National Emission Standards for Hazardous Air Pollutants for Chemical Recovery Combustion Sources at Kraft, Soda, Sulfite, and Stand-Alone Semichemical Pulp Mills, 97046-97095 [2016-30758]
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ENVIRONMENTAL PROTECTION
AGENCY
40 CFR Part 63
[EPA–HQ–OAR–2014–0741; FRL–9957–07–
OAR]
RIN 2060–AS46
National Emission Standards for
Hazardous Air Pollutants for Chemical
Recovery Combustion Sources at
Kraft, Soda, Sulfite, and Stand-Alone
Semichemical Pulp Mills
Environmental Protection
Agency (EPA).
ACTION: Proposed rule.
AGENCY:
The Environmental Protection
Agency (EPA) is proposing amendments
to the National Emission Standards for
Hazardous Air Pollutants (NESHAP) for
Chemical Recovery Combustion Sources
at Kraft, Soda, Sulfite, and Stand-Alone
Semichemical Pulp Mills to address the
results of the residual risk and
technology review (RTR) that the EPA is
required to conduct under the Clean Air
Act (CAA). These proposed
amendments include revisions to the
opacity monitoring provisions; addition
of electrostatic precipitator (ESP)
parameter monitoring provisions; a
requirement for 5-year periodic
emissions testing; revisions to
provisions addressing periods of
startup, shutdown, and malfunction
(SSM); and technical and editorial
changes. The EPA is proposing these
amendments to improve the
effectiveness of the rule.
DATES: Comments. Comments must be
received on or before February 28, 2017.
Under the Paperwork Reduction Act
(PRA), comments on the information
collection provisions are best assured of
consideration if the Office of
Management and Budget (OMB)
receives a copy of your comments on or
before January 30, 2017.
Public Hearing. A public hearing will
be held if requested by January 4, 2017.
ADDRESSES: Comments. Submit your
comments, identified by Docket ID No.
EPA–HQ–OAR–2014–0741, at https://
www.regulations.gov. Follow the online
instructions for submitting comments.
Once submitted, comments cannot be
edited or removed from Regulations.gov.
The EPA may publish any comment
received to its public docket. Do not
submit electronically any information
you consider to be Confidential
Business Information (CBI) or other
information whose disclosure is
restricted by statute. Multimedia
submissions (audio, video, etc.) must be
accompanied by a written comment.
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SUMMARY:
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The written comment is considered the
official comment and should include
discussion of all points you wish to
make. The EPA will generally not
consider comments or comment
contents located outside of the primary
submission (i.e., on the Web, cloud, or
other file sharing system). For
additional submission methods, the full
EPA public comment policy,
information about CBI or multimedia
submissions, and general guidance on
making effective comments, please visit
https://www2.epa.gov/dockets/
commenting-epa-dockets.
Instructions. Direct your comments to
Docket ID No. EPA–HQ–OAR–2014–
0741. The 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 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 email. The
https://www.regulations.gov Web site is
an ‘‘anonymous access’’ system, which
means the EPA will not know your
identity or contact information unless
you provide it in the body of your
comment. If you send an email
comment directly to the EPA without
going through https://
www.regulations.gov, your email
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, the 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 the EPA
cannot read your comment due to
technical difficulties and cannot contact
you for clarification, the EPA may not
be able to consider your comment.
Electronic files should not include
special characters or any form of
encryption and be free of any defects or
viruses. For additional information
about the EPA’s public docket, visit the
EPA Docket Center homepage at https://
www.epa.gov/dockets.
Docket. The EPA has established a
docket for this rulemaking under Docket
ID No. EPA–HQ–OAR–2014–0741. All
documents in the docket are listed in
the 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,
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is not placed on the Internet and will be
publicly available only in hard copy.
Publicly available docket materials are
available either electronically in
Regulations.gov or in hard copy at the
EPA Docket Center, Room 3334, EPA
WJC West Building, 1301 Constitution
Ave. NW., Washington, DC. The Public
Reading Room 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 EPA Docket Center is
(202) 566–1742.
Public Hearing. A public hearing will
be held, if requested by January 4, 2017,
to accept oral comments on this
proposed action. If a hearing is
requested, it will be held at the EPA’s
Washington, DC campus located at 1201
Constitution Avenue NW., Washington,
DC. The hearing, if requested, will begin
at 9:00 a.m. (local time) and will
conclude at 5:00 p.m. (local time) on
January 17, 2017. To request a hearing,
to register to speak at a hearing, or to
inquire if a hearing will be held, please
contact Ms. Aimee St. Clair at (919)
541–1063 or by email at stclair.aimee@
epa.gov. The last day to pre-register to
speak at a hearing, if one is held, will
be January 12, 2017.
Additionally, requests to speak will
be taken the day of the hearing at the
hearing registration desk, although
preferences on speaking times may not
be able to be fulfilled. Please note that
registration requests received before the
hearing will be confirmed by the EPA
via email. The EPA will make every
effort to accommodate all speakers who
arrive and register. Because the hearing
will be held at a United States
governmental facility, individuals
planning to attend the hearing should be
prepared to show valid picture
identification to the security staff in
order to gain access to the meeting
room. Please note that the REAL ID Act,
passed by Congress in 2005, established
new requirements for entering federal
facilities. If your driver’s license is
issued by Alaska, American Samoa,
Arizona, Kentucky, Louisiana, Maine,
Massachusetts, Minnesota, Montana,
New York, Oklahoma or the state of
Washington, you must present an
additional form of identification to enter
the federal building. Acceptable
alternative forms of identification
include: Federal employee badges,
passports, enhanced driver’s licenses
and military identification cards. In
addition, you will need to obtain a
property pass for any personal
belongings you bring with you. Upon
leaving the building, you will be
required to return this property pass to
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the security desk. No large signs will be
allowed in the building, cameras may
only be used outside of the building and
demonstrations will not be allowed on
federal property for security reasons.
Please note that any updates made to
any aspect of the hearing, including
whether or not a hearing will be held,
will be posted online at https://
www.epa.gov/stationary-sources-airpollution/kraft-soda-sulfite-and-standalone-semichemical-pulp-mills-mact-ii.
We ask that you contact Ms. Aimee St.
Clair at (919) 541–1063 or by email at
stclair.aimee@epa.gov or monitor our
Web site to determine if a hearing will
be held. The EPA does not intend to
publish a notice in the Federal Register
announcing any such updates. Please go
to https://www.epa.gov/stationarysources-air-pollution/kraft-soda-sulfiteand-stand-alone-semichemical-pulpmills-mact-ii for more information on
the public hearing.
FOR FURTHER INFORMATION CONTACT: For
questions about this proposed action,
contact Dr. Kelley Spence, Sector
Policies and Programs Division (Mail
Code: E143–03), Office of Air Quality
Planning and Standards, U.S.
Environmental Protection Agency,
Research Triangle Park, North Carolina
27711; telephone number: (919) 541–
3158; fax number: (919) 541–3470; and
email address: spence.kelley@epa.gov.
For specific information regarding the
risk modeling methodology, contact Mr.
James Hirtz, Health and Environmental
Impacts Division (Mail Code: C539–02),
Office of Air Quality Planning and
Standards, U.S. Environmental
Protection Agency, Research Triangle
Park, North Carolina 27711; telephone
number: (919) 541–0881; fax number:
(919) 541–0840; and email address:
hirtz.james@epa.gov. For information
about the applicability of the NESHAP
to a particular entity, contact Ms. Sara
Ayres, Office of Enforcement and
Compliance Assurance, U.S.
Environmental Protection Agency,
USEPA Region 5 (Mail Code: E–19J), 77
West Jackson Boulevard, Chicago IL
60604; telephone number: (312) 353–
6266; and email address: ayres.sara@
epa.gov.
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SUPPLEMENTARY INFORMATION:
Preamble Acronyms and
Abbreviations. We use multiple
acronyms and terms in this preamble.
While this list may not be exhaustive, to
ease the reading of this preamble and for
reference purposes, the EPA defines the
following terms and acronyms here:
AEGL acute exposure guideline levels
AERMOD air dispersion model used by the
HEM–3 model
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ANSI American National Standards
Institute
ASME American Society of Mechanical
Engineers
ASTM American Society for Testing and
Materials
ATSDR Agency for Toxic Substances and
Disease Registry
BACT best available control technology
BAT best available technology
BLO black liquor oxidation
BLS black liquor solids
CAA Clean Air Act
CaCO3 calcium carbonate
CalEPA California EPA
CBI Confidential Business Information
CEDRI Compliance and Emissions Data
Reporting Interface
CFR Code of Federal Regulations
CMS continuous monitoring system
COMS continuous opacity monitoring
system
CPMS continuous parameter monitoring
system
DCE direct contact evaporator
EJ environmental justice
EPA Environmental Protection Agency
ERPG Emergency Response Planning
Guidelines
ERT Electronic Reporting Tool
ESP electrostatic precipitator
FR Federal Register
gr/dscf grains per dry standard cubic foot
HAP hazardous air pollutant
HCCPD hexachlorocyclopentadiene
HCl hydrochloric acid
HEM–3 Human Exposure Model, Version
1.1.0
HF hydrogen fluoride
HI hazard index
HQ hazard quotient
IBR incorporation by reference
ICR Information Collection Request
IRIS Integrated Risk Information System
km kilometer
LAER lowest achievable emission rate
lb/hr pounds per hour
lb/ton pounds per ton
LOAEL lowest-observed-adverse-effect level
MACT maximum achievable control
technology
mg/kg-day milligrams per kilogram per day
mg/m3 milligrams per cubic meter
MIR maximum individual risk
Na2CO3 sodium carbonate
Na2S sodium sulfide
NAAQS National Ambient Air Quality
Standards
NAC National Advisory Committee
NAICS North American Industry
Classification System
NaOH sodium hydroxide
NAS National Academy of Sciences
NATA National Air Toxics Assessment
NCASI National Council for Air and Stream
Improvement
NDCE nondirect contact evaporator
NEI National Emissions Inventory
NESHAP National Emission Standards for
Hazardous Air Pollutants
NH3 ammonia
NOAA National Oceanic and Atmospheric
Administration
NOAEL no-observed-adverse-effect level
NRC National Research Council
NRDC Natural Resources Defense Council
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NSPS New Source Performance Standards
NTTAA National Technology Transfer and
Advancement Act
O&M operation and maintenance
O2 oxygen
OAQPS Office of Air Quality Planning and
Standards
OMB Office of Management and Budget
PAH polycyclic aromatic hydrocarbons
PB–HAP hazardous air pollutant known to
be persistent and bio-accumulative in the
environment
PDF portable document format
PEL probable effects level
PM particulate matter
PM2.5 fine particles (particulate matter with
particles less than 2.5 micrometers in
diameter)
POM polycyclic organic matter
ppm parts per million
PRA Paperwork Reduction Act
PTC Performance Test Code
QA quality assurance
RACT reasonably available control
technology
RBLC RACT/BACT/LAER Clearinghouse
REL reference exposure level
RFA Regulatory Flexibility Act
RfC reference concentration
RfD reference dose
RTO regenerative thermal oxidizer
RTR residual risk and technology review
SAB Science Advisory Board
SCC source classification code
SDT smelt dissolving tank
SOP standard operating procedure
SSM startup, shutdown, and malfunction
STAPPA/ State and Territorial Air
Pollution Program
ALAPCO Administrators/Association of
Local Air Pollution Control Officers
TEQ toxic equivalent
THC total hydrocarbon
TOSHI target organ-specific hazard index
tpy tons per year
TRIM.FaTE Total Risk Integrated
Methodology.Fate, Transport, and
Ecological Exposure model
TRS total reduced sulfur
UF uncertainty factor
mg/m3 micrograms per cubic meter
UMRA Unfunded Mandates Reform Act
URE unit risk estimate
yr year
Organization of this Document. The
information in this preamble is
organized as follows:
I. General Information
A. Executive Summary
B. Does this action apply to me?
C. Where can I get a copy of this document
and other related information?
D. What should I consider as I prepare my
comments for the EPA?
II. Background
A. What is the statutory authority for this
action?
B. What is this source category and how
does the current NESHAP regulate its
HAP emissions?
C. What data collection activities were
conducted to support this action?
D. What other relevant background
information and data are available?
III. Analytical Procedures
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A. How did we estimate post-MACT risks
posed by the source category?
B. How did we consider the risk results in
making decisions for this proposal?
C. How did we perform the technology
review?
IV. Analytical Results and Proposed
Decisions
A. What are the results of the risk
assessment and analyses?
B. What are our proposed decisions
regarding risk acceptability, ample
margin of safety, and adverse
environmental effects?
C. What are the results and proposed
decisions based on our technology
review?
D. What other actions are we proposing?
E. What compliance dates are we
proposing?
V. Summary of Cost, Environmental, and
Economic Impacts
A. What are the affected sources?
B. What are the air quality impacts?
C. What are the cost impacts?
D. What are the economic impacts?
E. What are the benefits?
VI. Request for Comments
VII. Submitting Data Corrections
VIII. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory
Planning and Review and Executive
Order 13563: Improving Regulation and
Regulatory Review
B. Paperwork Reduction Act (PRA)
C. Regulatory Flexibility Act (RFA)
D. Unfunded Mandates Reform Act
(UMRA)
E. Executive Order 13132: Federalism
F. Executive Order 13175: Consultation
and Coordination with Indian Tribal
Governments
G. Executive Order 13045: Protection of
Children from Environmental Health
Risks 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 (NTTAA) and 1 CFR
part 51
J. Executive Order 12898: Federal Actions
to Address Environmental Justice in
Minority Populations and Low-Income
Populations
I. General Information
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A. Executive Summary
1. Purpose of the Regulatory Action
Section 112(f)(2) of the CAA requires
the EPA to analyze and address the
residual risk associated with hazardous
air pollutant emissions from source
categories subject to maximum
achievable control technology (MACT)
standards. This review, known as the
residual risk review, is a one-time
review that the statute provides will be
done within 8 years of issuance of the
MACT standard. Section 112(d)(6) of the
CAA requires the EPA to review and
revise CAA section 112 emissions
standards, as necessary, taking into
account developments in practices,
processes, and control technologies.
Emission standards promulgated under
CAA section 112 are to be reviewed no
less often than every 8 years. The EPA
issued the NESHAP for Chemical
Recovery Combustion Sources at Kraft,
Soda, Sulfite, and Stand-Alone
Semichemical Mills (40 Code of Federal
Regulations (CFR) part 63, subpart MM)
in 2001. The 2001 emission standards
are due for review under CAA sections
112(d)(6) and 112(f)(2). In addition to
conducting the RTR for subpart MM, we
are evaluating the SSM provisions in the
rule in light of the United States Court
of Appeals for the District of Columbia
Circuit decision in Sierra Club v. EPA,
551 F.3d 1019 (D.C. Cir. 2008). As
explained in section IV of this preamble,
in the Sierra Club case, the D.C. Circuit
vacated the SSM exemption provisions
in the General Provisions for nonopacity
and opacity standards. Finally, the EPA
evaluated the rule to determine if
additional amendments were warranted
or necessary to ensure continuous
compliance with the standard and to
promote consistency with other
standards.
2. Summary of the Major Proposed
Revisions
The EPA is not proposing to make any
changes pursuant to 112(f)(2) as a result
of its residual risk review. The EPA is
proposing to reduce opacity limits as a
result of the technology review under
CAA section 112(d)(6). In addition, we
are proposing the following as part of
the technology review: Revising the
opacity monitoring provisions, requiring
ESP parameter monitoring for processes
equipped with ESPs, clarifying the
monitoring for combined ESP/wet
scrubber controls, and providing
alternative monitoring for smelt
dissolving tank (SDT) wet scrubbers.
As an additional action, we are
proposing to improve the compliance
provisions of the subpart by proposing
to require periodic air emissions
performance testing once every 5 years
for facilities subject to the standards for
Chemical Recovery Combustion Sources
at Kraft, Soda, Sulfite, and Stand-Alone
Semichemical Pulp Mills. To address
the SSM exemptions, we are proposing
amendments to subpart MM that will (1)
require facilities to meet the standard at
all times, including during periods of
SSM, and (2) provide alternative
monitoring parameters for wet scrubbers
and ESPs during these periods. We are
also proposing changes to the subpart
MM NESHAP and the General
Provisions applicability table to
eliminate the SSM exemption. To
increase the ease and efficiency of data
submittal and improve data
accessibility, we are proposing to
require mills to submit electronic copies
of compliance reports, which includes
performance test reports.
We are also proposing a number of
technical and editorial changes. These
changes include the following:
Clarifying the location in 40 CFR part 60
of applicable EPA test methods;
updating the facility name for Cosmo
Specialty Fibers; revising the definitions
section in 40 CFR 63.861; corrected
misspelling in 40 CFR 63.862(c),
revising multiple sections to remove
reference to former smelters and former
black liquor gasification system at
Georgia-Pacific’s facility in Big Island,
Virginia; revising the monitoring
requirements section; revising the
performance test requirements section
to specify the conditions for conducting
performance tests and to revise the
ambient O2 concentration in Equations
7 and 8; revising the recordkeeping
requirements section in 40 CFR 63.866
to include the requirement to record
information on failures to meet the
applicable standard; revising the
terminology in the delegation of
authority section in 40 CFR 63.868 to
match the definitions in 40 CFR 63.90;
and revising the General Provisions
applicability table (Table 1 to subpart
MM of part 63) to align with those
sections of the General Provisions that
have been amended or reserved over
time.
3. Costs and Benefits
Table 1 summarizes the costs of this
action. See section V of this preamble
for further discussion.
TABLE 1—SUMMARY OF THE COSTS OF THIS PROPOSED ACTION
Capital cost,
$ million
Requirement
Change in opacity monitoring provisions for recovery furnaces and lime kilns ......................................................
ESP parameter monitoring ......................................................................................................................................
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5.7
Annual cost,
$ million
8.8
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TABLE 1—SUMMARY OF THE COSTS OF THIS PROPOSED ACTION—Continued
Requirement
Capital cost,
$ million
Periodic emissions testing .......................................................................................................................................
Incremental reporting/recordkeeping .......................................................................................................................
........................
0.50
1.1
1.9
Total nationwide ...............................................................................................................................................
48
13
The EPA estimates that the proposed
changes to the opacity limits and
monitoring allowances will reduce PM
emissions by approximately 235 (tons
per year) tpy and fine particle (PM2.5)
emissions by approximately 112 tpy.
Periodic testing will tend to reduce
emissions by providing incentive for
facilities to maintain their control
systems and make periodic adjustments
to ensure peak performance. Eliminating
the SSM exemption will reduce
emissions by requiring facilities to meet
the applicable standard during SSM
periods. See section V of this preamble
for further discussion.
B. Does this action apply to me?
Table 2 of this preamble lists the
NESHAP and associated regulated
industrial source categories that are the
subject of this proposal. Table 2 is not
intended to be exhaustive, but rather
provides a guide for readers regarding
the entities that this proposed action is
likely to affect. The proposed standards,
once promulgated, will be directly
applicable to the affected sources.
Federal, state, local, and tribal
government entities would not be
affected by this proposed action. As
defined in the Initial List of Categories
of Sources Under Section 112(c)(1) of
the Clean Air Act Amendments of 1990
(see 57 FR 31576, July 16, 1992), the
‘‘Pulp and Paper Production’’ source
category is any facility engaged in the
production of pulp and/or paper. The
EPA developed the NESHAPs for the
Annual cost,
$ million
source category in phases. This
NESHAP, 40 CFR part 63, subpart MM,
regulates chemical recovery combustion
sources at kraft, soda, sulfite, and standalone semichemical pulp mills. The
NESHAP for non-combustion sources
(40 CFR part 63, subpart S) regulates
non-combustion processes at mills that
(1) chemically pulp wood fiber (using
kraft, sulfite, soda, and semichemical
methods), (2) mechanically pulp wood
fiber (e.g., groundwood,
thermomechanical, pressurized), (3)
pulp secondary fibers (deinked and nondeinked), (4) pulp non-wood material,
and (5) manufacture paper. This
proposal only addresses the RTR for
subpart MM, and does not propose any
amendments to subpart S.
TABLE 2—NESHAP AND INDUSTRIAL SOURCE CATEGORIES AFFECTED BY THIS PROPOSED ACTION
NAICS code a
Source category
NESHAP
Pulp and Paper Production .................
Chemical Recovery Combustion Sources at Kraft, Soda, Sulfite, and StandAlone Semichemical Pulp Mills.
a North
American Industry Classification System.
D. What should I consider as I prepare
my comments for the EPA?
C. Where can I get a copy of this
document and other related
information?
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32211, 32212, 32213
In addition to being available in the
docket, an electronic copy of this action
is available on the Internet through the
EPA’s Stationary Sources of Air
Pollution Web site, a forum for
information and technology exchange in
various areas of air pollution control. A
redline version of the regulatory
language that incorporates the proposed
changes in this action is available in the
docket for this action (Docket ID No.
EPA–HQ–OAR–2014–0741). Following
signature by the EPA Administrator, the
EPA will post a copy of this proposed
action at: https://www.epa.gov/
stationary-sources-air-pollution/kraftsoda-sulfite-and-stand-alonesemichemical-pulp-mills-mact-ii.
Following publication in the Federal
Register, the EPA will post the Federal
Register version of the proposal and key
technical documents at this same Web
site. Information on the overall RTR
program is available at https://
www3.epa.gov/ttn/atw/rrisk/rtrpg.html.
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Submitting CBI. Do not submit
information containing CBI to the EPA
through https://www.regulations.gov or
email. 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 the 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
comments that includes information
claimed as CBI, you must submit a copy
of the comments that does not contain
the information claimed as CBI for
inclusion in the public docket. If you
submit a CD–ROM or disk that does not
contain CBI, mark the outside of the
disk or CD–ROM clearly that it does not
contain CBI. Information not marked as
CBI will be included in the public
docket and the EPA’s electronic public
docket without prior notice. Information
marked as CBI will not be disclosed
except in accordance with procedures
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set forth in 40 CFR part 2. Send or
deliver information identified as CBI
only to the following address: OAQPS
Document Control Officer (C404–02),
OAQPS, U.S. Environmental Protection
Agency, Research Triangle Park, North
Carolina 27711, Attention Docket ID No.
EPA–HQ–OAR–2014–0741.
II. Background
A. What is the statutory authority for
this action?
Section 112 of the CAA establishes a
two-stage regulatory process to address
emissions of hazardous air pollutants
(HAPs) from stationary sources. In the
first stage, after the EPA has identified
categories of sources emitting one or
more of the HAPs listed in CAA section
112(b), CAA section 112(d) requires the
Agency to promulgate technology-based
NESHAPs for those sources. ‘‘Major
sources’’ are those that emit or have the
potential to emit 10 tpy or more of a
single HAP or 25 tpy or more of any
combination of HAPs. For major
sources, the technology-based NESHAP
must reflect the maximum degree of
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emission reductions of HAPs achievable
(after considering cost, energy
requirements, and non-air quality health
and environmental impacts) and are
commonly referred to as MACT
standards.
MACT standards must reflect the
maximum degree of emissions reduction
achievable through the application of
measures, processes, methods, systems,
or techniques, including, but not limited
to, measures that: (1) Reduce the volume
of or eliminate pollutants through
process changes, substitution of
materials, or other modifications; (2)
enclose systems or processes to
eliminate emissions; (3) capture or treat
pollutants when released from a
process, stack, storage, or fugitive
emissions point; (4) are design,
equipment, work practice, or
operational standards (including
requirements for operator training or
certification); or (5) are a combination of
the above. CAA section 112(d)(2)(A)–
(E). The MACT standards may take the
form of design, equipment, work
practice, or operational standards where
the EPA first determines either that: (1)
A pollutant cannot be emitted through
a conveyance designed and constructed
to emit or capture the pollutant, or that
any requirement for, or use of, such a
conveyance would be inconsistent with
law; or (2) the application of
measurement methodology to a
particular class of sources is not
practicable due to technological and
economic limitations. CAA section
112(h)(1)–(2).
The MACT ‘‘floor’’ is the minimum
control level allowed for MACT
standards promulgated under CAA
section 112(d)(3) and may not be based
on cost considerations. For new sources,
the MACT floor cannot be less stringent
than the emissions control that is
achieved in practice by the bestcontrolled similar source. The MACT
floor for existing sources can be less
stringent than floors for new sources,
but not less stringent than the average
emissions limitation achieved by the
best-performing 12 percent of existing
sources in the category or subcategory
(or the best-performing five sources for
categories or subcategories with fewer
than 30 sources). In developing MACT
standards, the EPA must also consider
control options that are more stringent
than the floor. We may establish
standards more stringent than the floor
based on considerations of the cost of
achieving the emission reductions, any
non-air quality health and
environmental impacts, and energy
requirements.
The EPA is then required to review
these technology-based standards and
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revise them ‘‘as necessary (taking into
account developments in practices,
processes, and control technologies)’’ no
less frequently than every 8 years. CAA
section 112(d)(6). In conducting this
review, the EPA is not required to
recalculate the MACT floor. Natural
Resources Defense Council (NRDC) v.
EPA, 529 F.3d 1077, 1084 (D.C. Cir.
2008). Association of Battery Recyclers,
Inc. v. EPA, 716 F.3d 667 (D.C. Cir.
2013).
The second stage in standard-setting
focuses on reducing any remaining (i.e.,
‘‘residual’’) risk according to CAA
section 112(f). Section 112(f)(1) of the
CAA required that the EPA prepare a
report to Congress discussing (among
other things) methods of calculating the
risks posed (or potentially posed) by
sources after implementation of the
MACT standards, the public health
significance of those risks, and the
EPA’s recommendations as to legislation
regarding such remaining risk. The EPA
prepared and submitted the Residual
Risk Report to Congress, EPA–453/R–
99–001 (Risk Report) in March 1999.
Section 112(f)(2) of the CAA then
provides that if Congress does not act on
any recommendation in the Risk Report,
the EPA must analyze and address
residual risk for each category or
subcategory of sources 8 years after
promulgation of such standards
pursuant to CAA section 112(d).
Section 112(f)(2) of the CAA requires
the EPA to determine for source
categories subject to MACT standards
whether promulgation of additional
standards is needed to provide an ample
margin of safety to protect public health.
Section 112(f)(2)(B) of the CAA
expressly preserves the EPA’s use of the
two-step process for developing
standards to address any residual risk
and the Agency’s interpretation of
‘‘ample margin of safety’’ developed in
the National Emissions Standards for
Hazardous Air Pollutants: Benzene
Emissions from Maleic Anhydride
Plants, Ethylbenzene/Styrene Plants,
Benzene Storage Vessels, Benzene
Equipment Leaks, and Coke By-Product
Recovery Plants (Benzene NESHAP) (54
FR 38044, September 14, 1989). The
EPA notified Congress in the Risk
Report that the Agency intended to use
the Benzene NESHAP approach in
making CAA section 112(f) residual risk
determinations (EPA–453/R–99–001, p.
ES–11). The EPA subsequently adopted
this approach in its residual risk
determinations and, in a challenge to
the risk review for the Synthetic Organic
Chemical Manufacturing source
category, the United States Court of
Appeals for the District of Columbia
Circuit upheld as reasonable the EPA’s
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interpretation that CAA section 112(f)(2)
incorporates the approach established in
the Benzene NESHAP. See NRDC v.
EPA, 529 F.3d 1077, 1083 (D.C. Cir.
2008) (‘‘[S]ubsection 112(f)(2)(B)
expressly incorporates the EPA’s
interpretation of the Clean Air Act from
the Benzene standard, complete with a
citation to the Federal Register.’’); see
also, A Legislative History of the Clean
Air Act Amendments of 1990, vol. 1, p.
877 (Senate debate on Conference
Report).
The first step in the process of
evaluating residual risk is the
determination of acceptable risk. If risks
are unacceptable, the EPA cannot
consider cost in identifying the
emissions standards necessary to bring
risks to an acceptable level. The second
step is the determination of whether
standards must be further revised in
order to provide an ample margin of
safety to protect public health. The
ample margin of safety is the level at
which the standards must be set, unless
an even more stringent standard is
necessary to prevent, taking into
consideration costs, energy, safety, and
other relevant factors, an adverse
environmental effect.
1. Step 1—Determination of
Acceptability
The Agency in the Benzene NESHAP
concluded that ‘‘the acceptability of risk
under section 112 is best judged on the
basis of a broad set of health risk
measures and information’’ and that the
‘‘judgment on acceptability cannot be
reduced to any single factor.’’ Benzene
NESHAP at 38046. The determination of
what represents an ‘‘acceptable’’ risk is
based on a judgment of ‘‘what risks are
acceptable in the world in which we
live’’ (Risk Report at 178, quoting NRDC
v. EPA, 824 F. 2d 1146, 1165 (D.C. Cir.
1987) (en banc) (‘‘Vinyl Chloride’’),
recognizing that our world is not riskfree.
In the Benzene NESHAP, we stated
that ‘‘EPA will generally presume that if
the risk to [the maximum exposed]
individual is no higher than
approximately one in 10 thousand, that
risk level is considered acceptable.’’ 54
FR at 38045, September 14, 1989. We
discussed the maximum individual
lifetime cancer risk (or maximum
individual risk (MIR)) as being ‘‘the
estimated risk that a person living near
a plant would have if he or she were
exposed to the maximum pollutant
concentrations for 70 years.’’ Id. We
explained that this measure of risk ‘‘is
an estimate of the upper bound of risk
based on conservative assumptions,
such as continuous exposure for 24
hours per day for 70 years.’’ Id. We
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acknowledged that maximum
individual lifetime cancer risk ‘‘does not
necessarily reflect the true risk, but
displays a conservative risk level which
is an upper-bound that is unlikely to be
exceeded.’’ Id.
Understanding that there are both
benefits and limitations to using the
MIR as a metric for determining
acceptability, we acknowledged in the
Benzene NESHAP that ‘‘consideration of
maximum individual risk . . . must
take into account the strengths and
weaknesses of this measure of risk.’’ Id.
Consequently, the presumptive risk
level of 100-in-1 million (1-in-10
thousand) provides a benchmark for
judging the acceptability of maximum
individual lifetime cancer risk, but does
not constitute a rigid line for making
that determination. Further, in the
Benzene NESHAP, we noted that:
‘‘[p]articular attention will also be
accorded to the weight of evidence presented
in the risk assessment of potential
carcinogenicity or other health effects of a
pollutant. While the same numerical risk
may be estimated for an exposure to a
pollutant judged to be a known human
carcinogen, and to a pollutant considered a
possible human carcinogen based on limited
animal test data, the same weight cannot be
accorded to both estimates. In considering
the potential public health effects of the two
pollutants, the Agency’s judgment on
acceptability, including the MIR, will be
influenced by the greater weight of evidence
for the known human carcinogen.’’
Id. at 38046. The Agency also
explained in the Benzene NESHAP that:
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‘‘[i]n establishing a presumption for MIR,
rather than a rigid line for acceptability, the
Agency intends to weigh it with a series of
other health measures and factors. These
include the overall incidence of cancer or
other serious health effects within the
exposed population, the numbers of persons
exposed within each individual lifetime risk
range and associated incidence within,
typically, a 50 km exposure radius around
facilities, the science policy assumptions and
estimation uncertainties associated with the
risk measures, weight of the scientific
evidence for human health effects, other
quantified or unquantified health effects,
effects due to co-location of facilities, and coemission of pollutants.’’
Id. at 38045. In some cases, these
health measures and factors taken
together may provide a more realistic
description of the magnitude of risk in
the exposed population than that
provided by maximum individual
lifetime cancer risk alone.
As noted earlier, in NRDC v. EPA, the
court held that CAA section 112(f)(2)
‘‘incorporates the EPA’s interpretation
of the Clean Air Act from the Benzene
Standard.’’ The court further held that
Congress’ incorporation of the Benzene
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standard applies equally to carcinogens
and non-carcinogens. 529 F.3d at 1081–
82. Accordingly, we also consider noncancer risk metrics in our determination
of risk acceptability and ample margin
of safety.
2. Step 2—Determination of Ample
Margin of Safety
Section 112(f)(2) of the CAA requires
the EPA to determine, for source
categories subject to MACT standards,
whether those standards provide an
ample margin of safety to protect public
health. As explained in the Benzene
NESHAP, ‘‘the second step of the
inquiry, determining an ‘ample margin
of safety,’ again includes consideration
of all of the health factors, and whether
to reduce the risks even further . . . .
Beyond that information, additional
factors relating to the appropriate level
of control will also be considered,
including costs and economic impacts
of controls, technological feasibility,
uncertainties, and any other relevant
factors. Considering all of these factors,
the Agency will establish the standard
at a level that provides an ample margin
of safety to protect the public health, as
required by section 112.’’ 54 FR at
38046, September 14, 1989.
According to CAA section
112(f)(2)(A), if the MACT standards for
HAP ‘‘classified as a known, probable,
or possible human carcinogen do not
reduce lifetime excess cancer risks to
the individual most exposed to
emissions from a source in the category
or subcategory to less than one in one
million,’’ the EPA must promulgate
residual risk standards for the source
category (or subcategory), as necessary
to provide an ample margin of safety to
protect public health. In doing so, the
EPA may adopt standards equal to
existing MACT standards if the EPA
determines that the existing standards
(i.e., the MACT standards) are
sufficiently protective. NRDC v. EPA,
529 F.3d 1077, 1083 (D.C. Cir. 2008) (‘‘If
EPA determines that the existing
technology-based standards provide an
‘ample margin of safety,’ then the
Agency is free to readopt those
standards during the residual risk
rulemaking.’’) The EPA must also adopt
more stringent standards, if necessary,
to prevent an adverse environmental
effect,1 but must consider cost, energy,
1 ‘‘Adverse environmental effect’’ is defined as
any significant and widespread adverse effect,
which may be reasonably anticipated to wildlife,
aquatic life, or natural resources, including adverse
impacts on populations of endangered or threatened
species or significant degradation of environmental
qualities over broad areas. CAA section 112(a)(7).
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97051
safety, and other relevant factors in
doing so.
The CAA does not specifically define
the terms ‘‘individual most exposed,’’
‘‘acceptable level,’’ and ‘‘ample margin
of safety.’’ In the Benzene NESHAP, 54
FR at 38044–38045, September 14, 1989,
the Agency stated as an overall
objective:
In protecting public health with an ample
margin of safety under section 112, EPA
strives to provide maximum feasible
protection against risks to health from
hazardous air pollutants by (1) protecting the
greatest number of persons possible to an
individual lifetime risk level no higher than
approximately 1-in-1 million and (2) limiting
to no higher than approximately 1-in-10
thousand [i.e., 100-in-1 million] the
estimated risk that a person living near a
plant would have if he or she were exposed
to the maximum pollutant concentrations for
70 years.
The Agency further stated that ‘‘[t]he
EPA also considers incidence (the
number of persons estimated to suffer
cancer or other serious health effects as
a result of exposure to a pollutant) to be
an important measure of the health risk
to the exposed population. Incidence
measures the extent of health risks to
the exposed population as a whole, by
providing an estimate of the occurrence
of cancer or other serious health effects
in the exposed population.’’ Id. at
38045.
In the ample margin of safety decision
process, the Agency again considers all
of the health risks and other health
information considered in the first step,
including the incremental risk reduction
associated with standards more
stringent than the MACT standard or a
more stringent standard that the EPA
has determined is necessary to ensure
risk is acceptable. In the ample margin
of safety analysis, the Agency considers
additional factors, including costs and
economic impacts of controls,
technological feasibility, uncertainties,
and any other relevant factors.
Considering all of these factors, the
Agency will establish the standard at a
level that provides an ample margin of
safety to protect the public health, as
required by CAA section 112(f). 54 FR
38046, September 14, 1989.
B. What is this source category and how
does the current NESHAP regulate its
HAP emissions?
The ‘‘Pulp and Paper Production’’
source category includes any facility
engaged in the production of pulp and/
or paper. The EPA developed the
NESHAPs for the source category in two
phases. The first phase, 40 CFR part 63,
subpart S, regulates pulping and paper
production processes, and was
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originally promulgated in 1998. The
second phase, 40 CFR part 63, subpart
MM, regulates chemical recovery
combustion sources at kraft, soda,
sulfite, and stand-alone semichemical
pulp mills, and was originally
promulgated in 2001. Another separate
NESHAP, 40 CFR part 63, subpart
DDDDD, covers other combustion
sources located at pulp mills, such as
industrial boilers. This proposal focuses
exclusively on the RTR for subpart MM.
The EPA is not proposing any
amendments to Subpart DDDDD or
subpart S in this notice.
Subpart MM of 40 CFR part 63 was
promulgated on January 12, 2001 (66 FR
3180). As promulgated in 2001, the
subpart MM MACT standard applies to
major sources of HAP emissions from
chemical recovery combustion sources
at kraft, soda, sulfite, and stand-alone
semichemical pulp mills. The chemical
recovery combustion sources include
kraft and soda recovery furnaces, SDTs,
and lime kilns; kraft black liquor
oxidation (BLO) units; sulfite
combustion units; and semichemical
combustion units. Subpart S was
promulgated on April 15, 1998 (63 FR
18504), and underwent a RTR, with
final amendments to subpart S
promulgated on September 11, 2012 (77
FR 55698).
This proposal includes both a risk
assessment and a technology review of
the emission sources in 40 CFR part 63,
subpart MM, as well as a risk
assessment of the whole facility. The
whole facility risk assessment includes
emissions from all sources of HAP at the
facility, including sources covered by
other NESHAP (e.g., boilers covered
under 40 CFR part 63, subpart DDDDD;
pulp and paper production processes
covered under 40 CFR part 63, subpart
S; paper coating operations covered
under 40 CFR part 63, subpart JJJJ).
According to results of the EPA’s 2011
pulp and paper information collection
request (ICR), and updates based on
more recent information, there are a
total of 108 major sources in the United
States that conduct chemical recovery
combustion operations, including 97
kraft pulp mills, 1 soda pulp mill, 3
sulfite pulp mills, and 7 stand-alone
semichemical pulp mills.
Subpart MM of 40 CFR part 63
includes numerical emission limits for
recovery furnaces, SDTs, lime kilns, and
sulfite and semichemical combustion
units. The control systems used by most
mills to meet the subpart MM emission
limits are as follows:
• Recovery furnaces: ESPs, wet
scrubbers, and nondirect contact
evaporator (NDCE) furnace design with
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dry-bottom ESP, and dry particulate
matter (PM) return system.
• Smelt dissolving tanks: Wet
scrubbers, mist eliminators, and venting
to recovery furnace.
• Lime kilns: ESPs and wet scrubbers.
• Sulfite combustion units: Wet
scrubbers and mist eliminators.
• Semichemical combustion units:
Wet scrubbers, ESPs, and regenerative
thermal oxidizers (RTOs).
C. What data collection activities were
conducted to support this action?
In February 2011, the EPA issued an
ICR, pursuant to CAA section 114, to
United States pulp and paper
manufacturers to gather information
needed to conduct the regulatory
reviews required under CAA sections
112(d)(6) and (f)(2). The EPA divided
the ICR into three parts. Part I requested
available information regarding 40 CFR
part 63, subpart S process equipment,
control devices, pulp and paper
production, bleaching, and other aspects
of facility operations to support the
subpart S technology review and the
review of the Kraft Pulp Mills New
Source Performance Standards (NSPS)
under 40 CFR part 60, subpart BB. Part
II requested updated inventory data for
all pulp and paper emission sources to
support the residual risk assessment for
the pulp and paper sector (including 40
CFR part 63, subparts S and MM) and
to supplement the National Emissions
Inventory (NEI) for the source category
for purposes of detailed residual risk
modeling. Part III requested available
information on subpart MM chemical
recovery combustion equipment, control
devices, and other pertinent
information, to support the subpart MM
technology review and the subpart BB
NSPS review. The response rate for the
ICR was 100 percent.
D. What other relevant background
information and data are available?
In addition to ICR responses, the EPA
reviewed a number of other information
sources to determine if there have been
developments in practices, processes, or
control technologies by chemical
recovery combustion sources. These
include:
• Permit limits from permits
submitted with ICR responses and
collected from state agencies.
• Information on air pollution control
options in the pulp and paper industry
from the RACT/BACT/LAER
Clearinghouse (RBLC).
• Information on best available
techniques in the pulp and paper
industry from a 2015 European
Commission document, titled Best
Available Techniques (BAT) Reference
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Document for the Production of Pulp,
Paper and Board.
• Information on the most effective
ways to control emissions of PM2.5 and
PM2.5 precursors from sources in various
industries, including the pulp and paper
industry, from a 2006 State and
Territorial Air Pollution Program
Administrators/Association of Local Air
Pollution Control Officers (STAPPA/
ALAPCO) document, titled Controlling
Fine Particulate Matter under the Clean
Air Act: A Menu of Options.
• Stack test data submitted with ICR
responses.
• Emissions factors from technical
bulletins prepared by the National
Council for Air and Stream
Improvement, Inc. (NCASI), a major
source of environmental data affecting
the pulp and paper industry.
III. Analytical Procedures
In this section, we describe the
analyses performed to support the
proposed decisions for the RTR and
other issues addressed in this proposal.
A. How did we estimate post-MACT
risks posed by the source category?
The EPA conducted a risk assessment
that provides estimates of the MIR
posed by the HAP emissions from each
source in the source category, the
hazard index (HI) for chronic exposures
to HAPs with the potential to cause noncancer health effects, and the hazard
quotient (HQ) for acute exposures to
HAPs with the potential to cause noncancer health effects. The assessment
also provides estimates of the
distribution of cancer risks within the
exposed populations, cancer incidence,
and an evaluation of the potential for
adverse environmental effects. The
seven sections that follow this
paragraph describe how we estimated
emissions and conducted the risk
assessment. The docket for this
rulemaking contains the following
document which provides more
information on the risk assessment
inputs and models: Residual Risk
Assessment for Pulp Mill Combustion
Sources in Support of the December
2016 Risk and Technology Review
Proposed Rule. The methods used to
assess risks (as described in the seven
primary steps below) are consistent with
those peer-reviewed by a panel of the
EPA’s Science Advisory Board (SAB) in
2009 and described in their peer review
report issued in 2010; 2 they are also
consistent with the key
2 U.S. EPA SAB. Risk and Technology Review
(RTR) Risk Assessment Methodologies: For Review
by the EPA’s Science Advisory Board with Case
Studies—MACT I Petroleum Refining Sources and
Portland Cement Manufacturing, May 2010.
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recommendations contained in that
report.
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1. How did we estimate actual
emissions and identify the emissions
release characteristics?
As discussed in section II.C of this
preamble, we used data from Part II of
the Pulp and Paper Sector ICR as the
basis for the risk assessments for the
pulp and paper sector (including 40
CFR part 63, subparts S and MM). Part
II of the ICR, which concluded in June
2011, targeted facilities that are major
sources of HAP emissions and involved
an update of pre-populated NEI data
spreadsheets (or creation of new
datasets). The NEI is a database that
contains information about sources that
emit criteria air pollutants, their
precursors and HAPs. The NEI database
includes estimates of actual annual air
pollutant emissions from point and
volume sources; emission release
characteristic data such as emission
release height, temperature, diameter,
velocity, and flow rate; and locational
latitude/longitude coordinates. We
asked pulp and paper mills to refine (or
create new) inventories based on their
NEI datasets for purposes of detailed
residual risk modeling. Refinements
included providing additional details
for HAP emission sources, providing
more specific information on the
location and characteristics of emission
points (e.g., updating emission release
coordinates and parameters), and
adding or updating HAP emissions data
for each emission release point. We
compiled the updated datasets for each
individual mill into a pulp and paper
Part II emissions database to create the
whole facility and MACT source
category residual risk modeling files.
The actual annual emissions data in
the pulp and paper emissions database
include limited data from actual
emissions tests and, in most cases,
estimates of actual emissions (based on
emissions factors) provided by sources
surveyed in Part II of the ICR. We
received a comprehensive set of
emissions test data and emissions
estimates that enabled us to conduct
risk modeling of detectable HAP
emissions for all major source facilities
in the MACT source category.
We conducted two substantial quality
assurance (QA) efforts on the Part II data
in order to create the modeling files
needed for the 40 CFR part 63, subpart
S residual risk assessment, which
included: (1) QA of the updated
inventory spreadsheets submitted by
each mill prior to import into the
compiled database; and (2) QA and
standardization of the compiled
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database.3 We needed modeling files for
both the subpart S category and the
whole facility, so our QA efforts focused
on data for all emission sources at pulp
and paper facilities, including 40 CFR
part 63, subpart MM emission sources.
We reviewed the Part II datasets to
ensure that the major pulp and paper
processes and pollutants were included
and properly identified, to ensure that
emissions from the various processes
were allocated to the correct source
category, and to identify emissions and
other data anomalies. We also
standardized the various codes (e.g.,
source classification codes (SCCs),
pollutant codes), eliminated duplicate
records, and checked geographic
coordinates. We reviewed emissions
release parameters for data gaps and
errors, assigned the proper default
parameters where necessary, assigned
emission process groups to distinguish
between processes with related SCCs,
and ensured that fugitive release
dimensions were specified or given
default values where necessary.
We requested comments on the
inventory in the preamble to the
December 27, 2011, 40 CFR part 63,
subpart S proposal. We requested
further updates to the mill-specific HAP
emissions data used in the risk
modeling, if needed. In 2012, we
received revisions to inventories for 81
facilities following proposal of the
subpart S residual risk review.4
While most of the inventory revisions
that we received after the proposal made
additional refinements to emissions
levels and release point details for 40
CFR part 63, subpart S sources, some
inventory revisions also made
refinements to data for 40 CFR part 63,
subpart MM sources. We incorporated
revisions to all process types into the
inventory to remodel facility-wide risk
and perform the complete scope of
residual risk modeling for subpart MM
emissions sources. We checked the 81
individual revision files to ensure they
were incorporated into the main
database correctly, and then further
reviewed the entire database.
We began compiling an initial draft
residual risk modeling input file for use
in the 40 CFR part 63, subpart MM
residual risk review in September
3 These QA efforts are discussed in a November
11, 2011 memorandum in the docket, titled Inputs
to the Pulp and Paper Industry October 2011
Residual Risk Modeling.
4 Review of the inventory revisions performed
prior to promulgation of 40 CFR part 63, subpart S
is documented in a May 8, 2012, memorandum in
the subpart S docket (EPA–HQ–OAR–2007–0544),
titled Recommendations Concerning Residual Risk
Remodeling for the Pulp and Paper Industry.
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2014.5 We made updates to the mill list
to account for facilities that recently
closed or reopened, and to mill
equipment configurations for facilities
that recently upgraded equipment. We
reviewed the inventory to ensure that
each record contained a facility ID,
emission unit ID, process ID, and
emission release point ID. We crosswalked regulatory codes, SCCs, and
emission process groups to identify and
correct any inconsistencies that may
have been introduced with the
inventory updates.
In addition to retaining the emission
process groups used in the previous 40
CFR part 63, subpart S modeling effort,
we added new emission process groups
for 40 CFR part 63, subpart MM sources
where necessary. We compared the
subpart MM emission process groups
with the Part III ICR database to ensure
that we included all known recovery
furnaces and lime kilns in the inventory
for the residual risk modeling. In
addition, we reviewed the presence or
absence of BLO systems (i.e., because
BLO systems are only expected to be
present at mills with direct contact
evaporator (DCE) recovery furnaces).
Finally, we checked the mills to ensure
emission process groups included SDTs
and sulfite and semichemical recovery
equipment, as expected.
We reviewed the pollutant codes in
the inventory to ensure the codes and
descriptions matched the latest NEI
lookup table used by the EPA for risk
model input files. We performed
extensive QA of the pollutant codes
prior to the 40 CFR part 63, subpart S
risk modeling, so few updates were
required.
We speciated data for a number of
HAPs, including chromium, mercury,
radionuclides, polycyclic organic matter
(POM), and dioxins/furans to facilitate
risk modeling. We speciated chromium
emissions as hexavalent chromium
(chromium VI) and trivalent chromium
(chromium III).6 We speciated mercury
emissions as particulate divalent
mercury, gaseous divalent mercury, and
gaseous elemental mercury. We
speciated total POM emissions
differently for each emission unit type
5 For more information, see the September 30,
2014 memorandum in the docket, titled Preparation
of Residual Risk Modeling Input File for Subpart
MM. The September 2014 memorandum describes
the source of the inventory data, discusses quality
assurance of the 40 CFR part 63, subpart MM data,
provides actual versus allowable and acute risk
multipliers for subpart MM sources, and identifies
potential outliers and suspect data for further
review.
6 For more information on pollutant speciation,
see the September 30, 2014 memorandum in the
docket, titled Preparation of Residual Risk
Modeling Input File for Subpart MM.
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based on the most common POM
compounds emitted from that unit. We
speciated dioxin/furan emissions based
on published emissions data in the
EPA’s dioxin/furan inventory report 7
or, if no speciation profile was available,
recalculated the emissions using
published emissions factors.8 Where
needed, we added/replaced emissions
estimates that were omitted, outdated,
out-of-scope, or inconsistent with
changes to mill equipment
configurations.
We reviewed all records for
consistency with respect to the emission
release point to ensure each record was
characterized by one set of coordinates
(latitude and longitude) and one set of
stack or fugitive parameters. We
checked fugitive parameters to ensure
there were no blanks and that the values
provided were reasonable and
consistent with the required national
defaults or other criteria. We reviewed
emission points labeled as stacks to
ensure no fugitive parameters were
identified. We checked exit gas flow rate
values against the stack velocity
provided to ensure there were no
inconsistencies. We mapped the
emission point coordinates for each
facility to determine if they were
properly placed on the mill site. We also
added control information from the Part
III ICR database or mills’ title V permits
to the input file for 40 CFR part 63,
subpart MM sources.
The emissions inventory for 40 CFR
part 63, subpart MM sources identifies
emissions of the following HAP known
to be persistent and bio-accumulative in
the environment (PB–HAPs): Cadmium
compounds, lead compounds, mercury
compounds, POM, dioxins/furans, and
hexachlorobenzene. Risk-based
screening levels are available for Tier 1
screening for all of the above PB–HAPs,
with the exception of
hexachlorobenzene.
Consistent with the EPA’s standard
practice in conducting risk assessments
for source categories, we conducted a
two-step process to determine: (1)
Whether PB–HAPs are being emitted;
and (2) whether they are being released
above screening levels. If these releases
are significantly above the screening
7 U.S. Environmental Protection Agency. An
Inventory of Sources and Environmental Releases of
Dioxin-Like Compounds in the United States for the
Years 1987, 1995, and 2000. Publication No. EPA/
600/P–03/002F. Available at: https://www.epa.gov/
ncea/pdfs/dioxin/2006/dioxin.pdf. November 2006.
Tables 4–14, 4–25, and 5–13.
8 National Council for Air and Stream
Improvement (NCASI). Compilation of ‘Air Toxic’
and Total Hydrocarbon Emissions Data for Pulp
and Paper Mill Sources—A Second Update.
Technical Bulletin No. 973. February 2010. Table
9.9.
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levels and the EPA has detailed
information on the releases and the site,
a complete multipathway analysis of the
site is conducted to estimate pathway
risks for the source category.
We considered actual emissions of the
ecological HAPs emitted from the 40
CFR part 63, subpart MM source
category in the ecological HAP analysis.
In addition to the PB–HAPs emitted
from the subpart MM source category
(except hexachlorobenzene), we
considered hydrochloric acid (HCl) and
hydrogen fluoride (HF) for ecological
HAP modeling. Further information
about the multipathway analysis
performed for this category follows in
section III.B.4 of this preamble.
In 2015, we posted the initial draft
risk model input file on our Technology
Transfer Network for additional review
by interested parties. This review
resulted in the submittal of additional
mill-specific inventory and receptor
revisions. As part of the review, we
identified potential outliers and suspect
data for 40 CFR part 63, subpart MM
sources in the emission inventory and
notified facilities to provide an
opportunity to review and revise their
emissions data, if needed. A total of 40
mills reviewed their emissions data,
with 38 of those mills submitting
inventory revisions to the EPA.9
Inventory revisions primarily
included mill name changes; revisions
to HAP metal, POM, and dioxin/furan
inventory data; and requests for removal
of hexachlorocyclopentadiene (HCCPD)
data from inventories, particularly for
SDTs, since HCCPD is not expected
from pulp mill sources. Where
necessary, we speciated the revised
chromium, mercury, and POM data that
the mills provided, using the
approaches described above. As part of
the review, we identified risk modeling
receptors improperly located on mill
property for correction in the Human
Exposure Model (Community and
Sector HEM–3 version 1.1.0) input files
before we performed risk modeling for
40 CFR part 63, subpart MM.
After we incorporated the revisions
into the input file, we conducted an
additional review of the file, which
included the following:
• Identified non-40 CFR part 63,
subpart MM mills in the inventory and
removed them.
• Identified additional mill name
changes and incorporated them in the
inventory.
• Reviewed fugitive parameters for
missing data.
9 For further information, see the October 16,
2015 memorandum in the docket, titled Review of
Pulp Mill Inventory Revisions Received in 2015.
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• Identified missing speciated
mercury and chromium data and
restored the data to the inventory.
• Reviewed location data for mills
that submitted inventory revisions and
corrected coordinates, as needed.
• Identified records for emissions
points with zero emissions for a given
pollutant and removed those records
from the inventory.
• Conducted emission process group
checks, resulting in a revision to an
emission process group that reflects a
change in SCC, and removal of records
with an emission process group no
longer applicable (specifically a BLO
unit for a mill that no longer operates
any DCE recovery furnaces that require
a BLO unit).
• Checked mills to ensure they had
the expected 40 CFR part 63, subpart
MM equipment, comparing the number
of recovery furnaces, lime kilns, and
SDTs to Part III ICR data to ensure each
emission unit was represented in the
inventory.
• Reviewed each emission unit for
the presence of an emissions value for
key expected pollutants (e.g., HAP
metals, HCl, methanol, dioxins/furans,
POM) and added emissions estimates
for those pollutants where needed.10
• Replaced obviously errant
emissions data (particularly dioxins/
furans) with revised estimates
calculated based on ICR-reported
throughput and emissions factors.
• Rechecked IDs, SCCs, regulatory
codes, pollutant codes, duplicate
pollutants, and HCCPD deletions.
2. How did we estimate MACTallowable emissions?
The available emissions data in the
RTR emissions dataset include estimates
of the mass of HAPs emitted during the
specified annual time period. In some
cases, these ‘‘actual’’ emission levels are
lower than the emission levels required
to comply with the current MACT
standards. The emissions level allowed
to be emitted by the MACT standards is
referred to as the ‘‘MACT-allowable’’
emissions level. We discussed the use of
both MACT-allowable and actual
emissions in the final Coke Oven
Batteries RTR (70 FR 19998–19999,
April 15, 2005) and in the proposed and
final Hazardous Organic NESHAP RTRs
(71 FR 34428, June 14, 2006, and 71 FR
76609, December 21, 2006,
respectively). In those actions, we noted
that assessing the risks at the MACTallowable level is inherently reasonable
10 For further information, see the February 16,
2016 memorandum in the docket, titled Approach
for Populating Missing and Erroneous Emissions
Estimates for Key HAP in the Subpart MM Residual
Risk Modeling Inventory.
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since these risks reflect the maximum
level facilities could emit and still
comply with national emission
standards. We also explained that it is
reasonable to consider actual emissions,
where such data are available, in both
steps of the risk analysis, in accordance
with the Benzene NESHAP approach.
(54 FR 38044, September 14, 1989.) It is
reasonable to consider actual emissions
because sources typically seek to
perform better than required by
emissions standards to provide an
operational margin to accommodate the
variability in manufacturing processes
and control device performance.
Facilities’ actual emissions may also be
significantly lower than MACTallowable emissions for other reasons
such as state requirements, better
performance of control devices than
required by the MACT standards, or
reduced production.
We estimated actual emissions based
on the Part II emissions inventory and
subsequent site-specific inventory
revisions provided by mills. To estimate
emissions at the MACT-allowable level,
we developed a ratio of MACTallowable emissions to actual emissions
for each source type for the facilities in
the 40 CFR part 63, subpart MM source
category. We developed this ratio based
on the level of control required by the
subpart MM MACT standards compared
to the level of reported actual emissions
from stack test reports provided with
Part III survey responses. For example,
stack test data indicated that SDTs
achieve PM levels of 0.108 pounds per
ton (lb/ton) black liquor solids (BLS), on
average, while the PM emission limit for
existing SDTs is 0.20 lb/ton BLS, so we
estimated that MACT-allowable
emissions of HAP metals from SDTs
(where PM is used as a surrogate) could
be as much as 1.8 times higher, and the
ratio of MACT-allowable to actual
emissions used was 1.8:1 for SDTs.11
After developing these ratios for each
emission point type in this source
category, we next applied these ratios
on an emission unit basis to the Part II
actual emissions data to obtain risk
estimates based on MACT-allowable
emissions.
3. How did we conduct dispersion
modeling, determine inhalation
exposures and estimate individual and
population inhalation risks?
Both long-term and short-term
inhalation exposure concentrations and
health risks from the source category
11 For more information, see the September 30,
2014 memorandum in the docket, titled Preparation
of Residual Risk Modeling Input File for Subpart
MM.
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addressed in this proposal were
estimated using HEM–3. The HEM–3
performs three primary risk assessment
activities: (1) Conducting dispersion
modeling to estimate the concentrations
of HAPs in ambient air, (2) estimating
long-term and short-term inhalation
exposures to individuals residing within
50 kilometers (km) of the modeled
sources,12 and (3) estimating individual
and population-level inhalation risks
using the exposure estimates and
quantitative dose-response information.
The air dispersion model used by the
HEM–3 model (AERMOD) is one of the
EPA’s preferred models for assessing
pollutant concentrations from industrial
facilities.13 To perform the dispersion
modeling and to develop the
preliminary risk estimates, HEM–3
draws on three data libraries. The first
is a library of meteorological data,
which is used for dispersion
calculations. This library includes 1
year (2014) of hourly surface and upper
air observations for more than 800
meteorological stations, selected to
provide coverage of the United States
and Puerto Rico. A second library of
United States Census Bureau census
block 14 internal point locations and
populations provides the basis of
human exposure calculations (U.S.
Census, 2010). In addition, for each
census block, the census library
includes the elevation and controlling
hill height, which are also used in
dispersion calculations. A third library
of pollutant unit risk factors and other
health benchmarks is used to estimate
health risks. These risk factors and
health benchmarks are the latest values
recommended by the EPA for HAPs and
other toxic air pollutants. These values
are available at https://www.epa.gov/
fera/dose-response-assessmentassessing-health-risks-associatedexposure-hazardous-air-pollutants and
are discussed in more detail later in this
section.
In developing the risk assessment for
chronic exposures, we used the
estimated annual average ambient air
concentrations of each HAP emitted by
each source for which we have
emissions data in the source category.
The air concentrations at each nearby
census block centroid were used as a
surrogate for the chronic inhalation
exposure concentration for all the
12 This metric comes from the Benzene NESHAP.
See 54 FR 38046.
13 U.S. EPA. Revision to the Guideline on Air
Quality Models: Adoption of a Preferred General
Purpose (Flat and Complex Terrain) Dispersion
Model and Other Revisions (70 FR 68218,
November 9, 2005).
14 A census block is the smallest geographic area
for which census statistics are tabulated.
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people who reside in that census block.
We calculated the MIR for each facility
as the cancer risk associated with a
continuous lifetime (24 hours per day,
7 days per week, and 52 weeks per year
for a 70-year period) exposure to the
maximum concentration at the centroid
of inhabited census blocks. Individual
cancer risks were calculated by
multiplying the estimated lifetime
exposure to the ambient concentration
of each of the HAP (in micrograms per
cubic meter (mg/m3)) by its unit risk
estimate (URE). The URE is an upper
bound estimate of an individual’s
probability of contracting cancer over a
lifetime of exposure to a concentration
of 1 microgram of the pollutant per
cubic meter of air. For residual risk
assessments, we generally use URE
values from the EPA’s Integrated Risk
Information System (IRIS). For
carcinogenic pollutants without IRIS
values, we look to other reputable
sources of cancer dose-response values,
often using California EPA (CalEPA)
URE values, where available. In cases
where new, scientifically credible dose
response values have been developed in
a manner consistent with the EPA
guidelines and have undergone a peer
review process similar to that used by
the EPA, we may use such doseresponse values in place of, or in
addition to, other values, if appropriate.
The EPA estimated incremental
individual lifetime cancer risks
associated with emissions from the
facilities in the source category as the
sum of the risks for each of the
carcinogenic HAP (including those
classified as carcinogenic to humans,
likely to be carcinogenic to humans, and
suggestive evidence of carcinogenic
potential 15) emitted by the modeled
sources. Cancer incidence and the
distribution of individual cancer risks
for the population within 50 km of the
15 These classifications also coincide with the
terms ‘‘known carcinogen, probable carcinogen, and
possible carcinogen,’’ respectively, which are the
terms advocated in the EPA’s Guidelines for
Carcinogen Risk Assessment, published in 1986 (51
FR 33992, September 24, 1986). In August 2000, the
document Supplemental Guidance for Conducting
Health Risk Assessment of Chemical Mixtures
(EPA/630/R–00/002) was published as a
supplement to the 1986 document. Copies of both
documents can be obtained from https://
cfpub.epa.gov/ncea/risk/recordisplay.cfm?
deid=20533&CFID=70315376&
CFTOKEN=71597944. Summing the risks of these
individual compounds to obtain the cumulative
cancer risks is an approach that was recommended
by the EPA’s SAB in their 2002 peer review of the
EPA’s National Air Toxics Assessment (NATA)
titled, NATA—Evaluating the National-scale Air
Toxics Assessment 1996 Data—an SAB Advisory,
available at https://yosemite.epa.gov/ sab/
sabproduct.nsf/
214C6E915BB04E14852570CA007A682C/ $File/
ecadv02001.pdf.
