Methods for Measurement of Filterable PM10, 12970-13012 [E9-6178]
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12970
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
ENVIRONMENTAL PROTECTION
AGENCY
40 CFR Part 51
[EPA–HQ–OAR–2008–0348; FRL–8784–5]
RIN 2060–AO58
Methods for Measurement of Filterable
PM10 and PM2.5 and Measurement of
Condensable Particulate Matter
Emissions From Stationary Sources
PWALKER on PROD1PC71 with PROPOSALS3
AGENCY: Environmental Protection
Agency (EPA).
ACTION: Proposed rule.
SUMMARY: This action proposes
amendments to Methods 201A and 202.
The proposed amendments to Method
201A would add a particle-sizing device
to allow for sampling of particulate
matter (PM) with mean aerodynamic
diameters less than or equal to 2.5
micrometers (μm) (PM2.5 or fine PM).
The proposed amendments to Method
202 would revise the sample collection
and recovery procedures of the method
to reduce the formation of reaction
artifacts that could lead to inaccurate
measurements of condensable
particulate matter (CPM). Additionally,
the proposed amendments to Method
202 would eliminate most of the
hardware and analytical options in the
existing method, thereby increasing the
precision of the method and improving
the consistency in the measurements
obtained between source tests
performed under different regulatory
authorities. Finally, in this notice we are
soliciting comments on whether to end
the transition period for CPM in the
New Source Review (NSR) program on
a date earlier than the current end date
of January 1, 2011. The proposed
amendments would improve the
measurement of fine particulates and
would help State and local agencies in
implementing CPM control measures to
attain the PM2.5 National Ambient Air
Quality Standards (NAAQS) which were
established to protect public health and
welfare.
DATES: Comments. Comments must be
received on or before May 26, 2009.
ADDRESSES: Submit your comments,
identified by Docket ID Number EPA–
HQ–OAR–2008–0348, by one of the
following methods:
• https://www.regulations.gov. Follow
the on-line instructions for submitting
comments.
• E-mail: Send your comments via
electronic mail to a-and-rdocket@epa.gov.
• Fax: (202) 566–9744.
• Mail: Methods for Measurement of
Filterable PM10 and PM2.5 and
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Measurement of Condensable
Particulate Matter Emissions from
Stationary Sources, Environmental
Protection Agency, Mailcode 2822T,
1200 Pennsylvania Ave., NW.,
Washington, DC 20460. Please include a
total of two copies.
• Hand Delivery: EPA Docket Center
EPA Headquarter Library, Room 3334,
EPA West Building, 1301 Constitution
Ave., NW., Washington, DC, 20460.
Such deliveries are accepted only
during the Docket’s normal hours of
operation, and special arrangements
should be made for deliveries of boxed
information.
Instructions: Direct your comments to
Docket ID No. EPA–HQ–OAR–2008–
0348. EPA’s policy is that all comments
received will be included in the public
docket without change and may be
made available online at https://
www.regulations.gov, including any
personal information provided, unless
the comment includes information
claimed to be Confidential Business
Information (CBI) or other information
whose disclosure is restricted by statute.
Do not submit information that you
consider to be CBI or otherwise
protected through https://
www.regulations.gov or e-mail. The
https://www.regulation.gov Web site is
an ‘‘anonymous access’’ system, which
means EPA will not know your identity
or contact information unless you
provide it in the body of your comment.
If you send an e-mail comment directly
to EPA without going through https://
www.regulations.gov, your e-mail
address will be automatically captured
and included as part of the comment
that is placed in the public docket and
made available on the Internet. If you
submit an electronic comment, EPA
recommends that you include your
name and other contact information in
the body of your comment and with any
disk or CD–ROM you submit. If EPA
cannot read your comment due to
technical difficulties and cannot contact
you for clarification, EPA may not be
able to consider your comment.
Electronic files should avoid the use of
special characters, any form of
encryption, and be free of any defects or
viruses. For additional information
about EPA’s public docket, visit the EPA
Docket Center homepage at https://
www.epa.gov/epahome/dockets.htm.
Docket: All documents in the docket
are listed in the https://
www.regulations.gov index. Although
listed in the index, some information is
not publicly available, e.g. , CBI or other
information whose disclosure is
restricted by statute. Certain other
material, such as copyrighted material,
will be publicly available only in hard
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copy. Publicly available docket
materials are available either
electronically in https://
www.regulations.gov or in hard copy at
the Methods for Measurement of
Filterable PM10 and PM2.5 and
Measurement of Condensable
Particulate Matter Emissions from
Stationary Sources Docket, EPA/DC,
EPA West Building, Room 3334, 1301
Constitution Ave., NW., Washington,
DC. The Public Reading Room/Docket
Center is open from 8:30 a.m. to 4:30
p.m., Monday through Friday, excluding
legal holidays. The telephone number
for the Public Reading Room is (202)
566–1744, and the telephone number for
the Air Docket Center is (202) 566–1742.
Public Hearing: If anyone contacts
EPA requesting to speak at a public
hearing concerning our proposal to
revise the PM test methods by April 14,
2009, we will hold a public hearing on
or about April 24, 2009. Persons
interested in presenting oral testimony
should contact Ms. Kristal Mozingo,
Measurement Policy Group (D243–05),
Sector Policies and Programs Division,
EPA, Research Triangle Park, NC 27711,
telephone number: (919) 541–9767, email address: mozingo.kristal@epa.gov.
Persons interested in attending the
public hearing should also call Ms.
Mozingo to verify the time, date, and
location of the hearing. A public hearing
will provide interested parties the
opportunity to present data, views, or
arguments concerning the proposed test
method revisions.
If a public hearing is held, it will be
held at 10 a.m. at the Conference
Facilities at EPA’s Main Campus,
Research Triangle Park, NC, or an
alternate site nearby.
FOR FURTHER INFORMATION CONTACT: For
general information, contact Ms.
Candace Sorrell, U.S. EPA, Office of Air
Quality Planning and Standards, Air
Quality Assessment Division,
Measurement Technology Group (E143–
02), Research Triangle Park, NC 27711;
telephone number: (919) 541–1064; fax
number; (919) 541–0516; e-mail
address: sorrell.candace@epa.gov. For
technical questions, contact Mr. Ron
Myers, U.S. EPA, Office of Air Quality
Planning and Standards, Sector Policies
and Programs Division, Measurement
Policy Group (D243–05), Research
Triangle Park, NC 27711; telephone
number: (919) 541–5407; fax number:
(919) 541–1039; e-mail address:
myers.ron@epa.gov.
SUPPLEMENTARY INFORMATION:
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Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
I. General Information
A. Does This Action Apply to Me?
This action would apply to you if you
operate a stationary source that is
subject to applicable requirements for
total PM or total PM10 where EPA
Method 202 is incorporated as a
component of the applicable
compliance method.
In addition, this action would apply
to you if Federal, State, or local agencies
take certain additional independent
actions. For example, this action would
apply to sources through actions by
State and local agencies which
implement CPM control measures to
attain the PM2.5 NAAQS and specify the
use of this test method to demonstrate
compliance with the control measure.
Actions that State and local agencies
would have to implement include: (1)
Adopting this method in rules or
permits (either by incorporation by
reference or by duplicating the method
in its entirety), and (2) promulgating an
emissions limit requiring the use of this
method (or an incorporated method
SIC 1
code
Category
Industry ................................................................
NAICS 2
code
3569
3569
3569
2911
4953
2621
2819
3241
3274
1222
1231
3334
3341
3312
3325
2493
2435
2436
332410
332410
332410
324110
562213
322110
325188
327310
327410
211111
212111
212112
212113
331312
331314
331111
331513
321219
321211
321212
12971
based upon this method). This action
would also apply to stationary sources
that are required to meet new applicable
CPM requirements established through
Federal or State permits or rules, such
as New Source Performance Standards
and New Source Review, which specify
the use of this test method to
demonstrate compliance with the
control measure.
The source categories and entities
potentially affected include, but are not
limited to, the following:
Examples of potentially regulated entities
Fossil fuel steam generators.
Industrial, commercial, institutional steam generating units.
Electricity generating units.
Petroleum refineries.
Municipal waste combustors.
Pulp and paper mills.
Sulfuric acid plants.
Portland Cement Plants.
Lime Manufacturing Plants.
Coal Preparation Plants.
Primary and Secondary Aluminum Plants.
Iron and Steel Plants.
Plywood and Reconstituted Products Plants.
1 Standard
2 North
Industrial Classification.
American Industrial Classification System.
PWALKER on PROD1PC71 with PROPOSALS3
B. What Should I Consider as I Prepare
My Comments for EPA?
disclosed except in accordance with
procedures set forth in 40 CFR part 2.
Do not submit information containing
CBI to EPA through https://
www.regulations.gov or e-mail. Send or
deliver information identified as CBI
only to the following address: Roberto
Morales, OAQPS Document Control
Officer (C404–02), U.S. EPA, Office of
Air Quality Planning and Standards,
Research Triangle Park, NC 27711,
Attention Docket ID No. EPA–HQ–
OAR–2008–0348. Clearly mark the part
or all of the information that you claim
to be CBI. For CBI information on a disk
or CD–ROM that you mail to EPA, mark
the outside of the disk or CD–ROM as
CBI, and then identify electronically
within the disk or CD–ROM the specific
information that is claimed as CBI. In
addition to one complete version of the
comment that includes information
claimed as CBI, a copy of the comment
that does not contain the information
claimed as CBI must be submitted for
inclusion in the public docket.
Information so marked will not be
C. Where Can I Obtain a Copy of This
Action and Other Related Information?
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In addition to being available in the
docket, an electronic copy of today’s
proposed amendments is also available
on the Worldwide Web (https://
www.epa.gov/ttn/) through the
Technology Transfer Network (TTN).
Following the Administrator’s signature,
a copy of the proposed amendment will
be posted on the TTN’s policy and
guidance page for newly proposed or
promulgated rules at https://
www.epa.gov/ttn/oarpg. The TTN
provides information and technology
exchange in various areas of air
pollution control.
D. How Is This Document Organized?
The information in this preamble is
organized as follows:
I. General Information
A. Does This Action Apply to Me?
B. What Should I Consider as I Prepare My
Comments for EPA?
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C. Where Can I Obtain a Copy of This Action
and Other Related Information?
D. How Is This Document Organized?
II. Background
A. Why Is EPA Issuing This Proposed
Rule?
B. Particulate Matter National Ambient Air
Quality Standards
C. Measuring PM Emissions
1. Method 201A
2. Method 202
III. This Action
A. What Are the Proposed Amendments to
Method 201A?
B. What Are the Proposed Amendments to
Method 202?
C. How Will the Proposed Amendments to
Methods 201A and 202 Affect Existing
Emission Inventories, Emission
Standards, and Permit Programs?
D. Request for Comments
1. Items Associated With Both Test
Methods
2. Items Associated With Method 201A
2. Items Associated With Method 202
IV. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory
Planning and Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
E. Executive Order 13132: Federalism
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F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
G. Executive Order 13045: Protection of
Children From Environmental Health
and Safety Risks
H. Executive Order 13211: Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use
I. National Technology Transfer and
Advancement Act
J. Executive Order 12898: Federal Actions
To Address Environmental Justice in
Minority Populations and Low-Income
Populations
PWALKER on PROD1PC71 with PROPOSALS3
II. Background
A. Why Is EPA Issuing This Proposed
Rule?
On April 25, 2007 (70 FR 20586), we
promulgated the Clean Air Fine Particle
Implementation Rule regarding the
Clean Air Act (CAA) requirements for
State and Tribal plans to implement the
1997 PM2.5 NAAQS. These rules require
that each State having a PM2.5
nonattainment area must submit, by
April 5, 2008, an attainment
demonstration and adopt regulations to
ensure the area will attain the standards
as expeditiously as practicable, but even
those areas for which the Administrator
determines an extension from the 2010
attainment date is appropriate may not
receive an extension later than a 2015
attainment date. The emissions
inventories and analyses used in the
attainment demonstrations must
consider filterable and condensable
fractions of PM2.5 emissions from
stationary sources that are significant
contributors of direct PM2.5 emissions.
Direct PM2.5 emissions means the solid
particles or liquid droplets emitted
directly from an air emissions source or
activity, or the gaseous emissions or
liquid droplets from an air emissions
source or activity that condense to form
PM or liquid droplets at ambient
temperatures.
The preamble to the April 25, 2007,
rule acknowledged that there remain
questions whether the available test
methods provide the most accurate
representation of primary PM emissions
even though some States have
established emissions limits for CPM.
As a result, the final rule established a
transitional period for developing
emissions limits and regulations for
condensable PM2.5. During this
transitional period, EPA has committed
to devote resources to assessing and
improving the available test methods for
CPM.
In response to this commitment and
to address the need for improved
measurement of fine PM, EPA is
proposing amendments to the following
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test methods in 40 CFR Part 51,
Appendix M (Recommended Test
Methods for State Implementation Plans
(SIPs)):
• Method 201A—Determination of
PM10 Emissions (Constant Sampling
Rate Procedure), and
• Method 202—Determination of
Condensable Particulate Emissions from
Stationary Sources.
These amendments to Method 201A
add a particle-sizing device to allow for
sampling of PM2.5, PM10, or both PM10
and PM2.5. With regard to Method 202,
we are aware that the method and the
various hardware and analytic options
described therein are sometimes applied
inappropriately, which can lead to
inaccurate and imprecise CPM
measurements. We are also aware that
Method 202 can produce inaccurate
CPM measurements when sampling
certain types of emissions sources, due
to formation of reaction artifacts. The
amendments to Method 202 revise the
sample collection and recovery
procedures of the method to provide for
more accurate and precise measurement
of CPM.
B. Particulate Matter National Ambient
Air Quality Standards
Section 108 and 109 of the CAA
govern the establishment and revision of
the NAAQS. Section 108 (42 U.S.C.
7408) directs the Administrator to
identify and list ‘‘air pollutants’’ that
‘‘in his judgment, may reasonably be
anticipated to endanger public health
and welfare’’ and whose ‘‘presence
* * * in the ambient air results from
numerous or diverse mobile or
stationary sources’’ and to issue air
quality criteria for those that are listed.
Air quality criteria are intended to
‘‘accurately reflect the latest scientific
knowledge useful in indicating the kind
and extent of identifiable effects on
public health or welfare which may be
expected from the presence of [a]
pollutant in ambient air* * *.’’ Section
109 (42 U.S.C. 7409) directs the
Administrator to propose and
promulgate primary and secondary
NAAQS for pollutants listed under
section 108 to protect public health and
welfare, respectively. Section 109 also
requires review of the NAAQS at 5-year
intervals and that an independent
scientific review committee ‘‘shall
complete a review of the criteria * * *
and the national primary and secondary
ambient air quality standards * * * and
shall recommend to the Administrator
any new * * * standards and revisions
of existing criteria and standards as may
be appropriate * * *.’’ Since the early
1980s, this independent review function
has been performed by the Clean Air
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Scientific Advisory Committee
(CASAC).
Initially EPA established the NAAQS
for PM on April 30, 1971 (36 FR 8186)
based on the original criteria document
(Department of Health, Education, and
Welfare, 1969). The reference method
specified for determining attainment of
the original standards was the highvolume sampler, which collects PM up
to a nominal size of 25 to 45 μm
(referred to as total suspended
particulates or TSP). On October 2, 1979
(44 FR 56730), EPA announced the first
periodic review of the air quality criteria
and NAAQS for PM, and significant
revisions to the original standards were
promulgated on July 1, 1987 (52 FR
24634). In that decision, EPA changed
the indicator for particles from TSP to
PM10. When that rule was challenged,
the court upheld revised standards in all
respects. Natural Resources Defense
Council v. Administrator, 902 F. 2d 962
(D.C. Cir. 1990, cert. denied, 498 U.S.
1082 (1991)).
In April 1994, EPA announced its
plans for the second periodic review of
the air quality criteria and NAAQS for
PM, and the Agency promulgated
significant revisions to the NAAQS on
July 18, 1997 (62 FR 38652). In that
decision, EPA revised the PM NAAQS
in several respects. While EPA
determined that the PM NAAQS should
continue to focus on particles less than
or equal to 10 μm in diameter (PM10),
EPA also determined that the fine and
coarse fractions of PM10 should be
considered separately. The EPA added
new standards, using PM2.5 as the
indicator for fine particles (with PM2.5
referring to particles with a nominal
mean aerodynamic diameter less than or
equal to 2.5 μm), and using PM10 as the
indicator for purposes of regulating the
coarse fraction of PM10.
Following promulgation of the 1997
PM NAAQS, petitions for review were
filed by a large number of parties,
addressing a broad range of issues. In
May 1999, a three-judge panel of the
U.S. Court of Appeals for the District of
Columbia Circuit issued an initial
decision that upheld EPA’s decision to
establish fine particle standards.
American Trucking Associations v.
EPA, 175 F.3d 1027, 1055 (D.C. Cir.
1999), reversed in part on other grounds
in Whitman v. American Trucking
Associations, 531 U.S. 457 (2001). The
Panel also found ‘‘ample support’’ for
EPA’s decision to regulate coarse
particle pollution but vacated the 1997
PM10 standards, concluding that EPA
had not provided a reasonable
explanation justifying use of PM10 as an
indicator for coarse particles. Id. at
1054–55. Pursuant to the court’s
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decision, EPA removed the vacated
1997 PM10 standards but retained the
pre-existing 1987 PM10 standards (65 FR
80776, December 22, 2000).
On October 23, 1997, EPA published
its plans for the third periodic review of
the air quality criteria and NAAQS for
PM (62 FR 55201), including the 1997
PM2.5 standards and the 1987 PM10
standards. On October 17, 2006, EPA
issued its final decisions to revise the
primary and secondary NAAQS for PM
to provide increased protection of
public health and welfare, respectively
(71 FR 61144). With regard to the
primary and secondary standards for
fine particles, EPA revised the level of
the 24-hour PM2.5 standard to 35 μg per
cubic meter (μg/m3), retained the level
of the annual PM2.5 annual standard at
15 μg/m3, and revised the form of the
annual PM2.5 standard by narrowing the
constraints on the optional use of spatial
averaging. With regard to the primary
and secondary standards for PM10, EPA
retained the 24-hour PM10 standard (150
μg/m3) and revoked the annual standard
because available evidence generally
did not suggest a link between long-term
exposure to current ambient levels of
coarse particles and health or welfare
effects.
PWALKER on PROD1PC71 with PROPOSALS3
C. Measuring PM Emissions
Section 110 of the CAA, as amended
(42 U.S.C. 7410), requires that State and
local air pollution control agencies
develop and submit plans for EPA
approval that provide for the
attainment, maintenance, and
enforcement of the NAAQS in each air
quality control region (or portion
thereof) within such State. These plans
are known as SIPs. 40 CFR part 51
(Requirements for Preparation,
Adoption, and Submittal of
Implementation Plans) specifies the
requirements for SIPs. Appendix A to
subpart A of 40 CFR part 51, defines
primary PM10 and PM2.5 as including
both the filterable and condensable
fractions of PM. Filterable PM consists
of those particles that are directly
emitted by a source as a solid or liquid
at the stack (or similar release
conditions) and captured on the filter of
a stack test train. Condensable PM is the
material that is in vapor phase at stack
conditions but which condenses and/or
reacts upon cooling and dilution in the
ambient air to form solid or liquid PM
immediately after discharge from the
stack.
Promulgation of the 1987 NAAQS
created the need for methods to quantify
PM10 emissions from stationary sources.
In response, EPA developed and
promulgated the following test methods:
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• Method 201A—Determination of
PM10 Emissions (Constant Sampling
Rate Procedure), and
• Method 202—Determination of
Condensable Particulate Emissions from
Stationary Sources.
1. Method 201A
On April 17, 1990 (56 FR 65433), EPA
promulgated Method 201A in Appendix
M of 40 CFR Part 51 to provide a test
method for measuring filterable PM10
emissions from stationary sources. In
EPA Method 201A, a gas sample is
extracted at a constant flow rate through
an in-stack sizing device which directs
particles with aerodynamic diameters
less than or equal to 10 μm to a filter.
The particulate mass collected on the
filter is determined gravimetrically after
removal of uncombined water. With the
exception of the PM10-sizing device, the
current Method 201A sampling train is
the same as the sampling train used for
EPA Method 17 of Appendix A–3 to 40
CFR Part 60.
Method 201A cannot be used to
measure emissions from stacks that have
entrained moisture droplets (e.g., from a
wet scrubber stack) since these stacks
may have water droplets that are larger
than the cut size of the PM10-sizing
device. The presence of moisture would
prevent an accurate measurement of
total PM10 since any PM10 dissolved in
larger water droplets would not be
collected by the sizing device and
would consequently be excluded in
determining the total PM10 mass. To
measure PM10 in stacks where water
droplets are known to exist, EPA’s
Technical Information Document (TID)
09 (Methods 201 and 201A in Presence
of Water Droplets), recommends use of
Method 5 of Appendix A–3 to 40 CFR
Part 60 (or a comparable method) and
consideration of the total particulate
catch as PM10 emissions.
Method 201A is also not applicable
for stacks with small diameters (i.e., 18
inches or less). The presence of the instack nozzle/cyclones and filter
assembly in a small duct will cause
significant cross-sectional area
interference and blockage leading to
incorrect flow calculation and particle
size separation. Additionally, the type
of metal used to construct the Method
201A cyclone may limit the
applicability of the method when
sampling at high stack temperatures
(e.g., stainless steel cyclones are
reported to gall and seize at
temperatures greater than 260 °C).
2. Method 202
On December 17, 1991 (56 FR 65433),
EPA promulgated Method 202 in
Appendix M of 40 CFR Part 51 to
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provide a test method for measuring
CPM from stationary sources. Method
202 uses water-filled impingers to cool,
condense, and collect materials that are
vaporous at stack conditions and
become solid or liquid PM at ambient
air temperatures. Method 202, as
promulgated, contains several optional
procedures that were intended to
accommodate the various test methods
used by State and local regulatory
entities at the time Method 202 was
being developed.
When conducted consistently and
carefully, Method 202 provides
acceptable precision for most emission
sources, and the method has been used
successfully in regulatory programs
where the emission limits and
compliance demonstrations are
established based on a consistent
application of Method 202 and its
associated options. However, when the
same emission source is tested using
different combinations of the optional
procedures, there may appear to be large
variations in the measured CPM
emissions. Additionally, during
validation of the promulgated method,
we determined that sulfur dioxide (SO2)
gas (a typical component of emissions
from several types of stationary sources)
can be absorbed partially in the
impinger solutions and can react
chemically to form sulfuric acid. This
sulfuric acid ‘‘artifact’’ is not related to
the primary emission of CPM from the
source but may be counted erroneously
as CPM when using Method 202. As we
have maintained consistently, the
artifact formation can be reduced by at
least 90 percent if a one-hour nitrogen
purge of the impinger water is used to
remove SO2 before it can form sulfuric
acid (this is our preferred application of
the Method 202 optional procedures).
Inappropriate use (or omission) of the
preferred or optional procedures in
Method 202 can increase the potential
for artifact formation.
Considering the potential for
variations in measured CPM emissions,
we believe that further verification and
refinement of Method 202 is appropriate
to minimize the potential for artifact
formation. We have performed several
studies to assess artifact formation when
using Method 202. The results of our
1998 laboratory study and field
evaluation commissioned to evaluate
the impinger approach can be found in
‘‘Laboratory and Field Evaluation of the
EPA Method 5 Impinger Catch for
Measuring Condensible Matter from
Stationary Sources’’ at the following
Internet address: https://www.epa.gov/
ttn/emc/methods/m202doc1.pdf.
Essentially, the 1998 study verified the
need for a nitrogen purge when SO2 is
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present in stack gas and also provided
guidance for analyzing the collected
samples. In 2005, an EPA contractor
conducted a second study (‘‘Laboratory
Evaluation of Method 202 to Determine
Fate of SO2 in Impinger Water’’) that
replicated some of the earlier EPA work
and addressed some additional issues.
The report of that work is available at
the following Internet address: https://
www.epa.gov/ttn/emc/methods/
m202doc2.pdf. This report also verified
the need for a nitrogen purge and
identified the primary factors that affect
artifact formation.
Also in 2005, a private testing
contractor presented a possible minor
modification to Method 202 at the Air
and Waste Management Association
(AWMA) specialty conference. The
proposed modification, described in
their presentation titled ‘‘Optimized
Method 202 Sampling Train to
Minimize the Biases Associated with
Method 202 Measurement of
Condensable Particulate Matter
Emissions,’’ involved the elimination of
water from the first impingers. The
presentation (which is available at the
following Internet address: https://
www.epa.gov/ttn/emc/methods/
m202doc3.pdf) concluded that
modification of the promulgated method
to use dry impingers resulted in a
significant additional reduction in the
sulfate artifact.
In 2006, we began to conduct
laboratory studies, in collaboration with
several stakeholders, to characterize the
artifact formation and other
uncertainties associated with
conducting Method 202 and to identify
procedures that would minimize
uncertainties when using Method 202.
Since August 2006, we have held two
workshops in Research Triangle Park,
North Carolina. These meetings were
held to present and seek comments on
our plan for evaluating potential
modifications to Method 202 that would
reduce artifact formation. Also, these
meetings were held to discuss our
progress in characterizing the
performance of the modified method,
issues that require additional
investigation, the results of our
laboratory studies, and our
commitments to extend the
investigation through stakeholders
external to EPA. We held another
meeting with experienced stack testers
and vendors of emissions monitoring
equipment to discuss hardware issues
associated with modifications of the
sampling equipment and the glassware
for the proposed CPM test method.
Summaries of the method evaluations,
as well as meeting minutes from our
workshops, can be found at the
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following Internet address: https://
www.epa.gov/ttn/emc/methods/
method202.html.
The laboratory studies that were
performed fulfill a commitment in the
preamble to the Clean Air Fine Particle
Implementation Rule (72 FR 20586,
April 25, 2007) to examine the
relationship between several critical
CPM sampling and analysis parameters
and, to the extent necessary, propose
revisions to incorporate improvements
in the method. While these
improvements in the stationary source
test method for CPM will provide for
more accurate and precise measurement
of all PM, the addition of PM2.5 as an
indicator of health and welfare effects
by the 1997 NAAQS revisions generates
the need to quantify PM2.5 emissions
from stationary sources. To respond to
this need, we are proposing revisions to
incorporate this capability into the test
method for filterable PM10.
III. This Action
This action proposes to provide the
capability of measuring PM2.5 using
Method 201A and to provide for more
accurate measurement of the filterable
and condensable components of fine PM
(particles with mean aerodynamic
diameters less than or equal to 2.5 m)
and coarse PM (particles with mean
aerodynamic diameters less than or
equal to 10 m) when using Method 202.
Method 201A proposed amendments
would add a particle-sizing cyclone to
the sampling train. Method 202
proposed amendments would reduce
the formation of sulfuric acid artifact by
at least an additional 90 percent
(compared to our recommended
procedures for the existing Method 202),
provide for greater consistency between
testing contractors in method
application, improve the precision of
the method, and provide for more
accurate quantification of direct (i.e.,
primary) PM emissions to the ambient
air (the method will not measure
secondarily-formed PM). The proposed
amendments would also affect the
measurement of total PM, PM10, and
PM2.5. Additionally, we are proposing to
revise the format of Methods 201A and
202 to be consistent with the format
developed by EPA’s Environmental
Monitoring Management Council
(EMMC). A guidance document
describing the EMMC format can be
found at the following Internet address:
https://www.epa.gov/ttn/emc/guidlnd/
gd-045.pdf.
A. What Are the Proposed Amendments
to Method 201A?
On July 18, 1997 (62 FR 38652), we
revised the NAAQS for PM to add new
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standards for fine particles, using PM2.5
as the indicator. This action will modify
the current Method 201A sampling train
configuration to allow for measurement
of filterable PM10, filterable PM2.5, or
both filterable PM10 and filterable PM2.5
from stationary sources. These
amendments combine the existing
method with the PM2.5 cyclone to create
a sampling train that includes a total of
two cyclones (one cyclone to size
particles with aerodynamic diameters
greater than 10 m and one cyclone to
size particles with aerodynamic
diameters greater than 2.5 m) and a final
filter to collect particles with
aerodynamic diameters less than or
equal to 2.5 m. The PM2.5 cyclone would
be inserted between the PM10 cyclone
and the filter of the Method 201A
sampling train.
We are not proposing any
amendments to address the use of this
method when the stack gas has
entrained moisture or when the method
is used for stack gases with high
temperatures. In July 1979, we
published a research document (EPA–
600/7–79–166) to report the preliminary
development of a method for measuring
and characterizing the particles in the
vent stream from a wet scrubber used to
control sulfur oxide emissions. The
method was based on the use of a
heated, electrified wire placed in the
vent stream. When a water droplet
impacted the wire, the electric current
flowing through the wire was attenuated
in proportion to the size of the water
droplet. We decided it was not
appropriate to promulgate the
preliminary method and, at this time,
we are not aware of any commerciallyavailable equipment that can determine
the aerodynamic size of PM contained
in, or dissolved in, liquid water droplets
as they would exist in the ambient air
following release and evaporation in the
ambient air. While we are aware of
several optical aerosol droplet
spectrometers for measuring the size
distribution of liquid droplets in
exhaust gases, we are not aware of any
commercial instruments that can
measure size distributions of particles
emitted from stationary sources. We also
lack knowledge on the relative effects of
solids concentration in the liquid
droplets and the possible presence of
dry particles in addition to the liquid
droplets. Consequently, we recommend
the use of EPA Method 5 (40 CFR Part
60, Appendix A–3—Determination of
Particulate Matter Emissions from
Stationary Sources) when measuring PM
in stacks with saturated water vapors
containing entrained water droplets.
