSI/HI
Standard 1.1-1.2, ``Rotodynamic (Centrifugal) Pumps For Nomenclature
And Definitions'' (ANSI/HI 1.1-1.2-2014; incorporated by reference, see
Sec. 431.463), or the 2014 version of ANSI/HI Standard 2.1-2.2,
``Rotodynamic (Vertical) Pumps For Nomenclature And Definitions''
(ANSI/HI 2.1-2.2-2014; incorporated by reference, see Sec. 431.463).
In cases where definitions reference design intent, DOE will consider
marketing materials, labels and certifications, and equipment design to
determine design intent.
* * * * *
Basic model means all units of a given class of pump manufactured
by one manufacturer, having the same primary
[[Page 36921]]
energy source, and having essentially identical electrical, physical,
and functional (or hydraulic) characteristics that affect energy
consumption, energy efficiency, water consumption, or water efficiency;
and, in addition, for pumps that are subject to the standards specified
in Sec. 431.465(b), the following provisions also apply:
(1) All variations in numbers of stages of bare RSV and ST pumps
must be considered a single basic model;
(2) Pump models for which the bare pump differs in impeller
diameter, or impeller trim, may be considered a single basic model; and
(3) Pump models for which the bare pump differs in number of stages
or impeller diameter and which are sold with motors (or motors and
controls) of varying horsepower may only be considered a single basic
model if:
(i) For ESCC, ESFM, IL, and RSV pumps, each motor offered in the
basic model has a nominal full load motor efficiency rated at the
Federal minimum (see the current table for NEMA Design B motors at
Sec. 431.25) or the same number of bands above the Federal minimum for
each respective motor horsepower (see Table 3 of appendix A to subpart
Y of this part); or
(ii) For ST pumps, each motor offered in the basic model has a full
load motor efficiency at the default nominal full load submersible
motor efficiency shown in Table 2 of appendix A to subpart Y of this
part or the same number of bands above the default nominal full load
submersible motor efficiency for each respective motor horsepower (see
Table 3 of appendix A to subpart Y of this part).
Basket strainer means a perforated or otherwise porous receptacle,
mounted within a housing on the suction side of a pump, that prevents
solid debris from entering a pump. The basket strainer receptacle is
capable of passing spherical solids of 1 mm in diameter, and can be
removed by hand or using only simple tools (e.g., screwdriver, pliers,
open-ended wrench).
* * * * *
Dedicated-purpose pool pump comprises self-priming pool filter
pumps, non-self-priming pool filter pumps, waterfall pumps, pressure
cleaner booster pumps, integral sand-filter pool pumps, integral-
cartridge filter pool pumps, storable electric spa pumps, and rigid
electric spa pumps.
Dedicated-purpose pool pump motor total horsepower means the
product of the dedicated-purpose pool pump nominal motor horsepower and
the dedicated-purpose pool pump service factor of a motor used on a
dedicated-purpose pool pump based on the maximum continuous duty motor
power output rating allowable for the motor's nameplate ambient rating
and insulation class. (Dedicated-purpose pool pump motor total
horsepower is also referred to in the industry as service factor
horsepower or motor capacity.)
Dedicated-purpose pool pump service factor means a multiplier
applied to the rated horsepower of a pump motor to indicate the percent
above nameplate horsepower at which the motor can operate continuously
without exceeding its allowable insulation class temperature limit.
Designed and marketed means that the equipment is designed to
fulfill the indicated application and, when distributed in commerce, is
designated and marketed for that application, with the designation on
the packaging and any publicly available documents (e.g., product
literature, catalogs, and packaging labels).
* * * * *
Freeze protection control means a pool pump control that, at a
certain ambient temperature, turns on the dedicated-purpose pool pump
to circulate water for a period of time to prevent the pool and water
in plumbing from freezing.
* * * * *
Integral means a part of the device that cannot be removed without
compromising the device's function or destroying the physical integrity
of the unit.
Integral cartridge-filter pool pump means a pump that requires a
removable cartridge filter, installed on the suction side of the pump,
for operation; and the cartridge filter cannot be bypassed.
Integral sand-filter pool pump means a pump distributed in commerce
with a sand filter that cannot be bypassed.
* * * * *
Multi-speed dedicated-purpose pool pump means a dedicated-purpose
pool pump that is capable of operating at more than two discrete, pre-
determined operating speeds separated by speed increments greater than
100 rpm, where the lowest speed is less than or equal to half of the
maximum operating speed and greater than zero, and must be distributed
in commerce with an on-board pool pump control (i.e., variable speed
drive and user interface or programmable switch) that changes the speed
in response to pre-programmed user preferences and allows the user to
select the duration of each speed and/or the on/off times.
* * * * *
Non-self-priming pool filter pump means a pool filter pump that is
not certified under NSF/ANSI 50-2015 (incorporated by reference, see
Sec. 431.463) to be self-priming and is not capable of re-priming to a
vertical lift of at least 5.0 feet with a true priming time less than
or equal to 10.0 minutes, when tested in accordance with section F of
appendix B or C of this subpart, and is not a waterfall pump.
Pool filter pump means an end suction pump that:
(1) Either:
(i) Includes an integrated basket strainer; or
(ii) Does not include an integrated basket strainer, but requires a
basket strainer for operation, as stated in manufacturer literature
provided with the pump; and
(2) May be distributed in commerce connected to, or packaged with,
a sand filter, removable cartridge filter, or other filtration
accessory, so long as the filtration accessory are connected with
consumer-removable connections that allow the filtration accessory to
be bypassed.
* * * * *
Pressure cleaner booster pump means an end suction, dry rotor pump
designed and marketed for pressure-side pool cleaner applications, and
which may be UL listed under ANSI/UL 1081-2016 (incorporated by
reference, see Sec. 431.463).
* * * * *
Removable cartridge filter means a filter component with fixed
dimensions that captures and removes suspended particles from water
flowing through the unit. The removable cartridge filter is not capable
of passing spherical solids of 1 mm in diameter or greater, and can be
removed from the filter housing by hand or using only simple tools
(e.g., screwdrivers, pliers, open-ended wrench).
Rigid electric spa pump means an end suction pump that does not
contain an integrated basket strainer or require a basket strainer for
operation as stated in manufacturer literature provided with the pump
and that meets the following three criteria:
(1) Is assembled with four through bolts that hold the motor rear
endplate, rear bearing, rotor, front bearing, front endplate, and the
bare pump together as an integral unit;
(2) Is constructed with buttress threads at the inlet and discharge
of the bare pump; and
(3) Uses a casing or volute and connections constructed of a non-
metallic material.
* * * * *
Sand filter means a device designed to filter water through sand or
an alternate sand-type media.
[[Page 36922]]
Self-priming pool filter pump means a pool filter pump that is
certified under NSF/ANSI 50-2015 (incorporated by reference, see Sec.
431.463) to be self-priming or is capable of re-priming to a vertical
lift of at least 5.0 feet with a true priming time less than or equal
to 10.0 minutes, when tested in accordance with section F of appendix B
or C of this subpart, and is not a waterfall pump.
Self-priming pump means a pump that either is a self-priming pool
filter pump or a pump that:
(1) Is designed to lift liquid that originates below the centerline
of the pump inlet;
(2) Contains at least one internal recirculation passage; and
(3) Requires a manual filling of the pump casing prior to initial
start-up, but is able to re-prime after the initial start-up without
the use of external vacuum sources, manual filling, or a foot valve.
* * * * *
Single-speed dedicated-purpose pool pump means a dedicated-purpose
pool pump that is capable of operating at only one speed.
Storable electric spa pump means a pump that is distributed in
commerce with one or more of the following:
(1) An integral heater; and
(2) An integral air pump.
Submersible pump means a pump that is designed to be operated with
the motor and bare pump fully submerged in the pumped liquid.
* * * * *
Two-speed dedicated-purpose pool pump means a dedicated-purpose
pool pump that is capable of operating at only two different pre-
determined operating speeds, where the low operating speed is less than
or equal to half of the maximum operating speed and greater than zero,
and must be distributed in commerce either:
(1) With a pool pump control (e.g., variable speed drive and user
interface or switch) that is capable of changing the speed in response
to user preferences; or
(2) Without a pool pump control that has the capability to change
speed in response to user preferences, but is unable to operate without
the presence of such a pool pump control.