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sources were also estimated for the
source category as part of this
assessment by summing individual
risks. A distance of 50 km is consistent
with both the analysis supporting the
1989 Benzene NESHAP (54 FR 38044,
September 14, 1989) and the limitations
of Gaussian dispersion models,
including AERMOD.
To assess the risk of non-cancer
health effects from chronic exposures,
we summed the HQ for each of the HAP
that affects a common target organ
system to obtain the HI for that target
organ system (or target organ-specific
HI, TOSHI). The HQ is the estimated
exposure divided by the chronic
reference value, which is a value
selected from one of several sources.
First, the chronic reference level can be
the EPA reference concentration (RfC)
(https://iaspub.epa.gov/sor_internet/
registry/termreg/searchandretrieve/
glossariesandkeywordlists/
search.do?details=&
vocabName=IRIS%20Glossary), defined
as ‘‘an estimate (with uncertainty
spanning perhaps an order of
magnitude) of a continuous inhalation
exposure to the human population
(including sensitive subgroups) that is
likely to be without an appreciable risk
of deleterious effects during a lifetime.’’
Alternatively, in cases where an RfC
from the EPA’s IRIS database is not
available or where the EPA determines
that using a value other than the RfC is
appropriate, the chronic reference level
can be a value from the following
prioritized sources: (1) The Agency for
Toxic Substances and Disease Registry
(ATSDR) Minimum Risk Level (https://
www.atsdr.cdc.gov/mrls/index.asp),
which is defined as ‘‘an estimate of
daily human exposure to a hazardous
substance that is likely to be without an
appreciable risk of adverse non-cancer
health effects (other than cancer) over a
specified duration of exposure’’; (2) the
CalEPA Chronic Reference Exposure
Level (REL) (https://oehha.ca.gov/air/
crnr/notice-adoption-air-toxics-hotspots-program-guidance-manualpreparation-health-risk-0), which is
defined as ‘‘the concentration level (that
is expressed in units of micrograms per
cubic meter (mg/m3) for inhalation
exposure and in a dose expressed in
units of milligram per kilogram-day
(mg/kg-day) for oral exposures), at or
below which no adverse health effects
are anticipated for a specified exposure
duration’’; or (3), as noted above, a
scientifically credible dose-response
value that has been developed in a
manner consistent with the EPA
guidelines and has undergone a peer
review process similar to that used by
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the EPA, in place of or in concert with
other values.
As mentioned above, in order to
characterize non-cancer chronic effects,
and in response to key
recommendations from the SAB, the
EPA selects dose-response values that
reflect the best available science for all
HAPs included in RTR risk
assessments.16 More specifically, for a
given HAP, the EPA examines the
availability of inhalation reference
values from the sources included in our
tiered approach (e.g., IRIS first, ATSDR
second, CalEPA third) and determines
which inhalation reference value
represents the best available science.
Thus, as new inhalation reference
values become available, the EPA will
typically evaluate them and determine
whether they should be given
preference over those currently being
used in RTR risk assessments.
The EPA also evaluated screening
estimates of acute exposures and risks
for each of the HAP (for which
appropriate acute dose-response values
are available) at the point of highest
potential off-site exposure for each
facility. To do this, the EPA estimated
the risks when both the peak (hourly)
emissions rate and worst-case
dispersion conditions occur. We also
assume that a person is located at the
point of highest impact during that same
time. In accordance with our mandate in
section 112 of the CAA, we use the
point of highest off-site exposure to
assess the potential risk to the
maximally exposed individual. The
acute HQ is the estimated acute
exposure divided by the acute doseresponse value. In each case, the EPA
calculated acute HQ values using best
available, short-term dose-response
values. These acute dose-response
values, which are described below,
include the acute REL, acute exposure
guideline levels (AEGL) and emergency
response planning guidelines (ERPG) for
1-hour exposure durations. As
discussed below, we used conservative
assumptions for emissions rates,
meteorology, and exposure location.
As described in the CalEPA’s Air
Toxics Hot Spots Program Risk
Assessment Guidelines, Part I, The
Determination of Acute Reference
Exposure Levels for Airborne Toxicants,
an acute REL value (https://
oehha.ca.gov/air/general-info/oehhaacute-8-hour-and-chronic-referenceexposure-level-rel-summary) is defined
as ‘‘the concentration level at or below
16 The SAB peer review of RTR Risk Assessment
Methodologies is available at https://
yosemite.epa.gov/sab/sabproduct.nsf/
4AB3966E263D943A8525771F00668381/$File/EPASAB-10-007-unsigned.pdf.
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which no adverse health effects are
anticipated for a specified exposure
duration.’’ Id. at page 2. Acute REL
values are based on the most sensitive,
relevant, adverse health effect reported
in the peer-reviewed medical and
toxicological literature. Acute REL
values are designed to protect the most
sensitive individuals in the population
through the inclusion of margins of
safety. Because margins of safety are
incorporated to address data gaps and
uncertainties, exceeding the REL does
not automatically indicate an adverse
health impact.
Acute exposure guideline level values
were derived in response to
recommendations from the National
Research Council (NRC). The National
Advisory Committee (NAC) for the
Development of Acute Exposure
Guideline Levels for Hazardous
Substances—usually referred to as the
AEGL Committee or the NAC/AEGL
committee developed AEGL values for
at least 273 of the 329 chemicals on the
AEGL priority chemical list. The last
meeting of the NAC/AEGL Committee
was in April 2010, and its charter
expired in October 2011. The NAC/
AEGL Committee ended in October
2011, but the AEGL program continues
to operate at the EPA and works with
the National Academies to publish final
AEGLs (https://www.epa.gov/aegl).
As described in Standing Operating
Procedures (SOP) for Developing Acute
Exposure Guideline Levels for
Hazardous Substances, ‘‘The NRC’s
previous name for acute exposure
levels—community emergency exposure
levels—was replaced by the term AEGL
to reflect the broad application of these
values to planning, response, and
prevention in the community, the
workplace, transportation, the military,
and the remediation of Superfund sites’’
(https://www.epa.gov/aegl/processdeveloping-acute-exposure-guidelinelevels-aegls) Id. at 2.17 The AEGL values
represent threshold exposure limits for
the general public and are applicable to
emergency exposures ranging from 10
minutes to 8 hours. ‘‘The primary
purpose of the AEGL program is to
develop guideline levels for once-in-alifetime, short-term exposures to
airborne concentrations of acutely toxic,
high-priority chemicals.’’ Id. at 21.
‘‘More specifically, the AEGL values
will be used for conducting various risk
assessments to aid in the development
of emergency preparedness and
prevention plans, as well as real-time
17 National Academy of Sciences (NAS), 2001.
Standing Operating Procedures for Developing
Acute Exposure Levels for Hazardous Chemicals,
page 2.
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emergency response actions, for
accidental chemical releases at fixed
facilities and from transport carriers.’’
Id. at 31.
The AEGL–1 value is then specifically
defined as ‘‘the airborne concentration
(expressed as ppm (parts per million) or
mg/m3 (milligrams per cubic meter)) of
a substance above which it is predicted
that the general population, including
susceptible individuals, could
experience notable discomfort,
irritation, or certain asymptomatic
nonsensory effects. However, the effects
are not disabling and are transient and
reversible upon cessation of exposure.’’
Id. at 3. The document also notes that,
‘‘Airborne concentrations below AEGL–
1 represent exposure levels that can
produce mild and progressively
increasing but transient and
nondisabling odor, taste, and sensory
irritation or certain asymptomatic,
nonsensory effects.’’ Id. Similarly, the
document defines AEGL–2 values as
‘‘the airborne concentration (expressed
as parts per million or milligrams per
cubic meter) of a substance above which
it is predicted that the general
population, including susceptible
individuals, could experience
irreversible or other serious, long-lasting
adverse health effects or an impaired
ability to escape.’’ Id.
Emergency response planning
guideline values are derived for use in
emergency response, as described in the
American Industrial Hygiene
Association’s Emergency Response
Planning (ERP) Committee document
titled, ERPGS Procedures and
Responsibilities (https://www.aiha.org/
get-involved/AIHAGuideline
Foundation/EmergencyResponse
PlanningGuidelines/Documents/
ERPG%20Committee%20Standard%20
Operating%20Procedures%20%20-%20
March%202014%20Revision%20%28
Updated%2010-2-2014%29.pdf), which
states that, ‘‘Emergency Response
Planning Guidelines were developed for
emergency planning and are intended as
health based guideline concentrations
for single exposures to chemicals.’’ 18 Id.
at 1. The ERPG–1 value is defined as
‘‘the maximum airborne concentration
below which nearly all individuals
could be exposed for up to 1 hour
without experiencing more than mild,
transient health effects or without
perceiving a clearly defined,
objectionable odor.’’ Id. at 2. Similarly,
the ERPG–2 value is defined as ‘‘the
maximum airborne concentration below
which nearly all individuals could be
18 ERP Committee Procedures and
Responsibilities. November 1, 2006. American
Industrial Hygiene Association.
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exposed for up to 1 hour without
experiencing or developing irreversible
or other serious adverse health effects or
symptoms that could impair an
individual’s ability to take protective
action.’’ Id. at 1.
As can be seen from the definitions
above, the AEGL and ERPG values
include the similarly-defined severity
levels 1 and 2. For many chemicals, a
severity level 1 value AEGL or ERPG has
not been developed because the types of
effects for these chemicals are not
consistent with the AEGL–1/ERPG–1
definitions; in these instances, we
compare higher severity level AEGL–2
or ERPG–2 values to our modeled
exposure levels to screen for potential
acute concerns. When AEGL–1/ERPG–1
values are available, they are used in
our acute risk assessments.
Acute REL values for 1-hour exposure
durations are typically lower than their
corresponding AEGL–1 and ERPG–1
values. Even though their definitions are
slightly different, AEGL–1 values are
often the same as the corresponding
ERPG–1 values, and AEGL–2 values are
often equal to ERPG–2 values.
Maximum HQ values from our acute
screening risk assessments typically
result when basing them on the acute
REL value for a particular pollutant. In
cases where our maximum acute HQ
value exceeds 1, we also report the HQ
value based on the next highest acute
dose-response value (usually the AEGL–
1 and/or the ERPG–1 value).
To develop screening estimates of
acute exposures in the absence of hourly
emissions data, generally we first
develop estimates of maximum hourly
emissions rates by multiplying the
average actual annual hourly emissions
rates by a default factor to cover
routinely variable emissions. We choose
the factor to use partially based on
process knowledge and engineering
judgment. The factor chosen also
reflects a Texas study of short-term
volatile organic compound (VOC)
emissions variability, which showed
that most peak emission events in a
heavily-industrialized four-county area
(Harris, Galveston, Chambers, and
Brazoria Counties, Texas) were less than
twice the annual average hourly
emissions rate. The highest peak
emissions event was 74 times the
annual average hourly emissions rate,
and the 99th percentile ratio of peak
hourly emissions rate to the annual
average hourly emissions rate was 9.19
19 Allen, et al., 2004. Variable Industrial VOC
Emissions and their impact on ozone formation in
the Houston Galveston Area. Texas Environmental
Research Consortium. https://www.researchgate.
net/publication/237593060_Variable_Industrial_
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Considering this analysis, to account for
more than 99 percent of the peak hourly
emissions, we apply a conservative
screening multiplication factor of 10 to
the average annual hourly emissions
rate in our acute exposure screening
assessments as our default approach.
However, we use a factor other than 10
if we have information that indicates
that a different factor is appropriate for
a particular source category. For this
source category, median peak-to-mean
multipliers ranging from 1.1 to 4.7 were
developed for 40 CFR part 63, subpart
MM emission process groups based on
the routine annual emissions data and
peak hourly emissions data obtained
from Part II survey data. A further
discussion of why these factors were
chosen can be found in the
memorandum, Preparation of Residual
Risk Modeling Input File for Subpart
MM, available in the docket for this
rulemaking.
As part of our acute risk assessment
process, for cases where acute HQ
values from the screening step were less
than or equal to 1 (even under the
conservative assumptions of the
screening analysis), acute impacts were
deemed negligible and no further
analysis was performed for these HAPs.
See the Residual Risk Assessment for
Pulp Mill Combustion Sources in
Support of the December 2016 Risk and
Technology Review Proposed Rule for
more details. Ideally, we would prefer to
have continuous measurements over
time to see how the emissions vary by
each hour over an entire year. Having a
frequency distribution of hourly
emissions rates over a year would allow
us to perform a probabilistic analysis to
estimate potential threshold
exceedances and their frequency of
occurrence. Such an evaluation could
include a more complete statistical
treatment of the key parameters and
elements adopted in this screening
analysis. Recognizing that this level of
data is rarely available, we instead rely
on the multiplier approach.
To better characterize the potential
health risks associated with estimated
acute exposures to HAPs, and in
response to a key recommendation from
the SAB’s peer review of the EPA’s RTR
risk assessment methodologies,20 we
generally examine a wider range of
available acute health metrics (e.g.,
RELs, AEGL) than we do for our chronic
risk assessments. This is in response to
VOC_Emissions_and_their_Impact_on_Ozone_
Formation_in_the_Houston_Galveston_Area.
20 The SAB peer review of RTR Risk Assessment
Methodologies is available at https://
yosemite.epa.gov/sab/sabproduct.nsf/
4AB3966E263D943A8525771F00668381/$File/EPASAB-10-007-unsigned.pdf.
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the SAB’s acknowledgement that there
are generally more data gaps and
inconsistencies in acute reference
values than there are in chronic
reference values. In some cases, when
Reference Value Arrays 21 for HAPs
have been developed, we consider
additional acute values (i.e.,
occupational and international values)
to provide a more complete risk
characterization.
4. How did we conduct the
multipathway exposure and risk
screening?
The EPA conducted a screening
analysis examining the potential for
significant human health risks due to
exposures via routes other than
inhalation (i.e., ingestion). We first
determined whether any sources in the
source category emitted PB–HAP. The
PB–HAP compounds or compound
classes are identified for the screening
from the EPA’s Air Toxics Risk
Assessment Library (available at https://
www2.epa.gov/fera/risk-assessmentand-modeling-air-toxics-riskassessment-reference-library).
For the 40 CFR part 63, subpart MM
source category, we identified emissions
of cadmium compounds, lead
compounds, mercury compounds, POM,
dioxins/furans, and hexachlorobenzene.
Because one or more of these PB–HAPs
are emitted by at least one facility in the
subpart MM source category, we
proceeded to the next step of the
evaluation. In this step, we determined
whether the facility-specific emissions
rates of the emitted PB–HAP were large
enough to create the potential for
significant non-inhalation human health
risks under reasonable worst-case
conditions. To facilitate this step, we
have developed emissions rate
screening levels for several PB–HAPs
using a hypothetical upper-end
screening exposure scenario developed
for use in conjunction with the EPA’s
Total Risk Integrated Methodology Fate,
Transport, and Ecological Exposure
(TRIM.FaTE) model. The PB–HAPs with
emissions rate screening levels are:
Lead, cadmium, dioxins/furans,
mercury compounds, and POM. We
conducted a sensitivity analysis on the
screening scenario to ensure that its key
design parameters would represent the
upper end of the range of possible
values, such that it would represent a
21 U.S. EPA. (2009) Chapter 2.9, Chemical
Specific Reference Values for Formaldehyde in
Graphical Arrays of Chemical-Specific Health Effect
Reference Values for Inhalation Exposures (Final
Report). U.S. Environmental Protection Agency,
Washington, DC, EPA/600/R–09/061, 2009, and
available online at https://cfpub.epa.gov/ncea/cfm/
recordisplay.cfm?deid=211003.
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conservative, but not impossible,
scenario. The facility-specific emissions
for each PB–HAP were compared to the
emission rate screening levels for these
PB–HAPs to assess the potential for
significant human health risks via noninhalation pathways. We call this
application of the TRIM.FaTE model the
Tier 1 TRIM-screen or Tier 1 screen.
For the purpose of developing
emission rate screening values for our
Tier 1 TRIM-screen, we derived
emission levels for these PB–HAPs
(other than lead compounds) at which
the maximum excess lifetime cancer
risk would be 1-in-1 million (i.e., for
dioxins/furans and POM) or, for HAPs
that cause non-cancer health effects (i.e.,
cadmium compounds and mercury
compounds), the maximum HQ would
be 1. If the emissions rate of any PB–
HAP included in the Tier 1 screen
exceeds the Tier 1 screening emissions
level for any facility, we conduct a
second screen, which we call the Tier 2
TRIM-screen or Tier 2 screen.
In the Tier 2 screen, the location of
each facility that exceeded the Tier 1
emission level is used to refine the
assumptions associated with the
environmental scenario while
maintaining the exposure scenario
assumptions. A key assumption that is
part of the Tier 1 screen is that a lake
is located near the facility; we confirm
the existence of lakes near the facility as
part of the Tier 2 screen. We then adjust
the risk-based Tier 1 screening value for
each PB–HAP for each facility based on
an understanding of how exposure
concentrations estimated for the
screening scenario change with
meteorology and environmental
assumptions. PB–HAP emissions that do
not exceed these new Tier 2 screening
levels are considered to pose no
unacceptable risks. If the PB–HAP
emissions for a facility exceed the Tier
2 screening levels and data are
available, we may decide to conduct a
more refined Tier 3 multipathway
assessment. There are several analyses
that can be included in a Tier 3 screen
depending upon the extent of
refinement warranted, including
validating that the lake is fishable and
considering plume-rise to estimate
emissions lost above the mixing layer. If
the Tier 3 screen is exceeded, the EPA
may further refine the assessment.
In evaluating the potential
multipathway risk from emissions of
lead compounds, rather than developing
a screening emissions rate for them, we
compared maximum estimated chronic
inhalation exposures with the level of
the current National Ambient Air
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Quality Standard (NAAQS) for lead.22
Values below the level of the primary
(health-based) lead NAAQS were
considered to have a low potential for
multipathway risk.
For further information on the
multipathway analysis approach, see
the document titled Residual Risk
Assessment for Pulp Mill Combustion
Sources in Support of the December
2016 Risk and Technology Review
Proposed Rule, which is available in the
docket for this action.
5. How did we conduct the
environmental risk screening
assessment?
a. Adverse Environmental Effect
The EPA conducts a screening
assessment to examine the potential for
adverse environmental effects as
required under section 112(f)(2)(A) of
the CAA. Section 112(a)(7) of the CAA
defines ‘‘adverse environmental effect’’
as ‘‘any significant and widespread
adverse effect, which may reasonably be
anticipated, to wildlife, aquatic life, or
other natural resources, including
adverse impacts on populations of
endangered or threatened species or
significant degradation of
environmental quality over broad
areas.’’
b. Environmental HAPs
The EPA focuses on seven HAPs,
which we refer to as ‘‘environmental
HAPs,’’ in its screening analysis: Five
PB–HAPs and two acid gases. The five
PB–HAPs are cadmium, dioxins/furans,
POM, mercury (both inorganic mercury
and methyl mercury) and lead
compounds. The two acid gases are HCl
and HF. The rationale for including
these seven HAPs in the environmental
risk screening analysis is presented
below.
The HAPs that persist and
bioaccumulate are of particular
environmental concern because they
accumulate in the soil, sediment, and
water. The PB–HAPs are taken up,
through sediment, soil, water, and/or
22 In doing so, the EPA notes that the legal
standard for a primary NAAQS—that a standard is
requisite to protect public health and provide an
adequate margin of safety (CAA section 109(b))—
differs from the CAA section 112(f) standard
(requiring among other things that the standard
provide an ‘‘ample margin of safety’’). However, the
primary lead NAAQS is a reasonable measure of
determining risk acceptability (i.e., the first step of
the Benzene NESHAP analysis) since it is designed
to protect the most susceptible group in the human
population—children, including children living
near major lead emitting sources. 73 FR 67002/3; 73
FR 67000/3; 73 FR 67005/1. In addition, applying
the level of the primary lead NAAQS at the risk
acceptability step is conservative, since that
primary lead NAAQS reflects an adequate margin
of safety.
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ingestion of other organisms, by plants
or animals (e.g., small fish) at the
bottom of the food chain. As larger and
larger predators consume these
organisms, concentrations of the PB–
HAPs in the animal tissues increases as
does the potential for adverse effects.
The five PB–HAPs we evaluate as part
of our screening analysis account for
99.8 percent of all PB–HAP emissions
nationally from stationary sources (on a
mass basis from the 2005 EPA NEI).
In addition to accounting for almost
all of the mass of PB–HAPs emitted, we
note that the TRIM.FaTE model that we
use to evaluate multipathway risk
allows us to estimate concentrations of
cadmium compounds, dioxins/furans,
POM, and mercury in soil, sediment and
water. For lead compounds, we
currently do not have the ability to
calculate these concentrations using the
TRIM.FaTE model. Therefore, to
evaluate the potential for adverse
environmental effects from lead
compounds, we compare the estimated
exposures from the source category
emissions of lead with the level of the
secondary NAAQS for lead.23 We
consider values below the level of the
secondary lead NAAQS to be unlikely to
cause adverse environmental effects.
Due to their well-documented
potential to cause direct damage to
terrestrial plants, we include two acid
gases, HCl and HF, in the environmental
screening analysis. According to the
2005 NEI, HCl and HF account for about
99 percent (on a mass basis) of the total
acid gas HAPs emitted by stationary
sources in the United States. In addition
to the potential to cause direct damage
to plants, high concentrations of HF in
the air have been linked to fluorosis in
livestock. Air concentrations of these
HAPs are already calculated as part of
the human multipathway exposure and
risk screening analysis using the HEM3–
AERMOD air dispersion model, and we
are able to use the air dispersion
modeling results to estimate the
potential for an adverse environmental
effect.
The EPA acknowledges that other
HAPs beyond the seven HAPs discussed
above may have the potential to cause
adverse environmental effects.
Therefore, the EPA may include other
relevant HAPs in its environmental risk
screening in the future, as modeling
23 The Secondary Lead NAAQS is a reasonable
measure of determining whether there is an adverse
environmental effect since it was established
considering ‘‘effects on soils, water, crops,
vegetation, man-made materials, animals, wildlife,
weather, visibility and climate, damage to and
deterioration of property, and hazards to
transportation, as well as effects on economic
values and on personal comfort and well-being.’’
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science and resources allow. The EPA
invites comment on the extent to which
other HAPs emitted by the source
category may cause adverse
environmental effects. Such information
should include references to peerreviewed ecological effects benchmarks
that are of sufficient quality for making
regulatory decisions, as well as
information on the presence of
organisms located near facilities within
the source category that such
benchmarks indicate could be adversely
affected.
c. Ecological Assessment Endpoints and
Benchmarks for PB–HAP
An important consideration in the
development of the EPA’s screening
methodology is the selection of
ecological assessment endpoints and
benchmarks. Ecological assessment
endpoints are defined by the ecological
entity (e.g., aquatic communities
including fish and plankton) and its
attributes (e.g., frequency of mortality).
Ecological assessment endpoints can be
established for organisms, populations,
communities or assemblages, and
ecosystems.
For PB–HAPs (other than lead
compounds), we evaluated the
following community-level ecological
assessment endpoints to screen for
organisms directly exposed to HAPs in
soils, sediment, and water:
• Local terrestrial communities (i.e.,
soil invertebrates, plants) and
populations of small birds and
mammals that consume soil
invertebrates exposed to PB–HAPs in
the surface soil;
• Local benthic (i.e., bottom sediment
dwelling insects, amphipods, isopods,
and crayfish) communities exposed to
PB–HAPs in sediment in nearby water
bodies; and
• Local aquatic (water-column)
communities (including fish and
plankton) exposed to PB–HAP in nearby
surface waters.
For PB–HAPs (other than lead
compounds), we also evaluated the
following population-level ecological
assessment endpoint to screen for
indirect HAP exposures of top
consumers via the bioaccumulation of
HAPs in food chains:
• Piscivorous (i.e., fish-eating)
wildlife consuming PB–HAPcontaminated fish from nearby water
bodies.
For cadmium compounds, dioxins/
furans, POM, and mercury, we
identified the available ecological
benchmarks for each assessment
endpoint. An ecological benchmark
represents a concentration of HAPs (e.g.,
0.77 mg of HAP per liter of water) that
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has been linked to a particular
environmental effect level through
scientific study. For PB–HAPs we
identified, where possible, ecological
benchmarks at the following effect
levels:
• Probable effect levels (PEL): Level
above which adverse effects are
expected to occur frequently;
• Lowest-observed-adverse-effect
level (LOAEL): The lowest exposure
level tested at which there are
biologically significant increases in
frequency or severity of adverse effects;
and
• No-observed-adverse-effect levels
(NOAEL): The highest exposure level
tested at which there are no biologically
significant increases in the frequency or
severity of adverse effect.
We established a hierarchy of
preferred benchmark sources to allow
selection of benchmarks for each
environmental HAP at each ecological
assessment endpoint. In general, the
EPA sources that are used at a
programmatic level (e.g., Office of
Water, Superfund Program) were used
in the analysis, if available. If
unavailable, the EPA benchmarks used
in regional programs (e.g., Superfund)
were used. If benchmarks were not
available at a programmatic or regional
level, we used benchmarks developed
by other federal agencies (e.g., National
Oceanic and Atmospheric
Administration (NOAA)) or state
agencies.
Benchmarks for all effect levels are
not available for all PB–HAPs and
assessment endpoints. In cases where
multiple effect levels were available for
a particular PB–HAP and assessment
endpoint, we use all of the available
effect levels to help us to determine
whether ecological risks exist and, if so,
whether the risks could be considered
significant and widespread.
d. Ecological Assessment Endpoints and
Benchmarks for Acid Gases
The environmental screening analysis
also evaluated potential damage and
reduced productivity of plants due to
direct exposure to acid gases in the air.
For acid gases, we evaluated the
following ecological assessment
endpoint:
• Local terrestrial plant communities
with foliage exposed to acidic gaseous
HAPs in the air.
The selection of ecological
benchmarks for the effects of acid gases
on plants followed the same approach
as for PB–HAPs (i.e., we examine all of
the available chronic benchmarks). For
HCl, the EPA identified chronic
benchmark concentrations. We note that
the benchmark for chronic HCl exposure
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to plants is greater than the reference
concentration for chronic inhalation
exposure for human health. This means
that where the EPA includes regulatory
requirements to prevent an exceedance
of the reference concentration for
human health, additional analyses for
adverse environmental effects of HCl
would not be necessary.
For HF, the EPA identified chronic
benchmark concentrations for plants
and evaluated chronic exposures to
plants in the screening analysis. High
concentrations of HF in the air have also
been linked to fluorosis in livestock.
However, the HF concentrations at
which fluorosis in livestock occur are
higher than those at which plant
damage begins. Therefore, the
benchmarks for plants are protective of
both plants and livestock.
srobinson on DSK5SPTVN1PROD with PROPOSALS3
e. Screening Methodology
For the environmental risk screening
analysis, the EPA first looked at whether
any facilities in the 40 CFR part 63,
subpart MM source category emitted
any of the seven environmental HAPs.
Because we found that one or more of
the seven environmental HAPs
evaluated are emitted by at least one
facility in the source category, we
proceeded to the second step of the
evaluation.
f. PB–HAP Methodology
For cadmium, mercury, POM, and
dioxins/furans, the environmental
screening analysis consists of two tiers,
while lead compounds are analyzed
differently as discussed earlier. In the
first tier, we determined whether the
maximum facility-specific emission
rates of each of the emitted
environmental HAPs were large enough
to create the potential for adverse
environmental effects under reasonable
worst-case environmental conditions.
These are the same environmental
conditions used in the human
multipathway exposure and risk
screening analysis.
To facilitate this step, TRIM.FaTE was
run for each PB–HAP under
hypothetical environmental conditions
designed to provide conservatively high
HAP concentrations. The model was set
to maximize runoff from terrestrial
parcels into the modeled lake, which in
turn, maximized the chemical
concentrations in the water, the
sediments, and the fish. The resulting
media concentrations were then used to
back-calculate a screening level
emission rate that corresponded to the
relevant exposure benchmark
concentration value for each assessment
endpoint. To assess emissions from a
facility, the reported emission rate for
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each PB–HAP was compared to the
screening level emission rate for that
PB–HAP for each assessment endpoint.
If emissions from a facility do not
exceed the Tier 1 screening level, the
facility ‘‘passes’’ the screen, and,
therefore, is not evaluated further under
the screening approach. If emissions
from a facility exceed the Tier 1
screening level, we evaluate the facility
further in Tier 2.
In Tier 2 of the environmental
screening analysis, the emission rate
screening levels are adjusted to account
for local meteorology and the actual
location of lakes in the vicinity of
facilities that did not pass the Tier 1
screen. The modeling domain for each
facility in the Tier 2 analysis consists of
8 octants. Each octant contains 5
modeled soil concentrations at various
distances from the facility (5 soil
concentrations × 8 octants = total of 40
soil concentrations per facility) and 1
lake with modeled concentrations for
water, sediment and fish tissue. In the
Tier 2 environmental risk screening
analysis, the 40 soil concentration
points are averaged to obtain an average
soil concentration for each facility for
each PB–HAP. For the water, sediment,
and fish tissue concentrations, the
highest value for each facility for each
pollutant is used. If emission
concentrations from a facility do not
exceed the Tier 2 screening level, the
facility passes the screen, and typically
is not evaluated further. If emissions
from a facility exceed the Tier 2
screening level, the facility does not
pass the screen and, therefore, may have
the potential to cause adverse
environmental effects. Such facilities
are evaluated further to investigate
factors such as the magnitude and
characteristics of the area of exceedance.
g. Acid Gas Methodology
The environmental screening analysis
evaluates the potential phytotoxicity
and reduced productivity of plants due
to chronic exposure to acid gases. The
environmental risk screening
methodology for acid gases is a singletier screen that compares the average
off-site ambient air concentration over
the modeling domain to ecological
benchmarks for each of the acid gases.
Because air concentrations are
compared directly to the ecological
benchmarks, emission-based screening
levels are not calculated for acid gases
as they are in the ecological risk
screening methodology for PB–HAPs.
For purposes of ecological risk
screening, the EPA identifies a potential
for adverse environmental effects to
plant communities from exposure to
acid gases when the average
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concentration of the HAP around a
facility exceeds the LOAEL ecological
benchmark. In such cases, we further
investigate factors such as the
magnitude and characteristics of the
area of exceedance (e.g., land use of
exceedance area, size of exceedance
area) to determine if there is an adverse
environmental effect. For further
information on the environmental
screening analysis approach, see the
Residual Risk Assessment for Pulp Mill
Combustion Sources in Support of the
December 2016 Risk and Technology
Review Proposed Rule, which is
available in the docket for this action.
6. How did we conduct facility-wide
assessments?
To put the source category risks in
context, we typically examine the risks
from the entire ‘‘facility,’’ where the
facility includes all HAP-emitting
operations within a contiguous area and
under common control. In other words,
we examine the HAP emissions not only
from the source category emission
points of interest, but also emissions of
HAPs from all other emission sources at
the facility for which we have data.
There are currently 108 major sources
subject to the 40 CFR part 63, subpart
MM source category which includes
chemical recovery combustion sources
(e.g., recovery furnace, SDT, lime kiln).
Nearly all major sources also have
boilers on site. These facilities engage in
chemical or mechanical pulping,
papermaking, paper coating, landfills,
petroleum storage and transfer, and
other operations. Therefore, where data
were available, we performed a facilitywide risk assessment for these major
sources as part of this action. For this
source category, we conducted the
facility-wide assessment using the data
from Part II of the Pulp and Paper Sector
ICR.
We analyzed risks due to the
inhalation of HAPs that are emitted
‘‘facility-wide’’ for the populations
residing within 50 km of each facility,
consistent with the methods used for
the source category analysis described
above. For these facility-wide risk
analyses, the modeled source category
risks were compared to the facility-wide
risks to determine the portion of facilitywide risks that could be attributed to the
source category addressed in this
proposal. We specifically examined the
facility that was associated with the
highest estimate of risk and determined
the percentage of that risk attributable to
the source category of interest. The
document titled Residual Risk
Assessment for Pulp Mill Combustion
Sources in Support of the December
2016 Risk and Technology Review
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Proposed Rule, available in the docket
for this action, provides the
methodology and results of the facilitywide analyses, including all facilitywide risks and the percentage of source
category contribution to facility-wide
risks.
7. How did we consider uncertainties in
risk assessment?
In the Benzene NESHAP, the Agency
concluded that risk estimation
uncertainty should be considered in our
decision-making under the ample
margin of safety framework. Uncertainty
and the potential for bias are inherent in
all risk assessments, including those
performed for this proposal. Although
uncertainty exists, we believe that our
approach, which used conservative
tools and assumptions, ensures that our
decisions are health-protective and
environmentally protective. A brief
discussion of the uncertainties in the
RTR emissions dataset, dispersion
modeling, inhalation exposure
estimates, and dose-response
relationships follows below. Where
relevant to the estimated exposures, the
lack of short-term dose-response values
at different levels of severity should be
factored into the risk characterization as
potential uncertainties. A more
thorough discussion of these
uncertainties is included in the
document titled Residual Risk
Assessment for Pulp Mill Combustion
Sources in Support of the December
2016 Risk and Technology Review
Proposed Rule, which is available in the
docket for this action.
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a. Uncertainties in the RTR Emissions
Dataset
Although the development of the RTR
emissions dataset involved quality
assurance/quality control processes,
various uncertainties exist. Thus, the
accuracy of emissions values will vary
depending on the source of the data, the
degree to which data are incomplete or
missing, the degree to which
assumptions made to complete the
datasets are accurate, errors in emission
estimates, and other factors. The
emission estimates considered in this
analysis generally are annual totals for
certain years, and they do not reflect
short-term fluctuations during the
course of a year or variations from year
to year. The estimates of peak hourly
emission rates for the acute effects
screening assessment were based on an
emission adjustment factor applied to
the average annual hourly emission
rates, which are intended to account for
emission fluctuations due to normal
facility operations.
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b. Uncertainties in Dispersion Modeling
We recognize there is uncertainty in
ambient concentration estimates
associated with any model, including
the EPA’s recommended regulatory
dispersion model, AERMOD. In using a
model to estimate ambient pollutant
concentrations, the user chooses certain
options to apply. For RTR assessments,
we select some model options that have
the potential to overestimate ambient air
concentrations (e.g., not including
plume depletion or pollutant
transformation). We select other model
options that have the potential to
underestimate ambient impacts (e.g., not
including building downwash). Other
options that we select have the potential
to either under- or overestimate ambient
levels (e.g., meteorology and receptor
locations). On balance, considering the
directional nature of the uncertainties
commonly present in ambient
concentrations estimated by dispersion
models, the approach we apply in the
RTR assessments should yield unbiased
estimates of ambient HAP
concentrations.
c. Uncertainties in Inhalation Exposure
The EPA did not include the effects
of human mobility on exposures in the
assessment. Specifically, short-term
mobility and long-term mobility
between census blocks in the modeling
domain were not considered.24 The
approach of not considering short or
long-term population mobility does not
bias the estimate of the theoretical MIR
(by definition), nor does it affect the
estimate of cancer incidence because the
total population number remains the
same. It does, however, affect the shape
of the distribution of individual risks
across the affected population, shifting
it toward higher estimated individual
risks at the upper end and reducing the
number of people estimated to be at
lower risks, thereby increasing the
estimated number of people at specific
high risk levels (e.g., 1-in-10 thousand
or 100-in-1 million).
In addition, the assessment predicted
the chronic exposures at the centroid of
each populated census block as
surrogates for the exposure
concentrations for all people living in
that block. Using the census block
centroid to predict chronic exposures
tends to over-predict exposures for
people in the census block who live
farther from the facility and underpredict exposures for people in the
24 Short-term mobility is movement from one
micro-environment to another over the course of
hours or days. Long-term mobility is movement
from one residence to another over the course of a
lifetime.
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census block who live closer to the
facility. Thus, using the census block
centroid to predict chronic exposures
may lead to a potential understatement
or overstatement of the true maximum
impact, but is an unbiased estimate of
average risk and incidence. We reduce
this uncertainty by analyzing large
census blocks near facilities using aerial
imagery and adjusting the location of
the block centroid to better represent the
population in the block, as well as
adding additional receptor locations
where the block population is not well
represented by a single location.
The assessment evaluates the cancer
inhalation risks associated with
pollutant exposures over a 70-year
period, which is the assumed lifetime of
an individual. In reality, both the length
of time that modeled emission sources
at facilities actually operate (i.e., more
or less than 70 years) and the domestic
growth or decline of the modeled
industry (i.e., the increase or decrease in
the number or size of domestic
facilities) will influence the future risks
posed by a given source or source
category. Depending on the
characteristics of the industry, these
factors will, in most cases, result in an
overestimate both in individual risk
levels and in the total estimated number
of cancer cases. However, in the
unlikely scenario where a facility
maintains, or even increases, its
emissions levels over a period of more
than 70 years, residents live beyond 70
years at the same location, and the
residents spend most of their days at
that location, then the cancer inhalation
risks could potentially be
underestimated. However, annual
cancer incidence estimates from
exposures to emissions from these
sources would not be affected by the
length of time an emissions source
operates.
The exposure estimates used in these
analyses assume chronic exposures to
ambient (outdoor) levels of pollutants.
Because most people spend the majority
of their time indoors, actual exposures
may not be as high, depending on the
characteristics of the pollutants
modeled. For many of the HAPs, indoor
levels are roughly equivalent to ambient
levels, but for very reactive pollutants or
larger particles, indoor levels are
typically lower. This factor has the
potential to result in an overestimate of
25 to 30 percent of exposures.25
In addition to the uncertainties
highlighted above, there are several
factors specific to the acute exposure
25 U.S. EPA. National-Scale Air Toxics
Assessment for 1996. (EPA 453/R–01–003; January
2001; page 85.)
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assessment that the EPA conducts as
part of the risk review under section 112
of the CAA that should be highlighted.
The accuracy of an acute inhalation
exposure assessment depends on the
simultaneous occurrence of
independent factors that may vary
greatly, such as hourly emissions rates,
meteorology, and the present of humans
at the location of the maximum
concentration. In the acute screening
assessment that we conduct under the
RTR program, we assume that peak
emissions from the source category and
worst-case meteorological conditions
co-occur, thus, resulting in maximum
ambient concentrations. These two
events are unlikely to occur at the same
time, making these assumptions
conservative. We then include the
additional assumption that a person is
located at this point during this same
time period. For this source category,
these assumptions would tend to be
worst-case actual exposures, as it is
unlikely that a person would be located
at the point of maximum exposure
during the time when peak emissions
and worst-case meteorological
conditions occur simultaneously.
d. Uncertainties in Dose-Response
Relationships
There are uncertainties inherent in
the development of the dose-response
values used in our risk assessments for
cancer effects from chronic exposures
and non-cancer effects from both
chronic and acute exposures. Some
uncertainties may be considered
quantitatively, and others generally are
expressed in qualitative terms. We note
as a preface to this discussion a point on
dose-response uncertainty that is
brought out in the EPA’s 2005 Cancer
Guidelines; namely, that ‘‘the primary
goal of EPA actions is protection of
human health; accordingly, as an
Agency policy, risk assessment
procedures, including default options
that are used in the absence of scientific
data to the contrary, should be health
protective’’ (EPA’s 2005 Cancer
Guidelines, pages 1–7). This is the
approach followed here as summarized
in the next several paragraphs. A
complete detailed discussion of
uncertainties and variability in doseresponse relationships is given in the
Residual Risk Assessment for Pulp Mill
Combustion Sources in Support of the
December 2016 Risk and Technology
Review Proposed Rule, which is
available in the docket for this action.
Cancer URE values used in our risk
assessments are those that have been
developed to generally provide an upper
bound estimate of risk. That is, they
represent a ‘‘plausible upper limit to the
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true value of a quantity’’ (although this
is usually not a true statistical
confidence limit).26 In some
circumstances, the true risk could be as
low as zero; however, in other
circumstances the risk could be
greater.27 When developing an upper
bound estimate of risk and to provide
risk values that do not underestimate
risk, health-protective default
approaches are generally used. To err on
the side of ensuring adequate health
protection, the EPA typically uses the
upper bound estimates rather than
lower bound or central tendency
estimates in our risk assessments, an
approach that may have limitations for
other uses (e.g., priority-setting or
expected benefits analysis).
Chronic non-cancer RfC and reference
dose (RfD) values represent chronic
exposure levels that are intended to be
health-protective levels. Specifically,
these values provide an estimate (with
uncertainty spanning perhaps an order
of magnitude) of a continuous
inhalation exposure (i.e., the RfC) or a
daily oral exposure (i.e., the RfD) to the
human population (including sensitive
subgroups) that is likely to be without
an appreciable risk of deleterious effects
during a lifetime. To derive values that
are intended to be ‘‘without appreciable
risk,’’ the methodology relies upon an
uncertainty factor (UF) approach (U.S.
EPA, 1993 and 1994) which considers
uncertainty, variability and gaps in the
available data. The UFs are applied to
derive reference values that are
intended to protect against appreciable
risk of deleterious effects. The UFs are
commonly default values,28 e.g., factors
26 IRIS glossary (https://iaspub.epa.gov/sor_
internet/registry/termreg/searchandretrieve/
glossariesandkeywordlists/search.do?details=&
vocabName=IRIS%20Glossary).
27 An exception to this is the URE for benzene,
which is considered to cover a range of values, each
end of which is considered to be equally plausible,
and which is based on maximum likelihood
estimates.
28 According to the NRC report, Science and
Judgment in Risk Assessment (NRC, 1994)
‘‘[Default] options are generic approaches, based on
general scientific knowledge and policy judgment,
that are applied to various elements of the risk
assessment process when the correct scientific
model is unknown or uncertain.’’ The 1983 NRC
report, Risk Assessment in the Federal Government:
Managing the Process, defined default option as
‘‘the option chosen on the basis of risk assessment
policy that appears to be the best choice in the
absence of data to the contrary’’ (NRC, 1983a, p. 63).
Therefore, default options are not rules that bind
the Agency; rather, the Agency may depart from
them in evaluating the risks posed by a specific
substance when it believes this to be appropriate.
In keeping with the EPA’s goal of protecting public
health and the environment, default assumptions
are used to ensure that risk to chemicals is not
underestimated (although defaults are not intended
to overtly overestimate risk). See U.S. EPA, An
Examination of EPA Risk Assessment Principles
and Practices, EPA/100/B–04/001, 2004 available
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of 10 or 3, used in the absence of
compound-specific data; where data are
available, UFs may also be developed
using compound-specific information.
When data are limited, more
assumptions are needed and more UFs
are used. Thus, there may be a greater
tendency to overestimate risk in the
sense that further study might support
development of reference values that are
higher (i.e., less potent) because fewer
default assumptions are needed.
However, for some pollutants, it is
possible that risks may be
underestimated.
While collectively termed ‘‘UF,’’ these
factors account for a number of different
quantitative considerations when using
observed animal (usually rodent) or
human toxicity data in the development
of the RfC. The UFs are intended to
account for: (1) variation in
susceptibility among the members of the
human population (i.e., inter-individual
variability); (2) uncertainty in
extrapolating from experimental animal
data to humans (i.e., interspecies
differences); (3) uncertainty in
extrapolating from data obtained in a
study with less-than-lifetime exposure
(i.e., extrapolating from sub-chronic to
chronic exposure); (4) uncertainty in
extrapolating the observed data to
obtain an estimate of the exposure
associated with no adverse effects; and
(5) uncertainty when the database is
incomplete or there are problems with
the applicability of available studies.
Many of the UFs used to account for
variability and uncertainty in the
development of acute reference values
are quite similar to those developed for
chronic durations, but they more often
use individual UF values that may be
less than 10. The UFs are applied based
on chemical-specific or health effectspecific information (e.g., simple
irritation effects do not vary appreciably
between human individuals, hence a
value of 3 is typically used), or based on
the purpose for the reference value (see
the following paragraph). The UFs
applied in acute reference value
derivation include: (1) Heterogeneity
among humans; (2) uncertainty in
extrapolating from animals to humans;
(3) uncertainty in lowest observed
adverse effect (exposure) level to no
observed adverse effect (exposure) level
adjustments; and (4) uncertainty in
accounting for an incomplete database
on toxic effects of potential concern.
Additional adjustments are often
applied to account for uncertainty in
at: https://training.fws.gov/resources/courseresources/pesticides/Risk%20Assessment/
Risk%20Assessment%20Principles%20
and%20Practices.pdf.
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extrapolation from observations at one
exposure duration (e.g., 4 hours) to
derive an acute reference value at
another exposure duration (e.g., 1 hour).
Not all acute reference values are
developed for the same purpose, and
care must be taken when interpreting
the results of an acute assessment of
human health effects relative to the
reference value or values being
exceeded. Where relevant to the
estimated exposures, the lack of shortterm dose-response values at different
levels of severity should be factored into
the risk characterization as potential
uncertainties.
For a group of compounds that are
unspeciated (e.g., glycol ethers), we
conservatively use the most protective
reference value of an individual
compound in that group to estimate
risk. Similarly, for an individual
compound in a group (e.g., ethylene
glycol diethyl ether) that does not have
a specified reference value, we also
apply the most protective reference
value from the other compounds in the
group to estimate risk.
e. Uncertainties in the Multipathway
Assessment
For each source category, we
generally rely on site-specific levels of
PB–HAP emissions to determine
whether a refined assessment of the
impacts from multipathway exposures
is necessary. This determination is
based on the results of a three-tiered
screening analysis that relies on the
outputs from models that estimate
environmental pollutant concentrations
and human exposures for four PB–
HAPs. Two important types of
uncertainty associated with the use of
these models in RTR risk assessments
and inherent to any assessment that
relies on environmental modeling are
model uncertainty and input
uncertainty.29
Model uncertainty concerns whether
the selected models are appropriate for
the assessment being conducted and
whether they adequately represent the
actual processes that might occur for
that situation. An example of model
uncertainty is the question of whether
the model adequately describes the
movement of a pollutant through the
soil. This type of uncertainty is difficult
to quantify. However, based on feedback
received from previous EPA SAB
reviews and other reviews, we are
29 In the context of this discussion, the term
‘‘uncertainty’’ as it pertains to exposure and risk
encompasses both variability in the range of
expected inputs and screening results due to
existing spatial, temporal, and other factors, as well
as uncertainty in being able to accurately estimate
the true result.
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confident that the models used in the
screen are appropriate and state-of-theart for the multipathway risk
assessments conducted in support of
RTR.
Input uncertainty is concerned with
how accurately the models have been
configured and parameterized for the
assessment at hand. For Tier 1 of the
multipathway screen, we configured the
models to avoid underestimating
exposure and risk. This was
accomplished by selecting upper-end
values from nationally-representative
datasets for the more influential
parameters in the environmental model,
including selection and spatial
configuration of the area of interest, lake
location and size, meteorology, surface
water and soil characteristics, and
structure of the aquatic food web. We
also assume an ingestion exposure
scenario and values for human exposure
factors that represent reasonable
maximum exposures.
In Tier 2 of the multipathway
assessment, we refine the model inputs
to account for meteorological patterns in
the vicinity of the facility versus using
upper-end national values, and we
identify the actual location of lakes near
the facility rather than the default lake
location that we apply in Tier 1. By
refining the screening approach in Tier
2 to account for local geographical and
meteorological data, we decrease the
likelihood that concentrations in
environmental media are overestimated,
thereby increasing the usefulness of the
screen. The assumptions and the
associated uncertainties regarding the
selected ingestion exposure scenario are
the same for Tier 1 and Tier 2.
For both Tiers 1 and 2 of the
multipathway assessment, our approach
to addressing model input uncertainty is
generally cautious. We choose model
inputs from the upper end of the range
of possible values for the influential
parameters used in the models, and we
assume that the exposed individual
exhibits ingestion behavior that would
lead to a high total exposure. This
approach reduces the likelihood of not
identifying high risks for adverse
impacts.
Despite the uncertainties, when
individual pollutants or facilities do
screen out, we are confident that the
potential for adverse multipathway
impacts on human health is very low.
On the other hand, when individual
pollutants or facilities do not screen out,
it does not mean that multipathway
impacts are significant, only that we
cannot rule out that possibility and that
a refined multipathway analysis for the
site might be necessary to obtain a more
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accurate risk characterization for the
source category.
For further information on
uncertainties and the Tier 1 and 2
screening methods, refer to the risk
document, Appendix 6, Technical
Support Document for TRIM-Based
Multipathway Tiered Screening
Methodology for RTR.
f. Uncertainties in the Environmental
Risk Screening Assessment
For each source category, we
generally rely on site-specific levels of
environmental HAP emissions to
perform an environmental screening
assessment. The environmental
screening assessment is based on the
outputs from models that estimate
environmental HAP concentrations. The
same models, specifically the
TRIM.FaTE multipathway model and
the AERMOD air dispersion model, are
used to estimate environmental HAP
concentrations for both the human
multipathway screening analysis and for
the environmental screening analysis.
Therefore, both screening assessments
have similar modeling uncertainties.
Two important types of uncertainty
associated with the use of these models
in RTR environmental screening
assessments (and inherent to any
assessment that relies on environmental
modeling) are model uncertainty and
input uncertainty.30
Model uncertainty concerns whether
the selected models are appropriate for
the assessment being conducted and
whether they adequately represent the
movement and accumulation of
environmental HAP emissions in the
environment. For example, does the
model adequately describe the
movement of a pollutant through the
soil? This type of uncertainty is difficult
to quantify. However, based on feedback
received from previous EPA SAB
reviews and other reviews, we are
confident that the models used in the
screen are appropriate and state-of-theart for the environmental risk
assessments conducted in support of
our RTR analyses.
Input uncertainty is concerned with
how accurately the models have been
configured and parameterized for the
assessment at hand. For Tier 1 of the
environmental screen for PB–HAPs, we
configured the models to avoid
underestimating exposure and risk to
reduce the likelihood that the results
30 In the context of this discussion, the term
‘‘uncertainty,’’ as it pertains to exposure and risk
assessment, encompasses both variability in the
range of expected inputs and screening results due
to existing spatial, temporal, and other factors, as
well as uncertainty in being able to accurately
estimate the true result.
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indicate the risks are lower than they
actually are. This was accomplished by
selecting upper-end values from
nationally-representative datasets for
the more influential parameters in the
environmental model, including
selection and spatial configuration of
the area of interest, the location and size
of any bodies of water, meteorology,
surface water and soil characteristics,
and structure of the aquatic food web.
In Tier 1, we used the maximum
facility-specific emissions for the PB–
HAPs (other than lead compounds,
which were evaluated by comparison to
the Secondary Lead NAAQS) that were
included in the environmental
screening assessment and each of the
media when comparing to ecological
benchmarks. This is consistent with the
conservative design of Tier 1 of the
screen. In Tier 2 of the environmental
screening analysis for PB–HAPs, we
refine the model inputs to account for
meteorological patterns in the vicinity
of the facility versus using upper-end
national values, and we identify the
locations of water bodies near the
facility location. By refining the
screening approach in Tier 2 to account
for local geographical and
meteorological data, we decrease the
likelihood that concentrations in
environmental media are overestimated,
thereby increasing the usefulness of the
screen. To better represent widespread
impacts, the modeled soil
concentrations are averaged in Tier 2 to
obtain one average soil concentration
value for each facility and for each PB–
HAP. For PB–HAP concentrations in
water, sediment, and fish tissue, the
highest value for each facility for each
pollutant is used.
For the environmental screening
assessment for acid gases, we employ a
single-tiered approach. We use the
modeled air concentrations and
compare those with ecological
benchmarks.
For both Tiers 1 and 2 of the
environmental screening assessment,
our approach to addressing model input
uncertainty is generally cautious. We
choose model inputs from the upper
end of the range of possible values for
the influential parameters used in the
models, and we assume that the
exposed individual exhibits ingestion
behavior that would lead to a high total
exposure. This approach reduces the
likelihood of not identifying potential
risks for adverse environmental impacts.
Uncertainty also exists in the
ecological benchmarks for the
environmental risk screening analysis.
We established a hierarchy of preferred
benchmark sources to allow selection of
benchmarks for each environmental
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HAP at each ecological assessment
endpoint. In general, EPA benchmarks
used at a programmatic level (e.g.,
Office of Water, Superfund Program)
were used if available. If unavailable,
we used EPA benchmarks used in
regional programs (e.g., Superfund
Program). If benchmarks were not
available at a programmatic or regional
level, we used benchmarks developed
by other agencies (e.g., NOAA) or by
state agencies.
In all cases (except for lead
compounds, which were evaluated
through a comparison to the NAAQS),
we searched for benchmarks at the
following three effect levels, as
described in section III.A.5 of this
preamble:
1. A no-effect level (i.e., NOAEL).
2. Threshold-effect level (i.e.,
LOAEL).
3. Probable effect level (i.e., PEL).
For some ecological assessment
endpoint/environmental HAP
combinations, we could identify
benchmarks for all three effect levels,
but for most, we could not. In one case,
where different agencies derived
significantly different numbers to
represent a threshold for effect, we
included both. In several cases, only a
single benchmark was available. In
cases where multiple effect levels were
available for a particular PB–HAP and
assessment endpoint, we used all of the
available effect levels to help us to
determine whether risk exists and if the
risks could be considered significant
and widespread.
The EPA evaluates the following
seven HAPs in the environmental risk
screening assessment: cadmium,
dioxins/furans, POM, mercury (both
inorganic mercury and methyl mercury),
lead compounds, HCl, and HF, where
applicable. These seven HAPs represent
pollutants that can cause adverse
impacts for plants and animals either
through direct exposure to HAPs in the
air or through exposure to HAPs that is
deposited from the air onto soils and
surface waters. These seven HAPs also
represent those HAPs for which we can
conduct a meaningful environmental
risk screening assessment. For other
HAPs not included in our screening
assessment, the model has not been
parameterized such that it can be used
for that purpose. In some cases,
depending on the HAP, we may not
have appropriate multipathway models
that allow us to predict the
concentration of that pollutant. The EPA
acknowledges that other HAPs beyond
the seven HAPs that we are evaluating
may have the potential to cause adverse
environmental effects and, therefore, the
EPA may evaluate other relevant HAPs
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in the future, as modeling science and
resources allow.
Further information on uncertainties
and the Tier 1 and 2 environmental
screening methods is provided in
Appendix 6 of the document, Technical
Support Document for TRIM-Based
Multipathway Tiered Screening
Methodology for RTR. Also, see the
document titled Residual Risk
Assessment for Pulp Mill Combustion
Sources in Support of the December
2016 Risk and Technology Review
Proposed Rule, available in the docket
for this action.
B. How did we consider the risk results
in making decisions for this proposal?
As discussed in section II.A of this
preamble, in evaluating and developing
standards under CAA section 112(f)(2),
we apply a two-step process to address
residual risk. In the first step, the EPA
determines whether risks are acceptable.
This determination ‘‘considers all health
information, including risk estimation
uncertainty, and includes a presumptive
limit on maximum individual lifetime
[cancer] risk (MIR) 31 of approximately
[1-in-10 thousand] [i.e., 100-in-1
million].’’ 54 FR 38045, September 14,
1989. If risks are unacceptable, the EPA
must determine the emissions standards
necessary to bring risks to an acceptable
level without considering costs. In the
second step of the process, the EPA
considers whether the emissions
standards provide an ample margin of
safety ‘‘in consideration of all health
information, including the number of
persons at risk levels higher than
approximately 1-in-1 million, as well as
other relevant factors, including costs
and economic impacts, technological
feasibility, and other factors relevant to
each particular decision.’’ Id. The EPA
must promulgate emission standards
necessary to provide an ample margin of
safety. After conducting the ample
margin of safety analysis, we consider
whether a more stringent standard is
necessary to prevent, taking into
consideration, costs, energy, safety, and
other relevant factors, an adverse
environmental effect.
In past residual risk actions, the EPA
considered a number of human health
risk metrics associated with emissions
from the categories under review,
including the MIR, the number of
persons in various risk ranges, cancer
incidence, the maximum non-cancer HI
and the maximum acute non-cancer
hazard. See, e.g., 72 FR 25138, May 3,
31 Although defined as ‘‘maximum individual
risk,’’ MIR refers only to cancer risk. MIR, one
metric for assessing cancer risk, is the estimated
risk were an individual exposed to the maximum
level ofa pollutant for a lifetime.
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2007; and 71 FR 42724, July 27, 2006.
The EPA considered this health
information for both actual and
allowable emissions. See, e.g., 75 FR
65068, October 21, 2010; 75 FR 80220,
December 21, 2010; 76 FR 29032, May
19, 2011. The EPA also discussed risk
estimation uncertainties and considered
the uncertainties in the determination of
acceptable risk and ample margin of
safety in these past actions. The EPA
considered this same type of
information in support of this action.
The Agency is considering these
various measures of health information
to inform our determinations of risk
acceptability and ample margin of safety
under CAA section 112(f). As explained
in the Benzene NESHAP, ‘‘the first step
judgment on acceptability cannot be
reduced to any single factor’’ and, thus,
‘‘[t]he Administrator believes that the
acceptability of risk under [previous]
section 112 is best judged on the basis
of a broad set of health risk measures
and information.’’ 54 FR 38046,
September 14, 1989. Similarly, with
regard to the ample margin of safety
determination, ‘‘the Agency again
considers all of the health risk and other
health information considered in the
first step. Beyond that information,
additional factors relating to the
appropriate level of control will also be
considered, including cost and
economic impacts of controls,
technological feasibility, uncertainties,
and any other relevant factors.’’ Id.
The Benzene NESHAP approach
provides flexibility regarding factors the
EPA may consider in making
determinations and how the EPA may
weigh those factors for each source
category. In responding to comment on
our policy under the Benzene NESHAP,
the EPA explained that:
‘‘[t]he policy chosen by the Administrator
permits consideration of multiple measures
of health risk. Not only can the MIR figure
be considered, but also incidence, the
presence of non-cancer health effects, and the
uncertainties of the risk estimates. In this
way, the effect on the most exposed
individuals can be reviewed as well as the
impact on the general public. These factors
can then be weighed in each individual case.
This approach complies with the Vinyl
Chloride mandate that the Administrator
ascertain an acceptable level of risk to the
public by employing [her] expertise to assess
available data. It also complies with the
Congressional intent behind the CAA, which
did not exclude the use of any particular
measure of public health risk from the EPA’s
consideration with respect to CAA section
112 regulations, and thereby implicitly
permits consideration of any and all
measures of health risk which the
Administrator, in [her] judgment, believes are
appropriate to determining what will ‘protect
the public health’.’’
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See 54 FR at 38057, September 14, 1989.
Thus, the level of the MIR is only one
factor to be weighed in determining
acceptability of risks. The Benzene
NESHAP explained that ‘‘an MIR of
approximately one in 10 thousand
should ordinarily be the upper end of
the range of acceptability. As risks
increase above this benchmark, they
become presumptively less acceptable
under CAA section 112, and would be
weighed with the other health risk
measures and information in making an
overall judgment on acceptability. Or,
the Agency may find, in a particular
case, that a risk that includes MIR less
than the presumptively acceptable level
is unacceptable in the light of other
health risk factors.’’ Id. at 38045.
Similarly, with regard to the ample
margin of safety analysis, the EPA stated
in the Benzene NESHAP that: ‘‘EPA
believes the relative weight of the many
factors that can be considered in
selecting an ample margin of safety can
only be determined for each specific
source category. This occurs mainly
because technological and economic
factors (along with the health-related
factors) vary from source category to
source category.’’ Id. at 38061. We also
consider the uncertainties associated
with the various risk analyses, as
discussed earlier in this preamble, in
our determinations of acceptability and
ample margin of safety.
The EPA notes that it has not
considered certain health information to
date in making residual risk
determinations. At this time, we do not
attempt to quantify those HAP risks that
may be associated with emissions from
other facilities that do not include the
source categories in question, mobile
source emissions, natural source
emissions, persistent environmental
pollution, or atmospheric
transformation in the vicinity of the
sources in these categories.
The Agency understands the potential
importance of considering an
individual’s total exposure to HAPs in
addition to considering exposure to
HAP emissions from the source category
and facility. We recognize that such
consideration may be particularly
important when assessing non-cancer
risks, where pollutant-specific exposure
health reference levels (e.g., RfCs) are
based on the assumption that thresholds
exist for adverse health effects. For
example, the Agency recognizes that,
although exposures attributable to
emissions from a source category or
facility alone may not indicate the
potential for increased risk of adverse
non-cancer health effects in a
population, the exposures resulting
from emissions from the facility in
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combination with emissions from all of
the other sources (e.g., other facilities) to
which an individual is exposed may be
sufficient to result in increased risk of
adverse non-cancer health effects. In
May 2010, the SAB advised the EPA
‘‘that RTR assessments will be most
useful to decision makers and
communities if results are presented in
the broader context of aggregate and
cumulative risks, including background
concentrations and contributions from
other sources in the area.’’ 32
In response to the SAB
recommendations, the EPA is
incorporating cumulative risk analyses
into its RTR risk assessments, including
those reflected in this proposal. The
Agency is: (1) Conducting facility-wide
assessments, which include source
category emission points as well as
other emission points within the
facilities; (2) considering sources in the
same category whose emissions result in
exposures to the same individuals; and
(3) for some persistent and
bioaccumlative pollutants, analyzing the
ingestion route of exposure. In addition,
the RTR risk assessments have always
considered aggregate cancer risk from
all carcinogens and aggregate noncancer HI from all non-carcinogens
affecting the same target organ system.