With this application of EPA Method 5,
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all of the collected material would be
considered PM2.5.
B. What Are the Proposed Amendments
to Method 202?
This action proposes amendments
incorporating modifications that would
reduce the formation of artifacts at both
low and high concentrations of SO2 in
the sample gas stream. The
modifications were developed based on
the method evaluations discussed in
Section II.C.2 of this preamble.
Method 202, as promulgated in 1991,
is a set of sampling procedures for
collecting PM in water-filled impingers
and a set of sample recovery procedures
that are performed on the water
following its collection. The water-filled
impingers are nearly identical to the
four chilled impingers used in standard
stationary source sampling trains for PM
(e.g., Method 5 and Method 17 of
Appendix A–3 and A–6, 40 CFR Part
60). In principle, CPM is collected in the
impinger portion of a Method 17-type
sampling train. Our preferred operation
of the promulgated method requires that
the impinger contents be purged with
nitrogen after the test run to remove
dissolved SO2 gas from the impinger
contents. The impinger solution is then
extracted with methylene chloride to
separate the organic CPM from the
inorganic CPM. The organic and
aqueous fractions are then dried and the
residues weighed. The sum of both
fractions represents the total CPM.
These proposed amendments to
Method 202 sampling train and sample
recovery procedures would achieve at
least an additional 90 percent reduction
in sulfuric acid artifact formation
compared to the current Method 202
using the nitrogen purge option, provide
testing contractors with a more
standardized application of the method,
improve the precision of the method,
and quantify more accurately direct PM
emission to the ambient air.
The proposed changes to the sampling
train of this method include:
• Installing a condenser between the
filter in the front-half of the sample train
and the first impinger to cool the sample
gases to ambient temperature (less than
30 °C);
• Installing a recirculation pump in
the ambient water bath to supply
cooling water to the condenser;
• Changing the first two impingers
from wet to dry, and placing these two
dry impingers in a water bath at ambient
temperature (less than 30 °C) (the first
dry impinger will use a short-stem
insert, and the second dry impinger will
use a long-stem insert);
• Requiring the use of an out-of-stack,
low-temperature filter (i.e., the CPM
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filter), as described in EPA Method 8,
between the second and third impingers
(a Teflon filter is used in place of the
fiberglass filter described in EPA
Method 8); and
• Requiring that the temperature of
the sample gas drawn through the CPM
filter be maintained at ambient
temperature (less than 30 °C).
It should be noted that under Method
202, the use of a CPM filter is an
optional procedure that is used typically
if the collection efficiency of the
impinger is suspected to be low. These
proposed amendments would make the
use of a CPM filter a required procedure.
The proposed changes to Method 202
include:
• Extracting the CPM filter with water
and organic solvent;
• Evaporating the liquid collected in
the impingers in an oven or on a hot
plate down to a minimum volume of 10
milliliters, instead of all the way to
dryness;
• Evaporating the remaining liquid to
dryness at ambient temperature prior to
neutralization with ammonium
hydroxide;
• Titrating the reconstituted residue
with 0.1 normal ammonium hydroxide
and a pH meter;
• Evaporating the neutralized liquid
to a minimum volume of 10 milliliters
in an oven or hot plate;
• Evaporating the final volume to
dryness at ambient temperature; and
• Weighing the CPM sample residue
to constant weight after allowing a
minimum of 24 hours for equilibration
in a desiccator.
Note that the requirements to evaporate
liquids at ambient temperature and to
titrate the reconstituted liquid exist
already as options under this method.
These optional steps are typically
performed to retain CPM that might be
lost at higher evaporation temperatures.
Under these proposed amendments,
these options would be required
procedures.
C. How Will the Proposed Amendments
to Methods 201A and 202 Affect
Existing Emission Inventories, Emission
Standards, and Permit Programs?
We anticipate that, over time, the
changes in the test methods proposed in
this action will result in, among other
positive outcomes, more accurate
emissions inventories of direct PM
emissions and emissions standards that
are more indicative of the actual impact
of the source on the ambient air quality.
Accurate emission inventories are
critical for regulatory agencies to
develop the control strategies and
demonstrations necessary to attain air
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quality standards. If implemented, the
proposed test method revisions would
have the potential to improve our
understanding of PM emissions due to
the increased availability of more
accurate emission tests and, eventually,
through the incorporation of less biased
test data into existing emissions factors.
For CPM, the use of the proposed
method would likely reveal a reduced
level of CPM emissions from a source
compared to the emissions that would
have been measured using Method 202,
as typically performed. However, there
may be some cases where the proposed
test method would reveal an increased
level of CPM emissions from a source,
depending on the relative emissions of
filterable and CPM emissions from the
source. For example, the existing
Method 202 allows complete
evaporation of the water containing
inorganic PM at 105 °C (221 °F), where
the proposed revision requires the last
10 ml of the water to be evaporated at
room temperature (not to exceed 30 °C
(85 °F)) thereby retaining the CPM that
would evaporate at the increased
temperature.
Prior to our adoption of the 1997
PM2.5 NAAQS, several State and local
air pollution control agencies had
developed emission inventories that
included CPM. Additionally, some
agencies established enforceable CPM
emissions limits or otherwise required
that PM emissions testing include
measurement of CPM. While this
approach was viable in cases where the
same test method was used to develop
the CPM regulatory limits and to
demonstrate facility compliance, there
are substantial inconsistencies within
and between States regarding the
completeness and accuracy of CPM
emission inventories and the test
methods used to measure CPM
emissions and to demonstrate facility
compliance.
These amendments would serve to
mitigate the potential difficulties that
can arise when we and other regulatory
entities attempt to use the test data from
State and local agencies whose CPM test
methods are inconsistent to develop
emission factors, determine program
applicability, or to establish emissions
limits for CPM emission sources within
a particular jurisdiction. For example,
problems can arise when the test
method used to develop a CPM
emission limit is not the same as the test
method specified in the rule for
demonstrating compliance because the
different test methods may quantify
different components of PM (e.g.,
filterable versus condensable). Also,
when emissions from State inventories
are modeled to assess compliance with
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the NAAQS, the determination of direct
PM emissions may be biased high or
low, depending on the test methods
used to estimate PM emissions, and the
atmospheric conversion of SO2 to
sulfates (or SO3) may be inaccurate or
double-counted. Additionally, some
State and local regulatory authorities
have assumed that EPA Method 5 of
Appendix A–3 to 40 CFR Part 60
(Determination of Particulate Matter
Emissions from Stationary Sources)
provides a reasonable estimate of PM10
emissions. This assumption is incorrect
because Method 5 does not provide
particle sizing of the filterable
component and does not quantify
particulate caught in the impinger
portion of the sampling train. Similar
assumptions for measurements of PM2.5
will result in greater inaccuracies.
With regard to State permitting
programs, we recognize that, in some
cases, existing Best Available Control
Technology (BACT), Lowest Achievable
Emission Rate (LAER), or Reasonably
Available Control Technology (RACT)
limits have been based on an identified
control technology, and that the data
used to determine the performance of
that technology and establish the limits
may have focused on filterable PM and
thus did not completely characterize PM
emissions to the ambient air. While the
source test methods used by State
programs that developed the applicable
permit limit may not have fully
characterized the PM emissions, we
have no information that would indicate
that the test methods are inappropriate
indicators of the control technologies’
performance for the portion of PM
emissions that was addressed by the
applicable requirement. As promulgated
in the Clean Air Fine Particle
Implementation Rule, after January 1,
2011, States are required to consider
inclusion of CPM emissions in new or
revised emissions limits which they
establish. We will defer to the
individual State’s judgment as to
whether, and at what time, it is
appropriate to revise existing facility
emission limits or operating permits to
incorporate information from the
revised CPM test method when it is
promulgated.
With regard to operating permits, the
Title V permit program does not
generally impose new substantive air
quality control requirements. In general,
once emissions limits are established as
CAA requirements under the SIP or a
SIP-approved pre-construction review
permit, they are included in the Title V
permits. Obviously, Title V permits may
have to be updated to reflect any
revision of existing emission limits or
new emission limits created in the
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context of the underlying applicable
requirements. Also, if a permit contains
the previously promulgated test
methods, it is not a given that the permit
would always have to be revised should
these test methods changes be finalized
(e.g., where test methods are
incorporated into existing permits
through incorporation by reference, no
permit terms or conditions would
necessarily have to change to reflect
changes to those test methods). In any
event, the need for action in the
permitting context due to these
proposed changes to the test methods
would be controlled by several factors,
such as the exact wording of the existing
operating permit, the requirements of
the EPA-approved SIP, and any changes
that may be made to pre-construction
review permits with respect to a
particular source test method that did
not include CPM or on a set of
procedures in Method 202 which
underestimated emissions.
In recognition of these issues, the
Clean Air Fine Particle Implementation
Rule contains provisions establishing a
transition period for developing
emission limits for condensable direct
PM2.5 that are needed to demonstrate
attainment of the PM2.5 NAAQS. As
discussed in the April 25, 2007, Clean
Air Fine Particle Implementation Rule
(72 FR 20586) and in the May 16, 2008,
promulgation of the New Source Review
Program Implementation for fine
particulate matter (73 FR 28321), the
transition period, which ends January 1,
2011, allows time to resolve and adopt
appropriate testing procedures for CPM
emissions and to collect total primary
(filterable and condensable) PM2.5
emissions data that are more
representative of the emissions of each
source in their areas. In the PM2.5 NSR
Implementation Rule, we stated that as
part of this test methods rulemaking, we
would ‘‘take comment on an earlier
closing date for the transition period in
the NSR program if we are on track to
meet our expectation to complete the
test method rule much earlier than
January 1, 2011.’’ See 73 FR at 28344.
Accordingly, we are hereby soliciting
comments on ending the NSR transition
period for CPM on a date 60 to 90 days
after the promulgation date of this test
methods rulemaking.
During the transition period, we are
available to provide technical support to
States, as requested, in establishing
emissions testing requirements. We will
also solicit the involvement of
interested stakeholders to collect new
direct filterable and CPM emissions data
using methodologies that provide more
representative data of a source’s direct
PM2.5 emissions. These data will be
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used by us, States, and others to
improve emissions factors and to help
establish or revise source emissions
limits in implementation plans. The
transition period will also provide time
for additional method evaluations.
During the transition period, we expect
that some States will continue to
develop more complete inventories of
direct PM2.5 emissions, particularly for
CPM. As needed to demonstrate
attainment of the PM NAAQS, we also
expect States to address the control of
direct PM2.5 emissions, including CPM,
with any new actions taken after
January 1, 2011 and to address CPM
emissions in any direct PM2.5
regulations or limits developed under
any new PM NAAQS.
As with other methods, any new
procedures approved by us will produce
data that will be incorporated into the
tools (e.g., emission factors, emission
inventories, air quality modeling) used
to assess the attainment of air quality
standards. However, we do not believe
that it is necessary to update continually
the assessment tools or revise previous
air quality analyses until evidence is
presented that a mid-course corrective
action is needed to achieve the air
quality standards (a mid-course review
is required by April 2011 for each area
with an approved attainment date in
2014 or 2015). At that time, updated
inventories and air quality models may
be needed to identify and characterize
the emission sources that are impeding
adequate progress towards attaining the
air quality standards. Additionally, the
new test data could be used to improve
the applicability and performance
evaluations of various control
technologies.
D. Request for Comments
We encourage stakeholders to
continue to participate in the process to
refine Methods 201A and 202. We are
requesting public comments on all
aspects of the proposed test methods.
EPA has already engaged several
stakeholder groups as described in
Section II.C of this preamble.
Stakeholders and other members of the
public who have not yet participated are
encouraged to submit comments. EPA is
soliciting as many constructive
comments as possible in order to make
the most appropriate changes to the
methods.
We are specifically interested in
recommended alternatives to replace
what we have proposed. When
submitting comments on alternative
approaches, please submit supporting
information to substantiate the
improvements that are achieved with
your recommendation. For
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recommended changes to the
procedures, include supporting
technical data and any associated cost
information. For example, if you are
proposing an alternative procedure,
include data or information that would
demonstrate how the alternative
procedure would equal or improve the
bias and precision of the proposed
methods. In addition, provide data or
cost information that would show the
cost implications to testing companies
and analytical laboratories of
implementing the alternative procedure.
Although our request for comments is
not limited to these items, the following
are examples of items for which we are
specifically requesting comment.
1. Items Associated With Both Test
Methods
The proposed test methods are based
upon EPA’s assessment of comments
made on the Clean Air Fine Particle
Implementation Rule (April 25, 2007, 70
FR 20586). Commenters expressed that
there is an overarching need for test
methods that are unbiased with respect
to primary particulate matter emissions
to the atmosphere and that the test
methods must provide a high degree of
consistency (precision) in these
measurements. As a result, we reduced
the numerous options and alternative
procedures in the existing methods to a
single set of prescriptive procedures that
already existed within the methods. In
addition, we made a few minor changes
to reduce further the bias caused by
sulfate artifacts. We are requesting
comments on the specific set of
procedures we have proposed and any
replacement procedures that would be
less demanding but that would achieve
or improve bias and precision. We are
also requesting comments on our
decision to eliminate options or
alternatives within the existing methods
that may not achieve comparable
results. If we were to consider
alternative procedures that may not
achieve comparable results, then what
level of difference would be acceptable?
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2. Items Associated With Method 201A
Regarding this proposed method,
stakeholders have commented on the
sample duration that would be required
to collect a weighable mass. EPA is
requesting comments on alternative
methodologies or hardware that would
reduce the sample duration in order to
reach a reasonable detection limit or to
demonstrate that emissions are below
the regulatory limit. Commenters should
provide information or data, including
cost information, which supports their
recommendation.
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Stakeholders have expressed concern
about the configuration and size of the
proposed sampling train. Specifically,
commenters have expressed concern
that the size and length of the combined
PM10 cyclone and the PM2.5 cyclone and
filter require larger port opening(s) and
a very large stack cross section to
minimize blockage. In addition,
stakeholders have stated that it is
difficult to maintain stack temperature
in the sampling train. Therefore, EPA
requests comments on alternatives to
the proposed procedures or hardware.
EPA requests comments on alternative
procedures or configurations that would
reduce the blockage. EPA also requests
comments on alternative configurations
that would allow testers to maintain
stack temperature in the sampling train,
thus reducing or eliminating
condensation in the primary or filterable
particulate portions of the method.
Recommendations to revise the
sampling train size or configuration
should include an assessment of the
impacts of the recommended revisions
on the sample size, required sample
duration, and ability to collect a
representative sample. Commenters
should provide information or data,
including cost information that supports
their recommendation.
3. Items Associated With Method 202
Stakeholders originally expressed
concern about the formation of artifacts
in Method 202 when sulfur dioxide was
present in the stack gas. Based on
laboratory experiments, the proposed
revision to Method 202 eliminates at
least an additional 90 percent of the
artifact over the best practices
procedures of the existing Method 202.
In addition, the laboratory experiments
show that the proposed revision to
Method 202 reduces artifact at or below
the detection limits of the method. EPA
requests comments on any further
concerns with the formation of artifacts
in the proposed method.
Stakeholders have expressed concern
about glassware cleaning. Specifically,
stakeholders have questioned the
requirement to bake glassware at 300 °C
for 6 hours prior to use in order to
reduce the background level of CPM.
Stakeholders have stated that many
stack testing firms and some analytical
laboratories may not have ovens that
can achieve this temperature. EPA
requests information on the
performance of a lower temperature
oven in effectively reducing the blank
level of CPM.
Another stakeholder concern is
whether glassware needs to be
completely cleaned between sampling
runs. The proposed method requires
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clean glassware at the start of each new
source category test. EPA requests
comments on alternatives that would
minimize the cost of glassware
preparation and reduce bias due to
carryover from tests at the same source
category and between source categories.
Commenters should submit data or
information to demonstrate that their
alternative procedure would reduce or
minimize the carryover or blank and
would minimize the cost to prepare
glassware.
Stakeholders expressed concern about
the need for Method 202 following
filtration at less than 30 °C (85 °F). EPA
requests comments on how to clarify
when Method 202 is or is not required.
Stakeholders have expressed concern
about the appropriate type of CPM filter
required by the proposed method. EPA
requests comments on the construction
material and porosity of the filter.
Commenters should address the capture
efficiency required by the method (i.e.,
the filter must have an efficiency of at
least 99.95 percent (<0.05 percent
penetration) on 0.3 micron particles).
Commenters should include how their
alternative would minimize the blank
contribution from the filters.
Commenters have expressed concern
about the additional analytical steps
required to process the CPM filter. The
proposed method requires extraction
and combination of the filter extract
with the appropriate impinger samples
to accurately collect and measure
sulfuric acid and other condensable
material. Commenters should address
alternative procedures for CPM filter
analysis that would generate precise and
unbiased analysis of CPM collected on
the CPM filter.
Stakeholders have expressed concern
about maintaining the stack gas flow
through the Teflon® membrane filter.
Stakeholders have commented on their
need to use a supplementary support
filter to maintain flow through the
sample filter. EPA requests comments
regarding the use of a support filter that
would help maintain stack gas flow
while minimizing or eliminating the
support filter’s contribution to the
sample mass. EPA requests comments
on the use of this alternative and its
potential impact on bias and precision,
as well as its potential impact on cost.
IV. Statutory and Executive Order
Reviews
A. Executive Order 12866: Regulatory
Planning and Review
Under Executive Order (EO) 12866
(58 FR 51735, October 4, 1993), this
proposed action is a ‘‘significant
regulatory action’’ since it raises novel
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legal or policy issues arising out of legal
mandates, the President’s priorities, or
the principles set forth in this Executive
Order. Accordingly, EPA submitted this
proposed action to the Office of
Management and Budget (OMB) for
review under Executive Order 12866
and any changes made in response to
OMB recommendations have been
documented in the docket for this
action.
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B. Paperwork Reduction Act
This proposed action does not impose
an information collection burden under
the provisions of the Paperwork
Reduction Act, 44 U.S.C. 3501 et seq.
Burden is defined at 5 CFR 1320.3(b).
The proposed amendments do not
contain any reporting or recordkeeping
requirements. The proposed
amendments revise two existing source
test methods to allow one method to
perform additional particle sizing at 2.5
micrometers and to improve the
precision and accuracy of the other test
method.
C. Regulatory Flexibility Act
The Regulatory Flexibility Act (RFA)
generally requires an agency to prepare
a regulatory flexibility analysis of any
rule subject to notice and comment
rulemaking requirements under the
Administrative Procedure Act or any
other statute unless the agency certifies
that the rule will not have a significant
economic impact on a substantial
number of small entities. Small entities
include small businesses, small
organizations, and small governmental
jurisdictions.
For purposes of assessing the impacts
of this rule on small entities, small
entity is defined as: (1) A small business
as defined by the Small Business
Administration’s (SBA) regulations at 13
CFR 121.201; (2) a small governmental
jurisdiction that is a government of a
city, county, town, school district or
special district with a population of less
than 50,000; and (3) a small
organization that is any not-for-profit
enterprise which is independently
owned and operated and is not
dominant in its field.
After considering the economic
impacts of this proposed rule on small
entities, I certify that this action will not
have a significant economic impact on
a substantial number of small entities.
We do not anticipate that the proposed
changes to Methods 201A and 202 will
result in a significant economic impact
on small entities. Most of the emission
sources that will be required by State
regulatory agencies (and Federal
regulators after 2011) to conduct tests
using the revised methods are those that
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have PM emissions of 100 tons per year
or more. EPA expects that few, if any,
of these emission sources will be small
entities.
Although this proposed rule will not
have a significant economic impact on
a substantial number of small entities,
EPA nonetheless has tried to reduce the
impact of this rule on small entities. In
this preamble, we explained that this
rule does not require any entities to use
these proposed test methods. Such a
requirement would be mandated by a
separate independent regulatory action.
We indicated that upon promulgation of
this rule, some entities may be required
to use these test methods as a result of
existing permits or regulations. Since
the cost to use the proposed test
methods is comparable to the cost of the
methods they replace, little or no
significant economic impact to small
entities will accompany the increased
precision and accuracy of the revised
test methods which are proposed. We
also indicated that after January 1, 2011,
when the transition period established
in the Clean Air Fine Particle
Implementation Rule expires, States are
required to consider inclusion of
pollutants measured by these test
methods in new or revised regulations.
The economic impacts caused by any
new or revised State regulations for fine
PM would be associated with those
State rules and not with this proposal to
modify the existing test methods.
Consequently, we believe that this rule
imposes little if any adverse economic
impact to small entities. However, we
continue to be interested in the
potential impacts of the proposed rule
on small entities and welcome
comments on issues related to such
impacts.
D. Unfunded Mandates Reform Act
This rule does not contain a Federal
mandate that may result in expenditures
of $100 million or more for State, local,
and tribal governments, in the aggregate,
or the private sector in any one year.
The incremental costs associated with
conducting the revised test methods
(expected to be less than $1,000 per test)
do not impose a significant burden on
sources. Thus, this rule is not subject to
the requirements of sections 202 and
205 of the UMRA.
This rule is also not subject to the
requirements of section 203 of UMRA
because it contains no regulatory
requirements that might significantly or
uniquely affect small governments. The
low incremental cost associated with
the revised test methods mitigates any
significant or unique effects on small
governments.
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E. Executive Order 13132: Federalism
Executive Order 13132, entitled
‘‘Federalism’’ (64 FR 43255, August 10,
1999), requires EPA to develop an
accountable process to ensure
‘‘meaningful and timely input by State
and local officials in the development of
regulatory policies that have federalism
implications.’’ ‘‘Policies that have
federalism implications’’ is defined in
the Executive Order to include
regulations that have ‘‘substantial direct
effects 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.’’
This proposed rule does not have
federalism implications. It will not have
substantial direct effects 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, as specified in
Executive Order 13132. In cases where
a source of PM2.5 emissions is owned by
a State or local government, those
governments may incur a minimal
compliance costs associated with
conducting tests to quantify PM2.5
emissions using the revised methods
when they are promulgated. However,
such tests would be conducted at the
discretion of the State or local
government and the compliance costs
are not expected to impose a significant
burden on those governments. Thus,
Executive Order 13132 does not apply
to this rule.
In the spirit of Executive Order 13132,
and consistent with EPA policy to
promote communications between EPA
and State and local governments, EPA
specifically solicits comment on this
proposed rule from State and local
officials.
F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
This action does not have tribal
implications, as specified in Executive
Order 13175 (65 FR 67249, November 9,
2000). In cases where a source of PM2.5
emissions is owned by a tribal
government, those governments may
incur minimal compliance costs
associated with conducting tests to
quantify PM2.5 emissions using the
revised methods when they are
promulgated. However, such tests
would be conducted at the discretion of
the tribal government and the
compliance costs are not expected to
impose a significant burden on those
governments. Thus, Executive Order
13175 does not apply to this action.
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EPA specifically solicits additional
comment on this proposed rule from
tribal officials.
G. Executive Order 13045: Protection of
Children From Environmental Health
and Safety Risks
EPA interprets EO 13045 (62 FR
19885, April 23, 1997) as applying only
to those regulatory actions that concern
health or safety risks, such that the
analysis required under section 5–501 of
the EO has the potential to influence the
regulation. This action is not subject to
EO 13045 because it does not establish
an environmental standard intended to
mitigate health or safety risks.
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H. Executive Order 13211: Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use
This action is not a ‘‘significant
energy action’’ as defined in Executive
Order 13211 (66 FR 28355 (May 22,
2001)), because it is not likely to have
a significant adverse effect on the
supply, distribution, or use of energy.
This rule revises existing EPA test
methods and does not affect energy
supply, distribution, or use.
I. National Technology Transfer and
Advancement Act
Section 12(d) of the National
Technology Transfer and Advancement
Act of 1995 (‘‘NTTAA’’), Public Law
104–113 (15 U.S.C. 272 note) directs
EPA to use voluntary consensus
standards (VCS) in its regulatory
activities unless to do so would be
inconsistent with applicable law or
otherwise impractical. Voluntary
consensus standards are technical
standards (e.g., materials specifications,
test methods, sampling procedures, and
business practices) that are developed or
adopted by voluntary consensus
standards bodies. NTTAA directs EPA
to provide Congress, through OMB,
explanations when the Agency decides
not to use available and applicable
voluntary consensus standards.
The rulemaking involves technical
standards. Therefore, the Agency
conducted a search to identify
potentially applicable voluntary
consensus standards. However, we
identified no such standards, and none
were brought to our attention in
comments. Therefore, EPA has decided
to amend portions of existing EPA test
methods. While no comprehensive
source test methods were identified,
EPA identified two VCS which were
applicable for use within the amended
test methods. The first VCS cited in this
proposal is American Society for
Testing and Materials (ASTM) Method
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D2986–95a (1999), ‘‘Standard Method
for Evaluation of Air, Assay Media by
the Monodisperse DOP (Dioctyl
Phthalate) Smoke Test,’’ for its
procedures to conduct filter efficiency
tests. The second VCS cited in this
proposed rule is ASTM D1193–06,
‘‘Standard Specification for Reagent
Water,’’ for the proper selection of
distilled ultra-filtered water. These VCS
are available from the American Society
for Testing and Materials, 100 Barr
Harbor Drive, Post Office Box C700,
West Conshohocken, PA 19428–2959.
EPA welcomes comments on this
aspect of the proposed rulemaking and,
specifically, invites the public to
identify potentially applicable VCS and
to explain why such standards should
be used in this regulation.
J. Executive Order 12898: Federal
Actions To Address Environmental
Justice in Minority Populations and
Low-Income Populations
Executive Order (EO) 12898 (59 FR
7629, February 16, 1994) establishes
federal executive policy on
environmental justice. Its main
provision directs federal agencies, to the
greatest extent practicable and
permitted by law, to make
environmental justice part of their
mission by identifying and addressing,
as appropriate, disproportionately high
and adverse human health or
environmental effects of their programs,
policies, and activities on minority
populations and low-income
populations in the United States.
EPA has determined that this
proposed rule will not have
disproportionately high and adverse
human health or environmental effects
on minority or low-income populations
because it does not affect the level of
protection provided to human health or
the environment. The proposed
amendments revise existing test
methods to improve the accuracies of
the measurements which are expected
to improve environmental quality and
reduce health risks for areas that may be
designated as nonattainment.
List of Subjects in 40 CFR Part 51
Administrative practice and
procedure, Air pollution control, Carbon
monoxide, Incorporation by reference,
Intergovernmental relations, Lead,
Nitrogen oxide, Ozone, Particulate
matter, Reporting and recordkeeping
requirements, Sulfur compounds,
Volatile organic compounds.
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Dated: March 16, 2009.
Lisa P. Jackson,
Administrator.
For the reasons set out in the
preamble, title 40, chapter I of the Code
of Federal Regulations is proposed to be
amended as follows:
PART 51—[AMENDED]
1. The authority citation for part 51
continues to read as follows:
Authority: 23 U.S.C. 101; 42 U.S.C 7401–
7671q.
2. Amend Appendix M by revising
Methods 201A and 202 to read as
follows:
Appendix M to Part 51—Recommended
Test Methods for State Implementation
Plans
*
*
*
*
*
METHOD 201A—DETERMINATION OF
PM10 AND PM2.5 EMISSIONS FROM
STATIONARY SOURCES (Constant
Sampling Rate Procedure)
1.0 Scope and Applicability
1.1 Scope. The U.S. Environmental
Protection Agency (U.S. EPA or ‘‘we’’)
developed this method to describe the
procedures that the stack tester (‘‘you’’) must
follow to measure particulate matter
emissions equal to or less than a nominal
aerodynamic diameter of 10 micrometer
(PM10) and 2.5 micrometer (PM2.5). If the gas
filtration temperature exceeds 30 °C (85 °F),
this method includes procedures to measure
only filterable particulate matter (material
that does not pass through a filter or a
cyclone/filter combination). If the gas
filtration temperature exceeds 30 °C (85 °F),
and you must measure total primary (direct)
particulate matter emissions to the
atmosphere, both the filterable and
condensable (material that condenses after
passing through a filter) components, then
you must combine the procedures in this
method with the procedures in Method 202
for measuring condensable particulate
matter. However, if the gas filtration
temperature never exceeds 30 °C (85 °F), then
use of Method 202 is not required to measure
total primary particulate matter.
1.2 Applicability. You can use this
method to measure filterable particulate
matter from stationary sources only.
Filterable particulate matter is collected instack with this method (i.e., the method
measures materials that are solid or liquid at
stack conditions).
1.3 Responsibility. You are responsible
for obtaining the equipment and supplies you
will need to use this method. You must also
develop your own procedures for following
this method and any additional procedures to
ensure accurate sampling and analytical
measurements.
1.4 Results. To obtain results, you must
have a thorough knowledge of the following
test methods that are found in Appendices
A–1 through A–3 of 40 CFR Part 60.
(a) Method 1—Sample and Velocity
Traverses for Stationary Sources.
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(b) Method 2—Determination of Stack Gas
Velocity and Volumetric Flow Rate (Type S
Pitot Tube).
(c) Method 3—Gas Analysis for the
Determination of Dry Molecular Weight.
(d) Method 4—Determination of Moisture
Content in Stack Gases.
(e) Method 5—Determination of Particulate
Matter Emissions from Stationary Sources.