Variable-speed dedicated-purpose pool pump means a dedicated-
purpose pool pump that is capable of operating at a variety of user-
determined speeds, where all the speeds are separated by at most 100
rpm increments over the operating range and the lowest operating speed
is less than or equal to one-third of the maximum operating speed and
greater than zero. Such a pump must include a variable speed drive and
be distributed in commerce either:
(1) With a user interface that changes the speed in response to
pre-programmed user preferences and allows the user to select the
duration of each speed and/or the on/off times; or
(2) Without a user interface that changes the speed in response to
pre-programmed user preferences and allows the user to select the
duration of each speed and/or the on/off times, but is unable to
operate without the presence of a user interface.
Variable speed drive means equipment capable of varying the speed
of the motor.
Waterfall pump means a pool filter pump with a certified maximum
head less than or equal to 30.0 feet, and a maximum speed less than or
equal to 1,800 rpm.
0
8. Section 431.463 is amended by:
0
a. Revising paragraph (a);
0
b. Redesignating paragraphs (b) through (d) and (e) as paragraphs (c)
through (f) and (h), respectively;
0
c. Adding new paragraph (b);
0
d. In newly redesignated paragraph (d), adding paragraph (d)(4);
0
e. Adding new paragraphs (e) and (g); and
0
f. In newly redesignated paragraph (h), adding paragraph (h)(2).
The revisions and additions read as follows:
Sec. 431.463 Materials incorporated by reference.
(a) General. DOE incorporates by reference the following standards
into subpart Y of this part. The material listed has been approved for
incorporation by reference by the Director of the Federal Register in
accordance with 5 U.S.C. 552(a) and 1 CFR part 51. Any subsequent
amendment to a standard by the standard-setting organization will not
affect the DOE test procedures unless and until amended by DOE.
Material is incorporated as it exists on the date of the approval, and
notification of any change in the material will be published in the
Federal Register. All approved material can be obtained from the
sources listed in this section and is available for inspection at the
U.S. Department of Energy, Office of Energy Efficiency and Renewable
Energy, Building Technologies Program, Sixth Floor, 950 L'Enfant Plaza
SW., Washington, DC 20024, (202) 586-2945, or go to: https://www1.eere.energy.gov/buildings/appliance_standards. It is also
available for inspection at the National Archives and Records
Administration (NARA). For information on the availability of this
material at NARA, call 202-741-6030, or go to: www.archives.gov/federal_register/code_of_federal_regulations/ibr_locations.html.
(b) CSA. Canadian Standards Association, 5060 Spectrum Way, Suite
100, Mississauga, Ontario, L4W 5N6, Canada, (800) 463-6727.
www.csagroup.org.
(1) CSA C747-2009 (Reaffirmed 2014), (``CSA C747-2009 (RA 2014)''),
``Energy efficiency test methods for small motors,'' CSA reaffirmed
2014, IBR approved for appendices B and C to this subpart, as follows:
(i) Section 1, ``Scope'';
(ii) Section 3, ``Definitions'';
(iii) Section 5, ``General Test Requirements''; and
(iv) Section 6, ``Test Method.''
(2) [Reserved]
* * * * *
(d) * * *
(4) HI 40.6-2014, (``HI 40.6-2014-B''), ``Methods for Rotodynamic
Pump Efficiency Testing'' (except sections 40.6.4.1 ``Vertically
suspended pumps'', 40.6.4.2 ``Submersible pumps'', 40.6.5.3 ``Test
report'', 40.6.5.5 ``Test conditions'', 40.6.5.5.2 ``Speed of rotation
during test'', and 40.6.6.1 ``Translation of test results to rated
speed of rotation'', Appendix A ``Test arrangements (normative)'': A.7
``Testing at temperatures exceeding 30 [deg]C (86[emsp14][deg]F)'', and
Appendix B, ``Reporting of test results (normative)''), copyright 2014,
IBR approved for appendices B and C to this subpart.
(e) IEEE. Institute of Electrical and Electronics Engineers, Inc.,
45 Hoes Lane, P.O. Box 1331, Piscataway, NJ 08855-1331, (732) 981-0060.
https://www.ieee.org.
(1) IEEE Std 113-1985, (``IEEE 113-1985''), ``IEEE Guide: Test
Procedures for Direct-Current Machines,'' copyright 1985, IBR approved
for appendices B and C to this subpart, as follows:
(i) Section 3, Electrical Measurements and Power Sources for all
Test Procedures:
(A) Section 3.1, ``Instrument Selection Factors'';
(B) Section 3.4 ``Power Measurement''; and
(C) Section 3.5 ``Power Sources'';
(ii) Section 4, Preliminary Tests:
(A) Section 4.1, Reference Conditions, Section 4.1.2, ``Ambient
Air''; and
(B) Section 4.1, Reference Conditions, Section 4.1.4 ``Direction of
Rotation''; and
(iii) Section 5, Performance Determination:
(A) Section 5.4, Efficiency, Section 5.4.1, ``Reference
Conditions''; and
(B) Section 5.4.3, Direct Measurements of Input and Output,
[[Page 36923]]
Section 5.4.3.2 ``Dynomometer or Torquemeter Method.''
(2) IEEE Std 114-2010, (``IEEE 114-2010''), ``IEEE Standard Test
Procedure for Single-Phase Induction Motors,'' approved September 30,
2010, IBR approved for appendices B and C to this subpart, as follows:
(i) Section 3, ``General tests'', Section 3.2, ``Tests with load'';
(ii) Section 4 ``Testing facilities''; and
(iii) Section 5, ``Measurements'':
(A) Section 5.2 ``Mechanical measurements'';
(B) Section 5.3 ``Temperature measurements''; and
(iv) Section 6 ``Tests.''
* * * * *
(g) NSF. NSF International. 789 N. Dixboro Road, Ann Arbor, MI
48105, (743) 769-8010. www.nsf.org.
(1) NSF/ANSI 50-2015, ``Equipment for Swimming Pools, Spas, Hot
Tubs and Other Recreational Water Facilities,'' Annex C, ``(normative
Test methods for the evaluation of centrifugal pumps,'' Section C.3,
``Self-priming capability,'' ANSI approved January 26, 2015, IBR
approved for Sec. 431.462 and appendices B and C to this subpart.
(2) [Reserved]
(h) * * *
(2) UL 1081, (``ANSI/UL 1081-2016''), ``Standard for Swimming Pool
Pumps, Filters, and Chlorinators,'' 7th Edition, ANSI approved October
21, 2016, IBR approved for Sec. 431.462.
0
9. Section 431.464 is revised to read as follows:
Sec. 431.464 Test procedure for the measurement of energy efficiency,
energy consumption, and other performance factors of pumps.
(a) General pumps--(1) Scope. This paragraph (a) provides the test
procedures for determining the constant and variable load pump energy
index for:
(i) The following categories of clean water pumps:
(A) End suction close-coupled (ESCC);
(B) End suction frame mounted/own bearings (ESFM);
(C) In-line (IL);
(D) Radially split, multi-stage, vertical, in-line casing diffuser
(RSV); and
(E) Submersible turbine (ST) pumps.
(ii) With the following characteristics:
(A) Flow rate of 25 gpm or greater at BEP and full impeller
diameter;
(B) Maximum head of 459 feet at BEP and full impeller diameter and
the number of stages required for testing (see section 1.2.2 of
appendix A of this subpart);
(C) Design temperature range from 14 to 248 [deg]F;
(D) Designed to operate with either:
(1) A 2- or 4-pole induction motor; or
(2) A non-induction motor with a speed of rotation operating range
that includes speeds of rotation between 2,880 and 4,320 revolutions
per minute (rpm) and/or 1,440 and 2,160 rpm, and in either case, the
driver and impeller must rotate at the same speed;
(E) For ST pumps, a 6-inch or smaller bowl diameter; and
(F) For ESCC and ESFM pumps, a specific speed less than or equal to
5,000 when calculated using U.S. customary units.