Although we are interested in placing
source category and facility-wide HAP
risks in the context of total HAP risks
from all sources combined in the
vicinity of each source, we are
concerned about the uncertainties of
doing so. Because of the contribution to
total HAP risk from emission sources
other than those that we have studied in
depth during this RTR review, such
estimates of total HAP risks would have
significantly greater associated
uncertainties than the source category or
facility-wide estimates. Such aggregate
or cumulative assessments would
compound those uncertainties, making
the assessments too unreliable.
C. How did we perform the technology
review?
Our technology review focused on the
identification and evaluation of
developments in practices, processes,
and control technologies that have
occurred since the MACT standards
were promulgated. Where we identified
such developments, in order to inform
32 The EPA’s responses to this and all other key
recomendations of the SAB’s advisory on RTR risk
assessment methodologies (which is available at:
https://yosemite.epa.gov/sab/sabproduct.nsf/
4AB3966E263D943A8525771F00668381/$File/EPASAB-10-007-unsigned.pdf) are outlined in a
memorandum to this rulemaking docket from David
Guinnup titled, EPA’s Actions in Response to the
Key Recommendations of the SAB Review of RTR
Risk Assessment Methodologies.
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our decision of whether it is
‘‘necessary’’ to revise the emissions
standards, we analyzed the technical
feasibility of applying these
developments and the estimated costs,
energy implications, non-air
environmental impacts, as well as
considering the emission reductions.
We also considered the appropriateness
of applying controls to new sources
versus retrofitting existing sources.
Based on our analyses of the available
data and information, we identified
potential developments in practices,
processes, and control technologies. For
this exercise, a ‘‘development’’ was
considered to be any of the following
that was not considered during the
development of the promulgated
subpart MM standards that could result
in significant additional reductions of
regulated HAP emissions:
• Add-on control technology or other
equipment not previously identified;
• Improvements in add-on control
technology or other equipment;
• Work practices or operational
procedures that were not previously
identified;
• Process change or pollution
prevention alternative that could be
broadly applied to further reduce HAP
emissions; and
• Improvements in work practices,
operational procedures, process
changes, or pollution prevention
alternatives.
In addition to reviewing the practices,
processes, and control technologies that
were considered at the time we
originally developed the NESHAP, we
reviewed a variety of data sources in our
investigation of potential practices,
processes, or controls to consider.
Among the sources we reviewed were
the practices, processes and control
technologies considered in the NESHAP
for various industries that were
promulgated since the MACT standards
being reviewed in this action. We
requested information from facilities
regarding developments in practices,
processes or control technology through
Part III of the Pulp and Paper Sector
ICR. The ICR data provided information
on the process and emission controls
currently in use on chemical recovery
combustion sources, and provided
emissions data to assess the
performance of current emissions
controls. We reviewed continuous
opacity monitoring data for ESPcontrolled recovery furnaces and lime
kilns. We also consulted the EPA’s
RBLC to determine whether it contained
any practices, processes or control
technologies for the types of processes
covered by the 40 CFR part 63, subpart
MM source category.33 We conducted a
general search of the Internet for
information on control technologies
applicable to pulp mill combustion
sources. We also reviewed information
from other sources, such as state and/or
local permitting agency databases.
Each of the evaluations listed above
considered and reviewed the
technologies suitable to demonstrate
compliance with the requirements listed
in 40 CFR 63.860 through 63.868
(subpart MM).34
IV. Analytical Results and Proposed
Decisions
A. What are the results of the risk
assessment and analyses?
1. Inhalation Risk Assessment Results
The inhalation risk modeling
performed to estimate risks based on
actual and allowable emissions relied
primarily on emissions data from the
ICR. The results of the chronic baseline
inhalation cancer risk assessment
indicate that, based on estimates of
current actual and allowable emissions
under 40 CFR part 63, subpart MM, the
MIR posed by the MACT source
category was 4-in-1 million. The total
estimated cancer incidence from the
MACT source category based on actual
emission levels is 0.01 excess cancer
cases per year, or 1 case every 100 years,
while the cancer incidence for allowable
emissions is 0.02 excess cancer cases
per year, or 1 case every 50 years. Air
emissions of chromium VI,
formaldehyde, and naphthalene
contributed 31 percent, 18 percent, and
13 percent, respectively, to this cancer
incidence. We estimated approximately
7,600 people to have cancer risks greater
than or equal to 1-in-1 million
considering actual and allowable
emissions from subpart MM sources,
refer to Table 3.
TABLE 3—INHALATION RISK ASSESSMENT SUMMARY FOR PULP MILL COMBUSTION SOURCES SOURCE CATEGORY—
(SUBPART MM)
Cancer MIR
(in-1 million)
Based on actual
emissions
Source Category
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Whole Facility .....
Based on allowable emissions
4 (naphthalene,
acetaldehyde).
20 (arsenic, chromium VI).
4 (naphthalene,
acetaldehyde).
............................
Cancer
incidence
(cases per
year)
Population
with risk of
1-in-1 million
or more
Population
with risk of
10-in-1 million
or more
7,600
0
HI < 1
HI < 1
0.05
440,000
280
HI = 1
HI = 1
2. Acute Risk Results
33 See the memorandum in the docket titled,
Summary of RBLC and Other Findings to Suppport
the Residual Risk and Technology Review of
Chemical Recovery Combustion Sources NESHAP.
34 See the memorandum in the docket titled,
Section 112(d)(6) Technology Review fo the
NESHAP for Chemical Recovery Combustion
Sourcces at Kraft, Soda, Sulfite, and Stand-Alone
Semichemical Pulp Mills.
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Our screening analysis for worst-case
acute impacts based on actual emissions
did not identify impacts associated with
any pollutants that exceeded an HQ
value of 1 based upon the REL. For the
acute risk screening analysis, we
calculated acute hourly multipliers
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Max chronic
noncancer HI
(allowables)
0.01
We estimated the maximum modeled
chronic non-cancer HI (TOSHI) value
for the source category based on actual
and allowable emissions to be 0.3, with
acrolein emissions from lime kilns
accounting for 92 percent of the HI.
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Max chronic
noncancer HI
(actuals)
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based on the median of peak-to-mean
ratio for 14 emission process groups
ranging from 1.3 to 4.7, with emissions
from the semichemical recovery process
having the highest hourly peak
emissions with a multiplier of 4.7. For
more information on how we calculated
the acute hourly multipliers, refer to the
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risk document, Appendix 1, Preparation
of Residual Risk Modeling Input File for
Subpart MM dated September 30, 2014.
3. Multipathway Risk Screening Results
Results of the worst-case Tier 1
screening analysis identified emissions
(based on estimates of actual emissions)
exceeding the PB–HAP emission cancer
screening rates for dioxin/furans and
polycyclic aromatic hydrocarbons
(PAH) and the non-cancer screening
threshold for mercury. For the
compounds and facilities that did not
screen out at Tier 1, we conducted a
Tier 2 screen. The Tier 2 screen replaces
some of the assumptions used in Tier 1
with site-specific data, including the
location of fishable lakes and local
precipitation, wind direction and speed.
The Tier 2 screen continues to rely on
high-end assumptions about
consumption of local fish and locally
grown or raised foods (adult female
angler at 99th percentile consumption
for fish for the subsistence fisherman
scenario and 90th percentile
consumption for locally grown or raised
foods for the farmer scenario). For
facilities for which the Tier 2 screening
value(s) indicate a potential health risk
to the public, we can conduct a Tier 3
multipathway screen. Tier 3 has three
individual stages: (1) Lake assessment to
assess fishability and accessibility; (2)
plume-rise calculations to estimate the
emissions exiting the mixing layer and
resulting in no ground-level exposures;
(3) TRIMFaTE hourly screening runs
using the layout for the farm and/or fish
location that best characterizes the
facility being modeled. We progress
through Tier 3 stages until the facility’s
screening values indicate that emissions
are unlikely to pose health risks to the
public, or until all three stages are
complete. A Tier 3 screen was required
for one facility that exceeded the Tier 2
screen for mercury. It is important to
note that, even with the inclusion of
some site-specific information in the
Tier 2 and 3 analysis, the multipathway
screening analysis is still a very
conservative, health-protective
assessment (i.e., upper-bound
consumption of local fish and locally
grown and/or raised foods) and in all
likelihood yields results that serve as an
upper-bound multipathway risk
associated with a facility.
While the screening analysis is not
designed to produce a quantitative risk
result, the factor by which the emissions
exceed the threshold serves as a rough
gauge of the ‘‘upper-limit’’ risks we
would expect from a facility. Thus, for
example, if a facility emitted a PB–HAP
carcinogen at a level 2 times the
screening threshold, we can say with a
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high degree of confidence that the actual
maximum cancer risks will be less than
2-in-1 million. Likewise, if a facility
emitted a noncancer PB–HAP at a level
2 times the screening threshold, the
maximum noncancer hazard would
represent an HQ less than 2. The high
degree of confidence comes from the
fact that the screens are developed using
the very conservative (health-protective)
assumptions that we describe above.
a. Cancer Risk Screening
Results of the worst-case Tier 1
screening analysis indicate that 85 of
the 108 facilities with pulp mill
combustion sources exceeded the PB–
HAP emission cancer screening rates
(based on estimates of actual emissions)
for dioxin/furans and PAH. The EPA
conducted a Tier 2 cancer screening
analysis of the 85 facilities that were
found to exceed the Tier 1 screening
value. Nineteen of these facilities with
subpart MM MACT source category
sources emitted dioxin/furans and PAH
above a cancer screening value of 1 for
the subsistence fisher and farmer
scenarios. In the Tier 2 analysis, the
individual dioxin/furan congener
emissions are all scaled based on their
toxicity relative to 2,3,7,8tetrachlorodibenzo-p-dioxin and are
reported as toxic equivalents (TEQs),
and all PAH congener emissions are
scaled based on their toxicity relative to
benzo(a)pyrene and are reported as
TEQs. The maximum Tier 2 cancer
screening value for the subsistence
fisher scenario and the farmer scenario
for this source category was equal to 10,
which represents a maximum cancer
risks that would be less than 10-in-1
million. The EPA did not conduct
further cancer screening for this source
category and considered this result
along with all the risk results as part of
determining whether the risks are
acceptable (as discussed in section B).
b. Non-Cancer Risk Screening
Results of the worst-case Tier 1
screening analysis indicate that 59 of
the 108 plants sources exceeded the Tier
1 non-cancer screen value for mercury.
The EPA conducted a Tier 2 chronic
non-cancer screening analysis of the 59
facilities, resulting in 9 facilities
emitting divalent mercury above the
non-cancer screening value of 1 for the
subsistence fisher scenario. The highest
exceedance of the Tier 2 non-cancer
mercury screen value for pulp mill
combustion sources under 40 CFR part
63, subpart MM was equal to 5. The risk
associated with divalent mercury is
based on its ability to transform into the
most toxic form of mercury as methyl
mercury.
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The Tier 2 non-cancer screening
analysis for the 9 facilities indicated
potential risks greater than or equal to
2 but less than 5 times the non-cancer
screening level for the subsistence fisher
scenario. More refined screening using
Tier 3 was conducted for the 9 facilities
flagged in Tier 2. The Tier 3 screen
examined the set of lakes from which
the fisher might ingest fish (Stage 1).
Any lakes that appeared to not be
fishable or not publicly accessible were
removed from the assessment, and the
screening assessment was repeated.
After we made the determination that
the critical lakes were fishable, we
analyzed plume rise data for each of the
sites (Stage 2). The results of the Tier 3
screen (Stage 2) showed one facility
with a non-cancer screen value of 2.
We conducted the final screening
stage of Tier 3 for this single facility
utilizing a time-series assessment (Stage
3). In this stage, we conducted a new
mercury run using TRIM.FaTE for each
relevant lake that represents a risk
concern based upon the Tier 3 plumerise assessment. For these model runs,
we started with the screening
configuration corresponding to the lake
location, but instead of the static
meteorology and stack parameters used
in previous screening tiers and stages,
we used site-specific hourly
meteorology and the hourly plume-rise
values calculated in the Tier 3 plumerise assessment. Allowing TRIM.FaTE to
model chemical fate and transport with
hour-by-hour changes in meteorology
and plume rise produces a more
accurate estimate of chemical
concentrations in media of interest, as
compared to the static values used in
Tier 2 and the post-processing
adjustments made in the Tier 3 plumerise assessment. If the potential risk
(estimated using this Tier 3 time-series
approach) associated with a facility’s
PB–HAP emissions are lower than the
screening value, we consider the
emissions to pose no significant risk.
This Tier 3 screen resulted in lowering
the maximum exceedance of the screen
value for the highest site from 2 to 1.
Further details on the refined
multipathway screening analysis are in
Appendix 10, Attachment 1 of the risk
report, ‘‘Residual Risk Assessment for
Pulp Mill Combustion Sources in
Support of the December 2016 Risk and
Technology Review Proposed Rule’’.
4. Environmental Risk Screening Results
As described in section III.A of this
document, we conducted an
environmental risk screening
assessment for the 40 CFR part 63,
subpart MM source category for the
following seven HAPs: PAH, mercury
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(methyl mercury and mercuric
chloride), cadmium, lead, dioxin/furans,
HCl, and HF.
In the Tier 1 screening analysis for
PB–HAPs (other than lead, which we
evaluated differently), one modeled soil
parcel for one facility in the source
category exceeded a surface soil—
threshold level benchmark
(invertebrates) for mercuric chloride by
2. There were no Tier 1 exceedances of
any benchmarks for the other pollutants;
PAH, cadmium and dioxins/furans.
Therefore, we conducted a Tier 2 screen
for mercuric chloride only. In the Tier
2 screen for mercuric chloride, none of
the individual modeled concentrations
for any facility in the source category
exceeded any of the ecological
benchmarks.
For lead, we did not estimate any
exceedances of the secondary lead
NAAQS. For HCl and HF, the average
modeled concentration around each
facility (i.e., the average concentration
of all off-site data points in the
modeling domain) did not exceed any
ecological benchmark. In addition, each
individual modeled concentration of
HCl and HF (i.e., each off-site data point
in the modeling domain) was below the
ecological benchmarks for all facilities.
5. Facility-Wide Risk Results
Considering facility-wide emissions at
the 108 plants, we estimated the MIR to
be 20-in-1 million driven by arsenic and
chromium VI emissions, and calculated
the chronic non-cancer TOSHI value to
be 1 driven by emissions of acrolein
(refer to Table 3). The above cancer and
non-cancer risks are driven by
emissions from the industrial boilers.
We estimated approximately 440,000
people to have cancer risks greater than
or equal to 1-in-1 million considering
whole facility emissions from 81 of the
108 facilities modeled from the pulp
and paper production industry (refer to
Table 3). From these 81, 2 facilities have
cancer risks greater than or equal to 10in-1 million (but less than 20-in-1
million) with approximately 300 being
exposed at these levels.
6. What demographic groups might
benefit from this regulation?
To determine whether or not to
conduct a demographics analysis, which
is an assessment of risks to individual
demographic groups, we look at a
combination of factors, including the
MIR, non-cancer TOSHI, population
around the facilities in the source
category, and other relevant factors. For
the 40 CFR part 63, subpart MM source
category, we examined the potential for
any environmental justice (EJ) issues
that might be associated with the source
category, by performing a demographic
analysis of the population close to the
facilities. In this analysis, we evaluated
the distribution of HAP-related cancer
and non-cancer risks from the subpart
MM source category across different
social, demographic, and economic
groups within the populations living
near facilities identified as having the
highest risks. The methodology and the
results of the demographic analyses are
included in a technical report, Risk and
Technology Review—Analysis of SocioEconomic Factors For Populations
Living Near Pulp Mill Combustion
Sources, available in the docket for this
action.
The results of the demographic
analysis are summarized in Table 4
below. These results, for various
demographic groups, are based on the
estimated risks from actual emissions
levels for the population living within
50 km of the facilities.
TABLE 4—SUBPART MM SOURCE CATEGORY DEMOGRAPHIC RISK ANALYSIS RESULTS
Nationwide
Total Population ...........................................................................................................................
Population
with cancer
risk at or
above 1-in-1
million
Population
with chronic
hazard index
above 1
312,861,265
7,600
0
72
28
67
33
0
0
72
13
1.1
14
67
28
0.4
5
0
0
0
0
17
83
3
97
0
0
14
86
16
84
0
0
15
85
18
82
0
0
Race by Percent
White ............................................................................................................................................
All Other Races ...........................................................................................................................
Race by Percent
White ............................................................................................................................................
African American .........................................................................................................................
Native American ..........................................................................................................................
Other and Multiracial ...................................................................................................................
Ethnicity by Percent
Hispanic .......................................................................................................................................
Non-Hispanic ...............................................................................................................................
Income by Percent
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Below Poverty Level ....................................................................................................................
Above Poverty Level ....................................................................................................................
Education by Percent
Over age 25 and without High School Diploma ..........................................................................
Over age 25 and with a High School Diploma ............................................................................
The results of the 40 CFR part 63,
subpart MM source category
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demographic analysis indicate that
emissions from the source category
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expose approximately 7,600 people to a
cancer risk at or above 1-in-1 million
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and no one exposed to a chronic noncancer TOSHI greater than 1. The
specific demographic results indicate
that the percentage of the population
potentially impacted by emissions is
greater than its corresponding national
percentage for the minority population
(33 percent for the source category
compared to 28 percent nationwide), the
African American population (28
percent for the source category
compared to 13 percent nationwide) and
for the population over age 25 without
a high school diploma (18 percent for
the source category compared to 15
percent nationwide). The proximity
results (irrespective of risk) indicate that
the population percentages for certain
demographic categories within 5 km of
source category emissions are greater
than the corresponding national
percentage for those same
demographics. The following
demographic percentages for
populations residing within close
proximity to facilities with chemical
recovery combustion sources are higher
than the corresponding nationwide
percentage: African American, ages 65
and up, over age 25 without a high
school diploma, and below the poverty
level.
The risks due to HAP emissions from
this source category are low for all
populations (e.g., inhalation cancer risks
are less than 4-in-1 million for all
populations and non-cancer hazard
indices are less than 1). Furthermore,
we do not expect this proposal to
achieve significant reductions in HAP
emissions. Section IV.C of this preamble
addresses opportunities as part of the
technology review to further reduce
HAP emissions. These technologies
were found not to be cost-effective.
Therefore, we conclude that this
proposal 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. However, this
proposal, if finalized, will provide
additional benefits to these
demographic groups by improving the
compliance, monitoring, and
implementation of the NESHAP.
B. What are our proposed decisions
regarding risk acceptability, ample
margin of safety, and adverse
environmental effects?
1. Risk Acceptability
As noted in section II.A of this
preamble, the EPA sets standards under
CAA section 112(f)(2) using ‘‘a two-step
standard-setting approach, with an
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analytical first step to determine an
’acceptable risk’ that considers all
health information, including risk
estimation uncertainty, and includes a
presumptive limit on MIR of
approximately 1-in-10 thousand.’’ (54
FR 38045, September 14, 1989).
In this proposal, the EPA estimated
risks based on both actual and allowable
emissions from pulp mill combustion
sources. As discussed above, in
determining acceptability, we
considered risks based on both actual
and allowable emissions. Based on the
risk assessment results described above,
the EPA is proposing that the risks are
acceptable.
The baseline inhalation cancer risk
from the source category was 4-in-1million for the most exposed individual
based on actual and allowable
emissions. The total estimated
incidence of cancer for this source
category due to inhalation exposures is
0.02 excess cancer cases per year, or 1
case in 50 years. The Agency estimates
that the maximum chronic non-cancer
TOSHI from inhalation exposure for this
source category has an HI equal to 0.3
based upon both actual and allowable
emissions. Lime kilns account for a
large portion (92 percent) of the HI.
The multipathway screening analysis,
based upon actual emissions, indicates
the excess cancer risk from this source
category is less than 10-in-1 million
based on dioxins/furans and PAH
emissions, with PAH emissions
accounting for 99 percent of these
potential risks from the fisher and the
farmer scenarios. There were no
facilities within this source category
with a multipathway non-cancer screen
value greater than 1 for cadmium or
mercury. In evaluating the potential for
multipathway effects from emissions of
lead, we compared modeled maximum
annual lead concentrations to the
secondary NAAQS for lead (0.15 mg/
m3). Results of this analysis estimate
that the NAAQS for lead would not be
exceeded at any off-site locations.
To put the risks from the source
category in context, we also evaluated
facility-wide risk. Our facility-wide
assessment, based on actual emissions,
estimated the MIR to be 20-in-1 million
driven by arsenic and chromium VI
emissions, and estimated the chronic
non-cancer TOSHI value to be 1 driven
by emissions of acrolein. We estimated
approximately 440,000 people to have
cancer risks greater than or equal to 1in-1 million considering facility-wide
emissions from the pulp and paper
production industry (see Table 3). The
above cancer and non-cancer risks are
driven by emissions from industrial
boilers, representing 62 percent of the
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cancer risks and 95 percent of the noncancer risks. Emissions from the 40 CFR
part 63, subpart MM sources represent
only 6 percent of the total facility-wide
cancer risk of 20-in-1 million.
The screening assessment of worstcase acute inhalation impacts indicates
no pollutants exceeding an HQ value of
1 based on the REL, with an estimated
worst-case maximum acute HQ of 0.3
for acrolein based on the 1-hour REL.
A review of the uncertainties in the
risk assessment identified one
additional key consideration, and that is
the quality of data associated with the
whole-facility emissions. The data
provided from the power boilers were
collected in 2009 and represent preMACT emissions before any controls.
The uncertainty introduced by using
pre-MACT boiler emissions data may
result in an overestimated risk estimate
for the whole-facility analysis for both
cancer and non-cancer impacts.
Considering all of the available health
risk information, we propose that risks
from the source category are acceptable.
2. Ample Margin of Safety Analysis
As directed by section 112(f)(2), we
conducted an additional analysis to
determine whether additional standards
are needed to provide an ample margin
of safety to protect public health. Under
this ample margin of safety analysis, we
evaluated the cost and feasibility of
available control technologies and other
measures that could be applied in this
source category to further reduce the
risks (or potential risks) due to
emissions of HAPs identified in our risk
assessment, along with all of the health
risks and other health information
considered in our determination of risk
acceptability.
Although we are proposing that the
risks from the subpart MM source
category are acceptable, inhalation risk
estimates are above 1-in-1 million at the
actual and MACT-allowable emission
levels for approximately 7,600
individuals in the exposed population.
The HAP risk drivers contributing to the
inhalation risks in excess of 1-in-1
million include primarily the gaseous
organic HAPs acetaldehyde and
naphthalene. Additional gaseous
organic HAPs contributing to the risk
includes benzene, chloroprene,
formaldehyde, 2-methylnaphthalene,
7,12-dimethylbenz[a]anthracene,
acenaphthene, acenaphthylene, and
fluoranthene. More than 80-percent of
the mass emissions of these compounds
originate from NDCE recovery furnaces,
and DCE recovery furnaces (including
BLO systems). We considered options
for further reducing gaseous organic
HAP emissions from NDCE and DCE
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recovery furnaces. The greatest
reduction in gaseous organic HAP
emissions that could be achieved for
DCE recovery furnaces would result
from DCE-to-NDCE furnace conversions
or replacements of DCE furnaces with
NDCE systems. We estimated furnace
emissions to be reduced when a DCE
furnace is converted (or replaced with
NDCE design). Conversion or
replacement of a DCE system with an
NDCE system results in removal of the
BLO system and elimination of 100
percent of the BLO emissions. For NDCE
recovery furnaces with wet ESP
systems, conversion of the wet ESP
system to a dry system can further
reduce gaseous organic HAPs. Section
IV.C.1 of this preamble discusses the
costs and impacts associated with DCE
conversions (or replacements) and wetto-dry ESP conversions for NDCE
recovery furnaces. The overall cost of
these options is an estimated $1.4
billion to $3.7 billion in capital cost and
$120 million to $440 million in
annualized cost. Application of this
option would achieve an estimated
emission reduction of 2,920 tpy of
gaseous organic HAPs (including risk
drivers and other gaseous organic
HAPs), and the corresponding costeffectiveness ranges from $45,000 to
$153,000 per ton of emissions reduced.
The non-air environmental impacts,
energy impacts, and secondary air
emissions associated with the options
described above are discussed in a
memorandum in the docket. Due to the
low level of current risk and the
substantial costs associated with these
options, we are proposing that
additional emission reductions from the
source category are not necessary to
provide an ample margin of safety.
srobinson on DSK5SPTVN1PROD with PROPOSALS3
3. Adverse Environmental Effects
Based on the results of our
environmental risk screening
assessment, we propose to conclude that
there is not an adverse environmental
effect as a result of HAP emissions from
the 40 CFR part 63, subpart MM source
category.35 Thus, we are proposing that
it is not necessary to set a more stringent
standard to prevent an adverse
environmental effect.
35 The environmental screening analysis is
documented in Residual Risk Assessment for Pulp
Mill Combustion Sources in Support of the
December 2016 Risk and Technology Review
Proposed Rule, in the docket for this action.
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C. What are the results and proposed
decisions based on our technology
review?
1. Kraft and Soda Recovery Furnaces
The ability to recover pulping
chemicals is imperative to the kraft and
soda process, and is achieved by
burning spent pulping liquor (i.e., black
liquor) in a recovery furnace. The
recovery furnace is easily identified at a
pulp mill because it is typically the
tallest equipment on site. The purpose
of the recovery furnace is to: (1) Recover
inorganic pulping chemicals (e.g.,
sodium sulfide (Na2S) and sodium
hydroxide (NaOH) in kraft mills and
NaOH in soda mills); and (2) produce
steam. The recovered inorganic pulping
chemicals are reused in the process, and
the steam is used to generate electricity
and for process heating. Prior to being
fired in the recovery furnace, black
liquor recovered from pulp washing is
concentrated using an NDCE or DCE.
The NDCE is an indirect, steam-heated
black liquor concentrator. The DCE uses
the hot combustion gases exiting the
furnace to increase the solids content of
the black liquor. A BLO system precedes
the DCE to reduce malodorous total
reduced sulfur (TRS) emissions that can
be stripped in the DCE when hot flue
gases from the recovery furnace come in
contact with the black liquor. The BLO
system uses molecular oxygen (O2) or
air to oxidize Na2S to nonvolatile
sodium thiosulfate (Na2S2O3) to reduce
the potential for stripping. Outputs from
recovery furnaces include molten smelt
(primarily Na2S and sodium carbonate
(Na2CO3)), flue gases, and steam. The
smelt exits from the bottom of the
furnace into an SDT, where the recovery
of kraft pulping chemicals continues.
Particulate matter (primarily sodium
sulfate (Na2SO4) [salt cake] and Na2CO3)
entrained in the flue gases is also
recovered using an ESP, which deposits
the collected material into a chemical
ash tank or salt cake mix tank for
subsequent addition into the
concentrated black liquor.
We reviewed ICR data on recovery
furnace design and emissions controls
for purposes of the technology review.
There are currently 148 kraft and soda
recovery furnaces in the United States,
including 36 existing DCE furnaces, 108
existing NDCE furnaces, and 4 recovery
furnaces subject to the new source
limits under 40 CFR part 63, subpart
MM. The vast majority (96 percent) of
recovery furnaces have ESP control,
including the 4 NDCE recovery furnaces
subject to the new source limits under
subpart MM. Three of the DCE furnaces
and one of the NDCE furnaces have an
ESP followed by a wet scrubber. Two
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NDCE furnaces have a wet scrubber
alone. The one remaining soda recovery
furnace is a subpart MM new source
with ESP control. As we noted in 2001,
when subpart MM was promulgated, we
project no new DCE recovery furnaces to
be installed in the future, because more
energy-efficient NDCE technology is
now prevalent.
Recovery furnace ESPs can be further
characterized as wet- or dry-bottom
ESPs having either a wet or dry PM
return system. A wet-bottom ESP uses
either oxidized or unoxidized black
liquor to collect the PM and carry it to
the salt cake mix tank via a wet PM
return system. A dry-bottom ESP routes
the captured PM to the mix tank via a
screw conveyor or drag chain without
the use of liquid, typically with a dry
PM return system. However, there are
some dry-bottom ESPs with a wet PM
return system that use black liquor or
other process liquids to transport the
dry collected PM to the mix tank.
Approximately 60 percent of recovery
furnaces in the United States (or 90
recovery furnaces) have a dry-bottom
ESP with a dry PM return system
(including two furnaces with a drybottom ESP followed by a scrubber).
Recovery furnace gaseous organic
HAP. Subpart MM of 40 CFR part 63
contains a gaseous organic HAP limit of
0.025 lb/ton BLS (measured as
methanol) for new recovery furnaces
based on use of an NDCE recovery
furnace with a dry-bottom ESP and a
dry PM return system. Recovery furnace
system design impacts gaseous organic
HAP emissions. Non-direct contact
evaporator recovery furnaces emit less
gaseous organic HAPs because there is
no contact between the incoming black
liquor and hot flue gases in the
evaporator and there is no BLO system.
Replacement of DCE recovery furnace
systems with a new NDCE recovery
furnace or conversion of an existing
DCE furnace to an NDCE design
(referred to as a ‘‘low-odor conversion’’),
along with removal of the associated
BLO system, provides the greatest
reduction in gaseous organic HAP
emissions. Use of a dry-bottom ESP
system with a dry PM return also
reduces gaseous organic HAP emissions.
Analysis of ICR data for our
technology review revealed that the
number of DCE recovery furnaces in the
United States continues to decrease as
facilities with older DCE furnaces either
close or, where feasible, replace aging
DCE furnaces or convert them to NDCE
systems. When subpart MM was
proposed in 1998, 39 percent of
recovery furnaces (82 units) were DCE
systems. Today, only 36 DCE recovery
furnaces remain, which is 24 percent of
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the recovery furnace population
(including 2 DCE recovery furnaces that
are only used as backup systems for
times when other NDCE furnaces onsite
are not operating).
We analyzed the costs and
environmental impacts of replacement
or conversion of the remaining DCE
recovery furnaces as part of our
technology review. High capital costs of
an estimated $1.3 to $3.7 billion and
annualized costs of an estimated $120 to
$440 million are associated with
recovery furnace installation (or
conversion) projects due to the integral
nature of the recovery furnace within
the pulp mill and the number of
upstream and downstream equipment
components that must be removed,
replaced, or reengineered along with the
recovery furnace itself. These costs
would be borne by 21 facilities that
continue to operate DCE recovery
furnaces and are not already projected
to replace these systems in the absence
of any regulatory action. The cost
effectiveness of recovery furnace
conversions or replacements is also
high, at an estimated $44,000 to
$159,000 per ton of gaseous organic
HAPs reduced. We estimated a range of
costs based on multiple information
sources.
We also considered the costs and
impacts associated with converting the
remaining NDCE recovery furnace wetbottom ESPs in the industry to drybottom ESPs. Capital costs are an
estimated $56.1 million for wet-to-dry
bottom ESP conversions at 11 mills with
NDCE recovery furnaces, with cost
effectiveness of $54,000 per ton of
gaseous organic HAPs removed.
The total costs of the gaseous organic
HAP options we considered are an
estimated $1.4 to $3.7 billion in capital
cost borne by 32 facilities, to achieve an
estimated emission reduction of 2,920
tpy of gaseous organic HAP at a cost
effectiveness of $45,000 to $153,000 per
ton of gaseous organic HAPs removed.
Collateral TRS emission reductions are
an estimated 1,250 tpy at a cost
effectiveness of $104,000 to $357,000
per ton of TRS reduced. Given the high
capital costs and high cost per ton of
emissions reduced, we are not
proposing additional regulation of
recovery furnace gaseous organic HAP
emissions as a result of the technology
review.
Recovery furnace PM. Under the
current 40 CFR part 63, subpart MM,
PM is a surrogate for HAP metal
emissions. Subpart MM requires
existing recovery furnaces to meet a PM
emission limit of 0.044 grains per dry
standard cubic foot (gr/dscf) at 8 percent
O2 and requires new recovery furnaces
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to meet a PM limit of 0.015 gr/dscf at
8-percent O2. We recently analyzed PM
emissions test data collected with the
2011 Pulp and Paper Sector ICR for
purposes of the Kraft Pulp Mill NSPS
review promulgated on April 4, 2014
(79 FR 18952). We reviewed the PM
data tabulated for the NSPS review in
the context of the existing and new
source PM limits for the subpart MM
NESHAP technology review. The
dataset included more than 200
filterable PM stack tests, including some
repeat tests, on nearly all of the recovery
furnaces in the United States using a
variety of PM emission controls (ESP,
ESP and wet scrubber combinations,
and wet scrubbers). The PM stack test
data revealed little or no distinction
between DCE and NDCE recovery
furnaces for PM emissions. Nearly all of
the recovery furnaces tested met the
current existing source limit (0.044 gr/
dscf),36 and several met the new source
limit (0.015 gr/dscf), though there was a
considerable scatter of emission test
results between 0.015 and 0.044 gr/dscf,
including variability in test results for
the same units tested multiple times.
There was also variability in the
performance of the different types of
ESP or ESP and scrubber systems such
that no one type of control system
seemed to perform better than another.
Based on the data, wet scrubbing of
recovery furnace exhaust gases (either
alone or in conjunction with an ESP)
does not necessarily improve filterable
PM removal. After reviewing the
recovery furnace PM emissions data, we
concluded that the current subpart MM
emission limits of 0.044 gr/dscf and
0.015 gr/dscf continue to represent the
performance of existing and new
recovery furnaces, respectively. The
technology review did not reveal any
developments in practices, processes,
and control technologies for reducing
PM emissions from recovery furnaces
that have occurred since promulgation
of subpart MM. Therefore, we are not
proposing any changes to the PM
emission limits for purposes of the
technology review. As discussed below,
we estimated incidental incremental
improvements in PM emissions as part
of our analysis of the opacity monitoring
limit for recovery furnaces.
2. Kraft and Soda Lime Kilns
In kraft and soda pulp mills, the lime
kiln is part of the causticizing process
in which green liquor from the SDT is
converted to white liquor. The function
36 Exceptions included a few stack tests that were
repeated, or recovery furnaces that participate in
the PM bubble compliance option under 40 CFR
part 63, subpart MM.
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of the lime kiln is to oxidize lime mud
(calcium carbonate, CaCO3) to reburned
lime (calcium oxide, CaO) in a process
known as calcining. Lime kiln air
pollution control devices include wet
scrubbers, ESPs, or a combination
system including an ESP followed by a
wet scrubber. The 2011 ICR data
indicate that, of 130 lime kilns in the
United States, 89 kilns have wet
scrubbers, 30 kilns have ESPs, and 11
kilns have ESP-wet scrubber
combinations.
Subpart MM, 40 CFR part 63, includes
a PM limit of 0.064 gr/dscf at 10-percent
O2 (which is a surrogate limit for HAP
metals) for existing lime kilns. For new
or reconstructed lime kilns, the subpart
MM limit is 0.010 gr/dscf at 10-percent
O2 based on use of a high-efficiency
ESP. Subpart MM does not distinguish
between fuel types. Lime kilns typically
burn natural gas, fuel oil, petroleum
coke, or a combination of these fuels.
They may also burn noncondensable
gases (NCGs) or pulp mill byproducts
such as tall oil.
The EPA recently reviewed PM stack
test data from more than 250 filterable
PM stack tests (including several repeat
tests) on 110 lime kilns in the United
States for purposes of the Kraft Pulp
Mill NSPS review. The EPA interpreted
this same dataset in the context of
conducting the technology review of the
subpart MM PM limits for lime kilns.
The tests included lime kilns with
scrubbers, ESPs and ESP-wet scrubber
combination controls. Most of the
scrubber-controlled kilns achieved the
subpart MM existing source limit (0.064
gr/dscf at 10-percent O2) with the
exception of kilns that participate in the
PM bubble compliance alternative. The
data suggested that scrubber-controlled
kilns would not be expected to meet the
subpart MM new source limit of 0.010
gr/dscf at 10-percent O2. The EPA found
that ESP and ESP-wet scrubber controls
typically reduce PM to lower levels than
wet scrubbers alone. The ESP-wet
scrubber systems did not necessarily
perform better on filterable PM than the
ESPs alone. Several existing ESP and
ESP-wet scrubber controlled kilns
consistently met the 0.064 gr/dscf
existing source limit, and often met the
new source limit of 0.010 gr/dscf at 10percent O2. The EPA observed test
results between the existing and new
source limit for existing sources with
ESP and ESP-wet scrubber systems. Our
review of the PM emissions test data for
lime kilns suggests that the subpart MM
limits for lime kilns are appropriate. For
purposes of the subpart MM technology
review, the EPA has identified no
practices, processes, or controls for PM
emissions from lime kilns beyond those
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identified when subpart MM was
developed. Therefore, the EPA is not
proposing any changes to the existing
PM limits of 0.064 gr/dscf at 10-percent
O2 for existing lime kilns and 0.010 gr/
dscf at 10-percent O2 for new and
reconstructed lime kilns.
srobinson on DSK5SPTVN1PROD with PROPOSALS3
3. Recovery Furnace and Lime Kiln
Monitoring
This subsection discusses our review
of the opacity and ESP monitoring
provisions for recovery furnaces and
lime kilns with ESPs or combined ESP
and wet scrubber systems.
Continuous opacity monitoring.
Subpart MM of 40 CFR part 63 requires
continuous monitoring of opacity to
demonstrate ongoing compliance with
the PM concentration limits for ESPcontrolled recovery furnaces and lime
kilns. The current PM opacity limits
under subpart MM are 35-percent
opacity for existing recovery furnaces
and 20-percent opacity for existing lime
kilns, new lime kilns, and new recovery
furnaces. Subpart MM contains an
opacity monitoring allowance for
existing sources where 6 percent of the
6-minute opacity averages during a
quarter (excluding periods of SSM and
periods when the facility is not
operating) may exceed the 35-percent
recovery furnace or 20-percent lime kiln
opacity limit without being considered
a violation. Subpart MM currently
contains a corrective action threshold of
10 consecutive 6-minute averages above
20-percent opacity for new and existing
recovery furnaces and lime kilns.
The EPA reviewed recovery furnace
and lime kiln continuous opacity
monitoring system (COMS) data for
purposes of the technology review to
evaluate the current 40 CFR part 63,
subpart MM opacity limits and 6percent monitoring allowance. The EPA
performed a similar review of the COMS
data for the subpart BBa NSPS review
promulgated April 4, 2014 (79 FR
18952). The EPA’s analysis of the
recovery furnace COMS data for subpart
MM is included in a memorandum in
the docket.37 Our conclusions from
reviewing the opacity data in the
context of subpart MM are consistent
with the conclusions reached for the
2014 NSPS review.
The COMS data for 135 recovery
furnaces show that the majority of
existing recovery furnaces, regardless of
design (DCE or NDCE), and with most
controls, are meeting a 20-percent
opacity limit based on a 6-minute
37 See memorandum titled, Review of the
Continuous Opacity Monitoring Data from the Pulp
and Paper ICR Responses for Subpart MM Sources,
in the docket.
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average, with fewer than 2 percent of
averaging periods exceeding 20-percent
opacity, including periods of startup
and shutdown. The EPA also reviewed
state permits and found many recovery
furnaces with permit limits of 20percent opacity. Therefore, the EPA
concludes that this information is
evidence that there has been a
development in existing recovery
furnace operating practices that
supports reducing the existing source
opacity limit from 35-percent to 20percent and revising the monitoring
allowance for the 20-percent opacity
limit from 6 percent to a 2-percent
monitoring allowance as part of the 40
CFR part 63, subpart MM technology
review process.
The COMS data for 28 ESP-controlled
lime kilns show that all of the existing
lime kilns are meeting the 20-percent
opacity limit based on a 6-minute
average, with nearly all performing at a
1-percent monitoring allowance,
including periods of startup and
shutdown. The EPA considers this
information as evidence that there has
been a development in existing lime
kiln operating practices and that this
development supports revising the
monitoring allowance from 6 percent to
a 1-percent monitoring allowance for
opacity as part of the 40 CFR part 63,
subpart MM technology review process.
Subpart MM of 40 CFR part 63
currently requires that the opacity
allowance be calculated based on the
percent of the operating time in a
quarter in which excess emissions are
recorded. The Agency is proposing to
change the reporting requirement
frequency, as discussed in section
IV.D.4, and, therefore, analyzed both
quarterly and semiannual averaging
periods when reviewing the proposed
monitoring allowance discussed above.
The EPA considered the impacts of
various opacity monitoring options as
part of the technology review. The
opacity regulatory options considered
for kraft and soda recovery furnaces
were:
Baseline Option 1: 35-percent opacity
(existing) or 20-percent opacity (new),
20-percent corrective action level, 6percent monitoring allowance, quarterly
reporting.
Option 2: 35-percent opacity, 20percent corrective action level, 2percent monitoring allowance,
semiannual reporting.
Option 3: 20-percent opacity, 6percent monitoring allowance, quarterly
reporting.
Option 4: 20-percent opacity, 2percent monitoring allowance,
semiannual reporting.
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Option 5: 20-percent opacity, 2percent monitoring allowance, quarterly
reporting.
The opacity regulatory options
considered for kraft and soda ESPcontrolled lime kilns were:
Baseline Option 1: 20-percent opacity
and corrective action level with 6percent allowance, quarterly reporting.
Option 2: 20-percent opacity with a 1percent monitoring allowance,
semiannual reporting.
Option 3: 20-percent opacity with a 1percent monitoring allowance, quarterly
reporting.
For purposes of estimating costs and
impacts of the regulatory options, we
assumed that recovery furnaces and
ESP-controlled lime kilns that did not
meet the regulatory options in our
COMS analysis would require ESP
maintenance and testing to improve
opacity performance, or an ESP
upgrade. The EPA also reviewed PM
performance levels (based on PM stack
test data) for emission units not meeting
the opacity limits under consideration
in at least one reporting period. If the
PM performance level achieved met the
PM performance expected from an
upgraded ESP (0.015 gr/dscf at 8percent O2 for recovery furnaces or
0.010 gr/dscf at 10-percent O2 for lime
kilns), then we assumed that the ESP
would only require improved annual
maintenance and testing to achieve the
opacity options. Otherwise, we assumed
that units would require an ESP upgrade
to meet the opacity options.
Although we are not proposing any
changes to the PM metal HAP limits as
part of the technology review, ESP
upgrades to meet a tighter opacity
monitoring limit would have the effect
of reducing PM emissions. We estimated
recovery furnace upgrade costs for
adding two parallel fields to an existing
ESP resulting in a PM performance level
of 0.015 gr/dscf at 8-percent O2. For
lime kilns, we estimated costs based on
adding one field to the existing ESP to
achieve a PM performance level of 0.01
gr/dscf at 10-percent O2. For each
emission unit expected to require an
ESP upgrade, we estimated the potential
reduction in PM emissions by
subtracting the PM limit expected to be
achieved by the upgraded ESP from the
lower of the current PM permit limit or
the actual PM performance level for the
emission unit.
The EPA’s full analysis of the cost and
impacts associated with the regulatory
options for opacity (including energy
and secondary air impacts) is presented
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in a memorandum in the docket.38 Table and cost effectiveness of the opacity
5 summarizes the number of impacted
regulatory options.
facilities, estimated cost, PM reductions,
TABLE 5—COSTS AND IMPACTS OF OPACITY REGULATORY OPTIONS
2015$
Number of
mills impacted
Option
Capital costs,
$million
Incremental
HAP reduction,
tpy
Annualized
costs,
$million/yr
Cost
effectiveness
$/ton PM1
Recovery Furnaces Opacity Monitoring Limit Options
Baseline Option 1: No change. 35% opacity,
20% corrective action level (CAL), 6% monitoring allowance (MA), quarterly (Q) reporting.
Option 2: 35% opacity, 20% CAL, 2% MA, semiannual (SA) reporting.
Option 3: 20% opacity, 6% MA, Q reporting ......
Option 4: 20% opacity, 2% MA, SA reporting ....
Option 5: 20% opacity, 2% MA, Q reporting ......
0
0
0
0 .....................................
NA
1
0
0.087
0 .....................................
NA
7
12
19
27
42
74
5.4
8.7
15
188 (PM), 85 (PM2.5) .....
235 (PM), 112 (PM2.5) ...
364 (PM), 170 (PM2.5) ...
28,400
36,800
41,000
Lime Kiln Opacity Monitoring Limit Options
Option 1: No change. 20% opacity, 6% MA, Q
reporting.
Option 2: 20% opacity, 1% MA, SA reporting ....
0
0
0
0 .....................................
NA
2
0
0.068
0 .....................................
NA
Option 3: 20% opacity, 1% MA, Q reporting ......
Same as option 2
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1 HAP metals comprise less than 0.5-percent of the PM emissions (0.03-percent for recovery furnaces or 0.48-percent for lime kilns). Thus, the
cost effectiveness specifically for HAP metals is orders of magnitude greater than that shown for PM (>$5.5 million per ton HAP metals).
After considering the costs and
impacts of the regulatory options for
opacity, we are proposing recovery
furnace option 4 and lime kiln option 2
for opacity monitoring. These options
are representative of the actual
performance of 40 CFR part 63, subpart
MM emission units based on our
analysis of the COMS data, and also
align closely with the opacity limits,
monitoring allowances, and semiannual
reporting requirements established for
new sources through the 2014 NSPS
review. The EPA is proposing to reduce
the opacity limit for existing recovery
furnaces from 35-percent to 20-percent
opacity. Lowering the recovery furnace
opacity limit to 20 percent eliminates
the need for the 20-percent corrective
action level. Specifying a 20-percent
corrective action level is redundant
where the opacity limit is already set at
20-percent; therefore, we are proposing
to eliminate the subpart MM corrective
action level in 40 CFR 63.864(k)(1)(i) by
reserving this section. We are proposing
a monitoring allowance of 2-percent for
existing and new recovery furnaces. We
are proposing to retain the 20-percent
opacity limit and are proposing a
monitoring allowance of 1 percent for
opacity monitoring for lime kilns. We
are also proposing to reduce the
reporting frequency from quarterly to
semiannually, as discussed in section
IV.D.4 of this preamble. The proposed
semiannual averaging period would be
used for calculating the opacity
monitoring allowance, providing
flexibility for startup and shutdown
periods. The cost effectiveness of
recovery furnace option 4, $36,800 per
ton PM, is within the range of other
recent EPA regulations. There is no cost
effectiveness value for lime kiln option
2 because no incremental HAP
reductions were estimated. In addition
to proposing the revisions described
above, the EPA is requesting comment
on all of the options presented in Table
5.
ESP parameter monitoring. The EPA
is proposing to add an ESP parameter
monitoring requirement for recovery
furnaces and lime kilns equipped with
ESPs. The purpose of this is to provide
another indicator of ESP performance
and enable affected sources to show
continuous compliance with the HAP
metal standards (surrogate PM emission
limit) at all times, including periods
when the opacity monitoring allowance
is used. The EPA is proposing that these
sources monitor the secondary voltage
and secondary current (or, alternatively,
total secondary power) of each ESP
collection field. These ESP parameter
monitoring requirements are in addition
to opacity monitoring for recovery
furnaces equipped with ESPs alone. The
EPA is proposing that these ESP
parameters be monitored, recorded
every successive 15 minutes, and
averaged over the same semiannual
period as the opacity monitoring
allowance. The semiannual average of
the ESP parameters must remain above
the minimum limits established during
the PM performance test (i.e., above the
minimum secondary current and
secondary voltage or above minimum
total secondary power).
The EPA estimates that the
nationwide costs associated with adding
the proposed ESP parameter monitoring
requirements would be $5.7 million
capital and $1.4 million annualized
costs for ESP parameter monitors. All
mills with ESP-controlled recovery
furnaces and lime kilns are estimated to
be impacted.
Monitoring of ESPs followed by wet
scrubbers. Because moisture in wet
stacks interferes with opacity readings,
opacity is not a suitable monitoring
requirement for recovery furnaces or
lime kilns with wet scrubber stacks. The
EPA is therefore proposing to require
ESP and wet scrubber parameter
monitoring for emission units equipped
with an ESP followed by a wet scrubber.
The ESP parameters to be monitored are
38 See memorandum titled, Costs/Impacts of the
Subpart MM Residual Risk and Technology Review,
in the docket.
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secondary voltage and secondary
current (or, alternatively, total
secondary power), and the wet scrubber
parameters are pressure drop and
scrubber liquid flow rate. The EPA is
proposing that ESP and wet scrubber
parameters be recorded at least once
every successive 15-minute period and
reduced to 3-hour averages. The EPA
estimates no incremental costs to be
associated specifically with the
proposed monitoring requirements for
combined ESP-wet scrubber systems
because the ESP parameter monitoring
costs estimated above include ESPs in
combined control systems, and wet
scrubber parameter monitoring is
already required under 40 CFR part 63,
subpart MM.
4. Kraft and Soda Smelt Dissolving
Tanks
Smelt dissolving tanks are covered
vessels located below the recovery
furnace to collect molten smelt, one of
the main products from the combustion
of black liquor. Smelt is comprised
predominantly of Na2S and Na2CO3 and
is formed in the bottom of the recovery
furnace. The smelt is continuously
discharged through water-cooled smelt
spouts into the SDT where it is mixed
with weak wash water from the pulp
mill recausticizing area to form green
liquor, an aqueous solution of Na2CO3
and Na2S. The green liquor is
subsequently transferred to the
recausticizing area for reprocessing into
pulping liquor (i.e., white liquor). In the
soda pulping process, the molten smelt
and green liquor is predominantly
Na2CO3 because soda pulping is a nonsulfur process. Based on the 2011 Pulp
and Paper Sector ICR data, there are 161
kraft and soda SDTs in the United
States. Nearly all of the SDTs have wet
scrubbers that control the particulate
emissions, including HAP metals, from
this process. A small number of SDTs
use mist eliminators as the only means
of emissions control. Some new sources
were designed to vent emissions
through the recovery furnace as an
alternative to using wet scrubber control
alone, but also have a wet scrubber for
backup periods when venting to the
recovery furnace is not feasible.
SDT PM. The current 40 CFR part 63,
subpart MM PM emission limit (which
is a surrogate for HAP metals) for
existing SDTs is 0.20 lb/ton BLS. The
subpart MM PM limit for new and
reconstructed sources with initial
startup in 2001 or later is 0.12 lb/ton
BLS based on the use of a highefficiency wet scrubber.
The EPA analyzed SDT PM stack test
data collected with the 2011 Pulp and
Paper Sector ICR for the NSPS review
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promulgated on April 4, 2014 (79 FR
18952). We reviewed this same dataset
in the context of subpart MM for
purposes of the 40 CFR part 63, subpart
MM technology review. The stack test
data show that nearly all SDTs have
achieved the subpart MM existing
source limit of 0.20 lb/ton BLS (with the
exception of a few SDTs with mist
eliminators and SDTs included in the
PM bubble compliance option under
subpart MM). There were many existing
scrubber-controlled SDTs with
emissions between the new source limit
of 0.12 lb/ton BLS and the existing
source limit of 0.20 lb/ton BLS. The
practice of routing SDT emissions
through the recovery furnace has an
unquantified effect on PM emissions
because no emission test data are
available to differentiate SDT emissions
from the recovery furnace emissions in
these systems. The EPA has identified
no practices, processes, or controls for
SDTs beyond those identified at the
time of subpart MM development, nor
any incremental improvements in the
ability of wet scrubbers to reduce PM.
Therefore, the EPA is not proposing any
changes to the current existing and new
source PM limits in subpart MM for
kraft and soda mill SDTs. The EPA has
identified no regulatory options for
SDTs for further consideration under
the subpart MM technology review.
SDT parameter monitoring. Subpart
MM specifies monitoring of scrubber
liquid flow rate and pressure drop for
SDTs equipped with wet scrubbers.
Facilities may have difficulty meeting
the minimum pressure drop
requirement during startup and
shutdown, as expected due to the
reduced (and changing) volumetric flow
of stack gases during startup and
shutdown. The EPA is proposing to
consider only scrubber liquid flow rate
during these periods (i.e., excess
emissions would include any 3-hour
period when BLS are fired that the
scrubber flow rate does not meet the
minimum parameter limits set in the
initial performance test). This is
discussed further in section IV.D.1.
Based on previous alternative
monitoring requests for SDTs, the EPA
is also proposing to allow operators to
use SDT scrubber fan amperage as an
alternative to pressure drop
measurement for SDT dynamic
scrubbers operating at ambient pressure
or for low-energy entrainment scrubbers
on SDTs where the fan speed does not
vary.
5. Sulfite Combustion Units
When subpart MM was proposed in
1998, there were 15 sulfite pulp mills.
Today there are only three sulfite mills,
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including one using the magnesiumbased sulfite process and two mills
using the ammonia (NH3)-based sulfite
process. The EPA projects no new
sulfite mills to come online in the
United States in the next 5 years. Based
on a review of permits and ICR data that
the EPA has collected for these three
sulfite mills, we determined that there
are a total of eight sulfite combustion
units currently operating in the United
States.
Sulfite combustion unit PM. Subpart
MM of 40 CFR part 63 requires existing
sulfite combustion units to meet a PM
emission limit of 0.040 gr/dscf at 8percent O2, based on the use of a fiberbed demister system. Subpart MM
requires new sulfite combustion units to
meet a PM limit of 0.020 gr/dscf at 8percent O2, based on the combined use
of a wet scrubber and fiber-bed demister
system.39 The PM emission limits are a
surrogate for HAP metals.
For the 40 CFR part 63 subpart MM
technology review, the EPA reviewed
ICR data on sulfite processes and
controls, title V permit limits, and PM
stack test data for the three sulfite pulp
mills currently operating in the United
States. Each sulfite mill has a unique
configuration of sulfite combustion
units and corresponding site-specific
limits. Two facilities with sulfite
combustion units subject to a PM permit
limit of 0.04 gr/dscf achieved this limit
based on actual measurement data
submitted (with the exception of one
test above the limit that was superseded
by a more recent test). Another facility
(Cosmo Specialty Fibers in Cosmopolis,
Washington) has a site-specific PM
permit limit of 0.10 gr/dscf for its
chemical recovery combustion units,
and instead reduces PM emissions from
the hog fuel dryer at the plant site. The
chemical recovery combustion units
(which have a combined stack) have
achieved average PM emissions of 0.054
gr/dscf. The hog fuel dryer is permitted
at 10 pounds per hour (lb/hr) of PM and
has achieved PM emissions of 1.2 and
1.5 lb/hr in two tests. The EPA’s
technology review found no
developments in practices, processes, or
controls since the promulgation of
subpart MM for PM emissions from
sulfite combustion units. The EPA is
proposing to retain the 0.040 and 0.020
gr/dscf at 8-percent O2 PM limits for
existing and new sulfite combustion
units. The EPA has identified no
39 Although any control system could be used to
meet the emission limits for sulfite combustion
units, the existing source limit is consistent with
the performance of a fiber-bed demister system and
the new source limit is consistent with the
performance of a wet scrubber with a fiber-bed
demister.
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regulatory options for sulfite
combustion units for further
consideration under the subpart MM
technology review.
Sulfite combustion unit parameter
monitoring. Subpart MM of 40 CFR part
63 specifies monitoring of scrubber
liquid flow rate and pressure drop for
sulfite combustion units equipped with
wet scrubbers. Facilities may have
difficulty meeting the minimum
pressure drop requirement during
startup and shutdown, as expected due
to the reduced (and changing)
volumetric flow of stack gases during
startup and shutdown. The EPA is
proposing to consider only scrubber
liquid flow rate during startup and
shutdown periods (i.e., excess emissions
would include any 3-hour period when
spent pulping liquor is fired that the
scrubber flow rate does not meet the
minimum parameter limits set in the
initial performance test). The EPA is
proposing no changes for parameter
monitoring of the fiber-bed demister
system, which is addressed under the
alternative monitoring provisions of
subpart MM.
6. Semichemical Combustion Units
When 40 CFR part 63, subpart MM,
was originally proposed in 1998, there
were 14 semichemical combustion units
at 14 stand-alone semichemical pulp
mills. Today, there are seven
semichemical combustion units at seven
mills in the United States, at six of
which combustion units and mills are
operating.40 Semichemical combustion
unit design types include: Fluidized-bed
reactor (two units, one operating),
recovery furnace (four units), and rotary
liquor kiln (one unit).
Semichemical combustion unit total
hydrocarbon (THC). The current 40 CFR
part 63, subpart MM standards require
existing and new semichemical
combustion units to reduce total
gaseous organic HAP emissions
(measured as THC) by 90 percent or
meet a total gaseous organic HAP
emission limit (measured as THC) of
2.97 lb/ton of BLS fired.
For the 40 CFR part 63, subpart MM
RTR, the EPA reviewed ICR data on
processes and control configurations,
title V permit limits, and THC stack test
data for the stand-alone semichemical
pulp mills currently operating in the
United States. The review of permit
limits indicated that all semichemical
combustion units are subject to the 2.97
lb/ton BLS THC limit specified in
subpart MM for existing and new units.
Performance of the different
40 One additional stand-alone semichemical
pump mill ceased operation in late 2015.
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semichemical combustion units varies
considerably for THC. While most units
achieve the 2.97 lb/ton BLS THC limit,
at least one unit relied on the 90-percent
reduction compliance option included
in subpart MM to address variability.
The EPA has identified no regulatory
options for semichemical combustion
units for purposes of the subpart MM
RTR, given that no practices, processes,
or controls beyond those considered
during the original rule development
have emerged.
Semichemical combustion unit
parameter monitoring. Subpart MM of
40 CFR part 63 requires semichemical
combustion units using RTOs to
measure and record RTO operating
temperature to demonstrate compliance
with the standard for gaseous organic
HAP (measured as THC). As noted
previously, no practices, processes, or
controls beyond those considered
during the original rule development
have emerged. Consequently, the EPA is
proposing no changes for the current
parameter monitoring requirements.
D. What other actions are we proposing?
In addition to the proposed actions
described above, we are proposing
additional revisions. We are proposing
revisions to the SSM provisions of the
MACT rule in order to ensure that they
are consistent with the court decision in
Sierra Club v. EPA, 551 F.3d 1019 (D.C.
Cir. 2008), which vacated two
provisions that exempted sources from
the requirement to comply with
otherwise applicable CAA section
112(d) emission standards during
periods of SSM. We also are proposing
various other changes, including 5-year
periodic emissions testing for selected
process equipment, semiannual
electronic reporting for all excess
emissions reports, electronic submittal
of compliance reports (which include
performance test reports), incorporation
by reference, and various technical and
editorial changes. Our analyses and
proposed changes related to these issues
are discussed in sections IV.D.1 through
6 of this preamble.
1. Startup, Shutdown, and Malfunction
In its 2008 decision in Sierra Club v.
EPA, 551 F.3d 1019 (D.C. Cir. 2008), the
United States Court of Appeals for the
District of Columbia Circuit vacated
portions of two provisions in the EPA’s
CAA section 112 regulations governing
the emissions of HAPs during periods of
SSM. Specifically, the Court vacated the
SSM exemption contained in 40 CFR
63.6(f)(1) and 40 CFR 63.6(h)(1), holding
that under section 302(k) of the CAA,
emissions standards or limitations must
be continuous in nature and that the
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SSM exemption violates the CAA’s
requirement that some CAA section 112
standards apply continuously.
We are proposing the elimination of
the SSM exemption in this rule.
Consistent with Sierra Club v. EPA, we
are proposing standards in this rule that
apply at all times. We are also proposing
several revisions to Table 1 (the General
Provisions Applicability Table) as is
explained in more detail below. For
example, we are proposing to eliminate
the incorporation of the General
Provisions’ requirement that the source
develop an SSM plan. We also are
proposing to eliminate and revise
certain recordkeeping and reporting
requirements related to the SSM
exemption as further described below.
The EPA has attempted to ensure that
the provisions we are proposing to
eliminate are inappropriate,
unnecessary, or redundant in the
absence of the SSM exemption. We are
specifically seeking comment on
whether we have successfully done so.
Periods of startup and shutdown. In
reviewing the standards in this rule, the
EPA has taken into account startup and
shutdown periods and, for the reasons
explained below, is not proposing
alternate standards for those periods.
Subpart MM of 40 CFR part 63
requires continuous opacity monitoring
to indicate ongoing compliance with the
PM emission limits. In developing
proposed standards for subpart MM, the
EPA reviewed numerous continuous
opacity monitoring datasets that
included periods of startup and
shutdown, and concluded that the
affected units will be able to comply
with the proposed standards at all
times. The proposed subpart MM also
requires RTO operating temperature and
ESP and wet scrubber parameter
monitoring. Parameter limits apply at all
times, including during startup and
shutdown. The proposed subpart MM
requires RTO operating temperature and
wet scrubber and ESP operating
parameters to be recorded at least once
every 15 minutes. Subpart MM specifies
corrective action levels in 40 CFR
63.864(k)(1) and violation levels in 40
CFR 63.864(k)(2) which would be
reported as excess emissions under 40
CFR 63.867(c). For RTO temperature,
subpart MM requires corrective action
when any 1-hour temperature falls
below the average temperature
established during the performance test.
Subpart MM considers any 3-hour RTO
temperature that falls below the average
established during the performance test
to be a violation. Subpart MM requires
the ESP and scrubber parameters to be
averaged over a 3-hour block, except for
ESPs with COMS, which would have
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ESP parameters averaged semiannually.
The corrective action level for wet
scrubber and ESP operating parameters
(when opacity is not also measured) is
triggered when any 3-hour average is
outside of the limit established during
the performance test. A violation would
occur when six or more of the 3-hour
average parameter values within a 6month period are outside of the limits
established during the performance test.
Violations based on opacity would be
considered over a semiannual period.