1.5 Additional Methods. We do not
anticipate that you will need additional test
methods to measure ambient contributions of
particulate matter to source emissions
because ambient contributions are
insignificant for most of the sources that are
expected to be measured using this test
method. However, when an adjustment for
the ambient air particulate matter is needed,
use the ambient air reference methods to
quantify the ambient air contribution. If the
source gas filtration temperature never
exceeds 30 °C (85 °F) and condensable
particulate is not measured by Method 202,
then the correction for ambient particulate
matter must be adjusted for condensable
material that vaporizes at the process
temperature.
1.6 Limitations. You cannot use this
method to measure emissions following a wet
scrubber because this method is not
applicable for in-stack gases containing water
droplets. To measure PM10 and PM2.5 in
emissions where water droplets are known to
exist, we recommend that you use Method 5.
This method may not be suitable for sources
with stack gas temperatures exceeding 260 °C
(500 °F). You may need to take extraordinary
measures—including the use of specialty
metals (e.g., Inconel) to achieve reliable
particulate mass since the threads of the
cyclones may gall or seize, thus preventing
the recovery of the collected particulate
matter and rendering the cyclone unusable
for subsequent use.
1.7 Conditions. You can use this method
to obtain both particle sizing and total
filterable particulate if the isokinetics are
within 90–110 percent, the number of
sampling points is the same as Method 5 or
17, and the in-stack filter temperature is
within the acceptable range. The acceptable
range for the in-stack filter temperature is
generally defined as the typical range of
temperature for emission gases. The
acceptable range varies depending on the
source and control technology. To satisfy
Method 5 criteria, you may need to remove
the in-stack filter and use an out-of-stack
filter and recover the PM in the probe
between the PM2.5 particle sizer and the
filter. In addition, to satisfy Method 5 and
Method 17 criteria, you may need to sample
from more than 12 traverse points. Be aware
that this method determines in-stack PM10
and PM2.5 filterable emissions by sampling
from a recommended maximum of 12 sample
points, at a constant flow rate through the
train (the constant flow is necessary to
maintain the size cuts of the cyclones), and
with a filter that is at the stack temperature.
In contrast, Method 5 or Method 17 trains are
operated isokinetically with varying flow
rates through the train. Method 5 and Method
17 require sampling from as many as 24
sample points. Method 5 uses an out-of-stack
filter that is maintained at a constant
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temperature of 120 °C (248 °F). Further, to
use this method in place of Method 5 or
Method 17, you must extend the sampling
time so that you collect the minimum mass
necessary for weighing on each portion of
this sampling train. Also, if you are using this
method as an alternative to a required
performance test, then you must receive
approval from the appropriate authorities
prior to conducting the test.
2.0 Summary of Method
2.1 Summary. To measure PM10 and
PM2.5, extract a sample of gas at a
predetermined constant flow rate through an
in-stack sizing device. The sizing device
separates particles with nominal
aerodynamic diameters of 10 microns and 2.5
microns. To minimize variations in the
isokinetic sampling conditions, you must
establish well-defined limits. Once a sample
is obtained, remove uncombined water from
the particulate, then use gravimetric analysis
to determine the particulate mass for each
size fraction. Changes in the original Method
201A of Appendix M to 40 CFR part 51,
supplement the filterable particulate
procedures with the PM2.5 cyclone from a
conventional five-stage cascade cyclone train.
The addition of a PM2.5 cyclone between the
PM10 cyclone and the stack temperature filter
in the sampling train supplements the
measurement of PM10 with the measurement
of fine particulate matter. Without the
addition of the PM2.5 cyclone, the filterable
particulate portion of the sampling train may
be used to measure total and PM10 emissions.
Likewise, with the exclusion of the PM10
cyclone, the filterable particulate portion of
the sampling train may be used to measure
total and PM2.5 emissions. Figure 1 of Section
17 presents the schematic of the sampling
train configured with these changes.
3.0 Definitions
[Reserved]
4.0 Interferences
You cannot use this method to measure
emissions following a wet scrubber because
this method is not applicable for in-stack
gases containing water droplets. Stacks with
entrained moisture droplets may have water
droplets larger than the cut sizes for the
cyclones. These water droplets normally
contain particles and dissolved solids that
become PM10 and PM2.5 following
evaporation of the water.
5.0 Safety
Disclaimer: You may have to use
hazardous materials, operations, and
equipment while using this method. We do
not provide information on appropriate
safety and health practices. You are
responsible for determining the applicability
of regulatory limitations and establishing
appropriate safety and health practices.
Handle materials and equipment properly.
6.0 Equipment and Supplies
Figure 2 of Section 17 shows details of the
combined cyclone heads used in this
method. The sampling train is the same as
Method 17 of Appendix A–6 to Part 60 with
the exception of the PM10 and PM2.5 sizing
devices. The following sections describe the
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sampling train’s primary design features in
detail.
6.1 Filterable Particulate Sampling Train
Components.
6.1.1 Nozzle. You must use stainless steel
(316 or equivalent) or Teflon®-coated
stainless steel nozzles with a sharp tapered
leading edge. We recommend one of the 12
nozzles listed in Figure 3 of Section 17
because they meet design specifications
when PM10 cyclones are used as part of the
sampling train. We also recommend that you
have a large number of nozzles in small
diameter increments available to increase the
likelihood of using a single nozzle for the
entire traverse. We recommend one of the
nozzles listed in Figure 4A or 4B of Section
17 because they meet design specifications
when PM2.5 cyclones are used without PM10
cyclones as part of the sampling train.
6.1.2 PM10 and PM2.5 Sizing Device. Use
a stainless steel (316 or equivalent) PM10 and
PM2.5 sizing devices. The sizing devices must
be cyclones that meet the design
specifications shown in Figures 3, 4, 5, and
6 of Section 17. Use a caliper to verify the
dimensions of the PM10 and PM2.5 sizing
devices to within ±0.02 cm of the design
specifications. Example suppliers of PM10
and PM2.5 sizing devices include the
following:
(a) Environmental Supply Company, Inc.,
2142 Geer Street, Durham, North Carolina
27704, (919) 956–9688 (phone), (919) 682–
0333 (fax).
(b) Apex Instruments, P.O. Box 727, 125
Quantum Street, Holly Springs, North
Carolina 27540, (919) 557–7300 (phone),
(919) 557–7110 (fax).
(c) Andersen Instruments Inc., 500
Technology Court, Smyrna, Georgia 30082,
(770) 319–9999 (phone), (770) 319–0336
(fax).
You may use alternative particle sizing
devices if they meet the requirements in
Development and Laboratory Evaluation of a
Five-Stage Cyclone System, EPA–600/7–78–
008 (incorporated by reference) and are
approved by the Administrator. The Director
of the Federal Register approves this
incorporation by reference in accordance
with 5 U.S.C. 552(a) and 1 CFR part 51. You
may obtain a copy from National Technical
Information Service, https://www.ntis.gov or
(800) 553–6847. You may inspect a copy at
the Office of Federal Register, 800 North
Capitol Street, NW., Suite 700, Washington,
DC.
6.1.3 Filter Holder. Use a filter holder
that is either stainless steel (316 or
equivalent) or Teflon®-coated stainless steel.
A heated glass filter holder may be
substituted for the steel filter holder when
filtration is performed out-of-stack.
Commercial size filter holders are available
depending upon project requirements,
including commercial filter holders to
support 25-, 47-, and 63-mm diameter filters.
Commercial size filter holders contain a
Teflon® O-ring, a stainless steel screen that
supports the filter, and a final Teflon® Oring. Screw the assembly together and attach
to the outlet of cyclone IV.
6.1.4 Pitot Tube. You must use a pitot
tube made of heat resistant tubing. Attach the
pitot tube to the probe with stainless steel
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fittings. Follow the specifications for the
pitot tube and its orientation to the inlet
nozzle given in Section 6.1.1.3 of Method 5.
6.1.5 Probe Liner. The probe extension
must be glass-lined or Teflon®. Follow the
specifications in Section 6.1.1.2 of Method 5.
6.1.6 Differential Pressure Gauge,
Condensers, Metering Systems, Barometer,
and Gas Density Determination Equipment.
Follow the requirements in Sections 6.1.1.4
through 6.1.3 of Method 5, as applicable.
6.2 Sample Recovery Equipment.
6.2.1 Filterable Particulate Recovery. Use
the following equipment to quantitatively
determine the amount of filterable particulate
matter recovered from the sampling train.
Follow the requirements specified in
Sections 6.2.1 through 6.2.8 of Method 5,
respectively.
(a) Filter holder brushes
(b) Wash bottles
(c) Glass sample storage containers
(d) Petri dishes
(e) Graduated cylinders and balance
(f) Plastic storage containers
(g) Funnel
(h) Rubber policeman
7.0 Reagents, Standards, and Sampling
Media
7.1 Sample Collection. To collect a
sample, you will need a filter and silica gel.
You must also have water and crushed ice.
Additional information on these items is in
the following paragraphs.
7.1.1 Filter. Use a glass fiber, quartz, or
Teflon® filter that does not a have an organic
binder. The filter must also have an
efficiency of at least 99.95 percent (<0.05
percent penetration) on 0.3 micron dioctyl
phthalate smoke particles. Conduct the filter
efficiency test in accordance with ASTM
Method D2986–95a—Standard Method for
Evaluation of Air, Assay Media by the
Monodisperse DOP (Dioctyl Phthalate)
Smoke Test (incorporated by reference). The
Director of the Federal Register approves this
incorporation by reference in accordance
with 5 U.S.C. 552(a) and 1 CFR part 51. You
may obtain a copy from American Society for
Testing and Materials (ASTM), 100 Barr
Harbor Drive, Post Office Box C700, West
Conshohocken, PA 19428–2959. You may
inspect a copy at the Office of Federal
Register, 800 North Capitol Street, NW., Suite
700, Washington, DC. Alternatively, you may
use test data from the supplier’s quality
control program. If the source you are
sampling has sulfur dioxide (SO2) or sulfite
(SO3) emissions, you must use a filter that
will not react with SO2 or SO3. Depending on
your application and project data quality
objectives (DQOs), filters are commercially
available in 25-, 47-, 83-, and 110-mm sizes.
7.1.2 Silica Gel. Use an indicating-type
silica gel of 6 to 16 mesh. We must approve
other types of desiccants (equivalent or
better) before you use them. Allow the silica
gel to dry for 2 hours at 175 °C (350 °F) if
it is being reused. You do not have to dry
new silica gel.
7.1.3 Crushed ice. Obtain from the best
readily available source.
7.2 Sample Recovery and Analysis
Reagents. You will need acetone and
anhydrous sodium sulfate for the sample
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analysis. Unless otherwise indicated, all
reagents must conform to the specifications
established by the Committee on Analytical
Reagents of the American Chemical Society.
If such specifications are not available, then
use the best available grade. Additional
information on each of these items is in the
following paragraphs.
7.2.1 Acetone. Use acetone that is stored
in a glass bottle. Do not use acetone from a
metal container because it normally produces
a high residue blank. You must use acetone
with blank values <1 ppm, by weight residue.
Analyze acetone blanks prior to field use to
confirm low blank values. In no case shall a
blank value of greater than 1E–06 of the
weight of acetone used in sample recovery be
subtracted from the sample weight (i.e., the
maximum blank correction is 0.079 mg per
100 mL of acetone used to recover samples).
7.2.2 Particulate Sample Desiccant. Use
indicating-type anhydrous sodium sulfate to
desiccate samples prior to weighing.
8.0 Sample collection, Preservation,
Storage, and Transport
8.1 Qualifications. This is a complex test
method. To obtain reliable results, you must
be trained and experienced with in-stack
filtration systems (such as cyclones,
impactors, and thimbles) and their
operations.
8.2 Preparations. Follow the pretest
preparation instructions in Section 8.1 of
Method 5.
8.3 Site Setup. You must complete the
following to properly set up for this test:
(a) Determine the sampling site location
and traverse points.
(b) Calculate probe/cyclone blockage.
(c) Verify the absence of cyclonic flow.
(d) Complete a preliminary velocity profile,
and select a nozzle.
8.3.1 Sampling Site Location and
Traverse Point Determination. Follow the
standard procedures in Method 1 to select
the appropriate sampling site. Then do all of
the following:
(a) Sampling site. Choose a location that
maximizes the distance from upstream and
downstream flow disturbances.
(b) Traverse points. The recommended
maximum number of total traverse points at
any location is 12 as shown in Figure 7 of
Section 17. Prevent the disturbance and
capture of any solids accumulated on the
inner wall surfaces by maintaining a 1-inch
distance from the stack wall (1⁄2 inch for
sampling locations less than 24 inches in
diameter).
(c) Round or rectangular duct or stack. If
a duct or stack is round with two ports
located 90 degrees apart, use six sampling
points on each diameter. Use a 3 x 4
sampling point layout for rectangular ducts
or stacks. Consult with the Administrator to
receive approval for other layouts before you
use them.
(d) Sampling ports. To accommodate the
in-stack cyclones for this method, you may
need larger diameter sampling ports than
those used by Method 5 or Method 17 for
total filterable particulate sampling. When
you must use nozzles smaller than 0.16 inch
in diameter, the sampling port diameter must
be 6 inches. Do not use the conventional 4-
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inch diameter port because the combined
dimension of the PM10 cyclone and the
nozzle extending from the cyclone exceeds
the internal diameter of the port.
[Note: If the port nipple is short, you may
be able to ‘‘hook’’ the sampling head through
a smaller port into the duct or stack.]
8.3.2 Probe/Cyclone Blockage
Calculations. Follow the procedures in the
next two sections, as appropriate.
8.3.2.1 Ducts with diameters greater than
24 inches.
Minimize the blockage effects of the
combination of the in-stack nozzle/cyclones
and filter assembly for ducts with diameters
greater than 24 inches by keeping the crosssectional area of the assembly at 3 percent or
less of the cross-sectional area of the duct.
8.3.2.2 Ducts with diameters between 18
and 24 inches. Ducts with diameters between
18 and 24 inches have blockage effects
ranging from 3 to 6 percent, as illustrated in
Figure 8 of Section 17. Therefore, when you
conduct tests on these small ducts, you must
adjust the observed velocity pressures for the
estimated blockage factor whenever the
combined sampling apparatus blocks more
than 3 percent of the stack or duct (see
Sections 8.7.2.2 and 8.7.2.3 on the probe
blockage factor and the final adjusted
velocity pressure, respectively).
8.3.3 Cyclonic Flow. Do not use the
combined cyclone sampling head at sampling
locations subject to cyclonic flow. Also, you
must follow procedures in Method 1 to
determine the presence or absence of
cyclonic flow and then perform the following
calculations.
(a) As per Section 11.4 of Method 1, find
and record the angle that has a null velocity
pressure for each traverse point using a Stype pitot tube.
(b) Average the absolute values of the
angles that have a null velocity pressure. Do
not use the sampling location if the average
absolute value exceeds 20°.
[Note: You can minimize the effects of
cyclonic flow conditions by moving the
sampling location, placing gas flow
straighteners upstream of the sampling
location or applying a modified sampling
approach as described in EPA Guideline
Document 008. You may need to obtain an
alternate method approval prior to using a
modified sampling approach.]
8.3.4 Preliminary Velocity Profile.
Conduct a preliminary velocity traverse by
following Method 2 velocity traverse
procedures. The purpose of the preliminary
velocity profile is to determine all of the
following:
(a) The gas sampling rate for the combined
probe/cyclone sampling head in order to
meet the required particle size cut.
(b) The appropriate nozzle to maintain the
required gas sampling rate for the velocity
pressure range and isokinetic range. If the
isokinetic range cannot be met (e.g., batch
processes, extreme process flow or
temperature variation), void the sample or
use methods subject to the approval of the
Administrator to correct the data.
(c) The necessary sampling duration to
obtain sufficient particulate catch weights.
8.3.4.1 Preliminary traverse. You must
use an S-type pitot tube with a conventional
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thermocouple to conduct the traverse.
Conduct the preliminary traverse as close as
possible to the anticipated testing time on
sources that are subject to hour-by-hour gas
flow rate variations of approximately ±20
percent and/or gas temperature variations of
approximately ±10 °C (±50 °F).
[Note: You should be aware that these
variations can cause errors in the cyclone cut
diameters and the isokinetic sampling
velocities.]
8.3.4.2 Velocity pressure range. Insert the
S-type pitot tube at each traverse point, and
record the range of velocity pressures
measured on data form in Method 2. You will
use this later to select the appropriate nozzle.
8.3.4.3 Initial gas stream viscosity and
molecular weight. Determine the average gas
temperature, average gas oxygen content,
average carbon dioxide content, and
estimated moisture content. You will use this
information to calculate the initial gas stream
viscosity (Equation 3) and molecular weight
(Equations 1 and 2).
[Note: You must follow the instructions
outlined in Method 4 to estimate the
moisture content. You may use a wet bulbdry bulb measurement or hand-held
hygrometer measurement to estimate the
moisture content of sources with gas
temperatures less than 71 °C (160 °F).]
8.3.4.4 Particulate matter concentration
in the gas stream. Determine the particulate
matter concentration for the PM2.5 and the
PM2.5 to PM10 components of the gas stream
through qualitative measurements or
estimates. Having an idea of the particulate
concentration in the gas stream is not
essential but will help you determine the
appropriate sampling time to acquire
sufficient particulate matter weight for better
accuracy at the source emission level. The
collectable particulate matter weight
requirements depend primarily on the types
of filter media and weighing capabilities that
are available and needed to characterize the
emissions. Estimate the collectable
particulate matter concentrations in the >10
micrometer, ≤10 and >2.5 micrometers, and
≤2.5 micrometer size ranges. Typical
particulate matter concentrations are listed in
Table 1 of Section 17. Additionally, relevant
sections of AP–42 may contain particle size
distributions for processes characterized in
those sections and Appendix B2 of AP–42
contains generalized particle size
distributions for nine industrial process
categories (e.g., stationary internal
combustion engines firing gasoline or diesel
fuel, calcining of aggregate or unprocessed
ores). The generalized particle size
distributions can be used if source-specific
particle size distributions are unavailable.
Appendix B2 also contains typical collection
efficiencies of various particulate control
devices and example calculations showing
how to estimate uncontrolled total
particulate emissions, uncontrolled sizespecific emissions, and controlled sizespecific particulate emissions.
8.4 Pre-test Calculations. You must
perform pre-test calculations to help select
the appropriate gas sampling rate through
cyclone I (PM10) and cyclone IV (PM2.5).
Choosing the appropriate sampling rate will
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allow you to maintain the appropriate
particle cut diameters based upon
preliminary gas stream measurements, as
specified in Table 2 of Section 17.
8.4.1 Gas Sampling Rate. The gas
sampling rate is defined by the performance
curves for both cyclones, as illustrated in
Figure 9 of Section 17. You must use the
calculations in Section 8.5 to achieve the
appropriate cut size specification for each
cyclone. The optimum gas sampling rate is
the overlap zone defined as the range below
the cyclone IV 2.25 micrometer curve down
to the cyclone I 11.0 micrometer curve (area
between the two dark, solid lines in Figure
9 of Section 17).
8.4.2 Choosing the Appropriate Sampling
Rate. You must select a gas sampling rate in
the middle of the overlap zone (discussed in
Section 8.4.1), as illustrated in Figure 9 of
Section 17 to maximize the acceptable
tolerance for slight variations in flow
characteristics at the sampling location. The
overlap zone is also a weak function of the
gas composition.
[Note: The acceptable range is limited,
especially for gas streams with temperatures
less than approximately 100 °F. At lower
temperatures, it may be necessary to perform
the PM10 and PM2.5 separately in order to
meet the necessary particle size criteria
shown in Table 2 of Section 17.0.]
8.5 Test Calculations. You must perform
all of the calculations in Table 3 of Section
17 and the calculations described in Sections
8.5.1 through 8.5.5.
8.5.1 The Assumed Reynolds Number.
Verify the assumed Reynolds number (Nre) by
substituting the sampling rate (Qs) calculated
in Equation 7 into Equation 8. Then use
Table 5 of Section 17 to determine if the Nre
used in Equation 5 was correct.
8.5.2 Final Sampling Rate. Recalculate
the final sampling rate (Qs) if the assumed
Reynolds number used in your initial
calculation is not correct. Use Equation 7 to
recalculate the optimum sampling rate (Qs).
8.5.3 Meter Box DH. Use Equation 9 to
calculate the meter box DH after you
calculate the optimum sampling rate and
confirm the Reynolds number.
[Note: The stack gas temperature may vary
during the test, which could affect the
sampling rate. If the stack gas temperature
varies, you must make slight adjustments in
the meter box DH to maintain the correct
constant cut diameters. Therefore, use
Equation 9 to recalculate the DH values for
50°F above and below the stack temperature
measured during the preliminary traverse
(see Section 8.3.4.1), and document this
information in Table 4 of Section 17.]
8.5.4 Choosing a Sampling Nozzle. Select
one or more nozzle sizes to provide for near
isokinetic sampling rate (that is, 80 percent
to 120 percent). This will also minimize an
isokinetic sampling error for the particles at
each point. First calculate the mean stack gas
velocity, vs, using Equation 11. See Section
8.7.2 for information on correcting for
blockage and use of different pitot tube
coefficients. Then use Equation 12 to
calculate the diameter of a nozzle that
provides for isokinetic sampling at the mean
stack gas velocity at flow Qs. From the
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available nozzles just smaller and just larger
of this diameter, D, select the most promising
nozzle. Perform the following steps for the
selected nozzle.
8.5.4.1 Minimum/maximum nozzle/stack
velocity ratio. Use Equation 14 to calculate
the minimum nozzle/stack velocity ratio,
Rmin. Use Equation 15 to calculate the
maximum nozzle/stack velocity ratio, Rmax.
8.5.4.2 Minimum gas velocity. Use
Equation 16 to calculate the minimum gas
velocity (vmin) if Rmin is an imaginary number
(negative value under the square root
function) or if Rmin is less than 0.5. Use
Equation 17 to calculate vmin if Rmin is greater
than or equal to 0.5.
8.5.4.3 Maximum stack velocity. Use
Equation 18 to calculate the maximum stack
velocity (vmax) if Rmax is less than 1.5. Use
Equation 19 to calculate the stack velocity if
Rmax is greater than or equal to 1.5.
8.5.4.4 Conversion of gas velocities to
velocity pressure. Use Equation 20 to convert
vmin to minimum velocity pressure, Dpmin.
Use Equation 21 to convert vmax to maximum
velocity pressure, Dpmax.
8.5.4.5 Compare minimum and maximum
velocity pressures with the observed velocity
pressures at all traverse points during the
preliminary test (see Section 8.3.4.2).
8.5.5 Optimum sampling nozzle. The
nozzle you selected is appropriate if all the
observed velocity pressures during the
preliminary test fall within the range of the
Dpmin and Dpmax. Make sure the following
requirements are met. Then follow the
procedures in Sections 8.5.5.1 and 8.5.5.2.
(a) Choose an optimum nozzle that
provides for isokinetic sampling conditions
as close to 100 percent as possible. This is
prudent because even if there are slight
variations in the gas flow rate, gas
temperature, or gas composition during the
actual test, you have the maximum assurance
of satisfying the isokinetic criteria. Generally,
one of the two candidate nozzles selected
will be closer to optimum (see Section 8.5.4).
(b) When testing is for PM2.5 only, you may
have only two traverse points out of 12 that
are outside the range of the Dpmin and Dpmax
(i.e., 16 percent failure rate rounded to the
nearest whole number). If the coarse fraction
for PM10 determination is included, only one
traverse point out of 12 can fall outside the
minimum-maximum velocity pressure range
(i.e., 8 percent failure rate rounded to the
nearest whole number).
8.5.5.1 Precheck. Visually check the
selected nozzle for dents before use.
8.5.5.2 Attach the pre-selected nozzle.
Screw the pre-selected nozzle onto the main
body of cyclone I using Teflon® tape. Use a
union and cascade adaptor to connect the
cyclone IV inlet to the outlet of cyclone I (see
Figure 2 of Section 17).
8.6 Sampling Train Preparation. A
schematic of the sampling train used in this
method is shown in Figure 1 of Section 17.
First, assemble the train and complete the
leak check on the combined cyclone
sampling head and pitot tube. Use the
following procedures to prepare the sampling
train.
[Note: Do not contaminate the sampling
train during preparation and assembly. Keep
all openings where contamination can occur
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covered until just prior to assembly or until
sampling is about to begin.]
8.6.1 Sampling Head and Pitot Tube.
Assemble the combined cyclone train. The Orings used in the train have a temperature
limit of approximately 205 °C (400 °F). Use
cyclones with stainless steel sealing rings
when stack temperatures exceed 205 °C (400
°F). This method may not be suitable for
sources with stack gas temperatures
exceeding 260 °C (500 °F). You may need to
take extraordinary measures including the
use of specialty metals (e.g., Inconel) to
achieve reliable particulate mass since the
threads of the cyclones may gall or seize,
thus preventing the recovery of the collected
particulate matter and rendering the cyclone
unusable for subsequent use. You must also
keep the nozzle covered to protect it from
nicks and scratches.
8.6.2 Filterable Particulate Filter Holder
and Pitot Tube. Attach the pre-selected filter
holder to the end of the combined cyclone
sampling head (see Figure 2 of Section 17).
Attach the S-type pitot tube to the combined
cyclones after the sampling head is fully
attached to the end of the probe.
[Note: The pitot tube tip must be mounted:
slightly beyond the combined head cyclone
sampling assembly; and at least one inch off
the gas flow path into the cyclone nozzle.
This is similar to the pitot tube placement in
Method 17.]
Weld the sensing lines to the outside of the
probe to ensure proper alignment of the pitot
tube. Provide unions on the sensing lines so
that you can connect and disconnect the Stype pitot tube tips from the combined
cyclone sampling head before and after each
run.
[Note: Calibrate the pitot tube on the
sampling head because the cyclone body is
a potential source flow disturbance.]
8.6.3 Filter. You must number and tare
the filters before use. To tare the filters,
desiccate each filter at 20 ± 5.6 °C (68 ± 10
°F) and ambient pressure for at least 24 hours
and weigh at intervals of at least 6 hours to
a constant weight, i.e., <0.5 mg change from
previous weighing; record results to the
nearest 0.1 mg. During each weighing, the
filter must not be exposed to the laboratory
atmosphere for longer than 2 minutes and a
relative humidity above 50 percent.
Alternatively, the filters may be oven-dried at
104 °C (220 °F) for 2 to 3 hours, desiccated
for 2 hours, and weighed. Use tweezers or
clean disposable surgical gloves to place a
labeled (identified) and pre-weighed filter in
both filterable and condensable particulate
filter holders. You must center the filter and
properly place the gasket so that the sample
gas stream will not circumvent the filter.
Check the filter for tears after the assembly
is completed. Then screw the filter housing
together to prevent the seal from leaking.
8.6.7 Moisture Trap. If you are measuring
only filterable particulate (or you are sure
that the filtration temperature will be
maintained below 30 °C (85 °F)), then an
empty modified Greenburg Smith impinger
followed by an impinger containing silica gel
is required. Alternatives described in Method
5 may also be used to collect moisture that
passes through the ambient filter. If you are
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measuring condensable particulate matter in
combination with this method, then follow
the procedures in Method 202 for moisture
collection.
8.6.8 Leak Check. Use the procedures
outlined in Section 8.4 of Method 5 to leak
check the entire sampling system.
Specifically perform the following
procedures:
8.6.8.1 Sampling train. You must pretest
the entire sampling train for leaks. The
pretest leak check must have a leak rate of
not more than 0.02 ACFM or 4 percent of the
average sample flow during the test run,
whichever is less. Additionally, you must
conduct the leak check at a vacuum equal to
or greater than the vacuum anticipated
during the test run. Enter the leak check
results on the field test data sheet (see
Section 11.1) for the specific test.
[Note: Do not conduct a leak check during
port changes.]
8.6.8.2 Pitot tube assembly. After you
leak check the sample train, perform a leak
check of the pitot tube assembly. Follow the
procedures outlined in Section 8.4.1 of
Method 5.
8.6.9 Sampling Head. You must preheat
the combined sampling head to the stack
temperature of the gas stream at the test
location (±10 °C, ±50 °F). This will heat the
sampling head and prevent moisture from
condensing from the sample gas stream.
Record the site barometric pressure and stack
pressure on the field test data sheet.
8.6.9.1 Unsaturated stacks. You must
complete a passive warmup (of 30–40 min)
within the stack before the run begins to
avoid internal condensation.
[Note: Unsaturated stacks do not have
entrained droplets and operate at
temperatures above the local dew point of the
stack gas.]
8.6.9.2 Shortened warm-up of
unsaturated stacks. You can shorten the
warmup time by thermostated heating
outside the stack (such as by a heat gun).
Then place the heated sampling head inside
the stack and allow the temperature to
equilibrate.
8.7 Sampling Train Operation. Operate
the sampling train the same as described in
Section 4.1.5 of Method 5, except use the
procedures in this section for isokinetic
sampling and flow rate adjustment. Maintain
the flow rate calculated in Section 8.4.1
throughout the run, provided the stack
temperature is within 28 °C (50 °F) of the
temperature used to calculate DH. If stack
temperatures vary by more than 28 °C (50 °F),
use the appropriate DH value calculated in
Section 8.5.3. Determine the minimum
number of traverse points as in Figure 7 of
Section 17. Determine the minimum total
projected sampling time (tr), based on
achieving the data quality objectives or
emission limit of the affected facility. We
recommend you round the number of
minutes sampled at each point to the nearest
15 seconds. Perform the following
procedures:
8.7.1 Sample Point Dwell Time. You
must calculate the dwell time (that is,
sampling time) for each sampling point to
ensure that the overall run provides a
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velocity-weighted average that is
representative of the entire gas stream. Vary
the dwell time, or sampling time, at each
traverse point proportionately with the point
velocity.