(iii) Except for the following pumps:
(A) Fire pumps;
(B) Self-priming pumps;
(C) Prime-assist pumps;
(D) Magnet driven pumps;
(E) Pumps designed to be used in a nuclear facility subject to 10
CFR part 50, ``Domestic Licensing of Production and Utilization
Facilities''; and
(F) Pumps meeting the design and construction requirements set
forth in Military Specifications: MIL-P-17639F, ``Pumps, Centrifugal,
Miscellaneous Service, Naval Shipboard Use'' (as amended); MIL-P-
17881D, ``Pumps, Centrifugal, Boiler Feed, (Multi-Stage)'' (as
amended); MIL-P-17840C, ``Pumps, Centrifugal, Close-Coupled, Navy
Standard (For Surface Ship Application)'' (as amended); MIL-P-18682D,
``Pump, Centrifugal, Main Condenser Circulating, Naval Shipboard'' (as
amended); and MIL-P-18472G, ``Pumps, Centrifugal, Condensate, Feed
Booster, Waste Heat Boiler, And Distilling Plant'' (as amended).
Military specifications and standards are available for review at
https://everyspec.com/MIL-SPECS.
(2) Testing and calculations. Determine the applicable constant
load pump energy index (PEICL) or variable load pump energy
index (PEIVL) using the test procedure set forth in appendix
A of this subpart.
(b) Dedicated-purpose pool pumps--(1) Scope. This paragraph (b)
provides the test procedures for determining the weighted energy factor
(WEF), rated hydraulic horsepower, dedicated-purpose pool pump nominal
motor horsepower, dedicated-purpose pool pump motor total horsepower,
dedicated-purpose pool pump service factor, and other pump performance
parameters for:
(i) The following varieties of dedicated-purpose pool pumps:
(A) Self-priming pool filter pumps;
(B) Non-self-priming pool filter pumps;
(C) Waterfall pumps; and
(D) Pressure cleaner booster pumps;
(ii) Served by single-phase or polyphase input power;
(iii) Except for:
(A) Submersible pumps; and
(B) Self-priming and non-self-priming pool filter pumps with
hydraulic output power greater than or equal to 2.5 horsepower.
(2) Testing and calculations. Determine the weighted energy factor
(WEF) using the test procedure set forth in appendix B or appendix C of
this subpart, as applicable.
0
10. Section 431.466 is revised to read as follows:
Sec. 431.466 Pumps labeling requirements.
(a) General pumps. For the pumps described in Sec. 431.464(a), the
following requirements apply to units manufactured on the same date
that compliance is required with any applicable standards prescribed in
Sec. 431.465.
(1) Pump nameplate--(i) Required information. The permanent
nameplate must be marked clearly with the following information:
(A) For bare pumps and pumps sold with electric motors but not
continuous or non-continuous controls, the rated pump energy index--
constant load (PEICL), and for pumps sold with motors and
continuous or non-continuous controls, the rated pump energy index--
variable load (PEIVL);
(B) The bare pump model number; and
(C) If transferred directly to an end-user, the unit's impeller
diameter, as distributed in commerce. Otherwise, a space must be
provided for the impeller diameter to be filled in.
(ii) Display of required information. All orientation, spacing,
type sizes, typefaces, and line widths to display this required
information must be the same as or similar to the display of the other
performance data on the pump's permanent nameplate. The
PEICL or PEIVL, as appropriate to a given pump
model, must be identified in the form ``PEICL ____'' or
``PEIVL ____.'' The model number must be in one of the
following forms: ``Model ____'' or ``Model number ____'' or ``Model No.
____.'' The unit's impeller diameter must be in the form ``Imp. Dia.
____(in.).''
(2) Disclosure of efficiency information in marketing materials.
(i) The same information that must appear on a pump's permanent
nameplate pursuant to paragraph (a)(1)(i) of this section, must also be
prominently displayed:
(A) On each page of a catalog that lists the pump; and
(B) In other materials used to market the pump.
(ii) [Reserved]
[[Page 36924]]
(b) Dedicated-purpose pool pumps. For the pumps described in Sec.
431.464(b), the following requirements apply on the same date that
compliance is required with any applicable standards prescribed in
Sec. 431.465.
(1) Pump nameplate--(i) Required information. The permanent
nameplate must be marked clearly with the following information:
(A) The weighted energy factor (WEF); and
(B) The dedicated-purpose pool pump motor total horsepower.
(ii) Display of required information. All orientation, spacing,
type sizes, typefaces, and line widths to display this required
information must be the same as or similar to the display of the other
performance data on the pump's permanent nameplate.
(A) The WEF must be identified in the form ``WEF ____.''
(B) The dedicated-purpose pool pump motor total horsepower must be
identified in one of the following forms: ``Dedicated-purpose pool pump
motor total horsepower _____,'' ``DPPP motor total horsepower _____,''
``motor total horsepower _____,'' ``motor THP _____,'' or ``THP
_____.''
(2) [Reserved]
Appendix A to Subpart Y of Part 431 [Amended]
0
11. In the introductory note to appendix A of subpart Y of part 431,
remove the reference ``10 CFR 431.464'' and add in its place ``10 CFR
431.464(a)''.
0
12. Add appendices B and C to subpart Y of part 431 to read as follows:
Appendix B to Subpart Y of Part 431--Uniform Test Method for the
Measurement of Energy Efficiency of Dedicated-Purpose Pool Pumps
Note: On February 5, 2018 but before July 19, 2021, any
representations made with respect to the energy use or efficiency of
dedicated-purpose pool pumps subject to testing pursuant to 10 CFR
431.464(b) must be made in accordance with the results of testing
pursuant to this appendix. Any optional representations of energy
factor (EF) must be accompanied by a representation of weighted
energy factor (WEF).
I. Test Procedure for Dedicated-Purpose Pool Pumps
A. General
A.1 Test Method. To determine the weighted energy factor (WEF)
for dedicated-purpose pool pumps, perform ``wire-to-water'' testing
in accordance with HI 40.6-2014-B, except section 40.6.4.1,
``Vertically suspended pumps''; section 40.6.4.2, ``Submersible
pumps''; section 40.6.5.3, ``Test report''; section 40.6.5.5, ``Test
conditions''; section 40.6.5.5.2, ``Speed of rotation during
testing''; section 40.6.6.1, ``Translation of test results to rated
speed of rotation''; section 40.6.6.2, ``Pump efficiency''; section
40.6.6.3, ``Performance curve''; section A.7, ``Testing at
temperatures exceeding 30 [deg]C (86[emsp14][deg]F)''; and appendix
B, ``Reporting of test results''; (incorporated by reference, see
Sec. 431.463) with the modifications and additions as noted
throughout the provisions below. Do not use the test points
specified in section 40.6.5.5.1, ``Test procedure'' of HI 40.6-2014-
B and instead use those test points specified in section D.3 of this
appendix for the applicable dedicated-purpose pool pump variety and
speed configuration. When determining overall efficiency, best
efficiency point, or other applicable pump energy performance
information, section 40.6.5.5.1, ``Test procedure''; section
40.6.6.2, ``Pump efficiency''; and section 40.6.6.3, ``Performance
curve'' must be used, as applicable. For the purposes of applying
this appendix, the term ``volume per unit time,'' as defined in
section 40.6.2, ``Terms and definitions,'' of HI 40.6-2014-B shall
be deemed to be synonymous with the term ``flow rate'' used
throughout that standard and this appendix.
A.2. Calculations and Rounding. All terms and quantities refer
to values determined in accordance with the procedures set forth in
this appendix for the rated pump. Perform all calculations using raw
measured values without rounding. Round WEF, EF, maximum head,
vertical lift, and true priming time values to the tenths place
(i.e., 0.1) and rated hydraulic horsepower to the thousandths place
(i.e., 0.001). Round all other reported values to the hundredths
place unless otherwise specified.
B. Measurement Equipment
B.1 For the purposes of measuring flow rate, speed of rotation,
temperature, and pump power output, the equipment specified in HI
40.6-2014-B Appendix C (incorporated by reference, see Sec.
431.463) necessary to measure head, speed of rotation, flow rate,
and temperature must be used and must comply with the stated
accuracy requirements in HI 40.6-2014-B Table 40.6.3.2.3, except as
specified in section B.1.1 and B.1.2 of this appendix. When more
than one instrument is used to measure a given parameter, the
combined accuracy, calculated as the root sum of squares of
individual instrument accuracies, must meet the specified accuracy
requirements.