For new or existing kraft or soda
recovery furnaces, a violation would
occur when any opacity is greater than
20 percent for 2 percent or more of the
operating time when spent liquor is
fired within a semiannual period. For
new or existing lime kilns, a violation
would occur when any opacity is greater
than 20 percent for 1 percent or more of
the operating time when lime mud is
fired in a semiannual period. A
violation would also occur when the
recovery furnace or lime kiln ESP
secondary voltage and secondary
current (or total secondary power)
averaged over the semiannual period are
below the minimum operating limits
established during the performance test,
with the exception of secondary current
(or total secondary power) during
periods of startup and shutdown.
To address the need for ESPs to warm
to a specified temperature (typically
above 200 °F) before full power is
applied to the transformer-rectifier set,
the EPA is proposing to define excess
emissions (i.e., the corrective action and
violation levels) as opacity and ESP
parameter measurements below the
minimum requirements during times
when BLS or lime mud is fired (as
applicable), based on several responses
to the ICR indicating that mills with ESP
minimum temperature requirements
bring the ESP online before introducing
BLS or lime mud into the recovery
furnace or lime kiln, respectively. The
EPA is also proposing language that
would allow affected units to use wet
scrubber liquid flow rate to demonstrate
compliance during periods of startup
and shutdown because pressure drop is
difficult to achieve during these periods.
Periods of malfunction. Periods of
startup, normal operations, and
shutdown are all predictable and
routine aspects of a source’s operations.
Malfunctions, in contrast, are neither
predictable nor routine. Instead they
are, by definition, sudden, infrequent,
and not reasonably preventable failures
of emissions control, process or
monitoring equipment. (40 CFR 63.2)
(Definition of malfunction). The EPA
interprets CAA section 112 as not
requiring emissions that occur during
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periods of malfunction to be factored
into development of CAA section 112
standards. Under CAA section 112,
emissions standards for new sources
must be no less stringent than the level
‘‘achieved’’ by the best controlled
similar source and for existing sources
generally must be no less stringent than
the average emission limitation
‘‘achieved’’ by the best performing 12
percent of sources in the category. There
is nothing in CAA section 112 that
directs the Agency to consider
malfunctions in determining the level
‘‘achieved’’ by the best performing
sources when setting emission
standards. As the District of Columbia
Circuit Court has recognized, the phrase
‘‘average emissions limitation achieved
by the best performing 12 percent of’’
sources ‘‘says nothing about how the
performance of the best units is to be
calculated.’’ Nat’l Ass’n of Clean Water
Agencies v. EPA, 734 F.3d 1115, 1141
(D.C. Cir. 2013). While the EPA
accounts for variability in setting
emissions standards, nothing in CAA
section 112 requires the Agency to
consider malfunctions as part of that
analysis. A malfunction should not be
treated in the same manner as the type
of variation in performance that occurs
during routine operations of a source. A
malfunction is a failure of the source to
perform in a ‘‘normal or usual manner’’
and no statutory language compels the
EPA to consider such events in setting
section CAA 112 standards.
Further, accounting for malfunctions
in setting emission standards would be
difficult, if not impossible, given the
myriad of different types of
malfunctions that can occur across all
sources in the category and given the
difficulties associated with predicting or
accounting for the frequency, degree,
and duration of various malfunctions
that might occur. As such, the
performance of units that are
malfunctioning is not ‘‘reasonably’’
foreseeable. See, e.g., Sierra Club v.
EPA, 167 F.3d 658, 662 (D.C. Cir. 1999)
(‘‘The EPA typically has wide latitude
in determining the extent of datagathering necessary to solve a problem.
We generally defer to an agency’s
decision to proceed on the basis of
imperfect scientific information, rather
than to ‘invest the resources to conduct
the perfect study.’ ’’) See also,
Weyerhaeuser v. Costle, 590 F.2d 1011,
1058 (D.C. Cir. 1978) (‘‘In the nature of
things, no general limit, individual
permit, or even any upset provision can
anticipate all upset situations. After a
certain point, the transgression of
regulatory limits caused by
‘uncontrollable acts of third parties,’
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such as strikes, sabotage, operator
intoxication or insanity, and a variety of
other eventualities, must be a matter for
the administrative exercise of case-bycase enforcement discretion, not for
specification in advance by
regulation.’’). In addition, emissions
during a malfunction event can be
significantly higher than emissions at
any other time of source operation. For
example, if an air pollution control
device with 99-percent removal goes offline as a result of a malfunction (as
might happen if, for example, the bags
in a baghouse catch fire) and the
emission unit is a steady state type unit
that would take days to shut down, the
source would go from 99-percent
control to zero control until the control
device was repaired. The source’s
emissions during the malfunction
would be 100 times higher than during
normal operations. As such, the
emissions over a 4-day malfunction
period would exceed the annual
emissions of the source during normal
operations. As this example illustrates,
accounting for malfunctions could lead
to standards that are not reflective of
(and significantly less stringent than)
levels that are achieved by a wellperforming non-malfunctioning source.
It is reasonable to interpret CAA section
112 to avoid such a result. The EPA’s
approach to malfunctions is consistent
with CAA section 112 and is a
reasonable interpretation of the statute.
In the event that a source fails to
comply with the applicable CAA section
112(d) standards as a result of a
malfunction event, the EPA would
determine an appropriate response
based on, among other things, the good
faith efforts of the source to minimize
emissions during malfunction periods,
including preventative and corrective
actions, as well as root cause analyses
to ascertain and rectify excess
emissions. The EPA would also
consider whether the source’s failure to
comply with the CAA section 112(d)
standard was, in fact, sudden,
infrequent, not reasonably preventable,
and was not instead caused in part by
poor maintenance or careless operation.
40 CFR 63.2 (definition of malfunction).
If the EPA determines in a particular
case that an enforcement action against
a source for violation of an emission
standard is warranted, the source can
raise any and all defenses in that
enforcement action and the Federal
District Court will determine what, if
any, relief is appropriate. The same is
true for citizen enforcement actions.
Similarly, the presiding officer in an
administrative proceeding can consider
any defense raised and determine
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whether administrative penalties are
appropriate.
In summary, the EPA interpretation of
the CAA and, in particular, CAA section
112 is reasonable and encourages
practices that will avoid malfunctions.
Administrative and judicial procedures
for addressing exceedances of the
standards fully recognize that violations
may occur despite good faith efforts to
comply and can accommodate those
situations.
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a. General Duty
We are proposing to revise the
General Provisions table (Table 1) entry
for 40 CFR 63.6(e) by re-designating it
as 40 CFR 63.6(e)(1)(i) and changing the
‘‘yes’’ in column 3 to a ‘‘no.’’ Section
63.6(e)(1)(i) describes the general duty
to minimize emissions. Some of the
language in that section is no longer
necessary or appropriate in light of the
elimination of the SSM exemption. We
are proposing instead to add general
duty regulatory text at 40 CFR 63.860(d)
that reflects the general duty to
minimize emissions while eliminating
the reference to periods covered by an
SSM exemption. The current language
in 40 CFR 63.6(e)(1)(i) characterizes
what the general duty entails during
periods of SSM. With the elimination of
the SSM exemption, there is no need to
differentiate between normal operations
and SSM events in describing the
general duty. Therefore, the language
the EPA is proposing for 40 CFR
63.860(d) does not include that language
from 40 CFR 63.6(e)(1).
We are also proposing to revise the
General Provisions table (Table 1) to add
an entry for 40 CFR 63.6(e)(1)(ii) and
include a ‘‘no’’ in column 3. Section
63.6(e)(1)(ii) imposes requirements that
are not necessary with the elimination
of the SSM exemption or are redundant
with the general duty requirement being
added at 40 CFR 63.860(d).
b. SSM Plan
We are proposing to revise the
General Provisions table (Table 1) to add
an entry for 40 CFR 63.6(e)(3) and
include a ‘‘no’’ in column 3. Generally,
the paragraphs under 40 CFR 63.6(e)(3)
require development of an SSM plan
and specify SSM recordkeeping and
reporting requirements related to the
SSM plan. As noted, the EPA is
proposing to remove the SSM
exemptions. Therefore, affected units
will be subject to an emission standard
during such events. The applicability of
a standard during such events will
ensure that sources have ample
incentive to plan for and achieve
compliance and, thus, the SSM plan
requirements are no longer necessary.
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c. Compliance With Standards
We are proposing to revise the
General Provisions table (Table 1)
entries for 40 CFR 63.6(f) and (h) by redesignating these sections as 40 CFR
63.6(f)(1) and (h)(1) and including a
‘‘no’’ in column 3. The current language
of 40 CFR 63.6(f)(1) and (h)(1) exempts
sources from non-opacity and opacity
standards during periods of SSM. As
discussed above, the court in Sierra
Club vacated the exemptions contained
in this provision and held that the CAA
requires that some CAA section 112
standard apply continuously. Consistent
with Sierra Club, the EPA is proposing
to revise standards in this rule to apply
at all times.
d. Performance Testing
We are proposing to revise the
General Provisions table (Table 1) entry
for 40 CFR 63.7(e) by re-designating it
as 40 CFR 63.7(e)(1) and including a
‘‘no’’ in column 3. Section 63.7(e)(1)
describes performance testing
requirements. The EPA is instead
proposing to add a performance testing
requirement at 40 CFR 63.865. The
proposed performance testing
provisions require testing under
representative operating conditions,
excluding periods of startup and
shutdown. As in 40 CFR 63.7(e)(1),
performance tests conducted under this
subpart should not be conducted during
malfunctions because conditions during
malfunctions are often not
representative of normal operating
conditions. The EPA is proposing to add
language that requires the owner or
operator to record the process
information that is necessary to
document operating conditions during
the test and include in such record an
explanation to support that such
conditions represent normal operation.
Section 63.7(e) requires that the owner
or operator make available to the
Administrator such records ‘‘as may be
necessary to determine the condition of
the performance test’’ available to the
Administrator upon request, but does
not specifically require the information
to be recorded. The regulatory text the
EPA is proposing to add to this
provision builds on that requirement
and makes explicit the requirement to
record the information.
e. Monitoring
We are proposing to revise the
General Provisions table (Table 1) by redesignating 40 CFR 63.8(c) as 40 CFR
63.8(c)(1), adding entries for 40 CFR
63.8(c)(1)(i) through (iii) and including
‘‘no’’ in column 3 for paragraphs (i) and
(iii). The cross-references to the general
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duty and SSM plan requirements in
those subparagraphs are not necessary
in light of other requirements of 40 CFR
63.8 that require good air pollution
control practices (40 CFR 63.8(c)(1)) and
that set out the requirements of a quality
control program for monitoring
equipment (40 CFR 63.8(d)).
We are also proposing to revise the
General Provisions table (Table 1) by
adding an entry for 40 CFR 63.8(d)(3)
and including a ‘‘no’’ in column 3. The
final sentence in 40 CFR 63.8(d)(3)
refers to the General Provisions’ SSM
plan requirement which is no longer
applicable. The EPA is proposing to add
to the rule at 40 CFR 63.864(f) text that
is identical to 40 CFR 63.8(d)(3) except
that the final sentence is replaced with
the following sentence: ‘‘The program of
corrective action should be included in
the plan required under 40 CFR
63.8(d)(2).’’
f. Recordkeeping
We are proposing to revise the
General Provisions table (Table 1) by
adding an entry for 40 CFR 63.10(b)(2)(i)
and including a ‘‘no’’ in column 3.
Section 63.10(b)(2)(i) describes the
recordkeeping requirements during
startup and shutdown. These recording
provisions are no longer necessary
because the EPA is proposing that
recordkeeping and reporting applicable
to normal operations will apply to
startup and shutdown. Special
provisions applicable to startup and
shutdown, such as a startup and
shutdown plan, have been removed
from the rule (with exceptions
discussed below) thereby reducing the
need for additional recordkeeping for
startup and shutdown periods.
Records of startup and shutdown
periods are proposed to be required
under 40 CFR 63.866(c)(8) to help
characterize minor exceptions to
reporting. The EPA is proposing no
reporting of wet scrubber pressure drop
or ESP secondary current (or total
secondary power) during periods of
startup and shutdown because it is not
feasible to meet operating limits
established under normal operation for
these parameters during startup and
shutdown. Instead, the EPA is
proposing that wet scrubber liquid flow
rate (or fan amperage) and ESP
secondary voltage be monitored during
startup and shutdown.
We are also proposing to revise the
General Provisions table (Table 1) by
adding an entry for 40 CFR
63.10(b)(2)(ii) and including a ‘‘no’’ in
column 3. Section 63.10(b)(2)(ii)
describes the recordkeeping
requirements during a malfunction. The
EPA is proposing to add such
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requirements to 40 CFR 63.866(d). The
regulatory text we are proposing to add
differs from the General Provisions it is
replacing in that the General Provisions
requires the creation and retention of a
record of the occurrence and duration of
each malfunction of process, air
pollution control, and monitoring
equipment. The EPA is proposing that
this requirement apply to any failure to
meet an applicable standard and is
requiring that the source record the
date, time, and duration of the failure
rather than the ‘‘occurrence.’’ The EPA
is also proposing to add to 40 CFR
63.866(d) a requirement that sources
keep records that include a list of the
affected source or equipment and
actions taken to minimize emissions, an
estimate of the quantity of each
regulated pollutant emitted over the
emission limit for which the source
failed to meet the standard, and a
description of the method used to
estimate the emissions. Examples of
such methods would include productloss calculations, mass balance
calculations, measurements when
available, or engineering judgment
based on known process parameters.
The EPA is proposing to require that
sources keep records of this information
to ensure that there is adequate
information to allow the EPA to
determine the severity of any failure to
meet a standard, and to provide data
that may document how the source met
the general duty to minimize emissions
when the source has failed to meet an
applicable standard.
We are also proposing to revise the
General Provisions table (Table 1) by
adding an entry for 40 CFR
63.10(b)(2)(iv) and (v) and including a
’’no’’ in column 3. When applicable, the
provision requires sources to record
actions taken during SSM events when
actions were inconsistent with their
SSM plan. The requirement is no longer
appropriate because SSM plans will no
longer be required. The requirement
previously applicable under 40 CFR
63.10(b)(2)(iv)(B) to record actions to
minimize emissions and record
corrective actions is now applicable by
reference to 40 CFR 63.866(d).
We are also proposing to revise the
General Provisions table (Table 1) by
adding an entry for 40 CFR 63.10(c)(15)
and including a ‘‘no’’ in column 3. The
EPA is proposing that 40 CFR
63.10(c)(15) no longer apply. When
applicable, the provision allows an
owner or operator to use the affected
source’s SSM plan or records kept to
satisfy the recordkeeping requirements
of the SSM plan, specified in 40 CFR
63.6(e), to also satisfy the requirements
of 40 CFR 63.10(c)(10) through (12). The
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EPA is proposing to eliminate this
requirement because SSM plans would
no longer be required, and, therefore, 40
CFR 63.10(c)(15) no longer serves any
useful purpose for affected units.
g. Reporting
We are proposing to revise the
General Provisions table (Table 1) entry
for 40 CFR 63.10(d)(5) by re-designating
it as 40 CFR 63.10(d)(5)(i) and changing
the ‘‘yes’’ in column 3 to a ‘‘no.’’ Section
63.10(d)(5)(i) describes the periodic
reporting requirements for startups,
shutdowns, and malfunctions. To
replace the General Provisions reporting
requirement, the EPA is proposing to
add reporting requirements to 40 CFR
63.867(c). The replacement language
differs from the General Provisions
requirement in that it eliminates
periodic SSM reports as a stand-alone
report. We are proposing language that
requires sources that fail to meet an
applicable standard at any time to report
the information concerning such events
in the semiannual report to be required
under the proposed rule. We are
proposing that the report must contain
the number, date, time, duration, and
the cause of such events (including
unknown cause, if applicable), a list of
the affected source or equipment, an
estimate of the quantity of each
regulated pollutant emitted over any
emission limit, and a description of the
method used to estimate the emissions.
Examples of such methods would
include product-loss calculations, mass
balance calculations, measurements
when available, or engineering
judgment based on known process
parameters. The EPA is proposing this
requirement to ensure that there is
adequate information to determine
compliance, to allow the EPA to
determine the severity of the failure to
meet an applicable standard, and to
provide data that may document how
the source met the general duty to
minimize emissions during a failure to
meet an applicable standard.
We will no longer require owners or
operators to determine whether actions
taken to correct a malfunction are
consistent with an SSM plan, because
plans would no longer be required. The
proposed amendments, therefore,
eliminate the cross reference to 40 CFR
63.10(d)(5)(i) that contains the
description of the previously required
SSM report format and submittal
schedule from this section. These
specifications are no longer necessary
because the events will be reported in
otherwise required reports with similar
format and submittal requirements.
We are also proposing to revise the
General Provisions table (Table 1) to add
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an entry for 40 CFR 63.10(d)(5)(ii) and
include a ‘‘no’’ in column 3. Section
63.10(d)(5)(ii) describes an immediate
report for startups, shutdown, and
malfunctions when a source failed to
meet an applicable standard, but did not
follow the SSM plan. We will no longer
require owners and operators to report
when actions taken during a startup,
shutdown, or malfunction were not
consistent with an SSM plan, because
plans would no longer be required.
2. 5-Year Periodic Emissions Testing
As part of an ongoing effort to
improve compliance with various
federal air emission regulations, the
EPA reviewed the testing and
monitoring requirements of 40 CFR part
63, subpart MM and is proposing the
following change. The EPA is proposing
to require facilities complying with the
standards for chemical recovery
combustion sources at kraft, soda,
sulfite, and stand-alone semichemical
pulp mills to conduct periodic air
emissions performance testing, with the
first of the periodic performance tests to
be conducted within 3 years of the
effective date of the revised standards
and thereafter before the facilities renew
their 40 CFR part 70 operating permits,
but no longer than 5 years following the
previous performance test. Periodic
performance tests are already required
by permitting authorities for some
facilities. Further, the EPA believes that
requiring periodic performance tests
will help to ensure that control systems
are properly maintained over time,
thereby reducing the potential for acute
emissions episodes. This proposal
would require periodic air emissions
testing for filterable PM once every 5
years for existing and new kraft and
soda recovery furnaces, SDTs, and lime
kilns and sulfite combustion units. In
addition, this proposal would require
air emissions testing for methanol once
every 5 years for new kraft and soda
recovery furnaces. This proposal would
also require periodic air emissions
testing for THC for existing and new
semichemical combustion units.
3. Continuous Parameter Monitoring
System (CPMS) Operating Limits
We are proposing to specify
procedures for establishing operating
limits based on data recorded by CPMS.
The 40 CFR part 63, subpart MM
emission standards are comprised of
numerical emission limits, with
compliance demonstrated through
periodic performance tests, and
operating limits such as opacity limits
or continuously monitored parameter
limits used to demonstrate ongoing
compliance in between performance
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tests. Currently, the subpart MM
regulatory text refers extensively to
operating parameter ranges and is not as
specific as more recent NESHAPs in
specifying how operating limits are to
be determined. Therefore, we are
proposing language to clarify the
procedures for establishing parameter
limits.
As noted previously, we are
proposing ESP parameter monitoring
requirements for recovery furnaces and
lime kilns with ESPs or combined ESP
and wet scrubber controls. This
proposal would require ESP parameters
be recorded at least once every
successive 15-minute period, and the
recorded readings be reduced to
semiannual averages for ESPs (i.e.,
where opacity monitoring requirements
also apply) or 3-hour averages for ESPs
followed by a wet scrubber. Similarly,
this proposal would require wet
scrubber parameters, including pressure
drop across the scrubber (or fan
amperage for certain SDT scrubbers) and
scrubbing liquid flow rate, be recorded
at least every 15-minutes and reduced to
3-hour averages. This proposal would
require RTO temperature be recorded
every 15 minutes and reduced to a 1hour average for purposes of assessing
when corrective action is required
under 40 CFR 63.864(k)(1), and reduced
to a 3-hour average under 40 CFR
63.864(k)(2) for purposes of assessing
violations.
We are proposing that the ESP and
wet scrubber operating limits be
established as the average of the
parameter values associated with each
performance test run. For example, the
proposal would require the recorded
readings during each test run be
averaged to arrive at the parameter value
associated with three test runs, and the
three values be averaged to arrive at the
operating limit. The proposal would
require these revised procedures be
used beginning with the first periodic
performance test proposed to be
required under 40 CFR 63.865. Wet
scrubbers and ESPs have minimum
operating limits, such that the EPA
would consider 3-hour average values
below the minimum operating limit to
be a monitoring exceedance to be
reported under 40 CFR 63.867(c). Also,
in the spirit of ensuring continuous
compliance, we are proposing to
eliminate the language in 40 CFR
63.864(k)(3) that allowed no more than
one non-opacity monitoring exceedance
to be attributed to any 24-hour period.
4. Reporting Frequency
Subpart MM of 40 CFR part 63
currently requires owners and operators
of subpart MM facilities to submit
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quarterly excess emissions reports for
monitoring exceedances and periods of
noncompliance and semiannual reports
when no excess emissions have
occurred during the reporting period.
These excess emission reports are
typically submitted as a hard copy to
the delegated authority, and reports in
this form usually are not readily
available for the EPA and public to
analyze. The Agency is proposing that
semiannual electronic reporting would
provide ample data to assess a facility’s
performance with regard to the emission
standards in subpart MM. The EPA is
proposing that all excess emissions
reports be submitted on a semiannual
basis, to conform to the semiannual
reporting frequency employed by the
electronic reporting system discussed in
the following section. The EPA requests
comment on maintaining quarterly
reporting for reports of monitoring
exceedances and periods of
noncompliance.
5. Electronic Reporting
The EPA is proposing that owners and
operators of 40 CFR part 63, subpart
MM facilities submit electronic copies
of compliance reports, which include
performance test reports, semiannual
reports, and notifications, through the
EPA’s Central Data Exchange (CDX)
using the Compliance and Emissions
Data Reporting Interface (CEDRI).
Specifically, we are proposing that
owners and operators submit
performance test reports through the
Electronic Reporting Tool (ERT) and
submit notifications and semiannual
reports through CEDRI. The EPA
believes that the electronic submittal of
the reports addressed in this proposed
rulemaking will increase the usefulness
of the data contained in those reports,
is in keeping with current trends in data
availability, will further assist in the
protection of public health and the
environment, and will ultimately result
in less burden on the regulated
community. Under current
requirements, paper reports are often
stored in filing cabinets or boxes, which
make the reports more difficult to obtain
and use for data analysis and sharing.
Electronic storage of such reports would
make data more accessible for review,
analyses, and sharing. Electronic
reporting can also eliminate paperbased, manual processes, thereby saving
time and resources, simplifying data
entry, eliminating redundancies,
minimizing data reporting errors and
providing data quickly and accurately to
the affected facilities, air agencies, the
EPA, and the public.
In 2011, in response to Executive
Order 13563, the EPA developed a
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plan 41 to periodically review its
regulations to determine if they should
be modified, streamlined, expanded, or
repealed in an effort to make regulations
more effective and less burdensome.
The plan includes replacing outdated
paper reporting with electronic
reporting. In keeping with this plan and
the White House’s Digital Government
Strategy,42 in 2013 the EPA issued an
agency-wide policy specifying that new
regulations will require reports to be
electronic to the maximum extent
possible. By requiring electronic
submission of specified reports in this
proposed rule, the EPA is taking steps
to implement this policy.
The EPA Web site that stores the
submitted electronic data, WebFIRE,
will be easily accessible to everyone and
will provide a user-friendly interface
that any stakeholder could access. By
making data readily available, electronic
reporting increases the amount of data
that can be used for many purposes.
One example is the development of
emissions factors. An emissions factor is
a representative value that attempts to
relate the quantity of a pollutant
released to the atmosphere with an
activity associated with the release of
that pollutant (e.g., kilograms of
particulate emitted per megagram of
coal burned). Such factors facilitate the
estimation of emissions from various
sources of air pollution and are an
important tool in developing emissions
inventories, which in turn are the basis
for numerous efforts, including trends
analysis, regional, and local scale air
quality modeling, regulatory impact
assessments, and human exposure
modeling. Emissions factors are also
widely used in regulatory applicability
determinations and in permitting
decisions.
The EPA has received feedback from
stakeholders asserting that many of the
EPA’s emissions factors are outdated or
not representative of a particular
industry emission source. While the
EPA believes that the emissions factors
are suitable for their intended purpose,
we recognize that the quality of
emissions factors varies based on the
extent and quality of underlying data.
We also recognize that emissions
profiles on different pieces of
equipment can change over time due to
41 Improving Our Regulations: Final Plan for
Periodic Retrospective Reviews of Existing
Regulations, August 2011. Available at https://
www.epa.gov/sites/roduction/files/2015-09-/
documents/eparetroreviewplan-aug2011_0.pdf.
42 Digital Government: Buildiing a 21st Century
Platform to Better Serve the American People, May
2012. Available at https://www.whitehouse.gov/sites/
default/files/omb/egov/digital-government/digitalgovernment-strategy/pdf.
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a number of factors (fuel changes,
equipment improvements, industry
work practices), and it is important for
emissions factors to be updated to keep
up with these changes. The EPA is
currently pursuing emissions factor
development improvements that
include procedures to incorporate the
source test data that we are proposing be
submitted electronically. By requiring
the electronic submission of the reports
identified in this proposed action, the
EPA would be able to access and use the
submitted data to update emissions
factors more quickly and efficiently,
creating factors that are characteristic of
what is currently representative of the
relevant industry sector. Likewise, an
increase in the number of test reports
used to develop the emissions factors
will provide more confidence that the
factor is of higher quality and
representative of the whole industry
sector.
Additionally, by making the records,
data and reports addressed in this
proposed rulemaking readily available,
the EPA, the regulated community and
the public will benefit when the EPA
conducts periodic reviews of its rules.
As a result of having performance test
reports and air emission reports readily
accessible, our ability to carry out
comprehensive reviews will be
increased and achieved within a shorter
period of time. These data will provide
useful information on control
efficiencies being achieved and
maintained in practice within a source
category and across source categories for
regulated sources and pollutants. These
reports can also be used to inform the
technology-review process by providing
information on improvements to add-on
control technology and new control
technology.
Under an electronic reporting system,
the EPA’s Office of Air Quality Planning
and Standards (OAQPS) would have air
emissions and performance test data in
hand; OAQPS would not have to collect
these data from the EPA Regional offices
or from delegated authorities or industry
sources in cases where these reports are
not submitted to the EPA Regional
offices. Thus, we anticipate fewer or less
substantial ICRs in conjunction with
prospective CAA-required technology
and risk-based reviews may be needed.
We expect this to result in a decrease in
time spent by industry to respond to
data collection requests. We also expect
the ICRs to contain less extensive stack
testing provisions, as we will already
have stack test data electronically.
Reduced testing requirements would be
a cost savings to industry. The EPA
should also be able to conduct these
required reviews more quickly, as
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OAQPS will not have to include the ICR
collection time in the process or spend
time collecting reports from the EPA
Regional Offices. While the regulated
community may benefit from a reduced
burden of ICRs, the general public
benefits from the Agency’s ability to
provide these required reviews more
quickly, resulting in increased public
health and environmental protection.
Electronic reporting could minimize
submission of unnecessary or
duplicative reports in cases where
facilities report to multiple government
agencies and the agencies opt to rely on
the EPA’s electronic reporting system to
view report submissions. Where
delegated authorities continue to require
a paper copy of these reports and will
accept a hard copy of the electronic
report, facilities will have the option to
print paper copies of the electronic
reporting forms to submit to the
delegated authorities, and, thus,
minimize the time spent reporting to
multiple agencies. Additionally,
maintenance and storage costs
associated with retaining paper records
could likewise be minimized by
replacing those records with electronic
records of electronically submitted data
and reports.
Delegated authorities could benefit
from more streamlined and automated
review of the electronically submitted
data. For example, because the
performance test data would be readilyavailable in a standard electronic
format, delegated authorities would be
able to review reports and data
electronically rather than having to
conduct a review of the reports and data
manually. Having reports and associated
data in electronic format will facilitate
review through the use of software
‘‘search’’ options, as well as the
downloading and analyzing of data in
spreadsheet format. Additionally,
delegated authorities would benefit
from the reported data being accessible
to them through the EPA’s electronic
reporting system wherever and
whenever they want or need access (as
long as they have access to the Internet).
The ability to access and review air
emission report information
electronically will assist delegated
authorities to more quickly and
accurately determine compliance with
the applicable regulations, potentially
allowing a faster response to violations
which could minimize harmful air
emissions. This benefits both delegated
authorities and the general public.
The proposed electronic reporting of
data is consistent with electronic data
trends (e.g., electronic banking and
income tax filing). Electronic reporting
of environmental data is already
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common practice in many media offices
at the EPA. The changes being proposed
in this rulemaking are needed to
continue the EPA’s transition to
electronic reporting.
As noted above, we are proposing that
40 CFR part 63, subpart MM
performance test reports be submitted
through the EPA’s ERT. All of the test
methods listed under subpart MM are
currently supported by the ERT, with
the exception of Method 308 in 40 CFR
part 63, appendix A. The proposal
would require that performance test
results collected using test methods that
are not supported by the ERT as listed
on the EPA’s ERT Web site at the time
of the test be submitted in portable
document format (PDF) using the
attachment module of the ERT.
In addition to electronically reporting
the results of performance tests, we are
proposing the requirement to
electronically submit notifications and
the semiannual excess emissions report
and/or summary report required in 40
CFR 63.867. The proposal would require
the owner or operator use the
appropriate electronic form or
spreadsheet template in CEDRI for the
subpart or an alternate electronic file
format consistent with the form’s
extensible markup language (XML)
schema. If neither the reporting form
nor the spreadsheet template specific to
the subpart are available at the time that
the report is due, the owner or operator
would upload an electronic copy of the
report in CEDRI. The owner or operator
would begin submitting reports
electronically using the reporting form
or spreadsheet template with the next
report that is due, once the electronic
form or template has been available for
at least 90 days. The EPA is currently
working to develop the forms and a
spreadsheet template for subpart MM.
We are specifically taking comment on
the content, layout, and overall design
of the forms and spreadsheet template,
which are discussed in a memorandum
in the docket titled Electronic Reporting
for Subpart MM Excess Emission
Reports.
As part of this review, we have
specified in 40 CFR 63.867 the reporting
requirements from the 40 CFR part 63
General Provisions for the excess
emissions and summary reports. We
believe that specifying the General
Provision reporting requirements for the
proposed semiannual reports in 40 CFR
part 63, subpart MM, will help
eliminate confusion as to which report
is submitted (e.g., full excess emissions
report or summary report) and the
content of the required report. Based on
the criteria specified in the General
Provisions, subpart MM requires a full
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excess emissions report under any of the
following three conditions: (1) The total
duration of monitoring exceedances is
one percent or more of the total
reporting period operating time, or (2)
the total continuous monitoring system
(CMS) downtime is five percent or more
of the total reporting period operating
time, or (3) any violations according to
40 CFR 63.864(k)(2) occurred. Subpart
MM requires only an abbreviated
summary report when none of the three
conditions apply for the semiannual
reporting period.
As stated in 40 CFR 63.867(a), the
proposal also requires that notifications
be reported electronically though
CEDRI. Currently, there are no templates
for notifications in CEDRI for this
subpart. Therefore, the owner or
operator must submit their notifications
in PDF. Examples of such notifications
include (but are not limited to) the
following: Initial notifications,
notifications of compliance status,
notifications of a performance test,
notifications of CMS performance
evaluation, and notifications of opacity
and visible emissions observations.
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6. Incorporation by Reference Under 1
CFR part 51
The EPA is proposing regulatory text
that includes incorporation by reference
(IBR). In accordance with requirements
of 1 CFR 51.5, the EPA is proposing to
incorporate by reference the following
document described in the amendments
to 40 CFR 63.14:
• EPA–454/R–98–015, Office of Air
Quality Planning and Standards
(OAQPS), Fabric Filter Bag Leak
Detection Guidance, September 1997,
IBR approved for 40 CFR 63.864(e).
This document provides guidance on
the use of triboelectric monitors as
fabric filter bag leak detectors. The
document includes fabric filter and
monitoring system descriptions;
guidance on monitor selection,
installation, setup, adjustment, and
operation; and quality assurance
procedures. The EPA has made, and
will continue to make, this document
generally available electronically
through https://www.regulations.gov
and/or in hard copy at the appropriate
EPA office (see the ADDRESSES section of
this preamble for more information). In
addition, this document is available on
the EPA Technical Air Pollution
Resources Emission Measurement
Center Web page (https://www.epa.gov/
emc) under Continuous Emission
Monitoring.
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7. Technical and Editorial Changes
The following lists additional changes
that address technical and editorial
corrections:
• Made revisions throughout 40 CFR
part 63, subpart MM, to clarify the
location in 40 CFR part 60 of applicable
EPA test methods;
• Made revisions throughout 40 CFR
part 63, subpart MM, to update the
facility name for Cosmo Specialty
Fibers;
• Revised the definitions section in
40 CFR 63.861 to:
Æ Remove the definition for ‘‘black
liquor gasification’’ and remove
reference to black liquor gasification in
the definitions for ‘‘kraft recovery
furnace,’’ ‘‘recovery furnace,’’
‘‘semichemical combustion unit,’’ and
‘‘soda recovery furnace’’;
Æ Remove the SSM exemption from
the definition for ‘‘modification’’;
Æ Clarify that the definition for
‘‘particulate matter’’ refers to filterable
PM;
Æ Removed reference to use of onehalf of the method detection limit for
non-detect Method 29 measurements
within the definition of ‘‘hazardous air
pollutant (HAP) metals’’ because the full
detection limit in emission
measurements is now typically used for
compliance determination in NESHAPs,
with the limited exception of TEQ
determination for dioxins and furans;
and
Æ Remove the definition for ‘‘startup’’
that pertains to the former black liquor
gasification system at Georgia-Pacific’s
facility in Big Island, Virginia.
• Corrected misspelling in 40 CFR
63.862(c).
• Revised multiple sections (40 CFR
63.863, 63.866, and 63.867) to remove
reference to the former smelters and
former black liquor gasification system
at Georgia-Pacific’s facility in Big Island,
Virginia.
• Revised the monitoring
requirements section in 40 CFR 63.864
to:
Æ Add reference to Performance
Specification 1 (PS–1) in COMS
monitoring provisions;
Æ Add IBR for bag leak detection
systems;
Æ Specify written procedures for CMS
recording frequency and reducing data
into averages; and
Æ Clarify ongoing compliance
provisions to address startup and
shutdown periods when certain
parameters cannot be met.
• Revised the performance test
requirements section in 40 CFR 63.865
to specify the conditions for conducting
performance tests and to revise the
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97081
ambient O2 concentration in Equations
7 and 8 from 21 percent to 20.9 percent
to bring 40 CFR part 63, subpart MM, in
line with the rest of the NESHAPs.
• Revised the recordkeeping
requirements section in 40 CFR 63.866
to include the requirement to record
information on failures to meet the
applicable standard.
• Revised the terminology in the
delegation of authority section in 40
CFR 63.868 to match the definitions in
40 CFR 63.90.
• Revised the General Provisions
applicability table (Table 1 to subpart
MM of part 63) to align with those
sections of the General Provisions that
have been amended or reserved over
time.
E. What compliance dates are we
proposing?
The compliance date for the revisions
we are proposing here is 1 year after the
date of publication of the final rule in
the Federal Register, with the exception
of the following: (1) Facilities must
conduct the first of the 5-year periodic
performance tests within 3 years of the
effective date of the standards (that is,
the date 3 years after the date of
publication of the final rule in the
Federal Register), and must conduct the
subsequent periodic performance tests
before renewing the facility’s 40 CFR
part 70 operating permit, but no longer
than 5 years following the previous
performance test; and (2) facilities must
submit performance test data through
the ERT within 60 days after the date of
completing each performance test.
V. Summary of Cost, Environmental,
and Economic Impacts
A. What are the affected sources?
There are currently 108 major source
pulp and paper mills operating in the
United States that conduct chemical
recovery combustion operations,
including 97 kraft pulp mills, 1 soda
pulp mill, 3 sulfite pulp mills, and 7
stand-alone semichemical pulp mills.
The 40 CFR part 63, subpart MM,
affected source regulated at kraft or soda
pulp mills is each existing chemical
recovery system, defined as all existing
DCE and NDCE recovery furnaces,
SDTs, and lime kilns. The DCE recovery
furnace system is defined as the DCE
recovery furnace and any BLO system,
if present, at the pulp mill. New affected
sources at kraft or soda pulp mills
include each new NDCE or DCE
recovery furnace and associated SDT,
and each new lime kiln. Subpart MM
affected sources also include each new
or existing chemical recovery
combustion unit located at a sulfite pulp
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mill or at a stand-alone semichemical
pulp mill.
B. What are the air quality impacts?
At the current level of control,
emissions of HAPs (HAP metals, acid
gases, and gaseous organic HAP) are
approximately 11,600 tpy. Current
emissions of PM (a surrogate pollutant
for HAP metals) and TRS (emitted by
the same mechanism as gaseous organic
HAP) are approximately 23,200 tpy and
3,600 tpy, respectively.
The proposed amendments will
require an estimated 108 mills to
conduct periodic testing for their
chemical recovery combustion
operations, 96 mills equipped with ESP
controls to meet more stringent opacity
limits and monitoring allowances and
conduct ESP parameter monitoring, and
all 108 major sources with equipment
subject to the 40 CFR part 63, subpart
MM standards to operate without the
SSM exemption. The EPA estimates that
the proposed changes to the opacity
limits and monitoring allowances will
reduce PM emissions by approximately
235 tpy and PM2.5 emissions by
approximately 112 tpy. We were unable
to quantify the specific emissions
reductions associated with periodic
emissions testing or eliminating the
SSM exemption, and we expect no
emissions reductions with ESP
parameter monitoring. However,
periodic testing will tend to reduce
emissions by providing incentive for
facilities to maintain their control
systems and make periodic adjustments
to ensure peak performance. Eliminating
the SSM exemption will reduce
emissions by requiring facilities to meet
the applicable standard during SSM
periods.
Indirect or secondary air emissions
impacts are impacts that would result
from the increased electricity usage
associated with the operation of control
devices (i.e., increased secondary
emissions of criteria pollutants from
power plants). Energy impacts consist of
the electricity and steam needed to
operate control devices and other
equipment that would be required
under this proposed rule. The EPA
estimates that the proposed changes to
the opacity limits and monitoring
allowances will result in energy impacts
of 106,000 million British thermal units
per year and criteria pollutant emissions
of 29 tpy (which includes PM, carbon
monoxide, nitrogen oxides, and sulfur
dioxide). The EPA expects no secondary
air emissions impacts or energy impacts
from the other proposed requirements.
Section IV.C of this preamble presents
estimates of the air quality impacts
associated with the regulatory options
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that were not selected for inclusion in
this proposed rule. For further
information, see the memorandum
titled, Costs/Impacts of the Subpart MM
Residual Risk and Technology Review,
in the docket for this action.
C. What are the cost impacts?
Subpart MM of 40 CFR part 63 mills
will incur costs to meet more stringent
opacity limits and monitoring
allowances, conduct periodic testing,
and perform new ESP parameter
monitoring. Costs associated with
elimination of the startup and shutdown
exemption were estimated as part of the
reporting and recordkeeping costs and
include time for re-evaluating
previously developed SSM record
systems. The EPA estimates the
nationwide capital costs associated with
the new testing and monitoring
requirements to be $48 million. The
EPA estimates the total nationwide
annualized costs associated with these
new requirements to be $13 million per
year. Section IV.C of this preamble
presents cost estimates associated with
the regulatory options that were not
selected for inclusion in this rule. For
further information, see the
memorandum titled Costs/Impacts of
the Subpart MM Residual Risk and
Technology Review, in the docket for
this action.
D. What are the economic impacts?
The economic impact analysis is
designed to inform decision makers
about the potential economic
consequences of a regulatory action. For
the current proposal, the EPA performed
a partial-equilibrium analysis of
national pulp and paper product
markets to estimate potential paper
product market and consumer and
producer welfare impacts of the
proposed regulatory options.
Across proposed regulatory options,
the EPA estimates market-level changes
in the paper and paperboard markets to
be insignificant. For the proposed
option, the EPA predicts national-level
weighted average paper and paperboard
prices to increase about 0.01 percent,
but predicts total quantities to decrease
less than 0.01 percent.
In addition, the EPA performed a
screening analysis for impacts on small
businesses by comparing estimated
annualized engineering compliance
costs at the firm-level to firm sales. The
screening analysis found that the ratio
of compliance cost to firm revenue falls
below 1-percent for the three small
companies likely to be affected by the
proposal. For small firms, the minimum
and maximum cost-to-sales ratios are
less than 1 percent.
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More information and details of this
analysis is provided in the technical
document titled Economic Impact
Analysis for Proposed Revisions to the
National Emissions Standards for
Hazardous Air Pollutants, Subpart MM,
for the Pulp and Paper Industry, which
is available in the docket for this
proposed rule (Docket ID No. EPA–HQ–
OAR–2014–0741).
E. What are the benefits?
The EPA estimates the proposed
changes to the opacity limits and
monitoring allowances at the 16
impacted mills will reduce PM
emissions by approximately 235 tpy and
PM2.5 emissions by approximately 112
tpy. Because these proposed
amendments are not considered
economically significant, as defined by
Executive Order 12866, we did not
monetize the benefits of reducing these
emissions. This does not mean that
there are no benefits associated with the
reduction in metal HAPs from this rule.
We expect that these avoided emissions
will reduce health effects associated
with exposure to air pollution, and we
provide below a qualitative description
of benefits associated with reducing
PM2.5. In addition, we anticipate the
specific control technologies associated
with these proposed amendments will
result in minor disbenefits from
additional energy consumption.
Directly emitted particles are
precursors to secondary formation of
PM2.5. Controls installed to reduce HAP
emissions would also reduce ambient
concentrations of PM2.5. Reducing
exposure to PM2.5 is associated with
significant human health benefits,
including avoiding mortality and
morbidity from cardiovascular and
respiratory illnesses. Researchers have
associated PM2.5 exposure with adverse
health effects in numerous toxicological,
clinical, and epidemiological studies
(U.S. EPA, 2009).43 When adequate data
and resources are available and a
regulatory impact analysis is required,
the EPA generally quantifies several
health effects associated with exposure
to PM2.5 (e.g., U.S. EPA, 2012).44 These
43 U.S. Environmental Protection agency (U.S.
EPA). 2009. Integrated Science Assessment for
Particulate Matter (Final Report). EPA–600–R–08–
139F. National Center for Environmental
Assessment—RTP Division. Available on the
Internet at https://cfpub.epa.gov/ncea/risk/
recordisplay.cfm?deid=216546.
44 U.S. Environmental Protection Agency (U.S.
EPA). 2012. Regulatory Impact Analysis for the
Final Revisions to the National Ambient Air Quality
Standards for Particulate Matter. Office of Air and
Radiation, Research Triange Park, NC. Available on
the Internet at https://www3.epa.gov/thn/ecas/
regdata/RIAs/finalria.pdf and https://
www3.epa.gov/ttnecas1/regdata/RIAs/
PMRIACombinedFile_Bookmarked.pdf.
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health effects include premature
mortality for adults and infants,
cardiovascular morbidities such as heart
attacks, hospital admissions, and
respiratory morbidities such as asthma
attacks, acute bronchitis, hospital and
emergency department visits, work loss
days, restricted activity days, and
respiratory symptoms. The scientific
literature also suggests that exposure to
PM2.5 is associated with adverse effects
on birth weight, pre-term births,
pulmonary function, and other
cardiovascular and respiratory effects
(U.S. EPA, 2009), but the EPA has not
quantified these impacts in its benefits
analyses.
VI. Request for Comments
We solicit comments on all aspects of
this proposed action. In addition to
general comments on this proposed
action, we are also interested in
additional data that may improve the
risk assessments and other analyses. We
are specifically interested in receiving
any improvements to the data used in
the site-specific emissions profiles used
for risk modeling. Such data should
include supporting documentation in
sufficient detail to allow
characterization of the quality and
representativeness of the data or
information. Section VII of this
preamble provides more information on
submitting data.
srobinson on DSK5SPTVN1PROD with PROPOSALS3
VII. Submitting Data Corrections
The site-specific emissions profiles
used in the source category risk and
demographic analyses and instructions
are available for download on the RTR
Web site at: https://www3.epa.gov/ttn/
atw/rrisk/rtrpg.html. The data files
include detailed information for each
HAP emissions release point for the
facilities in the source category.
If you believe that the data are not
representative or are inaccurate, please
identify the data in question, provide
your reason for concern, and provide
any ‘‘improved’’ data that you have, if
available. When you submit data, we
request that you provide documentation
of the basis for the revised values to
support your suggested changes. To
submit comments on the data
downloaded from the RTR Web site,
complete the following steps:
1. Within this downloaded file, enter
suggested revisions to the data fields
appropriate for that information.
2. Fill in the commenter information
fields for each suggested revision (i.e.,
commenter name, commenter
organization, commenter email address,
commenter phone number, and revision
comments).
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3. Gather documentation for any
suggested emissions revisions (e.g.,
performance test reports, material
balance calculations, etc.).
4. Send the entire downloaded file
with suggested revisions in Microsoft®
Access format and all accompanying
documentation to Docket ID No. EPA–
HQ–OAR–2014–0741 (through one of
the methods described in the ADDRESSES
section of this preamble).
5. If you are providing comments on
a single facility or multiple facilities,
you need only submit one file for all
facilities. The file should contain all
suggested changes for all sources at that
facility. We request that all data revision
comments be submitted in the form of
updated Microsoft® Excel files that are
generated by the Microsoft® Access file.
These files are provided on the RTR
Web site at: https://www3.epa.gov/ttn/
atw/rrisk/rtrpg.html.
VIII. Statutory and Executive Order
Reviews
Additional information about these
statutes and Executive Orders can be
found at https://www.epa.gov/lawsregulations/laws-and-executive-orders.
A. Executive Order 12866: Regulatory
Planning and Review and Executive
Order 13563: Improving Regulation and
Regulatory Review
This action is not a significant
regulatory action and was therefore not
submitted to OMB for review.
B. Paperwork Reduction Act (PRA)
The information collection activities
in this proposed rule have been
submitted for approval to OMB under
the PRA. The ICR document that the
EPA prepared has been assigned EPA
ICR number 1805.08. You can find a
copy of the ICR in the docket for this
rule, and it is briefly summarized here.
The information collection
requirements are not enforceable until
OMB approves them. The information
requirements are based on notification,
recordkeeping, and reporting
requirements in the NESHAP General
Provisions (40 CFR part 63, subpart A),
which are essential in determining
compliance and mandatory for all
operators subject to national emissions
standards. These recordkeeping and
reporting requirements are specifically
authorized by CAA section 114 (42
U.S.C. 7414). All information submitted
to the EPA pursuant to the
recordkeeping and reporting
requirements for which a claim of
confidentiality is made is safeguarded
according to Agency policies set forth in
40 CFR part 2, subpart B.
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We are proposing changes to the
paperwork requirements for 40 CFR part
63, subpart MM, in the form of
eliminating the SSM reporting and SSM
plan requirements, adding periodic
emissions testing for selected process
equipment, revising opacity monitoring
provisions, adding parameter
monitoring for ESPs, changing the
frequency of all excess emissions
reports to semiannual, and requiring
electronic submittal of all compliance
reports (including performance test
reports).
Respondents/affected entities:
Respondents include chemical pulp
mills operating equipment subject to 40
CFR part 63, subpart MM.
Respondent’s obligation to respond:
Mandatory (authorized by section 114 of
the CAA).
Estimated number of respondents:
108.
Frequency of response: The frequency
of responses varies depending on the
burden item. Responses include initial
notifications, reports of periodic
performance tests, and semiannual
compliance reports.
Total estimated burden: The annual
recordkeeping and reporting burden for
this information collection, averaged
over the first 3 years of this ICR, is
estimated to total 139,600 labor hours
per year. Burden is defined at 5 CFR
1320.3(b).
Total estimated cost: $17.7 million
per year, including $14.4 million per
year in labor costs and $3.29 million per
year in annualized capital and operation
and maintenance costs.
An agency may not conduct or
sponsor, and a person is not required to
respond to, a collection of information
unless it displays a currently valid OMB
control number. The OMB control
numbers for the EPA’s regulations in 40
CFR are listed in 40 CFR part 9.
Submit your comments on the
Agency’s need for this information, the
accuracy of the provided burden
estimates, and any suggested methods
for minimizing respondent burden, to
the EPA using the docket identified at
the beginning of this rule. You may also
send your ICR-related comments to
OMB’s Office of Information and
Regulatory Affairs via email to
OIRA_submission@omb.eop.gov,
Attention: Desk Officer for the EPA.
Since OMB is required to make a
decision concerning the ICR between 30
and 60 days after receipt, OMB must
receive comments no later than January
30, 2017. The EPA will respond to any
ICR-related comments in the final rule.
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C. Regulatory Flexibility Act (RFA)
I certify that this action will not have
a significant economic impact on a
substantial number of small entities
under the RFA. In making this
determination, the impact of concern is
any significant adverse economic
impact on small entities. An agency may
certify that a rule will not have a
significant economic impact on a
substantial number of small entities if
the rule relieves regulatory burden, has
no net burden or otherwise has a
positive economic effect on the small
entities subject to the rule. The EPA
estimates that all affected small entities
will have annualized costs of less than
1 percent of their sales. We have,
therefore, concluded that this action
will have no net regulatory burden for
all directly regulated small entities. For
more information on the small entity
impacts associated with this proposed
rule, please refer to the Economic
Impact and Small Business Analyses in
the public docket.
D. Unfunded Mandates Reform Act
(UMRA)
This action does not contain an
unfunded mandate of $100 million or
more as described in UMRA, 2 U.S.C.
1531–1538, and does not significantly or
uniquely affect small governments. The
action imposes no enforceable duty on
any state, local, or tribal governments or
the private sector.
srobinson on DSK5SPTVN1PROD with PROPOSALS3
E. Executive Order 13132: Federalism
This action 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.
F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
This action does not have tribal
implications as specified in Executive
Order 13175. It will not have substantial
direct effects on tribal governments, on
the relationship between the federal
government and Indian tribes, or on the
distribution of power and
responsibilities between the federal
government and Indian tribes, as
specified in Executive Order 13175.
This rule imposes requirements on
owners and operators of kraft, soda,
sulfite, and stand-alone semichemical
pulp mills and not tribal governments.
The EPA does not know of any pulp
mills owned or operated by Indian tribal
governments, or located within tribal
lands. However, if there are any, the
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effect of this rule on communities of
tribal governments would not be unique
or disproportionate to the effect on other
communities. Thus, Executive Order
13175 does not apply to this action.
G. Executive Order 13045: Protection of
Children From Environmental Health
Risks and Safety Risks
This action is not subject to Executive
Order 13045 because it is not
economically significant as defined in
Executive Order 12866, and because the
EPA does not believe the environmental
health or safety risks addressed by this
action present a disproportionate risk to
children. This action’s health and risk
assessments are contained in sections III
and IV of this preamble and further
documented in the risk report, titled
Residual Risk Assessment for Pulp Mill
Combustion Sources in Support of the
December 2016 Risk and Technology
Review Proposed Rule, in the docket for
this action.
H. Executive Order 13211: Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use
This action is not subject to Executive
Order 13211, because it is not a
significant regulatory action under
Executive Order 12866.
I. National Technology Transfer and
Advancement Act (NTTAA) and 1 CFR
part 51
This action involves technical
standards. While the EPA identified
ASTM D6784–02 (Reapproved 2008),
‘‘Standard Test Method for Elemental,
Oxidized, Particle-Bound and Total
Mercury Gas Generated from Coal-Fired
Stationary Sources (Ontario Hydro
Method)’’ as being potentially
applicable, the Agency does not propose
to use it. The use of this voluntary
consensus standard would be
impractical because this standard is
only acceptable as an alternative to the
portion of Method 29 for mercury, and
mercury is not regulated under 40 CFR
part 63, subpart MM.
J. Executive Order 12898: Federal
Actions To Address Environmental
Justice in Minority Populations and
Low-Income Populations
The EPA believes that this action will
not have potential disproportionately
high and adverse human health or
environmental effects on minority
populations, low-income populations,
and/or indigenous peoples, as specified
in Executive Order 12898 (59 FR 7629,
February 16, 1994). The documentation
for this decision is contained in section
IV.B of this preamble and the technical
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report titled Risk and Technology
Review—Analysis of Socio-Economic
Factors for Populations Living Near
Pulp Mill Combustion Sources, which is
located in the public docket for this
action.
We examined the potential for any EJ
issues that might be associated with the
source category, by performing a
demographic analysis of the population
close to the facilities. In this analysis,
we evaluated the distribution of HAPrelated cancer and non-cancer risks
from the 40 CFR part 63, subpart MM
source category across different social,
demographic, and economic groups
within the populations living near
facilities identified as having the highest
risks. The methodology and the results
of the demographic analyses are
included in a technical report, Risk and
Technology Review—Analysis of SocioEconomic Factors for Populations Living
Near Pulp Mill Combustion Sources,
available in the docket for this action.
The results of the 40 CFR part 63,
subpart MM source category
demographic analysis indicate that
emissions from the source category
expose approximately 7,600 people to a
cancer risk at or above 1-in-1 million
and no one exposed to a chronic noncancer TOSHI greater than 1. The
specific demographic results indicate
that the percentage of the population
potentially impacted by emissions is
greater than its corresponding national
percentage for the minority population
(33 percent for the source category
compared to 28 percent nationwide), the
African American population (28
percent for the source category
compared to 13 percent nationwide) and
for the population over age 25 without
a high school diploma (18 percent for
the source category compared to 15
percent nationwide). The proximity
results (irrespective of risk) indicate that
the population percentages for certain
demographic categories within 5 km of
source category emissions are greater
than the corresponding national
percentage for those same
demographics. The following
demographic percentages for
populations residing within close
proximity to facilities with pulp mill
combustion sources are higher than the
corresponding nationwide percentage:
African American, ages 65 and up, over
age 25 without a high school diploma,
and below the poverty level.
The risks due to HAP emissions from
this source category are low for all
populations (e.g., inhalation cancer risks
are less than 4-in-1 million for all
populations and non-cancer hazard
indices are less than 1). Furthermore,
we do not expect this proposal to
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achieve significant reductions in HAP
emissions. Therefore, we conclude that
this proposal 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. However, this
proposal, if finalized, will provide
additional benefits to these
demographic groups by improving the
compliance, monitoring, and
implementation of the NESHAP.
List of Subjects in 40 CFR Part 63
Environmental protection,
Administrative practice and procedure,
Air pollution control, Hazardous
substances, Incorporation by reference,
Intergovernmental relations, Pulp and
paper mills, Reporting and
recordkeeping requirements.
Dated: December 13, 2016.
Gina McCarthy,
Administrator.
For the reasons set out in the
preamble, title 40, chapter I, part 63 of
the Code of Federal Regulations is
proposed to be amended as follows:
PART 63—[AMENDED]
1. The authority citation for part 63
continues to read as follows:
■
Authority: 42 U.S.C. 7401 et seq.
Subpart A—[Amended]
2. Section 63.14 is amended by
revising paragraph (m)(3) to read as
follows:
■
§ 63.14
Incorporations by reference.
*
*
*
*
*
(m) * * *
(3) EPA–454/R–98–015, Office of Air
Quality Planning and Standards
(OAQPS), Fabric Filter Bag Leak
Detection Guidance, September 1997,
IBR approved for §§ 63.548(e), 63.864(e),
63.7525(j), 63.8450(e), 63.8600(e), and
63.11224(f).
Subpart MM—[Amended]
3. Section 63.860 is amended by
revising paragraphs (b)(5) and (7) and
adding paragraph (d) to read as follows:
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■
§ 63.860 Applicability and designation of
affected source.
*
*
*
*
*
(b) * * *
(5) Each new or existing sulfite
combustion unit located at a sulfite pulp
mill, except such existing units at
Cosmo Specialty Fibers’ Cosmopolis,
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Washington facility (Emission Unit no.
AP–10).
*
*
*
*
*
(7) The requirements of the alternative
standard in § 63.862(d) apply to the hog
fuel dryer at Cosmo Specialty Fibers’
Cosmopolis, Washington facility
(Emission Unit no. HD–14).
*
*
*
*
*
(d) At all times, the owner or operator
must operate and maintain any affected
source, including associated air
pollution control equipment and
monitoring equipment, in a manner
consistent with safety and good air
pollution control practices for
minimizing emissions. The general duty
to minimize emissions does not require
the owner or operator to make any
further efforts to reduce emissions if
levels required by the applicable
standard have been achieved.
Determination of whether a source is
operating in compliance with operation
and maintenance requirements will be
based on information available to the
Administrator which may include, but
is not limited to, monitoring results,
review of operation and maintenance
procedures, review of operation and
maintenance records, and inspection of
the source.
■ 4. Section 63.861 is amended by:
■ a. Removing the definitions for ‘‘Black
liquor gasification’’ and ‘‘Startup’’;
■ b. Revising the definitions for
‘‘Hazardous air pollutants (HAP)
metals,’’ ‘‘Hog fuel dryer,’’ ‘‘Kraft
recovery furnace,’’ ‘‘Modification,’’
‘‘Particulate matter (PM),’’ ‘‘Recovery
furnace,’’ ‘‘Semichemical combustion
unit,’’ ‘‘Soda recovery furnace,’’ and
‘‘Total hydrocarbons (THC).’’
The revisions read as follows:
§ 63.861
Definitions.
*
*
*
*
*
Hazardous air pollutants (HAP)
metals means the sum of all emissions
of antimony, arsenic, beryllium,
cadmium, chromium, cobalt, lead,
manganese, mercury, nickel, and
selenium as measured by EPA Method
29 (40 CFR part 60, appendix A–8).
Hog fuel dryer means the equipment
that combusts fine particles of wood
waste (hog fuel) in a fluidized bed and
directs the heated exhaust stream to a
rotary dryer containing wet hog fuel to
be dried prior to combustion in the hog
fuel boiler at Cosmo Specialty Fibers’
Cosmopolis, Washington facility. The
hog fuel dryer at Cosmo Specialty
Fibers’ Cosmopolis, Washington facility
is Emission Unit no. HD–14.
*
*
*
*
*
Kraft recovery furnace means a
recovery furnace that is used to burn
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black liquor produced by the kraft
pulping process, as well as any recovery
furnace that burns black liquor
produced from both the kraft and
semichemical pulping processes, and
includes the direct contact evaporator, if
applicable.
*
*
*
*
*
Modification means, for the purposes
of § 63.862(a)(1)(ii)(E)(1), any physical
change (excluding any routine part
replacement or maintenance) or
operational change that is made to the
air pollution control device that could
result in an increase in PM emissions.
*
*
*
*
*
Particulate matter (PM) means total
filterable particulate matter as measured
by EPA Method 5 (40 CFR part 60,
appendix A–3), EPA Method 17
(§ 63.865(b)(1)) (40 CFR part 60,
appendix A–6), or EPA Method 29 (40
CFR part 60, appendix A–8).
*
*
*
*
*
Recovery furnace means an enclosed
combustion device where concentrated
black liquor produced by the kraft or
soda pulping process is burned to
recover pulping chemicals and produce
steam.
*
*
*
*
*
Semichemical combustion unit means
any equipment used to combust or
pyrolyze black liquor at stand-alone
semichemical pulp mills for the purpose
of chemical recovery.
*
*
*
*
*
Soda recovery furnace means a
recovery furnace used to burn black
liquor produced by the soda pulping
process and includes the direct contact
evaporator, if applicable.
*
*
*
*
*
Total hydrocarbons (THC) means the
sum of organic compounds measured as
carbon using EPA Method 25A (40 CFR
part 60, appendix A–7).
■ 5. Section 63.862 is amended by
revising paragraphs (c)(1) and (d) to read
as follows:
§ 63.862
Standards.
*
*
*
*
*
(c) Standards for gaseous organic
HAP. (1) The owner or operator of any
new recovery furnace at a kraft or soda
pulp mill must ensure that the
concentration or gaseous organic HAP,
as measured by methanol, discharged to
the atmosphere is no greater than 0.012
kg/Mg (0.025 lb/ton) of black liquor
solids fired.
*
*
*
*
*
(d) Alternative standard. As an
alternative to meeting the requirements
of paragraph (a)(2) of this section, the
owner or operator of the existing hog
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fuel dryer at Cosmo Specialty Fibers’
Cosmopolis, Washington facility
(Emission Unit no. HD–14) must ensure
that the mass of PM in the exhaust gases
discharged to the atmosphere from the
hog fuel dryer is less than or equal to
4.535 kilograms per hour (kg/hr) (10.0
pounds per hour (lb/hr)).
■ 6. Section 63.863 is amended by
revising paragraph (c) to read as follows:
§ 63.863
Compliance dates.
*
*
*
*
*
(c) The owner or operator of an
existing or new affected source or
process unit must comply with the
revised requirements published on
[insert date of publication of final rule
in the Federal Register] no later than
[insert date 1 year after date of
publication of final rule in the Federal
Register], with the exception of the
following:
(1) The first of the 5-year periodic
performance tests must be conducted
within 3 years of the effective date of
the revised standards, by [insert date 3
years after date of publication of final
rule in the Federal Register], and
thereafter before renewing the facility’s
40 CFR part 70 operating permit, but no
longer than 5 years following the
previous performance test; and
(2) The date to submit performance
test data through the ERT is within 60
days after the date of completing each
performance test.
■ 7. Section 63.864 is revised to read as
follows:
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§ 63.864
Monitoring requirements.
(a)–(c) [Reserved]
(d) Continuous opacity monitoring
system (COMS). The owner or operator
of each affected kraft or soda recovery
furnace or lime kiln equipped with an
ESP must install, calibrate, maintain,
and operate a COMS in accordance with
Performance Specification 1 (PS–1) in
appendix B to 40 CFR part 60 and the
provisions in §§ 63.6(h) and 63.8 and
paragraphs (d)(1) through (5) of this
section.