8.7.1.1 Dwell time at first sampling point.
Calculate the dwell time for the first point,
t1, using Equation 22. You must use the data
from the preliminary traverse. Here, Ntp
equals the total number of traverse points.
8.7.1.2 Dwell time at remaining sampling
points. Calculate the dwell time at each of
the remaining traverse points, tn, using
Equation 23. This time you must use the
actual test run data.
[Note: Round the dwell times to the nearest
15 seconds.] Each traverse point must have
a dwell time of at least 2 minutes.
8.7.2 Adjusted Velocity Pressure. When
selecting your sampling points using your
preliminary velocity traverse data, your
preliminary velocity pressures must be
adjusted to take into account the increase in
velocity due to blockage. Also, you must
adjust your preliminary velocity data for
differences in pitot tube coefficients. Use the
following instructions to adjust the
preliminary velocity pressure.
8.7.2.1 Different pitot tube coefficient.
You must use Equation 24 to correct the
recorded preliminary velocity pressures if the
pitot tube mounted on the combined cyclone
sampling head has a different pitot tube
coefficient than the pitot tube used during
the preliminary velocity traverse (see Section
8.3.4).
8.7.2.2 Probe blockage factor. You must
use Equation 25 to calculate an average probe
blockage correction factor (bf) if the diameter
of your stack or duct is between 18 and 24
inches. A probe blockage factor is calculated
because of the flow blockage caused by the
relatively large cross-sectional area of the
combined cyclone sampling head, as
discussed in Section 8.3.2.2 and illustrated in
Figure 8 of Section 17.
[Note: The sampling head (including the
PM10 cyclone, PM2.5 cyclone, pitot and filter
holder) has a projected area of approximately
20.5 square inches when oriented into the gas
stream. As the probe is moved from the most
outer to the most inner point, the amount of
blockage that actually occurs ranges from
approximately 4 square inches to the full
20.5 inches. The average cross-sectional area
blocked is 12 square inches.]
8.7.2.3 Final adjusted velocity pressure.
Calculate the final adjusted velocity pressure
(Dps2) using Equation 26.
[Note: Figure 8 of Section 17 illustrates that
the blockage effect of the large combined
cyclone sampling head increases rapidly
below diameters of 18 inches. Therefore, you
must follow the procedures outlined in
Method 1A to conduct tests in small stacks
(< inches diameter). You must conduct the
velocity traverse downstream of the sampling
location or immediately before the test run.]
8.7.3 Sample Collection. Collect samples
the same as described in Section 4.1.5 of
Method 5, except use the procedures in this
section for isokinetic sampling and flow rate
adjustment. Maintain the flow rate calculated
in Section 8.5 throughout the run, provided
the stack temperature is within 28 °C (50 °F)
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of the temperature used to calculate DH. If
stack temperatures vary by more than 28 °C
(50 °F), use the appropriate DH value
calculated in Section 8.5.3. Calculate the
dwell time at each traverse point as in
Equations 22 and 23. In addition to these
procedures, you must also use running starts
and stops if the static pressure at the
sampling location is more negative than 5 in.
water column. This prevents back pressure
from rupturing the sample filter. If you use
a running start, adjust the flow rate to the
calculated value after you perform the leak
check (see Section 8.4).
8.7.3.1 Level and zero manometers.
Periodically check the level and zero point of
the manometers during the traverse.
Vibrations and temperature changes may
cause them to drift.
8.7.3.2 Portholes. Clean the portholes
prior to the test run. This will minimize the
chance of collecting deposited material in the
nozzle.
8.7.3.3 Sampling procedures. Verify that
the combined cyclone sampling head
temperature is at stack temperature (± 10 °C,
± 50 °F).
[Note: For many stacks, portions of the
cyclones and filter will be external to the
stack during part of the sampling traverse.
Therefore, you must heat or insulate portions
of the cyclones and filter that are not within
the stack in order to maintain the sampling
head temperature at the stack temperature.
Maintaining the temperature will insure
proper particle sizing and prevent
condensation on the walls of the cyclones.]
Remove the protective cover from the
nozzle. To begin sampling, immediately start
the pump and adjust the flow to calculated
isokinetic conditions. Position the probe at
the first sampling point with the nozzle
pointing directly into the gas stream. Ensure
the probe/pitot tube assembly is leveled.
[Note: When the probe is in position, block
off the openings around the probe and
porthole to prevent unrepresentative dilution
of the gas stream.]
(a) Traverse the stack cross-section, as
required by Method 1 with the exception that
you are only required to perform a 12-point
traverse. Do not bump the cyclone nozzle
into the stack walls when sampling near the
walls or when removing or inserting the
probe through the portholes. This will
minimize the chance of extracting deposited
materials.
(b) Record the data required on the field
test data sheet for each run. Record the initial
dry gas meter reading. Then take dry gas
meter readings at the following times: the
beginning and end of each sample time
increment; when changes in flow rates are
made; and when sampling is halted. Compare
the velocity pressure measurements
(Equations 20 and 21) with the velocity
pressure measured during the preliminary
traverse. Keep the meter box DH at the value
calculated in Section 8.5.3 for the stack
temperature that is observed during the test.
Record all the point-by-point data and other
source test parameters on the field test data
sheet. Do not leak check the sampling system
during port changes.
(c) Maintain the flow through the sampling
system at the last sampling point. Remove
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the sampling train from the stack while it is
still operating (running stop). Then stop the
pump, and record the final dry gas meter
reading and other test parameters on the field
test data sheet.
8.7.4 Process Data. You must document
data and information on the process unit
tested, the particulate control system used to
control emissions, any non-particulate
control system that may affect particulate
emissions, the sampling train conditions, and
weather conditions. Discontinue the test if
the operating conditions may cause nonrepresentative particulate emissions.
8.7.4.1 Particulate control system data.
Use the process and control system data to
determine if representative operating
conditions were maintained throughout the
testing period.
8.7.4.2 Sampling train data. Use the
sampling train data to confirm that the
measured particulate emissions are accurate
and complete.
8.7.5 Sample Recovery. First remove the
sample head (combined cyclone/filter
assembly) from the stack. After the sample
head is removed, perform a post-test leak
check of the probe and sample train. Then
recover the components from the cyclone/
filter. Refer to the following sections for more
detailed information.
8.7.5.1 Remove sampling head. At the
conclusion of the test, document final test
conditions and remove the pitot tube and
combined cyclone sampling head from the
source. Make sure that you do not scrape the
pitot tube or the combined cyclone sampling
head against the port or stack walls.
[Note: After you stop the gas flow, make
sure you keep the combined cyclone head
level to avoid tipping dust from the cyclone
cups into the filter and/or down-comer lines.]
After cooling and when the probe can be
safely handled, wipe off all external surfaces
near the cyclone nozzle, and cap the inlet to
cyclone I. Remove the combined cyclone/
filter sampling head from the probe. Cap the
outlet of the filter housing to prevent
particulate matter from entering the
assembly.
8.7.5.2 Leak check probe/sample train
assembly (post-test). Leak check the
remainder of the probe and sample train
assembly (including meter box) after
removing the combined cyclone head/filter.
You must conduct the leak rate at a vacuum
equal to or greater than the maximum
vacuum achieved during the test run. Enter
the results of the leak check onto the field
test data sheet. If the leak rate of the sampling
train (without the combined cyclone
sampling head) exceeds 0.02 ACFM or 4
percent of the average sampling rate during
the test run (whichever is less), the run is
invalid, and you must repeat it.
8.7.5.3 Weigh or measure the volume of
the liquid collected in the water collection
impingers and silica trap. Measure the liquid
in the first impingers to within 1 ml using a
clean graduated cylinder or by weighing it to
within 0.5 g using a balance. Record the
volume of the liquid or weight of the liquid
present to be used to calculate the moisture
content of the effluent gas.
8.7.5.4 If a balance is available in the
field, weigh the silica impinger to within 0.5
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g. Note the color of the indicating silica gel
in the last impinger to determine whether it
has been completely spent, and make a
notation of its condition. If you are
measuring condensable particulate matter in
combination with this method, then leave the
silica in the impinger for recovery after the
post-test nitrogen purge is complete.
8.7.5.5 Recovery of particulate matter.
Recovery involves the quantitative transfer of
particles in the following size range: > 10
micrometers; ≤ 10 micrometers but > 2.5
micrometers; and ≤ 2.5 micrometers. You
must use a Nylon or Teflon brush and an
acetone rinse to recover particles from the
combined cyclone/filter sampling head. Use
the following procedures for each container.
(a) Container #1, ≤ PM2.5 micrometer
filterable particulate—Use tweezers and/or
clean disposable surgical gloves to remove
the filter from the filter holder. Place the
filter in the petri dish that you identified as
Container #1. Using a dry Nylon bristle brush
and/or a sharp-edged blade, carefully transfer
any particulate matter and/or filter fibers that
adhere to the filter holder gasket or filter
support screen to the petri dish. Seal the
container. This container holds particles ≤
2.5 micrometers that are caught on the instack filter.
(b) Container #2, > PM10 micrometer
filterable particulate—Quantitatively recover
the particulate matter from the cyclone I cup
and acetone rinses (and brush cleaning) of
the cyclone cup, internal surface of the
nozzle, and cyclone I internal surfaces,
including the outside surface of the
downcomer line. Seal the container and mark
the liquid level on the outside of the
container. You must keep any dust found on
the outside of cyclone I and cyclone nozzle
external surfaces out of the sample. This
container holds particulate matter > 10
micrometers.
(c) Container #3, Filterable particulate ≤ 10
micrometer and > 2.5 micrometers—Place the
solids from cyclone cup IV and the acetone
(and brush cleaning) rinses of the cyclone I
turnaround cup (above inner downcomer
line), inside of the downcomer line, and
interior surfaces of cyclone IV into Container
#3. Seal the container and mark the liquid
level on the outside. This container holds
particulate matter ≤ 10 micrometers but > 2.5
micrometers.
(d) Container #4, ≤ PM2.5 micrometers
acetone rinses of the exit tube of cyclone IV
and front half of the filter holder—Retrieve
the acetone rinses (and brush cleaning) of the
exit tube of cyclone IV and the front half of
the filter holder in container #4. Seal the
container and mark the liquid level on the
outside of the container. This container holds
particulate matter that is ≤ 2.5 micrometers.
(e) Container #5, Cold impinger water—If
the water from the cold impinger used for
moisture collection has been weighed in the
field, it can be discarded. Otherwise
quantitatively transfer liquid from the cold
impinger that follows the ambient filter into
a clean sample bottle (glass or plastic). Mark
the liquid level on the bottle. This container
holds the remainder of the liquid water from
the emission gases.
(f) Container #6, Silica Gel Absorbent—
Transfer the silica gel to its original container
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and seal. A funnel may make it easier to pour
the silica gel without spilling. A rubber
policeman may be used as an aid in removing
the silica gel from the impinger. It is not
necessary to remove the small amount of
silica gel dust particles that may adhere to
the impinger wall and are difficult to remove.
Since the gain in weight is to be used for
moisture calculations, do not use any water
or other liquids to transfer the silica gel. If
the silica gel has been weighed in the field
to measure water content, it can be
discarded. Otherwise the contents of
Container #6 are weighed during sample
analysis.
(g) Container #7, Acetone Rinse Blank—
Take 100 ml of the acetone directly from the
wash bottle you used, and place it in
Container #7 labeled Acetone Rinse Blank.
8.7.6 Transport Procedures. Containers
must remain in an upright position at all
times during shipping. You do not have to
ship the containers under dry or blue ice.
9.0 Quality Control
9.1 Daily Quality Checks. You must
perform daily quality checks using data
quality indicators that require review of
recording and transfer of raw data,
calculations, and documentation of testing
procedures.
9.2 Calculation Verification. Verify the
calculations by independent, manual checks.
You must flag any suspect data and identify
the nature of the problem and potential effect
on data quality. After you complete the test,
prepare a data summary, and compile all the
calculations and raw data sheets.
9.3 Conditions. You must document data
and information on the process unit tested,
the particulate control system used to control
emissions, any non-particulate control
system that may affect particulate emissions,
the sampling train conditions, and weather
conditions. Discontinue the test if the
operating conditions may cause nonrepresentative particulate emissions.
9.4 Health and Safety Plan. Develop a
health and safety plan to ensure the safety of
your employees who are on site conducting
the particulate emission test. Your plan must
conform to all applicable OSHA, MSHA, and
DOT regulatory requirements. The
procedures must also conform to the plant
health and safety requirements.
9.5 Calibration Checks. Perform
calibration check procedures on analytical
balances each time they are used.
9.6 Glassware. Use class A volumetric
glassware for titrations, or calibrate your
equipment against NIST traceable glassware.
PWALKER on PROD1PC71 with PROPOSALS3
10.0
Calibration and Standardization
[Note: Maintain a laboratory log of all
calibrations.]
10.1 Gas Flow Velocities. Measure the gas
flow velocities at the sampling locations
using Method 2. You must use an S-type
pitot tube that meets the required EPA
specifications (EPA Publication 600/4–77–
0217b) during these velocity measurements.
You must also complete the following:
(a) Visually inspect the S-type pitot tube
before sampling.
(b) Leak check both legs of the pitot tube
before and after sampling.
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01:35 Mar 25, 2009
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(c) Maintain proper orientation of the Stype pitot tube while making measurements.
10.1.1 S-type pitot tube orientation. The
S-type pitot tube is oriented properly when
the yaw and the pitch axis are 90 degrees to
the air flow.
10.1.2 Average velocity pressure record.
Instead of recording either high or low
values, record the average velocity pressure
at each point during flow measurements.
10.1.3 Pitot tube coefficient. Determine
the pitot tube coefficient based on physical
measurement techniques described in
Method 2.
[Note: You must calibrate the pitot tube on
the sampling head because of potential
interferences from the cyclone body. Refer to
Section 8.7.2 for additional information.]
10.2 Thermocouple Calibration. Calibrate
the thermocouples using the procedures
described in Section 10.1.4.1.2 of Method 2
to calibrate the thermocouples. Calibrate each
temperature sensor at a minimum of three
points over the anticipated range of use
against an NIST-traceable mercury-in-glass
thermometer.
10.3 Nozzles. You may use stainless steel
(316 or equivalent) or Teflon®-coated nozzles
for isokinetic sampling. Make sure that all
nozzles are thoroughly cleaned, visually
inspected, and calibrated according to the
procedure outlined in Section 10.1 of Method
5.
10.4 Dry Gas Meter Calibration. Calibrate
your dry gas meter following the calibration
procedures in Section 16.1 of Method 5.
Also, make sure you fully calibrate the dry
gas meter to determine the volume correction
factor prior to field use. Post-test calibration
checks must be performed as soon as possible
after the equipment has been returned to the
shop. Your pretest and post-test calibrations
must agree within ±5 percent.
11.0 Analytical Procedures
11.1 Analytical Data Sheet. Record all
data on the analytical data sheet. Obtain the
data sheet from Figure 5–6 of Method 5.
Alternatively, data may be recorded
electronically using software applications
such as the Electronic Reporting Tool (ERT)
located at the following internet address:
(https://www.epa.gov/ttn/chief/ert/ert_
tool.html).
11.2 Dry Weight of Particulate Matter.
Determine the dry weight of particulate
following procedures outlined in this section.
11.2.1 Container #1, ≤ PM 2.5 micrometer
filterable particulate. Transfer the filter and
any loose particulate from the sample
container to a tared glass weighing dish.
Desiccate for 24 hours in a desiccator
containing anhydrous calcium sulfate or
indicating silica gel. Weigh to a constant
weight, and report the results to the nearest
0.1 mg. For the purposes of this section, the
term ‘‘constant weight’’ means a difference of
no more than 0.5 mg or 1 percent of total
weight less tare weight, whichever is greater,
between two consecutive weighings, with no
less than 6 hours of desiccation time between
weighings.
11.2.2 Container #2, > PM 10 micrometer
filterable particulate acetone rinse.
Separately treat this container like Container
#1.
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12985
11.2.3 Container #3, Filterable particulate
≤ 10 micrometer and ≥ 2.5 micrometers
acetone rinse. Separately treat this container
like Container #1.
11.2.4 Container #4, ≤ PM 2.5 micrometers
acetone rinse of the exit tube of cyclone IV
and front half of the filter holder. Note the
level of liquid in the container, and confirm
on the analysis sheet whether leakage
occurred during transport. If a noticeable
amount of leakage has occurred, either void
the sample or use methods, subject to the
approval of the Administrator, to correct the
final results. Quantitatively transfer the
contents to a tared 250 ml beaker, and
evaporate to dryness at ambient temperature
and pressure. Desiccate for 24 hours, and
weigh to a constant weight. Report the results
to the nearest 0.1 g.
11.2.5 Container #5, Cold impinger water.
If the amount of water has not been
determined in the field, note the level of
liquid in the container, and confirm on the
analysis sheet whether leakage occurred
during transport. If a noticeable amount of
leakage has occurred, either void the sample
or use methods, subject to the approval of the
Administrator, to correct the final results.
Measure the liquid in this container either
volumetrically to ±1 ml or gravimetrically to
±0.5 g.
11.2.6 Container #6, Silica gel absorbent.
Weigh the spent silica gel (or silica gel plus
impinger) to the nearest 0.5 g using a balance.
This step may be conducted in the field.
11.2.7 Container #7, Acetone rinse blank.
Use 100 ml of acetone from the blank
container for this analysis. If insufficient
liquid is available or if the acetone has been
lost due to container breakage, either void the
sample or use methods, subject to the
approval of the Administrator, to correct the
final results. Transfer 100 ml of the acetone
to a clean 250 ml beaker. Evaporate the
acetone at room temperature and pressure in
a laboratory hood to approximately 10 ml.
Quantitatively transfer the beaker contents to
a 50 ml preweighed tin, and evaporate to
dryness at room temperature and pressure in
a laboratory hood. Following evaporation,
desiccate the residue for 24 hours in a
desiccator containing anhydrous calcium
sulfate. Weigh and report the results to the
nearest 0.1 mg.
12.0 Calculations and Data Analysis
12.1 Nomenclature. Report results in
International System of Units (SI units)
unless the regulatory authority for
compliance testing specifies English units.
The following nomenclature is used.
A = Area of stack or duct at sampling
location, square inches.
An = Area of nozzle, square feet.
bf = Average blockage factor calculated in
Equation 25, dimensionless.
Bws = Moisture content of gas stream, fraction
e.g., 10% H2O is Bws = 0.10).
C = Cunningham correction factor for particle
diameter, Dp, and calculated using the
actual stack gas temperature,
dimensionless.
%CO2 = Carbon Dioxide content of gas
stream, % by volume.
Ca = Acetone blank concentration, mg/mg.
CfPM10 = Conc. of filterable PM10 particulate
matter, gr/DSCF.
E:\FR\FM\25MRP3.SGM
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PWALKER on PROD1PC71 with PROPOSALS3
12986
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
CfPM2.5 = Conc. of filterable PM2.5 particulate
matter, gr/DSCF.
Cp = Pitot coefficient for the combined
cyclone pitot, dimensionless.
Cp’ = Coefficient for the pitot used in the
preliminary traverse, dimensionless.
Cr = Re-estimated Cunningham correction
factor for particle diameter equivalent to
the actual cut size diameter and calculated
using the actual stack gas temperature,
dimensionless.
Ctf = Conc. of total filterable particulate
matter, gr/DSCF.
C1 = ¥150.3162 (micropoise)
C2 = 18.0614 (micropoise/K 0.5) = 13.4622
(micropoise/R 0.5)
C3 = 1.19183 × 10 6 (micropoise/K 2) =
3.86153 × 10 6 (micropoise/R 2)
C4 = 0.591123 (micropoise)
C5 = 91.9723 (micropoise)
C6 = 4.91705 × 10 ¥5 (micropoise/K 2) =
1.51761 × 10 ¥5 (micropoise/R 2)
D= Inner diameter of sampling nozzle
mounted on Cyclone I, in.
Dp = Physical particle size, micrometers.
D50 = Particle cut diameter, micrometers.
D50¥1= Re-calculated particle cut diameters
based on re-estimated Cr, micrometers.
D50LL = Cut diameter for cyclone I
corresponding to the 2.25 micrometer cut
diameter for cyclone IV, micrometers.
D50N = D50 value for cyclone IV calculated
during the Nth iterative step, micrometers.
D50 (N∂1) = D50 value for cyclone IV
calculated during the N+1 iterative step,
micrometers.
D50T = Cyclone I cut diameter corresponding
to the middle of the overlap zone shown
in Figure 9 of Section 17, micrometers.
I = Percent isokinetic sampling,
dimensionless.
in. = Inches
Kp = 85.49, [(ft/sec)/(pounds/mole ¥°R)].
ma = Mass of residue of acetone after
evaporation, mg.
Md = Molecular weight of dry gas, pounds/
pound mole.
Mw = Molecular weight of wet gas, pounds/
pound mole.
M1 = Milligrams of particulate matter
collected on the filter, ≤ 2.5 micrometers.
M2 = Milligrams of particulate matter
recovered from Container #2 (acetone
blank corrected), >10 micrometers.
M3 = Milligrams of particulate matter
recovered from Container #3 (acetone
blank corrected), ≤10 and >2.5
micrometers.
M4 = Milligrams of particulate matter
recovered from Container #4 (acetone
blank corrected), ≤2.5 micrometers.
Ntp = Number of iterative steps or total
traverse points.
Nre = Reynolds number, dimensionless.
%O2,wet = Oxygen content of gas stream, %
by volume of wet gas.
[Note: The oxygen percentage used in
Equation 3 is on a wet gas basis. That means
that since oxygen is typically measured on a
dry gas basis, the measured %O2 must be
multiplied by the quantity (1¥Bws) to
convert to the actual volume fraction.
Therefore, %O2,wet = (1¥Bws) * %O2, dry]
Pbar = Barometric pressure, in. Hg.
Ps = Absolute stack gas pressure, in. Hg.
Qs = Sampling rate for cyclone I to achieve
specified D50, ACFM.
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01:35 Mar 25, 2009
Jkt 217001
QsST = Dry gas sampling rate through the
sampling assembly, DSCFM.
QI = Sampling rate for cyclone I to achieve
specified D50, ACFM.
QIV = Sampling rate for cyclone IV to achieve
specified D50, ACFM.
Rmax = Nozzle/stack velocity ratio parameter,
dimensionless.
Rmin = Nozzle/stack velocity ratio parameter,
dimensionless.
Tm = Meter box and orifice gas temperature,
°R.
tn = Sampling time at point n, min.
tr = Total projected run time, min.
Ts = Absolute stack gas temperature, °R.
t1 = Sampling time at point 1, min.
vmax = Maximum gas velocity calculated from
Equations 18 or 19, ft/sec.
vmin = Minimum gas velocity calculated from
Equations 16 or 17, ft/sec.
vn = Sample gas velocity in the nozzle, ft/sec.
vs = Velocity of stack gas, ft/sec.
Va = Volume of acetone blank, ml.
Vaw = Volume of acetone used in blank wash,
ml.
Vc = Quantity of water captured in impingers
and silica gel, ml.
Vm = Dry gas meter volume sampled, ACF.
Vms = Dry gas meter volume sampled,
corrected to standard conditions, DSCF.
Vws = Volume of water vapor, SCF.
Vb = Volume of aliquot taken for IC analysis,
ml.
Vic = Volume of impinger contents sample,
ml.
Wa = Weight of residue in acetone blank
wash, mg.
Z = Ratio between estimated cyclone IV D50
values, dimensionless.
DH = Meter box orifice pressure drop, in.
W.C.
DH@ = Pressure drop across orifice at flow
rate of 0.75 SCFM at standard conditions,
in. W.C.
[Note: specific to each orifice and meter
box.]
[(Dp)0.5]avg = Average of square roots of the
velocity pressures measured during the
preliminary traverse, in. W.C.
Dpm = Observed velocity pressure using Stype pitot tube in preliminary traverse, in.
W.C.
Dpmax = Maximum velocity pressure, in. W.C.
Dpmin = Minimum velocity pressure, in. W.C.
Dpn = Velocity pressure measured at point n
during the test run, in. W.C.
Dps = Velocity pressure calculated in
Equation 24, in. W.C.
Dps1 = Velocity pressure adjusted for
combined cyclone pitot tube, in. W.C.
Dps2 = Velocity pressure corrected for
blockage, in. W.C.
Dp1 = Velocity pressure measured at point 1,
in. W.C.
g = Dry gas meter gamma value,
dimensionless.
μ = Gas viscosity, micropoise.
q = Total run time, minutes.
ra = Density of acetone, mg/ml (see label on
bottle).
12.0 = Constant calculated as 60 percent of
20.5 square inch cross-sectional area of
combined cyclone head, square inches.
12.2 Calculations. Perform all of the
calculations found in Table 6 of Section 17.
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Table 6 of Section 17 also provides
instructions and references for the
calculations.
12.3 Analyses. Analyze D50 of cyclone IV
and the concentrations of the particulate
matter in the various size ranges.
12.3.1 D50 of cyclone IV. To determine
the actual D50 for cyclone IV, recalculate the
Cunningham correction factor and the
Reynolds number for the best estimate of
cyclone IV D50. The following sections
describe additional information on how to
recalculate the Cunningham correction factor
and determine which Reynolds number to
use.
12.3.1.1 Cunningham correction factor.
Recalculate the initial estimate of the
Cunningham correction factor using the
actual test data. Insert the actual test run data
and D50 of 2.5 micrometers into Equation 4.
This will give you a new Cunningham
correction factor that is based on actual data.
12.3.1.2 Initial D50 for cyclone IV.
Determine the initial estimate for cyclone IV
D50 using the test condition Reynolds number
calculated with Equation 8 as indicated in
Table 3 of Section 17. Refer to the following
instructions.
(a) If the Reynolds number is less than
3,162, calculate the D50 for cyclone IV with
Equation 33, using actual test data.
(b) If the Reynolds number is equal to or
greater than 3,162, calculate the D50 for
cyclone IV with Equation 34, using actual
test data.
(c) Insert the ‘‘new’’ D50 value calculated
by either Equation 33 or 34 into Equation 35
to re-establish the Cunningham Correction
Factor (Cr).
[Note: Use the test condition calculated
Reynolds number to determine the most
appropriate equation (Equation 33 or 34).]
12.3.1.3 Re-establish cyclone IV D50. Use
the re-established Cunningham correction
factor (calculated in the previous step) and
the calculated Reynolds number to determine
D50–1.
(a) Use Equation 36 to calculate the reestablished cyclone IV D50–1 if the Reynolds
number is less than 3,162.
(b) Use Equation 37 to calculate the reestablished cyclone IV D50–1 if the Reynolds
number is equal to or greater than 3,162.
12.3.1.4 Establishing ‘‘Z’’ values. The ‘‘Z’’
value is the result of an analysis that you
must perform to determine if the
Cunningham correction factor is acceptable.
Compare the calculated cyclone IV D50
(either Equation 33 or 34) to the reestablished cyclone IV D50–1 (either Equation
36 or 37) values based upon the test
condition calculated Reynolds number
(Equation 38). Follow these procedures.
(a) Use Equation 38 to calculate the ‘‘Z’’.
If the ‘‘Z’’ value is between 0.99 and 1.01, the
D50–1 value is the best estimate of the cyclone
IV D50 cut diameter for your test run.
(b) If the ‘‘Z’’ value is greater than 1.01 or
less than 0.99, re-establish a Cunningham
correction factor based on the D50–1 value
determined in either Equations 36 or 37,
depending upon the test condition Reynolds
number.
(c) Use the second revised Cunningham
correction to re-calculate the cyclone IV D50.
(d) Repeat this iterative process as many
times as necessary using the prescribed
E:\FR\FM\25MRP3.SGM
25MRP3
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
equations until you achieve the criteria
documented in Equation 39.
12.3.2 Particulate concentration. Use the
particulate catch weights in the combined
cyclone sampling train to calculate the
concentration of particulate matter in the
various size ranges. You must correct the
concentrations for the acetone blank.
12.3.2.1 Acetone blank concentration.
Use Equation 41 to calculate the acetone
blank concentration (Ca).
12.3.2.2 Acetone blank weight. Use
Equation 42 to calculate the acetone blank
weight (Wa).
[Note: Correct each of the particulate
matter weights per size fraction by
subtracting the acetone blank weight (that is,
M2,3,4–Wa)].
12.3.2.3 Particulate weight catch per size
fraction. Subtract the weight of the acetone
blank from the particulate weight catch in
each size fraction.
[Note: Do not subtract a blank value of
greater than 0.001 percent of the weight of
the acetone used from the sample weight.
Use the following procedures.]
(a) Use Equation 43 to calculate the
particulate matter recovered from Containers
#1, #2, #3, and #4. This is the total
collectable particulate matter (Ctf).
(b) Use Equation 44 to determine the
quantitative recovery of PM10 particulate
matter (CfPM10) from Containers #1, #3, and
#4.
(c) Use Equation 45 to determine the
quantitative recovery of PM2.5 particulate
(CfPM2.5) recovered from Containers #1 and
#4.
12.4 Reporting. You must include the
following list of conventional elements in the
emissions test report.
(a) Emission test description including any
deviations from this protocol.
12987
(b) Summary data tables on a run-by-run
basis.
(c) Flowchart of the process or processes
tested.
(d) Sketch of the sampling location.
(e) Preliminary traverse data sheets
including cyclonic flow checks.
(f) Raw field data sheets.
(g) Laboratory analytical sheets and case
narratives.
(h) Sample calculations.
(i) Pretest and post-test calibration data.