B.1.1 Electrical measurement equipment for determining the
driver power input to the motor or controls must be capable of
measuring true root mean squared (RMS) current, true RMS voltage,
and real power up to the 40th harmonic of fundamental supply source
frequency, and have a combined accuracy of 2.0 percent
of the measured value at the fundamental supply source frequency.
B.1.2 Instruments for measuring distance (e.g., height above the
reference plane or water level) must be accurate to and have a
resolution of at least 0.1 inch.
B.2 Calibration. Calibration requirements for instrumentation
are specified in appendix D of HI 40.6-2014-B (incorporated by
reference, see Sec. 431.463). Historical calibration data may be
used to justify time periods up to three times longer than those
specified in table D.1 of HI 40.6-2014-B provided the supporting
historical data shows maintenance of calibration of the given
instrument up to the selected extended calibration interval on at
least two unique occasions, based on the interval specified in HI
40.6-2014-B.
C. Test Conditions and Tolerances
C.1 Pump Specifications. Conduct testing at full impeller
diameter in accordance with the test conditions, stabilization
requirements, and specifications of HI 40.6-2014-B section 40.6.3,
``Pump efficiency testing''; section 40.6.4, ``Considerations when
determining the efficiency of a pump''; section 40.6.5.4 (including
appendix A), ``Test arrangements''; and section 40.6.5.5, ``Test
conditions'' (incorporated by reference, see Sec. 431.463).
C.2 Power Supply Requirements. The following conditions also
apply to the mains power supplied to the DPPP motor or controls, if
any:
(1) Maintain the voltage within 5 percent of the
rated value of the motor,
(2) Maintain the frequency within 1 percent of the
rated value of the motor,
(3) Maintain the voltage unbalance of the power supply within
3 percent of the value with which the motor was rated,
and
(4) Maintain total harmonic distortion below 12 percent
throughout the test.
C.3 Test Conditions. Testing must be carried out with water that
is between 50 and 107 [deg]F with less than or equal to 15
nephelometric turbidity units (NTU).
C.4 Tolerances. For waterfall pumps, multi-speed self-priming
and non-self-priming pool filter pumps, and variable-speed self-
priming and non-self-priming pool filter pumps all measured load
points must be within 2.5 percent of the specified head
value and comply with any specified flow values or thresholds. For
all other dedicated-purpose pool pumps, all measured load points
must be within the greater of 2.5 percent of the
specified flow rate values or 0.5 gpm and comply with
any specified head values or thresholds.
D. Data Collection and Stabilization
D.1 Damping Devices. Use of damping devices, as described in
section 40.6.3.2.2 of HI 40.6-2014-B (incorporated by reference, see
Sec. 431.463), are only permitted to integrate up to the data
collection interval used during testing.
D.2 Stabilization. Record data at any tested load point only
under stabilized conditions, as defined in HI 40.6-2014-B section
40.6.5.5.1 (incorporated by reference, see Sec. 431.463), where a
minimum of two measurements are used to determine stabilization.
D.3 Test Points. Measure the flow rate in gpm, pump total head
in ft, the driver power input in W, and the speed of rotation in rpm
at each load point specified in Table 1 of this appendix for each
DPPP variety and speed configuration:
[[Page 36925]]
Table 1--Load Points (i) and Weights (wi) for Each DPPP Variety and Speed Configuration
--------------------------------------------------------------------------------------------------------------------------------------------------------
Number of Test points
load --------------------------------------------------------------
DPPP varieties Speed configuration(s) points Load point (i)
(n) Flow rate (Q) (GPM) Head (H) (ft) Speed (rpm)
--------------------------------------------------------------------------------------------------------------------------------------------------------
Self-Priming Pool Filter Pumps And Single-speed dedicated- 1 High............ Qhigh (gpm) = H = 0.0082 x Maximum speed
Non-Self-Priming Pool Filter Pumps. purpose pool pumps and Qmax_speed@C ** Qhigh\2\
all self-priming and
non-self-priming pool
filter pumps not
meeting the definition
of two-*, multi-, or
variable-speed
dedicated-purpose pool
pump.
Two-speed dedicated- 2 Low............. Qlow (gpm) = Flow rate H = 0.0082 x Lowest speed capable
purpose pool pumps *. associated with Qlow\2\ of meeting the
specified head and specified flow and
speed that is not head values, if any
below: ***.
31.1 gpm if
rated hydraulic
horsepower is >0.75
or
24.7 gpm if
rated hydraulic
horsepower is <=0.75
High............ Qhigh (gpm) = H = 0.0082 x Maximum speed.
Qmax_speed@C ** Qhigh\2\
Multi-speed and 2 Low............. Qlow (gpm) = H = 0.0082 x Lowest speed capable
variable-speed If rated Qlow\2\ of meeting the
dedicated-purpose pool hydraulic horsepower specified flow and
pumps. is >0.75, then Qlow head values.
>= 31.1 gpm
If rated
hydraulic horsepower
is <=0.75, then Qlow
>=24.7 gpm
High............ Qhigh (gpm) >=0.8 x H = 0.0082 x Lowest speed capable
Qmax_speed@C ** Qhigh\2\ of meeting the
specified flow and
head values.
Waterfall Pumps.................... Single-speed dedicated- 1 High............ Qlow (gpm) = Flow 17.0 ft Maximum speed.
purpose pool pumps. corresponding to
specified head
Pressure Cleaner Booster Pumps..... Any.................... 1 High............ 10.0 gpm >=60.0 ft Lowest speed capable
of meeting the
specified flow and
head values.
--------------------------------------------------------------------------------------------------------------------------------------------------------
* In order to apply the test points for two-speed self-priming and non-self-priming pool filter pumps, self-priming pool filter pumps that are greater
than or equal to 0.711 rated hydraulic horsepower that are two-speed dedicated-purpose pool pumps must also be distributed in commerce either: (1)
With a pool pump control (variable speed drive and user interface or switch) that changes the speed in response to pre-programmed user preferences and
allows the user to select the duration of each speed and/or the on/off times or (2) without a pool pump control that has such capability, but without
which the pump is unable to operate. Two-speed self-priming pool filter pumps greater than or equal to 0.711 rated hydraulic horsepower that do not
meet these requirements must be tested using the load point for single-speed self-priming or non-self-priming pool filter pumps, as appropriate.
** Qmax_speed@C = Flow at max speed on curve C (gpm)
*** If a two-speed pump has a low speed that results in a flow rate below the specified values, the low speed of that pump shall not be tested.
E. Calculations
E.1 Determination of Weighted Energy Factor. Determine the WEF
as a ratio of the measured flow and driver power input to the
dedicated-purpose pool pump in accordance with the following
equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.010
Where:
WEF = Weighted Energy Factor in kgal/kWh;
wi = weighting factor at each load point i, as specified in section
E.2 of this appendix;
Qi = flow at each load point i, in gpm;
Pi = driver power input to the motor (or controls, if present) at
each load point i, in watts;
i = load point(s), defined uniquely for each DPPP variety and speed
configuration as specified in section D.3 of this appendix; and
n = number of load point(s), defined uniquely for each DPPP variety
and speed configuration as specified in section D.3 of this
appendix.
E.2 Weights. When determining WEF, apply the weights specified
in Table 2 of this appendix for the applicable load points, DPPP
varieties, and speed configurations:
Table 2--Load Point Weights (wi)
----------------------------------------------------------------------------------------------------------------
Load point(s) i
DPPP varieties Speed configuration(s) -------------------------------
Low flow High flow
----------------------------------------------------------------------------------------------------------------
Self-Priming Pool Filter Pumps and Non-Self- Single-speed dedicated-purpose .............. 1.0
Priming Pool Filter Pumps. pool pumps and all self-priming
and non-self-priming pool filter
pumps not meeting the definition
of two-,* multi-, or variable-
speed dedicated-purpose pool
pump.
Two-speed dedicated-purpose pool 0.80 0.20
pumps *.
Multi-speed and variable-speed 0.80 0.20
dedicated-purpose pool pumps.
Waterfall Pumps.............................. Single-speed dedicated-purpose .............. 1.0
pool pumps.