(1)–(2) [Reserved]
(3) As specified in § 63.8(c)(4)(i), each
COMS must complete a minimum of
one cycle of sampling and analyzing for
each successive 10-second period and
one cycle of data recording for each
successive 6-minute period.
(4) As specified in § 63.8(g)(2), each 6minute COMS data average must be
calculated as the average of 36 or more
data points, equally spaced over each 6minute period.
(5) As specified in § 63.8(g)(4), each 6minute COMS data average should be
rounded to the nearest 1-percent
opacity.
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(e) Continuous parameter monitoring
system (CPMS). For each CPMS required
in this section, the owner or operator of
each affected source or process unit
must meet the requirements in
paragraphs (e)(1) through (14) of this
section.
(1) For any kraft or soda recovery
furnace or lime kiln using an ESP
emission control device, the owner or
operator must use the continuous
parameter monitoring devices specified
in paragraphs (e)(1)(i) and (ii) of this
section to determine and record
parameters at least once every
successive 15-minute period.
(i) A monitoring device for the
continuous measurement of the
secondary voltage of each ESP
collection field.
(ii) A monitoring device for the
continuous measurement of the
secondary current of each ESP
collection field.
(iii) Total secondary power may be
calculated as the product of the
secondary voltage and secondary
current measurements for each ESP
collection field and used to demonstrate
compliance as an alternative to the
secondary voltage and secondary
current measurements.
(2) For any kraft or soda recovery
furnace or lime kiln using an ESP
followed by a wet scrubber, the owner
or operator must use the continuous
parameter monitoring devices specified
in paragraphs (e)(1) and (10) of this
section. The opacity monitoring system
specified in paragraph (d) of this section
is not required for combination ESP/wet
scrubber control device systems.
(3)–(9) [Reserved]
(10) The owner or operator of each
affected kraft or soda recovery furnace,
kraft or soda lime kiln, sulfite
combustion unit, or kraft or soda smelt
dissolving tank equipped with a wet
scrubber must install, calibrate,
maintain, and operate a CPMS that can
be used to determine and record the
pressure drop across the scrubber and
the scrubbing liquid flow rate at least
once every successive 15-minute period
using the procedures in § 63.8(c), as
well as the procedures in paragraphs
(e)(10)(i) and (ii) of this section:
(i) A monitoring device used for the
continuous measurement of the pressure
drop of the gas stream across the
scrubber must be certified by the
manufacturer to be accurate to within a
gage pressure of ±500 pascals (±2 inches
of water gage pressure); and
(ii) A monitoring device used for
continuous measurement of the
scrubbing liquid flow rate must be
certified by the manufacturer to be
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accurate within ±5 percent of the design
scrubbing liquid flow rate.
(iii) As an alternative to pressure drop
measurement under paragraph (e)(3)(i)
of this section, a monitoring device for
measurement of fan amperage may be
used for smelt dissolving tank dynamic
scrubbers that operate at ambient
pressure or for low-energy entrainment
scrubbers where the fan speed does not
vary.
(11) The owner or operator of each
affected semichemical combustion unit
equipped with an RTO must install,
calibrate, maintain, and operate a CPMS
that can be used to determine and
record the operating temperature of the
RTO at least once every successive 15minute period using the procedures in
§ 63.8(c). The monitor must compute
and record the operating temperature at
the point of incineration of effluent
gases that are emitted using a
temperature monitor accurate to within
±1 percent of the temperature being
measured.
(12) The owner or operator of the
affected hog fuel dryer at Cosmo
Specialty Fibers’ Cosmopolis,
Washington facility (Emission Unit no.
HD–14) must meet the requirements in
paragraphs (e)(12)(i) through (xi) of this
section for each bag leak detection
system.
(i) The owner or operator must install,
calibrate, maintain, and operate each
triboelectric bag leak detection system
according to EPA–454/R–98–015,
‘‘Fabric Filter Bag Leak Detection
Guidance’’ (incorporated by reference—
see § 63.14). This document is available
from the U.S. Environmental Protection
Agency (U.S. EPA); Office of Air Quality
Planning and Standards; Emissions,
Monitoring and Analysis Division;
Emission Measurement Center, MD–
D205–02, Research Triangle Park, NC
27711. This document is also available
on the EPA Technical Air Pollution
Resources Emission Measurement
Center Web page under Continuous
Emission Monitoring. The owner or
operator must install, calibrate,
maintain, and operate other types of bag
leak detection systems in a manner
consistent with the manufacturer’s
written specifications and
recommendations.
(ii) The bag leak detection system
must be certified by the manufacturer to
be capable of detecting PM emissions at
concentrations of 10 milligrams per
actual cubic meter (0.0044 grains per
actual cubic foot) or less.
(iii) The bag leak detection system
sensor must provide an output of
relative PM loadings.
(iv) The bag leak detection system
must be equipped with a device to
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continuously record the output signal
from the sensor.
(v) The bag leak detection system
must be equipped with an audible alarm
system that will sound automatically
when an increase in relative PM
emissions over a preset level is detected.
The alarm must be located where it is
easily heard by plant operating
personnel.
(vi) For positive pressure fabric filter
systems, a bag leak detector must be
installed in each baghouse compartment
or cell.
(vii) For negative pressure or induced
air fabric filters, the bag leak detector
must be installed downstream of the
fabric filter.
(viii) Where multiple detectors are
required, the system’s instrumentation
and alarm may be shared among
detectors.
(ix) The baseline output must be
established by adjusting the range and
the averaging period of the device and
establishing the alarm set points and the
alarm delay time according to section
5.0 of the ‘‘Fabric Filter Bag Leak
Detection Guidance’’ (incorporated by
reference—see § 63.14).
(x) Following initial adjustment of the
system, the sensitivity or range,
averaging period, alarm set points, or
alarm delay time may not be adjusted
except as detailed in the site-specific
monitoring plan. In no case may the
sensitivity be increased by more than
100 percent or decreased more than 50
percent over a 365-day period unless
such adjustment follows a complete
fabric filter inspection which
demonstrates that the fabric filter is in
good operating condition, as defined in
section 5.2 of the ‘‘Fabric Filter Bag
Leak Detection Guidance,’’
(incorporated by reference—see § 63.14).
Record each adjustment.
(xi) The owner or operator must
record the results of each inspection,
calibration, and validation check.
(13) The owner or operator of each
affected source or process unit that uses
an ESP, wet scrubber, RTO, or fabric
filter may monitor alternative control
device operating parameters subject to
prior written approval by the
Administrator. The request for approval
must also include the manner in which
the parameter operating limit is to be
set.
(14) The owner or operator of each
affected source or process unit that uses
an air pollution control system other
than an ESP, wet scrubber, RTO, or
fabric filter must provide to the
Administrator an alternative monitoring
request that includes the site-specific
monitoring plan described in paragraph
(a) of this section, a description of the
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control device, test results verifying the
performance of the control device, the
appropriate operating parameters that
will be monitored, how the operating
limit is to be set, and the frequency of
measuring and recording to establish
continuous compliance with the
standards. The alternative monitoring
request is subject to the Administrator’s
approval. The owner or operator of the
affected source or process unit must
install, calibrate, operate, and maintain
the monitor(s) in accordance with the
alternative monitoring request approved
by the Administrator. The owner or
operator must include in the
information submitted to the
Administrator proposed performance
specifications and quality assurance
procedures for the monitors. The
Administrator may request further
information and will approve acceptable
test methods and procedures. The
owner or operator must monitor the
parameters as approved by the
Administrator using the methods and
procedures in the alternative monitoring
request.
(f) Data quality assurance. The owner
or operator shall keep CMS data quality
assurance procedures consistent with
the requirements in § 63.8(d)(1) and (2)
on record for the life of the affected
source or until the affected source is no
longer subject to the provisions of this
part, to be made available for
inspection, upon request, by the
Administrator. If the performance
evaluation plan in § 63.8(d)(2) is
revised, the owner or operator shall
keep previous (i.e., superseded) versions
of the performance evaluation plan on
record to be made available for
inspection, upon request, by the
Administrator, for a period of 5 years
after each revision to the plan. The
program of corrective action should be
included in the plan required under
§ 63.8(d)(2).
(g) Gaseous organic HAP. The owner
or operator of each affected source or
process unit complying with the
gaseous organic HAP standard of
§ 63.862(c)(1) through the use of an
NDCE recovery furnace equipped with a
dry ESP system is not required to
conduct any continuous monitoring to
demonstrate compliance with the
gaseous organic HAP standard.
(h) Monitoring data. As specified in
§ 63.8(g)(5), monitoring data recorded
during periods of unavoidable CMS
breakdowns, out-of-control periods,
repairs, maintenance periods,
calibration checks, and zero (low-level)
and high level adjustments must not be
included in any data average computed
under this part.
(i) [Reserved]
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(j) Determination of operating limits.
(1) During the initial or periodic
performance test required in § 63.865,
the owner or operator of any affected
source or process unit must establish
operating limits for the monitoring
parameters in paragraphs (e)(1) and (2)
and (e)(10) through (14) of this section,
as appropriate; or
(2) The owner or operator may base
operating limits on values recorded
during previous performance tests or
conduct additional performance tests for
the specific purpose of establishing
operating limits, provided that test data
used to establish the operating limits are
or have been obtained using the test
methods required in this subpart. The
owner or operator of the affected source
or process unit must certify that all
control techniques and processes have
not been modified subsequent to the
testing upon which the data used to
establish the operating parameter limits
were obtained.
(3) The owner or operator of an
affected source or process unit may
establish expanded or replacement
operating limits for the monitoring
parameters listed in paragraphs (e)(1)
and (2) and (e)(10) through (14) of this
section and established in paragraph
(j)(1) or (2) of this section during
subsequent performance tests using the
test methods in § 63.865.
(4) The owner or operator of the
affected source or process unit must
continuously monitor each parameter
and determine the arithmetic average
value of each parameter during each
performance test. Multiple performance
tests may be conducted to establish a
range of parameter values.
(5) New, expanded, or replacement
operating limits for the monitoring
parameter values listed in paragraphs
(e)(1) and (2) and (e)(10) through (14) of
this section should be determined as
described in paragraphs (j)(5)(i) through
(iii) below.
(i) The owner or operator of an
affected source or process unit that uses
a wet scrubber must set a minimum
scrubber pressure drop operating limit
as the average of the pressure drop
values associated with each test run.
(A) For a smelt dissolving tank
dynamic wet scrubber operating at
ambient pressure or for low-energy
entrainment scrubbers where fan speed
does not vary, the minimum fan
amperage operating limit must be set as
the average of the fan amperage values
associated with each test run.
(B) [Reserved]
(ii) The owner operator of an affected
source equipped with an ESP must set
the minimum operating secondary
current and secondary voltage as the
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average of the values associated with
each test run.
(iii) The owner operator of an affected
source equipped with an RTO must set
the minimum operating temperature of
the RTO as the average of the values
associated with each test run.
(6) [Reserved]
(k) On-going compliance provisions.
(1) Following the compliance date,
owners or operators of all affected
sources or process units are required to
implement corrective action if the
monitoring exceedances in paragraphs
(k)(1)(ii) through (vii) of this section
occur during times when spent pulping
liquor or lime mud is fired (as
applicable). Corrective action can
include completion of transient startup
and shutdown conditions as
expediently as possible.
(i) [Reserved]
(ii) For a new or existing kraft or soda
recovery furnace, kraft or soda smelt
dissolving tank, kraft or soda lime kiln,
or sulfite combustion unit equipped
with a wet scrubber, when any 3-hour
average parameter value is below the
minimum operating limit established in
paragraph (j) of this section, with the
exception of pressure drop during
periods of startup and shutdown.
(iii) For a new or existing kraft or soda
recovery furnace or lime kiln equipped
with an ESP followed by a wet scrubber,
when:
(A) Any 3-hour average scrubber
parameter value is below the minimum
operating limit established in paragraph
(j) of this section, with the exception of
pressure drop during periods of startup
and shutdown; and
(B) Any 3-hour average ESP secondary
voltage and secondary current (or total
secondary power) values are below the
minimum operating limits established
during performance testing, with the
exception of secondary current (or total
secondary power) during periods of
startup and shutdown.
(iv) For a new or existing
semichemical combustion unit
equipped with an RTO, when any 1hour average temperature falls below
the minimum temperature operating
limit established in paragraph (j) of this
section.
(v) For the hog fuel dryer at Cosmo
Specialty Fibers’ Cosmopolis,
Washington facility (Emission Unit no.
HD–14), when the bag leak detection
system alarm sounds.
(vi) For an affected source or process
unit equipped with an ESP, wet
scrubber, RTO, or fabric filter and
monitoring alternative operating
parameters established in paragraph
(e)(13) of this section, when any 3-hour
average value does not meet the
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operating limit established in paragraph
(j) of this section.
(vii) For an affected source or process
unit equipped with an alternative air
pollution control system and monitoring
operating parameters approved by the
Administrator as established in
paragraph (e)(14) of this section, when
any 3-hour average value does not meet
the operating limit established in
paragraph (j) of this section.
(2) Following the compliance date,
owners or operators of all affected
sources or process units are in violation
of the standards of § 63.862 if the
monitoring exceedances in paragraphs
(k)(2)(i) through (ix) of this section
occur during times when spent pulping
liquor or lime mud is fired (as
applicable):
(i) For a new or existing kraft or soda
recovery furnace equipped with an ESP,
when opacity is greater than 20 percent
for 2 percent or more of the operating
time within any semiannual period;
(ii) For a new or existing kraft or soda
lime kiln equipped with an ESP, when
opacity is greater than 20 percent for 1
percent or more of the operating time
within any semiannual period;
(iii) For a new or existing kraft or soda
recovery furnace or lime kiln equipped
with an ESP, when the ESP secondary
voltage and secondary current (or total
secondary power) averaged over the
semiannual period are below the
minimum operating limits established
during the performance test, with the
exception of secondary current (or total
secondary power) during periods of
startup and shutdown;
(iv) For a new or existing kraft or soda
recovery furnace, kraft or soda smelt
dissolving tank, kraft or soda lime kiln,
or sulfite combustion unit equipped
with a wet scrubber, when six or more
3-hour average parameter values within
any 6-month reporting period are below
the minimum operating limits
established in paragraph (j) of this
section, with the exception of pressure
drop during periods of startup and
shutdown;
(v) For a new or existing kraft or soda
recovery furnace or lime kiln equipped
with an ESP followed by a wet scrubber,
when:
(A) Six or more 3-hour average
scrubber parameter values within any 6month reporting period are outside the
range of values established in paragraph
(j) of this section, with the exception of
pressure drop during periods of startup
and shutdown; and
(B) Six or more 3-hour average ESP
secondary voltage and secondary
current (or total secondary power)
values within any 6-month reporting
period are below the minimum
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operating limits established during
performance testing, with the exception
of secondary current (or total secondary
power) during periods of startup and
shutdown;
(vi) For a new or existing
semichemical combustion unit
equipped with an RTO, when any 3hour average temperature falls below
the temperature established in
paragraph (j) of this section;
(vii) For the hog fuel dryer at Cosmo
Specialty Fibers’ Cosmopolis,
Washington facility (Emission Unit no.
HD–14), when corrective action is not
initiated within 1 hour of a bag leak
detection system alarm and the alarm is
engaged for more than 5 percent of the
total operating time in a 6-month block
reporting period. In calculating the
operating time fraction, if inspection of
the fabric filter demonstrates that no
corrective action is required, no alarm
time is counted; if corrective action is
required, each alarm is counted as a
minimum of 1 hour; if corrective action
is not initiated within 1 hour, the alarm
time is counted as the actual amount of
time taken to initiate corrective action;
(viii) For an affected source or process
unit equipped with an ESP, wet
scrubber, RTO, or fabric filter and
monitoring alternative operating
parameters established in paragraph
(e)(13) of this section, when six or more
3-hour average values within any 6month reporting period do not meet the
operating limits established in
paragraph (j) of this section; and
(ix) For an affected source or process
unit equipped with an alternative air
pollution control system and monitoring
operating parameters approved by the
Administrator as established in
paragraph (e)(14) of this section, when
six or more 3-hour average values
within any 6-month reporting period do
not meet the operating limits
established in paragraph (j) of this
section.
(3) [Reserved]
■ 8. Section 63.865 is amended by
revising the introductory text and
paragraphs (b)(1) through (5), (c)(1), and
(d)introductory text to read as follows:
§ 63.865 Performance test requirements
and test methods.
The owner or operator of each
affected source or process unit subject to
the requirements of this subpart is
required to conduct an initial
performance test and periodic
performance tests using the test
methods and procedures listed in § 63.7
and paragraph (b) of this section. The
owner or operator must conduct the first
of the periodic performance tests within
3 years of the effective date of the
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explanation to support that such
conditions represent normal operation.
Upon request, the owner or operator
shall make available to the
Administrator such records as may be
necessary to determine the conditions of
performance tests.
*
*
*
*
*
(b) * * *
(1) For purposes of determining the
concentration or mass of PM emitted
from each kraft or soda recovery
furnace, sulfite combustion unit, smelt
dissolving tank, lime kiln, or the hog
fuel dryer at Cosmo Specialty Fibers’
Cosmopolis, Washington facility
(Emission Unit no. HD–14), Method 5 in
appendix A–3 of 40 CFR part 60 or
Method 29 in appendix A–8 of 40 CFR
part 60 must be used, except that
Method 17 in appendix A–6 of 40 CFR
part 60 may be used in lieu of Method
5 or Method 29 if a constant value of
0.009 g/dscm (0.004 gr/dscf) is added to
the results of Method 17, and the stack
temperature is no greater than 205 °C
(400 °F). For Methods 5, 29, and 17, the
sampling time and sample volume for
each run must be at least 60 minutes
and 0.90 dscm (31.8 dscf), and water
must be used as the cleanup solvent
instead of acetone in the sample
recovery procedure.
(2) For sources complying with
§ 63.862(a) or (b), the PM concentration
must be corrected to the appropriate
oxygen concentration using Equation 7
of this section as follows:
Where:
Ccorr = the measured concentration corrected
for oxygen, g/dscm (gr/dscf);
Cmeas = the measured concentration
uncorrected for oxygen, g/dscm (gr/dscf);
X = the corrected volumetric oxygen
concentration (8 percent for kraft or soda
recovery furnaces and sulfite combustion
units and 10 percent for kraft or soda
lime kilns); and
Y = the measured average volumetric oxygen
concentration.
Method 3B. The gas sample must be
taken at the same time and at the same
traverse points as the particulate
sample.
(4) For purposes of complying with of
§ 63.862(a)(1)(ii)(A), the volumetric gas
flow rate must be corrected to the
appropriate oxygen concentration using
Equation 8 of this section as follows:
Where:
Qcorr = the measured volumetric gas flow rate
corrected for oxygen, dscm/min (dscf/
min).
Qmeas = the measured volumetric gas flow
rate uncorrected for oxygen, dscm/min
(dscf/min).
Y = the measured average volumetric oxygen
concentration.
X = the corrected volumetric oxygen
concentration (8 percent for kraft or soda
recovery furnaces and 10 percent for
kraft or soda lime kilns).
1981—Part 10 (incorporated by
reference—see § 63.14) may be used as
an alternative to using Method 3B; and
(iv) For purposes of determining
moisture content of stack gas, Method 4
in appendix A–3 of 40 CFR part 60 must
be used.
*
*
*
*
*
(c) * * *
(1) The owner or operator complying
through the use of an NDCE recovery
furnace equipped with a dry ESP system
is required to conduct periodic
performance testing using Method 308
in appendix A of this part, as well as the
methods listed in paragraphs (b)(5)(i)
through (iv) of this section to
demonstrate compliance with the
gaseous organic HAP standard. The
requirements and equations in
paragraph (b)(2) of this section must be
met and utilized, respectively.
*
*
*
*
*
(d) The owner or operator seeking to
determine compliance with the gaseous
organic HAP standards in § 63.862(c)(2)
for semichemical combustion units
must use Method 25A in appendix A–
7 of 40 CFR part 60, as well as the
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methods listed in paragraphs (b)(5)(i)
through (iv) of this section. The
sampling time for each Method 25A run
must be at least 60 minutes. The
calibration gas for each Method 25A run
must be propane.
*
*
*
*
*
■ 9. Section 63.866 is revised to read as
follows:
§ 63.866
Recordkeeping requirements.
(a) [Reserved]
(b) The owner or operator of an
affected source or process unit must
maintain records of any occurrence
when corrective action is required
under § 63.864(k)(1), and when a
violation is noted under § 63.864(k)(2).
Record the time corrective action was
initiated and completed, and the
corrective action taken.
(c) In addition to the general records
required by § 63.10(b)(2)(iii) and (vi)
through (xiv), the owner or operator
must maintain records of the
information in paragraphs (c)(1) through
(8) of this section:
(1) Records of black liquor solids
firing rates in units of Mg/d or ton/d for
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(5)(i) For purposes of selecting
sampling port location and number of
traverse points, Method 1 or 1A in
appendix A–1 of 40 CFR part 60 must
be used;
(ii) For purposes of determining stack
gas velocity and volumetric flow rate,
Method 2, 2A, 2C, 2D, or 2F in appendix
A–1 of 40 CFR part 60 or Method 2G in
appendix A–2 of 40 CFR part 60 must
be used;
(iii) For purposes of conducting gas
analysis, Method 3, 3A, or 3B in
appendix A–2 of 40 CFR part 60 must
be used. The voluntary consensus
standard ANSI/ASME PTC 19.10–
(3) Method 3A or 3B in appendix A–
2 of 40 CFR part 60 must be used to
determine the oxygen concentration.
The voluntary consensus standard
ANSI/ASME PTC 19.10–1981—Part 10
(incorporated by reference—see § 63.14)
may be used as an alternative to using
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revised standards and thereafter before
renewing their 40 CFR part 70 operating
permit but at intervals no longer than 5
years following the previous
performance test. Performance tests
shall be conducted under such
conditions as the Administrator
specifies to the owner or operator based
on representative performance of the
affected source for the period being
tested. Representative conditions
exclude periods of startup and
shutdown. The owner or operator may
not conduct performance tests during
periods of malfunction. The owner or
operator must record the process
information that is necessary to
document operating conditions during
the test and include in such record an
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all recovery furnaces and semichemical
combustion units;
(2) Records of CaO production rates in
units of Mg/d or ton/d for all lime kilns;
(3) Records of parameter monitoring
data required under § 63.864, including
any period when the operating
parameter levels were inconsistent with
the levels established during the
performance test;
(4) Records and documentation of
supporting calculations for compliance
determinations made under § 63.865(a)
through (d);
(5) Records of parameter operating
limits established for each affected
source or process unit;
(6) Records certifying that an NDCE
recovery furnace equipped with a dry
ESP system is used to comply with the
gaseous organic HAP standard in
§ 63.862(c)(1);
(7) For the bag leak detection system
on the hog fuel dryer fabric filter at
Cosmo Specialty Fibers’ Cosmopolis,
Washington facility (Emission Unit no.
HD–14), records of each alarm, the time
of the alarm, the time corrective action
was initiated and completed, and a brief
description of the cause of the alarm
and the corrective action taken; and
(8) Records of the date, time, and
duration of each startup and/or
shutdown period, recording the periods
when the affected source was subject to
the standard applicable to startup and
shutdown.
(d)(1) In the event that an affected
unit fails to meet an applicable
standard, including any emission limit
or operating limit, record the number of
failures. For each failure record the date,
start time, and duration of each failure
along with a brief explanation of the
cause.
(2) For each failure to meet an
applicable standard, record and retain a
list of the affected sources or equipment,
an estimate of the quantity of each
regulated pollutant emitted over any
emission limit and a description of the
method used to estimate the emissions.
(3) Record actions taken to minimize
emissions in accordance with
§ 63.860(d) and any corrective actions
taken to return the affected unit to its
normal or usual manner of operation.
■ 10. Section 63.867 is revised to read
as follows:
§ 63.867
Reporting requirements.
(a) Notifications. (1) The owner or
operator of any affected source or
process unit must submit the applicable
notifications from subpart A of this part,
as specified in Table 1 of this subpart.
(2) [Reserved]
(3) In addition to the requirements in
subpart A of this part, the owner or
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operator of the hog fuel dryer at Cosmo
Specialty Fibers’ Cosmopolis,
Washington, facility (Emission Unit no.
HD–14) must include analysis and
supporting documentation
demonstrating conformance with EPA
guidance and specifications for bag leak
detection systems in § 63.864(e)(12) in
the Notification of Compliance Status.
(b) Additional reporting requirements
for HAP metals standards. (1) Any
owner or operator of a group of process
units in a chemical recovery system at
a mill complying with the PM emissions
limits in § 63.862(a)(1)(ii) must submit
the PM emissions limits determined in
§ 63.865(a) for each affected kraft or
soda recovery furnace, smelt dissolving
tank, and lime kiln to the Administrator
for approval. The emissions limits must
be submitted as part of the notification
of compliance status required under
subpart A of this part.
(2) Any owner or operator of a group
of process units in a chemical recovery
system at a mill complying with the PM
emissions limits in § 63.862(a)(1)(ii)
must submit the calculations and
supporting documentation used in
§ 63.865(a)(1) and (2) to the
Administrator as part of the notification
of compliance status required under
subpart A of this part.
(3) After the Administrator has
approved the emissions limits for any
process unit, the owner or operator of a
process unit must notify the
Administrator before any of the actions
in paragraphs (b)(3)(i) through (iv) of
this section are taken:
(i) The air pollution control system for
any process unit is modified or
replaced;
(ii) Any kraft or soda recovery
furnace, smelt dissolving tank, or lime
kiln in a chemical recovery system at a
kraft or soda pulp mill complying with
the PM emissions limits in
§ 63.862(a)(1)(ii) is shut down for more
than 60 consecutive days;
(iii) A continuous monitoring
parameter or the value or range of
values of a continuous monitoring
parameter for any process unit is
changed; or
(iv) The black liquor solids firing rate
for any kraft or soda recovery furnace
during any 24-hour averaging period is
increased by more than 10 percent
above the level measured during the
most recent performance test.
(4) An owner or operator of a group
of process units in a chemical recovery
system at a mill complying with the PM
emissions limits in § 63.862(a)(1)(ii) and
seeking to perform the actions in
paragraph (b)(3)(i) or (ii) of this section
must recalculate the overall PM
emissions limit for the group of process
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units and resubmit the documentation
required in paragraph (b)(2) of this
section to the Administrator. All
modified PM emissions limits are
subject to approval by the
Administrator.
(c) Excess emissions report. The
owner or operator must submit
semiannual excess emissions reports
containing the information specified in
paragraphs (c)(1) through (5) of this
section. The owner or operator must
submit semiannual excess emission
reports following the procedure
specified in paragraph (d)(2) of this
section.
(1) If the total duration of excess
emissions or process control system
parameter exceedances for the reporting
period is less than 1-percent of the total
reporting period operating time, and
CMS downtime is less than 5-percent of
the total reporting period operating
time, only the summary report is
required to be submitted in accordance
with § 63.10(e)(3)(vii). This report will
be titled ‘‘Summary Report—Gaseous
and Opacity Excess Emissions and
Continuous Monitoring System
Performance’’ in accordance with
§ 63.10(e)(3)(vi) and must contain the
information required in § 63.10(e)(3), as
specified in paragraphs (c)(1)(i) through
(x) of this section. When no exceedances
of parameters have occurred, the owner
or operator must submit the summary
report stating that no excess emissions
occurred during the reporting period. In
addition to a statement verifying that no
excess emissions occurred during the
reporting period, this report must
contain the information required in
§ 63.10(e)(3) only as specified in
paragraphs (c)(1)(i) through (x) of this
section. The summary report must be
submitted following the procedure
specified in paragraph (d)(2) of this
section.
(i) The company name and address
and name of the affected facility.
(ii) Beginning and ending dates of the
reporting period.
(iii) An identification of each process
unit with the corresponding air
pollution control device, being included
in the semiannual report, including the
pollutants monitored at each process
unit, and the total operating time for
each process unit.
(iv) An identification of the applicable
emission limits, operating parameter
limits, and averaging times.
(v) An identification of the monitoring
equipment used for each process unit
and the corresponding model number.
(vi) Date of the last CMS certification
or audit.
(vii) An emission data summary,
including the total duration of excess
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emissions (recorded in minutes for
opacity and hours for gases), the
duration of excess emissions expressed
as a percent of operating time, and
reason for the excess emissions (e.g.,
startup/shutdown, control equipment
problems, other known reasons, or other
unknown reasons).
(viii) A CMS performance summary,
including the total duration of CMS
downtime, the duration of downtime
expressed as a percent of operating time,
and reason for the downtime (e.g.,
monitoring equipment malfunction,
non-monitoring equipment malfunction,
quality assurance, quality control
calibrations, other known causes, or
other unknown causes).
(ix) A description of changes to CMS,
processes, or controls since last
reporting period.
(x) A certification by a certifying
official of truth, accuracy and
completeness. This will state that, based
on information and belief formed after
reasonable inquiry, the statements and
information in the document are true,
accurate, and complete.
(2) [Reserved]
(3) If measured parameters meet any
of the conditions specified in
§ 63.864(k)(1) or (2), the owner or
operator of the affected source must
submit a semiannual report describing
the excess emissions that occurred. If
the total duration of monitoring
exceedances for the reporting period is
1-percent or greater of the total reporting
period operating time, or the total CMS
downtime for the reporting period is 5percent or greater of the total reporting
period operating time, or any violations
according to § 63.864(k)(2) occurred,
information from both the summary
report and the excess emissions and
continuous monitoring system
performance report must be submitted.
This report will be titled ‘‘Excess
Emissions and Continuous Monitoring
System Performance Report’’ and must
contain the information specified in
paragraphs (c)(1)(i) through (x) of this
section, in addition to the information
required in § 63.10(c)(5) through (14), as
specified in paragraphs (c)(3)(i) through
(vi) of this section. Reporting
monitoring exceedances does not
constitute a violation of the applicable
standard unless the criteria in
§ 63.864(k)(2) are reached.
(i) An identification of the date and
time identifying each period during
which the CMS was inoperative except
for zero (low-level) and high-level
checks.
(ii) An identification of the date and
time identifying each period during
which the CMS was out of control, as
defined in § 63.8(c)(7).
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22:02 Dec 29, 2016
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(iii) The specific identification of each
period of excess emissions and
parameter monitoring exceedances as
described in paragraphs (c)(3)(iii)(A)
through (C) of this section.
(A) For opacity:
(1) The total number of 6-minute
averages in the reporting period
(excluding process unit downtime).
(2) The number of 6-minute averages
in the reporting period removed due to
invalid readings.
(3) The number of 6-minute averages
in the reporting period that exceeded
the 20-percent opacity limit.
(4) The percent of 6-minute averages
in the reporting period that exceed the
20-percent opacity limit.
(5) An identification of each
exceedance by start time, date, and
cause of exceedance (including startup/
shutdown, control equipment problems,
other known reasons, or other unknown
reasons).
(B) For ESP operating parameters:
(1) The type of operating parameters
monitored for compliance (total
secondary power, or secondary voltage
and secondary current).
(2) The operating limits established
during the performance test.
(3) For systems only controlled with
an ESP, the operating parameters
averaged over the semiannual reporting
period.
(4) For combined ESP and wet
scrubber control systems, the number of
3-hour ESP and wet scrubber parameter
averages below the minimum operating
limit established during the
performance test.
(5) An identification of each
exceedance by start time, date, and
cause of exceedance (including startup/
shutdown, control equipment problems,
other known reasons, or other unknown
reasons).
(C) For wet scrubber operating
parameters:
(1) The operating limits established
during the performance test for
scrubbing liquid flow rate and pressure
drop across the scrubber (or fan
amperage if used for smelt dissolving
tank scrubbers).
(2) The number of 3-hour wet
scrubber parameter averages below the
minimum operating limit established
during the performance test, if
applicable.
(3) An identification of each
exceedance by start time, date, and
cause of exceedance (including startup/
shutdown, control equipment problems,
other known reasons, or other unknown
reasons).
(D) For RTO operating temperature:
(1) The operating limit established
during the performance test.
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Sfmt 4702
97091
(2) The number of 1-hour and 3-hour
temperature averages below the
minimum operating limit established
during the performance test.
(3) An identification of each
exceedance by start time, date, and
cause of exceedance including startup/
shutdown, control equipment problems,
other known reasons, or other unknown
reasons).
(iv) The nature and cause of any
malfunction (if known).
(v) The corrective action taken or
preventative measures adopted.
(vi) The nature of repairs and
adjustments to the CMS that was
inoperative or out of control.
(4) If a source fails to meet an
applicable standard, report such events
in the semiannual excess emissions
report. Report the number of failures to
meet an applicable standard. For each
instance, report the date, time and
duration of each failure. For each failure
the report must include a list of the
affected sources or equipment, an
estimate of the quantity of each
regulated pollutant emitted over any
emission limit, and a description of the
method used to estimate the emissions.
(5) The owner or operator of an
affected source or process unit subject to
the requirements of this subpart and
subpart S of this part may combine
excess emissions and/or summary
reports for the mill.
(d) Electronic reporting. (1) Within 60
days after the date of completing each
performance test (as defined in § 63.2)
required by this subpart, the owner or
operator must submit the results of the
performance test following the
procedure specified in either paragraph
(d)(1)(i) or (ii) of this section.
(i) For data collected using test
methods supported by the EPA’s
Electronic Reporting Tool (ERT) as
listed on the EPA’s ERT Web site
(https://www.epa.gov/electronicreporting-air-emissions/electronicreporting-tool-ert) at the time of the test,
the owner or operator must submit the
results of the performance test to the
EPA via the Compliance and Emissions
Data Reporting Interface (CEDRI).
(CEDRI can be accessed through the
EPA’s Central Data Exchange (CDX)
(https://cdx.epa.gov/).) Performance test
data must be submitted in a file format
generated through the use of the EPA’s
ERT or an alternate electronic file
format consistent with the extensible
markup language (XML) schema listed
on the EPA’s ERT Web site. If the owner
or operator claims that some of the
performance test information being
submitted is confidential business
information (CBI), the owner or operator
must submit a complete file generated
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through the use of the EPA’s ERT or an
alternate electronic file consistent with
the XML schema listed on the EPA’s
ERT Web site, including information
claimed to be CBI, on a compact disc,
flash drive, or other commonly used
electronic storage media to the EPA. The
electronic media must be clearly marked
as CBI and mailed to U.S. EPA/OAPQS/
CORE CBI Office, Attention: Group
Leader, Measurement Policy Group, MD
C404–02, 4930 Old Page Rd., Durham,
NC 27703. The same ERT or alternate
file with the CBI omitted must be
submitted to the EPA via the EPA’s CDX
as described earlier in this paragraph
(d)(1)(i).
(ii) For data collected using test
methods that are not supported by the
EPA’s ERT as listed on the EPA’s ERT
Web site at the time of the test, the
owner or operator must attach an
electronic copy of the complete
performance test report containing the
methods not included in the ERT in the
attachment module of the ERT in
portable document format (PDF) and
submit the results of the performance
test to the EPA via CEDRI.
(2) The owner or operator must
submit notification and semiannual
reports to the EPA via the CEDRI.
(CEDRI can be accessed through the
EPA’s CDX (https://cdx.epa.gov).) The
owner or operator must use the
appropriate electronic report in CEDRI
for this subpart or an alternative
electronic file format consistent with the
XML schema listed on the CEDRI Web
site (https://www.epa.gov/electronicreporting-air-emissions/complianceand-emissions-data-reporting-interfacecedri). If neither the reporting form nor
the spreadsheet template specific to this
subpart are available in CEDRI at the
time that the report is due, you must
upload an electronic copy of the report
in CEDRI. Once the form or spreadsheet
template has been available in CEDRI
for at least 90 calendar days, you must
begin submitting all subsequent reports
via CEDRI using the form or spreadsheet
template. The reports must be submitted
by the deadlines specified in this
subpart, regardless of the method in
which the reports are submitted.
■ 11. Section 63.868 is amended by
revising paragraphs (b)(2) through (4) to
read as follows:
§ 63.868
Delegation of authority.
*
*
*
*
*
(b) * * *
(2) Approval of a major change to test
method under § 63.7(e)(2)(ii) and (f) and
as defined in § 63.90.
(3) Approval of a major change to
monitoring under § 63.8(f) and as
defined in § 63.90.
(4) Approval of a major change to
recordkeeping/reporting under § 63.10(f)
and as defined in § 63.90.
■ 12. Table 1 to subpart MM of part 63
is revised to read as follows:
TABLE 1 TO SUBPART MM OF PART 63—GENERAL PROVISIONS APPLICABILITY TO SUBPART MM
General provisions reference
Summary of requirements
Applies to subpart MM
Explanation
63.1(a)(1) .....................
General applicability of the General Provisions.
Yes .............................
Additional terms defined in § 63.861; when
overlap between subparts A and MM of
this part, subpart MM takes precedence.
63.1(a)(2)–(14) ............
Yes.
63.1(b)(1) .....................
General applicability of the General Provisions.
Initial applicability determination .....................
63.1(b)(2) .....................
Title V operating permit—see 40 CFR part 70
Yes .............................
63.1(b)(3) .....................
Record of the applicability determination .......
No ...............................
63.1(c)(1) .....................
Applicability of subpart A of this part after a
relevant standard has been set.
Yes .............................
63.1(c)(2) .....................
Title V permit requirement ..............................
Yes .............................
63.1(c)(3) .....................
63.1(c)(4) .....................
[Reserved] .......................................................
Requirements for existing source that obtains
an extension of compliance.
Notification requirements for an area source
that increases HAP emissions to major
source levels.
[Reserved] .......................................................
Applicability of permit program before a relevant standard has been set.
Definitions .......................................................
No.
Yes.
63.1(c)(5) .....................
63.1(d) .........................
63.1(e) .........................
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63.2 ..............................
63.3 ..............................
63.4 ..............................
63.5(a) .........................
63.5(b)(1) .....................
63.5(b)(2)
63.5(b)(3)
63.5(b)(4)
63.5(b)(5)
63.5(b)(6)
.....................
.....................
.....................
.....................
.....................
VerDate Sep<11>2014
Units and abbreviations ..................................
Prohibited activities and circumvention ..........
Construction and reconstruction—applicability
Upon construction, relevant standards for
new sources.
[Reserved] .......................................................
New construction/reconstruction .....................
Construction/reconstruction notification ..........
Construction/reconstruction compliance .........
Equipment addition or process change ..........
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No ...............................
Subpart MM specifies the applicability in
§ 63.860.
All major affected sources are required to obtain a title V permit.
All affected sources are subject to subpart
MM according to the applicability definition
of subpart MM.
Subpart MM clarifies the applicability of each
paragraph of subpart A of this part to
sources subject to subpart MM.
All major affected sources are required to obtain a title V permit. There are no area
sources in the pulp and paper mill source
category.
Yes.
No.
Yes.
Yes .............................
Additional terms defined in § 63.861; when
overlap between subparts A and MM of
this part occurs, subpart MM takes precedence.
Yes.
Yes.
Yes.
Yes.
No.
Yes.
Yes.
Yes.
Yes.
Sfmt 4702
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97093
TABLE 1 TO SUBPART MM OF PART 63—GENERAL PROVISIONS APPLICABILITY TO SUBPART MM—Continued
General provisions reference
Summary of requirements
63.5(c) .........................
63.5(d) .........................
[Reserved] .......................................................
Application for approval of construction/reconstruction.
Construction/reconstruction approval .............
Construction/reconstruction approval based
on prior State preconstruction review.
Compliance with standards and maintenance
requirements—applicability.
Requirements for area source that increases
emissions to become major.
Compliance dates for new and reconstructed
sources.
Compliance dates for existing sources ...........
63.5(e) .........................
63.5(f) ..........................
63.6(a)(1) .....................
63.6(a)(2) .....................
63.6(b) .........................
63.6(c) .........................
63.6(d) .........................
63.6(e)(1)(i) ..................
63.6(e)(1)(ii) .................
63.6(e)(1)(iii) ................
63.6(e)(2) .....................
63.6(e)(3) .....................
63.6(f)(1) ......................
63.6(f)(2)–(3) ...............
63.6(g) .........................
63.6(h)(1) .....................
63.6(h)(2)–(9) ..............
63.6(i) ..........................
Applies to subpart MM
[Reserved] .......................................................
General duty to minimize emissions ...............
Requirement to correct malfunctions ASAP ...
Operation and maintenance requirements enforceable independent of emissions limitations.
[Reserved] .......................................................
Startup, shutdown, and malfunction plan
(SSMP).
Compliance with nonopacity emissions standards except during SSM.
Methods for determining compliance with
nonopacity emissions standards.
Compliance with alternative nonopacity emissions standards.
Compliance with opacity and visible emissions (VE) standards except during SSM.
Compliance with opacity and VE standards ...
No.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes, except for
sources granted extensions under
§ 63.863(c).
No.
No ...............................
No.
Yes.
Yes.
Yes.
No.
Yes .............................
63.8(a)(1)
63.8(a)(2)
63.8(a)(3)
63.8(a)(4)
.....................
.....................
.....................
.....................
Monitoring requirements—applicability ...........
Performance Specifications ............................
[Reserved] .......................................................
Monitoring with flares ......................................
Yes .............................
Yes.
No.
No ...............................
63.8(b)(1) .....................
63.8(b)(2)–(3) ..............
Conduct of monitoring .....................................
Specific requirements for installing and reporting on monitoring systems.
Operation and maintenance of CMS ..............
General duty to minimize emissions and CMS
operation.
Yes .............................
Yes.
63.7(a)(2) .....................
63.7(a)(3) .....................
63.7(a)(4) .....................
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63.7(b)(1) .....................
63.7(b)(2) .....................
63.8(c)(1) .....................
63.8(c)(1)(i) ..................
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See § 63.860(d) for general duty requirement.
No.
63.7(c) .........................
63.7(d) .........................
63.7(e)(1) .....................
63.7(e)(2)–(3) ..............
63.7(e)(4) .....................
63.7(f) ..........................
63.7(g) .........................
63.7(h) .........................
63.7(a)(1) .....................
Subpart MM specifically stipulates the compliance schedule for existing sources.
No.
No.
Extension of compliance with emission standards.
Exemption from compliance with emissions
standards.
Performance testing requirements—applicability.
Performance test dates ...................................
Performance test requests by Administrator
under CAA section 114.
Notification of delay in performance testing
due to force majeure.
Notification of performance test ......................
Notification of delay in conducting a scheduled performance test.
Quality assurance program .............................
Performance testing facilities ..........................
Conduct of performance tests ........................
Conduct of performance tests ........................
Testing under section 114 ..............................
Use of an alternative test method ..................
Data analysis, recordkeeping, and reporting ..
Waiver of performance tests ...........................
63.6(j) ..........................
Explanation
Subpart MM does not contain any opacity or
VE standards; however, § 63.864 specifies
opacity monitoring requirements.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
No ...............................
Yes.
Yes.
Yes.
Yes.
Yes .............................
Yes .............................
No.
Sfmt 4702
See § 63.865.
§ 63.865(c)(1) specifies the only exemption
from performance testing allowed under
subpart MM.
See § 63.864.
The use of flares to meet the standards in
subpart MM is not anticipated.
See § 63.864.
See § 63.864.
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TABLE 1 TO SUBPART MM OF PART 63—GENERAL PROVISIONS APPLICABILITY TO SUBPART MM—Continued
General provisions reference
Summary of requirements
63.8(c)(1)(ii) .................
Reporting requirements for SSM when action
not described in SSMP.
Requirement to develop SSM plan for CMS ..
Monitoring system installation .........................
CMS requirements ..........................................
Continuous
opacity
monitoring
system
(COMS) minimum procedures.
Zero and high level calibration check requirements.
Out-of-control periods .....................................
CMS quality control program ..........................
Written procedures for CMS ...........................
Performance evaluation of CMS .....................
Notification of performance evaluation ...........
Submission of site-specific performance evaluation test plan.
Conduct of performance evaluation and performance evaluation dates.
Reporting performance evaluation results ......
Use of an alternative monitoring method .......
Reduction of monitoring data ..........................
Notification requirements—applicability and
general information.
Initial notifications ............................................
Request for extension of compliance .............
Notification that source subject to special
compliance requirements.
Notification of performance test ......................
Notification of opacity and VE observations ...
63.8(c)(1)(iii) ................
63.8(c)(2)–(3) ...............
63.8(c)(4) .....................
63.8(c)(5) .....................
63.8(c)(6) .....................
63.8(c)(7)–(8) ...............
63.8(d)(1)–(2) ..............
63.8(d)(3) .....................
63.8(e)(1) .....................
63.8(e)(2) .....................
63.8(e)(3) .....................
63.8(e)(4) .....................
63.8(e)(5) .....................
63.8(f) ..........................
63.8(g) .........................
63.9(a) .........................
63.9(b) .........................
63.9(c) .........................
63.9(d) .........................
63.9(e) .........................
63.9(f) ..........................
63.9(g)(1) .....................
63.9(g)(2) .....................
63.9(g)(3) .....................
63.9(h) .........................
63.9(i) ..........................
63.9(j) ..........................
63.10(a) .......................
63.10(b)(1) ...................
63.10(b)(2)(i) ................
Applies to subpart MM
Yes.
No.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes .............................
No ...............................
Yes.
Yes.
Yes.
See § 63.864.
See § 63.864(f).
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes.
Yes .............................
Additional notification requirements for
sources with CMS.
Notification of compliance with opacity emissions standard.
Notification that criterion to continue use of
alternative to relative accuracy testing has
been exceeded.
Notification of compliance status ....................
Adjustment to time periods or postmark deadlines for submittal and review of required
communications.
Change in information already provided .........
Recordkeeping
requirements—applicability
and general information.
Records retention ............................................
Recordkeeping of occurrence and duration of
startups and shutdowns.
Subpart MM does not contain any opacity or
VE standards; however, § 63.864 specifies
opacity monitoring requirements.
Yes.
Yes.
Yes .............................
Subpart MM does not contain any opacity or
VE
emissions
standards;
however,
§ 63.864 specifies opacity monitoring requirements.
Yes.
Yes.
Yes.
Yes .............................
Yes.
No ...............................
63.10(b)(2)(ii) ...............
Recordkeeping of failures to meet a standard
No ...............................
63.10(b)(2)(iii) ..............
63.10(b)(2)(iv)–(v) ........
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Explanation
Maintenance records ......................................
Actions taken to minimize emissions during
SSM.
Recordkeeping for CMS malfunctions ............
Other CMS requirements ................................
Records retention for sources not subject to
relevant standard.
Additional recordkeeping requirements for
sources with CMS..
Use of SSM plan .............................................
General reporting requirements ......................
Reporting results of performance tests ..........
See § 63.866.
See § 63.866(c)(8) for recordkeeping of the
date, time, and duration of each startup
and/or shutdown period.
See § 63.866(d) for recordkeeping of (1) date,
time and duration; (2) listing of affected
source or equipment, and an estimate of
the quantity of each regulated pollutant
emitted over the standard; and (3) actions
to minimize emissions and correct the failure.
Yes.
No.
63.10(b)(2)(vi) ..............
63.10(b)(2)(vii)-(xiv) .....
63.10(b)(3) ...................
63.10(c)(1)–(14) ...........
63.10(c)(15) .................
63.10(d)(1) ...................
63.10(d)(2) ...................
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Yes.
Yes.
Yes .............................
Applicability
§ 63.860.
Yes.
No.
Yes.
Yes.
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are
given
in
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97095
TABLE 1 TO SUBPART MM OF PART 63—GENERAL PROVISIONS APPLICABILITY TO SUBPART MM—Continued
General provisions reference
Summary of requirements
Applies to subpart MM
Explanation
63.10(d)(3) ...................
Reporting results of opacity or VE observations.
Yes .............................
Subpart MM does not include any opacity or
VE standards; however, § 63.864 specifies
opacity monitoring requirements.
63.10(d)(4) ...................
63.10(d)(5)(i) ................
Progress reports .............................................
Periodic startup, shutdown, and malfunction
reports.
Immediate startup, shutdown, and malfunction reports.
Additional reporting requirements for sources
with CMS.
Waiver of recordkeeping and reporting requirements.
Control device requirements for flares ...........
Yes.
No ...............................
State authority and delegations ......................
Addresses of State air pollution control agencies and EPA Regional Offices.
Incorporations by reference ............................
Availability of information and confidentiality ..
Requirements for Performance Track member facilities.
Yes.
Yes.
63.10(d)(5)(ii) ...............
63.10(e) .......................
63.10(f) ........................
63.11 ............................
63.12 ............................
63.13 ............................
63.14 ............................
63.15 ............................
63.16 ............................
No ...............................
See § 63.867(c)(3) for malfunction reporting
requirements.
See § 63.867(c)(3) for malfunction reporting
requirements.
Yes.
Yes.
No ...............................
The use of flares to meet the standards in
subpart MM is not anticipated.
Yes.
Yes.
Yes.
[FR Doc. 2016–30758 Filed 12–29–16; 8:45 am]
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Agencies
[Federal Register Volume 81, Number 251 (Friday, December 30, 2016)]
[Proposed Rules]
[Pages 97046-97095]
From the Federal Register Online via the Government Publishing Office [www.gpo.gov]
[FR Doc No: 2016-30758]
[[Page 97045]]
Vol. 81
Friday,
No. 251
December 30, 2016
Part V
Environmental Protection Agency
-----------------------------------------------------------------------
40 CFR Part 63
National Emission Standards for Hazardous Air Pollutants for Chemical
Recovery Combustion Sources at Kraft, Soda, Sulfite, and Stand-Alone
Semichemical Pulp Mills; Proposed Rule
Federal Register / Vol. 81 , No. 251 / Friday, December 30, 2016 /
Proposed Rules
[[Page 97046]]
-----------------------------------------------------------------------
ENVIRONMENTAL PROTECTION AGENCY
40 CFR Part 63
[EPA-HQ-OAR-2014-0741; FRL-9957-07-OAR]
RIN 2060-AS46
National Emission Standards for Hazardous Air Pollutants for
Chemical Recovery Combustion Sources at Kraft, Soda, Sulfite, and
Stand-Alone Semichemical Pulp Mills
AGENCY: Environmental Protection Agency (EPA).
ACTION: Proposed rule.
-----------------------------------------------------------------------
SUMMARY: The Environmental Protection Agency (EPA) is proposing
amendments to the National Emission Standards for Hazardous Air
Pollutants (NESHAP) for Chemical Recovery Combustion Sources at Kraft,
Soda, Sulfite, and Stand-Alone Semichemical Pulp Mills to address the
results of the residual risk and technology review (RTR) that the EPA
is required to conduct under the Clean Air Act (CAA). These proposed
amendments include revisions to the opacity monitoring provisions;
addition of electrostatic precipitator (ESP) parameter monitoring
provisions; a requirement for 5-year periodic emissions testing;
revisions to provisions addressing periods of startup, shutdown, and
malfunction (SSM); and technical and editorial changes. The EPA is
proposing these amendments to improve the effectiveness of the rule.
DATES: Comments. Comments must be received on or before February 28,
2017. Under the Paperwork Reduction Act (PRA), comments on the
information collection provisions are best assured of consideration if
the Office of Management and Budget (OMB) receives a copy of your
comments on or before January 30, 2017.
Public Hearing. A public hearing will be held if requested by
January 4, 2017.
ADDRESSES: Comments. Submit your comments, identified by Docket ID No.
EPA-HQ-OAR-2014-0741, at https://www.regulations.gov. Follow the online
instructions for submitting comments. Once submitted, comments cannot
be edited or removed from Regulations.gov. The EPA may publish any
comment received to its public docket. Do not submit electronically any
information you consider to be Confidential Business Information (CBI)
or other information whose disclosure is restricted by statute.
Multimedia submissions (audio, video, etc.) must be accompanied by a
written comment. The written comment is considered the official comment
and should include discussion of all points you wish to make. The EPA
will generally not consider comments or comment contents located
outside of the primary submission (i.e., on the Web, cloud, or other
file sharing system). For additional submission methods, the full EPA
public comment policy, information about CBI or multimedia submissions,
and general guidance on making effective comments, please visit https://www2.epa.gov/dockets/commenting-epa-dockets.
Instructions. Direct your comments to Docket ID No. EPA-HQ-OAR-
2014-0741. The 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 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 email. The
https://www.regulations.gov Web site is an ``anonymous access'' system,
which means the EPA will not know your identity or contact information
unless you provide it in the body of your comment. If you send an email
comment directly to the EPA without going through https://www.regulations.gov, your email 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, the 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 the EPA cannot read your comment due to technical
difficulties and cannot contact you for clarification, the EPA may not
be able to consider your comment. Electronic files should not include
special characters or any form of encryption and be free of any defects
or viruses. For additional information about the EPA's public docket,
visit the EPA Docket Center homepage at https://www.epa.gov/dockets.
Docket. The EPA has established a docket for this rulemaking under
Docket ID No. EPA-HQ-OAR-2014-0741. All documents in the docket are
listed in the 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, is not placed on the Internet and will be
publicly available only in hard copy. Publicly available docket
materials are available either electronically in Regulations.gov or in
hard copy at the EPA Docket Center, Room 3334, EPA WJC West Building,
1301 Constitution Ave. NW., Washington, DC. The Public Reading Room 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 EPA Docket Center is
(202) 566-1742.
Public Hearing. A public hearing will be held, if requested by
January 4, 2017, to accept oral comments on this proposed action. If a
hearing is requested, it will be held at the EPA's Washington, DC
campus located at 1201 Constitution Avenue NW., Washington, DC. The
hearing, if requested, will begin at 9:00 a.m. (local time) and will
conclude at 5:00 p.m. (local time) on January 17, 2017. To request a
hearing, to register to speak at a hearing, or to inquire if a hearing
will be held, please contact Ms. Aimee St. Clair at (919) 541-1063 or
by email at stclair.aimee@epa.gov. The last day to pre-register to
speak at a hearing, if one is held, will be January 12, 2017.
Additionally, requests to speak will be taken the day of the
hearing at the hearing registration desk, although preferences on
speaking times may not be able to be fulfilled. Please note that
registration requests received before the hearing will be confirmed by
the EPA via email. The EPA will make every effort to accommodate all
speakers who arrive and register. Because the hearing will be held at a
United States governmental facility, individuals planning to attend the
hearing should be prepared to show valid picture identification to the
security staff in order to gain access to the meeting room. Please note
that the REAL ID Act, passed by Congress in 2005, established new
requirements for entering federal facilities. If your driver's license
is issued by Alaska, American Samoa, Arizona, Kentucky, Louisiana,
Maine, Massachusetts, Minnesota, Montana, New York, Oklahoma or the
state of Washington, you must present an additional form of
identification to enter the federal building. Acceptable alternative
forms of identification include: Federal employee badges, passports,
enhanced driver's licenses and military identification cards. In
addition, you will need to obtain a property pass for any personal
belongings you bring with you. Upon leaving the building, you will be
required to return this property pass to
[[Page 97047]]
the security desk. No large signs will be allowed in the building,
cameras may only be used outside of the building and demonstrations
will not be allowed on federal property for security reasons.
Please note that any updates made to any aspect of the hearing,
including whether or not a hearing will be held, will be posted online
at https://www.epa.gov/stationary-sources-air-pollution/kraft-soda-sulfite-and-stand-alone-semichemical-pulp-mills-mact-ii. We ask that
you contact Ms. Aimee St. Clair at (919) 541-1063 or by email at
stclair.aimee@epa.gov or monitor our Web site to determine if a hearing
will be held. The EPA does not intend to publish a notice in the
Federal Register announcing any such updates. Please go to https://www.epa.gov/stationary-sources-air-pollution/kraft-soda-sulfite-and-stand-alone-semichemical-pulp-mills-mact-ii for more information on the
public hearing.
FOR FURTHER INFORMATION CONTACT: For questions about this proposed
action, contact Dr. Kelley Spence, Sector Policies and Programs
Division (Mail Code: E143-03), Office of Air Quality Planning and
Standards, U.S. Environmental Protection Agency, Research Triangle
Park, North Carolina 27711; telephone number: (919) 541-3158; fax
number: (919) 541-3470; and email address: spence.kelley@epa.gov. For
specific information regarding the risk modeling methodology, contact
Mr. James Hirtz, Health and Environmental Impacts Division (Mail Code:
C539-02), Office of Air Quality Planning and Standards, U.S.
Environmental Protection Agency, Research Triangle Park, North Carolina
27711; telephone number: (919) 541-0881; fax number: (919) 541-0840;
and email address: hirtz.james@epa.gov. For information about the
applicability of the NESHAP to a particular entity, contact Ms. Sara
Ayres, Office of Enforcement and Compliance Assurance, U.S.
Environmental Protection Agency, USEPA Region 5 (Mail Code: E-19J), 77
West Jackson Boulevard, Chicago IL 60604; telephone number: (312) 353-
6266; and email address: ayres.sara@epa.gov.
SUPPLEMENTARY INFORMATION:
Preamble Acronyms and Abbreviations. We use multiple acronyms and
terms in this preamble. While this list may not be exhaustive, to ease
the reading of this preamble and for reference purposes, the EPA
defines the following terms and acronyms here:
AEGL acute exposure guideline levels
AERMOD air dispersion model used by the HEM-3 model
ANSI American National Standards Institute
ASME American Society of Mechanical Engineers
ASTM American Society for Testing and Materials
ATSDR Agency for Toxic Substances and Disease Registry
BACT best available control technology
BAT best available technology
BLO black liquor oxidation
BLS black liquor solids
CAA Clean Air Act
CaCO3 calcium carbonate
CalEPA California EPA
CBI Confidential Business Information
CEDRI Compliance and Emissions Data Reporting Interface
CFR Code of Federal Regulations
CMS continuous monitoring system
COMS continuous opacity monitoring system
CPMS continuous parameter monitoring system
DCE direct contact evaporator
EJ environmental justice
EPA Environmental Protection Agency
ERPG Emergency Response Planning Guidelines
ERT Electronic Reporting Tool
ESP electrostatic precipitator
FR Federal Register
gr/dscf grains per dry standard cubic foot
HAP hazardous air pollutant
HCCPD hexachlorocyclopentadiene
HCl hydrochloric acid
HEM-3 Human Exposure Model, Version 1.1.0
HF hydrogen fluoride
HI hazard index
HQ hazard quotient
IBR incorporation by reference
ICR Information Collection Request
IRIS Integrated Risk Information System
km kilometer
LAER lowest achievable emission rate
lb/hr pounds per hour
lb/ton pounds per ton
LOAEL lowest-observed-adverse-effect level
MACT maximum achievable control technology
mg/kg-day milligrams per kilogram per day
mg/m\3\ milligrams per cubic meter
MIR maximum individual risk
Na2CO3 sodium carbonate
Na2S sodium sulfide
NAAQS National Ambient Air Quality Standards
NAC National Advisory Committee
NAICS North American Industry Classification System
NaOH sodium hydroxide
NAS National Academy of Sciences
NATA National Air Toxics Assessment
NCASI National Council for Air and Stream Improvement
NDCE nondirect contact evaporator
NEI National Emissions Inventory
NESHAP National Emission Standards for Hazardous Air Pollutants
NH3 ammonia
NOAA National Oceanic and Atmospheric Administration
NOAEL no-observed-adverse-effect level
NRC National Research Council
NRDC Natural Resources Defense Council
NSPS New Source Performance Standards
NTTAA National Technology Transfer and Advancement Act
O&M operation and maintenance
O2 oxygen
OAQPS Office of Air Quality Planning and Standards
OMB Office of Management and Budget
PAH polycyclic aromatic hydrocarbons
PB-HAP hazardous air pollutant known to be persistent and bio-
accumulative in the environment
PDF portable document format
PEL probable effects level
PM particulate matter
PM2.5 fine particles (particulate matter with particles
less than 2.5 micrometers in diameter)
POM polycyclic organic matter
ppm parts per million
PRA Paperwork Reduction Act
PTC Performance Test Code
QA quality assurance
RACT reasonably available control technology
RBLC RACT/BACT/LAER Clearinghouse
REL reference exposure level
RFA Regulatory Flexibility Act
RfC reference concentration
RfD reference dose
RTO regenerative thermal oxidizer
RTR residual risk and technology review
SAB Science Advisory Board
SCC source classification code
SDT smelt dissolving tank
SOP standard operating procedure
SSM startup, shutdown, and malfunction
STAPPA/ State and Territorial Air Pollution Program
ALAPCO Administrators/Association of Local Air Pollution Control
Officers
TEQ toxic equivalent
THC total hydrocarbon
TOSHI target organ-specific hazard index
tpy tons per year
TRIM.FaTE Total Risk Integrated Methodology.Fate, Transport, and
Ecological Exposure model
TRS total reduced sulfur
UF uncertainty factor
[mu]g/m3 micrograms per cubic meter
UMRA Unfunded Mandates Reform Act
URE unit risk estimate
yr year
Organization of this Document. The information in this preamble is
organized as follows:
I. General Information
A. Executive Summary
B. Does this action apply to me?
C. Where can I get a copy of this document and other related
information?
D. What should I consider as I prepare my comments for the EPA?
II. Background
A. What is the statutory authority for this action?
B. What is this source category and how does the current NESHAP
regulate its HAP emissions?
C. What data collection activities were conducted to support
this action?
D. What other relevant background information and data are
available?
III. Analytical Procedures
[[Page 97048]]
A. How did we estimate post-MACT risks posed by the source
category?
B. How did we consider the risk results in making decisions for
this proposal?
C. How did we perform the technology review?
IV. Analytical Results and Proposed Decisions
A. What are the results of the risk assessment and analyses?
B. What are our proposed decisions regarding risk acceptability,
ample margin of safety, and adverse environmental effects?