(j) Chain of custody forms.
(k) Documentation of process and air
pollution control system data.
12.5 Equations. Use the following
equations to complete the calculations
required in this test method.
Molecular Weight of Dry Gas. Calculate the
molecular weight of the dry gas using
Equation 1.
M d = 0.44 ( % CO 2 ) + 0.32 ( % O 2 ) + 0.28 (100 − % O 2 − % CO 2 )
Eq. 1
Molecular Weight of Wet Gas. Calculate the
molecular weight of the stack gas on a wet
basis using Equation 2.
M w = M d (1 − Bws ) + 18 ( Bws )
Eq. 2
Gas Viscosity. Calculate the gas viscosity
using Equation 3. This equation uses
constants for gas temperatures in °R.
Ts + C3 Ts−2 + C4 ( % O 2, wet ) − C5 Bws + C6 Bws Ts2
Eq. 3
PWALKER on PROD1PC71 with PROPOSALS3
Cut Diameter for Cyclone I for the Middle
of the Overlap Zone.
01:35 Mar 25, 2009
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⎛ 11 + D50 LL ⎞
D50 T = ⎜
⎟
2
⎝
⎠
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( N re
EP25MR09.004
EP25MR09.003
factor is for a 2.25 micrometer diameter
particle.
⎡M P ⎤
D50 LL = 9.507 C0.3007 ⎢ w s ⎥
⎣ Ts ⎦
VerDate Nov<24>2008
Eq. 4
Eq. 5
< 3,162 )
Sampling Rate.
Eq. 6
EP25MR09.001
Lower Limit Cut Diameter for Cyclone I for
Nre < 3,162. The Cunningham correction
0.5
EP25MR09.002
⎡ μ ⎤ ⎡ Ts ⎤
C = 1 + 0.0057193 ⎢
⎥ ⎢
⎥
⎢ Ps D p ⎥ ⎣ M w ⎦
⎦
⎣
EP25MR09.005
Cunningham Correction Factor. The
Cunningham correction factor is calculated
for a 2.25 micrometer diameter particle.
E:\FR\FM\25MRP3.SGM
25MRP3
EP25MR09.000
μ = C1 + C2
12988
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
Qs = Q I = 0.07296 ( μ )
⎡ Ts ⎤
⎢
⎥
⎣ M w Ps ⎦
0.2949
⎡ 1 ⎤
⎢
⎥
⎣ D50 T ⎦
1.4102
Eq. 7
Reynolds Number.
⎡P M ⎤ ⎡Q ⎤
N re = 8.64 × 105 ⎢ s w ⎥ ⎢ s ⎥
⎣ Ts ⎦ ⎣ μ ⎦
EP25MR09.017
Eq. 8
Meter Box Orifice Pressure Drop.
⎡1.083 Tm M d ΔH @ ⎤
⎢
⎥
Pbar
⎣
⎦
EP25MR09.016
Eq. 9
⎡M P ⎤
D50 LL = 10.0959 C0.4400 ⎢ w s ⎥
⎣ Ts ⎦
0.0600
EP25MR09.015
factor is for a 2.25 micrometer diameter
particle.
Equation 10
< 3162 )
( N re
EP25MR09.014
Lower Limit Cut Diameter for Cyclone I for
Nre ≥ 3,162. The Cunningham correction
2
Eq. 11
Velocity of Gas in Nozzle.
⎛ Qs ⎞
⎜ 60 ⎟
Vn = ⎝ ⎠
An
0.5
Eq. 12
Minimum Nozzle/Stack Velocity Ratio
Parameter.
Eq. 13
0.5
⎞
⎟
⎟
⎠
0.5
⎞
⎟
⎟
⎠
0.5
⎤
⎥
⎥
⎦
Eq. 14
⎤
⎥
⎥
⎦
Eq. 15
EP25MR09.009
⎡
⎛
0.2603 ( μ ) ( Qs )
= ⎢ 0.2457 + ⎜ 0.3072 −
⎜
⎢
v1.5
n
⎝
⎣
PWALKER on PROD1PC71 with PROPOSALS3
R max
⎡
⎛
0.2603 ( μ ) ( Qs )
= ⎢ 0.4457 + ⎜ 0.5690 +
⎜
⎢
v1.5
n
⎝
⎣
Minimum Gas Velocity for Rmin ≤ 0.5.
v min = v n (0.5)
Eq. 16
v min = v n R min
0.5
Eq. 17
Maximum Gas Velocity for Rmax < 1.5.
v max = v n R max
01:35 Mar 25, 2009
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Eq. 18
Maximum Gas Velocity for Rmax ≥ 1.5.
Minimum Gas Velocity for Rmin ≥ 0.5.
VerDate Nov<24>2008
EP25MR09.008
Maximum Nozzle/Stack Velocity Ratio
Parameter.
E:\FR\FM\25MRP3.SGM
25MRP3
EP25MR09.007
R min
⎡
Ts ⎤
⎢
⎥
⎢
⎣ Ps M w ⎥
⎦
EP25MR09.006
⎡ 3.056 Qs ⎤
D = ⎢
⎥
⎦
⎣ vs
( Δ p ) )avg
EP25MR09.011
Calculated Nozzle Diameter for Acceptable
Sampling Rate.
(
EP25MR09.010
vs = K p C p
EP25MR09.013
Velocity of Stack Gas. Correct the mean
preliminary velocity pressure for Cp and
blockage using Equations 23, 24, and 25.
EP25MR09.012
⎡ Q (1 − Bws ) Ps ⎤
ΔH = ⎢ s
⎥
Ts
⎣
⎦
12989
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
Minimum Velocity Pressure.
Δ p min = 1.3686 × 10
−4
⎡ Ps M w ⎤
⎢
⎥
⎣ Ts ⎦
⎡ v min ⎤
⎢
⎥
⎢ Cp ⎥
⎣
⎦
2
Eq. 20
EP25MR09.030
Eq. 19
Maximum Velocity Pressure.
2
EP25MR09.029
⎡ Ps M w ⎤ ⎡ v max ⎤
⎥
⎢
⎥ ⎢
⎥
⎣ Ts ⎦ ⎢ Cp ⎦
⎣
Eq. 21
EP25MR09.028
Δ p max = 1.3686 × 10
−4
⎡ Cp ⎤
Δ ps = Δ p m ⎢ ⎥
⎢ Cp ⎥
⎣ ⎦
Eq. 23
Δ p1
⎡
⎤
1
Δ ps 2 = Δ ps 1 ⎢
⎥
⎢ (1 − bf ) ⎥
⎣
⎦
Eq. 26
Eq. 27
Volume of Water Vapor.
Eq. 29
EP25MR09.021
Vws = 0.04707 Vc
Eq. 28
Moisture Content of Gas Stream.
EP25MR09.020
Eq. 30
Qs =
01:35 Mar 25, 2009
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29.92
QsST
528
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⎡
⎤ ⎡ Ts ⎤
1
⎢
⎥ ⎢ ⎥
⎢ (1 − Bws ) ⎥ ⎣ Ps ⎦
⎣
⎦
Fmt 4701
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EP25MR09.019
Sampling Rate.
PWALKER on PROD1PC71 with PROPOSALS3
2
ep25mr09.023
ΔH ⎞ ⎤
⎡⎛
⎢ ⎜ Pbar + 13.6 ⎟ ⎥
⎡ 528 ⎤
⎝
⎠⎥
= ⎢
[ γ Vm ] ⎢
29.92 ⎥
Tm
⎥
⎢
⎣
⎦
⎥
⎢
⎦
⎣
⎤
⎡
Vws
Bws = ⎢
⎥
⎣ Vms + Vws ⎦
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Eq. 25
Velocity Pressure.
Eq. 24
Average Probe Blockage Factor.
Sample Flow Rate at Standard Conditions.
Vms
θ
12.0
A
Dry Gas Volume Sampled at Standard
Conditions.
v ms
QsST =
bf =
2
EP25MR09.026
Adjusted Velocity Pressure.
EP25MR09.025
Δ pn
t n = t1
Eq. 22
)
EP25MR09.024
Sampling Time at Point n. You must use
the actual test run data at each point, n, and
test run point 1.
(
⎤
Δ p1 ⎥ ⎡ t r ⎤
⎥ ⎢N ⎥
Δp
⎢
⎥
⎥ ⎣ tp ⎦
avg ⎦
EP25MR09.022
⎡
t1 = ⎢
⎢
⎢
⎣
EP25MR09.027
Sampling Time at Point 1. Ntp is the total
number of traverse points. You must use the
preliminary velocity traverse data.
Eq. 31
E:\FR\FM\25MRP3.SGM
25MRP3
EP25MR09.018
v max = v n (1.5 )
12990
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
[Note: The viscosity and Reynolds Number
must be recalculated using the actual stack
temperature, moisture, and oxygen content.
Actual Particle Cut Diameter for Cyclone I.
This is based on actual temperatures and
pressures measured during the test run.
0.2091
⎡ Ts ⎤
D50 = 0.15625 ⎢
⎥
⎣ M w Ps ⎦
⎡μ ⎤
⎢ ⎥
⎣ Qs ⎦
0.7091
Eq. 32
Particle Cut Diameter for Nre < 3,162 for
Cyclone IV. C must be recalculated using the
actual test run data and a D50 (Dp) of 2.5.
1.1791
⎡1⎤
⎢C⎥
⎣ ⎦
0.5
⎡ Ts ⎤
⎢
⎥
⎣ Ps M w ⎦
0.6790
0.8058
⎡μ ⎤
D50 = 0.0024302 ⎢ ⎥
⎣ Qs ⎦
⎡1⎤
⎢C⎥
⎣ ⎦
0.5
⎡ Ts ⎤
⎢
⎥
⎣ Ps M w ⎦
0.3058
Equation 33
( N re < 3162 )
Particle Cut Diameter for Nre ≥ 3,162 for
Cyclone IV. C must be recalculated using the
actual test run data and a D50 (Dp) of 2.5.
0.5
Eq. 35
Re-calculated Particle Cut Diameter for Nre
< 3,162.
1.1791
0.5
⎡1⎤
⎢ ⎥
⎣ Cr ⎦
⎡ Ts ⎤
⎢
⎥
⎣ Ps M w ⎦
0.6790
Equation 36
( N re < 3162 )
Re-calculated Particle Cut Diameter for N
≥ 3,162.
0.8058
Ratio (Z) Between D50 and D50–1 Values.
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0.5
⎡ Ts ⎤
⎢
⎥
⎣ Ps M w ⎦
D50 − 1
D50
⎛ D50N
⎜
⎜ D50
N+1
⎝
⎞⎤
⎟ ⎥ ≤ 1.01
⎟⎥
⎠⎦
0.3058
Fmt 4701
Sfmt 4725
Equation 37
< 3162 )
( N re
Acceptance Criteria for Z Values. The
number of iterative steps is represented by N.
Eq. 38
Z=
⎡
0.99 ≤ ⎢ Z =
⎢
⎣
⎡1⎤
⎢ ⎥
⎣ Cr ⎦
EP25MR09.032
D50 −1
⎡μ ⎤
= 0.019723 ⎢ ⎥
⎣ Qs ⎦
Eq. 39
E:\FR\FM\25MRP3.SGM
EP25MR09.034
EP25MR09.035
⎡μ ⎤
D50 −1 = 0.0024302 ⎢ ⎥
⎣ Qs ⎦
EP25MR09.036
EP25MR09.037
⎡ μ ⎤ ⎡ Ts ⎤
Cr = 1 + 0.0057193 ⎢
⎥ ⎢
⎥
⎣ Ps D50 ⎦ ⎣ M w ⎦
EP25MR09.038
appropriate D50 from Equation 32 or 33 (or
Equation 36 or 37 if reiterating).
EP25MR09.033
Re-estimated Cunningham Correction
Factor. You must use the actual test run
Reynolds Number (Nre) value and select the
Equation 34
< 3162 )
( N re
25MRP3
EP25MR09.031
D50
⎡μ ⎤
= 0.019723 ⎢ ⎥
⎣ Qs ⎦
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
12991
Percent Isokinetic Sampling.
⎛
⎞
100 Ts Vms 29.92
I= ⎜
⎜ 60 v ‚ A P (1 − B ) 528 ⎟
⎟
s
n
s
ws
⎝
⎠
Acetone Blank Concentration.
Ca =
ma
Va ρa
Eq. 40
Acetone Blank Weight.
Wa = Ca Vaw ρa
Eq. 41
Concentration of Total Filterable
Particulate Matter.
Eq. 42
⎛ 7000 ⎞ ⎡ M1 + M 2 + M 3 + M 4 ⎤
Ct f = ⎜
⎥
⎟ ⎢
Vms
⎝ 453,592 ⎠ ⎣
⎦
Eq. 43
Concentration of Filterable PM10
Particulate Matter.
⎛ 7000 ⎞ ⎡ M1 + M 3 + M 4 ⎤
CfPM 10 = ⎜
⎥
⎟ ⎢
Vms
⎝ 453,592 ⎠ ⎣
⎦
Eq. 44
Concentration of Filterable PM2.5
Particulate Matter.
17.0 Tables, Diagrams, Flowcharts, and
Validation Data
You must use the following tables,
diagrams, flowcharts, and data to complete
this test method successfully.
PWALKER on PROD1PC71 with PROPOSALS3
TABLE 1—TYPICAL PARTICULATE MATTER CONCENTRATIONS
Particle size range
Concentration and % by weight
Total collectable particulate ......................................................................
≤ 10 and > 2.5 micrometers .....................................................................
≤ 2.5 micrometers .....................................................................................
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40% of total collectable particulate matter.
20% of total collectable particulate matter.
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16.0 References
We used the following references to
develop this test method:
1. Dawes, S.S., and W.E. Farthing.
‘‘Application Guide for Measurement of
PM2.5 at Stationary Sources,’’ U.S.
Environmental Protection Agency,
Atmospheric Research and Exposure
Assessment Laboratory, Research Triangle
Park, NC 27511, EPA–600/3–90/057 (NTIS
No.: PB 90–247198), November 1990.
2. U.S. Environmental Protection Agency,
Federal Reference Methods 1 through 5 and
Method 17, 40 CFR 60, Appendix A.
EP25MR09.043
15.0 Waste Management
[Reserved]
EP25MR09.042
14.0 Pollution Prevention
[Reserved]
3. Richards, J.R. ‘‘Test protocol: PCA PM10/
PM2.5 Emission Factor Chemical
Characterization Testing,’’ PCA R&D Serial
No. 2081, Portland Cement Association,
1996.
4. Farthing and Co-workers, 1988a ‘‘PM10
Source Measurement Methodology: Field
Studies,’’ EPA 600/3–88/055, NTIS PB89–
194287/AS, U.S. Environmental Protection
Agency, Research Triangle Park, NC 27711.
5. Farthing and Dawes, 1988b ‘‘Application
Guide for Source PM10 Measurement with
Constant Sampling Rate,’’ EPA/600/3–88–
057, U.S. Environmental Protection Agency,
Research Triangle Park, NC 27711.
EP25MR09.041
μm particles in laboratory tests (Farthing,
1988b).
EP25MR09.040
13.0 Method Performance
(a) Field evaluation of PM10 and total
particulate matter showed that the precision
of constant sampling rate method was the
same magnitude as Method 17
(approximately 5 percent). Precision in PM10
and PM10 fraction between multiple trains
showed standard deviations of 2 to 4 percent
and total mass compared to 4.7 percent
observed for Method 17 in simultaneous test
runs at a Portland cement clinker cooler
exhaust. The accuracy of the constant
sampling rate PM10 method for total mass,
referenced to Method 17, was ¥2± 4.4
percent. A small bias was found between
Method 201A and Method 17 total
particulate matter (10%) (Farthing, 1988).
(b) Laboratory evaluation and guidance for
PM10 cyclones were designed to limit error
due to spatial variations to 10 percent. The
maximum allowable error due to anisokinetic
sampling was limited to ±20 percent for 10
Eq. 45
EP25MR09.039
⎛ 7000 ⎞ ⎡ M1 + M 4 ⎤
CfPM 2.5 = ⎜
⎥
⎟ ⎢
⎝ 453,592 ⎠ ⎣ Vms
⎦
12992
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
TABLE 2—REQUIRED CYCLONE CUT DIAMETERS (D50)
Min. cut diameter
(Micrometer)
Cyclone
PM10 Cyclone (Cyclone I from five stage cyclone) .................................................................................................
PM2.5 Cyclone (Cyclone IV from five stage cyclone) ..............................................................................................
Max. cut
diameter
(Micrometer)
9
2.25
11
2.75
TABLE 3—PRETEST CALCULATIONS
If you are using . . .
To calculate . . .
Then use . . .
Preliminary data .........................................................................
Dry gas molecular weight (Md) and preliminary moisture content of the gas stream.
Stack gas temperature, and oxygen and moisture content of
the gas stream.
Gas viscosity, μ .........................................................................
Reynolds Number c (Nre) ...........................................................
Nre < 3,162 .................................................................................
D50LL from Equation 5 ...............................................................
dry gas molecular weight, Md ...................................................
wet gas molecular weight, MW .................................................
Equation 1.
Equation 2 a.
gas viscosity, μ .........................................................................
Equation 3.
Cunningham correction factor b, C ...........................................
preliminary lower limit cut diameter for cyclone I, D50LL ..........
Equation 4.
Equation 5.
cut diameter for cyclone I for middle of the overlap zone,
D50T.
final sampling rate for cyclone I, QI(Qs) ...................................
(verify) the assumed Reynolds number ...................................
Equation 6.
D50T from Equation 6 .................................................................
QI(Qs) from Equation 7 ..............................................................
Equation 7.
Equation 8.
a Use Method 4 to determine the moisture content of the stack gas. Use a wet bulb-dry bulb measurement device or hand-held hygrometer to
estimate moisture content of sources with gas temperature less than 160 °F.
b For the lower cut diameter of cyclone IV, 2.25 micrometer.
c Verify the assumed Reynolds number using the procedure in Section 8.5.1, before proceeding to Equation 9.
TABLE 4—DH VALUES BASED ON PRELIMINARY TRAVERSE DATA
Ts¥50°
Stack temperature (°R)
DH, (in. W.C.) ...........................................................................................................................................
Ts
¥
Ts + 50°
¥
¥
TABLE 5—VERIFICATION OF THE ASSUMED REYNOLDS NUMBER
If the Nre is . . .
Then . . .
And . . .
< 3,162 ............................................
≥ 3,162 ............................................
Calculate DH for the meter box.
Recalculate D50LL using Equation 10 ........................
Substitute the ‘‘new’’ D50LL into Equation 6 to recalculate D50T.
TABLE 6—CALCULATIONS FOR RECOVERY OF PM10 AND PM2.5
Calculations
Instructions and references
Average dry gas meter temperature ........................................
Average orifice pressure drop ..................................................
Dry gas volume (Vms) ...............................................................
See field test data sheet.
See field test data sheet.
Use Equation 27 to correct the sample volume measured by the dry gas meter to
standard conditions (20 °C,760 mm Hg or 68 °F, 29.92 in. Hg).
Must be calculated using Equation 28.
Use Equation 29 to determine the water condensed in the impingers and silica
gel combination. Determine the total moisture catch by measuring the change
in volume or weight in the impingers and weighing the silica gel.
Calculate this with Equation 30.
Calculate this with Equation 31.
Use Equation 8 to calculate the actual Reynolds number during test conditions.
Calculate this with Equation 32. This calculation is based on the average temperatures and pressures measured during the test run.
Calculate this with Equation 11.
Calculate this with Equation 40.
Dry gas sampling rate (QsST) ...................................................
Volume of water condensed (Vws) ...........................................
PWALKER on PROD1PC71 with PROPOSALS3
Moisture content of gas stream (Bws) ......................................
Sampling rate (Qs) ....................................................................
Test condition Reynolds numbera ............................................
Actual D50 of Cyclone I ............................................................
Stack gas velocity (vs) ..............................................................
Percent isokinetic rate (%I) ......................................................
a Calculate the Reynolds number at the cyclone IV inlet during the test based on: (1) The sampling rate for the combined cyclone head, (2) the
actual gas viscosity for the test, and (3) the dry and wet gas stream molecular weights.
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Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
BILLING CODE 6560–50–C
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PWALKER on PROD1PC71 with PROPOSALS3
METHOD 202—DRY IMPINGER METHOD
FOR DETERMINING CONDENSABLE
PARTICULATE EMISSIONS FROM
STATIONARY SOURCES
1.0 Scope and Applicability
1.1 Scope. The U.S. Environmental
Protection Agency (U.S. EPA or ‘‘we’’)
developed this method to describe the
procedures that the stack tester (‘‘you’’) must
follow to measure condensable particulate
matter (CPM) emissions from stationary
sources. This method includes procedures for
measuring both organic and inorganic CPM.
1.2 Applicability. You can use this
method to measure CPM from stationary
source emissions after filterable particulate
matter has been removed. CPM is measured
in the emissions after removal from the stack
and after passing through a filter. You can
use Method 17 to collect condensable and
filterable particulate material from sources
operating at stack temperatures and/or
samples collected below 30 °C (85 °F) if the
filter is treated as described in Sections
8.5.4.4 and 11.2.1 of this method. You may
use this method only for stationary source
emission measurements.
1.3 Responsibility. You are responsible
for obtaining the equipment and supplies you
will need to use this method. You must also
develop your own procedures for following
this method and any additional procedures to
ensure accurate sampling and analytical
measurements.
1.4 Results. To obtain reliable results, you
must have a thorough knowledge of the
following test methods that are found in
Appendices A–1 through A–3 and A–6 to
Part 60, and in Appendix M to Part 51:
(a) Method 1—Sample and Velocity
Traverses for Stationary Sources.
(b) Method 2—Determination of Stack Gas
Velocity and Volumetric Flow Rate (Type S
Pitot Tube).
(c) Method 3—Gas Analysis for the
Determination of Dry Molecular Weight.
(d) Method 4—Determination of Moisture
Content in Stack Gases.
(e) Method 5—Determination of Particulate
Matter Emissions from Stationary Sources.
(f) Method 17—Determination of
Particulate Matter Emissions from Stationary
Sources (in-stack filtration method).
(g) Method 201A—Determination of PM10
and PM2.5 Emissions from Stationary Sources
(Constant Sampling Rate Procedure)
1.5 Additional Methods. You will need
additional test methods to measure filterable
particulate matter. You may use this method
to collect CPM in conjunction with Method
5 or 17 of Appendices A–1 through A–3 and
A–6 to Part 60 or, Method 201A of Appendix
M to Part 51. The sample train operation and
front end recovery and analysis are
conducted according to the filterable
particulate method you choose. This method
addresses the equipment, preparation, and
analysis necessary to measure only CPM.
1.6 Limitations. You can use this method
to measure emissions following a wet
scrubber only when this method is combined
with a filterable particulate method that
operates at high enough temperatures to
cause water droplets sampled through the
probe to become gaseous.
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1.7 Conditions. You must maintain
isokinetic sampling conditions to meet the
requirements of the filterable particulate
method used in conjunction with this
method. You must sample at the required
number of sampling points specified in
Method 5, 17, or 201A. Also, if you are using
this method as an alternative to a required
performance test method, you must receive
approval from the appropriate authorities
prior to conducting the test.
2.0 Summary of Method
2.1 Summary. The CPM is collected in
dry impingers after filterable particulate
material has been collected on filters
maintained above 30 °C (85 °F) using Method
5, 17, or 201A. The organic and aqueous
fractions of the impingers and an out-of-stack
CPM filter are then taken to dryness and
weighed. The total of all fractions represents
the CPM. Compared to the December 17,
1991 promulgated Method 202, this method
removes water from the impingers and
includes the addition of a condenser
followed by a water dropout impinger
immediately after the final in-stack or heated
filter. This method also includes the addition
of one modified Greenburg Smith impinger
and a CPM filter following the water dropout
impinger. Figure 1 of Section 18 presents the
schematic of the sampling train configured
with these changes.
2.1.1 Condensable Particulate Matter.
CPM is collected in the water dropout
impinger, the modified Greenburg Smith
impinger, and the CPM filter of the sampling
train as described in this method. The
impinger contents are purged with nitrogen
(N2) immediately after sample collection to
remove dissolved sulfur dioxide (SO2) gases
from the impinger. The CPM filter is
extracted with water and methylene chloride.
The impinger solution is then extracted with
methylene chloride (MeCl2). The organic and
aqueous fractions are dried and the residues
are weighed. The total of the aqueous and
organic fractions represents the CPM.
2.1.2 Dry Impinger and Additional Filter.
The potential artifacts from SO2 are reduced
using a condenser and dropout impinger to
separate CPM from reactive gases. No water
is added to the impingers prior to the start
of sampling. To improve the collection
efficiency of CPM, an additional filter (the
CPM filter) is placed between the second and
third impingers.
3.0 Definitions
3.1 Primary PM. Primary PM (also known
as direct PM) means particles that enter the
atmosphere as a direct emission from a stack
or an open source. Primary PM comprises
two components: filterable PM and
condensable PM. These two PM components
have no upper particle size limit.
3.2 Filterable PM. Filterable PM means
particles that are emitted directly by a source
as a solid or liquid at stack or release
conditions and captured on the filter of a
stack test train.
3.3 Primary PM10. Primary PM10 (also
known as direct PM10, total PM10, PM10 or
filterable PM10, and condensable PM,
individually) means particulate matter with
an aerodynamic diameter equal to or less
than 10 micrometers.
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3.4 Primary PM2.5. Primary PM2.5 (also
known as direct PM2.5, total PM2.5, PM2.5, or
filterable PM2.5, and condensable PM,
individually) means solid particles emitted
directly from an air emissions source or
activity, or gaseous emissions or liquid
droplets from an air emissions source or
activity that condense to form particulate
matter at ambient temperatures. Direct PM2.5
emissions include elemental carbon, directly
emitted organic carbon, directly emitted
sulfate, directly emitted nitrate, and other
inorganic particles (including but not limited
to crustal material, metals, and sea salt).
3.5 Condensable PM (CPM). Condensable
PM means material that is vapor phase at
stack conditions, but which condenses and/
or reacts upon cooling and dilution in the
ambient air to form solid or liquid PM
immediately after discharge from the stack.
Note that all condensable PM is assumed to
be in the PM2.5 size fraction (Reference: Part
51, Subpart Z (51.1000)).
4.0
Interferences [Reserved]
5.0 Safety
Disclaimer: You may have to use
hazardous materials, operations, and
equipment while performing this method.
We do not provide information on
appropriate safety and health practices. You
are responsible for determining the
applicability of regulatory limitations and
establishing appropriate safety and health
practices. Handle materials and equipment
properly.
6.0 Equipment and Supplies
The equipment used in the filterable
particulate portion of the sampling train is
described in Methods 5 and 17 of Appendix
A–1 through A–3 and A–6 to Part 60 and
Method 201A in Appendix M to Part 51. The
equipment used in the CPM portion of the
train is described in this section.
6.1 Condensable Particulate Sampling
Train Components. The sampling train for
this method is consistent with the sampling
train for collecting filterable particulate using
Method 5, 17, or 201A with the following
exceptions or additions:
6.1.1 Condenser and Impingers. You must
add the following components to the
filterable particulate sampling train: A
Method 23 type condenser as described in
Section 2.1.2 of Method 23 of Appendix A–
8 to Part 60, followed by a dropout impinger
or flask, followed by a modified GreenburgSmith impinger with an open tube tip as
described in Section 6.1.1.8 of Method 5.
6.1.2 CPM Filter Holder. The modified
Greenburg-Smith impinger is followed by a
filter holder that is either glass, stainless steel
(316 or equivalent), or Teflon®-coated
stainless steel. Commercial size filter holders
are available depending on project
requirements. Use a commercial filter holder
capable of supporting 47 mm or greater
diameter filters. Commercial size filter
holders contain a Teflon® O-ring, stainless
steel, ceramic or Teflon® filter support and
a final Teflon® O-ring. At the exit of the CPM
filter, install a Teflon®-coated or stainless
steel encased thermocouple that is in contact
with the gas stream.
6.1.3 Long Stem Impinger Insert. You will
need a long stem modified Greenburg Smith
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PWALKER on PROD1PC71 with PROPOSALS3
impinger insert for the dropout impinger to
perform the nitrogen purge of the sampling
train.
6.2 Sample Recovery Equipment.
6.2.1 Condensable Particulate Matter
Recovery.
6.2.1.1 Nitrogen Purge Line. You must
use inert tubing and fittings capable of
delivering at least 20 liters/min of nitrogen
gas to the impinger train from a standard gas
cylinder (see Figure 2 of Section 18). You
may use standard 0.6 cm (1/4-in.) tubing and
compression fittings in conjunction with an
adjustable pressure regulator and needle
valve.
6.2.1.2 Rotameter. You must use a
rotameter capable of measuring gas flow up
to 20 L/min. The rotameter must be accurate
to 5 percent of full scale.
6.2.1.3 Ultra-high Purity (UHP) Nitrogen
Gas. Compressed ultra-pure nitrogen,
regulator, and filter must be capable of
providing at least 20 L/min purge gas for 1
hour through the sampling train.
6.3 Analysis. The following equipment is
necessary for CPM sample recovery and
analysis:
6.3.1 Separatory Funnel. Glass, 1 liter.
6.3.2 Weighing Tins. 50 mL.
6.3.3 Glass Beakers. 300 to 500 mL.
6.3.4 Drying Equipment. Hot plate or
oven with temperature control.
6.3.5 Pipets. 5 mL.
6.3.6 Burette. Glass, 0 to 100 mL in 0.1
mL graduations.