[[Page 36926]]
Pressure Cleaner Booster Pump................ Any.............................. .............. 1.0
----------------------------------------------------------------------------------------------------------------
* In order to apply the test points for two-speed self-priming and non-self-priming pool filter pumps, self-
priming pool filter pumps that are greater than or equal to 0.711 rated hydraulic horsepower that are two-
speed dedicated-purpose pool pumps must also be distributed in commerce either: (1) With a pool pump control
(variable speed drive and user interface or switch) that changes the speed in response to pre-programmed user
preferences and allows the user to select the duration of each speed and/or the on/off times or (2) without a
pool pump control that has such capability, but without which the pump is unable to operate. Two-speed self-
priming pool filter pumps greater than or equal to 0.711 rated hydraulic horsepower that do not meet these
requirements must be tested using the load point for single-speed self-priming or non-self-priming pool filter
pumps, as appropriate.
E.3 Determination of Horsepower and True Power Factor Metrics
E.3.1 Determine the pump power output at any load point i using
the following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.011
Where:
Pu,i = the measured pump power output at load point i of the tested
pump, in hp;
Qi = the measured flow rate at load point i of the tested pump, in
gpm;
Hi = pump total head at load point i of the tested pump, in ft; and
SG = the specific gravity of water at specified test conditions,
which is equivalent to 1.00.
E.3.1.1 Determine the rated hydraulic horsepower as the pump
power output measured on the reference curve at maximum rotating
speed and full impeller diameter for the rated pump.
E.3.2 For dedicated-purpose pool pumps with single-phase AC
motors or DC motors, determine the dedicated-purpose pool pump
nominal motor horsepower as the product of the measured full load
speed and torque, adjusted to the appropriate units, as shown in the
following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.012
Where:
Pnm = the dedicated-purpose pool pump nominal total horsepower at
full load, in hp;
T = output torque at full load, in lb-ft; and
n = the motor speed at full load, in rpm.
Full-load speed and torque shall be determined based on the
maximum continuous duty motor power output rating allowable for the
motor's nameplate ambient rating and insulation class.
E.3.2.1 For single-phase AC motors, determine the measured speed
and torque at full load according to either section E.3.2.1.1 or
E.3.2.1.2 of this appendix.
E.3.2.1.1 Use the procedures in section 3.2, ``Tests with
load''; section 4 ``Testing facilities''; section 5.2 ``Mechanical
measurements''; section 5.3 ``Temperature measurements''; and
section 6 ``Tests'' of IEEE 114-2010 (incorporated by reference, see
Sec. 431.463), or
E.3.2.1.2 Use the applicable procedures in section 5, ``General
test requirements'' and section 6, ``Tests'' of CSA C747-2009 (RA
2014); except in section 6.4(b) the conversion factor shall be 5252,
only measurements at full load are required in section 6.5, and
section 6.6 shall be disregarded (incorporated by reference, see
Sec. 431.463).
E.3.2.2 For DC motors, determine the measured speed and torque
at full load according to either section E.3.2.2.1 or E.3.2.2.2 of
this appendix.
E.3.2.2.1 Use the procedures in section 3.1, ``Instrument
Selection Factors''; section 3.4 ``Power Measurement'': Section 3.5
``Power Sources''; section 4.1.2 ``Ambient Air''; section 4.1.4
``Direction of Rotation''; section 5.4.1 ``Reference Conditions'';
and section 5.4.3.2 ``Dynomometer or Torquemeter Method'' of IEEE
113-1985 (incorporated by reference, see Sec. 431.463), or
E.3.2.2.2 Use the applicable procedures in section 5, ``General
test requirements'' and section 6, ``Tests'' of CSA C747-2009 (RA
2014); except in section 6.4(b) the conversion factor shall be 5252,
only measurements at full load are required in section 6.5, and
section 6.6 shall be disregarded (incorporated by reference, see
Sec. 431.463).
E.3.3 For dedicated-purpose pool pumps with single-phase AC
motors or DC motors, the dedicated-purpose pool pump service factor
is equal to 1.0.
E.3.4 Determine the dedicated-purpose pool pump motor total
horsepower according to section E.3.4.1 of this appendix for
dedicated-purpose pool pumps with single-phase AC motors or DC
motors and section E.3.4.2 of this appendix for dedicated-purpose
pool pumps with polyphase AC motors.
E.3.4.1 For dedicated-purpose pool pumps with single-phase AC
motors or DC motors, determine the dedicated-purpose pool pump motor
total horsepower as the product of the dedicated-purpose pool pump
nominal motor horsepower, determined in accordance with section
E.3.2 of this appendix, and the dedicated-purpose pool pump service
factor, determined in accordance with section E.3.3 of this
appendix.
E.3.4.2 For dedicated-purpose pool pumps with polyphase AC
induction motors, determine the dedicated-purpose pool pump motor
total horsepower as the product of the rated nominal motor
horsepower and the rated service factor of the motor.
E.3.5 Determine the true power factor at each applicable load
point specified in Table 1 of this appendix for each DPPP variety
and speed configuration as a ratio of driver power input to the
motor (or controls, if present) (Pi), in watts, divided by the
product of the voltage in volts and the current in amps at each load
point i, as shown in the following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.013
Where:
PFi = true power factor at each load point i, dimensionless;
Pi = driver power input to the motor (or controls, if present) at
each load point i, in watts;
Vi = voltage at each load point i, in volts;
Ii = current at each load point i, in amps; and
i = load point(s), defined uniquely for each DPPP variety and speed
configuration as specified in section D.3 of this appendix.
E.4 Determination of Maximum Head. Determine the maximum head
for self-priming pool filter pumps, non-self-priming pool filter
pumps, and waterfall pumps by measuring the head at maximum speed
and the minimum flow rate at which the pump is designed to operate
continuously or safely, where the minimum flow rate is assumed to be
zero unless stated otherwise in the manufacturer literature.
F. Determination of Self-Priming Capability
F.1 Test Method. Determine the vertical lift and true priming
time of non-self-priming pool filter pumps and self-priming pool
filter pumps that are not already certified as self-priming under
NSF/ANSI 50-2015 (incorporated by reference, see Sec. 431.463) by
testing such pumps pursuant to section C.3 of appendix C of NSF/ANSI
50-2015, except for the modifications and exceptions listed in the
following sections F.1.1 through F.1.5 of this appendix:
F.1.1 Where section C.3.2, ``Apparatus,'' and section C.3.4,
``Self-priming capability test method,'' of NSF/ANSI 50-2015
(incorporated by reference, see Sec. 431.463) state that the
``suction line must be essentially as shown in annex C, figure
C.1;'' the phrase ``essentially as shown in Annex C, figure C.1''
means:
The centerline of the pump impeller shaft is situated a
vertical distance equivalent to the specified vertical lift (VL),
calculated in accordance with section F.1.1.1. of this appendix,
above the water level of a water tank of sufficient volume as to
maintain a constant water surface level for the duration of the
test;
[[Page 36927]]
The pump draws water from the water tank with a riser
pipe that extends below the water level a distance of at least 3
times the riser pipe diameter (i.e., 3 pipe diameters);
The suction inlet of the pump is at least 5 pipe
diameters from any obstructions, 90[deg] bends, valves, or fittings;
and
The riser pipe is of the same pipe diameter as the pump
suction inlet.
F.1.1.1 The vertical lift (VL) must be normalized to 5.0 feet at
an atmospheric pressure of 14.7 psia and a water density of 62.4 lb/
ft\3\ in accordance with the following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.014
Where:
VL = vertical lift of the test apparatus from the waterline to the
centerline of the pump impeller shaft, in ft;
[rho]test = density of test fluid, in lb/ft\3\; and
Pabs,test = absolute barometric pressure of test apparatus location
at centerline of pump impeller shaft, in psia.
F.1.2 The equipment accuracy requirements specified in section
B, ``Measurement Equipment,'' of this appendix also apply to this
section F, as applicable.
F.1.2.1 All measurements of head (gauge pressure), flow, and
water temperature must be taken at the pump suction inlet and all
head measurements must be normalized back to the centerline of the
pump impeller shaft in accordance with section A.3.1.3.1 of HI 40.6-
2014-B (incorporated by reference, see Sec. 431.463).