C. What are the results and proposed decisions based on our
technology review?
D. What other actions are we proposing?
E. What compliance dates are we proposing?
V. Summary of Cost, Environmental, and Economic Impacts
A. What are the affected sources?
B. What are the air quality impacts?
C. What are the cost impacts?
D. What are the economic impacts?
E. What are the benefits?
VI. Request for Comments
VII. Submitting Data Corrections
VIII. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory Planning and Review and
Executive Order 13563: Improving Regulation and Regulatory Review
B. Paperwork Reduction Act (PRA)
C. Regulatory Flexibility Act (RFA)
D. Unfunded Mandates Reform Act (UMRA)
E. Executive Order 13132: Federalism
F. Executive Order 13175: Consultation and Coordination with
Indian Tribal Governments
G. Executive Order 13045: Protection of Children from
Environmental Health Risks 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 (NTTAA) and
1 CFR part 51
J. Executive Order 12898: Federal Actions to Address
Environmental Justice in Minority Populations and Low-Income
Populations
I. General Information
A. Executive Summary
1. Purpose of the Regulatory Action
Section 112(f)(2) of the CAA requires the EPA to analyze and
address the residual risk associated with hazardous air pollutant
emissions from source categories subject to maximum achievable control
technology (MACT) standards. This review, known as the residual risk
review, is a one-time review that the statute provides will be done
within 8 years of issuance of the MACT standard. Section 112(d)(6) of
the CAA requires the EPA to review and revise CAA section 112 emissions
standards, as necessary, taking into account developments in practices,
processes, and control technologies. Emission standards promulgated
under CAA section 112 are to be reviewed no less often than every 8
years. The EPA issued the NESHAP for Chemical Recovery Combustion
Sources at Kraft, Soda, Sulfite, and Stand-Alone Semichemical Mills (40
Code of Federal Regulations (CFR) part 63, subpart MM) in 2001. The
2001 emission standards are due for review under CAA sections 112(d)(6)
and 112(f)(2). In addition to conducting the RTR for subpart MM, we are
evaluating the SSM provisions in the rule in light of the United States
Court of Appeals for the District of Columbia Circuit decision in
Sierra Club v. EPA, 551 F.3d 1019 (D.C. Cir. 2008). As explained in
section IV of this preamble, in the Sierra Club case, the D.C. Circuit
vacated the SSM exemption provisions in the General Provisions for
nonopacity and opacity standards. Finally, the EPA evaluated the rule
to determine if additional amendments were warranted or necessary to
ensure continuous compliance with the standard and to promote
consistency with other standards.
2. Summary of the Major Proposed Revisions
The EPA is not proposing to make any changes pursuant to 112(f)(2)
as a result of its residual risk review. The EPA is proposing to reduce
opacity limits as a result of the technology review under CAA section
112(d)(6). In addition, we are proposing the following as part of the
technology review: Revising the opacity monitoring provisions,
requiring ESP parameter monitoring for processes equipped with ESPs,
clarifying the monitoring for combined ESP/wet scrubber controls, and
providing alternative monitoring for smelt dissolving tank (SDT) wet
scrubbers.
As an additional action, we are proposing to improve the compliance
provisions of the subpart by proposing to require periodic air
emissions performance testing once every 5 years for facilities subject
to the standards for Chemical Recovery Combustion Sources at Kraft,
Soda, Sulfite, and Stand-Alone Semichemical Pulp Mills. To address the
SSM exemptions, we are proposing amendments to subpart MM that will (1)
require facilities to meet the standard at all times, including during
periods of SSM, and (2) provide alternative monitoring parameters for
wet scrubbers and ESPs during these periods. We are also proposing
changes to the subpart MM NESHAP and the General Provisions
applicability table to eliminate the SSM exemption. To increase the
ease and efficiency of data submittal and improve data accessibility,
we are proposing to require mills to submit electronic copies of
compliance reports, which includes performance test reports.
We are also proposing a number of technical and editorial changes.
These changes include the following: Clarifying the location in 40 CFR
part 60 of applicable EPA test methods; updating the facility name for
Cosmo Specialty Fibers; revising the definitions section in 40 CFR
63.861; corrected misspelling in 40 CFR 63.862(c), revising multiple
sections to remove reference to former smelters and former black liquor
gasification system at Georgia-Pacific's facility in Big Island,
Virginia; revising the monitoring requirements section; revising the
performance test requirements section to specify the conditions for
conducting performance tests and to revise the ambient O2 concentration
in Equations 7 and 8; revising the recordkeeping requirements section
in 40 CFR 63.866 to include the requirement to record information on
failures to meet the applicable standard; revising the terminology in
the delegation of authority section in 40 CFR 63.868 to match the
definitions in 40 CFR 63.90; and revising the General Provisions
applicability table (Table 1 to subpart MM of part 63) to align with
those sections of the General Provisions that have been amended or
reserved over time.
3. Costs and Benefits
Table 1 summarizes the costs of this action. See section V of this
preamble for further discussion.
Table 1--Summary of the Costs of This Proposed Action
------------------------------------------------------------------------
Capital cost, Annual cost, $
Requirement $ million million
------------------------------------------------------------------------
Change in opacity monitoring provisions 42 8.8
for recovery furnaces and lime kilns...
ESP parameter monitoring................ 5.7 1.4
[[Page 97049]]
Periodic emissions testing.............. .............. 1.1
Incremental reporting/recordkeeping..... 0.50 1.9
-------------------------------
Total nationwide.................... 48 13
------------------------------------------------------------------------
The EPA estimates that the proposed changes to the opacity limits
and monitoring allowances will reduce PM emissions by approximately 235
(tons per year) tpy and fine particle (PM2.5) emissions by
approximately 112 tpy. Periodic testing will tend to reduce emissions
by providing incentive for facilities to maintain their control systems
and make periodic adjustments to ensure peak performance. Eliminating
the SSM exemption will reduce emissions by requiring facilities to meet
the applicable standard during SSM periods. See section V of this
preamble for further discussion.
B. Does this action apply to me?
Table 2 of this preamble lists the NESHAP and associated regulated
industrial source categories that are the subject of this proposal.
Table 2 is not intended to be exhaustive, but rather provides a guide
for readers regarding the entities that this proposed action is likely
to affect. The proposed standards, once promulgated, will be directly
applicable to the affected sources. Federal, state, local, and tribal
government entities would not be affected by this proposed action. As
defined in the Initial List of Categories of Sources Under Section
112(c)(1) of the Clean Air Act Amendments of 1990 (see 57 FR 31576,
July 16, 1992), the ``Pulp and Paper Production'' source category is
any facility engaged in the production of pulp and/or paper. The EPA
developed the NESHAPs for the source category in phases. This NESHAP,
40 CFR part 63, subpart MM, regulates chemical recovery combustion
sources at kraft, soda, sulfite, and stand-alone semichemical pulp
mills. The NESHAP for non-combustion sources (40 CFR part 63, subpart
S) regulates non-combustion processes at mills that (1) chemically pulp
wood fiber (using kraft, sulfite, soda, and semichemical methods), (2)
mechanically pulp wood fiber (e.g., groundwood, thermomechanical,
pressurized), (3) pulp secondary fibers (deinked and non-deinked), (4)
pulp non-wood material, and (5) manufacture paper. This proposal only
addresses the RTR for subpart MM, and does not propose any amendments
to subpart S.
Table 2--NESHAP and Industrial Source Categories Affected by This Proposed Action
----------------------------------------------------------------------------------------------------------------
Source category NESHAP NAICS code \a\
----------------------------------------------------------------------------------------------------------------
Pulp and Paper Production...................... Chemical Recovery Combustion Sources 32211, 32212, 32213
at Kraft, Soda, Sulfite, and Stand-
Alone Semichemical Pulp Mills.
----------------------------------------------------------------------------------------------------------------
\a\ North American Industry Classification System.
C. Where can I get a copy of this document and other related
information?
In addition to being available in the docket, an electronic copy of
this action is available on the Internet through the EPA's Stationary
Sources of Air Pollution Web site, a forum for information and
technology exchange in various areas of air pollution control. A
redline version of the regulatory language that incorporates the
proposed changes in this action is available in the docket for this
action (Docket ID No. EPA-HQ-OAR-2014-0741). Following signature by the
EPA Administrator, the EPA will post a copy of this proposed action at:
https://www.epa.gov/stationary-sources-air-pollution/kraft-soda-sulfite-and-stand-alone-semichemical-pulp-mills-mact-ii. Following
publication in the Federal Register, the EPA will post the Federal
Register version of the proposal and key technical documents at this
same Web site. Information on the overall RTR program is available at
https://www3.epa.gov/ttn/atw/rrisk/rtrpg.html.
D. What should I consider as I prepare my comments for the EPA?
Submitting CBI. Do not submit information containing CBI to the EPA
through https://www.regulations.gov or email. 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 the 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 comments that includes information claimed
as CBI, you must submit a copy of the comments that does not contain
the information claimed as CBI for inclusion in the public docket. If
you submit a CD-ROM or disk that does not contain CBI, mark the outside
of the disk or CD-ROM clearly that it does not contain CBI. Information
not marked as CBI will be included in the public docket and the EPA's
electronic public docket without prior notice. Information marked as
CBI will not be disclosed except in accordance with procedures set
forth in 40 CFR part 2. Send or deliver information identified as CBI
only to the following address: OAQPS Document Control Officer (C404-
02), OAQPS, U.S. Environmental Protection Agency, Research Triangle
Park, North Carolina 27711, Attention Docket ID No. EPA-HQ-OAR-2014-
0741.
II. Background
A. What is the statutory authority for this action?
Section 112 of the CAA establishes a two-stage regulatory process
to address emissions of hazardous air pollutants (HAPs) from stationary
sources. In the first stage, after the EPA has identified categories of
sources emitting one or more of the HAPs listed in CAA section 112(b),
CAA section 112(d) requires the Agency to promulgate technology-based
NESHAPs for those sources. ``Major sources'' are those that emit or
have the potential to emit 10 tpy or more of a single HAP or 25 tpy or
more of any combination of HAPs. For major sources, the technology-
based NESHAP must reflect the maximum degree of
[[Page 97050]]
emission reductions of HAPs achievable (after considering cost, energy
requirements, and non-air quality health and environmental impacts) and
are commonly referred to as MACT standards.
MACT standards must reflect the maximum degree of emissions
reduction achievable through the application of measures, processes,
methods, systems, or techniques, including, but not limited to,
measures that: (1) Reduce the volume of or eliminate pollutants through
process changes, substitution of materials, or other modifications; (2)
enclose systems or processes to eliminate emissions; (3) capture or
treat pollutants when released from a process, stack, storage, or
fugitive emissions point; (4) are design, equipment, work practice, or
operational standards (including requirements for operator training or
certification); or (5) are a combination of the above. CAA section
112(d)(2)(A)-(E). The MACT standards may take the form of design,
equipment, work practice, or operational standards where the EPA first
determines either that: (1) A pollutant cannot be emitted through a
conveyance designed and constructed to emit or capture the pollutant,
or that any requirement for, or use of, such a conveyance would be
inconsistent with law; or (2) the application of measurement
methodology to a particular class of sources is not practicable due to
technological and economic limitations. CAA section 112(h)(1)-(2).
The MACT ``floor'' is the minimum control level allowed for MACT
standards promulgated under CAA section 112(d)(3) and may not be based
on cost considerations. For new sources, the MACT floor cannot be less
stringent than the emissions control that is achieved in practice by
the best-controlled similar source. The MACT floor for existing sources
can be less stringent than floors for new sources, but not less
stringent than the average emissions limitation achieved by the best-
performing 12 percent of existing sources in the category or
subcategory (or the best-performing five sources for categories or
subcategories with fewer than 30 sources). In developing MACT
standards, the EPA must also consider control options that are more
stringent than the floor. We may establish standards more stringent
than the floor based on considerations of the cost of achieving the
emission reductions, any non-air quality health and environmental
impacts, and energy requirements.
The EPA is then required to review these technology-based standards
and revise them ``as necessary (taking into account developments in
practices, processes, and control technologies)'' no less frequently
than every 8 years. CAA section 112(d)(6). In conducting this review,
the EPA is not required to recalculate the MACT floor. Natural
Resources Defense Council (NRDC) v. EPA, 529 F.3d 1077, 1084 (D.C. Cir.
2008). Association of Battery Recyclers, Inc. v. EPA, 716 F.3d 667
(D.C. Cir. 2013).
The second stage in standard-setting focuses on reducing any
remaining (i.e., ``residual'') risk according to CAA section 112(f).
Section 112(f)(1) of the CAA required that the EPA prepare a report to
Congress discussing (among other things) methods of calculating the
risks posed (or potentially posed) by sources after implementation of
the MACT standards, the public health significance of those risks, and
the EPA's recommendations as to legislation regarding such remaining
risk. The EPA prepared and submitted the Residual Risk Report to
Congress, EPA-453/R-99-001 (Risk Report) in March 1999. Section
112(f)(2) of the CAA then provides that if Congress does not act on any
recommendation in the Risk Report, the EPA must analyze and address
residual risk for each category or subcategory of sources 8 years after
promulgation of such standards pursuant to CAA section 112(d).
Section 112(f)(2) of the CAA requires the EPA to determine for
source categories subject to MACT standards whether promulgation of
additional standards is needed to provide an ample margin of safety to
protect public health. Section 112(f)(2)(B) of the CAA expressly
preserves the EPA's use of the two-step process for developing
standards to address any residual risk and the Agency's interpretation
of ``ample margin of safety'' developed in the National Emissions
Standards for Hazardous Air Pollutants: Benzene Emissions from Maleic
Anhydride Plants, Ethylbenzene/Styrene Plants, Benzene Storage Vessels,
Benzene Equipment Leaks, and Coke By-Product Recovery Plants (Benzene
NESHAP) (54 FR 38044, September 14, 1989). The EPA notified Congress in
the Risk Report that the Agency intended to use the Benzene NESHAP
approach in making CAA section 112(f) residual risk determinations
(EPA-453/R-99-001, p. ES-11). The EPA subsequently adopted this
approach in its residual risk determinations and, in a challenge to the
risk review for the Synthetic Organic Chemical Manufacturing source
category, the United States Court of Appeals for the District of
Columbia Circuit upheld as reasonable the EPA's interpretation that CAA
section 112(f)(2) incorporates the approach established in the Benzene
NESHAP. See NRDC v. EPA, 529 F.3d 1077, 1083 (D.C. Cir. 2008)
(``[S]ubsection 112(f)(2)(B) expressly incorporates the EPA's
interpretation of the Clean Air Act from the Benzene standard, complete
with a citation to the Federal Register.''); see also, A Legislative
History of the Clean Air Act Amendments of 1990, vol. 1, p. 877 (Senate
debate on Conference Report).
The first step in the process of evaluating residual risk is the
determination of acceptable risk. If risks are unacceptable, the EPA
cannot consider cost in identifying the emissions standards necessary
to bring risks to an acceptable level. The second step is the
determination of whether standards must be further revised in order to
provide an ample margin of safety to protect public health. The ample
margin of safety is the level at which the standards must be set,
unless an even more stringent standard is necessary to prevent, taking
into consideration costs, energy, safety, and other relevant factors,
an adverse environmental effect.
1. Step 1--Determination of Acceptability
The Agency in the Benzene NESHAP concluded that ``the acceptability
of risk under section 112 is best judged on the basis of a broad set of
health risk measures and information'' and that the ``judgment on
acceptability cannot be reduced to any single factor.'' Benzene NESHAP
at 38046. The determination of what represents an ``acceptable'' risk
is based on a judgment of ``what risks are acceptable in the world in
which we live'' (Risk Report at 178, quoting NRDC v. EPA, 824 F. 2d
1146, 1165 (D.C. Cir. 1987) (en banc) (``Vinyl Chloride''), recognizing
that our world is not risk-free.
In the Benzene NESHAP, we stated that ``EPA will generally presume
that if the risk to [the maximum exposed] individual is no higher than
approximately one in 10 thousand, that risk level is considered
acceptable.'' 54 FR at 38045, September 14, 1989. We discussed the
maximum individual lifetime cancer risk (or maximum individual risk
(MIR)) as being ``the estimated risk that a person living near a plant
would have if he or she were exposed to the maximum pollutant
concentrations for 70 years.'' Id. We explained that this measure of
risk ``is an estimate of the upper bound of risk based on conservative
assumptions, such as continuous exposure for 24 hours per day for 70
years.'' Id. We
[[Page 97051]]
acknowledged that maximum individual lifetime cancer risk ``does not
necessarily reflect the true risk, but displays a conservative risk
level which is an upper-bound that is unlikely to be exceeded.'' Id.
Understanding that there are both benefits and limitations to using
the MIR as a metric for determining acceptability, we acknowledged in
the Benzene NESHAP that ``consideration of maximum individual risk . .
. must take into account the strengths and weaknesses of this measure
of risk.'' Id. Consequently, the presumptive risk level of 100-in-1
million (1-in-10 thousand) provides a benchmark for judging the
acceptability of maximum individual lifetime cancer risk, but does not
constitute a rigid line for making that determination. Further, in the
Benzene NESHAP, we noted that:
``[p]articular attention will also be accorded to the weight of
evidence presented in the risk assessment of potential
carcinogenicity or other health effects of a pollutant. While the
same numerical risk may be estimated for an exposure to a pollutant
judged to be a known human carcinogen, and to a pollutant considered
a possible human carcinogen based on limited animal test data, the
same weight cannot be accorded to both estimates. In considering the
potential public health effects of the two pollutants, the Agency's
judgment on acceptability, including the MIR, will be influenced by
the greater weight of evidence for the known human carcinogen.''
Id. at 38046. The Agency also explained in the Benzene NESHAP that:
``[i]n establishing a presumption for MIR, rather than a rigid
line for acceptability, the Agency intends to weigh it with a series
of other health measures and factors. These include the overall
incidence of cancer or other serious health effects within the
exposed population, the numbers of persons exposed within each
individual lifetime risk range and associated incidence within,
typically, a 50 km exposure radius around facilities, the science
policy assumptions and estimation uncertainties associated with the
risk measures, weight of the scientific evidence for human health
effects, other quantified or unquantified health effects, effects
due to co-location of facilities, and co-emission of pollutants.''
Id. at 38045. In some cases, these health measures and factors
taken together may provide a more realistic description of the
magnitude of risk in the exposed population than that provided by
maximum individual lifetime cancer risk alone.
As noted earlier, in NRDC v. EPA, the court held that CAA section
112(f)(2) ``incorporates the EPA's interpretation of the Clean Air Act
from the Benzene Standard.'' The court further held that Congress'
incorporation of the Benzene standard applies equally to carcinogens
and non-carcinogens. 529 F.3d at 1081-82. Accordingly, we also consider
non-cancer risk metrics in our determination of risk acceptability and
ample margin of safety.
2. Step 2--Determination of Ample Margin of Safety
Section 112(f)(2) of the CAA requires the EPA to determine, for
source categories subject to MACT standards, whether those standards
provide an ample margin of safety to protect public health. As
explained in the Benzene NESHAP, ``the second step of the inquiry,
determining an `ample margin of safety,' again includes consideration
of all of the health factors, and whether to reduce the risks even
further . . . . Beyond that information, additional factors relating to
the appropriate level of control will also be considered, including
costs and economic impacts of controls, technological feasibility,
uncertainties, and any other relevant factors. Considering all of these
factors, the Agency will establish the standard at a level that
provides an ample margin of safety to protect the public health, as
required by section 112.'' 54 FR at 38046, September 14, 1989.
According to CAA section 112(f)(2)(A), if the MACT standards for
HAP ``classified as a known, probable, or possible human carcinogen do
not reduce lifetime excess cancer risks to the individual most exposed
to emissions from a source in the category or subcategory to less than
one in one million,'' the EPA must promulgate residual risk standards
for the source category (or subcategory), as necessary to provide an
ample margin of safety to protect public health. In doing so, the EPA
may adopt standards equal to existing MACT standards if the EPA
determines that the existing standards (i.e., the MACT standards) are
sufficiently protective. NRDC v. EPA, 529 F.3d 1077, 1083 (D.C. Cir.
2008) (``If EPA determines that the existing technology-based standards
provide an `ample margin of safety,' then the Agency is free to readopt
those standards during the residual risk rulemaking.'') The EPA must
also adopt more stringent standards, if necessary, to prevent an
adverse environmental effect,\1\ but must consider cost, energy,
safety, and other relevant factors in doing so.
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\1\ ``Adverse environmental effect'' is defined as any
significant and widespread adverse effect, which may be reasonably
anticipated to wildlife, aquatic life, or natural resources,
including adverse impacts on populations of endangered or threatened
species or significant degradation of environmental qualities over
broad areas. CAA section 112(a)(7).
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The CAA does not specifically define the terms ``individual most
exposed,'' ``acceptable level,'' and ``ample margin of safety.'' In the
Benzene NESHAP, 54 FR at 38044-38045, September 14, 1989, the Agency
stated as an overall objective:
In protecting public health with an ample margin of safety under
section 112, EPA strives to provide maximum feasible protection
against risks to health from hazardous air pollutants by (1)
protecting the greatest number of persons possible to an individual
lifetime risk level no higher than approximately 1-in-1 million and
(2) limiting to no higher than approximately 1-in-10 thousand [i.e.,
100-in-1 million] the estimated risk that a person living near a
plant would have if he or she were exposed to the maximum pollutant
concentrations for 70 years.
The Agency further stated that ``[t]he EPA also considers incidence
(the number of persons estimated to suffer cancer or other serious
health effects as a result of exposure to a pollutant) to be an
important measure of the health risk to the exposed population.
Incidence measures the extent of health risks to the exposed population
as a whole, by providing an estimate of the occurrence of cancer or
other serious health effects in the exposed population.'' Id. at 38045.
In the ample margin of safety decision process, the Agency again
considers all of the health risks and other health information
considered in the first step, including the incremental risk reduction
associated with standards more stringent than the MACT standard or a
more stringent standard that the EPA has determined is necessary to
ensure risk is acceptable. In the ample margin of safety analysis, the
Agency considers additional factors, including costs and economic
impacts of controls, technological feasibility, uncertainties, and any
other relevant factors. Considering all of these factors, the Agency
will establish the standard at a level that provides an ample margin of
safety to protect the public health, as required by CAA section 112(f).
54 FR 38046, September 14, 1989.
B. What is this source category and how does the current NESHAP
regulate its HAP emissions?
The ``Pulp and Paper Production'' source category includes any
facility engaged in the production of pulp and/or paper. The EPA
developed the NESHAPs for the source category in two phases. The first
phase, 40 CFR part 63, subpart S, regulates pulping and paper
production processes, and was
[[Page 97052]]
originally promulgated in 1998. The second phase, 40 CFR part 63,
subpart MM, regulates chemical recovery combustion sources at kraft,
soda, sulfite, and stand-alone semichemical pulp mills, and was
originally promulgated in 2001. Another separate NESHAP, 40 CFR part
63, subpart DDDDD, covers other combustion sources located at pulp
mills, such as industrial boilers. This proposal focuses exclusively on
the RTR for subpart MM. The EPA is not proposing any amendments to
Subpart DDDDD or subpart S in this notice.
Subpart MM of 40 CFR part 63 was promulgated on January 12, 2001
(66 FR 3180). As promulgated in 2001, the subpart MM MACT standard
applies to major sources of HAP emissions from chemical recovery
combustion sources at kraft, soda, sulfite, and stand-alone
semichemical pulp mills. The chemical recovery combustion sources
include kraft and soda recovery furnaces, SDTs, and lime kilns; kraft
black liquor oxidation (BLO) units; sulfite combustion units; and
semichemical combustion units. Subpart S was promulgated on April 15,
1998 (63 FR 18504), and underwent a RTR, with final amendments to
subpart S promulgated on September 11, 2012 (77 FR 55698).
This proposal includes both a risk assessment and a technology
review of the emission sources in 40 CFR part 63, subpart MM, as well
as a risk assessment of the whole facility. The whole facility risk
assessment includes emissions from all sources of HAP at the facility,
including sources covered by other NESHAP (e.g., boilers covered under
40 CFR part 63, subpart DDDDD; pulp and paper production processes
covered under 40 CFR part 63, subpart S; paper coating operations
covered under 40 CFR part 63, subpart JJJJ).
According to results of the EPA's 2011 pulp and paper information
collection request (ICR), and updates based on more recent information,
there are a total of 108 major sources in the United States that
conduct chemical recovery combustion operations, including 97 kraft
pulp mills, 1 soda pulp mill, 3 sulfite pulp mills, and 7 stand-alone
semichemical pulp mills.
Subpart MM of 40 CFR part 63 includes numerical emission limits for
recovery furnaces, SDTs, lime kilns, and sulfite and semichemical
combustion units. The control systems used by most mills to meet the
subpart MM emission limits are as follows:
Recovery furnaces: ESPs, wet scrubbers, and nondirect
contact evaporator (NDCE) furnace design with dry-bottom ESP, and dry
particulate matter (PM) return system.
Smelt dissolving tanks: Wet scrubbers, mist eliminators,
and venting to recovery furnace.
Lime kilns: ESPs and wet scrubbers.
Sulfite combustion units: Wet scrubbers and mist
eliminators.
Semichemical combustion units: Wet scrubbers, ESPs, and
regenerative thermal oxidizers (RTOs).
C. What data collection activities were conducted to support this
action?
In February 2011, the EPA issued an ICR, pursuant to CAA section
114, to United States pulp and paper manufacturers to gather
information needed to conduct the regulatory reviews required under CAA
sections 112(d)(6) and (f)(2). The EPA divided the ICR into three
parts. Part I requested available information regarding 40 CFR part 63,
subpart S process equipment, control devices, pulp and paper
production, bleaching, and other aspects of facility operations to
support the subpart S technology review and the review of the Kraft
Pulp Mills New Source Performance Standards (NSPS) under 40 CFR part
60, subpart BB. Part II requested updated inventory data for all pulp
and paper emission sources to support the residual risk assessment for
the pulp and paper sector (including 40 CFR part 63, subparts S and MM)
and to supplement the National Emissions Inventory (NEI) for the source
category for purposes of detailed residual risk modeling. Part III
requested available information on subpart MM chemical recovery
combustion equipment, control devices, and other pertinent information,
to support the subpart MM technology review and the subpart BB NSPS
review. The response rate for the ICR was 100 percent.
D. What other relevant background information and data are available?
In addition to ICR responses, the EPA reviewed a number of other
information sources to determine if there have been developments in
practices, processes, or control technologies by chemical recovery
combustion sources. These include:
Permit limits from permits submitted with ICR responses
and collected from state agencies.
Information on air pollution control options in the pulp
and paper industry from the RACT/BACT/LAER Clearinghouse (RBLC).
Information on best available techniques in the pulp and
paper industry from a 2015 European Commission document, titled Best
Available Techniques (BAT) Reference Document for the Production of
Pulp, Paper and Board.
Information on the most effective ways to control
emissions of PM2.5 and PM2.5 precursors from
sources in various industries, including the pulp and paper industry,
from a 2006 State and Territorial Air Pollution Program Administrators/
Association of Local Air Pollution Control Officers (STAPPA/ALAPCO)
document, titled Controlling Fine Particulate Matter under the Clean
Air Act: A Menu of Options.
Stack test data submitted with ICR responses.
Emissions factors from technical bulletins prepared by the
National Council for Air and Stream Improvement, Inc. (NCASI), a major
source of environmental data affecting the pulp and paper industry.
III. Analytical Procedures
In this section, we describe the analyses performed to support the
proposed decisions for the RTR and other issues addressed in this
proposal.
A. How did we estimate post-MACT risks posed by the source category?
The EPA conducted a risk assessment that provides estimates of the
MIR posed by the HAP emissions from each source in the source category,
the hazard index (HI) for chronic exposures to HAPs with the potential
to cause non-cancer health effects, and the hazard quotient (HQ) for
acute exposures to HAPs with the potential to cause non-cancer health
effects. The assessment also provides estimates of the distribution of
cancer risks within the exposed populations, cancer incidence, and an
evaluation of the potential for adverse environmental effects. The
seven sections that follow this paragraph describe how we estimated
emissions and conducted the risk assessment. The docket for this
rulemaking contains the following document which provides more
information on the risk assessment inputs and models: Residual Risk
Assessment for Pulp Mill Combustion Sources in Support of the December
2016 Risk and Technology Review Proposed Rule. The methods used to
assess risks (as described in the seven primary steps below) are
consistent with those peer-reviewed by a panel of the EPA's Science
Advisory Board (SAB) in 2009 and described in their peer review report
issued in 2010; \2\ they are also consistent with the key
[[Page 97053]]
recommendations contained in that report.
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\2\ U.S. EPA SAB. Risk and Technology Review (RTR) Risk
Assessment Methodologies: For Review by the EPA's Science Advisory
Board with Case Studies--MACT I Petroleum Refining Sources and
Portland Cement Manufacturing, May 2010.
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1. How did we estimate actual emissions and identify the emissions
release characteristics?
As discussed in section II.C of this preamble, we used data from
Part II of the Pulp and Paper Sector ICR as the basis for the risk
assessments for the pulp and paper sector (including 40 CFR part 63,
subparts S and MM). Part II of the ICR, which concluded in June 2011,
targeted facilities that are major sources of HAP emissions and
involved an update of pre-populated NEI data spreadsheets (or creation
of new datasets). The NEI is a database that contains information about
sources that emit criteria air pollutants, their precursors and HAPs.
The NEI database includes estimates of actual annual air pollutant
emissions from point and volume sources; emission release
characteristic data such as emission release height, temperature,
diameter, velocity, and flow rate; and locational latitude/longitude
coordinates. We asked pulp and paper mills to refine (or create new)
inventories based on their NEI datasets for purposes of detailed
residual risk modeling. Refinements included providing additional
details for HAP emission sources, providing more specific information
on the location and characteristics of emission points (e.g., updating
emission release coordinates and parameters), and adding or updating
HAP emissions data for each emission release point. We compiled the
updated datasets for each individual mill into a pulp and paper Part II
emissions database to create the whole facility and MACT source
category residual risk modeling files.
The actual annual emissions data in the pulp and paper emissions
database include limited data from actual emissions tests and, in most
cases, estimates of actual emissions (based on emissions factors)
provided by sources surveyed in Part II of the ICR. We received a
comprehensive set of emissions test data and emissions estimates that
enabled us to conduct risk modeling of detectable HAP emissions for all
major source facilities in the MACT source category.
We conducted two substantial quality assurance (QA) efforts on the
Part II data in order to create the modeling files needed for the 40
CFR part 63, subpart S residual risk assessment, which included: (1) QA
of the updated inventory spreadsheets submitted by each mill prior to
import into the compiled database; and (2) QA and standardization of
the compiled database.\3\ We needed modeling files for both the subpart
S category and the whole facility, so our QA efforts focused on data
for all emission sources at pulp and paper facilities, including 40 CFR
part 63, subpart MM emission sources.
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\3\ These QA efforts are discussed in a November 11, 2011
memorandum in the docket, titled Inputs to the Pulp and Paper
Industry October 2011 Residual Risk Modeling.
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We reviewed the Part II datasets to ensure that the major pulp and
paper processes and pollutants were included and properly identified,
to ensure that emissions from the various processes were allocated to
the correct source category, and to identify emissions and other data
anomalies. We also standardized the various codes (e.g., source
classification codes (SCCs), pollutant codes), eliminated duplicate
records, and checked geographic coordinates. We reviewed emissions
release parameters for data gaps and errors, assigned the proper
default parameters where necessary, assigned emission process groups to
distinguish between processes with related SCCs, and ensured that
fugitive release dimensions were specified or given default values
where necessary.
We requested comments on the inventory in the preamble to the
December 27, 2011, 40 CFR part 63, subpart S proposal. We requested
further updates to the mill-specific HAP emissions data used in the
risk modeling, if needed. In 2012, we received revisions to inventories
for 81 facilities following proposal of the subpart S residual risk
review.\4\
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\4\ Review of the inventory revisions performed prior to
promulgation of 40 CFR part 63, subpart S is documented in a May 8,
2012, memorandum in the subpart S docket (EPA-HQ-OAR-2007-0544),
titled Recommendations Concerning Residual Risk Remodeling for the
Pulp and Paper Industry.
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While most of the inventory revisions that we received after the
proposal made additional refinements to emissions levels and release
point details for 40 CFR part 63, subpart S sources, some inventory
revisions also made refinements to data for 40 CFR part 63, subpart MM
sources. We incorporated revisions to all process types into the
inventory to remodel facility-wide risk and perform the complete scope
of residual risk modeling for subpart MM emissions sources. We checked
the 81 individual revision files to ensure they were incorporated into
the main database correctly, and then further reviewed the entire
database.
We began compiling an initial draft residual risk modeling input
file for use in the 40 CFR part 63, subpart MM residual risk review in
September 2014.\5\ We made updates to the mill list to account for
facilities that recently closed or reopened, and to mill equipment
configurations for facilities that recently upgraded equipment. We
reviewed the inventory to ensure that each record contained a facility
ID, emission unit ID, process ID, and emission release point ID. We
cross-walked regulatory codes, SCCs, and emission process groups to
identify and correct any inconsistencies that may have been introduced
with the inventory updates.
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\5\ For more information, see the September 30, 2014 memorandum
in the docket, titled Preparation of Residual Risk Modeling Input
File for Subpart MM. The September 2014 memorandum describes the
source of the inventory data, discusses quality assurance of the 40
CFR part 63, subpart MM data, provides actual versus allowable and
acute risk multipliers for subpart MM sources, and identifies
potential outliers and suspect data for further review.
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In addition to retaining the emission process groups used in the
previous 40 CFR part 63, subpart S modeling effort, we added new
emission process groups for 40 CFR part 63, subpart MM sources where
necessary. We compared the subpart MM emission process groups with the
Part III ICR database to ensure that we included all known recovery
furnaces and lime kilns in the inventory for the residual risk
modeling. In addition, we reviewed the presence or absence of BLO
systems (i.e., because BLO systems are only expected to be present at
mills with direct contact evaporator (DCE) recovery furnaces). Finally,
we checked the mills to ensure emission process groups included SDTs
and sulfite and semichemical recovery equipment, as expected.
We reviewed the pollutant codes in the inventory to ensure the
codes and descriptions matched the latest NEI lookup table used by the
EPA for risk model input files. We performed extensive QA of the
pollutant codes prior to the 40 CFR part 63, subpart S risk modeling,
so few updates were required.
We speciated data for a number of HAPs, including chromium,
mercury, radionuclides, polycyclic organic matter (POM), and dioxins/
furans to facilitate risk modeling. We speciated chromium emissions as
hexavalent chromium (chromium VI) and trivalent chromium (chromium
III).\6\ We speciated mercury emissions as particulate divalent
mercury, gaseous divalent mercury, and gaseous elemental mercury. We
speciated total POM emissions differently for each emission unit type
[[Page 97054]]
based on the most common POM compounds emitted from that unit. We
speciated dioxin/furan emissions based on published emissions data in
the EPA's dioxin/furan inventory report \7\ or, if no speciation
profile was available, recalculated the emissions using published
emissions factors.\8\ Where needed, we added/replaced emissions
estimates that were omitted, outdated, out-of-scope, or inconsistent
with changes to mill equipment configurations.
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\6\ For more information on pollutant speciation, see the
September 30, 2014 memorandum in the docket, titled Preparation of
Residual Risk Modeling Input File for Subpart MM.
\7\ U.S. Environmental Protection Agency. An Inventory of
Sources and Environmental Releases of Dioxin-Like Compounds in the
United States for the Years 1987, 1995, and 2000. Publication No.
EPA/600/P-03/002F. Available at: https://www.epa.gov/ncea/pdfs/dioxin/2006/dioxin.pdf. November 2006. Tables 4-14, 4-25, and 5-13.
\8\ National Council for Air and Stream Improvement (NCASI).
Compilation of `Air Toxic' and Total Hydrocarbon Emissions Data for
Pulp and Paper Mill Sources--A Second Update. Technical Bulletin No.
973. February 2010. Table 9.9.
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We reviewed all records for consistency with respect to the
emission release point to ensure each record was characterized by one
set of coordinates (latitude and longitude) and one set of stack or
fugitive parameters. We checked fugitive parameters to ensure there
were no blanks and that the values provided were reasonable and
consistent with the required national defaults or other criteria. We
reviewed emission points labeled as stacks to ensure no fugitive
parameters were identified. We checked exit gas flow rate values
against the stack velocity provided to ensure there were no
inconsistencies. We mapped the emission point coordinates for each
facility to determine if they were properly placed on the mill site. We
also added control information from the Part III ICR database or mills'
title V permits to the input file for 40 CFR part 63, subpart MM
sources.
The emissions inventory for 40 CFR part 63, subpart MM sources
identifies emissions of the following HAP known to be persistent and
bio-accumulative in the environment (PB-HAPs): Cadmium compounds, lead
compounds, mercury compounds, POM, dioxins/furans, and
hexachlorobenzene. Risk-based screening levels are available for Tier 1
screening for all of the above PB-HAPs, with the exception of
hexachlorobenzene.
Consistent with the EPA's standard practice in conducting risk
assessments for source categories, we conducted a two-step process to
determine: (1) Whether PB-HAPs are being emitted; and (2) whether they
are being released above screening levels. If these releases are
significantly above the screening levels and the EPA has detailed
information on the releases and the site, a complete multipathway
analysis of the site is conducted to estimate pathway risks for the
source category.
We considered actual emissions of the ecological HAPs emitted from
the 40 CFR part 63, subpart MM source category in the ecological HAP
analysis. In addition to the PB-HAPs emitted from the subpart MM source
category (except hexachlorobenzene), we considered hydrochloric acid
(HCl) and hydrogen fluoride (HF) for ecological HAP modeling. Further
information about the multipathway analysis performed for this category
follows in section III.B.4 of this preamble.
In 2015, we posted the initial draft risk model input file on our
Technology Transfer Network for additional review by interested
parties. This review resulted in the submittal of additional mill-
specific inventory and receptor revisions. As part of the review, we
identified potential outliers and suspect data for 40 CFR part 63,
subpart MM sources in the emission inventory and notified facilities to
provide an opportunity to review and revise their emissions data, if
needed. A total of 40 mills reviewed their emissions data, with 38 of
those mills submitting inventory revisions to the EPA.\9\
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\9\ For further information, see the October 16, 2015 memorandum
in the docket, titled Review of Pulp Mill Inventory Revisions
Received in 2015.
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Inventory revisions primarily included mill name changes; revisions
to HAP metal, POM, and dioxin/furan inventory data; and requests for
removal of hexachlorocyclopentadiene (HCCPD) data from inventories,
particularly for SDTs, since HCCPD is not expected from pulp mill
sources. Where necessary, we speciated the revised chromium, mercury,
and POM data that the mills provided, using the approaches described
above. As part of the review, we identified risk modeling receptors
improperly located on mill property for correction in the Human
Exposure Model (Community and Sector HEM-3 version 1.1.0) input files
before we performed risk modeling for 40 CFR part 63, subpart MM.
After we incorporated the revisions into the input file, we
conducted an additional review of the file, which included the
following:
Identified non-40 CFR part 63, subpart MM mills in the
inventory and removed them.
Identified additional mill name changes and incorporated
them in the inventory.
Reviewed fugitive parameters for missing data.
Identified missing speciated mercury and chromium data and
restored the data to the inventory.
Reviewed location data for mills that submitted inventory
revisions and corrected coordinates, as needed.
Identified records for emissions points with zero
emissions for a given pollutant and removed those records from the
inventory.
Conducted emission process group checks, resulting in a
revision to an emission process group that reflects a change in SCC,
and removal of records with an emission process group no longer
applicable (specifically a BLO unit for a mill that no longer operates
any DCE recovery furnaces that require a BLO unit).
Checked mills to ensure they had the expected 40 CFR part
63, subpart MM equipment, comparing the number of recovery furnaces,
lime kilns, and SDTs to Part III ICR data to ensure each emission unit
was represented in the inventory.
Reviewed each emission unit for the presence of an
emissions value for key expected pollutants (e.g., HAP metals, HCl,
methanol, dioxins/furans, POM) and added emissions estimates for those
pollutants where needed.\10\
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\10\ For further information, see the February 16, 2016
memorandum in the docket, titled Approach for Populating Missing and
Erroneous Emissions Estimates for Key HAP in the Subpart MM Residual
Risk Modeling Inventory.
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Replaced obviously errant emissions data (particularly
dioxins/furans) with revised estimates calculated based on ICR-reported
throughput and emissions factors.
Rechecked IDs, SCCs, regulatory codes, pollutant codes,
duplicate pollutants, and HCCPD deletions.
2. How did we estimate MACT-allowable emissions?
The available emissions data in the RTR emissions dataset include
estimates of the mass of HAPs emitted during the specified annual time
period. In some cases, these ``actual'' emission levels are lower than
the emission levels required to comply with the current MACT standards.
The emissions level allowed to be emitted by the MACT standards is
referred to as the ``MACT-allowable'' emissions level. We discussed the
use of both MACT-allowable and actual emissions in the final Coke Oven
Batteries RTR (70 FR 19998-19999, April 15, 2005) and in the proposed
and final Hazardous Organic NESHAP RTRs (71 FR 34428, June 14, 2006,
and 71 FR 76609, December 21, 2006, respectively). In those actions, we
noted that assessing the risks at the MACT-allowable level is
inherently reasonable
[[Page 97055]]
since these risks reflect the maximum level facilities could emit and
still comply with national emission standards. We also explained that
it is reasonable to consider actual emissions, where such data are
available, in both steps of the risk analysis, in accordance with the
Benzene NESHAP approach. (54 FR 38044, September 14, 1989.) It is
reasonable to consider actual emissions because sources typically seek
to perform better than required by emissions standards to provide an
operational margin to accommodate the variability in manufacturing
processes and control device performance. Facilities' actual emissions
may also be significantly lower than MACT-allowable emissions for other
reasons such as state requirements, better performance of control
devices than required by the MACT standards, or reduced production.
We estimated actual emissions based on the Part II emissions
inventory and subsequent site-specific inventory revisions provided by
mills. To estimate emissions at the MACT-allowable level, we developed
a ratio of MACT-allowable emissions to actual emissions for each source
type for the facilities in the 40 CFR part 63, subpart MM source
category. We developed this ratio based on the level of control
required by the subpart MM MACT standards compared to the level of
reported actual emissions from stack test reports provided with Part
III survey responses. For example, stack test data indicated that SDTs
achieve PM levels of 0.108 pounds per ton (lb/ton) black liquor solids
(BLS), on average, while the PM emission limit for existing SDTs is
0.20 lb/ton BLS, so we estimated that MACT-allowable emissions of HAP
metals from SDTs (where PM is used as a surrogate) could be as much as
1.8 times higher, and the ratio of MACT-allowable to actual emissions
used was 1.8:1 for SDTs.\11\
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\11\ For more information, see the September 30, 2014 memorandum
in the docket, titled Preparation of Residual Risk Modeling Input
File for Subpart MM.
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After developing these ratios for each emission point type in this
source category, we next applied these ratios on an emission unit basis
to the Part II actual emissions data to obtain risk estimates based on
MACT-allowable emissions.
3. How did we conduct dispersion modeling, determine inhalation
exposures and estimate individual and population inhalation risks?
Both long-term and short-term inhalation exposure concentrations
and health risks from the source category addressed in this proposal
were estimated using HEM-3. The HEM-3 performs three primary risk
assessment activities: (1) Conducting dispersion modeling to estimate
the concentrations of HAPs in ambient air, (2) estimating long-term and
short-term inhalation exposures to individuals residing within 50
kilometers (km) of the modeled sources,\12\ and (3) estimating
individual and population-level inhalation risks using the exposure
estimates and quantitative dose-response information.
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\12\ This metric comes from the Benzene NESHAP. See 54 FR 38046.
---------------------------------------------------------------------------
The air dispersion model used by the HEM-3 model (AERMOD) is one of
the EPA's preferred models for assessing pollutant concentrations from
industrial facilities.\13\ To perform the dispersion modeling and to
develop the preliminary risk estimates, HEM-3 draws on three data
libraries. The first is a library of meteorological data, which is used
for dispersion calculations. This library includes 1 year (2014) of
hourly surface and upper air observations for more than 800
meteorological stations, selected to provide coverage of the United
States and Puerto Rico. A second library of United States Census Bureau
census block \14\ internal point locations and populations provides the
basis of human exposure calculations (U.S. Census, 2010). In addition,
for each census block, the census library includes the elevation and
controlling hill height, which are also used in dispersion
calculations. A third library of pollutant unit risk factors and other
health benchmarks is used to estimate health risks. These risk factors
and health benchmarks are the latest values recommended by the EPA for
HAPs and other toxic air pollutants. These values are available at
https://www.epa.gov/fera/dose-response-assessment-assessing-health-risks-associated-exposure-hazardous-air-pollutants and are discussed in
more detail later in this section.
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\13\ U.S. EPA. Revision to the Guideline on Air Quality Models:
Adoption of a Preferred General Purpose (Flat and Complex Terrain)
Dispersion Model and Other Revisions (70 FR 68218, November 9,
2005).
\14\ A census block is the smallest geographic area for which
census statistics are tabulated.
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In developing the risk assessment for chronic exposures, we used
the estimated annual average ambient air concentrations of each HAP
emitted by each source for which we have emissions data in the source
category. The air concentrations at each nearby census block centroid
were used as a surrogate for the chronic inhalation exposure
concentration for all the people who reside in that census block. We
calculated the MIR for each facility as the cancer risk associated with
a continuous lifetime (24 hours per day, 7 days per week, and 52 weeks
per year for a 70-year period) exposure to the maximum concentration at
the centroid of inhabited census blocks. Individual cancer risks were
calculated by multiplying the estimated lifetime exposure to the
ambient concentration of each of the HAP (in micrograms per cubic meter
([mu]g/m\3\)) by its unit risk estimate (URE). The URE is an upper
bound estimate of an individual's probability of contracting cancer
over a lifetime of exposure to a concentration of 1 microgram of the
pollutant per cubic meter of air. For residual risk assessments, we
generally use URE values from the EPA's Integrated Risk Information
System (IRIS). For carcinogenic pollutants without IRIS values, we look
to other reputable sources of cancer dose-response values, often using
California EPA (CalEPA) URE values, where available. In cases where
new, scientifically credible dose response values have been developed
in a manner consistent with the EPA guidelines and have undergone a
peer review process similar to that used by the EPA, we may use such
dose-response values in place of, or in addition to, other values, if
appropriate.
The EPA estimated incremental individual lifetime cancer risks
associated with emissions from the facilities in the source category as
the sum of the risks for each of the carcinogenic HAP (including those
classified as carcinogenic to humans, likely to be carcinogenic to
humans, and suggestive evidence of carcinogenic potential \15\) emitted
by the modeled sources. Cancer incidence and the distribution of
individual cancer risks for the population within 50 km of the
[[Page 97056]]
sources were also estimated for the source category as part of this
assessment by summing individual risks. A distance of 50 km is
consistent with both the analysis supporting the 1989 Benzene NESHAP
(54 FR 38044, September 14, 1989) and the limitations of Gaussian
dispersion models, including AERMOD.
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\15\ These classifications also coincide with the terms ``known
carcinogen, probable carcinogen, and possible carcinogen,''
respectively, which are the terms advocated in the EPA's Guidelines
for Carcinogen Risk Assessment, published in 1986 (51 FR 33992,
September 24, 1986). In August 2000, the document Supplemental
Guidance for Conducting Health Risk Assessment of Chemical Mixtures
(EPA/630/R-00/002) was published as a supplement to the 1986
document. Copies of both documents can be obtained from https://cfpub.epa.gov/ncea/risk/recordisplay.cfm?deid=20533&CFID=70315376&CFTOKEN=71597944. Summing
the risks of these individual compounds to obtain the cumulative
cancer risks is an approach that was recommended by the EPA's SAB in
their 2002 peer review of the EPA's National Air Toxics Assessment
(NATA) titled, NATA--Evaluating the National-scale Air Toxics
Assessment 1996 Data--an SAB Advisory, available at https://yosemite.epa.gov/ sab/sabproduct.nsf/
214C6E915BB04E14852570CA007A682C/ $File/ecadv02001.pdf.
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To assess the risk of non-cancer health effects from chronic
exposures, we summed the HQ for each of the HAP that affects a common
target organ system to obtain the HI for that target organ system (or
target organ-specific HI, TOSHI). The HQ is the estimated exposure
divided by the chronic reference value, which is a value selected from
one of several sources. First, the chronic reference level can be the
EPA reference concentration (RfC) (https://iaspub.epa.gov/sor_internet/registry/termreg/searchandretrieve/glossariesandkeywordlists/search.do?details=&vocabName=IRIS%20Glossary), defined as ``an estimate
(with uncertainty spanning perhaps an order of magnitude) of a
continuous inhalation exposure to the human population (including
sensitive subgroups) that is likely to be without an appreciable risk
of deleterious effects during a lifetime.'' Alternatively, in cases
where an RfC from the EPA's IRIS database is not available or where the
EPA determines that using a value other than the RfC is appropriate,
the chronic reference level can be a value from the following
prioritized sources: (1) The Agency for Toxic Substances and Disease
Registry (ATSDR) Minimum Risk Level (https://www.atsdr.cdc.gov/mrls/index.asp), which is defined as ``an estimate of daily human exposure
to a hazardous substance that is likely to be without an appreciable
risk of adverse non-cancer health effects (other than cancer) over a
specified duration of exposure''; (2) the CalEPA Chronic Reference
Exposure Level (REL) (https://oehha.ca.gov/air/crnr/notice-adoption-air-toxics-hot-spots-program-guidance-manual-preparation-health-risk-0),
which is defined as ``the concentration level (that is expressed in
units of micrograms per cubic meter ([mu]g/m\3\) for inhalation
exposure and in a dose expressed in units of milligram per kilogram-day
(mg/kg-day) for oral exposures), at or below which no adverse health
effects are anticipated for a specified exposure duration''; or (3), as
noted above, a scientifically credible dose-response value that has
been developed in a manner consistent with the EPA guidelines and has
undergone a peer review process similar to that used by the EPA, in
place of or in concert with other values.
As mentioned above, in order to characterize non-cancer chronic
effects, and in response to key recommendations from the SAB, the EPA
selects dose-response values that reflect the best available science
for all HAPs included in RTR risk assessments.\16\ More specifically,
for a given HAP, the EPA examines the availability of inhalation
reference values from the sources included in our tiered approach
(e.g., IRIS first, ATSDR second, CalEPA third) and determines which
inhalation reference value represents the best available science. Thus,
as new inhalation reference values become available, the EPA will
typically evaluate them and determine whether they should be given
preference over those currently being used in RTR risk assessments.
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\16\ The SAB peer review of RTR Risk Assessment Methodologies is
available at https://yosemite.epa.gov/sab/sabproduct.nsf/
4AB3966E263D943A8525771F00668381/$File/EPA-SAB-10-007-unsigned.pdf.
---------------------------------------------------------------------------
The EPA also evaluated screening estimates of acute exposures and
risks for each of the HAP (for which appropriate acute dose-response
values are available) at the point of highest potential off-site
exposure for each facility. To do this, the EPA estimated the risks
when both the peak (hourly) emissions rate and worst-case dispersion
conditions occur. We also assume that a person is located at the point
of highest impact during that same time. In accordance with our mandate
in section 112 of the CAA, we use the point of highest off-site
exposure to assess the potential risk to the maximally exposed
individual. The acute HQ is the estimated acute exposure divided by the
acute dose-response value. In each case, the EPA calculated acute HQ
values using best available, short-term dose-response values. These
acute dose-response values, which are described below, include the
acute REL, acute exposure guideline levels (AEGL) and emergency
response planning guidelines (ERPG) for 1-hour exposure durations. As
discussed below, we used conservative assumptions for emissions rates,
meteorology, and exposure location.
As described in the CalEPA's Air Toxics Hot Spots Program Risk
Assessment Guidelines, Part I, The Determination of Acute Reference
Exposure Levels for Airborne Toxicants, an acute REL value (https://oehha.ca.gov/air/general-info/oehha-acute-8-hour-and-chronic-reference-exposure-level-rel-summary) is defined as ``the concentration level at
or below which no adverse health effects are anticipated for a
specified exposure duration.'' Id. at page 2. Acute REL values are
based on the most sensitive, relevant, adverse health effect reported
in the peer-reviewed medical and toxicological literature. Acute REL
values are designed to protect the most sensitive individuals in the
population through the inclusion of margins of safety. Because margins
of safety are incorporated to address data gaps and uncertainties,
exceeding the REL does not automatically indicate an adverse health
impact.
Acute exposure guideline level values were derived in response to
recommendations from the National Research Council (NRC). The National
Advisory Committee (NAC) for the Development of Acute Exposure
Guideline Levels for Hazardous Substances--usually referred to as the
AEGL Committee or the NAC/AEGL committee developed AEGL values for at
least 273 of the 329 chemicals on the AEGL priority chemical list. The
last meeting of the NAC/AEGL Committee was in April 2010, and its
charter expired in October 2011. The NAC/AEGL Committee ended in
October 2011, but the AEGL program continues to operate at the EPA and
works with the National Academies to publish final AEGLs (https://www.epa.gov/aegl).
As described in Standing Operating Procedures (SOP) for Developing
Acute Exposure Guideline Levels for Hazardous Substances, ``The NRC's
previous name for acute exposure levels--community emergency exposure
levels--was replaced by the term AEGL to reflect the broad application
of these values to planning, response, and prevention in the community,
the workplace, transportation, the military, and the remediation of
Superfund sites'' (https://www.epa.gov/aegl/process-developing-acute-exposure-guideline-levels-aegls) Id. at 2.\17\ The AEGL values
represent threshold exposure limits for the general public and are
applicable to emergency exposures ranging from 10 minutes to 8 hours.
``The primary purpose of the AEGL program is to develop guideline
levels for once-in-a-lifetime, short-term exposures to airborne
concentrations of acutely toxic, high-priority chemicals.'' Id. at 21.
``More specifically, the AEGL values will be used for conducting
various risk assessments to aid in the development of emergency
preparedness and prevention plans, as well as real-time
[[Page 97057]]
emergency response actions, for accidental chemical releases at fixed
facilities and from transport carriers.'' Id. at 31.
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\17\ National Academy of Sciences (NAS), 2001. Standing
Operating Procedures for Developing Acute Exposure Levels for
Hazardous Chemicals, page 2.
---------------------------------------------------------------------------
The AEGL-1 value is then specifically defined as ``the airborne
concentration (expressed as ppm (parts per million) or mg/m3
(milligrams per cubic meter)) of a substance above which it is
predicted that the general population, including susceptible
individuals, could experience notable discomfort, irritation, or
certain asymptomatic nonsensory effects. However, the effects are not
disabling and are transient and reversible upon cessation of
exposure.'' Id. at 3. The document also notes that, ``Airborne
concentrations below AEGL-1 represent exposure levels that can produce
mild and progressively increasing but transient and nondisabling odor,
taste, and sensory irritation or certain asymptomatic, nonsensory
effects.'' Id. Similarly, the document defines AEGL-2 values as ``the
airborne concentration (expressed as parts per million or milligrams
per cubic meter) of a substance above which it is predicted that the
general population, including susceptible individuals, could experience
irreversible or other serious, long-lasting adverse health effects or
an impaired ability to escape.'' Id.
Emergency response planning guideline values are derived for use in
emergency response, as described in the American Industrial Hygiene
Association's Emergency Response Planning (ERP) Committee document
titled, ERPGS Procedures and Responsibilities (https://www.aiha.org/get-involved/AIHAGuidelineFoundation/EmergencyResponsePlanningGuidelines/Documents/ERPG%20Committee%20Standard%20Operating%20Procedures%20%20-%20March%202014%20Revision%20%28Updated%2010-2-2014%29.pdf), which
states that, ``Emergency Response Planning Guidelines were developed
for emergency planning and are intended as health based guideline
concentrations for single exposures to chemicals.'' \18\ Id. at 1. The
ERPG-1 value is defined as ``the maximum airborne concentration below
which nearly all individuals could be exposed for up to 1 hour without
experiencing more than mild, transient health effects or without
perceiving a clearly defined, objectionable odor.'' Id. at 2.
Similarly, the ERPG-2 value is defined as ``the maximum airborne
concentration below which nearly all individuals could be exposed for
up to 1 hour without experiencing or developing irreversible or other
serious adverse health effects or symptoms that could impair an
individual's ability to take protective action.'' Id. at 1.
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\18\ ERP Committee Procedures and Responsibilities. November 1,
2006. American Industrial Hygiene Association.
---------------------------------------------------------------------------
As can be seen from the definitions above, the AEGL and ERPG values
include the similarly-defined severity levels 1 and 2. For many
chemicals, a severity level 1 value AEGL or ERPG has not been developed
because the types of effects for these chemicals are not consistent
with the AEGL-1/ERPG-1 definitions; in these instances, we compare
higher severity level AEGL-2 or ERPG-2 values to our modeled exposure
levels to screen for potential acute concerns. When AEGL-1/ERPG-1
values are available, they are used in our acute risk assessments.
Acute REL values for 1-hour exposure durations are typically lower
than their corresponding AEGL-1 and ERPG-1 values. Even though their
definitions are slightly different, AEGL-1 values are often the same as
the corresponding ERPG-1 values, and AEGL-2 values are often equal to
ERPG-2 values. Maximum HQ values from our acute screening risk
assessments typically result when basing them on the acute REL value
for a particular pollutant. In cases where our maximum acute HQ value
exceeds 1, we also report the HQ value based on the next highest acute
dose-response value (usually the AEGL-1 and/or the ERPG-1 value).
To develop screening estimates of acute exposures in the absence of
hourly emissions data, generally we first develop estimates of maximum
hourly emissions rates by multiplying the average actual annual hourly
emissions rates by a default factor to cover routinely variable
emissions. We choose the factor to use partially based on process
knowledge and engineering judgment. The factor chosen also reflects a
Texas study of short-term volatile organic compound (VOC) emissions
variability, which showed that most peak emission events in a heavily-
industrialized four-county area (Harris, Galveston, Chambers, and
Brazoria Counties, Texas) were less than twice the annual average
hourly emissions rate. The highest peak emissions event was 74 times
the annual average hourly emissions rate, and the 99th percentile ratio
of peak hourly emissions rate to the annual average hourly emissions
rate was 9.\19\ Considering this analysis, to account for more than 99
percent of the peak hourly emissions, we apply a conservative screening
multiplication factor of 10 to the average annual hourly emissions rate
in our acute exposure screening assessments as our default approach.
However, we use a factor other than 10 if we have information that
indicates that a different factor is appropriate for a particular
source category. For this source category, median peak-to-mean
multipliers ranging from 1.1 to 4.7 were developed for 40 CFR part 63,
subpart MM emission process groups based on the routine annual
emissions data and peak hourly emissions data obtained from Part II
survey data. A further discussion of why these factors were chosen can
be found in the memorandum, Preparation of Residual Risk Modeling Input
File for Subpart MM, available in the docket for this rulemaking.
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\19\ Allen, et al., 2004. Variable Industrial VOC Emissions and
their impact on ozone formation in the Houston Galveston Area. Texas
Environmental Research Consortium. https://www.researchgate.net/publication/237593060_Variable_Industrial_VOC_Emissions_and_their_Impact_on_Ozone_Formation_in_the_Houston_Galveston_Area.
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As part of our acute risk assessment process, for cases where acute
HQ values from the screening step were less than or equal to 1 (even
under the conservative assumptions of the screening analysis), acute
impacts were deemed negligible and no further analysis was performed
for these HAPs. See the Residual Risk Assessment for Pulp Mill
Combustion Sources in Support of the December 2016 Risk and Technology
Review Proposed Rule for more details. Ideally, we would prefer to have
continuous measurements over time to see how the emissions vary by each
hour over an entire year. Having a frequency distribution of hourly
emissions rates over a year would allow us to perform a probabilistic
analysis to estimate potential threshold exceedances and their
frequency of occurrence. Such an evaluation could include a more
complete statistical treatment of the key parameters and elements
adopted in this screening analysis. Recognizing that this level of data
is rarely available, we instead rely on the multiplier approach.
To better characterize the potential health risks associated with
estimated acute exposures to HAPs, and in response to a key
recommendation from the SAB's peer review of the EPA's RTR risk
assessment methodologies,\20\ we generally examine a wider range of
available acute health metrics (e.g., RELs, AEGL) than we do for our
chronic risk assessments. This is in response to
[[Page 97058]]
the SAB's acknowledgement that there are generally more data gaps and
inconsistencies in acute reference values than there are in chronic
reference values. In some cases, when Reference Value Arrays \21\ for
HAPs have been developed, we consider additional acute values (i.e.,
occupational and international values) to provide a more complete risk
characterization.
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\20\ The SAB peer review of RTR Risk Assessment Methodologies is
available at https://yosemite.epa.gov/sab/sabproduct.nsf/
4AB3966E263D943A8525771F00668381/$File/EPA-SAB-10-007-unsigned.pdf.
\21\ U.S. EPA. (2009) Chapter 2.9, Chemical Specific Reference
Values for Formaldehyde in Graphical Arrays of Chemical-Specific
Health Effect Reference Values for Inhalation Exposures (Final
Report). U.S. Environmental Protection Agency, Washington, DC, EPA/
600/R-09/061, 2009, and available online at https://cfpub.epa.gov/ncea/cfm/recordisplay.cfm?deid=211003.
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4. How did we conduct the multipathway exposure and risk screening?