6.3.7 Analytical Balance. Analytical
balance capable of weighing 0.0001 g (0.1
milligram). For extremely low emission
sources, a balance capable of weighing
0.00001 g (0.01 milligram) may be required.
6.3.8 pH Meter. A meter capable of
determining the acidity of liquid within 0.1
pH units.
7.0 Reagents and Standards
7.1 Sample Collection. To collect a
sample, you will need a Teflon® filter,
crushed ice, and silica gel. You must also
have water and nitrogen gas to purge the
sampling train. You will find additional
information on each of these items in the
following summaries.
7.1.1 Filter. You must use a Teflon®
membrane filter that does not have an
organic binder. The filter must also have an
efficiency of at least 99.95 percent (<0.05
percent penetration) on 0.3 micron particles.
You may use test data from the supplier’s
quality control program to document filter
efficiency. If the source you are sampling has
SO2 or sulfur trioxide (SO3) emissions, then
you must use a filter that will not react with
SO2 or SO3. Depending on your application
and project data quality objectives (DQOs),
filters are commercially available in 47 mm
and larger sizes.
7.1.2 Silica Gel. Use an indicating-type
silica gel of 6 to 16 mesh. We must approve
other types of desiccants (equivalent or
better) before you use them. Allow the silica
gel to dry for 2 hours at 175 °C (350 °F) if
it is being reused. You do not have to dry
new silica gel.
7.1.3 Water. Use deionized distilled ultrafiltered water (to conform to ASTM D1193–
06, Type 1 water or equivalent) (incorporated
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by reference) to recover material caught in
the impinger, if required. The Director of the
Federal Register approves this incorporation
by reference in accordance with 5 U.S.C.
552(a) and 1 CFR part 51. You may obtain a
copy from American Society for Testing and
Materials (ASTM), 100 Barr Harbor Drive,
Post Office Box C700, West Conshohocken,
PA 19428–2959. You may inspect a copy at
the Office of Federal Register, 800 North
Capitol Street, NW., Suite 700, Washington,
DC.
7.1.4 Crushed Ice. Obtain from the best
readily available source.
7.1.5 Nitrogen Gas. Use Ultra-High Purity
(UHP) compressed nitrogen or equivalent to
purge the sampling train. The compressed
nitrogen you use to purge the sampling train
must contain no more than 1 ppm oxygen, 1
ppm total hydrocarbons as carbon, and 2
ppm moisture.
7.2 Sample Recovery and Analytical
Reagents. You will need acetone, MeCl2,
anhydrous sodium sulfate, ammonia
hydroxide (NH4OH), and deionized water for
the sample recovery and analysis. Unless
otherwise indicated, all reagents must
conform to the specifications established by
the Committee on Analytical Reagents of the
American Chemical Society. If such
specifications are not available, then use the
best available grade. Find additional
information on each of these items in the
following paragraphs:
7.2.1 Acetone. Use acetone that is stored
in a glass bottle. Do not use acetone from a
metal container because it normally produces
a high residue blank. You must use acetone
with blank values <1 ppm, by weight,
residue.
7.2.2 Methylene Chloride, American
Chemical Society (ACS) grade. You must use
methylene chloride with a blank value <1.5
ppm, by weight, residue.
7.2.3 Water. Use deionized distilled ultrafiltered water (to conform to ASTM D1193–
06, Type 1 or equivalent) (incorporated by
reference) to recover material caught in the
impinger.
7.2.4 Condensable Particulate Sample
Desiccant. Use indicating-type anhydrous
sodium sulfate to desiccate water and organic
extract residue samples.
7.2.5 Ammonium Hydroxide. Use NIST
traceable or equivalent (0.1 N) NH4OH.
7.2.6 Standard Buffer Solutions. Use one
buffer with a neutral pH and a second buffer
solution with an acid pH.
8.0 Sample Collection, Preservation,
Storage, and Transport
8.1 Qualifications. This is a complex test
method. To obtain reliable results, you must
be trained and experienced with in-stack
filtration systems (such as, cyclones,
impactors, and thimbles) and impinger and
moisture train systems.
8.2 Preparations. You must clean
glassware prior to field tests as described in
Section 8.4, including baking glassware at
300 °C for 6 hours prior to use. Cleaned,
baked glassware is used at the start of each
new source category tested. Analyze reagent
blanks (water, acetone, and methylene
chloride) before field tests to verify low blank
concentrations. Follow the pretest
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preparation instructions in Section 8.1 of
Method 5.
8.3 Site Setup. You must follow the
procedures required by filterable particulate
sampling method setup run in conjunction
with this method including:
(a) Determining the sampling site location
and traverse points.
(b) Calculating probe/cyclone blockage.
(c) Verifying the absence of cyclonic flow.
(d) Completing a preliminary velocity
profile, and selecting a nozzle(s).
8.3.1 Sampling Site Location and
Traverse Point. Determination. Follow the
standard procedures in Method 1 of
Appendix A–1 to Part 60 to select the
appropriate sampling site. Then you must do
all of the following:
8.3.1.1 Sampling site. Choose a location
that maximizes the distance from upstream
and downstream flow disturbances.
8.3.1.2 Traverse points. Use the
recommended maximum number of traverse
points at any location, as found in Methods
5, 17, or 201A, whichever is applicable to
your test requirements. You must prevent the
disturbance and capture of any solids
accumulated on the inner wall surfaces by
maintaining a 1-inch distance from the stack
wall (1⁄2 inch for sampling locations less than
24 inches in diameter).
8.4 Sampling Train Preparation. A
schematic of the sampling train used in this
method is shown in Figure 1 of Section 18.
All sampling train glassware must be cleaned
prior to the test with soap and water, and
rinsed using tap water, deionized water,
acetone, and finally, MeCl2. It is important to
completely remove all silicone grease from
areas that will be exposed to the MeCl2 rinse
during sample recovery. After cleaning, you
must bake glassware at 300 °C for 6 hours
prior to each source type sampled. Prior to
each sampling run, the train glassware used
to collect condensable particulate matter
must be rinsed thoroughly with deionized,
distilled ultra-filtered water that conforms to
ASTM D1193–06, Type 1 or equivalent
(incorporated by reference).
8.4.1 Condenser and Dropout Impinger.
Add a Method 23 type condenser and a
condensate dropout impinger without
bubbler tube after the final in-stack or out-ofstack hot filter assembly. The Method 23 type
stack gas condenser is described in Section
2.1.2 of Method 23. It must be capable of
cooling the stack gas to less than 30 °C (85
°F).
8.4.2 Backup Impinger. The dropout
impinger is followed by a modified
Greenburg Smith impinger with no taper (see
Figure 1 of Section 18). Place the dropout
and other impingers in an insulated box with
water at ≤ 30 °C (≤ 85 °F). At the start of the
tests, the water dropout and backup impinger
must be clean, without any water or reagent
added.
8.4.3 CPM Filter. Place a filter holder
with a filter meeting the requirements in
Section 6.1.2 following the modified
Greenburg-Smith impinger. The connection
between the CPM filter and the moisture trap
impinger includes a thermocouple fitting that
provides a leak-free seal between the
thermocouple and the stack gas.
[Note: A thermocouple well is not
sufficient for this purpose because the
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Teflon® or steel encased thermocouple must
be in contact with the sample gas).]
8.4.4 Moisture Traps. You must use a
modified Greenburg-Smith impinger
containing 100 mL of water or the alternative
described in Method 5 followed by an
impinger containing silica gel to collect
moisture that passes through the CPM filter.
You must maintain the gas temperature
below 20°C (68 °F) at the exit of the moisture
traps.
8.4.5 Silica Gel Trap. Place 200 to 300 g
of silica gel in each of several air-tight
containers. Weigh each container, including
silica gel, to the nearest 0.5 g, and record this
weight on the filterable particulate data
sheet. As an alternative, the silica gel need
not be preweighed, but may be weighed
directly in its impinger or sampling holder
just prior to train assembly.
8.4.6 Leak-Check (Pretest). Use the
procedures outlined in Method 5, 17, or
201A as appropriate to leak check the entire
sampling system. Specifically, perform the
following procedures:
8.4.6.1 Sampling Train. You must pretest
the entire sampling train for leaks. The
pretest leak-check must have a leak rate of
not more than 0.02 actual cubic feet per
minute (ACFM) or 4 percent of the average
sample flow during the test run, whichever
is less. Additionally, you must conduct the
leak-check at a vacuum equal to or greater
than the vacuum anticipated during the test
run. Enter the leak-check results on the field
test data sheet for the filterable particulate
method.
(Note: Conduct leak-checks during port
changes only as allowed by the filterable
particulate method used with this method).
8.4.6.2 Pitot Tube Assembly. After you
leak-check the sample train, perform a leakcheck of the pitot tube assembly. Follow the
procedures outlined in Section 8.4.1 of
Method 5.
8.5 Sampling Train Operation. Operate
the sampling train as described in the
filterable particulate sampling method (i.e.,
Method 5, 17, or 201A) with the following
additions or exceptions:
8.5.1 CPM Filter Assembly. On the field
data sheet for the filterable particulate
method, record the CPM filter temperature
readings at the beginning of each sample time
increment and when sampling is halted.
Maintain the CPM filter ≤30 °C (≤85 °F)
during sample collection.
8.5.2 Leak-Check Probe/Sample Train
Assembly (Post-Test). Conduct the leak rate
check according to the filterable particulate
sampling method used during sampling. If
required, conduct the leak-check at a vacuum
equal to or greater than the maximum
vacuum achieved during the test run. If the
leak rate of the sampling train exceeds 0.02
ACFM or 4 percent of the average sampling
rate during the test run (whichever is less),
then the run is invalid and you must repeat
it.
8.5.3 Post-Test Nitrogen Purge. As soon
as possible after the post-test leak-check,
detach the probe, any cyclones, and in-stack
or hot filters from the condenser and
impinger train. Leave the ice in the second
impinger box to prevent removal of moisture
during the purge. If necessary, add more ice
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during the purge to maintain the gas
temperature measured at the exit of the silica
gel impinger below 20 °C (68 °F).
8.5.3.1 If no water was collected before
the CPM filter, then you may skip the
remaining purge steps and proceed with
sample recovery (see Section 8.5.4).
8.5.3.2 Replace the short stem impinger
insert with a modified Greenberg Smith
impinger insert. The impinger tip length
must extend below the water level in the
impinger catch. If insufficient water was
collected, you must add a measured amount
of degassed deionized, distilled ultra-filtered
ASTM D1193–06, Type 1 or equivalent)
(incorporated by reference) water until the
impinger tip is at least 1 cm below the
surface of the water. You must record the
amount of water added to the dropout
impinger (see Figure 4 of Section 18) to
correct the moisture content of the effluent
gas.
(Note: Prior to use, water must be degassed
using a nitrogen purge bubbled through the
water for at least 15 minutes to remove
dissolved oxygen).
8.5.3.3 With no flow of gas through the
clean purge line and fittings, attach the line
to a purged inline filter. Connect the filter
outlet to the input of the impinger train (see
Figure 2 of Section 18). To avoid over- or
under-pressurizing the impinger array,
slowly commence the nitrogen gas flow
through the line while simultaneously
opening the meter box pump valve(s). Adjust
the pump bypass and nitrogen delivery rates
to obtain the following conditions: (1) 20
liters/min or DH@, and (2) a positive overflow
rate through the rotameter of less than 2
liters/min. Condition (2) guarantees that the
nitrogen delivery system is operating at
greater than ambient pressure and prevents
the possibility of passing ambient air (rather
than nitrogen) through the impingers. During
the purge, continue operation of the
condenser recirculation pump, and heat or
cool the water surrounding the first two
impingers to maintain the gas temperature
measured at the exit of the CPM filter below
30 °C (85 °F). Continue the purge under these
conditions for 1 hour, checking the rotameter
and DH value(s) periodically. After 1 hour,
simultaneously turn off the delivery and
pumping systems.
8.5.3.4 Weigh the liquid, or measure the
volume of the liquid collected in the dropout,
impingers, and silica trap. Measure the liquid
in the first impinger to within 1 mL using a
clean graduated cylinder or by weighing it to
within 0.5 g using a balance. Record the
volume or weight of liquid present to be used
to calculate the moisture content of the
effluent gas in the field log notebook.
8.5.3.5 If a balance is available in the
field, weigh the silica impinger to within 0.5
g. Note the color of the indicating silica gel
in the last impinger to determine whether it
has been completely spent, and make a
notation of its condition in the field log book.
8.5.4 Sample Recovery.
8.5.4.1 Recovery of Filterable Particulate
Matter. Recovery of filterable particulate
matter involves the quantitative transfer of
particles according to the filterable
particulate sampling method (i.e., Method 5,
17 or 201A).
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8.5.4.2 CPM Container #1, Aqueous
Liquid Impinger Contents. Quantitatively
transfer liquid from the dropout and the
impinger prior to the CPM filter into a clean
sample bottle (glass or plastic). Rinse the
probe extension, condenser, each impinger
and the connecting glassware, and the front
half of the CPM filter housing twice with
water. Recover the rinse water, and add it to
the same sample bottle. Mark the liquid level
on the bottle. CPM Container #1 holds the
water soluble CPM captured in the
impingers.
8.5.4.3 CPM Container #2, Organic
Rinses. Follow the water rinses of the probe
extension, condenser, each impinger and all
of the connecting glassware and front half of
the CPM filter with an acetone rinse. Then
repeat the entire procedure with two rinses
of MeCl2, and save both solvents in a separate
glass container identified as CPM Container
#2. Mark the liquid level on the jar.
8.5.4.4 CPM Container #3, CPM filter
Sample. Use tweezers and/or clean
disposable surgical gloves to remove the filter
from the CPM filter holder. Place the filter in
the petri dish identified as CPM Container
#3.
8.5.4.5 CPM Container #4, Cold Impinger
Water. You must weigh or measure the
volume of the contents of CPM Container #4
either in the field or during sample analysis
(see Section 11.2.3). If the water from the
cold impinger has been weighed in the field,
it can be discarded. Otherwise, quantitatively
transfer liquid from the cold impinger that
follows the CPM filter into a clean sample
bottle (glass or plastic). Mark the liquid level
on the bottle. This container holds the
remainder of the liquid water from the
emission gases.
8.5.4.6 CPM Container #5, Silica Gel
Absorbent. You must weigh the contents of
CPM Container #5 in the field or during
sample analysis (see Section 11.2.4). If the
silica gel has been weighed in the field to
measure water content, then it can be
discarded. Otherwise, transfer the silica gel
to its original container and seal. A funnel
may make it easier to pour the silica gel
without spilling. A rubber policeman may be
used as an aid in removing the silica gel from
the impinger. It is not necessary to remove
the small amount of silica gel dust particles
that may adhere to the impinger wall and are
difficult to remove. Since the gain in weight
is to be used for moisture calculations, do not
use any water or other liquids to transfer the
silica gel.
8.5.4.7 CPM Container #6, Acetone Rinse
Blank. Take 150 mL of the acetone directly
from the wash bottle you used, and place it
in CPM Container #6, labeled Acetone Rinse
Blank (see Section 11.2.5 for analysis). Mark
the liquid level on the bottle.
8.5.4.8 CPM Container #7, Water Rinse
Blank. Take 150 mL of the water directly
from the wash bottle you used, and place it
in CPM Container #7, labeled Water Rinse
Blank (see Section 11.2.6 for analysis). Mark
the liquid level on the bottle.
8.5.4.9 CPM Container #8, Methylene
Chloride Rinse Blank. Take 150 mL of the
MeCl2 directly from the wash bottle you
used, and place it in CPM Container #8,
labeled Methylene Chloride Rinse Blank (see
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Section 11.2.7 for analysis). Mark the liquid
level on the bottle.
8.5.5 Transport procedures. Containers
must remain in an upright position at all
times during shipping. You do not have to
ship the containers under dry or blue ice.
However, samples must be maintained at or
below 30 °C (85 °F) during shipping.
9.0 Quality Control
9.1 Daily Quality Checks. You must
perform daily quality checks of field log
books and data entries and calculations using
data quality indicators from this method and
your site-specific test plan. You must review
and evaluate recorded and transferred raw
data, calculations, and documentation of
testing procedures. You must initial or sign
log book pages and data entry forms that
were reviewed.
9.2 Calculation Verification. Verify the
calculations by independent, manual checks.
You must flag any suspect data and identify
the nature of the problem and potential effect
on data quality. After you complete the test,
prepare a data summary and compile all the
calculations and raw data sheets.
9.3 Conditions. You must document data
and information on the process unit tested,
the particulate control system used to control
emissions, any non-particulate control
system that may affect particulate emissions,
the sampling train conditions, and weather
conditions. Discontinue the test if the
operating conditions may cause nonrepresentative particulate emissions.
9.4 Health and Safety Plan. Develop a
health and safety plan to ensure the safety of
your employees who are on-site conducting
the particulate emission test. Your plan must
conform with all applicable Occupational
Safety and Health Administration (OSHA),
Mine Safety and Health Administration
(MSHA), and Department of Transportation
(DOT) regulatory requirements. The
procedures must also conform to the plant
health and safety requirements.
9.5 Calibration Checks. Perform
calibration check procedures on analytical
balances each time they are used.
9.6 Glassware. Use class A volumetric
glassware for titrations, or calibrate your
equipment against National Institute of
Standards and Technology (NIST) traceable
glassware.
9.7 Analytical Balance. Check the
calibration of your analytical balance each
day you weigh CPM samples. You must use
NIST Class S weights at a mass
approximately equal to the weight of the
sample plus container you will weigh.
9.8 Reagent Blanks. You must run blanks
of water, acetone, and methylene chloride
used for field recovery and sample analysis.
Analyze at least one sample (100 mL
minimum) of each reagent that you plan to
use for sample recovery and analysis before
you begin testing. Running blanks before
field use will verify low blank
concentrations, thereby reducing the
potential for a high field blank on test
samples.
9.9 Field Reagent Blanks. You must run
at least one field blank of water, acetone, and
methylene chloride you use for field
recovery. Running independent reagent field
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blanks will verify that low blank
concentrations were maintained during field
solvent use and demonstrate that reagents
have not been contaminated during field
tests.
9.10 Field Train Blank. You must recover
a minimum of one field train blank for each
set of compliance tests at the facility. You
must assemble the sampling train as it will
be used for testing. Prior to the purge, you
must add 100 mL of water to the first
impinger and record this data on Figure 3.
You must purge the assembled train as
described in Sections 8.5.3.2. and 8.5.3.3.
You must recover field train blank samples
as described in Section 8.5.4. From the field
sample weight, you will subtract the
condensable particulate mass you determine
with this blank train or 0.002 g (2.0 mg),
whichever is less.
9.11 Audit Procedure. Concurrent with
compliance sample analysis, and if available,
analyze audit material to evaluate the
technique of the analyst and the standards
preparation. Use the same staff, analytical
reagents, and analytical system for both
compliance samples and the EPA audit
sample. If this condition is met, auditing of
subsequent compliance analyses for the same
enforcement agency within 30 days is not
required. An audit sample set may not be
used to validate different sets of compliance
samples under the jurisdiction of different
enforcement agencies, unless prior
arrangements are made with both
enforcement agencies.
9.12 Audit Samples. As of the publication
date of this test method, audit materials are
not available. If audit materials become
available, audit samples will be supplied
only to enforcement agencies for compliance
tests. Audit samples can be requested by a
State agency. Audit materials are requested
online by authorized regulatory authorities at
the following internet address: https://
www.sscap.net/. Authorization can be
obtained by contacting an EPA Emission
Measurement Center QA Team Member
listed on the EPA TTN Web site at the
following internet address: https://
www.epa.gov/ttn/emc/email.html#qaqc. The
request for the audit sample must be made
at least 30 days prior to the scheduled
compliance sample analysis.
9.13 Audit Results. Calculate the audit
sample concentration according to the
calculation procedure described in the audit
instructions included with the audit sample.
Fill in the audit sample concentration and
the analyst’s name on the audit response
form included with the audit instructions.
Send one copy to the EPA Regional Office or
the appropriate enforcement agency.
10.0 Calibration and Standardization
Maintain a log of all condensable
particulate sampling and analysis
calibrations. Include copies of the relevant
portions of the calibration and field logs in
the final test report.
10.1 Thermocouple Calibration. You
must calibrate the thermocouples using the
procedures described in Section 10.1.4.1.2 of
Method 2 of Appendix A–1 to Part 60.
Calibrate each temperature sensor at a
minimum of three points over the anticipated
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range of use against an NIST-traceable
mercury-in-glass thermometer.
10.2 Ammonium Hydroxide. The 0.1 N
NH4OH used for titrations in this method is
made as follows: Add 7 mL of concentrated
(14.8 M) NH4OH to l liter of water.
Standardize against standardized 0.1 N
H2SO4, and calculate the exact normality
using a procedure parallel to that described
in Section 5.5 of Method 6 of Appendix A–
4 to 40 CFR part 60. Alternatively, purchase
0.1 N NH4OH that has been standardized
against a NIST reference material. Record the
normality on the Condensable Particulate
Matter Work Table (see Figure 5 of Section
18).
11.0 Analytical Procedures
11.1 Analytical Data Sheets. (a) Record
the filterable particulate field data on the
appropriate (i.e., Method 5, 17, or 201A)
analytical data sheets. Alternatively, data
may be recorded electronically using
software applications such as the Electronic
Reporting Tool (ERT), available at the
following internet address: https://
www.epa.gov/ttn/chief/ert/ert_tool.html.
Record the condensable particulate data on
the Condensable Particulate Matter Work
Table (see Figure 5 of Section 18).
(b) Measure the liquid in all containers
either volumetrically to ± 1 mL or
gravimetrically to ± 0.5 g. Confirm on the
filterable particulate analytical data sheet
whether leakage occurred during transport. If
a noticeable amount of leakage has occurred,
either void the sample or use methods,
subject to the approval of the Administrator,
to correct the final results.
11.2 Condensable Particulate Matter
Analysis. See the flow chart in Figure 6 of
Section 18 for the steps to process and
combine fractions from the CPM train.
11.2.1 Container #3, CPM Filter Sample.
Extract the filter recovered from the low
temperature portion of the train, and
combine the extracts with the organic and
inorganic fractions resulting from the
aqueous impinger sample recovery. If the
sample was collected by Method 17 because
the stack temperature was below 30 °C (85
°F), process the filter extracts as described in
this section without combination with any
other portion from the train.
11.2.1.1 Extract the water soluble
(aqueous or inorganic) CPM from the CPM
filter as described in this section. Fold the
CPM filter in quarters, and place it into a 50
mL extraction tube. Add sufficient deionized
ultra-filtered water to cover the filter (e.g., 10
mL of water). Place the extractor tube into a
sonication bath and extract the water soluble
material for a minimum of 2 minutes.
Combine the aqueous extract with the
contents of Container #1. Repeat this
extraction step twice for a total of three
extractions.
11.2.1.2 Extract the organic soluble CPM
from the CPM filter as described in this
section. Add sufficient methylene chloride to
cover the filter (e.g., 10 mL of water). Place
the extractor tube into a sonication bath and
extract the organic soluble material for a
minimum of 2 minutes. Combine the organic
extract with the contents of Container #2.
Repeat this extraction step twice for a total
of three extractions.
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evaporation, desiccate the residue for 24
hours in a desiccator containing anhydrous
calcium sulfate. Weigh at intervals of at least
6 hours to a constant weight (i.e., ≤ 0.5 mg
change from previous weighing), and report
results to the nearest 0.1 mg on Figure 3.
12.0 Calculations and Data Analysis
12.1 Nomenclature. Report results in
International System of Units (SI units)
unless the regulatory authority for
compliance testing specifies English units.
The following nomenclature is used.
DH@ = Pressure drop across orifice at flow
rate of 0.75 SCFM at standard conditions,
in. W.C.
[Note: specific to each orifice and meter
box.]
12.2 Calculations. Use the following
equations to complete the calculations
required in this test method. Enter the
appropriate results from these calculations
on the Condensable Particulate Matter Work
Table (see Figure 5 of Section 18).
12.2.1 Mass of ammonia correction.
Correction for ammonia added during
titration of 100 mL aqueous CPM sample.
This calculation assumes no waters of
hydration.
m C = 17.03 × v t × N
Eq. 1
12.2.2 Mass of the Field Blank (mg). Per
Section 9.9, the mass of the field blank, mfb,
shall not exceed 2.0 mg.
m fb = mib + m ob
12.2.3
mi = m r − m c
12.2.4
E:\FR\FM\25MRP3.SGM
Eq. 3
Total Mass of CPM (mg).
m cpm = mi + m o − m fb
12.2.5
Eq. 2
Mass of Inorganic CPM (mg).
Eq. 4
Concentration of CPM (mg/dscf).
25MRP3
EP25MR09.048
17.03 = mg/milliequivalents for ammonium
ion.
ACFM = Actual cubic feet per minute.
Ccpm = Concentration of the condensable
particulate matter in the stack gas, dry
basis, corrected to standard conditions,
milligrams/dry standard cubic foot.
mc = Mass of the NH4∂ added to sample to
form ammonium sulfate, mg.
mcpm = Mass of the total condensable
particulate matter, mg.
mfb = Mass of field train total CPM blank, mg
mi = Mass of inorganic CPM matter, mg.
mib = Mass of field train inorganic CPM
blank, mg.
mo = Mass of organic CPM, mg.
mob = Mass of organic field train blank, mg.
mr = Mass of dried sample from inorganic
fraction, mg.
N = Normality of ammonium hydroxide
titrant.
Vm(std) = Volume of gas sample measured by
the dry gas meter, corrected to standard
conditions, dry standard cubic meter
(dscm) or dry standard cubic foot (dscf) as
defined in Equation 5–1 of Method 5.
Vt = Volume of NH4OH titrant, mL.
Vp = Volume of water added during train
purge.
EP25MR09.047
determined in the field, note the level of
liquid in the container, and confirm on the
filterable particulate analytical data sheet
whether leakage occurred during transport. If
a noticeable amount of leakage has occurred,
either void the sample or use methods,
subject to the approval of the Administrator,
to correct the final results. Measure the liquid
in Container #4 either volumetrically to ± 1
mL or gravimetrically to ± 0.5 g, and record
the volume or weight on the filterable
particulate analytical data sheet of the
filterable particulate matter test method.
11.2.4 CPM Container #5, Silica Gel
Absorbent. Weigh the spent silica gel (or
silica gel plus impinger) to the nearest 0.5 g
using a balance. This step may be conducted
in the field. Record the weight on the
filterable particulate analytical data sheet of
the filterable particulate matter test method.
11.2.5 Container #6, Acetone Field Rinse
Blank. Use 100 mL of acetone from the blank
container for this analysis. If insufficient
liquid is available or if the acetone has been
lost due to container breakage, either void the
sample, or use methods, subject to the
approval of the Administrator, to correct the
final results. Transfer 100 mL of the acetone
to a clean 250-mL beaker. Evaporate the
acetone at room temperature (not to exceed
30 °C (85 °F)) and pressure in a laboratory
hood to approximately 10 mL. Quantitatively
transfer the beaker contents to a 50-mL
preweighed tin, and evaporate to dryness at
room temperature (not to exceed 30 °C (85
°F)) and pressure in a laboratory hood.
Following evaporation, desiccate the residue
for 24 hours in a desiccator containing
anhydrous calcium sulfate. Weigh at
intervals of at least 6 hours to a constant
weight (i.e., ≤ 0.5 mg change from previous
weighing), and report results to the nearest
0.1 mg on Figure 3.
11.2.6 Water Rinse Field Blank, Container
#7. Use 100 mL of the water from the blank
container for this analysis. If insufficient
liquid is available, or if the water has been
lost due to container breakage, either void the
sample, or use methods, subject to the
approval of the Administrator, to correct the
final results. Transfer the water to a clean
250-mL beaker, and evaporate to
approximately 10 mL liquid in the oven at
105 °C. Quantitatively transfer the beaker
contents to a clean preweighed 50-mL tin,
and evaporate to dryness at room
temperature (not to exceed 30 °C (85 °F)) and
pressure in a laboratory hood. Following
evaporation, desiccate the residue for 24
hours in a desiccator containing anhydrous
calcium sulfate. Weigh at intervals of at least
6 hours to a constant weight (i.e., ≤ 0.5 mg
change from previous weighing) and report
results to the nearest 0.1 mg on Figure 3.
11.2.7 Methylene Chloride Field Reagent
Blank, Container #8. Use 100 mL of MeCl2
from the blank container for this analysis.
Transfer 100 mL of the MeCl2 to a clean 250mL beaker. Evaporate the methylene chloride
at room temperature (not to exceed 30 °C (85
°F)) and pressure in a laboratory hood to
approximately 10 mL. Quantitatively transfer
the beaker contents to a 50-mL preweighed
tin, and evaporate to dryness at room
temperature (not to exceed 30 °C (85 °F)) and
pressure in a laboratory hood. Following
EP25MR09.046
11.2.2 CPM Container #1, Aqueous
Liquid Impinger Contents. Analyze the water
soluble CPM in Container 1 as described in
this section. Place the contents of Container
#1 into a separatory funnel. Add
approximately 30 mL of MeCl2 to the funnel,
mix well, and drain off the lower organic
phase. Repeat this procedure twice with 30
mL of MeCl2 each time combining the
organic phase from each extraction. Each
time, leave a small amount of the organic/
MeCl2 phase in the separatory funnel,
ensuring that no water is collected in the
organic phase. This extraction should yield
about 90 mL of organic extract.
11.2.2.1 CPM Container #2. Combine the
organic extract from Container #1 with the
organic train rinse in Container 2.