F.1.3 All tests must be conducted with clear water that meets
the requirements adopted in section C.3 of this appendix.
F.1.4 In section C.3.4, ``Self-priming capability test method,''
of NSF/ANSI 50-2015 (incorporated by reference, see Sec. 431.463),
``the elapsed time to steady discharge gauge reading or full
discharge flow'' is determined when the changes in head and flow,
respectively, are within the tolerance values specified in table
40.6.3.2.2, ``Permissible amplitude of fluctuation as a percentage
of mean value of quantity being measured at any test point,'' of HI
40.6-2014-B (incorporated by reference, see Sec. 431.463). The
measured priming time (MPT) is determined as the point in time when
the stabilized load point is first achieved, not when stabilization
is determined. In addition, the true priming time (TPT) is
equivalent to the MPT.
F.1.5 The maximum true priming time for each test run must not
exceed 10.0 minutes. Disregard section C.3.5 of NSF/ANSI 50-2015
(incorporated by reference, see Sec. 431.463).
G. Optional Testing and Calculations
G.1 Energy Factor. When making representations regarding the EF
of dedicated-purpose pool pumps, determine EF on one of four system
curves (A, B, C, or D) and at any given speed (s) according to the
following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.015
Where:
EFX,s = the energy factor on system curve X at speed s in gal/Wh;
X = one of four possible system curves (A, B, C, or D), as defined
in section G.1.1 of this appendix;
s = the tested speed, in rpm;
QX,s = flow rate measured on system curve X at speed s in gpm; and
PX,s = driver power input to the motor (or controls, if present) on
system curve X at speed s in watts.
G.1.1 System Curves. The energy factor may be determined at any
speed (s) and on any of the four system curves A, B, C, and/or D
specified in the Table 3:
Table 3--Systems Curves for Optional EF Test Procedure
------------------------------------------------------------------------
System curve System curve equation *
------------------------------------------------------------------------
A......................................... H = 0.0167 x Q\2\
B......................................... H = 0.0500 x Q\2\
C......................................... H = 0.0082 x Q\2\
D......................................... H = 0.0044 x Q\2\
------------------------------------------------------------------------
* In the above table, Q refers to the flow rate in gpm and H refers to
head in ft.
G.2 Replacement Dedicated-Purpose Pool Pump Motors. To determine
the WEF for replacement DPPP motors, test each replacement DPPP
motor paired with each dedicated-purpose pool pump bare pump for
which the replacement DPPP motor is advertised to be paired, as
stated in the manufacturer's literature for that replacement DPPP
motor model, according to the testing and calculations described in
sections A, B, C, D, and E of this appendix. Alternatively, each
replacement DPPP motor may be tested with the most consumptive
dedicated-purpose pool pump bare pump for which it is advertised to
be paired, as stated in the manufacturer's literature for that
replacement DPPP motor model. If a replacement DPPP motor is not
advertised to be paired with any specific dedicated-purpose pool
pump bare pumps, test with the most consumptive dedicated-purpose
pool pump bare pump available.
Appendix C to Subpart Y of Part 431--Uniform Test Method for the
Measurement of Energy Efficiency of Dedicated-Purpose Pool Pumps
Note: Any representations made on or after July 19, 2021, with
respect to the energy use or efficiency of dedicated-purpose pool
pumps subject to testing pursuant to 10 CFR 431.464(b) must be made
in accordance with the results of testing pursuant to this appendix.
I. Test Procedure for Dedicated-Purpose Pool Pumps
A. General
A.1 Test Method. To determine the weighted energy factor (WEF)
for dedicated-purpose pool pumps, perform ``wire-to-water'' testing
in accordance with HI 40.6-2014-B, except section 40.6.4.1,
``Vertically suspended pumps''; section 40.6.4.2, ``Submersible
pumps''; section 40.6.5.3, ``Test report''; section 40.6.5.5, ``Test
conditions''; section 40.6.5.5.2, ``Speed of rotation during
testing''; section 40.6.6.1, ``Translation of test results to rated
speed of rotation''; section 40.6.6.2, ``Pump efficiency''; section
40.6.6.3, ``Performance curve''; section A.7, ``Testing at
temperatures exceeding 30 [deg]C (86[emsp14][deg]F)''; and appendix
B, ``Reporting of test results''; (incorporated by reference, see
Sec. 431.463) with the modifications and additions as noted
throughout the provisions below. Do not use the test points
specified in section 40.6.5.5.1, ``Test procedure'' of HI 40.6-2014-
B and instead use those test points specified in section D.3 of this
appendix for the applicable dedicated-purpose pool pump variety and
speed configuration. When determining overall efficiency, best
efficiency point, or other applicable pump energy performance
information, section 40.6.5.5.1, ``Test procedure''; section
40.6.6.2, ``Pump efficiency''; and section 40.6.6.3,
[[Page 36928]]
``Performance curve'' must be used, as applicable. For the purposes
of applying this appendix, the term ``volume per unit time,'' as
defined in section 40.6.2, ``Terms and definitions,'' of HI 40.6-
2014-B shall be deemed to be synonymous with the term ``flow rate''
used throughout that standard and this appendix .
A.2 Calculations and Rounding. All terms and quantities refer to
values determined in accordance with the procedures set forth in
this appendix for the rated pump. Perform all calculations using raw
measured values without rounding. Round WEF, maximum head, vertical
lift, and true priming time values to the tenths place (i.e., 0.1)
and rated hydraulic horsepower to the thousandths place (i.e.,
0.001). Round all other reported values to the hundredths place
unless otherwise specified.
B. Measurement Equipment
B.1 For the purposes of measuring flow rate, speed of rotation,
temperature, and pump power output, the equipment specified in HI
40.6-2014-B Appendix C (incorporated by reference, see Sec.
431.463) necessary to measure head, speed of rotation, flow rate,
and temperature must be used and must comply with the stated
accuracy requirements in HI 40.6-2014-B Table 40.6.3.2.3, except as
specified in sections B.1.1 and B.1.2 of this appendix. When more
than one instrument is used to measure a given parameter, the
combined accuracy, calculated as the root sum of squares of
individual instrument accuracies, must meet the specified accuracy
requirements.
B.1.1 Electrical measurement equipment for determining the
driver power input to the motor or controls must be capable of
measuring true root mean squared (RMS) current, true RMS voltage,
and real power up to the 40th harmonic of fundamental supply source
frequency, and have a combined accuracy of 2.0 percent
of the measured value at the fundamental supply source frequency.
B.1.2 Instruments for measuring distance (e.g., height above the
reference plane or water level) must be accurate to and have a
resolution of at least 0.1 inch.
B.2 Calibration. Calibration requirements for instrumentation
are specified in appendix D of HI 40.6-2014-B (incorporated by
reference, see Sec. 431.463). Historical calibration data may be
used to justify time periods up to three times longer than those
specified in table D.1 of HI 40.6-2014-B provided the supporting
historical data shows maintenance of calibration of the given
instrument up to the selected extended calibration interval on at
least two unique occasions, based on the interval specified in HI
40.6-2014-B.
C. Test Conditions and Tolerances
C.1 Pump Specifications. Conduct testing at full impeller
diameter in accordance with the test conditions, stabilization
requirements, and specifications of HI 40.6-2014-B section 40.6.3,
``Pump efficiency testing''; section 40.6.4, ``Considerations when
determining the efficiency of a pump''; section 40.6.5.4 (including
appendix A), ``Test arrangements''; and section 40.6.5.5, ``Test
conditions'' (incorporated by reference, see Sec. 431.463).
C.2 Power Supply Requirements. The following conditions also
apply to the mains power supplied to the DPPP motor or controls, if
any:
(1) Maintain the voltage within 5 percent of the
rated value of the motor,
(2) Maintain the frequency within 1 percent of the
rated value of the motor,
(3) Maintain the voltage unbalance of the power supply within
3 percent of the value with which the motor was rated,
and
(4) Maintain total harmonic distortion below 12 percent
throughout the test.
C.3 Test Conditions. Testing must be carried out with water that
is between 50 and 107 [deg]F with less than or equal to 15
nephelometric turbidity units (NTU).