The EPA conducted a screening analysis examining the potential for
significant human health risks due to exposures via routes other than
inhalation (i.e., ingestion). We first determined whether any sources
in the source category emitted PB-HAP. The PB-HAP compounds or compound
classes are identified for the screening from the EPA's Air Toxics Risk
Assessment Library (available at https://www2.epa.gov/fera/risk-assessment-and-modeling-air-toxics-risk-assessment-reference-library).
For the 40 CFR part 63, subpart MM source category, we identified
emissions of cadmium compounds, lead compounds, mercury compounds, POM,
dioxins/furans, and hexachlorobenzene. Because one or more of these PB-
HAPs are emitted by at least one facility in the subpart MM source
category, we proceeded to the next step of the evaluation. In this
step, we determined whether the facility-specific emissions rates of
the emitted PB-HAP were large enough to create the potential for
significant non-inhalation human health risks under reasonable worst-
case conditions. To facilitate this step, we have developed emissions
rate screening levels for several PB-HAPs using a hypothetical upper-
end screening exposure scenario developed for use in conjunction with
the EPA's Total Risk Integrated Methodology Fate, Transport, and
Ecological Exposure (TRIM.FaTE) model. The PB-HAPs with emissions rate
screening levels are: Lead, cadmium, dioxins/furans, mercury compounds,
and POM. We conducted a sensitivity analysis on the screening scenario
to ensure that its key design parameters would represent the upper end
of the range of possible values, such that it would represent a
conservative, but not impossible, scenario. The facility-specific
emissions for each PB-HAP were compared to the emission rate screening
levels for these PB-HAPs to assess the potential for significant human
health risks via non-inhalation pathways. We call this application of
the TRIM.FaTE model the Tier 1 TRIM-screen or Tier 1 screen.
For the purpose of developing emission rate screening values for
our Tier 1 TRIM-screen, we derived emission levels for these PB-HAPs
(other than lead compounds) at which the maximum excess lifetime cancer
risk would be 1-in-1 million (i.e., for dioxins/furans and POM) or, for
HAPs that cause non-cancer health effects (i.e., cadmium compounds and
mercury compounds), the maximum HQ would be 1. If the emissions rate of
any PB-HAP included in the Tier 1 screen exceeds the Tier 1 screening
emissions level for any facility, we conduct a second screen, which we
call the Tier 2 TRIM-screen or Tier 2 screen.
In the Tier 2 screen, the location of each facility that exceeded
the Tier 1 emission level is used to refine the assumptions associated
with the environmental scenario while maintaining the exposure scenario
assumptions. A key assumption that is part of the Tier 1 screen is that
a lake is located near the facility; we confirm the existence of lakes
near the facility as part of the Tier 2 screen. We then adjust the
risk-based Tier 1 screening value for each PB-HAP for each facility
based on an understanding of how exposure concentrations estimated for
the screening scenario change with meteorology and environmental
assumptions. PB-HAP emissions that do not exceed these new Tier 2
screening levels are considered to pose no unacceptable risks. If the
PB-HAP emissions for a facility exceed the Tier 2 screening levels and
data are available, we may decide to conduct a more refined Tier 3
multipathway assessment. There are several analyses that can be
included in a Tier 3 screen depending upon the extent of refinement
warranted, including validating that the lake is fishable and
considering plume-rise to estimate emissions lost above the mixing
layer. If the Tier 3 screen is exceeded, the EPA may further refine the
assessment.
In evaluating the potential multipathway risk from emissions of
lead compounds, rather than developing a screening emissions rate for
them, we compared maximum estimated chronic inhalation exposures with
the level of the current National Ambient Air Quality Standard (NAAQS)
for lead.\22\ Values below the level of the primary (health-based) lead
NAAQS were considered to have a low potential for multipathway risk.
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\22\ In doing so, the EPA notes that the legal standard for a
primary NAAQS--that a standard is requisite to protect public health
and provide an adequate margin of safety (CAA section 109(b))--
differs from the CAA section 112(f) standard (requiring among other
things that the standard provide an ``ample margin of safety'').
However, the primary lead NAAQS is a reasonable measure of
determining risk acceptability (i.e., the first step of the Benzene
NESHAP analysis) since it is designed to protect the most
susceptible group in the human population--children, including
children living near major lead emitting sources. 73 FR 67002/3; 73
FR 67000/3; 73 FR 67005/1. In addition, applying the level of the
primary lead NAAQS at the risk acceptability step is conservative,
since that primary lead NAAQS reflects an adequate margin of safety.
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For further information on the multipathway analysis approach, see
the document titled Residual Risk Assessment for Pulp Mill Combustion
Sources in Support of the December 2016 Risk and Technology Review
Proposed Rule, which is available in the docket for this action.
5. How did we conduct the environmental risk screening assessment?
a. Adverse Environmental Effect
The EPA conducts a screening assessment to examine the potential
for adverse environmental effects as required under section
112(f)(2)(A) of the CAA. Section 112(a)(7) of the CAA defines ``adverse
environmental effect'' as ``any significant and widespread adverse
effect, which may reasonably be anticipated, to wildlife, aquatic life,
or other natural resources, including adverse impacts on populations of
endangered or threatened species or significant degradation of
environmental quality over broad areas.''
b. Environmental HAPs
The EPA focuses on seven HAPs, which we refer to as ``environmental
HAPs,'' in its screening analysis: Five PB-HAPs and two acid gases. The
five PB-HAPs are cadmium, dioxins/furans, POM, mercury (both inorganic
mercury and methyl mercury) and lead compounds. The two acid gases are
HCl and HF. The rationale for including these seven HAPs in the
environmental risk screening analysis is presented below.
The HAPs that persist and bioaccumulate are of particular
environmental concern because they accumulate in the soil, sediment,
and water. The PB-HAPs are taken up, through sediment, soil, water,
and/or
[[Page 97059]]
ingestion of other organisms, by plants or animals (e.g., small fish)
at the bottom of the food chain. As larger and larger predators consume
these organisms, concentrations of the PB-HAPs in the animal tissues
increases as does the potential for adverse effects. The five PB-HAPs
we evaluate as part of our screening analysis account for 99.8 percent
of all PB-HAP emissions nationally from stationary sources (on a mass
basis from the 2005 EPA NEI).
In addition to accounting for almost all of the mass of PB-HAPs
emitted, we note that the TRIM.FaTE model that we use to evaluate
multipathway risk allows us to estimate concentrations of cadmium
compounds, dioxins/furans, POM, and mercury in soil, sediment and
water. For lead compounds, we currently do not have the ability to
calculate these concentrations using the TRIM.FaTE model. Therefore, to
evaluate the potential for adverse environmental effects from lead
compounds, we compare the estimated exposures from the source category
emissions of lead with the level of the secondary NAAQS for lead.\23\
We consider values below the level of the secondary lead NAAQS to be
unlikely to cause adverse environmental effects.
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\23\ The Secondary Lead NAAQS is a reasonable measure of
determining whether there is an adverse environmental effect since
it was established considering ``effects on soils, water, crops,
vegetation, man-made materials, animals, wildlife, weather,
visibility and climate, damage to and deterioration of property, and
hazards to transportation, as well as effects on economic values and
on personal comfort and well-being.''
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Due to their well-documented potential to cause direct damage to
terrestrial plants, we include two acid gases, HCl and HF, in the
environmental screening analysis. According to the 2005 NEI, HCl and HF
account for about 99 percent (on a mass basis) of the total acid gas
HAPs emitted by stationary sources in the United States. In addition to
the potential to cause direct damage to plants, high concentrations of
HF in the air have been linked to fluorosis in livestock. Air
concentrations of these HAPs are already calculated as part of the
human multipathway exposure and risk screening analysis using the HEM3-
AERMOD air dispersion model, and we are able to use the air dispersion
modeling results to estimate the potential for an adverse environmental
effect.
The EPA acknowledges that other HAPs beyond the seven HAPs
discussed above may have the potential to cause adverse environmental
effects. Therefore, the EPA may include other relevant HAPs in its
environmental risk screening in the future, as modeling science and
resources allow. The EPA invites comment on the extent to which other
HAPs emitted by the source category may cause adverse environmental
effects. Such information should include references to peer-reviewed
ecological effects benchmarks that are of sufficient quality for making
regulatory decisions, as well as information on the presence of
organisms located near facilities within the source category that such
benchmarks indicate could be adversely affected.
c. Ecological Assessment Endpoints and Benchmarks for PB-HAP
An important consideration in the development of the EPA's
screening methodology is the selection of ecological assessment
endpoints and benchmarks. Ecological assessment endpoints are defined
by the ecological entity (e.g., aquatic communities including fish and
plankton) and its attributes (e.g., frequency of mortality). Ecological
assessment endpoints can be established for organisms, populations,
communities or assemblages, and ecosystems.
For PB-HAPs (other than lead compounds), we evaluated the following
community-level ecological assessment endpoints to screen for organisms
directly exposed to HAPs in soils, sediment, and water:
Local terrestrial communities (i.e., soil invertebrates,
plants) and populations of small birds and mammals that consume soil
invertebrates exposed to PB-HAPs in the surface soil;
Local benthic (i.e., bottom sediment dwelling insects,
amphipods, isopods, and crayfish) communities exposed to PB-HAPs in
sediment in nearby water bodies; and
Local aquatic (water-column) communities (including fish
and plankton) exposed to PB-HAP in nearby surface waters.
For PB-HAPs (other than lead compounds), we also evaluated the
following population-level ecological assessment endpoint to screen for
indirect HAP exposures of top consumers via the bioaccumulation of HAPs
in food chains:
Piscivorous (i.e., fish-eating) wildlife consuming PB-HAP-
contaminated fish from nearby water bodies.
For cadmium compounds, dioxins/furans, POM, and mercury, we
identified the available ecological benchmarks for each assessment
endpoint. An ecological benchmark represents a concentration of HAPs
(e.g., 0.77 [mu]g of HAP per liter of water) that has been linked to a
particular environmental effect level through scientific study. For PB-
HAPs we identified, where possible, ecological benchmarks at the
following effect levels:
Probable effect levels (PEL): Level above which adverse
effects are expected to occur frequently;
Lowest-observed-adverse-effect level (LOAEL): The lowest
exposure level tested at which there are biologically significant
increases in frequency or severity of adverse effects; and
No-observed-adverse-effect levels (NOAEL): The highest
exposure level tested at which there are no biologically significant
increases in the frequency or severity of adverse effect.
We established a hierarchy of preferred benchmark sources to allow
selection of benchmarks for each environmental HAP at each ecological
assessment endpoint. In general, the EPA sources that are used at a
programmatic level (e.g., Office of Water, Superfund Program) were used
in the analysis, if available. If unavailable, the EPA benchmarks used
in regional programs (e.g., Superfund) were used. If benchmarks were
not available at a programmatic or regional level, we used benchmarks
developed by other federal agencies (e.g., National Oceanic and
Atmospheric Administration (NOAA)) or state agencies.
Benchmarks for all effect levels are not available for all PB-HAPs
and assessment endpoints. In cases where multiple effect levels were
available for a particular PB-HAP and assessment endpoint, we use all
of the available effect levels to help us to determine whether
ecological risks exist and, if so, whether the risks could be
considered significant and widespread.
d. Ecological Assessment Endpoints and Benchmarks for Acid Gases
The environmental screening analysis also evaluated potential
damage and reduced productivity of plants due to direct exposure to
acid gases in the air. For acid gases, we evaluated the following
ecological assessment endpoint:
Local terrestrial plant communities with foliage exposed
to acidic gaseous HAPs in the air.
The selection of ecological benchmarks for the effects of acid
gases on plants followed the same approach as for PB-HAPs (i.e., we
examine all of the available chronic benchmarks). For HCl, the EPA
identified chronic benchmark concentrations. We note that the benchmark
for chronic HCl exposure
[[Page 97060]]
to plants is greater than the reference concentration for chronic
inhalation exposure for human health. This means that where the EPA
includes regulatory requirements to prevent an exceedance of the
reference concentration for human health, additional analyses for
adverse environmental effects of HCl would not be necessary.
For HF, the EPA identified chronic benchmark concentrations for
plants and evaluated chronic exposures to plants in the screening
analysis. High concentrations of HF in the air have also been linked to
fluorosis in livestock. However, the HF concentrations at which
fluorosis in livestock occur are higher than those at which plant
damage begins. Therefore, the benchmarks for plants are protective of
both plants and livestock.
e. Screening Methodology
For the environmental risk screening analysis, the EPA first looked
at whether any facilities in the 40 CFR part 63, subpart MM source
category emitted any of the seven environmental HAPs. Because we found
that one or more of the seven environmental HAPs evaluated are emitted
by at least one facility in the source category, we proceeded to the
second step of the evaluation.
f. PB-HAP Methodology
For cadmium, mercury, POM, and dioxins/furans, the environmental
screening analysis consists of two tiers, while lead compounds are
analyzed differently as discussed earlier. In the first tier, we
determined whether the maximum facility-specific emission rates of each
of the emitted environmental HAPs were large enough to create the
potential for adverse environmental effects under reasonable worst-case
environmental conditions. These are the same environmental conditions
used in the human multipathway exposure and risk screening analysis.
To facilitate this step, TRIM.FaTE was run for each PB-HAP under
hypothetical environmental conditions designed to provide
conservatively high HAP concentrations. The model was set to maximize
runoff from terrestrial parcels into the modeled lake, which in turn,
maximized the chemical concentrations in the water, the sediments, and
the fish. The resulting media concentrations were then used to back-
calculate a screening level emission rate that corresponded to the
relevant exposure benchmark concentration value for each assessment
endpoint. To assess emissions from a facility, the reported emission
rate for each PB-HAP was compared to the screening level emission rate
for that PB-HAP for each assessment endpoint. If emissions from a
facility do not exceed the Tier 1 screening level, the facility
``passes'' the screen, and, therefore, is not evaluated further under
the screening approach. If emissions from a facility exceed the Tier 1
screening level, we evaluate the facility further in Tier 2.
In Tier 2 of the environmental screening analysis, the emission
rate screening levels are adjusted to account for local meteorology and
the actual location of lakes in the vicinity of facilities that did not
pass the Tier 1 screen. The modeling domain for each facility in the
Tier 2 analysis consists of 8 octants. Each octant contains 5 modeled
soil concentrations at various distances from the facility (5 soil
concentrations x 8 octants = total of 40 soil concentrations per
facility) and 1 lake with modeled concentrations for water, sediment
and fish tissue. In the Tier 2 environmental risk screening analysis,
the 40 soil concentration points are averaged to obtain an average soil
concentration for each facility for each PB-HAP. For the water,
sediment, and fish tissue concentrations, the highest value for each
facility for each pollutant is used. If emission concentrations from a
facility do not exceed the Tier 2 screening level, the facility passes
the screen, and typically is not evaluated further. If emissions from a
facility exceed the Tier 2 screening level, the facility does not pass
the screen and, therefore, may have the potential to cause adverse
environmental effects. Such facilities are evaluated further to
investigate factors such as the magnitude and characteristics of the
area of exceedance.
g. Acid Gas Methodology
The environmental screening analysis evaluates the potential
phytotoxicity and reduced productivity of plants due to chronic
exposure to acid gases. The environmental risk screening methodology
for acid gases is a single-tier screen that compares the average off-
site ambient air concentration over the modeling domain to ecological
benchmarks for each of the acid gases. Because air concentrations are
compared directly to the ecological benchmarks, emission-based
screening levels are not calculated for acid gases as they are in the
ecological risk screening methodology for PB-HAPs.
For purposes of ecological risk screening, the EPA identifies a
potential for adverse environmental effects to plant communities from
exposure to acid gases when the average concentration of the HAP around
a facility exceeds the LOAEL ecological benchmark. In such cases, we
further investigate factors such as the magnitude and characteristics
of the area of exceedance (e.g., land use of exceedance area, size of
exceedance area) to determine if there is an adverse environmental
effect. For further information on the environmental screening analysis
approach, see the Residual Risk Assessment for Pulp Mill Combustion
Sources in Support of the December 2016 Risk and Technology Review
Proposed Rule, which is available in the docket for this action.
6. How did we conduct facility-wide assessments?
To put the source category risks in context, we typically examine
the risks from the entire ``facility,'' where the facility includes all
HAP-emitting operations within a contiguous area and under common
control. In other words, we examine the HAP emissions not only from the
source category emission points of interest, but also emissions of HAPs
from all other emission sources at the facility for which we have data.
There are currently 108 major sources subject to the 40 CFR part 63,
subpart MM source category which includes chemical recovery combustion
sources (e.g., recovery furnace, SDT, lime kiln). Nearly all major
sources also have boilers on site. These facilities engage in chemical
or mechanical pulping, papermaking, paper coating, landfills, petroleum
storage and transfer, and other operations. Therefore, where data were
available, we performed a facility-wide risk assessment for these major
sources as part of this action. For this source category, we conducted
the facility-wide assessment using the data from Part II of the Pulp
and Paper Sector ICR.
We analyzed risks due to the inhalation of HAPs that are emitted
``facility-wide'' for the populations residing within 50 km of each
facility, consistent with the methods used for the source category
analysis described above. For these facility-wide risk analyses, the
modeled source category risks were compared to the facility-wide risks
to determine the portion of facility-wide risks that could be
attributed to the source category addressed in this proposal. We
specifically examined the facility that was associated with the highest
estimate of risk and determined the percentage of that risk
attributable to the source category of interest. The document titled
Residual Risk Assessment for Pulp Mill Combustion Sources in Support of
the December 2016 Risk and Technology Review
[[Page 97061]]
Proposed Rule, available in the docket for this action, provides the
methodology and results of the facility-wide analyses, including all
facility-wide risks and the percentage of source category contribution
to facility-wide risks.
7. How did we consider uncertainties in risk assessment?
In the Benzene NESHAP, the Agency concluded that risk estimation
uncertainty should be considered in our decision-making under the ample
margin of safety framework. Uncertainty and the potential for bias are
inherent in all risk assessments, including those performed for this
proposal. Although uncertainty exists, we believe that our approach,
which used conservative tools and assumptions, ensures that our
decisions are health-protective and environmentally protective. A brief
discussion of the uncertainties in the RTR emissions dataset,
dispersion modeling, inhalation exposure estimates, and dose-response
relationships follows below. Where relevant to the estimated exposures,
the lack of short-term dose-response values at different levels of
severity should be factored into the risk characterization as potential
uncertainties. A more thorough discussion of these uncertainties is
included in the document titled Residual Risk Assessment for Pulp Mill
Combustion Sources in Support of the December 2016 Risk and Technology
Review Proposed Rule, which is available in the docket for this action.
a. Uncertainties in the RTR Emissions Dataset
Although the development of the RTR emissions dataset involved
quality assurance/quality control processes, various uncertainties
exist. Thus, the accuracy of emissions values will vary depending on
the source of the data, the degree to which data are incomplete or
missing, the degree to which assumptions made to complete the datasets
are accurate, errors in emission estimates, and other factors. The
emission estimates considered in this analysis generally are annual
totals for certain years, and they do not reflect short-term
fluctuations during the course of a year or variations from year to
year. The estimates of peak hourly emission rates for the acute effects
screening assessment were based on an emission adjustment factor
applied to the average annual hourly emission rates, which are intended
to account for emission fluctuations due to normal facility operations.
b. Uncertainties in Dispersion Modeling
We recognize there is uncertainty in ambient concentration
estimates associated with any model, including the EPA's recommended
regulatory dispersion model, AERMOD. In using a model to estimate
ambient pollutant concentrations, the user chooses certain options to
apply. For RTR assessments, we select some model options that have the
potential to overestimate ambient air concentrations (e.g., not
including plume depletion or pollutant transformation). We select other
model options that have the potential to underestimate ambient impacts
(e.g., not including building downwash). Other options that we select
have the potential to either under- or overestimate ambient levels
(e.g., meteorology and receptor locations). On balance, considering the
directional nature of the uncertainties commonly present in ambient
concentrations estimated by dispersion models, the approach we apply in
the RTR assessments should yield unbiased estimates of ambient HAP
concentrations.
c. Uncertainties in Inhalation Exposure
The EPA did not include the effects of human mobility on exposures
in the assessment. Specifically, short-term mobility and long-term
mobility between census blocks in the modeling domain were not
considered.\24\ The approach of not considering short or long-term
population mobility does not bias the estimate of the theoretical MIR
(by definition), nor does it affect the estimate of cancer incidence
because the total population number remains the same. It does, however,
affect the shape of the distribution of individual risks across the
affected population, shifting it toward higher estimated individual
risks at the upper end and reducing the number of people estimated to
be at lower risks, thereby increasing the estimated number of people at
specific high risk levels (e.g., 1-in-10 thousand or 100-in-1 million).
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\24\ Short-term mobility is movement from one micro-environment
to another over the course of hours or days. Long-term mobility is
movement from one residence to another over the course of a
lifetime.
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In addition, the assessment predicted the chronic exposures at the
centroid of each populated census block as surrogates for the exposure
concentrations for all people living in that block. Using the census
block centroid to predict chronic exposures tends to over-predict
exposures for people in the census block who live farther from the
facility and under-predict exposures for people in the census block who
live closer to the facility. Thus, using the census block centroid to
predict chronic exposures may lead to a potential understatement or
overstatement of the true maximum impact, but is an unbiased estimate
of average risk and incidence. We reduce this uncertainty by analyzing
large census blocks near facilities using aerial imagery and adjusting
the location of the block centroid to better represent the population
in the block, as well as adding additional receptor locations where the
block population is not well represented by a single location.
The assessment evaluates the cancer inhalation risks associated
with pollutant exposures over a 70-year period, which is the assumed
lifetime of an individual. In reality, both the length of time that
modeled emission sources at facilities actually operate (i.e., more or
less than 70 years) and the domestic growth or decline of the modeled
industry (i.e., the increase or decrease in the number or size of
domestic facilities) will influence the future risks posed by a given
source or source category. Depending on the characteristics of the
industry, these factors will, in most cases, result in an overestimate
both in individual risk levels and in the total estimated number of
cancer cases. However, in the unlikely scenario where a facility
maintains, or even increases, its emissions levels over a period of
more than 70 years, residents live beyond 70 years at the same
location, and the residents spend most of their days at that location,
then the cancer inhalation risks could potentially be underestimated.
However, annual cancer incidence estimates from exposures to emissions
from these sources would not be affected by the length of time an
emissions source operates.
The exposure estimates used in these analyses assume chronic
exposures to ambient (outdoor) levels of pollutants. Because most
people spend the majority of their time indoors, actual exposures may
not be as high, depending on the characteristics of the pollutants
modeled. For many of the HAPs, indoor levels are roughly equivalent to
ambient levels, but for very reactive pollutants or larger particles,
indoor levels are typically lower. This factor has the potential to
result in an overestimate of 25 to 30 percent of exposures.\25\
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\25\ U.S. EPA. National-Scale Air Toxics Assessment for 1996.
(EPA 453/R-01-003; January 2001; page 85.)
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In addition to the uncertainties highlighted above, there are
several factors specific to the acute exposure
[[Page 97062]]
assessment that the EPA conducts as part of the risk review under
section 112 of the CAA that should be highlighted. The accuracy of an
acute inhalation exposure assessment depends on the simultaneous
occurrence of independent factors that may vary greatly, such as hourly
emissions rates, meteorology, and the present of humans at the location
of the maximum concentration. In the acute screening assessment that we
conduct under the RTR program, we assume that peak emissions from the
source category and worst-case meteorological conditions co-occur,
thus, resulting in maximum ambient concentrations. These two events are
unlikely to occur at the same time, making these assumptions
conservative. We then include the additional assumption that a person
is located at this point during this same time period. For this source
category, these assumptions would tend to be worst-case actual
exposures, as it is unlikely that a person would be located at the
point of maximum exposure during the time when peak emissions and
worst-case meteorological conditions occur simultaneously.
d. Uncertainties in Dose-Response Relationships
There are uncertainties inherent in the development of the dose-
response values used in our risk assessments for cancer effects from
chronic exposures and non-cancer effects from both chronic and acute
exposures. Some uncertainties may be considered quantitatively, and
others generally are expressed in qualitative terms. We note as a
preface to this discussion a point on dose-response uncertainty that is
brought out in the EPA's 2005 Cancer Guidelines; namely, that ``the
primary goal of EPA actions is protection of human health; accordingly,
as an Agency policy, risk assessment procedures, including default
options that are used in the absence of scientific data to the
contrary, should be health protective'' (EPA's 2005 Cancer Guidelines,
pages 1-7). This is the approach followed here as summarized in the
next several paragraphs. A complete detailed discussion of
uncertainties and variability in dose-response relationships is given
in the Residual Risk Assessment for Pulp Mill Combustion Sources in
Support of the December 2016 Risk and Technology Review Proposed Rule,
which is available in the docket for this action.
Cancer URE values used in our risk assessments are those that have
been developed to generally provide an upper bound estimate of risk.
That is, they represent a ``plausible upper limit to the true value of
a quantity'' (although this is usually not a true statistical
confidence limit).\26\ In some circumstances, the true risk could be as
low as zero; however, in other circumstances the risk could be
greater.\27\ When developing an upper bound estimate of risk and to
provide risk values that do not underestimate risk, health-protective
default approaches are generally used. To err on the side of ensuring
adequate health protection, the EPA typically uses the upper bound
estimates rather than lower bound or central tendency estimates in our
risk assessments, an approach that may have limitations for other uses
(e.g., priority-setting or expected benefits analysis).
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\26\ IRIS glossary (https://iaspub.epa.gov/sor_internet/registry/termreg/searchandretrieve/glossariesandkeywordlists/search.do?details=&vocabName=IRIS%20Glossary).
\27\ An exception to this is the URE for benzene, which is
considered to cover a range of values, each end of which is
considered to be equally plausible, and which is based on maximum
likelihood estimates.
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Chronic non-cancer RfC and reference dose (RfD) values represent
chronic exposure levels that are intended to be health-protective
levels. Specifically, these values provide an estimate (with
uncertainty spanning perhaps an order of magnitude) of a continuous
inhalation exposure (i.e., the RfC) or a daily oral exposure (i.e., the
RfD) to the human population (including sensitive subgroups) that is
likely to be without an appreciable risk of deleterious effects during
a lifetime. To derive values that are intended to be ``without
appreciable risk,'' the methodology relies upon an uncertainty factor
(UF) approach (U.S. EPA, 1993 and 1994) which considers uncertainty,
variability and gaps in the available data. The UFs are applied to
derive reference values that are intended to protect against
appreciable risk of deleterious effects. The UFs are commonly default
values,\28\ e.g., factors of 10 or 3, used in the absence of compound-
specific data; where data are available, UFs may also be developed
using compound-specific information. When data are limited, more
assumptions are needed and more UFs are used. Thus, there may be a
greater tendency to overestimate risk in the sense that further study
might support development of reference values that are higher (i.e.,
less potent) because fewer default assumptions are needed. However, for
some pollutants, it is possible that risks may be underestimated.
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\28\ According to the NRC report, Science and Judgment in Risk
Assessment (NRC, 1994) ``[Default] options are generic approaches,
based on general scientific knowledge and policy judgment, that are
applied to various elements of the risk assessment process when the
correct scientific model is unknown or uncertain.'' The 1983 NRC
report, Risk Assessment in the Federal Government: Managing the
Process, defined default option as ``the option chosen on the basis
of risk assessment policy that appears to be the best choice in the
absence of data to the contrary'' (NRC, 1983a, p. 63). Therefore,
default options are not rules that bind the Agency; rather, the
Agency may depart from them in evaluating the risks posed by a
specific substance when it believes this to be appropriate. In
keeping with the EPA's goal of protecting public health and the
environment, default assumptions are used to ensure that risk to
chemicals is not underestimated (although defaults are not intended
to overtly overestimate risk). See U.S. EPA, An Examination of EPA
Risk Assessment Principles and Practices, EPA/100/B-04/001, 2004
available at: https://training.fws.gov/resources/course-resources/pesticides/Risk%20Assessment/Risk%20Assessment%20Principles%20and%20Practices.pdf.
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While collectively termed ``UF,'' these factors account for a
number of different quantitative considerations when using observed
animal (usually rodent) or human toxicity data in the development of
the RfC. The UFs are intended to account for: (1) variation in
susceptibility among the members of the human population (i.e., inter-
individual variability); (2) uncertainty in extrapolating from
experimental animal data to humans (i.e., interspecies differences);
(3) uncertainty in extrapolating from data obtained in a study with
less-than-lifetime exposure (i.e., extrapolating from sub-chronic to
chronic exposure); (4) uncertainty in extrapolating the observed data
to obtain an estimate of the exposure associated with no adverse
effects; and (5) uncertainty when the database is incomplete or there
are problems with the applicability of available studies.
Many of the UFs used to account for variability and uncertainty in
the development of acute reference values are quite similar to those
developed for chronic durations, but they more often use individual UF
values that may be less than 10. The UFs are applied based on chemical-
specific or health effect-specific information (e.g., simple irritation
effects do not vary appreciably between human individuals, hence a
value of 3 is typically used), or based on the purpose for the
reference value (see the following paragraph). The UFs applied in acute
reference value derivation include: (1) Heterogeneity among humans; (2)
uncertainty in extrapolating from animals to humans; (3) uncertainty in
lowest observed adverse effect (exposure) level to no observed adverse
effect (exposure) level adjustments; and (4) uncertainty in accounting
for an incomplete database on toxic effects of potential concern.
Additional adjustments are often applied to account for uncertainty in
[[Page 97063]]
extrapolation from observations at one exposure duration (e.g., 4
hours) to derive an acute reference value at another exposure duration
(e.g., 1 hour).
Not all acute reference values are developed for the same purpose,
and care must be taken when interpreting the results of an acute
assessment of human health effects relative to the reference value or
values being exceeded. Where relevant to the estimated exposures, the
lack of short-term dose-response values at different levels of severity
should be factored into the risk characterization as potential
uncertainties.
For a group of compounds that are unspeciated (e.g., glycol
ethers), we conservatively use the most protective reference value of
an individual compound in that group to estimate risk. Similarly, for
an individual compound in a group (e.g., ethylene glycol diethyl ether)
that does not have a specified reference value, we also apply the most
protective reference value from the other compounds in the group to
estimate risk.
e. Uncertainties in the Multipathway Assessment
For each source category, we generally rely on site-specific levels
of PB-HAP emissions to determine whether a refined assessment of the
impacts from multipathway exposures is necessary. This determination is
based on the results of a three-tiered screening analysis that relies
on the outputs from models that estimate environmental pollutant
concentrations and human exposures for four PB-HAPs. Two important
types of uncertainty associated with the use of these models in RTR
risk assessments and inherent to any assessment that relies on
environmental modeling are model uncertainty and input uncertainty.\29\
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\29\ In the context of this discussion, the term ``uncertainty''
as it pertains to exposure and risk encompasses both variability in
the range of expected inputs and screening results due to existing
spatial, temporal, and other factors, as well as uncertainty in
being able to accurately estimate the true result.
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Model uncertainty concerns whether the selected models are
appropriate for the assessment being conducted and whether they
adequately represent the actual processes that might occur for that
situation. An example of model uncertainty is the question of whether
the model adequately describes the movement of a pollutant through the
soil. This type of uncertainty is difficult to quantify. However, based
on feedback received from previous EPA SAB reviews and other reviews,
we are confident that the models used in the screen are appropriate and
state-of-the-art for the multipathway risk assessments conducted in
support of RTR.
Input uncertainty is concerned with how accurately the models have
been configured and parameterized for the assessment at hand. For Tier
1 of the multipathway screen, we configured the models to avoid
underestimating exposure and risk. This was accomplished by selecting
upper-end values from nationally-representative datasets for the more
influential parameters in the environmental model, including selection
and spatial configuration of the area of interest, lake location and
size, meteorology, surface water and soil characteristics, and
structure of the aquatic food web. We also assume an ingestion exposure
scenario and values for human exposure factors that represent
reasonable maximum exposures.
In Tier 2 of the multipathway assessment, we refine the model
inputs to account for meteorological patterns in the vicinity of the
facility versus using upper-end national values, and we identify the
actual location of lakes near the facility rather than the default lake
location that we apply in Tier 1. By refining the screening approach in
Tier 2 to account for local geographical and meteorological data, we
decrease the likelihood that concentrations in environmental media are
overestimated, thereby increasing the usefulness of the screen. The
assumptions and the associated uncertainties regarding the selected
ingestion exposure scenario are the same for Tier 1 and Tier 2.
For both Tiers 1 and 2 of the multipathway assessment, our approach
to addressing model input uncertainty is generally cautious. We choose
model inputs from the upper end of the range of possible values for the
influential parameters used in the models, and we assume that the
exposed individual exhibits ingestion behavior that would lead to a
high total exposure. This approach reduces the likelihood of not
identifying high risks for adverse impacts.
Despite the uncertainties, when individual pollutants or facilities
do screen out, we are confident that the potential for adverse
multipathway impacts on human health is very low. On the other hand,
when individual pollutants or facilities do not screen out, it does not
mean that multipathway impacts are significant, only that we cannot
rule out that possibility and that a refined multipathway analysis for
the site might be necessary to obtain a more accurate risk
characterization for the source category.
For further information on uncertainties and the Tier 1 and 2
screening methods, refer to the risk document, Appendix 6, Technical
Support Document for TRIM-Based Multipathway Tiered Screening
Methodology for RTR.
f. Uncertainties in the Environmental Risk Screening Assessment
For each source category, we generally rely on site-specific levels
of environmental HAP emissions to perform an environmental screening
assessment. The environmental screening assessment is based on the
outputs from models that estimate environmental HAP concentrations. The
same models, specifically the TRIM.FaTE multipathway model and the
AERMOD air dispersion model, are used to estimate environmental HAP
concentrations for both the human multipathway screening analysis and
for the environmental screening analysis. Therefore, both screening
assessments have similar modeling uncertainties.
Two important types of uncertainty associated with the use of these
models in RTR environmental screening assessments (and inherent to any
assessment that relies on environmental modeling) are model uncertainty
and input uncertainty.\30\
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\30\ In the context of this discussion, the term
``uncertainty,'' as it pertains to exposure and risk assessment,
encompasses both variability in the range of expected inputs and
screening results due to existing spatial, temporal, and other
factors, as well as uncertainty in being able to accurately estimate
the true result.
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Model uncertainty concerns whether the selected models are
appropriate for the assessment being conducted and whether they
adequately represent the movement and accumulation of environmental HAP
emissions in the environment. For example, does the model adequately
describe the movement of a pollutant through the soil? This type of
uncertainty is difficult to quantify. However, based on feedback
received from previous EPA SAB reviews and other reviews, we are
confident that the models used in the screen are appropriate and state-
of-the-art for the environmental risk assessments conducted in support
of our RTR analyses.
Input uncertainty is concerned with how accurately the models have
been configured and parameterized for the assessment at hand. For Tier
1 of the environmental screen for PB-HAPs, we configured the models to
avoid underestimating exposure and risk to reduce the likelihood that
the results
[[Page 97064]]
indicate the risks are lower than they actually are. This was
accomplished by selecting upper-end values from nationally-
representative datasets for the more influential parameters in the
environmental model, including selection and spatial configuration of
the area of interest, the location and size of any bodies of water,
meteorology, surface water and soil characteristics, and structure of
the aquatic food web. In Tier 1, we used the maximum facility-specific
emissions for the PB-HAPs (other than lead compounds, which were
evaluated by comparison to the Secondary Lead NAAQS) that were included
in the environmental screening assessment and each of the media when
comparing to ecological benchmarks. This is consistent with the
conservative design of Tier 1 of the screen. In Tier 2 of the
environmental screening analysis for PB-HAPs, we refine the model
inputs to account for meteorological patterns in the vicinity of the
facility versus using upper-end national values, and we identify the
locations of water bodies near the facility location. By refining the
screening approach in Tier 2 to account for local geographical and
meteorological data, we decrease the likelihood that concentrations in
environmental media are overestimated, thereby increasing the
usefulness of the screen. To better represent widespread impacts, the
modeled soil concentrations are averaged in Tier 2 to obtain one
average soil concentration value for each facility and for each PB-HAP.
For PB-HAP concentrations in water, sediment, and fish tissue, the
highest value for each facility for each pollutant is used.
For the environmental screening assessment for acid gases, we
employ a single-tiered approach. We use the modeled air concentrations
and compare those with ecological benchmarks.
For both Tiers 1 and 2 of the environmental screening assessment,
our approach to addressing model input uncertainty is generally
cautious. We choose model inputs from the upper end of the range of
possible values for the influential parameters used in the models, and
we assume that the exposed individual exhibits ingestion behavior that
would lead to a high total exposure. This approach reduces the
likelihood of not identifying potential risks for adverse environmental
impacts.
Uncertainty also exists in the ecological benchmarks for the
environmental risk screening analysis. We established a hierarchy of
preferred benchmark sources to allow selection of benchmarks for each
environmental HAP at each ecological assessment endpoint. In general,
EPA benchmarks used at a programmatic level (e.g., Office of Water,
Superfund Program) were used if available. If unavailable, we used EPA
benchmarks used in regional programs (e.g., Superfund Program). If
benchmarks were not available at a programmatic or regional level, we
used benchmarks developed by other agencies (e.g., NOAA) or by state
agencies.
In all cases (except for lead compounds, which were evaluated
through a comparison to the NAAQS), we searched for benchmarks at the
following three effect levels, as described in section III.A.5 of this
preamble:
1. A no-effect level (i.e., NOAEL).
2. Threshold-effect level (i.e., LOAEL).
3. Probable effect level (i.e., PEL).
For some ecological assessment endpoint/environmental HAP
combinations, we could identify benchmarks for all three effect levels,
but for most, we could not. In one case, where different agencies
derived significantly different numbers to represent a threshold for
effect, we included both. In several cases, only a single benchmark was
available. In cases where multiple effect levels were available for a
particular PB-HAP and assessment endpoint, we used all of the available
effect levels to help us to determine whether risk exists and if the
risks could be considered significant and widespread.
The EPA evaluates the following seven HAPs in the environmental
risk screening assessment: cadmium, dioxins/furans, POM, mercury (both
inorganic mercury and methyl mercury), lead compounds, HCl, and HF,
where applicable. These seven HAPs represent pollutants that can cause
adverse impacts for plants and animals either through direct exposure
to HAPs in the air or through exposure to HAPs that is deposited from
the air onto soils and surface waters. These seven HAPs also represent
those HAPs for which we can conduct a meaningful environmental risk
screening assessment. For other HAPs not included in our screening
assessment, the model has not been parameterized such that it can be
used for that purpose. In some cases, depending on the HAP, we may not
have appropriate multipathway models that allow us to predict the
concentration of that pollutant. The EPA acknowledges that other HAPs
beyond the seven HAPs that we are evaluating may have the potential to
cause adverse environmental effects and, therefore, the EPA may
evaluate other relevant HAPs in the future, as modeling science and
resources allow.
Further information on uncertainties and the Tier 1 and 2
environmental screening methods is provided in Appendix 6 of the
document, Technical Support Document for TRIM-Based Multipathway Tiered
Screening Methodology for RTR. Also, see the document titled Residual
Risk Assessment for Pulp Mill Combustion Sources in Support of the
December 2016 Risk and Technology Review Proposed Rule, available in
the docket for this action.
B. How did we consider the risk results in making decisions for this
proposal?
As discussed in section II.A of this preamble, in evaluating and
developing standards under CAA section 112(f)(2), we apply a two-step
process to address residual risk. In the first step, the EPA determines
whether risks are acceptable. This determination ``considers all health
information, including risk estimation uncertainty, and includes a
presumptive limit on maximum individual lifetime [cancer] risk (MIR)
\31\ of approximately [1-in-10 thousand] [i.e., 100-in-1 million].'' 54
FR 38045, September 14, 1989. If risks are unacceptable, the EPA must
determine the emissions standards necessary to bring risks to an
acceptable level without considering costs. In the second step of the
process, the EPA considers whether the emissions standards provide an
ample margin of safety ``in consideration of all health information,
including the number of persons at risk levels higher than
approximately 1-in-1 million, as well as other relevant factors,
including costs and economic impacts, technological feasibility, and
other factors relevant to each particular decision.'' Id. The EPA must
promulgate emission standards necessary to provide an ample margin of
safety. After conducting the ample margin of safety analysis, we
consider whether a more stringent standard is necessary to prevent,
taking into consideration, costs, energy, safety, and other relevant
factors, an adverse environmental effect.
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\31\ Although defined as ``maximum individual risk,'' MIR refers
only to cancer risk. MIR, one metric for assessing cancer risk, is
the estimated risk were an individual exposed to the maximum level
ofa pollutant for a lifetime.
---------------------------------------------------------------------------
In past residual risk actions, the EPA considered a number of human
health risk metrics associated with emissions from the categories under
review, including the MIR, the number of persons in various risk
ranges, cancer incidence, the maximum non-cancer HI and the maximum
acute non-cancer hazard. See, e.g., 72 FR 25138, May 3,
[[Page 97065]]
2007; and 71 FR 42724, July 27, 2006. The EPA considered this health
information for both actual and allowable emissions. See, e.g., 75 FR
65068, October 21, 2010; 75 FR 80220, December 21, 2010; 76 FR 29032,
May 19, 2011. The EPA also discussed risk estimation uncertainties and
considered the uncertainties in the determination of acceptable risk
and ample margin of safety in these past actions. The EPA considered
this same type of information in support of this action.
The Agency is considering these various measures of health
information to inform our determinations of risk acceptability and
ample margin of safety under CAA section 112(f). As explained in the
Benzene NESHAP, ``the first step judgment on acceptability cannot be
reduced to any single factor'' and, thus, ``[t]he Administrator
believes that the acceptability of risk under [previous] section 112 is
best judged on the basis of a broad set of health risk measures and
information.'' 54 FR 38046, September 14, 1989. Similarly, with regard
to the ample margin of safety determination, ``the Agency again
considers all of the health risk and other health information
considered in the first step. Beyond that information, additional
factors relating to the appropriate level of control will also be
considered, including cost and economic impacts of controls,
technological feasibility, uncertainties, and any other relevant
factors.'' Id.
The Benzene NESHAP approach provides flexibility regarding factors
the EPA may consider in making determinations and how the EPA may weigh
those factors for each source category. In responding to comment on our
policy under the Benzene NESHAP, the EPA explained that:
``[t]he policy chosen by the Administrator permits consideration
of multiple measures of health risk. Not only can the MIR figure be
considered, but also incidence, the presence of non-cancer health
effects, and the uncertainties of the risk estimates. In this way,
the effect on the most exposed individuals can be reviewed as well
as the impact on the general public. These factors can then be
weighed in each individual case. This approach complies with the
Vinyl Chloride mandate that the Administrator ascertain an
acceptable level of risk to the public by employing [her] expertise
to assess available data. It also complies with the Congressional
intent behind the CAA, which did not exclude the use of any
particular measure of public health risk from the EPA's
consideration with respect to CAA section 112 regulations, and
thereby implicitly permits consideration of any and all measures of
health risk which the Administrator, in [her] judgment, believes are
appropriate to determining what will `protect the public health'.''
See 54 FR at 38057, September 14, 1989. Thus, the level of the MIR is
only one factor to be weighed in determining acceptability of risks.
The Benzene NESHAP explained that ``an MIR of approximately one in 10
thousand should ordinarily be the upper end of the range of
acceptability. As risks increase above this benchmark, they become
presumptively less acceptable under CAA section 112, and would be
weighed with the other health risk measures and information in making
an overall judgment on acceptability. Or, the Agency may find, in a
particular case, that a risk that includes MIR less than the
presumptively acceptable level is unacceptable in the light of other
health risk factors.'' Id. at 38045. Similarly, with regard to the
ample margin of safety analysis, the EPA stated in the Benzene NESHAP
that: ``EPA believes the relative weight of the many factors that can
be considered in selecting an ample margin of safety can only be
determined for each specific source category. This occurs mainly
because technological and economic factors (along with the health-
related factors) vary from source category to source category.'' Id. at
38061. We also consider the uncertainties associated with the various
risk analyses, as discussed earlier in this preamble, in our
determinations of acceptability and ample margin of safety.
The EPA notes that it has not considered certain health information
to date in making residual risk determinations. At this time, we do not
attempt to quantify those HAP risks that may be associated with
emissions from other facilities that do not include the source
categories in question, mobile source emissions, natural source
emissions, persistent environmental pollution, or atmospheric
transformation in the vicinity of the sources in these categories.
The Agency understands the potential importance of considering an
individual's total exposure to HAPs in addition to considering exposure
to HAP emissions from the source category and facility. We recognize
that such consideration may be particularly important when assessing
non-cancer risks, where pollutant-specific exposure health reference
levels (e.g., RfCs) are based on the assumption that thresholds exist
for adverse health effects. For example, the Agency recognizes that,
although exposures attributable to emissions from a source category or
facility alone may not indicate the potential for increased risk of
adverse non-cancer health effects in a population, the exposures
resulting from emissions from the facility in combination with
emissions from all of the other sources (e.g., other facilities) to
which an individual is exposed may be sufficient to result in increased
risk of adverse non-cancer health effects. In May 2010, the SAB advised
the EPA ``that RTR assessments will be most useful to decision makers
and communities if results are presented in the broader context of
aggregate and cumulative risks, including background concentrations and
contributions from other sources in the area.'' \32\
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\32\ The EPA's responses to this and all other key
recomendations of the SAB's advisory on RTR risk assessment
methodologies (which is available at: https://yosemite.epa.gov/sab/
sabproduct.nsf/4AB3966E263D943A8525771F00668381/$File/EPA-SAB-10-
007-unsigned.pdf) are outlined in a memorandum to this rulemaking
docket from David Guinnup titled, EPA's Actions in Response to the
Key Recommendations of the SAB Review of RTR Risk Assessment
Methodologies.
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In response to the SAB recommendations, the EPA is incorporating
cumulative risk analyses into its RTR risk assessments, including those
reflected in this proposal. The Agency is: (1) Conducting facility-wide
assessments, which include source category emission points as well as
other emission points within the facilities; (2) considering sources in
the same category whose emissions result in exposures to the same
individuals; and (3) for some persistent and bioaccumlative pollutants,
analyzing the ingestion route of exposure. In addition, the RTR risk
assessments have always considered aggregate cancer risk from all
carcinogens and aggregate non-cancer HI from all non-carcinogens
affecting the same target organ system.
Although we are interested in placing source category and facility-
wide HAP risks in the context of total HAP risks from all sources
combined in the vicinity of each source, we are concerned about the
uncertainties of doing so. Because of the contribution to total HAP
risk from emission sources other than those that we have studied in
depth during this RTR review, such estimates of total HAP risks would
have significantly greater associated uncertainties than the source
category or facility-wide estimates. Such aggregate or cumulative
assessments would compound those uncertainties, making the assessments
too unreliable.
C. How did we perform the technology review?
Our technology review focused on the identification and evaluation
of developments in practices, processes, and control technologies that
have occurred since the MACT standards were promulgated. Where we
identified such developments, in order to inform
[[Page 97066]]
our decision of whether it is ``necessary'' to revise the emissions
standards, we analyzed the technical feasibility of applying these
developments and the estimated costs, energy implications, non-air
environmental impacts, as well as considering the emission reductions.
We also considered the appropriateness of applying controls to new
sources versus retrofitting existing sources.
Based on our analyses of the available data and information, we
identified potential developments in practices, processes, and control
technologies. For this exercise, a ``development'' was considered to be
any of the following that was not considered during the development of
the promulgated subpart MM standards that could result in significant
additional reductions of regulated HAP emissions:
Add-on control technology or other equipment not
previously identified;
Improvements in add-on control technology or other
equipment;
Work practices or operational procedures that were not
previously identified;
Process change or pollution prevention alternative that
could be broadly applied to further reduce HAP emissions; and
Improvements in work practices, operational procedures,
process changes, or pollution prevention alternatives.
In addition to reviewing the practices, processes, and control
technologies that were considered at the time we originally developed
the NESHAP, we reviewed a variety of data sources in our investigation
of potential practices, processes, or controls to consider. Among the
sources we reviewed were the practices, processes and control
technologies considered in the NESHAP for various industries that were
promulgated since the MACT standards being reviewed in this action. We
requested information from facilities regarding developments in
practices, processes or control technology through Part III of the Pulp
and Paper Sector ICR. The ICR data provided information on the process
and emission controls currently in use on chemical recovery combustion
sources, and provided emissions data to assess the performance of
current emissions controls. We reviewed continuous opacity monitoring
data for ESP-controlled recovery furnaces and lime kilns. We also
consulted the EPA's RBLC to determine whether it contained any
practices, processes or control technologies for the types of processes
covered by the 40 CFR part 63, subpart MM source category.\33\ We
conducted a general search of the Internet for information on control
technologies applicable to pulp mill combustion sources. We also
reviewed information from other sources, such as state and/or local
permitting agency databases.
---------------------------------------------------------------------------
\33\ See the memorandum in the docket titled, Summary of RBLC
and Other Findings to Suppport the Residual Risk and Technology
Review of Chemical Recovery Combustion Sources NESHAP.
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Each of the evaluations listed above considered and reviewed the
technologies suitable to demonstrate compliance with the requirements
listed in 40 CFR 63.860 through 63.868 (subpart MM).\34\
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\34\ See the memorandum in the docket titled, Section 112(d)(6)
Technology Review fo the NESHAP for Chemical Recovery Combustion
Sourcces at Kraft, Soda, Sulfite, and Stand-Alone Semichemical Pulp
Mills.
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IV. Analytical Results and Proposed Decisions
A. What are the results of the risk assessment and analyses?
1. Inhalation Risk Assessment Results
The inhalation risk modeling performed to estimate risks based on
actual and allowable emissions relied primarily on emissions data from
the ICR. The results of the chronic baseline inhalation cancer risk
assessment indicate that, based on estimates of current actual and
allowable emissions under 40 CFR part 63, subpart MM, the MIR posed by
the MACT source category was 4-in-1 million. The total estimated cancer
incidence from the MACT source category based on actual emission levels
is 0.01 excess cancer cases per year, or 1 case every 100 years, while
the cancer incidence for allowable emissions is 0.02 excess cancer
cases per year, or 1 case every 50 years. Air emissions of chromium VI,
formaldehyde, and naphthalene contributed 31 percent, 18 percent, and
13 percent, respectively, to this cancer incidence. We estimated
approximately 7,600 people to have cancer risks greater than or equal
to 1-in-1 million considering actual and allowable emissions from
subpart MM sources, refer to Table 3.
Table 3--Inhalation Risk Assessment Summary for Pulp Mill Combustion Sources Source Category--(Subpart MM)
--------------------------------------------------------------------------------------------------------------------------------------------------------
Cancer MIR (in-1 million) Population
---------------------------------------- Cancer Population with risk of Max chronic Max chronic
incidence with risk of 1- 10-in-1 noncancer HI noncancer HI
Based on actual Based on allowable (cases per in-1 million million or (actuals) (allowables)
emissions emissions year) or more more
--------------------------------------------------------------------------------------------------------------------------------------------------------
Source Category................. 4 (naphthalene, 4 (naphthalene, 0.01 7,600 0 HI < 1 HI < 1
acetaldehyde). acetaldehyde).
Whole Facility.................. 20 (arsenic, .................. 0.05 440,000 280 HI = 1 HI = 1
chromium VI).
--------------------------------------------------------------------------------------------------------------------------------------------------------
We estimated the maximum modeled chronic non-cancer HI (TOSHI)
value for the source category based on actual and allowable emissions
to be 0.3, with acrolein emissions from lime kilns accounting for 92
percent of the HI.
2. Acute Risk Results
Our screening analysis for worst-case acute impacts based on actual
emissions did not identify impacts associated with any pollutants that
exceeded an HQ value of 1 based upon the REL. For the acute risk
screening analysis, we calculated acute hourly multipliers based on the
median of peak-to-mean ratio for 14 emission process groups ranging
from 1.3 to 4.7, with emissions from the semichemical recovery process
having the highest hourly peak emissions with a multiplier of 4.7. For
more information on how we calculated the acute hourly multipliers,
refer to the
[[Page 97067]]
risk document, Appendix 1, Preparation of Residual Risk Modeling Input
File for Subpart MM dated September 30, 2014.
3. Multipathway Risk Screening Results
Results of the worst-case Tier 1 screening analysis identified
emissions (based on estimates of actual emissions) exceeding the PB-HAP
emission cancer screening rates for dioxin/furans and polycyclic
aromatic hydrocarbons (PAH) and the non-cancer screening threshold for
mercury. For the compounds and facilities that did not screen out at
Tier 1, we conducted a Tier 2 screen. The Tier 2 screen replaces some
of the assumptions used in Tier 1 with site-specific data, including
the location of fishable lakes and local precipitation, wind direction
and speed. The Tier 2 screen continues to rely on high-end assumptions
about consumption of local fish and locally grown or raised foods
(adult female angler at 99th percentile consumption for fish for the
subsistence fisherman scenario and 90th percentile consumption for
locally grown or raised foods for the farmer scenario). For facilities
for which the Tier 2 screening value(s) indicate a potential health
risk to the public, we can conduct a Tier 3 multipathway screen. Tier 3
has three individual stages: (1) Lake assessment to assess fishability
and accessibility; (2) plume-rise calculations to estimate the
emissions exiting the mixing layer and resulting in no ground-level
exposures; (3) TRIMFaTE hourly screening runs using the layout for the
farm and/or fish location that best characterizes the facility being
modeled. We progress through Tier 3 stages until the facility's
screening values indicate that emissions are unlikely to pose health
risks to the public, or until all three stages are complete. A Tier 3
screen was required for one facility that exceeded the Tier 2 screen
for mercury. It is important to note that, even with the inclusion of
some site-specific information in the Tier 2 and 3 analysis, the
multipathway screening analysis is still a very conservative, health-
protective assessment (i.e., upper-bound consumption of local fish and
locally grown and/or raised foods) and in all likelihood yields results
that serve as an upper-bound multipathway risk associated with a
facility.
While the screening analysis is not designed to produce a
quantitative risk result, the factor by which the emissions exceed the
threshold serves as a rough gauge of the ``upper-limit'' risks we would
expect from a facility. Thus, for example, if a facility emitted a PB-
HAP carcinogen at a level 2 times the screening threshold, we can say
with a high degree of confidence that the actual maximum cancer risks
will be less than 2-in-1 million. Likewise, if a facility emitted a
noncancer PB-HAP at a level 2 times the screening threshold, the
maximum noncancer hazard would represent an HQ less than 2. The high
degree of confidence comes from the fact that the screens are developed
using the very conservative (health-protective) assumptions that we
describe above.
a. Cancer Risk Screening
Results of the worst-case Tier 1 screening analysis indicate that
85 of the 108 facilities with pulp mill combustion sources exceeded the
PB-HAP emission cancer screening rates (based on estimates of actual
emissions) for dioxin/furans and PAH. The EPA conducted a Tier 2 cancer
screening analysis of the 85 facilities that were found to exceed the
Tier 1 screening value. Nineteen of these facilities with subpart MM
MACT source category sources emitted dioxin/furans and PAH above a
cancer screening value of 1 for the subsistence fisher and farmer
scenarios. In the Tier 2 analysis, the individual dioxin/furan congener
emissions are all scaled based on their toxicity relative to 2,3,7,8-
tetrachlorodibenzo-p-dioxin and are reported as toxic equivalents
(TEQs), and all PAH congener emissions are scaled based on their
toxicity relative to benzo(a)pyrene and are reported as TEQs. The
maximum Tier 2 cancer screening value for the subsistence fisher
scenario and the farmer scenario for this source category was equal to
10, which represents a maximum cancer risks that would be less than 10-
in-1 million. The EPA did not conduct further cancer screening for this
source category and considered this result along with all the risk
results as part of determining whether the risks are acceptable (as
discussed in section B).
b. Non-Cancer Risk Screening
Results of the worst-case Tier 1 screening analysis indicate that
59 of the 108 plants sources exceeded the Tier 1 non-cancer screen
value for mercury. The EPA conducted a Tier 2 chronic non-cancer
screening analysis of the 59 facilities, resulting in 9 facilities
emitting divalent mercury above the non-cancer screening value of 1 for
the subsistence fisher scenario. The highest exceedance of the Tier 2
non-cancer mercury screen value for pulp mill combustion sources under
40 CFR part 63, subpart MM was equal to 5. The risk associated with
divalent mercury is based on its ability to transform into the most
toxic form of mercury as methyl mercury.
The Tier 2 non-cancer screening analysis for the 9 facilities
indicated potential risks greater than or equal to 2 but less than 5
times the non-cancer screening level for the subsistence fisher
scenario. More refined screening using Tier 3 was conducted for the 9
facilities flagged in Tier 2. The Tier 3 screen examined the set of
lakes from which the fisher might ingest fish (Stage 1). Any lakes that
appeared to not be fishable or not publicly accessible were removed
from the assessment, and the screening assessment was repeated. After
we made the determination that the critical lakes were fishable, we
analyzed plume rise data for each of the sites (Stage 2). The results
of the Tier 3 screen (Stage 2) showed one facility with a non-cancer
screen value of 2.
We conducted the final screening stage of Tier 3 for this single
facility utilizing a time-series assessment (Stage 3). In this stage,
we conducted a new mercury run using TRIM.FaTE for each relevant lake
that represents a risk concern based upon the Tier 3 plume-rise
assessment. For these model runs, we started with the screening
configuration corresponding to the lake location, but instead of the
static meteorology and stack parameters used in previous screening
tiers and stages, we used site-specific hourly meteorology and the
hourly plume-rise values calculated in the Tier 3 plume-rise
assessment. Allowing TRIM.FaTE to model chemical fate and transport
with hour-by-hour changes in meteorology and plume rise produces a more
accurate estimate of chemical concentrations in media of interest, as
compared to the static values used in Tier 2 and the post-processing
adjustments made in the Tier 3 plume-rise assessment. If the potential
risk (estimated using this Tier 3 time-series approach) associated with
a facility's PB-HAP emissions are lower than the screening value, we
consider the emissions to pose no significant risk. This Tier 3 screen
resulted in lowering the maximum exceedance of the screen value for the
highest site from 2 to 1. Further details on the refined multipathway
screening analysis are in Appendix 10, Attachment 1 of the risk report,
``Residual Risk Assessment for Pulp Mill Combustion Sources in Support
of the December 2016 Risk and Technology Review Proposed Rule''.
4. Environmental Risk Screening Results
As described in section III.A of this document, we conducted an
environmental risk screening assessment for the 40 CFR part 63, subpart
MM source category for the following seven HAPs: PAH, mercury
[[Page 97068]]
(methyl mercury and mercuric chloride), cadmium, lead, dioxin/furans,
HCl, and HF.
In the Tier 1 screening analysis for PB-HAPs (other than lead,
which we evaluated differently), one modeled soil parcel for one
facility in the source category exceeded a surface soil--threshold
level benchmark (invertebrates) for mercuric chloride by 2. There were
no Tier 1 exceedances of any benchmarks for the other pollutants; PAH,
cadmium and dioxins/furans. Therefore, we conducted a Tier 2 screen for
mercuric chloride only. In the Tier 2 screen for mercuric chloride,
none of the individual modeled concentrations for any facility in the
source category exceeded any of the ecological benchmarks.
For lead, we did not estimate any exceedances of the secondary lead
NAAQS. For HCl and HF, the average modeled concentration around each
facility (i.e., the average concentration of all off-site data points
in the modeling domain) did not exceed any ecological benchmark. In
addition, each individual modeled concentration of HCl and HF (i.e.,
each off-site data point in the modeling domain) was below the
ecological benchmarks for all facilities.
5. Facility-Wide Risk Results
Considering facility-wide emissions at the 108 plants, we estimated
the MIR to be 20-in-1 million driven by arsenic and chromium VI
emissions, and calculated the chronic non-cancer TOSHI value to be 1
driven by emissions of acrolein (refer to Table 3). The above cancer
and non-cancer risks are driven by emissions from the industrial
boilers.
We estimated approximately 440,000 people to have cancer risks
greater than or equal to 1-in-1 million considering whole facility
emissions from 81 of the 108 facilities modeled from the pulp and paper
production industry (refer to Table 3). From these 81, 2 facilities
have cancer risks greater than or equal to 10-in-1 million (but less
than 20-in-1 million) with approximately 300 being exposed at these
levels.
6. What demographic groups might benefit from this regulation?
To determine whether or not to conduct a demographics analysis,
which is an assessment of risks to individual demographic groups, we
look at a combination of factors, including the MIR, non-cancer TOSHI,
population around the facilities in the source category, and other
relevant factors. For the 40 CFR part 63, subpart MM source category,
we examined the potential for any environmental justice (EJ) issues
that might be associated with the source category, by performing a
demographic analysis of the population close to the facilities. In this
analysis, we evaluated the distribution of HAP-related cancer and non-
cancer risks from the subpart MM source category across different
social, demographic, and economic groups within the populations living
near facilities identified as having the highest risks. The methodology
and the results of the demographic analyses are included in a technical
report, Risk and Technology Review--Analysis of Socio-Economic Factors
For Populations Living Near Pulp Mill Combustion Sources, available in
the docket for this action.
The results of the demographic analysis are summarized in Table 4
below. These results, for various demographic groups, are based on the
estimated risks from actual emissions levels for the population living
within 50 km of the facilities.