11.2.2.2 Organic Fraction Weight
Determination. Place the organic phase in a
clean glass beaker. Evaporate the organic
extract at room temperature (not to exceed 30
°C (85 °F)) and pressure in a laboratory hood
to not less than 10 mL. Quantitatively
transfer the beaker contents to a 50-mL
preweighed tin, and evaporate to dryness at
room temperature (not to exceed 30 °C (85
°F)) and pressure in a laboratory hood.
Following evaporation, desiccate the organic
fraction for 24 hours in a desiccator
containing anhydrous calcium sulfate. Weigh
at intervals of at least 6 hours to a constant
weight (i.e., ≤ 0.5 mg change from previous
weighing), and report results to the nearest
0.1 mg on the Condensable Particulate Matter
Work Table (see Figure 5 of Section 18).
11.2.2.3 Inorganic Fraction Weight
Determination. Transfer the aqueous fraction
from the extraction to a clean 500-mL or
smaller beaker. Evaporate to no less than 10
mL liquid on a hot plate or in the oven at
105 °C, and allow to dry at room temperature
(not to exceed 30 °C (85 °F). You must ensure
that water and volatile acids have completely
evaporated before neutralizing nonvolatile
acids in the sample. Redissolve the residue
in 100 mL of deionized distilled ultra-filtered
water (ASTM D1193–06, Type 1 water or
equivalent) (incorporated by reference).
11.2.2.4 Use titration to neutralize acid in
the sample and remove water of hydration.
Calibrate the pH meter with the neutral and
acid buffer solutions; then titrate the sample
with 0.1N NH4OH to a pH of 7.0, as indicated
by the pH meter. Record the volume of titrant
used on the Condensable Particulate Matter
Work Table (see Figure 5 of Section 18).
11.2.2.5 Using a hot plate or an oven at
105 °C, evaporate the aqueous phase to
approximately 10 mL. Quantitatively transfer
the beaker contents to a 50-mL preweighed
tin, and evaporate to dryness at room
temperature (not to exceed 30 °C (85 °F)) and
pressure in a laboratory hood. Following
evaporation, desiccate the residue for 24
hours in a desiccator containing anhydrous
calcium sulfate. Weigh at intervals of at least
6 hours to a constant weight (i.e., ≤ 0.5 mg
change from previous weighing), and report
results to the nearest 0.1 mg on the
Condensable Particulate Matter Work Table
(see Figure 5 of Section 18).
11.2.2.6 Calculate the correction factor to
subtract the NH4∂ retained in the sample
using Equation 1 in Section 12.
11.2.3 CPM Container #4, Cold Impinger
Water. If the amount of water has not been
EP25MR09.045
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13008
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
m cpm
Vm (std )
sampling equipment should be managed as
RCRA organic waste.
Eq. 5
16.0
12.3 Emissions Test Report. Include the
following list of conventional elements in the
emissions test report.
(a) Emission test description including any
deviations from this protocol.
(b) Summary data tables on a run-by-run
basis that include the condensable
particulate mass.
(c) Flowchart of the process or processes
tested.
(d) Sketch of the sampling location.
(e) Preliminary traverse data sheets
including cyclonic flow checks.
(f) Raw field data sheets and copies of field
log pages.
(g) Laboratory analytical sheets and case
narratives.
(h) Pretest and post test reagent blank
results.
(i) Sample calculations.
(j) Pretest and post-test calibration data.
(k) Chain of custody forms.
(l) Documentation of process and air
pollution control system data.
13.0
Method Performance [Reserved]
14.0
Pollution Prevention [Reserved]
15.0
Waste Management
PWALKER on PROD1PC71 with PROPOSALS3
Solvent and water are evaporated in a
laboratory hood during analysis. No liquid
waste is generated in the performance of this
method. Organic solvents used to clean
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Alternative Procedures [Reserved]
17.0 References
1. U.S. Environmental Protection Agency,
Federal Reference Methods 1 through 5 and
Method 17, 40 CFR 60, Appendix A–1
through A–3 and A–6.
2. Richards, J., T. Holder, and D. Goshaw.
‘‘Optimized Method 202 Sampling Train to
Minimize the Biases Associated with Method
202 Measurement of Condensable Particulate
Matter Emissions.’’ Paper presented at Air &
Waste Management Association Hazardous
Waste Combustion Specialty Conference. St.
Louis, Missouri. November 2–3, 2005.
3. DeWees, W.D., S.C. Steinsberger, G.M.
Plummer, L.T. Lay, G.D. McAlister, and R.T.
Shigehara. ‘‘Laboratory and Field Evaluation
of the EPA Method 5 Impinger Catch for
Measuring Condensable Matter from
Stationary Sources.’’ Paper presented at the
1989 EPA/AWMA International Symposium
on Measurement of Toxic and Related Air
Pollutants. Raleigh, North Carolina. May 1–
5, 1989.
4. DeWees, W.D. and K.C. Steinsberger.
‘‘Method Development and Evaluation of
Draft Protocol for Measurement of
Condensable Particulate Emissions.’’ Draft
Report. November 17, 1989.
5. Texas Air Control Board, Laboratory
Division. ‘‘Determination of Particulate in
Stack Gases Containing Sulfuric Acid and/or
Sulfur Dioxide.’’ Laboratory Methods for
Determination of Air Pollutants. Modified
December 3, 1976.
PO 00000
Frm 00040
Fmt 4701
Sfmt 4702
6. Nothstein, Greg. Masters Thesis.
University of Washington. Department of
Environmental Health. Seattle, Washington.
7. ‘‘Particulate Source Test Procedures
Adopted by Puget Sound Air Pollution
Control Agency Board of Directors.’’ Puget
Sound Air Pollution Control Agency,
Engineering Division. Seattle, Washington.
August 11, 1983.
8. Commonwealth of Pennsylvania,
Department of Environmental Resources.
Chapter 139, Sampling and Testing (Title 25,
Rules and Regulations, Part I, Department of
Environmental Resources, Subpart C,
Protection of Natural Resources, Article III,
Air Resources). January 8, 1960.
9. Wisconsin Department of Natural
Resources. Air Management Operations
Handbook, Revision 3. January 11, 1988.
10. U.S. Environmental Protection Agency,
‘‘Laboratory Evaluation of Method 202 to
Determine Fate of SO2 in Impinger Water,’’
EPA Contract No. 68–D–02–061, Work
Assignment 3–14, September 30, 2005.
11. U.S. Environmental Protection Agency,
‘‘Evaluation and Improvement of
Condensable Particulate Matter
Measurement,’’ EPA Contract No. EP–D–07–
097, Work Assignment 2–03, October 2008.
12. Electric Power Research Institute
(EPRI), ‘‘Laboratory Comparison of Methods
to Sample and Analyze Condensable
Particulate Matter,’’ EPRI Agreement EP–
P24373/C11811 Condensable Particulate
Methods: EPRI Collaboration with EPA,
October 2008.
E:\FR\FM\25MRP3.SGM
25MRP3
EP25MR09.049
Ccpm =
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13009
EP25MR09.060
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EP25MR09.061
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Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 / Proposed Rules
FIGURE 3—FIELD TRAIN BLANK CONDENSABLE PARTICULATE CALCULATIONS
Field Train Blank Condensable Particulate
Calculations
Plant
Date
Blank No.
CPM Filter No.
Water volume added to purge train
(Vp)
FIGURE 3—FIELD TRAIN BLANK CONDENSABLE PARTICULATE CALCULATIONS—Continued
Mass
of
Inorganic
CPM
(mib)(Equation 3).
Mass of the Field Train Blank (not to
exceed 2.0 mg) (Equation 2).
ml
Field Reagent Blank Mass
Water (Section 11.2.6) .......................
Acetone (Section 11.2.5) ...................
Methylene Chloride (Section 11.2.7)
mg
mg
mg
Field Train Reagent Blank Mass
Mass of Organic CPM (mob)(Section
11.2.2.2).
mg
mg
mg
13011
FIGURE 4—OTHER FIELD TRAIN SAMPLE CONDENSABLE PARTICULATE
DATA
Other Field Train Sample Condensable
Particulate Data
Plant
Date
Run No.
CPM Filter No.
Water volume added to purge train
[max 50 mL] (Vp).
Date
Run No.
CPM Filter No.
Water volume added to purge train
[max 50 mL] (Vp).
Date
Run No.
CPM Filter No.
Water volume added to purge train
[max 50 mL] (Vp)
ml
ml
ml
FIGURE 5—CONDENSABLE PARTICULATE MATTER WORK TABLE
Calculations for Recovery of Condensable Particulate Matter (CPM)
Plant
Date
Run No.
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Sample Preparation—CPM Containers No. 1 and 2 (Section 11.1)
Was significant volume of water lost during transport? Yes or No .........................................................................
If Yes, measure the volume received ......................................................................................................................
Estimate the volume lost during transport ...............................................................................................................
Was significant volume of organic rinse lost during transport? Yes or No .............................................................
If Yes, measure the volume received. Estimate the volume lost during transport ..................................................
For Titration
Normality of NH4OH (N) (Section 10.2) ...................................................................................................................
Volume of titrant (Vt) (Section 11.2.2.4) ..................................................................................................................
Mass of NH4 added (mc) (Equation 1) .....................................................................................................................
For CPM Blank Weights
Inorganic Train Field Blank Mass(mib) (Section 9.9) ...............................................................................................
Organic Train Field Blank Mass (mob) (Section 9.9) ...............................................................................................
Mass of Train Field Blank (Mfb) (max. 2 mg) (Equation 2) .....................................................................................
For CPM Train Weights
Mass of Organic CPM (mo) (Section 11.2.2.2) ........................................................................................................
Mass of Inorganic CPM (mi) (Equation 3) ...............................................................................................................
Total CPM Mass (mcpm) (Equation 4) ......................................................................................................................
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llllllll
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llllllll
llllllll mL
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llllllll mL
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llllllll mg
llllllll mg
llllllll mg
llllllll mg
llllllll mg
llllllll mg
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[FR Doc. E9–6178 Filed 3–24–09; 8:45 am]
BILLING CODE 6560–50–C
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Agencies
[Federal Register Volume 74, Number 56 (Wednesday, March 25, 2009)]
[Proposed Rules]
[Pages 12970-13012]
From the Federal Register Online via the Government Printing Office [www.gpo.gov]
[FR Doc No: E9-6178]
[[Page 12969]]
-----------------------------------------------------------------------
Part III
Environmental Protection Agency
-----------------------------------------------------------------------
40 CFR Part 51
Methods for Measurement of Filterable PM10 and
PM2.5 and Measurement of Condensable Particulate Matter
Emissions from Stationary Sources; Proposed Rule
Federal Register / Vol. 74, No. 56 / Wednesday, March 25, 2009 /
Proposed Rules
[[Page 12970]]
-----------------------------------------------------------------------
ENVIRONMENTAL PROTECTION AGENCY
40 CFR Part 51
[EPA-HQ-OAR-2008-0348; FRL-8784-5]
RIN 2060-AO58
Methods for Measurement of Filterable PM10 and
PM2.5 and Measurement of Condensable Particulate Matter
Emissions From Stationary Sources
AGENCY: Environmental Protection Agency (EPA).
ACTION: Proposed rule.
-----------------------------------------------------------------------
SUMMARY: This action proposes amendments to Methods 201A and 202. The
proposed amendments to Method 201A would add a particle-sizing device
to allow for sampling of particulate matter (PM) with mean aerodynamic
diameters less than or equal to 2.5 micrometers ([mu]m)
(PM2.5 or fine PM). The proposed amendments to Method 202
would revise the sample collection and recovery procedures of the
method to reduce the formation of reaction artifacts that could lead to
inaccurate measurements of condensable particulate matter (CPM).
Additionally, the proposed amendments to Method 202 would eliminate
most of the hardware and analytical options in the existing method,
thereby increasing the precision of the method and improving the
consistency in the measurements obtained between source tests performed
under different regulatory authorities. Finally, in this notice we are
soliciting comments on whether to end the transition period for CPM in
the New Source Review (NSR) program on a date earlier than the current
end date of January 1, 2011. The proposed amendments would improve the
measurement of fine particulates and would help State and local
agencies in implementing CPM control measures to attain the
PM2.5 National Ambient Air Quality Standards (NAAQS) which
were established to protect public health and welfare.
DATES: Comments. Comments must be received on or before May 26, 2009.
ADDRESSES: Submit your comments, identified by Docket ID Number EPA-HQ-
OAR-2008-0348, by one of the following methods:
https://www.regulations.gov. Follow the on-line
instructions for submitting comments.
E-mail: Send your comments via electronic mail to a-and-r-docket@epa.gov.
Fax: (202) 566-9744.
Mail: Methods for Measurement of Filterable
PM10 and PM2.5 and Measurement of Condensable
Particulate Matter Emissions from Stationary Sources, Environmental
Protection Agency, Mailcode 2822T, 1200 Pennsylvania Ave., NW.,
Washington, DC 20460. Please include a total of two copies.
Hand Delivery: EPA Docket Center EPA Headquarter Library,
Room 3334, EPA West Building, 1301 Constitution Ave., NW., Washington,
DC, 20460. Such deliveries are accepted only during the Docket's normal
hours of operation, and special arrangements should be made for
deliveries of boxed information.
Instructions: Direct your comments to Docket ID No. EPA-HQ-OAR-
2008-0348. EPA's policy is that all comments received will be included
in the public docket without change and may be made available online at
https://www.regulations.gov, including any personal information
provided, unless the comment includes information claimed to be
Confidential Business Information (CBI) or other information whose
disclosure is restricted by statute. Do not submit information that you
consider to be CBI or otherwise protected through https://www.regulations.gov or e-mail. The https://www.regulation.gov Web site
is an ``anonymous access'' system, which means EPA will not know your
identity or contact information unless you provide it in the body of
your comment. If you send an e-mail comment directly to EPA without
going through https://www.regulations.gov, your e-mail address will be
automatically captured and included as part of the comment that is
placed in the public docket and made available on the Internet. If you
submit an electronic comment, EPA recommends that you include your name
and other contact information in the body of your comment and with any
disk or CD-ROM you submit. If EPA cannot read your comment due to
technical difficulties and cannot contact you for clarification, EPA
may not be able to consider your comment. Electronic files should avoid
the use of special characters, any form of encryption, and be free of
any defects or viruses. For additional information about EPA's public
docket, visit the EPA Docket Center homepage at https://www.epa.gov/epahome/dockets.htm.
Docket: All documents in the docket are listed in the https://www.regulations.gov index. Although listed in the index, some
information is not publicly available, e.g. , CBI or other information
whose disclosure is restricted by statute. Certain other material, such
as copyrighted material, will be publicly available only in hard copy.
Publicly available docket materials are available either electronically
in https://www.regulations.gov or in hard copy at the Methods for
Measurement of Filterable PM10 and PM2.5 and
Measurement of Condensable Particulate Matter Emissions from Stationary
Sources Docket, EPA/DC, EPA West Building, Room 3334, 1301 Constitution
Ave., NW., Washington, DC. The Public Reading Room/Docket Center is
open from 8:30 a.m. to 4:30 p.m., Monday through Friday, excluding
legal holidays. The telephone number for the Public Reading Room is
(202) 566-1744, and the telephone number for the Air Docket Center is
(202) 566-1742.
Public Hearing: If anyone contacts EPA requesting to speak at a
public hearing concerning our proposal to revise the PM test methods by
April 14, 2009, we will hold a public hearing on or about April 24,
2009. Persons interested in presenting oral testimony should contact
Ms. Kristal Mozingo, Measurement Policy Group (D243-05), Sector
Policies and Programs Division, EPA, Research Triangle Park, NC 27711,
telephone number: (919) 541-9767, e-mail address:
mozingo.kristal@epa.gov. Persons interested in attending the public
hearing should also call Ms. Mozingo to verify the time, date, and
location of the hearing. A public hearing will provide interested
parties the opportunity to present data, views, or arguments concerning
the proposed test method revisions.
If a public hearing is held, it will be held at 10 a.m. at the
Conference Facilities at EPA's Main Campus, Research Triangle Park, NC,
or an alternate site nearby.
FOR FURTHER INFORMATION CONTACT: For general information, contact Ms.
Candace Sorrell, U.S. EPA, Office of Air Quality Planning and
Standards, Air Quality Assessment Division, Measurement Technology
Group (E143-02), Research Triangle Park, NC 27711; telephone number:
(919) 541-1064; fax number; (919) 541-0516; e-mail address:
sorrell.candace@epa.gov. For technical questions, contact Mr. Ron
Myers, U.S. EPA, Office of Air Quality Planning and Standards, Sector
Policies and Programs Division, Measurement Policy Group (D243-05),
Research Triangle Park, NC 27711; telephone number: (919) 541-5407; fax
number: (919) 541-1039; e-mail address: myers.ron@epa.gov.
SUPPLEMENTARY INFORMATION:
[[Page 12971]]
I. General Information
A. Does This Action Apply to Me?
This action would apply to you if you operate a stationary source
that is subject to applicable requirements for total PM or total
PM10 where EPA Method 202 is incorporated as a component of
the applicable compliance method.
In addition, this action would apply to you if Federal, State, or
local agencies take certain additional independent actions. For
example, this action would apply to sources through actions by State
and local agencies which implement CPM control measures to attain the
PM2.5 NAAQS and specify the use of this test method to
demonstrate compliance with the control measure. Actions that State and
local agencies would have to implement include: (1) Adopting this
method in rules or permits (either by incorporation by reference or by
duplicating the method in its entirety), and (2) promulgating an
emissions limit requiring the use of this method (or an incorporated
method based upon this method). This action would also apply to
stationary sources that are required to meet new applicable CPM
requirements established through Federal or State permits or rules,
such as New Source Performance Standards and New Source Review, which
specify the use of this test method to demonstrate compliance with the
control measure.
The source categories and entities potentially affected include,
but are not limited to, the following:
------------------------------------------------------------------------
Examples of
Category SIC \1\ NAICS \2\ potentially
code code regulated entities
------------------------------------------------------------------------
Industry........................ 3569 332410 Fossil fuel steam
generators.
3569 332410 Industrial,
commercial,
institutional
steam generating
units.
3569 332410 Electricity
generating units.
2911 324110 Petroleum
refineries.
4953 562213 Municipal waste
combustors.
2621 322110 Pulp and paper
mills.
2819 325188 Sulfuric acid
plants.
3241 327310 Portland Cement
Plants.
3274 327410 Lime Manufacturing
Plants.
1222 211111 Coal Preparation
Plants.
1231 212111
212112
212113
3334 331312 Primary and
Secondary
Aluminum Plants.
3341 331314
3312 331111 Iron and Steel
Plants.
3325 331513
2493 321219 Plywood and
Reconstituted
Products Plants.
2435 321211
2436 321212
------------------------------------------------------------------------
\1\ Standard Industrial Classification.
\2\ North American Industrial Classification System.
B. What Should I Consider as I Prepare My Comments for EPA?
Do not submit information containing CBI to EPA through https://www.regulations.gov or e-mail. Send or deliver information identified
as CBI only to the following address: Roberto Morales, OAQPS Document
Control Officer (C404-02), U.S. EPA, Office of Air Quality Planning and
Standards, Research Triangle Park, NC 27711, Attention Docket ID No.
EPA-HQ-OAR-2008-0348. Clearly mark the part or all of the information
that you claim to be CBI. For CBI information on a disk or CD-ROM that
you mail to EPA, mark the outside of the disk or CD-ROM as CBI, and
then identify electronically within the disk or CD-ROM the specific
information that is claimed as CBI. In addition to one complete version
of the comment that includes information claimed as CBI, a copy of the
comment that does not contain the information claimed as CBI must be
submitted for inclusion in the public docket. Information so marked
will not be disclosed except in accordance with procedures set forth in
40 CFR part 2.
C. Where Can I Obtain a Copy of This Action and Other Related
Information?
In addition to being available in the docket, an electronic copy of
today's proposed amendments is also available on the Worldwide Web
(https://www.epa.gov/ttn/) through the Technology Transfer Network
(TTN). Following the Administrator's signature, a copy of the proposed
amendment will be posted on the TTN's policy and guidance page for
newly proposed or promulgated rules at https://www.epa.gov/ttn/oarpg.
The TTN provides information and technology exchange in various areas
of air pollution control.
D. How Is This Document Organized?
The information in this preamble is organized as follows:
I. General Information
A. Does This Action Apply to Me?
B. What Should I Consider as I Prepare My Comments for EPA?
C. Where Can I Obtain a Copy of This Action and Other Related
Information?
D. How Is This Document Organized?
II. Background
A. Why Is EPA Issuing This Proposed Rule?
B. Particulate Matter National Ambient Air Quality Standards
C. Measuring PM Emissions
1. Method 201A
2. Method 202
III. This Action
A. What Are the Proposed Amendments to Method 201A?
B. What Are the Proposed Amendments to Method 202?
C. How Will the Proposed Amendments to Methods 201A and 202
Affect Existing Emission Inventories, Emission Standards, and Permit
Programs?
D. Request for Comments
1. Items Associated With Both Test Methods
2. Items Associated With Method 201A
2. Items Associated With Method 202
IV. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory Planning and Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
E. Executive Order 13132: Federalism
[[Page 12972]]
F. Executive Order 13175: Consultation and Coordination With
Indian Tribal Governments
G. Executive Order 13045: Protection of Children From
Environmental Health and Safety Risks
H. Executive Order 13211: Actions Concerning Regulations That
Significantly Affect Energy Supply, Distribution, or Use
I. National Technology Transfer and Advancement Act
J. Executive Order 12898: Federal Actions To Address
Environmental Justice in Minority Populations and Low-Income
Populations
II. Background
A. Why Is EPA Issuing This Proposed Rule?
On April 25, 2007 (70 FR 20586), we promulgated the Clean Air Fine
Particle Implementation Rule regarding the Clean Air Act (CAA)
requirements for State and Tribal plans to implement the 1997 PM2.5
NAAQS. These rules require that each State having a PM2.5 nonattainment
area must submit, by April 5, 2008, an attainment demonstration and
adopt regulations to ensure the area will attain the standards as
expeditiously as practicable, but even those areas for which the
Administrator determines an extension from the 2010 attainment date is
appropriate may not receive an extension later than a 2015 attainment
date. The emissions inventories and analyses used in the attainment
demonstrations must consider filterable and condensable fractions of
PM2.5 emissions from stationary sources that are significant
contributors of direct PM2.5 emissions. Direct PM2.5 emissions means
the solid particles or liquid droplets emitted directly from an air
emissions source or activity, or the gaseous emissions or liquid
droplets from an air emissions source or activity that condense to form
PM or liquid droplets at ambient temperatures.
The preamble to the April 25, 2007, rule acknowledged that there
remain questions whether the available test methods provide the most
accurate representation of primary PM emissions even though some States
have established emissions limits for CPM. As a result, the final rule
established a transitional period for developing emissions limits and
regulations for condensable PM2.5. During this transitional period, EPA
has committed to devote resources to assessing and improving the
available test methods for CPM.
In response to this commitment and to address the need for improved
measurement of fine PM, EPA is proposing amendments to the following
test methods in 40 CFR Part 51, Appendix M (Recommended Test Methods
for State Implementation Plans (SIPs)):
Method 201A--Determination of PM10 Emissions (Constant
Sampling Rate Procedure), and
Method 202--Determination of Condensable Particulate
Emissions from Stationary Sources.
These amendments to Method 201A add a particle-sizing device to
allow for sampling of PM2.5, PM10, or both PM10 and PM2.5. With regard
to Method 202, we are aware that the method and the various hardware
and analytic options described therein are sometimes applied
inappropriately, which can lead to inaccurate and imprecise CPM
measurements. We are also aware that Method 202 can produce inaccurate
CPM measurements when sampling certain types of emissions sources, due
to formation of reaction artifacts. The amendments to Method 202 revise
the sample collection and recovery procedures of the method to provide
for more accurate and precise measurement of CPM.
B. Particulate Matter National Ambient Air Quality Standards
Section 108 and 109 of the CAA govern the establishment and
revision of the NAAQS. Section 108 (42 U.S.C. 7408) directs the
Administrator to identify and list ``air pollutants'' that ``in his
judgment, may reasonably be anticipated to endanger public health and
welfare'' and whose ``presence * * * in the ambient air results from
numerous or diverse mobile or stationary sources'' and to issue air
quality criteria for those that are listed. Air quality criteria are
intended to ``accurately reflect the latest scientific knowledge useful
in indicating the kind and extent of identifiable effects on public
health or welfare which may be expected from the presence of [a]
pollutant in ambient air* * *.'' Section 109 (42 U.S.C. 7409) directs
the Administrator to propose and promulgate primary and secondary NAAQS
for pollutants listed under section 108 to protect public health and
welfare, respectively. Section 109 also requires review of the NAAQS at
5-year intervals and that an independent scientific review committee
``shall complete a review of the criteria * * * and the national
primary and secondary ambient air quality standards * * * and shall
recommend to the Administrator any new * * * standards and revisions of
existing criteria and standards as may be appropriate * * *.'' Since
the early 1980s, this independent review function has been performed by
the Clean Air Scientific Advisory Committee (CASAC).
Initially EPA established the NAAQS for PM on April 30, 1971 (36 FR
8186) based on the original criteria document (Department of Health,
Education, and Welfare, 1969). The reference method specified for
determining attainment of the original standards was the high-volume
sampler, which collects PM up to a nominal size of 25 to 45 [mu]m
(referred to as total suspended particulates or TSP). On October 2,
1979 (44 FR 56730), EPA announced the first periodic review of the air
quality criteria and NAAQS for PM, and significant revisions to the
original standards were promulgated on July 1, 1987 (52 FR 24634). In
that decision, EPA changed the indicator for particles from TSP to
PM10. When that rule was challenged, the court upheld revised standards
in all respects. Natural Resources Defense Council v. Administrator,
902 F. 2d 962 (D.C. Cir. 1990, cert. denied, 498 U.S. 1082 (1991)).
In April 1994, EPA announced its plans for the second periodic
review of the air quality criteria and NAAQS for PM, and the Agency
promulgated significant revisions to the NAAQS on July 18, 1997 (62 FR
38652). In that decision, EPA revised the PM NAAQS in several respects.
While EPA determined that the PM NAAQS should continue to focus on
particles less than or equal to 10 [mu]m in diameter (PM10), EPA also
determined that the fine and coarse fractions of PM10 should be
considered separately. The EPA added new standards, using PM2.5 as the
indicator for fine particles (with PM2.5 referring to particles with a
nominal mean aerodynamic diameter less than or equal to 2.5 [mu]m), and
using PM10 as the indicator for purposes of regulating the coarse
fraction of PM10.
Following promulgation of the 1997 PM NAAQS, petitions for review
were filed by a large number of parties, addressing a broad range of
issues. In May 1999, a three-judge panel of the U.S. Court of Appeals
for the District of Columbia Circuit issued an initial decision that
upheld EPA's decision to establish fine particle standards. American
Trucking Associations v. EPA, 175 F.3d 1027, 1055 (D.C. Cir. 1999),
reversed in part on other grounds in Whitman v. American Trucking
Associations, 531 U.S. 457 (2001). The Panel also found ``ample
support'' for EPA's decision to regulate coarse particle pollution but
vacated the 1997 PM10 standards, concluding that EPA had not provided a
reasonable explanation justifying use of PM10 as an indicator for
coarse particles. Id. at 1054-55. Pursuant to the court's
[[Page 12973]]
decision, EPA removed the vacated 1997 PM10 standards but retained the
pre-existing 1987 PM10 standards (65 FR 80776, December 22, 2000).
On October 23, 1997, EPA published its plans for the third periodic
review of the air quality criteria and NAAQS for PM (62 FR 55201),
including the 1997 PM2.5 standards and the 1987 PM10 standards. On
October 17, 2006, EPA issued its final decisions to revise the primary
and secondary NAAQS for PM to provide increased protection of public
health and welfare, respectively (71 FR 61144). With regard to the
primary and secondary standards for fine particles, EPA revised the
level of the 24-hour PM2.5 standard to 35 [mu]g per cubic meter ([mu]g/
m\3\), retained the level of the annual PM2.5 annual standard at 15
[mu]g/m\3\, and revised the form of the annual PM2.5 standard by
narrowing the constraints on the optional use of spatial averaging.
With regard to the primary and secondary standards for PM10, EPA
retained the 24-hour PM10 standard (150 [mu]g/m\3\) and revoked the
annual standard because available evidence generally did not suggest a
link between long-term exposure to current ambient levels of coarse
particles and health or welfare effects.
C. Measuring PM Emissions
Section 110 of the CAA, as amended (42 U.S.C. 7410), requires that
State and local air pollution control agencies develop and submit plans
for EPA approval that provide for the attainment, maintenance, and
enforcement of the NAAQS in each air quality control region (or portion
thereof) within such State. These plans are known as SIPs. 40 CFR part
51 (Requirements for Preparation, Adoption, and Submittal of
Implementation Plans) specifies the requirements for SIPs. Appendix A
to subpart A of 40 CFR part 51, defines primary PM10 and PM2.5 as
including both the filterable and condensable fractions of PM.
Filterable PM consists of those particles that are directly emitted by
a source as a solid or liquid at the stack (or similar release
conditions) and captured on the filter of a stack test train.
Condensable PM is the material that is in vapor phase at stack
conditions but which condenses and/or reacts upon cooling and dilution
in the ambient air to form solid or liquid PM immediately after
discharge from the stack.
Promulgation of the 1987 NAAQS created the need for methods to
quantify PM10 emissions from stationary sources. In response, EPA
developed and promulgated the following test methods:
Method 201A--Determination of PM10 Emissions (Constant
Sampling Rate Procedure), and
Method 202--Determination of Condensable Particulate
Emissions from Stationary Sources.