C.4 Tolerances. For waterfall pumps, multi-speed self-priming
and non-self-priming pool filter pumps, and variable-speed self-
priming and non-self-priming pool filter pumps all measured load
points must be within 2.5 percent of the specified head
value and comply with any specified flow values or thresholds. For
all other dedicated-purpose pool pumps, all measured load points
must be within the greater of 2.5 percent of the
specified flow rate values or 0.5 gpm and comply with
any specified head values or thresholds.
D. Data Collection and Stabilization
D.1 Damping Devices. Use of damping devices, as described in
section 40.6.3.2.2 of HI 40.6-2014-B (incorporated by reference, see
Sec. 431.463), are only permitted to integrate up to the data
collection interval used during testing.
D.2 Stabilization. Record data at any tested load point only
under stabilized conditions, as defined in HI 40.6-2014-B section
40.6.5.5.1 (incorporated by reference, see Sec. 431.463), where a
minimum of two measurements are used to determine stabilization.
D.3 Test Points. Measure the flow rate in gpm, pump total head
in ft, the driver power input in W, and the speed of rotation in rpm
at each load point specified in Table 1 of this appendix for each
DPPP variety and speed configuration:
Table 1--Load Points (i) and Weights (wi) for Each DPPP Variety and Speed Configuration
--------------------------------------------------------------------------------------------------------------------------------------------------------
Number of Test points
load --------------------------------------------------------------
DPPP varieties Speed configuration(s) points Load point (i)
(n) Flow rate (Q) (GPM) Head (H) (ft) Speed (rpm)
--------------------------------------------------------------------------------------------------------------------------------------------------------
Self-Priming Pool Filter Pumps And Single-speed dedicated- 1 High............ Qhigh (gpm) = H = 0.0082 x Maximum speed.
Non-Self-Priming Pool Filter Pumps. purpose pool pumps and Qmax_speed@C ** Qhigh\2\
all self-priming and
non-self-priming pool
filter pumps not
meeting the definition
of two-*, multi-, or
variable-speed
dedicated-purpose pool
pump.
Two-speed dedicated- 2 Low............. Qlow (gpm) = Flow rate H = 0.0082 x Lowest speed capable
purpose pool pumps *. associated with Qlow\2\ of meeting the
specified head and specified flow and
speed that is not head values, if any.
below: ***
31.1 gpm if
rated hydraulic
horsepower is >0.75
or
24.7 gpm if
rated hydraulic
horsepower is <=0.75
High............ Qhigh (gpm) = H = 0.0082 x Maximum speed.
Qmax_speed@C ** Qlow\2\
Multi-speed and 2 Low............. Qlow (gpm) = H = 0.0082 x Lowest speed capable
variable-speed If rated Qlow\2\ of meeting the
dedicated-purpose pool hydraulic horsepower specified flow and
pumps. is >0.75, then Qlow head values.
>=31.1 gpm
If rated
hydraulic horsepower
is <=0.75, then Qlow
>=24.7 gpm
High............ Qhigh (gpm) >=0.8 x H = 0.0082 x Lowest speed capable
Qmax_speed@C ** Qhigh\2\ of meeting the
specified flow and
head values.
[[Page 36929]]
Waterfall Pumps.................... Single-speed dedicated- 1 High............ Qlow (gpm) = Flow 17.0 ft Maximum speed.
purpose pool pumps. corresponding to
specified head
Pressure Cleaner Booster Pumps..... Any.................... 1 High............ 10.0 gpm >=60.0 ft Lowest speed capable
of meeting the
specified flow and
head values.
--------------------------------------------------------------------------------------------------------------------------------------------------------
* In order to apply the test points for two-speed self-priming and non-self-priming pool filter pumps, self-priming pool filter pumps that are greater
than or equal to 0.711 rated hydraulic horsepower that are two-speed dedicated-purpose pool pumps must also be distributed in commerce either: (1)
With a pool pump control (variable speed drive and user interface or switch) that changes the speed in response to pre-programmed user preferences and
allows the user to select the duration of each speed and/or the on/off times or (2) without a pool pump control that has such capability, but without
which the pump is unable to operate. Two-speed self-priming pool filter pumps greater than or equal to 0.711 rated hydraulic horsepower that do not
meet these requirements must be tested using the load point for single-speed self-priming or non-self-priming pool filter pumps, as appropriate.
** Qmax_speed@C = Flow at max speed on curve C (gpm).
*** If a two-speed pump has a low speed that results in a flow rate below the specified values, the low speed of that pump shall not be tested.
E. Calculations
E.1 Determination of Weighted Energy Factor. Determine the WEF
as a ratio of the measured flow and driver power input to the
dedicated-purpose pool pump in accordance with the following
equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.016
Where:
WEF = Weighted Energy Factor in kgal/kWh;
Wi = weighting factor at each load point i, as specified in section
E.2 of this appendix;
Qi = flow at each load point i, in gpm;
Pi = driver power input to the motor (or controls, if present) at
each load point i, in watts;
i = load point(s), defined uniquely for each DPPP variety and speed
configuration as specified in section D.3 of this appendix; and
n = number of load point(s), defined uniquely for each DPPP variety
and speed configuration as specified in section D.3 of this
appendix.
E.2 Weights. When determining WEF, apply the weights specified
in Table 2 of this appendix for the applicable load points, DPPP
varieties, and speed configurations:
Table 2--Load Point Weights (wi)
----------------------------------------------------------------------------------------------------------------
Load point(s) i
DPPP varieties Speed configuration(s) -------------------------------
Low flow High flow
----------------------------------------------------------------------------------------------------------------
Self-Priming Pool Filter Pumps and Non-Self- Single-speed dedicated-purpose .............. 1.0
Priming Pool Filter Pumps. pool pumps and all self-priming
and non-self-priming pool filter
pumps not meeting the definition
of two-*, multi-, or variable-
speed dedicated-purpose pool
pump.
Two-speed dedicated-purpose pool 0.80 0.20
pumps *.
Multi-speed and variable-speed 0.80 0.20
dedicated-purpose pool pumps.
Waterfall Pumps.............................. Single-speed dedicated-purpose .............. 1.0
pool pumps.
Pressure Cleaner Booster Pump................ Any.............................. .............. 1.0
----------------------------------------------------------------------------------------------------------------
* In order to apply the test points for two-speed self-priming and non-self-priming pool filter pumps, self-
priming pool filter pumps that are greater than or equal to 0.711 rated hydraulic horsepower that are two-
speed dedicated-purpose pool pumps must also be distributed in commerce either: (1) With a pool pump control
(variable speed drive and user interface or switch) that changes the speed in response to pre-programmed user
preferences and allows the user to select the duration of each speed and/or the on/off times or (2) without a
pool pump control that has such capability, but without which the pump is unable to operate. Two-speed self-
priming pool filter pumps greater than or equal to 0.711 rated hydraulic horsepower that do not meet these
requirements must be tested using the load point for single-speed self-priming or non-self-priming pool filter
pumps, as appropriate.
E.3 Determination of Horsepower and True Power Factor Metrics
E.3.1 Determine the pump power output at any load point i using
the following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.017
Where:
Pu,i = the measured pump power output at load point i of the tested
pump, in hp;
Qi = the measured flow rate at load point i of the tested pump, in
gpm;
Hi = pump total head at load point i of the tested pump, in ft; and
SG = the specific gravity of water at specified test conditions,
which is equivalent to 1.00.
E.3.1.1 Determine the rated hydraulic horsepower as the pump
power output measured on the reference curve at maximum rotating
speed and full impeller diameter for the rated pump.
E.3.2 For dedicated-purpose pool pumps with single-phase AC
motors or DC motors, determine the dedicated-purpose pool pump
nominal motor horsepower as the product of the measured full load
speed and torque, adjusted to the appropriate units, as shown in the
following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.018
Where:
Pnm = the dedicated-purpose pool pump nominal total horsepower at
full load, in hp;
T = output torque at full load, in lb-ft; and
n = the motor speed at full load, in rpm.
Full-load speed and torque shall be determined based on the
maximum continuous duty motor power output rating allowable for the
motor's nameplate ambient rating and insulation class.
E.3.2.1 For single-phase AC motors, determine the measured speed
and torque at
[[Page 36930]]
full load according to either section E.3.2.1.1 or E.3.2.1.2 of this
appendix.
E.3.2.1.1 Use the procedures in section 3.2, ``Tests with
load''; section 4 ``Testing facilities''; section 5.2 ``Mechanical
measurements''; section 5.3 ``Temperature measurements''; and
section 6 ``Tests'' of IEEE 114-2010 (incorporated by reference, see
Sec. 431.463), or
E.3.2.1.2 Use the applicable procedures in section 5, ``General
test requirements'' and section 6, ``Tests'' of CSA C747-2009 (RA
2014); except in section 6.4(b) the conversion factor shall be 5252,
only measurements at full load are required in section 6.5, and
section 6.6 shall be disregarded (incorporated by reference, see
Sec. 431.463).
E.3.2.2 For DC motors, determine the measured speed and torque
at full load according to either section E.3.2.2.1 or E.3.2.2.2 of
this appendix.
E.3.2.2.1 Use the procedures in section 3.1, ``Instrument
Selection Factors''; section 3.4 ``Power Measurement'': Section 3.5
``Power Sources''; section 4.1.2 ``Ambient Air''; section 4.1.4
``Direction of Rotation''; section 5.4.1 ``Reference Conditions'';
and section 5.4.3.2 ``Dynomometer or Torquemeter Method'' of IEEE
113-1985 (incorporated by reference, see Sec. 431.463), or
E.3.2.2.2 Use the applicable procedures in section 5, ``General
test requirements'' and section 6, ``Tests'' of CSA C747-2009 (RA
2014); except in section 6.4(b) the conversion factor shall be 5252,
only measurements at full load are required in section 6.5, and
section 6.6 shall be disregarded (incorporated by reference, see
Sec. 431.463).
E.3.3 For dedicated-purpose pool pumps with single-phase AC
motors or DC motors, the dedicated-purpose pool pump service factor
is equal to 1.0.
E.3.4 Determine the dedicated-purpose pool pump motor total
horsepower according to section E.3.4.1 of this appendix for
dedicated-purpose pool pumps with single-phase AC motors or DC
motors and section E.3.4.2 of this appendix for dedicated-purpose
pool pumps with polyphase AC motors.
E.3.4.1 For dedicated-purpose pool pumps with single-phase AC
motors or DC motors, determine the dedicated-purpose pool pump motor
total horsepower as the product of the dedicated-purpose pool pump
nominal motor horsepower, determined in accordance with section
E.3.2 of this appendix, and the dedicated-purpose pool pump service
factor, determined in accordance with section E.3.3 of this
appendix.
E.3.4.2 For dedicated-purpose pool pumps with polyphase AC
induction motors, determine the dedicated-purpose pool pump motor
total horsepower as the product of the rated nominal motor
horsepower and the rated service factor of the motor.
E.3.5 Determine the true power factor at each applicable load
point specified in Table 1 of this appendix for each DPPP variety
and speed configuration as a ratio of driver power input to the
motor (or controls, if present) (Pi), in watts, divided by the
product of the voltage in volts and the current in amps at each load
point i, as shown in the following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.019
Where:
PFi = true power factor at each load point i, dimensionless;
Pi = driver power input to the motor (or controls, if present) at
each load point i, in watts;
Vi = voltage at each load point i, in volts;
Ii = current at each load point i, in amps; and
i = load point(s), defined uniquely for each DPPP variety and speed
configuration as specified in section D.3 of this appendix.
E.4 Determination of Maximum Head. Determine the maximum head
for self-priming pool filter pumps, non-self-priming pool filter
pumps, and waterfall pumps by measuring the head at maximum speed
and the minimum flow rate at which the pump is designed to operate
continuously or safely, where the minimum flow rate is assumed to be
zero unless stated otherwise in the manufacturer literature.
F. Determination of Self-Priming Capability
F.1 Test Method. Determine the vertical lift and true priming
time of non-self-priming pool filter pumps and self-priming pool
filter pumps that are not already certified as self-priming under
NSF/ANSI 50-2015 (incorporated by reference, see Sec. 431.463) by
testing such pumps pursuant to section C.3 of appendix C of NSF/ANSI
50-2015, except for the modifications and exceptions listed in the
following sections F.1.1 through F.1.5 of this appendix:
F.1.1 Where section C.3.2, ``Apparatus,'' and section C.3.4,
``Self-priming capability test method,'' of NSF/ANSI 50-2015
(incorporated by reference, see Sec. 431.463) state that the
``suction line must be essentially as shown in annex C, figure
C.1;'' the phrase ``essentially as shown in Annex C, figure C.1''
means:
(1) The centerline of the pump impeller shaft is situated a
vertical distance equivalent to the specified vertical lift (VL),
calculated in accordance with section F.1.1.1. of this appendix,
above the water level of a water tank of sufficient volume as to
maintain a constant water surface level for the duration of the
test;
(2) The pump draws water from the water tank with a riser pipe
that extends below the water level a distance of at least 3 times
the riser pipe diameter (i.e., 3 pipe diameters);
(3) The suction inlet of the pump is at least 5 pipe diameters
from any obstructions, 90[deg] bends, valves, or fittings; and
(4) The riser pipe is of the same pipe diameter as the pump
suction inlet.
F.1.1.1 The vertical lift (VL) must be normalized to 5.0 feet at
an atmospheric pressure of 14.7 psia and a water density of 62.4 lb/
ft\3\ in accordance with the following equation:
[GRAPHIC] [TIFF OMITTED] TR07AU17.020
Where:
VL = vertical lift of the test apparatus from the waterline to the
centerline of the pump impeller shaft, in ft;
[rho]test = density of test fluid, in lb/ft\3\; and
Pabs,test = absolute barometric pressure of test apparatus location
at centerline of pump impeller shaft, in psia.
F.1.2 The equipment accuracy requirements specified in section
B, ``Measurement Equipment,'' of this appendix also apply to this
section F, as applicable.
F.1.2.1 All measurements of head (gauge pressure), flow, and
water temperature must be taken at the pump suction inlet and all
head measurements must be normalized back to the centerline of the
pump impeller shaft in accordance with section A.3.1.3.1 of HI 40.6-
2014-B (incorporated by reference, see Sec. 431.463).
F.1.3 All tests must be conducted with clear water that meets
the requirements adopted in section C.3 of this appendix.
F.1.4 In section C.3.4, ``Self-priming capability test method,''
of NSF/ANSI 50-2015 (incorporated by reference, see Sec. 431.463),
``the elapsed time to steady discharge gauge reading or full
discharge flow'' is determined when the changes in head and flow,
respectively, are within the tolerance values specified in table
40.6.3.2.2, ``Permissible amplitude of fluctuation as a percentage
of mean value of quantity being measured at any test point,'' of HI
40.6-2014-B (incorporated by reference, see Sec. 431.463). The
measured priming time (MPT) is determined as the point in time when
the stabilized load point is first achieved, not when stabilization
is determined. In addition, the true priming time (TPT) is
equivalent to the MPT.
F.1.5 The maximum true priming time for each test run must not
exceed 10.0 minutes. Disregard section C.3.5 of NSF/ANSI 50-2015
(incorporated by reference, see Sec. 431.463).
[[Page 36931]]
G. Optional Testing and Calculations
G.1 Replacement Dedicated-Purpose Pool Pump Motors. To determine
the WEF for replacement DPPP motors, test each replacement DPPP
motor paired with each dedicated-purpose pool pump bare pump for
which the replacement DPPP motor is advertised to be paired, as
stated in the manufacturer's literature for that replacement DPPP
motor model, according to the testing and calculations described in
sections A, B, C, D, and E of this appendix. Alternatively, each
replacement DPPP motor may be tested with the most consumptive
dedicated-purpose pool pump bare pump for which it is advertised to
be paired, as stated in the manufacturer's literature for that
replacement DPPP motor model. If a replacement DPPP motor is not
advertised to be paired with any specific dedicated-purpose pool
pump bare pumps, test with the most consumptive dedicated-purpose
pool pump bare pump available.
Editorial note: This document was received for publication by
the Office of the Federal Register on July 19, 2017.
[FR Doc. 2017-15464 Filed 8-4-17; 8:45 am]
BILLING CODE 6450-01-P