1. Method 201A
On April 17, 1990 (56 FR 65433), EPA promulgated Method 201A in
Appendix M of 40 CFR Part 51 to provide a test method for measuring
filterable PM10 emissions from stationary sources. In EPA Method 201A,
a gas sample is extracted at a constant flow rate through an in-stack
sizing device which directs particles with aerodynamic diameters less
than or equal to 10 [mu]m to a filter. The particulate mass collected
on the filter is determined gravimetrically after removal of uncombined
water. With the exception of the PM10-sizing device, the current Method
201A sampling train is the same as the sampling train used for EPA
Method 17 of Appendix A-3 to 40 CFR Part 60.
Method 201A cannot be used to measure emissions from stacks that
have entrained moisture droplets (e.g., from a wet scrubber stack)
since these stacks may have water droplets that are larger than the cut
size of the PM10-sizing device. The presence of moisture would prevent
an accurate measurement of total PM10 since any PM10 dissolved in
larger water droplets would not be collected by the sizing device and
would consequently be excluded in determining the total PM10 mass. To
measure PM10 in stacks where water droplets are known to exist, EPA's
Technical Information Document (TID) 09 (Methods 201 and 201A in
Presence of Water Droplets), recommends use of Method 5 of Appendix A-3
to 40 CFR Part 60 (or a comparable method) and consideration of the
total particulate catch as PM10 emissions.
Method 201A is also not applicable for stacks with small diameters
(i.e., 18 inches or less). The presence of the in-stack nozzle/cyclones
and filter assembly in a small duct will cause significant cross-
sectional area interference and blockage leading to incorrect flow
calculation and particle size separation. Additionally, the type of
metal used to construct the Method 201A cyclone may limit the
applicability of the method when sampling at high stack temperatures
(e.g., stainless steel cyclones are reported to gall and seize at
temperatures greater than 260 [deg]C).
2. Method 202
On December 17, 1991 (56 FR 65433), EPA promulgated Method 202 in
Appendix M of 40 CFR Part 51 to provide a test method for measuring CPM
from stationary sources. Method 202 uses water-filled impingers to
cool, condense, and collect materials that are vaporous at stack
conditions and become solid or liquid PM at ambient air temperatures.
Method 202, as promulgated, contains several optional procedures that
were intended to accommodate the various test methods used by State and
local regulatory entities at the time Method 202 was being developed.
When conducted consistently and carefully, Method 202 provides
acceptable precision for most emission sources, and the method has been
used successfully in regulatory programs where the emission limits and
compliance demonstrations are established based on a consistent
application of Method 202 and its associated options. However, when the
same emission source is tested using different combinations of the
optional procedures, there may appear to be large variations in the
measured CPM emissions. Additionally, during validation of the
promulgated method, we determined that sulfur dioxide (SO2) gas (a
typical component of emissions from several types of stationary
sources) can be absorbed partially in the impinger solutions and can
react chemically to form sulfuric acid. This sulfuric acid ``artifact''
is not related to the primary emission of CPM from the source but may
be counted erroneously as CPM when using Method 202. As we have
maintained consistently, the artifact formation can be reduced by at
least 90 percent if a one-hour nitrogen purge of the impinger water is
used to remove SO2 before it can form sulfuric acid (this is
our preferred application of the Method 202 optional procedures).
Inappropriate use (or omission) of the preferred or optional procedures
in Method 202 can increase the potential for artifact formation.
Considering the potential for variations in measured CPM emissions,
we believe that further verification and refinement of Method 202 is
appropriate to minimize the potential for artifact formation. We have
performed several studies to assess artifact formation when using
Method 202. The results of our 1998 laboratory study and field
evaluation commissioned to evaluate the impinger approach can be found
in ``Laboratory and Field Evaluation of the EPA Method 5 Impinger Catch
for Measuring Condensible Matter from Stationary Sources'' at the
following Internet address: https://www.epa.gov/ttn/emc/methods/m202doc1.pdf. Essentially, the 1998 study verified the need for a
nitrogen purge when SO2 is
[[Page 12974]]
present in stack gas and also provided guidance for analyzing the
collected samples. In 2005, an EPA contractor conducted a second study
(``Laboratory Evaluation of Method 202 to Determine Fate of
SO2 in Impinger Water'') that replicated some of the earlier
EPA work and addressed some additional issues. The report of that work
is available at the following Internet address: https://www.epa.gov/ttn/emc/methods/m202doc2.pdf. This report also verified the need for a
nitrogen purge and identified the primary factors that affect artifact
formation.
Also in 2005, a private testing contractor presented a possible
minor modification to Method 202 at the Air and Waste Management
Association (AWMA) specialty conference. The proposed modification,
described in their presentation titled ``Optimized Method 202 Sampling
Train to Minimize the Biases Associated with Method 202 Measurement of
Condensable Particulate Matter Emissions,'' involved the elimination of
water from the first impingers. The presentation (which is available at
the following Internet address: https://www.epa.gov/ttn/emc/methods/m202doc3.pdf) concluded that modification of the promulgated method to
use dry impingers resulted in a significant additional reduction in the
sulfate artifact.
In 2006, we began to conduct laboratory studies, in collaboration
with several stakeholders, to characterize the artifact formation and
other uncertainties associated with conducting Method 202 and to
identify procedures that would minimize uncertainties when using Method
202. Since August 2006, we have held two workshops in Research Triangle
Park, North Carolina. These meetings were held to present and seek
comments on our plan for evaluating potential modifications to Method
202 that would reduce artifact formation. Also, these meetings were
held to discuss our progress in characterizing the performance of the
modified method, issues that require additional investigation, the
results of our laboratory studies, and our commitments to extend the
investigation through stakeholders external to EPA. We held another
meeting with experienced stack testers and vendors of emissions
monitoring equipment to discuss hardware issues associated with
modifications of the sampling equipment and the glassware for the
proposed CPM test method. Summaries of the method evaluations, as well
as meeting minutes from our workshops, can be found at the following
Internet address: https://www.epa.gov/ttn/emc/methods/method202.html.
The laboratory studies that were performed fulfill a commitment in
the preamble to the Clean Air Fine Particle Implementation Rule (72 FR
20586, April 25, 2007) to examine the relationship between several
critical CPM sampling and analysis parameters and, to the extent
necessary, propose revisions to incorporate improvements in the method.
While these improvements in the stationary source test method for CPM
will provide for more accurate and precise measurement of all PM, the
addition of PM2.5 as an indicator of health and welfare
effects by the 1997 NAAQS revisions generates the need to quantify
PM2.5 emissions from stationary sources. To respond to this
need, we are proposing revisions to incorporate this capability into
the test method for filterable PM10.
III. This Action
This action proposes to provide the capability of measuring
PM2.5 using Method 201A and to provide for more accurate
measurement of the filterable and condensable components of fine PM
(particles with mean aerodynamic diameters less than or equal to 2.5 m)
and coarse PM (particles with mean aerodynamic diameters less than or
equal to 10 m) when using Method 202. Method 201A proposed amendments
would add a particle-sizing cyclone to the sampling train. Method 202
proposed amendments would reduce the formation of sulfuric acid
artifact by at least an additional 90 percent (compared to our
recommended procedures for the existing Method 202), provide for
greater consistency between testing contractors in method application,
improve the precision of the method, and provide for more accurate
quantification of direct (i.e., primary) PM emissions to the ambient
air (the method will not measure secondarily-formed PM). The proposed
amendments would also affect the measurement of total PM,
PM10, and PM2.5. Additionally, we are proposing
to revise the format of Methods 201A and 202 to be consistent with the
format developed by EPA's Environmental Monitoring Management Council
(EMMC). A guidance document describing the EMMC format can be found at
the following Internet address: https://www.epa.gov/ttn/emc/guidlnd/gd-045.pdf.
A. What Are the Proposed Amendments to Method 201A?
On July 18, 1997 (62 FR 38652), we revised the NAAQS for PM to add
new standards for fine particles, using PM2.5 as the
indicator. This action will modify the current Method 201A sampling
train configuration to allow for measurement of filterable
PM10, filterable PM2.5, or both filterable
PM10 and filterable PM2.5 from stationary
sources. These amendments combine the existing method with the
PM2.5 cyclone to create a sampling train that includes a
total of two cyclones (one cyclone to size particles with aerodynamic
diameters greater than 10 m and one cyclone to size particles with
aerodynamic diameters greater than 2.5 m) and a final filter to collect
particles with aerodynamic diameters less than or equal to 2.5 m. The
PM2.5 cyclone would be inserted between the PM10
cyclone and the filter of the Method 201A sampling train.
We are not proposing any amendments to address the use of this
method when the stack gas has entrained moisture or when the method is
used for stack gases with high temperatures. In July 1979, we published
a research document (EPA-600/7-79-166) to report the preliminary
development of a method for measuring and characterizing the particles
in the vent stream from a wet scrubber used to control sulfur oxide
emissions. The method was based on the use of a heated, electrified
wire placed in the vent stream. When a water droplet impacted the wire,
the electric current flowing through the wire was attenuated in
proportion to the size of the water droplet. We decided it was not
appropriate to promulgate the preliminary method and, at this time, we
are not aware of any commercially-available equipment that can
determine the aerodynamic size of PM contained in, or dissolved in,
liquid water droplets as they would exist in the ambient air following
release and evaporation in the ambient air. While we are aware of
several optical aerosol droplet spectrometers for measuring the size
distribution of liquid droplets in exhaust gases, we are not aware of
any commercial instruments that can measure size distributions of
particles emitted from stationary sources. We also lack knowledge on
the relative effects of solids concentration in the liquid droplets and
the possible presence of dry particles in addition to the liquid
droplets. Consequently, we recommend the use of EPA Method 5 (40 CFR
Part 60, Appendix A-3--Determination of Particulate Matter Emissions
from Stationary Sources) when measuring PM in stacks with saturated
water vapors containing entrained water droplets. With this application
of EPA Method 5,
[[Page 12975]]
all of the collected material would be considered PM2.5.
B. What Are the Proposed Amendments to Method 202?
This action proposes amendments incorporating modifications that
would reduce the formation of artifacts at both low and high
concentrations of SO2 in the sample gas stream. The
modifications were developed based on the method evaluations discussed
in Section II.C.2 of this preamble.
Method 202, as promulgated in 1991, is a set of sampling procedures
for collecting PM in water-filled impingers and a set of sample
recovery procedures that are performed on the water following its
collection. The water-filled impingers are nearly identical to the four
chilled impingers used in standard stationary source sampling trains
for PM (e.g., Method 5 and Method 17 of Appendix A-3 and A-6, 40 CFR
Part 60). In principle, CPM is collected in the impinger portion of a
Method 17-type sampling train. Our preferred operation of the
promulgated method requires that the impinger contents be purged with
nitrogen after the test run to remove dissolved SO2 gas from
the impinger contents. The impinger solution is then extracted with
methylene chloride to separate the organic CPM from the inorganic CPM.
The organic and aqueous fractions are then dried and the residues
weighed. The sum of both fractions represents the total CPM.
These proposed amendments to Method 202 sampling train and sample
recovery procedures would achieve at least an additional 90 percent
reduction in sulfuric acid artifact formation compared to the current
Method 202 using the nitrogen purge option, provide testing contractors
with a more standardized application of the method, improve the
precision of the method, and quantify more accurately direct PM
emission to the ambient air.
The proposed changes to the sampling train of this method include:
Installing a condenser between the filter in the front-
half of the sample train and the first impinger to cool the sample
gases to ambient temperature (less than 30 [deg]C);
Installing a recirculation pump in the ambient water bath
to supply cooling water to the condenser;
Changing the first two impingers from wet to dry, and
placing these two dry impingers in a water bath at ambient temperature
(less than 30 [deg]C) (the first dry impinger will use a short-stem
insert, and the second dry impinger will use a long-stem insert);
Requiring the use of an out-of-stack, low-temperature
filter (i.e., the CPM filter), as described in EPA Method 8, between
the second and third impingers (a Teflon filter is used in place of the
fiberglass filter described in EPA Method 8); and
Requiring that the temperature of the sample gas drawn
through the CPM filter be maintained at ambient temperature (less than
30 [deg]C).
It should be noted that under Method 202, the use of a CPM filter is an
optional procedure that is used typically if the collection efficiency
of the impinger is suspected to be low. These proposed amendments would
make the use of a CPM filter a required procedure.
The proposed changes to Method 202 include:
Extracting the CPM filter with water and organic solvent;
Evaporating the liquid collected in the impingers in an
oven or on a hot plate down to a minimum volume of 10 milliliters,
instead of all the way to dryness;
Evaporating the remaining liquid to dryness at ambient
temperature prior to neutralization with ammonium hydroxide;
Titrating the reconstituted residue with 0.1 normal
ammonium hydroxide and a pH meter;
Evaporating the neutralized liquid to a minimum volume of
10 milliliters in an oven or hot plate;
Evaporating the final volume to dryness at ambient
temperature; and
Weighing the CPM sample residue to constant weight after
allowing a minimum of 24 hours for equilibration in a desiccator.
Note that the requirements to evaporate liquids at ambient temperature
and to titrate the reconstituted liquid exist already as options under
this method. These optional steps are typically performed to retain CPM
that might be lost at higher evaporation temperatures. Under these
proposed amendments, these options would be required procedures.
C. How Will the Proposed Amendments to Methods 201A and 202 Affect
Existing Emission Inventories, Emission Standards, and Permit Programs?
We anticipate that, over time, the changes in the test methods
proposed in this action will result in, among other positive outcomes,
more accurate emissions inventories of direct PM emissions and
emissions standards that are more indicative of the actual impact of
the source on the ambient air quality.
Accurate emission inventories are critical for regulatory agencies
to develop the control strategies and demonstrations necessary to
attain air quality standards. If implemented, the proposed test method
revisions would have the potential to improve our understanding of PM
emissions due to the increased availability of more accurate emission
tests and, eventually, through the incorporation of less biased test
data into existing emissions factors. For CPM, the use of the proposed
method would likely reveal a reduced level of CPM emissions from a
source compared to the emissions that would have been measured using
Method 202, as typically performed. However, there may be some cases
where the proposed test method would reveal an increased level of CPM
emissions from a source, depending on the relative emissions of
filterable and CPM emissions from the source. For example, the existing
Method 202 allows complete evaporation of the water containing
inorganic PM at 105 [deg]C (221 [deg]F), where the proposed revision
requires the last 10 ml of the water to be evaporated at room
temperature (not to exceed 30 [deg]C (85 [deg]F)) thereby retaining the
CPM that would evaporate at the increased temperature.
Prior to our adoption of the 1997 PM2.5 NAAQS, several
State and local air pollution control agencies had developed emission
inventories that included CPM. Additionally, some agencies established
enforceable CPM emissions limits or otherwise required that PM
emissions testing include measurement of CPM. While this approach was
viable in cases where the same test method was used to develop the CPM
regulatory limits and to demonstrate facility compliance, there are
substantial inconsistencies within and between States regarding the
completeness and accuracy of CPM emission inventories and the test
methods used to measure CPM emissions and to demonstrate facility
compliance.
These amendments would serve to mitigate the potential difficulties
that can arise when we and other regulatory entities attempt to use the
test data from State and local agencies whose CPM test methods are
inconsistent to develop emission factors, determine program
applicability, or to establish emissions limits for CPM emission
sources within a particular jurisdiction. For example, problems can
arise when the test method used to develop a CPM emission limit is not
the same as the test method specified in the rule for demonstrating
compliance because the different test methods may quantify different
components of PM (e.g., filterable versus condensable). Also, when
emissions from State inventories are modeled to assess compliance with
[[Page 12976]]
the NAAQS, the determination of direct PM emissions may be biased high
or low, depending on the test methods used to estimate PM emissions,
and the atmospheric conversion of SO2 to sulfates (or
SO3) may be inaccurate or double-counted. Additionally, some
State and local regulatory authorities have assumed that EPA Method 5
of Appendix A-3 to 40 CFR Part 60 (Determination of Particulate Matter
Emissions from Stationary Sources) provides a reasonable estimate of
PM10 emissions. This assumption is incorrect because Method
5 does not provide particle sizing of the filterable component and does
not quantify particulate caught in the impinger portion of the sampling
train. Similar assumptions for measurements of PM2.5 will
result in greater inaccuracies.
With regard to State permitting programs, we recognize that, in
some cases, existing Best Available Control Technology (BACT), Lowest
Achievable Emission Rate (LAER), or Reasonably Available Control
Technology (RACT) limits have been based on an identified control
technology, and that the data used to determine the performance of that
technology and establish the limits may have focused on filterable PM
and thus did not completely characterize PM emissions to the ambient
air. While the source test methods used by State programs that
developed the applicable permit limit may not have fully characterized
the PM emissions, we have no information that would indicate that the
test methods are inappropriate indicators of the control technologies'
performance for the portion of PM emissions that was addressed by the
applicable requirement. As promulgated in the Clean Air Fine Particle
Implementation Rule, after January 1, 2011, States are required to
consider inclusion of CPM emissions in new or revised emissions limits
which they establish. We will defer to the individual State's judgment
as to whether, and at what time, it is appropriate to revise existing
facility emission limits or operating permits to incorporate
information from the revised CPM test method when it is promulgated.
With regard to operating permits, the Title V permit program does
not generally impose new substantive air quality control requirements.
In general, once emissions limits are established as CAA requirements
under the SIP or a SIP-approved pre-construction review permit, they
are included in the Title V permits. Obviously, Title V permits may
have to be updated to reflect any revision of existing emission limits
or new emission limits created in the context of the underlying
applicable requirements. Also, if a permit contains the previously
promulgated test methods, it is not a given that the permit would
always have to be revised should these test methods changes be
finalized (e.g., where test methods are incorporated into existing
permits through incorporation by reference, no permit terms or
conditions would necessarily have to change to reflect changes to those
test methods). In any event, the need for action in the permitting
context due to these proposed changes to the test methods would be
controlled by several factors, such as the exact wording of the
existing operating permit, the requirements of the EPA-approved SIP,
and any changes that may be made to pre-construction review permits
with respect to a particular source test method that did not include
CPM or on a set of procedures in Method 202 which underestimated
emissions.
In recognition of these issues, the Clean Air Fine Particle
Implementation Rule contains provisions establishing a transition
period for developing emission limits for condensable direct
PM2.5 that are needed to demonstrate attainment of the
PM2.5 NAAQS. As discussed in the April 25, 2007, Clean Air
Fine Particle Implementation Rule (72 FR 20586) and in the May 16,
2008, promulgation of the New Source Review Program Implementation for
fine particulate matter (73 FR 28321), the transition period, which
ends January 1, 2011, allows time to resolve and adopt appropriate
testing procedures for CPM emissions and to collect total primary
(filterable and condensable) PM2.5 emissions data that are
more representative of the emissions of each source in their areas. In
the PM2.5 NSR Implementation Rule, we stated that as part of
this test methods rulemaking, we would ``take comment on an earlier
closing date for the transition period in the NSR program if we are on
track to meet our expectation to complete the test method rule much
earlier than January 1, 2011.'' See 73 FR at 28344. Accordingly, we are
hereby soliciting comments on ending the NSR transition period for CPM
on a date 60 to 90 days after the promulgation date of this test
methods rulemaking.
During the transition period, we are available to provide technical
support to States, as requested, in establishing emissions testing
requirements. We will also solicit the involvement of interested
stakeholders to collect new direct filterable and CPM emissions data
using methodologies that provide more representative data of a source's
direct PM2.5 emissions. These data will be used by us,
States, and others to improve emissions factors and to help establish
or revise source emissions limits in implementation plans. The
transition period will also provide time for additional method
evaluations. During the transition period, we expect that some States
will continue to develop more complete inventories of direct
PM2.5 emissions, particularly for CPM. As needed to
demonstrate attainment of the PM NAAQS, we also expect States to
address the control of direct PM2.5 emissions, including
CPM, with any new actions taken after January 1, 2011 and to address
CPM emissions in any direct PM2.5 regulations or limits
developed under any new PM NAAQS.
As with other methods, any new procedures approved by us will
produce data that will be incorporated into the tools (e.g., emission
factors, emission inventories, air quality modeling) used to assess the
attainment of air quality standards. However, we do not believe that it
is necessary to update continually the assessment tools or revise
previous air quality analyses until evidence is presented that a mid-
course corrective action is needed to achieve the air quality standards
(a mid-course review is required by April 2011 for each area with an
approved attainment date in 2014 or 2015). At that time, updated
inventories and air quality models may be needed to identify and
characterize the emission sources that are impeding adequate progress
towards attaining the air quality standards. Additionally, the new test
data could be used to improve the applicability and performance
evaluations of various control technologies.
D. Request for Comments
We encourage stakeholders to continue to participate in the process
to refine Methods 201A and 202. We are requesting public comments on
all aspects of the proposed test methods. EPA has already engaged
several stakeholder groups as described in Section II.C of this
preamble. Stakeholders and other members of the public who have not yet
participated are encouraged to submit comments. EPA is soliciting as
many constructive comments as possible in order to make the most
appropriate changes to the methods.
We are specifically interested in recommended alternatives to
replace what we have proposed. When submitting comments on alternative
approaches, please submit supporting information to substantiate the
improvements that are achieved with your recommendation. For
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recommended changes to the procedures, include supporting technical
data and any associated cost information. For example, if you are
proposing an alternative procedure, include data or information that
would demonstrate how the alternative procedure would equal or improve
the bias and precision of the proposed methods. In addition, provide
data or cost information that would show the cost implications to
testing companies and analytical laboratories of implementing the
alternative procedure. Although our request for comments is not limited
to these items, the following are examples of items for which we are
specifically requesting comment.
1. Items Associated With Both Test Methods
The proposed test methods are based upon EPA's assessment of
comments made on the Clean Air Fine Particle Implementation Rule (April
25, 2007, 70 FR 20586). Commenters expressed that there is an
overarching need for test methods that are unbiased with respect to
primary particulate matter emissions to the atmosphere and that the
test methods must provide a high degree of consistency (precision) in
these measurements. As a result, we reduced the numerous options and
alternative procedures in the existing methods to a single set of
prescriptive procedures that already existed within the methods. In
addition, we made a few minor changes to reduce further the bias caused
by sulfate artifacts. We are requesting comments on the specific set of
procedures we have proposed and any replacement procedures that would
be less demanding but that would achieve or improve bias and precision.
We are also requesting comments on our decision to eliminate options or
alternatives within the existing methods that may not achieve
comparable results. If we were to consider alternative procedures that
may not achieve comparable results, then what level of difference would
be acceptable?
2. Items Associated With Method 201A
Regarding this proposed method, stakeholders have commented on the
sample duration that would be required to collect a weighable mass. EPA
is requesting comments on alternative methodologies or hardware that
would reduce the sample duration in order to reach a reasonable
detection limit or to demonstrate that emissions are below the
regulatory limit. Commenters should provide information or data,
including cost information, which supports their recommendation.
Stakeholders have expressed concern about the configuration and
size of the proposed sampling train. Specifically, commenters have
expressed concern that the size and length of the combined
PM10 cyclone and the PM2.5 cyclone and filter
require larger port opening(s) and a very large stack cross section to
minimize blockage. In addition, stakeholders have stated that it is
difficult to maintain stack temperature in the sampling train.
Therefore, EPA requests comments on alternatives to the proposed
procedures or hardware. EPA requests comments on alternative procedures
or configurations that would reduce the blockage. EPA also requests
comments on alternative configurations that would allow testers to
maintain stack temperature in the sampling train, thus reducing or
eliminating condensation in the primary or filterable particulate
portions of the method. Recommendations to revise the sampling train
size or configuration should include an assessment of the impacts of
the recommended revisions on the sample size, required sample duration,
and ability to collect a representative sample. Commenters should
provide information or data, including cost information that supports
their recommendation.
3. Items Associated With Method 202
Stakeholders originally expressed concern about the formation of
artifacts in Method 202 when sulfur dioxide was present in the stack
gas. Based on laboratory experiments, the proposed revision to Method
202 eliminates at least an additional 90 percent of the artifact over
the best practices procedures of the existing Method 202. In addition,
the laboratory experiments show that the proposed revision to Method
202 reduces artifact at or below the detection limits of the method.
EPA requests comments on any further concerns with the formation of
artifacts in the proposed method.
Stakeholders have expressed concern about glassware cleaning.
Specifically, stakeholders have questioned the requirement to bake
glassware at 300 [deg]C for 6 hours prior to use in order to reduce the
background level of CPM. Stakeholders have stated that many stack
testing firms and some analytical laboratories may not have ovens that
can achieve this temperature. EPA requests information on the
performance of a lower temperature oven in effectively reducing the
blank level of CPM.
Another stakeholder concern is whether glassware needs to be
completely cleaned between sampling runs. The proposed method requires
clean glassware at the start of each new source category test. EPA
requests comments on alternatives that would minimize the cost of
glassware preparation and reduce bias due to carryover from tests at
the same source category and between source categories. Commenters
should submit data or information to demonstrate that their alternative
procedure would reduce or minimize the carryover or blank and would
minimize the cost to prepare glassware.
Stakeholders expressed concern about the need for Method 202
following filtration at less than 30 [deg]C (85 [deg]F). EPA requests
comments on how to clarify when Method 202 is or is not required.
Stakeholders have expressed concern about the appropriate type of
CPM filter required by the proposed method. EPA requests comments on
the construction material and porosity of the filter. Commenters should
address the capture efficiency required by the method (i.e., the filter
must have an efficiency of at least 99.95 percent (<0.05 percent
penetration) on 0.3 micron particles). Commenters should include how
their alternative would minimize the blank contribution from the
filters.
Commenters have expressed concern about the additional analytical
steps required to process the CPM filter. The proposed method requires
extraction and combination of the filter extract with the appropriate
impinger samples to accurately collect and measure sulfuric acid and
other condensable material. Commenters should address alternative
procedures for CPM filter analysis that would generate precise and
unbiased analysis of CPM collected on the CPM filter.
Stakeholders have expressed concern about maintaining the stack gas
flow through the Teflon[supreg] membrane filter. Stakeholders have
commented on their need to use a supplementary support filter to
maintain flow through the sample filter. EPA requests comments
regarding the use of a support filter that would help maintain stack
gas flow while minimizing or eliminating the support filter's
contribution to the sample mass. EPA requests comments on the use of
this alternative and its potential impact on bias and precision, as
well as its potential impact on cost.
IV. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory Planning and Review
Under Executive Order (EO) 12866 (58 FR 51735, October 4, 1993),
this proposed action is a ``significant regulatory action'' since it
raises novel
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legal or policy issues arising out of legal mandates, the President's
priorities, or the principles set forth in this Executive Order.
Accordingly, EPA submitted this proposed action to the Office of
Management and Budget (OMB) for review under Executive Order 12866 and
any changes made in response to OMB recommendations have been
documented in the docket for this action.
B. Paperwork Reduction Act
This proposed action does not impose an information collection
burden under the provisions of the Paperwork Reduction Act, 44 U.S.C.
3501 et seq. Burden is defined at 5 CFR 1320.3(b). The proposed
amendments do not contain any reporting or recordkeeping requirements.
The proposed amendments revise two existing source test methods to
allow one method to perform additional particle sizing at 2.5
micrometers and to improve the precision and accuracy of the other test
method.
C. Regulatory Flexibility Act
The Regulatory Flexibility Act (RFA) generally requires an agency
to prepare a regulatory flexibility analysis of any rule subject to
notice and comment rulemaking requirements under the Administrative
Procedure Act or any other statute unless the agency certifies that the
rule will not have a significant economic impact on a substantial
number of small entities. Small entities include small businesses,
small organizations, and small governmental jurisdictions.
For purposes of assessing the impacts of this rule on small
entities, small entity is defined as: (1) A small business as defined
by the Small Business Administration's (SBA) regulations at 13 CFR
121.201; (2) a small governmental jurisdiction that is a government of
a city, county, town, school district or special district with a
population of less than 50,000; and (3) a small organization that is
any not-for-profit enterprise which is independently owned and operated
and is not dominant in its field.
After considering the economic impacts of this proposed rule on
small entities, I certify that this action will not have a significant
economic impact on a substantial number of small entities. We do not
anticipate that the proposed changes to Methods 201A and 202 will
result in a significant economic impact on small entities. Most of the
emission sources that will be required by State regulatory agencies
(and Federal regulators after 2011) to conduct tests using the revised
methods are those that have PM emissions of 100 tons per year or more.
EPA expects that few, if any, of these emission sources will be small
entities.
Although this proposed rule will not have a significant economic
impact on a substantial number of small entities, EPA nonetheless has
tried to reduce the impact of this rule on small entities. In this
preamble, we explained that this rule does not require any entities to
use these proposed test methods. Such a requirement would be mandated
by a separate independent regulatory action. We indicated that upon
promulgation of this rule, some entities may be required to use these
test methods as a result of existing permits or regulations. Since the
cost to use the proposed test methods is comparable to the cost of the
methods they replace, little or no significant economic impact to small
entities will accompany the increased precision and accuracy of the
revised test methods which are proposed. We also indicated that after
January 1, 2011, when the transition period established in the Clean
Air Fine Particle Implementation Rule expires, States are required to
consider inclusion of pollutants measured by these test methods in new
or revised regulations. The economic impacts caused by any new or
revised State regulations for fine PM would be associated with those
State rules and not with this proposal to modify the existing test
methods. Consequently, we believe that this rule imposes little if any
adverse economic impact to small entities. However, we continue to be
interested in the potential impacts of the proposed rule on small
entities and welcome comments on