Table 4--Subpart MM Source Category Demographic Risk Analysis Results
----------------------------------------------------------------------------------------------------------------
Population
with cancer Population
Nationwide risk at or with chronic
above 1-in-1 hazard index
million above 1
----------------------------------------------------------------------------------------------------------------
Total Population................................................ 312,861,265 7,600 0
----------------------------------------------------------------------------------------------------------------
Race by Percent
----------------------------------------------------------------------------------------------------------------
White........................................................... 72 67 0
All Other Races................................................. 28 33 0
----------------------------------------------------------------------------------------------------------------
Race by Percent
----------------------------------------------------------------------------------------------------------------
White........................................................... 72 67 0
African American................................................ 13 28 0
Native American................................................. 1.1 0.4 0
Other and Multiracial........................................... 14 5 0
----------------------------------------------------------------------------------------------------------------
Ethnicity by Percent
----------------------------------------------------------------------------------------------------------------
Hispanic........................................................ 17 3 0
Non-Hispanic.................................................... 83 97 0
----------------------------------------------------------------------------------------------------------------
Income by Percent
----------------------------------------------------------------------------------------------------------------
Below Poverty Level............................................. 14 16 0
Above Poverty Level............................................. 86 84 0
----------------------------------------------------------------------------------------------------------------
Education by Percent
----------------------------------------------------------------------------------------------------------------
Over age 25 and without High School Diploma..................... 15 18 0
Over age 25 and with a High School Diploma...................... 85 82 0
----------------------------------------------------------------------------------------------------------------
The results of the 40 CFR part 63, subpart MM source category
demographic analysis indicate that emissions from the source category
expose approximately 7,600 people to a cancer risk at or above 1-in-1
million
[[Page 97069]]
and no one exposed to a chronic non-cancer TOSHI greater than 1. The
specific demographic results indicate that the percentage of the
population potentially impacted by emissions is greater than its
corresponding national percentage for the minority population (33
percent for the source category compared to 28 percent nationwide), the
African American population (28 percent for the source category
compared to 13 percent nationwide) and for the population over age 25
without a high school diploma (18 percent for the source category
compared to 15 percent nationwide). The proximity results (irrespective
of risk) indicate that the population percentages for certain
demographic categories within 5 km of source category emissions are
greater than the corresponding national percentage for those same
demographics. The following demographic percentages for populations
residing within close proximity to facilities with chemical recovery
combustion sources are higher than the corresponding nationwide
percentage: African American, ages 65 and up, over age 25 without a
high school diploma, and below the poverty level.
The risks due to HAP emissions from this source category are low
for all populations (e.g., inhalation cancer risks are less than 4-in-1
million for all populations and non-cancer hazard indices are less than
1). Furthermore, we do not expect this proposal to achieve significant
reductions in HAP emissions. Section IV.C of this preamble addresses
opportunities as part of the technology review to further reduce HAP
emissions. These technologies were found not to be cost-effective.
Therefore, we conclude that this proposal 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. However, this proposal, if finalized, will provide
additional benefits to these demographic groups by improving the
compliance, monitoring, and implementation of the NESHAP.
B. What are our proposed decisions regarding risk acceptability, ample
margin of safety, and adverse environmental effects?
1. Risk Acceptability
As noted in section II.A of this preamble, the EPA sets standards
under CAA section 112(f)(2) using ``a two-step standard-setting
approach, with an analytical first step to determine an 'acceptable
risk' that considers all health information, including risk estimation
uncertainty, and includes a presumptive limit on MIR of approximately
1-in-10 thousand.'' (54 FR 38045, September 14, 1989).
In this proposal, the EPA estimated risks based on both actual and
allowable emissions from pulp mill combustion sources. As discussed
above, in determining acceptability, we considered risks based on both
actual and allowable emissions. Based on the risk assessment results
described above, the EPA is proposing that the risks are acceptable.
The baseline inhalation cancer risk from the source category was 4-
in-1-million for the most exposed individual based on actual and
allowable emissions. The total estimated incidence of cancer for this
source category due to inhalation exposures is 0.02 excess cancer cases
per year, or 1 case in 50 years. The Agency estimates that the maximum
chronic non-cancer TOSHI from inhalation exposure for this source
category has an HI equal to 0.3 based upon both actual and allowable
emissions. Lime kilns account for a large portion (92 percent) of the
HI.
The multipathway screening analysis, based upon actual emissions,
indicates the excess cancer risk from this source category is less than
10-in-1 million based on dioxins/furans and PAH emissions, with PAH
emissions accounting for 99 percent of these potential risks from the
fisher and the farmer scenarios. There were no facilities within this
source category with a multipathway non-cancer screen value greater
than 1 for cadmium or mercury. In evaluating the potential for
multipathway effects from emissions of lead, we compared modeled
maximum annual lead concentrations to the secondary NAAQS for lead
(0.15 [mu]g/m3). Results of this analysis estimate that the NAAQS for
lead would not be exceeded at any off-site locations.
To put the risks from the source category in context, we also
evaluated facility-wide risk. Our facility-wide assessment, based on
actual emissions, estimated the MIR to be 20-in-1 million driven by
arsenic and chromium VI emissions, and estimated the chronic non-cancer
TOSHI value to be 1 driven by emissions of acrolein. We estimated
approximately 440,000 people to have cancer risks greater than or equal
to 1-in-1 million considering facility-wide emissions from the pulp and
paper production industry (see Table 3). The above cancer and non-
cancer risks are driven by emissions from industrial boilers,
representing 62 percent of the cancer risks and 95 percent of the non-
cancer risks. Emissions from the 40 CFR part 63, subpart MM sources
represent only 6 percent of the total facility-wide cancer risk of 20-
in-1 million.
The screening assessment of worst-case acute inhalation impacts
indicates no pollutants exceeding an HQ value of 1 based on the REL,
with an estimated worst-case maximum acute HQ of 0.3 for acrolein based
on the 1-hour REL.
A review of the uncertainties in the risk assessment identified one
additional key consideration, and that is the quality of data
associated with the whole-facility emissions. The data provided from
the power boilers were collected in 2009 and represent pre-MACT
emissions before any controls. The uncertainty introduced by using pre-
MACT boiler emissions data may result in an overestimated risk estimate
for the whole-facility analysis for both cancer and non-cancer impacts.
Considering all of the available health risk information, we
propose that risks from the source category are acceptable.
2. Ample Margin of Safety Analysis
As directed by section 112(f)(2), we conducted an additional
analysis to determine whether additional standards are needed to
provide an ample margin of safety to protect public health. Under this
ample margin of safety analysis, we evaluated the cost and feasibility
of available control technologies and other measures that could be
applied in this source category to further reduce the risks (or
potential risks) due to emissions of HAPs identified in our risk
assessment, along with all of the health risks and other health
information considered in our determination of risk acceptability.
Although we are proposing that the risks from the subpart MM source
category are acceptable, inhalation risk estimates are above 1-in-1
million at the actual and MACT-allowable emission levels for
approximately 7,600 individuals in the exposed population. The HAP risk
drivers contributing to the inhalation risks in excess of 1-in-1
million include primarily the gaseous organic HAPs acetaldehyde and
naphthalene. Additional gaseous organic HAPs contributing to the risk
includes benzene, chloroprene, formaldehyde, 2-methylnaphthalene, 7,12-
dimethylbenz[a]anthracene, acenaphthene, acenaphthylene, and
fluoranthene. More than 80-percent of the mass emissions of these
compounds originate from NDCE recovery furnaces, and DCE recovery
furnaces (including BLO systems). We considered options for further
reducing gaseous organic HAP emissions from NDCE and DCE
[[Page 97070]]
recovery furnaces. The greatest reduction in gaseous organic HAP
emissions that could be achieved for DCE recovery furnaces would result
from DCE-to-NDCE furnace conversions or replacements of DCE furnaces
with NDCE systems. We estimated furnace emissions to be reduced when a
DCE furnace is converted (or replaced with NDCE design). Conversion or
replacement of a DCE system with an NDCE system results in removal of
the BLO system and elimination of 100 percent of the BLO emissions. For
NDCE recovery furnaces with wet ESP systems, conversion of the wet ESP
system to a dry system can further reduce gaseous organic HAPs. Section
IV.C.1 of this preamble discusses the costs and impacts associated with
DCE conversions (or replacements) and wet-to-dry ESP conversions for
NDCE recovery furnaces. The overall cost of these options is an
estimated $1.4 billion to $3.7 billion in capital cost and $120 million
to $440 million in annualized cost. Application of this option would
achieve an estimated emission reduction of 2,920 tpy of gaseous organic
HAPs (including risk drivers and other gaseous organic HAPs), and the
corresponding cost-effectiveness ranges from $45,000 to $153,000 per
ton of emissions reduced. The non-air environmental impacts, energy
impacts, and secondary air emissions associated with the options
described above are discussed in a memorandum in the docket. Due to the
low level of current risk and the substantial costs associated with
these options, we are proposing that additional emission reductions
from the source category are not necessary to provide an ample margin
of safety.
3. Adverse Environmental Effects
Based on the results of our environmental risk screening
assessment, we propose to conclude that there is not an adverse
environmental effect as a result of HAP emissions from the 40 CFR part
63, subpart MM source category.\35\ Thus, we are proposing that it is
not necessary to set a more stringent standard to prevent an adverse
environmental effect.
---------------------------------------------------------------------------
\35\ The environmental screening analysis is documented in
Residual Risk Assessment for Pulp Mill Combustion Sources in Support
of the December 2016 Risk and Technology Review Proposed Rule, in
the docket for this action.
---------------------------------------------------------------------------
C. What are the results and proposed decisions based on our technology
review?
1. Kraft and Soda Recovery Furnaces
The ability to recover pulping chemicals is imperative to the kraft
and soda process, and is achieved by burning spent pulping liquor
(i.e., black liquor) in a recovery furnace. The recovery furnace is
easily identified at a pulp mill because it is typically the tallest
equipment on site. The purpose of the recovery furnace is to: (1)
Recover inorganic pulping chemicals (e.g., sodium sulfide
(Na2S) and sodium hydroxide (NaOH) in kraft mills and NaOH
in soda mills); and (2) produce steam. The recovered inorganic pulping
chemicals are reused in the process, and the steam is used to generate
electricity and for process heating. Prior to being fired in the
recovery furnace, black liquor recovered from pulp washing is
concentrated using an NDCE or DCE. The NDCE is an indirect, steam-
heated black liquor concentrator. The DCE uses the hot combustion gases
exiting the furnace to increase the solids content of the black liquor.
A BLO system precedes the DCE to reduce malodorous total reduced sulfur
(TRS) emissions that can be stripped in the DCE when hot flue gases
from the recovery furnace come in contact with the black liquor. The
BLO system uses molecular oxygen (O2) or air to oxidize
Na2S to nonvolatile sodium thiosulfate
(Na2S2O3) to reduce the potential for
stripping. Outputs from recovery furnaces include molten smelt
(primarily Na2S and sodium carbonate
(Na2CO3)), flue gases, and steam. The smelt exits
from the bottom of the furnace into an SDT, where the recovery of kraft
pulping chemicals continues. Particulate matter (primarily sodium
sulfate (Na2SO4) [salt cake] and
Na2CO3) entrained in the flue gases is also
recovered using an ESP, which deposits the collected material into a
chemical ash tank or salt cake mix tank for subsequent addition into
the concentrated black liquor.
We reviewed ICR data on recovery furnace design and emissions
controls for purposes of the technology review. There are currently 148
kraft and soda recovery furnaces in the United States, including 36
existing DCE furnaces, 108 existing NDCE furnaces, and 4 recovery
furnaces subject to the new source limits under 40 CFR part 63, subpart
MM. The vast majority (96 percent) of recovery furnaces have ESP
control, including the 4 NDCE recovery furnaces subject to the new
source limits under subpart MM. Three of the DCE furnaces and one of
the NDCE furnaces have an ESP followed by a wet scrubber. Two NDCE
furnaces have a wet scrubber alone. The one remaining soda recovery
furnace is a subpart MM new source with ESP control. As we noted in
2001, when subpart MM was promulgated, we project no new DCE recovery
furnaces to be installed in the future, because more energy-efficient
NDCE technology is now prevalent.
Recovery furnace ESPs can be further characterized as wet- or dry-
bottom ESPs having either a wet or dry PM return system. A wet-bottom
ESP uses either oxidized or unoxidized black liquor to collect the PM
and carry it to the salt cake mix tank via a wet PM return system. A
dry-bottom ESP routes the captured PM to the mix tank via a screw
conveyor or drag chain without the use of liquid, typically with a dry
PM return system. However, there are some dry-bottom ESPs with a wet PM
return system that use black liquor or other process liquids to
transport the dry collected PM to the mix tank. Approximately 60
percent of recovery furnaces in the United States (or 90 recovery
furnaces) have a dry-bottom ESP with a dry PM return system (including
two furnaces with a dry-bottom ESP followed by a scrubber).
Recovery furnace gaseous organic HAP. Subpart MM of 40 CFR part 63
contains a gaseous organic HAP limit of 0.025 lb/ton BLS (measured as
methanol) for new recovery furnaces based on use of an NDCE recovery
furnace with a dry-bottom ESP and a dry PM return system. Recovery
furnace system design impacts gaseous organic HAP emissions. Non-direct
contact evaporator recovery furnaces emit less gaseous organic HAPs
because there is no contact between the incoming black liquor and hot
flue gases in the evaporator and there is no BLO system. Replacement of
DCE recovery furnace systems with a new NDCE recovery furnace or
conversion of an existing DCE furnace to an NDCE design (referred to as
a ``low-odor conversion''), along with removal of the associated BLO
system, provides the greatest reduction in gaseous organic HAP
emissions. Use of a dry-bottom ESP system with a dry PM return also
reduces gaseous organic HAP emissions.
Analysis of ICR data for our technology review revealed that the
number of DCE recovery furnaces in the United States continues to
decrease as facilities with older DCE furnaces either close or, where
feasible, replace aging DCE furnaces or convert them to NDCE systems.
When subpart MM was proposed in 1998, 39 percent of recovery furnaces
(82 units) were DCE systems. Today, only 36 DCE recovery furnaces
remain, which is 24 percent of
[[Page 97071]]
the recovery furnace population (including 2 DCE recovery furnaces that
are only used as backup systems for times when other NDCE furnaces
onsite are not operating).
We analyzed the costs and environmental impacts of replacement or
conversion of the remaining DCE recovery furnaces as part of our
technology review. High capital costs of an estimated $1.3 to $3.7
billion and annualized costs of an estimated $120 to $440 million are
associated with recovery furnace installation (or conversion) projects
due to the integral nature of the recovery furnace within the pulp mill
and the number of upstream and downstream equipment components that
must be removed, replaced, or reengineered along with the recovery
furnace itself. These costs would be borne by 21 facilities that
continue to operate DCE recovery furnaces and are not already projected
to replace these systems in the absence of any regulatory action. The
cost effectiveness of recovery furnace conversions or replacements is
also high, at an estimated $44,000 to $159,000 per ton of gaseous
organic HAPs reduced. We estimated a range of costs based on multiple
information sources.
We also considered the costs and impacts associated with converting
the remaining NDCE recovery furnace wet-bottom ESPs in the industry to
dry-bottom ESPs. Capital costs are an estimated $56.1 million for wet-
to-dry bottom ESP conversions at 11 mills with NDCE recovery furnaces,
with cost effectiveness of $54,000 per ton of gaseous organic HAPs
removed.
The total costs of the gaseous organic HAP options we considered
are an estimated $1.4 to $3.7 billion in capital cost borne by 32
facilities, to achieve an estimated emission reduction of 2,920 tpy of
gaseous organic HAP at a cost effectiveness of $45,000 to $153,000 per
ton of gaseous organic HAPs removed. Collateral TRS emission reductions
are an estimated 1,250 tpy at a cost effectiveness of $104,000 to
$357,000 per ton of TRS reduced. Given the high capital costs and high
cost per ton of emissions reduced, we are not proposing additional
regulation of recovery furnace gaseous organic HAP emissions as a
result of the technology review.
Recovery furnace PM. Under the current 40 CFR part 63, subpart MM,
PM is a surrogate for HAP metal emissions. Subpart MM requires existing
recovery furnaces to meet a PM emission limit of 0.044 grains per dry
standard cubic foot (gr/dscf) at 8 percent O2 and requires
new recovery furnaces to meet a PM limit of 0.015 gr/dscf at 8-percent
O2. We recently analyzed PM emissions test data collected
with the 2011 Pulp and Paper Sector ICR for purposes of the Kraft Pulp
Mill NSPS review promulgated on April 4, 2014 (79 FR 18952). We
reviewed the PM data tabulated for the NSPS review in the context of
the existing and new source PM limits for the subpart MM NESHAP
technology review. The dataset included more than 200 filterable PM
stack tests, including some repeat tests, on nearly all of the recovery
furnaces in the United States using a variety of PM emission controls
(ESP, ESP and wet scrubber combinations, and wet scrubbers). The PM
stack test data revealed little or no distinction between DCE and NDCE
recovery furnaces for PM emissions. Nearly all of the recovery furnaces
tested met the current existing source limit (0.044 gr/dscf),\36\ and
several met the new source limit (0.015 gr/dscf), though there was a
considerable scatter of emission test results between 0.015 and 0.044
gr/dscf, including variability in test results for the same units
tested multiple times. There was also variability in the performance of
the different types of ESP or ESP and scrubber systems such that no one
type of control system seemed to perform better than another. Based on
the data, wet scrubbing of recovery furnace exhaust gases (either alone
or in conjunction with an ESP) does not necessarily improve filterable
PM removal. After reviewing the recovery furnace PM emissions data, we
concluded that the current subpart MM emission limits of 0.044 gr/dscf
and 0.015 gr/dscf continue to represent the performance of existing and
new recovery furnaces, respectively. The technology review did not
reveal any developments in practices, processes, and control
technologies for reducing PM emissions from recovery furnaces that have
occurred since promulgation of subpart MM. Therefore, we are not
proposing any changes to the PM emission limits for purposes of the
technology review. As discussed below, we estimated incidental
incremental improvements in PM emissions as part of our analysis of the
opacity monitoring limit for recovery furnaces.
---------------------------------------------------------------------------
\36\ Exceptions included a few stack tests that were repeated,
or recovery furnaces that participate in the PM bubble compliance
option under 40 CFR part 63, subpart MM.
---------------------------------------------------------------------------
2. Kraft and Soda Lime Kilns
In kraft and soda pulp mills, the lime kiln is part of the
causticizing process in which green liquor from the SDT is converted to
white liquor. The function of the lime kiln is to oxidize lime mud
(calcium carbonate, CaCO3) to reburned lime (calcium oxide,
CaO) in a process known as calcining. Lime kiln air pollution control
devices include wet scrubbers, ESPs, or a combination system including
an ESP followed by a wet scrubber. The 2011 ICR data indicate that, of
130 lime kilns in the United States, 89 kilns have wet scrubbers, 30
kilns have ESPs, and 11 kilns have ESP-wet scrubber combinations.
Subpart MM, 40 CFR part 63, includes a PM limit of 0.064 gr/dscf at
10-percent O2 (which is a surrogate limit for HAP metals)
for existing lime kilns. For new or reconstructed lime kilns, the
subpart MM limit is 0.010 gr/dscf at 10-percent O2 based on
use of a high-efficiency ESP. Subpart MM does not distinguish between
fuel types. Lime kilns typically burn natural gas, fuel oil, petroleum
coke, or a combination of these fuels. They may also burn
noncondensable gases (NCGs) or pulp mill byproducts such as tall oil.
The EPA recently reviewed PM stack test data from more than 250
filterable PM stack tests (including several repeat tests) on 110 lime
kilns in the United States for purposes of the Kraft Pulp Mill NSPS
review. The EPA interpreted this same dataset in the context of
conducting the technology review of the subpart MM PM limits for lime
kilns. The tests included lime kilns with scrubbers, ESPs and ESP-wet
scrubber combination controls. Most of the scrubber-controlled kilns
achieved the subpart MM existing source limit (0.064 gr/dscf at 10-
percent O2) with the exception of kilns that participate in
the PM bubble compliance alternative. The data suggested that scrubber-
controlled kilns would not be expected to meet the subpart MM new
source limit of 0.010 gr/dscf at 10-percent O2. The EPA
found that ESP and ESP-wet scrubber controls typically reduce PM to
lower levels than wet scrubbers alone. The ESP-wet scrubber systems did
not necessarily perform better on filterable PM than the ESPs alone.
Several existing ESP and ESP-wet scrubber controlled kilns consistently
met the 0.064 gr/dscf existing source limit, and often met the new
source limit of 0.010 gr/dscf at 10-percent O2. The EPA
observed test results between the existing and new source limit for
existing sources with ESP and ESP-wet scrubber systems. Our review of
the PM emissions test data for lime kilns suggests that the subpart MM
limits for lime kilns are appropriate. For purposes of the subpart MM
technology review, the EPA has identified no practices, processes, or
controls for PM emissions from lime kilns beyond those
[[Page 97072]]
identified when subpart MM was developed. Therefore, the EPA is not
proposing any changes to the existing PM limits of 0.064 gr/dscf at 10-
percent O2 for existing lime kilns and 0.010 gr/dscf at 10-
percent O2 for new and reconstructed lime kilns.
3. Recovery Furnace and Lime Kiln Monitoring
This subsection discusses our review of the opacity and ESP
monitoring provisions for recovery furnaces and lime kilns with ESPs or
combined ESP and wet scrubber systems.
Continuous opacity monitoring. Subpart MM of 40 CFR part 63
requires continuous monitoring of opacity to demonstrate ongoing
compliance with the PM concentration limits for ESP-controlled recovery
furnaces and lime kilns. The current PM opacity limits under subpart MM
are 35-percent opacity for existing recovery furnaces and 20-percent
opacity for existing lime kilns, new lime kilns, and new recovery
furnaces. Subpart MM contains an opacity monitoring allowance for
existing sources where 6 percent of the 6-minute opacity averages
during a quarter (excluding periods of SSM and periods when the
facility is not operating) may exceed the 35-percent recovery furnace
or 20-percent lime kiln opacity limit without being considered a
violation. Subpart MM currently contains a corrective action threshold
of 10 consecutive 6-minute averages above 20-percent opacity for new
and existing recovery furnaces and lime kilns.
The EPA reviewed recovery furnace and lime kiln continuous opacity
monitoring system (COMS) data for purposes of the technology review to
evaluate the current 40 CFR part 63, subpart MM opacity limits and 6-
percent monitoring allowance. The EPA performed a similar review of the
COMS data for the subpart BBa NSPS review promulgated April 4, 2014 (79
FR 18952). The EPA's analysis of the recovery furnace COMS data for
subpart MM is included in a memorandum in the docket.\37\ Our
conclusions from reviewing the opacity data in the context of subpart
MM are consistent with the conclusions reached for the 2014 NSPS
review.
---------------------------------------------------------------------------
\37\ See memorandum titled, Review of the Continuous Opacity
Monitoring Data from the Pulp and Paper ICR Responses for Subpart MM
Sources, in the docket.
---------------------------------------------------------------------------
The COMS data for 135 recovery furnaces show that the majority of
existing recovery furnaces, regardless of design (DCE or NDCE), and
with most controls, are meeting a 20-percent opacity limit based on a
6-minute average, with fewer than 2 percent of averaging periods
exceeding 20-percent opacity, including periods of startup and
shutdown. The EPA also reviewed state permits and found many recovery
furnaces with permit limits of 20-percent opacity. Therefore, the EPA
concludes that this information is evidence that there has been a
development in existing recovery furnace operating practices that
supports reducing the existing source opacity limit from 35-percent to
20-percent and revising the monitoring allowance for the 20-percent
opacity limit from 6 percent to a 2-percent monitoring allowance as
part of the 40 CFR part 63, subpart MM technology review process.
The COMS data for 28 ESP-controlled lime kilns show that all of the
existing lime kilns are meeting the 20-percent opacity limit based on a
6-minute average, with nearly all performing at a 1-percent monitoring
allowance, including periods of startup and shutdown. The EPA considers
this information as evidence that there has been a development in
existing lime kiln operating practices and that this development
supports revising the monitoring allowance from 6 percent to a 1-
percent monitoring allowance for opacity as part of the 40 CFR part 63,
subpart MM technology review process.
Subpart MM of 40 CFR part 63 currently requires that the opacity
allowance be calculated based on the percent of the operating time in a
quarter in which excess emissions are recorded. The Agency is proposing
to change the reporting requirement frequency, as discussed in section
IV.D.4, and, therefore, analyzed both quarterly and semiannual
averaging periods when reviewing the proposed monitoring allowance
discussed above.
The EPA considered the impacts of various opacity monitoring
options as part of the technology review. The opacity regulatory
options considered for kraft and soda recovery furnaces were:
Baseline Option 1: 35-percent opacity (existing) or 20-percent
opacity (new), 20-percent corrective action level, 6-percent monitoring
allowance, quarterly reporting.
Option 2: 35-percent opacity, 20-percent corrective action level,
2-percent monitoring allowance, semiannual reporting.
Option 3: 20-percent opacity, 6-percent monitoring allowance,
quarterly reporting.
Option 4: 20-percent opacity, 2-percent monitoring allowance,
semiannual reporting.
Option 5: 20-percent opacity, 2-percent monitoring allowance,
quarterly reporting.
The opacity regulatory options considered for kraft and soda ESP-
controlled lime kilns were:
Baseline Option 1: 20-percent opacity and corrective action level
with 6-percent allowance, quarterly reporting.
Option 2: 20-percent opacity with a 1-percent monitoring allowance,
semiannual reporting.
Option 3: 20-percent opacity with a 1-percent monitoring allowance,
quarterly reporting.
For purposes of estimating costs and impacts of the regulatory
options, we assumed that recovery furnaces and ESP-controlled lime
kilns that did not meet the regulatory options in our COMS analysis
would require ESP maintenance and testing to improve opacity
performance, or an ESP upgrade. The EPA also reviewed PM performance
levels (based on PM stack test data) for emission units not meeting the
opacity limits under consideration in at least one reporting period. If
the PM performance level achieved met the PM performance expected from
an upgraded ESP (0.015 gr/dscf at 8-percent O2 for recovery
furnaces or 0.010 gr/dscf at 10-percent O2 for lime kilns),
then we assumed that the ESP would only require improved annual
maintenance and testing to achieve the opacity options. Otherwise, we
assumed that units would require an ESP upgrade to meet the opacity
options.
Although we are not proposing any changes to the PM metal HAP
limits as part of the technology review, ESP upgrades to meet a tighter
opacity monitoring limit would have the effect of reducing PM
emissions. We estimated recovery furnace upgrade costs for adding two
parallel fields to an existing ESP resulting in a PM performance level
of 0.015 gr/dscf at 8-percent O2. For lime kilns, we
estimated costs based on adding one field to the existing ESP to
achieve a PM performance level of 0.01 gr/dscf at 10-percent
O2. For each emission unit expected to require an ESP
upgrade, we estimated the potential reduction in PM emissions by
subtracting the PM limit expected to be achieved by the upgraded ESP
from the lower of the current PM permit limit or the actual PM
performance level for the emission unit.
The EPA's full analysis of the cost and impacts associated with the
regulatory options for opacity (including energy and secondary air
impacts) is presented
[[Page 97073]]
in a memorandum in the docket.\38\ Table 5 summarizes the number of
impacted facilities, estimated cost, PM reductions, and cost
effectiveness of the opacity regulatory options.
---------------------------------------------------------------------------
\38\ See memorandum titled, Costs/Impacts of the Subpart MM
Residual Risk and Technology Review, in the docket.
Table 5--Costs and Impacts of Opacity Regulatory Options
--------------------------------------------------------------------------------------------------------------------------------------------------------
2015$
-------------------------------- Cost
Option Number of Annualized Incremental HAP reduction, tpy effectiveness
mills impacted Capital costs, costs, $/ton PM\1\
$million $million/yr
--------------------------------------------------------------------------------------------------------------------------------------------------------
Recovery Furnaces Opacity Monitoring Limit Options
--------------------------------------------------------------------------------------------------------------------------------------------------------
Baseline Option 1: No change. 35% opacity, 0 0 0 0........................................... NA
20% corrective action level (CAL), 6%
monitoring allowance (MA), quarterly (Q)
reporting.
Option 2: 35% opacity, 20% CAL, 2% MA, 1 0 0.087 0........................................... NA
semiannual (SA) reporting.
Option 3: 20% opacity, 6% MA, Q reporting. 7 27 5.4 188 (PM), 85 (PM2.5)........................ 28,400
Option 4: 20% opacity, 2% MA, SA reporting 12 42 8.7 235 (PM), 112 (PM2.5)....................... 36,800
Option 5: 20% opacity, 2% MA, Q reporting. 19 74 15 364 (PM), 170 (PM2.5)....................... 41,000
--------------------------------------------------------------------------------------------------------------------------------------------------------
Lime Kiln Opacity Monitoring Limit Options
--------------------------------------------------------------------------------------------------------------------------------------------------------
Option 1: No change. 20% opacity, 6% MA, Q 0 0 0 0........................................... NA
reporting.
Option 2: 20% opacity, 1% MA, SA reporting 2 0 0.068 0........................................... NA
-------------------------------------------------------------------------------------------------------------
Option 3: 20% opacity, 1% MA, Q reporting. Same as option 2
--------------------------------------------------------------------------------------------------------------------------------------------------------
\1\ HAP metals comprise less than 0.5-percent of the PM emissions (0.03-percent for recovery furnaces or 0.48-percent for lime kilns). Thus, the cost
effectiveness specifically for HAP metals is orders of magnitude greater than that shown for PM (>$5.5 million per ton HAP metals).
After considering the costs and impacts of the regulatory options
for opacity, we are proposing recovery furnace option 4 and lime kiln
option 2 for opacity monitoring. These options are representative of
the actual performance of 40 CFR part 63, subpart MM emission units
based on our analysis of the COMS data, and also align closely with the
opacity limits, monitoring allowances, and semiannual reporting
requirements established for new sources through the 2014 NSPS review.
The EPA is proposing to reduce the opacity limit for existing recovery
furnaces from 35-percent to 20-percent opacity. Lowering the recovery
furnace opacity limit to 20 percent eliminates the need for the 20-
percent corrective action level. Specifying a 20-percent corrective
action level is redundant where the opacity limit is already set at 20-
percent; therefore, we are proposing to eliminate the subpart MM
corrective action level in 40 CFR 63.864(k)(1)(i) by reserving this
section. We are proposing a monitoring allowance of 2-percent for
existing and new recovery furnaces. We are proposing to retain the 20-
percent opacity limit and are proposing a monitoring allowance of 1
percent for opacity monitoring for lime kilns. We are also proposing to
reduce the reporting frequency from quarterly to semiannually, as
discussed in section IV.D.4 of this preamble. The proposed semiannual
averaging period would be used for calculating the opacity monitoring
allowance, providing flexibility for startup and shutdown periods. The
cost effectiveness of recovery furnace option 4, $36,800 per ton PM, is
within the range of other recent EPA regulations. There is no cost
effectiveness value for lime kiln option 2 because no incremental HAP
reductions were estimated. In addition to proposing the revisions
described above, the EPA is requesting comment on all of the options
presented in Table 5.
ESP parameter monitoring. The EPA is proposing to add an ESP
parameter monitoring requirement for recovery furnaces and lime kilns
equipped with ESPs. The purpose of this is to provide another indicator
of ESP performance and enable affected sources to show continuous
compliance with the HAP metal standards (surrogate PM emission limit)
at all times, including periods when the opacity monitoring allowance
is used. The EPA is proposing that these sources monitor the secondary
voltage and secondary current (or, alternatively, total secondary
power) of each ESP collection field. These ESP parameter monitoring
requirements are in addition to opacity monitoring for recovery
furnaces equipped with ESPs alone. The EPA is proposing that these ESP
parameters be monitored, recorded every successive 15 minutes, and
averaged over the same semiannual period as the opacity monitoring
allowance. The semiannual average of the ESP parameters must remain
above the minimum limits established during the PM performance test
(i.e., above the minimum secondary current and secondary voltage or
above minimum total secondary power).
The EPA estimates that the nationwide costs associated with adding
the proposed ESP parameter monitoring requirements would be $5.7
million capital and $1.4 million annualized costs for ESP parameter
monitors. All mills with ESP-controlled recovery furnaces and lime
kilns are estimated to be impacted.
Monitoring of ESPs followed by wet scrubbers. Because moisture in
wet stacks interferes with opacity readings, opacity is not a suitable
monitoring requirement for recovery furnaces or lime kilns with wet
scrubber stacks. The EPA is therefore proposing to require ESP and wet
scrubber parameter monitoring for emission units equipped with an ESP
followed by a wet scrubber. The ESP parameters to be monitored are
[[Page 97074]]
secondary voltage and secondary current (or, alternatively, total
secondary power), and the wet scrubber parameters are pressure drop and
scrubber liquid flow rate. The EPA is proposing that ESP and wet
scrubber parameters be recorded at least once every successive 15-
minute period and reduced to 3-hour averages. The EPA estimates no
incremental costs to be associated specifically with the proposed
monitoring requirements for combined ESP-wet scrubber systems because
the ESP parameter monitoring costs estimated above include ESPs in
combined control systems, and wet scrubber parameter monitoring is
already required under 40 CFR part 63, subpart MM.
4. Kraft and Soda Smelt Dissolving Tanks
Smelt dissolving tanks are covered vessels located below the
recovery furnace to collect molten smelt, one of the main products from
the combustion of black liquor. Smelt is comprised predominantly of
Na2S and Na2CO3 and is formed in the
bottom of the recovery furnace. The smelt is continuously discharged
through water-cooled smelt spouts into the SDT where it is mixed with
weak wash water from the pulp mill recausticizing area to form green
liquor, an aqueous solution of Na2CO3 and
Na2S. The green liquor is subsequently transferred to the
recausticizing area for reprocessing into pulping liquor (i.e., white
liquor). In the soda pulping process, the molten smelt and green liquor
is predominantly Na2CO3 because soda pulping is a
non-sulfur process. Based on the 2011 Pulp and Paper Sector ICR data,
there are 161 kraft and soda SDTs in the United States. Nearly all of
the SDTs have wet scrubbers that control the particulate emissions,
including HAP metals, from this process. A small number of SDTs use
mist eliminators as the only means of emissions control. Some new
sources were designed to vent emissions through the recovery furnace as
an alternative to using wet scrubber control alone, but also have a wet
scrubber for backup periods when venting to the recovery furnace is not
feasible.
SDT PM. The current 40 CFR part 63, subpart MM PM emission limit
(which is a surrogate for HAP metals) for existing SDTs is 0.20 lb/ton
BLS. The subpart MM PM limit for new and reconstructed sources with
initial startup in 2001 or later is 0.12 lb/ton BLS based on the use of
a high-efficiency wet scrubber.
The EPA analyzed SDT PM stack test data collected with the 2011
Pulp and Paper Sector ICR for the NSPS review promulgated on April 4,
2014 (79 FR 18952). We reviewed this same dataset in the context of
subpart MM for purposes of the 40 CFR part 63, subpart MM technology
review. The stack test data show that nearly all SDTs have achieved the
subpart MM existing source limit of 0.20 lb/ton BLS (with the exception
of a few SDTs with mist eliminators and SDTs included in the PM bubble
compliance option under subpart MM). There were many existing scrubber-
controlled SDTs with emissions between the new source limit of 0.12 lb/
ton BLS and the existing source limit of 0.20 lb/ton BLS. The practice
of routing SDT emissions through the recovery furnace has an
unquantified effect on PM emissions because no emission test data are
available to differentiate SDT emissions from the recovery furnace
emissions in these systems. The EPA has identified no practices,
processes, or controls for SDTs beyond those identified at the time of
subpart MM development, nor any incremental improvements in the ability
of wet scrubbers to reduce PM. Therefore, the EPA is not proposing any
changes to the current existing and new source PM limits in subpart MM
for kraft and soda mill SDTs. The EPA has identified no regulatory
options for SDTs for further consideration under the subpart MM
technology review.
SDT parameter monitoring. Subpart MM specifies monitoring of
scrubber liquid flow rate and pressure drop for SDTs equipped with wet
scrubbers. Facilities may have difficulty meeting the minimum pressure
drop requirement during startup and shutdown, as expected due to the
reduced (and changing) volumetric flow of stack gases during startup
and shutdown. The EPA is proposing to consider only scrubber liquid
flow rate during these periods (i.e., excess emissions would include
any 3-hour period when BLS are fired that the scrubber flow rate does
not meet the minimum parameter limits set in the initial performance
test). This is discussed further in section IV.D.1.
Based on previous alternative monitoring requests for SDTs, the EPA
is also proposing to allow operators to use SDT scrubber fan amperage
as an alternative to pressure drop measurement for SDT dynamic
scrubbers operating at ambient pressure or for low-energy entrainment
scrubbers on SDTs where the fan speed does not vary.
5. Sulfite Combustion Units
When subpart MM was proposed in 1998, there were 15 sulfite pulp
mills. Today there are only three sulfite mills, including one using
the magnesium-based sulfite process and two mills using the ammonia
(NH3)-based sulfite process. The EPA projects no new sulfite mills to
come online in the United States in the next 5 years. Based on a review
of permits and ICR data that the EPA has collected for these three
sulfite mills, we determined that there are a total of eight sulfite
combustion units currently operating in the United States.
Sulfite combustion unit PM. Subpart MM of 40 CFR part 63 requires
existing sulfite combustion units to meet a PM emission limit of 0.040
gr/dscf at 8-percent O2, based on the use of a fiber-bed
demister system. Subpart MM requires new sulfite combustion units to
meet a PM limit of 0.020 gr/dscf at 8-percent O2, based on
the combined use of a wet scrubber and fiber-bed demister system.\39\
The PM emission limits are a surrogate for HAP metals.
---------------------------------------------------------------------------
\39\ Although any control system could be used to meet the
emission limits for sulfite combustion units, the existing source
limit is consistent with the performance of a fiber-bed demister
system and the new source limit is consistent with the performance
of a wet scrubber with a fiber-bed demister.
---------------------------------------------------------------------------
For the 40 CFR part 63 subpart MM technology review, the EPA
reviewed ICR data on sulfite processes and controls, title V permit
limits, and PM stack test data for the three sulfite pulp mills
currently operating in the United States. Each sulfite mill has a
unique configuration of sulfite combustion units and corresponding
site-specific limits. Two facilities with sulfite combustion units
subject to a PM permit limit of 0.04 gr/dscf achieved this limit based
on actual measurement data submitted (with the exception of one test
above the limit that was superseded by a more recent test). Another
facility (Cosmo Specialty Fibers in Cosmopolis, Washington) has a site-
specific PM permit limit of 0.10 gr/dscf for its chemical recovery
combustion units, and instead reduces PM emissions from the hog fuel
dryer at the plant site. The chemical recovery combustion units (which
have a combined stack) have achieved average PM emissions of 0.054 gr/
dscf. The hog fuel dryer is permitted at 10 pounds per hour (lb/hr) of
PM and has achieved PM emissions of 1.2 and 1.5 lb/hr in two tests. The
EPA's technology review found no developments in practices, processes,
or controls since the promulgation of subpart MM for PM emissions from
sulfite combustion units. The EPA is proposing to retain the 0.040 and
0.020 gr/dscf at 8-percent O2 PM limits for existing and new
sulfite combustion units. The EPA has identified no
[[Page 97075]]
regulatory options for sulfite combustion units for further
consideration under the subpart MM technology review.
Sulfite combustion unit parameter monitoring. Subpart MM of 40 CFR
part 63 specifies monitoring of scrubber liquid flow rate and pressure
drop for sulfite combustion units equipped with wet scrubbers.
Facilities may have difficulty meeting the minimum pressure drop
requirement during startup and shutdown, as expected due to the reduced
(and changing) volumetric flow of stack gases during startup and
shutdown. The EPA is proposing to consider only scrubber liquid flow
rate during startup and shutdown periods (i.e., excess emissions would
include any 3-hour period when spent pulping liquor is fired that the
scrubber flow rate does not meet the minimum parameter limits set in
the initial performance test). The EPA is proposing no changes for
parameter monitoring of the fiber-bed demister system, which is
addressed under the alternative monitoring provisions of subpart MM.
6. Semichemical Combustion Units
When 40 CFR part 63, subpart MM, was originally proposed in 1998,
there were 14 semichemical combustion units at 14 stand-alone
semichemical pulp mills. Today, there are seven semichemical combustion
units at seven mills in the United States, at six of which combustion
units and mills are operating.\40\ Semichemical combustion unit design
types include: Fluidized-bed reactor (two units, one operating),
recovery furnace (four units), and rotary liquor kiln (one unit).
---------------------------------------------------------------------------
\40\ One additional stand-alone semichemical pump mill ceased
operation in late 2015.
---------------------------------------------------------------------------
Semichemical combustion unit total hydrocarbon (THC). The current
40 CFR part 63, subpart MM standards require existing and new
semichemical combustion units to reduce total gaseous organic HAP
emissions (measured as THC) by 90 percent or meet a total gaseous
organic HAP emission limit (measured as THC) of 2.97 lb/ton of BLS
fired.
For the 40 CFR part 63, subpart MM RTR, the EPA reviewed ICR data
on processes and control configurations, title V permit limits, and THC
stack test data for the stand-alone semichemical pulp mills currently
operating in the United States. The review of permit limits indicated
that all semichemical combustion units are subject to the 2.97 lb/ton
BLS THC limit specified in subpart MM for existing and new units.
Performance of the different semichemical combustion units varies
considerably for THC. While most units achieve the 2.97 lb/ton BLS THC
limit, at least one unit relied on the 90-percent reduction compliance
option included in subpart MM to address variability. The EPA has
identified no regulatory options for semichemical combustion units for
purposes of the subpart MM RTR, given that no practices, processes, or
controls beyond those considered during the original rule development
have emerged.
Semichemical combustion unit parameter monitoring. Subpart MM of 40
CFR part 63 requires semichemical combustion units using RTOs to
measure and record RTO operating temperature to demonstrate compliance
with the standard for gaseous organic HAP (measured as THC). As noted
previously, no practices, processes, or controls beyond those
considered during the original rule development have emerged.
Consequently, the EPA is proposing no changes for the current parameter
monitoring requirements.
D. What other actions are we proposing?
In addition to the proposed actions described above, we are
proposing additional revisions. We are proposing revisions to the SSM
provisions of the MACT rule in order to ensure that they are consistent
with the court decision in Sierra Club v. EPA, 551 F.3d 1019 (D.C. Cir.
2008), which vacated two provisions that exempted sources from the
requirement to comply with otherwise applicable CAA section 112(d)
emission standards during periods of SSM. We also are proposing various
other changes, including 5-year periodic emissions testing for selected
process equipment, semiannual electronic reporting for all excess
emissions reports, electronic submittal of compliance reports (which
include performance test reports), incorporation by reference, and
various technical and editorial changes. Our analyses and proposed
changes related to these issues are discussed in sections IV.D.1
through 6 of this preamble.
1. Startup, Shutdown, and Malfunction
In its 2008 decision in Sierra Club v. EPA, 551 F.3d 1019 (D.C.
Cir. 2008), the United States Court of Appeals for the District of
Columbia Circuit vacated portions of two provisions in the EPA's CAA
section 112 regulations governing the emissions of HAPs during periods
of SSM. Specifically, the Court vacated the SSM exemption contained in
40 CFR 63.6(f)(1) and 40 CFR 63.6(h)(1), holding that under section
302(k) of the CAA, emissions standards or limitations must be
continuous in nature and that the SSM exemption violates the CAA's
requirement that some CAA section 112 standards apply continuously.
We are proposing the elimination of the SSM exemption in this rule.
Consistent with Sierra Club v. EPA, we are proposing standards in this
rule that apply at all times. We are also proposing several revisions
to Table 1 (the General Provisions Applicability Table) as is explained
in more detail below. For example, we are proposing to eliminate the
incorporation of the General Provisions' requirement that the source
develop an SSM plan. We also are proposing to eliminate and revise
certain recordkeeping and reporting requirements related to the SSM
exemption as further described below.
The EPA has attempted to ensure that the provisions we are
proposing to eliminate are inappropriate, unnecessary, or redundant in
the absence of the SSM exemption. We are specifically seeking comment
on whether we have successfully done so.
Periods of startup and shutdown. In reviewing the standards in this
rule, the EPA has taken into account startup and shutdown periods and,
for the reasons explained below, is not proposing alternate standards
for those periods.
Subpart MM of 40 CFR part 63 requires continuous opacity monitoring
to indicate ongoing compliance with the PM emission limits. In
developing proposed standards for subpart MM, the EPA reviewed numerous
continuous opacity monitoring datasets that included periods of startup
and shutdown, and concluded that the affected units will be able to
comply with the proposed standards at all times. The proposed subpart
MM also requires RTO operating temperature and ESP and wet scrubber
parameter monitoring. Parameter limits apply at all times, including
during startup and shutdown. The proposed subpart MM requires RTO
operating temperature and wet scrubber and ESP operating parameters to
be recorded at least once every 15 minutes. Subpart MM specifies
corrective action levels in 40 CFR 63.864(k)(1) and violation levels in
40 CFR 63.864(k)(2) which would be reported as excess emissions under
40 CFR 63.867(c). For RTO temperature, subpart MM requires corrective
action when any 1-hour temperature falls below the average temperature
established during the performance test. Subpart MM considers any 3-
hour RTO temperature that falls below the average established during
the performance test to be a violation. Subpart MM requires the ESP and
scrubber parameters to be averaged over a 3-hour block, except for ESPs
with COMS, which would have
[[Page 97076]]
ESP parameters averaged semiannually. The corrective action level for
wet scrubber and ESP operating parameters (when opacity is not also
measured) is triggered when any 3-hour average is outside of the limit
established during the performance test. A violation would occur when
six or more of the 3-hour average parameter values within a 6-month
period are outside of the limits established during the performance
test. Violations based on opacity would be considered over a semiannual
period. For new or existing kraft or soda recovery furnaces, a
violation would occur when any opacity is greater than 20 percent for 2
percent or more of the operating time when spent liquor is fired within
a semiannual period. For new or existing lime kilns, a violation would
occur when any opacity is greater than 20 percent for 1 percent or more
of the operating time when lime mud is fired in a semiannual period. A
violation would also occur when the recovery furnace or lime kiln ESP
secondary voltage and secondary current (or total secondary power)
averaged over the semiannual period are below the minimum operating
limits established during the performance test, with the exception of
secondary current (or total secondary power) during periods of startup
and shutdown.
To address the need for ESPs to warm to a specified temperature
(typically above 200[emsp14][deg]F) before full power is applied to the
transformer-rectifier set, the EPA is proposing to define excess
emissions (i.e., the corrective action and violation levels) as opacity
and ESP parameter measurements below the minimum requirements during
times when BLS or lime mud is fired (as applicable), based on several
responses to the ICR indicating that mills with ESP minimum temperature
requirements bring the ESP online before introducing BLS or lime mud
into the recovery furnace or lime kiln, respectively. The EPA is also
proposing language that would allow affected units to use wet scrubber
liquid flow rate to demonstrate compliance during periods of startup
and shutdown because pressure drop is difficult to achieve during these
periods.
Periods of malfunction. Periods of startup, normal operations, and
shutdown are all predictable and routine aspects of a source's
operations. Malfunctions, in contrast, are neither predictable nor
routine. Instead they are, by definition, sudden, infrequent, and not
reasonably preventable failures of emissions control, process or
monitoring equipment. (40 CFR 63.2) (Definition of malfunction). The
EPA interprets CAA section 112 as not requiring emissions that occur
during periods of malfunction to be factored into development of CAA
section 112 standards. Under CAA section 112, emissions standards for
new sources must be no less stringent than the level ``achieved'' by
the best controlled similar source and for existing sources generally
must be no less stringent than the average emission limitation
``achieved'' by the best performing 12 percent of sources in the
category. There is nothing in CAA section 112 that directs the Agency
to consider malfunctions in determining the level ``achieved'' by the
best performing sources when setting emission standards. As the
District of Columbia Circuit Court has recognized, the phrase ``average
emissions limitation achieved by the best performing 12 percent of''
sources ``says nothing about how the performance of the best units is
to be calculated.'' Nat'l Ass'n of Clean Water Agencies v. EPA, 734
F.3d 1115, 1141 (D.C. Cir. 2013). While the EPA accounts for
variability in setting emissions standards, nothing in CAA section 112
requires the Agency to consider malfunctions as part of that analysis.
A malfunction should not be treated in the same manner as the type of
variation in performance that occurs during routine operations of a
source. A malfunction is a failure of the source to perform in a
``normal or usual manner'' and no statutory language compels the EPA to
consider such events in setting section CAA 112 standards.
Further, accounting for malfunctions in setting emission standards
would be difficult, if not impossible, given the myriad of different
types of malfunctions that can occur across all sources in the category
and given the difficulties associated with predicting or accounting for
the frequency, degree, and duration of various malfunctions that might
occur. As such, the performance of units that are malfunctioning is not
``reasonably'' foreseeable. See, e.g., Sierra Club v. EPA, 167 F.3d
658, 662 (D.C. Cir. 1999) (``The EPA typically has wide latitude in
determining the extent of data-gathering necessary to solve a problem.
We generally defer to an agency's decision to proceed on the basis of
imperfect scientific information, rather than to `invest the resources
to conduct the perfect study.' '') See also, Weyerhaeuser v. Costle,
590 F.2d 1011, 1058 (D.C. Cir. 1978) (``In the nature of things, no
general limit, individual permit, or even any upset provision can
anticipate all upset situations. After a certain point, the
transgression of regulatory limits caused by `uncontrollable acts of
third parties,' such as strikes, sabotage, operator intoxication or
insanity, and a variety of other eventualities, must be a matter for
the administrative exercise of case-by-case enforcement discretion, not
for specification in advance by regulation.''). In addition, emissions
during a malfunction event can be significantly higher than emissions
at any other time of source operation. For example, if an air pollution
control device with 99-percent removal goes off-line as a result of a
malfunction (as might happen if, for example, the bags in a baghouse
catch fire) and the emission unit is a steady state type unit that
would take days to shut down, the source would go from 99-percent
control to zero control until the control device was repaired. The
source's emissions during the malfunction would be 100 times higher
than during normal operations. As such, the emissions over a 4-day
malfunction period would exceed the annual emissions of the source
during normal operations. As this example illustrates, accounting for
malfunctions could lead to standards that are not reflective of (and
significantly less stringent than) levels that are achieved by a well-
performing non-malfunctioning source. It is reasonable to interpret CAA
section 112 to avoid such a result. The EPA's approach to malfunctions
is consistent with CAA section 112 and is a reasonable interpretation
of the statute.
In the event that a source fails to comply with the applicable CAA
section 112(d) standards as a result of a malfunction event, the EPA
would determine an appropriate response based on, among other things,
the good faith efforts of the source to minimize emissions during
malfunction periods, including preventative and corrective actions, as
well as root cause analyses to ascertain and rectify excess emissions.
The EPA would also consider whether the source's failure to comply with
the CAA section 112(d) standard was, in fact, sudden, infrequent, not
reasonably preventable, and was not instead caused in part by poor
maintenance or careless operation. 40 CFR 63.2 (definition of
malfunction).
If the EPA determines in a particular case that an enforcement
action against a source for violation of an emission standard is
warranted, the source can raise any and all defenses in that
enforcement action and the Federal District Court will determine what,
if any, relief is appropriate. The same is true for citizen enforcement
actions. Similarly, the presiding officer in an administrative
proceeding can consider any defense raised and determine
[[Page 97077]]
whether administrative penalties are appropriate.
In summary, the EPA interpretation of the CAA and, in particular,
CAA section 112 is reasonable and encourages practices that will avoid
malfunctions. Administrative and judicial procedures for addressing
exceedances of the standards fully recognize that violations may occur
despite good faith efforts to comply and can accommodate those
situations.
a. General Duty
We are proposing to revise the General Provisions table (Table 1)
entry for 40 CFR 63.6(e) by re-designating it as 40 CFR 63.6(e)(1)(i)
and changing the ``yes'' in column 3 to a ``no.'' Section 63.6(e)(1)(i)
describes the general duty to minimize emissions. Some of the language
in that section is no longer necessary or appropriate in light of the
elimination of the SSM exemption. We are proposing instead to add
general duty regulatory text at 40 CFR 63.860(d) that reflects the
general duty to minimize emissions while eliminating the reference to
periods covered by an SSM exemption. The current language in 40 CFR
63.6(e)(1)(i) characterizes what the general duty entails during
periods of SSM. With the elimination of the SSM exemption, there is no
need to differentiate between normal operations and SSM events in
describing the general duty. Therefore, the language the EPA is
proposing for 40 CFR 63.860(d) does not include that language from 40
CFR 63.6(e)(1).
We are also proposing to revise the General Provisions table (Table
1) to add an entry for 40 CFR 63.6(e)(1)(ii) and include a ``no'' in
column 3. Section 63.6(e)(1)(ii) imposes requirements that are not
necessary with the elimination of the SSM exemption or are redundant
with the general duty requirement being added at 40 CFR 63.860(d).
b. SSM Plan
We are proposing to revise the General Provisions table (Table 1)
to add an entry for 40 CFR 63.6(e)(3) and include a ``no'' in column 3.
Generally, the paragraphs under 40 CFR 63.6(e)(3) require development
of an SSM plan and specify SSM recordkeeping and reporting requirements
related to the SSM plan. As noted, the EPA is proposing to remove the
SSM exemptions. Therefore, affected units will be subject to an
emission standard during such events. The applicability of a standard
during such events will ensure that sources have ample incentive to
plan for and achieve compliance and, thus, the SSM plan requirements
are no longer necessary.
c. Compliance With Standards
We are proposing to revise the General Provisions table (Table 1)
entries for 40 CFR 63.6(f) and (h) by re-designating these sections as
40 CFR 63.6(f)(1) and (h)(1) and including a ``no'' in column 3. The
current language of 40 CFR 63.6(f)(1) and (h)(1) exempts sources from
non-opacity and opacity standards during periods of SSM. As discussed
above, the court in Sierra Club vacated the exemptions contained in
this provision and held that the CAA requires that some CAA section 112
standard apply continuously. Consistent with Sierra Club, the EPA is
proposing to revise standards in this rule to apply at all times.
d. Performance Testing
We are proposing to revise the General Provisions table (Table 1)
entry for 40 CFR 63.7(e) by re-designating it as 40 CFR 63.7(e)(1) and
including a ``no'' in column 3. Section 63.7(e)(1) describes
performance testing requirements. The EPA is instead proposing to add a
performance testing requirement at 40 CFR 63.865. The proposed
performance testing provisions require testing under representative
operating conditions, excluding periods of startup and shutdown. As in
40 CFR 63.7(e)(1), performance tests conducted under this subpart
should not be conducted during malfunctions because conditions during
malfunctions are often not representative of normal operating
conditions. The EPA is proposing to add language that requires the
owner or operator to record the process information that is necessary
to document operating conditions during the test and include in such
record an explanation to support that such conditions represent normal
operation. Section 63.7(e) requires that the owner or operator make
available to the Administrator such records ``as may be necessary to
determine the condition of the performance test'' available to the
Administrator upon request, but does not specifically require the
information to be recorded. The regulatory text the EPA is proposing to
add to this provision builds on that requirement and makes explicit the
requirement to record the information.
e. Monitoring
We are proposing to revise the General Provisions table (Table 1)
by re-designating 40 CFR 63.8(c) as 40 CFR 63.8(c)(1), adding entries
for 40 CFR 63.8(c)(1)(i) through (iii) and including ``no'' in column 3
for paragraphs (i) and (iii). The cross-references to the general duty
and SSM plan requirements in those subparagraphs are not necessary in
light of other requirements of 40 CFR 63.8 that require good air
pollution control practices (40 CFR 63.8(c)(1)) and that set out the
requirements of a quality control program for monitoring equipment (40
CFR 63.8(d)).
We are also proposing to revise the General Provisions table (Table
1) by adding an entry for 40 CFR 63.8(d)(3) and including a ``no'' in
column 3. The final sentence in 40 CFR 63.8(d)(3) refers to the General
Provisions' SSM plan requirement which is no longer applicable. The EPA
is proposing to add to the rule at 40 CFR 63.864(f) text that is
identical to 40 CFR 63.8(d)(3) except that the final sentence is
replaced with the following sentence: ``The program of corrective
action should be included in the plan required under 40 CFR
63.8(d)(2).''
f. Recordkeeping
We are proposing to revise the General Provisions table (Table 1)
by adding an entry for 40 CFR 63.10(b)(2)(i) and including a ``no'' in
column 3. Section 63.10(b)(2)(i) describes the recordkeeping
requirements during startup and shutdown. These recording provisions
are no longer necessary because the EPA is proposing that recordkeeping
and reporting applicable to normal operations will apply to startup and
shutdown. Special provisions applicable to startup and shutdown, such
as a startup and shutdown plan, have been removed from the rule (with
exceptions discussed below) thereby reducing the need for additional
recordkeeping for startup and shutdown periods.
Records of startup and shutdown periods are proposed to be required
under 40 CFR 63.866(c)(8) to help characterize minor exceptions to
reporting. The EPA is proposing no reporting of wet scrubber pressure
drop or ESP secondary current (or total secondary power) during periods
of startup and shutdown because it is not feasible to meet operating
limits established under normal operation for these parameters during
startup and shutdown. Instead, the EPA is proposing that wet scrubber
liquid flow rate (or fan amperage) and ESP secondary voltage be
monitored during startup and shutdown.
We are also proposing to revise the General Provisions table (Table
1) by adding an entry for 40 CFR 63.10(b)(2)(ii) and including a ``no''
in column 3. Section 63.10(b)(2)(ii) describes the recordkeeping
requirements during a malfunction. The EPA is proposing to add such
[[Page 97078]]
requirements to 40 CFR 63.866(d). The regulatory text we are proposing
to add differs from the General Provisions it is replacing in that the
General Provisions requires the creation and retention of a record of
the occurrence and duration of each malfunction of process, air
pollution control, and monitoring equipment. The EPA is proposing that
this requirement apply to any failure to meet an applicable standard
and is requiring that the source record the date, time, and duration of
the failure rather than the ``occurrence.'' The EPA is also proposing
to add to 40 CFR 63.866(d) a requirement that sources keep records that
include a list of the affected source or equipment and actions taken to
minimize emissions, an estimate of the quantity of each regulated
pollutant emitted over the emission limit for which the source failed
to meet the standard, and a description of the method used to estimate
the emissions. Examples of such methods would include product-loss
calculations, mass balance calculations, measurements when available,
or engineering judgment based on known process parameters. The EPA is
proposing to require that sources keep records of this information to
ensure that there is adequate information to allow the EPA to determine
the severity of any failure to meet a standard, and to provide data
that may document how the source met the general duty to minimize
emissions when the source has failed to meet an applicable standard.
We are also proposing to revise the General Provisions table (Table
1) by adding an entry for 40 CFR 63.10(b)(2)(iv) and (v) and including
a ''no'' in column 3. When applicable, the provision requires sources
to record actions taken during SSM events when actions were
inconsistent with their SSM plan. The requirement is no longer
appropriate because SSM plans will no longer be required. The
requirement previously applicable under 40 CFR 63.10(b)(2)(iv)(B) to
record actions to minimize emissions and record corrective actions is
now applicable by reference to 40 CFR 63.866(d).
We are also proposing to revise the General Provisions table (Table
1) by adding an entry for 40 CFR 63.10(c)(15) and including a ``no'' in
column 3. The EPA is proposing that 40 CFR 63.10(c)(15) no longer
apply. When applicable, the provision allows an owner or operator to
use the affected source's SSM plan or records kept to satisfy the
recordkeeping requirements of the SSM plan, specified in 40 CFR
63.6(e), to also satisfy the requirements of 40 CFR 63.10(c)(10)
through (12). The EPA is proposing to eliminate this requirement
because SSM plans would no longer be required, and, therefore, 40 CFR
63.10(c)(15) no longer serves any useful purpose for affected units.
g. Reporting
We are proposing to revise the General Provisions table (Table 1)
entry for 40 CFR 63.10(d)(5) by re-designating it as 40 CFR
63.10(d)(5)(i) and changing the ``yes'' in column 3 to a ``no.''
Section 63.10(d)(5)(i) describes the periodic reporting requirements
for startups, shutdowns, and malfunctions. To replace the General
Provisions reporting requirement, the EPA is proposing to add reporting
requirements to 40 CFR 63.867(c). The replacement language differs from
the General Provisions requirement in that it eliminates periodic SSM
reports as a stand-alone report. We are proposing language that
requires sources that fail to meet an applicable standard at any time
to report the information concerning such events in the semiannual
report to be required under the proposed rule. We are proposing that
the report must contain the number, date, time, duration, and the cause
of such events (including unknown cause, if applicable), a list of the
affected source or equipment, an estimate of the quantity of each
regulated pollutant emitted over any emission limit, and a description
of the method used to estimate the emissions.
Examples of such methods would include product-loss calculations,
mass balance calculations, measurements when available, or engineering
judgment based on known process parameters. The EPA is proposing this
requirement to ensure that there is adequate information to determine
compliance, to allow the EPA to determine the severity of the failure
to meet an applicable standard, and to provide data that may document
how the source met the general duty to minimize emissions during a
failure to meet an applicable standard.
We will no longer require owners or operators to determine whether
actions taken to correct a malfunction are consistent with an SSM plan,
because plans would no longer be required. The proposed amendments,
therefore, eliminate the cross reference to 40 CFR 63.10(d)(5)(i) that
contains the description of the previously required SSM report format
and submittal schedule from this section. These specifications are no
longer necessary because the events will be reported in otherwise
required reports with similar format and submittal requirements.
We are also proposing to revise the General Provisions table (Table
1) to add an entry for 40 CFR 63.10(d)(5)(ii) and include a ``no'' in
column 3. Section 63.10(d)(5)(ii) describes an immediate report for
startups, shutdown, and malfunctions when a source failed to meet an
applicable standard, but did not follow the SSM plan. We will no longer
require owners and operators to report when actions taken during a
startup, shutdown, or malfunction were not consistent with an SSM plan,
because plans would no longer be required.
2. 5-Year Periodic Emissions Testing
As part of an ongoing effort to improve compliance with various
federal air emission regulations, the EPA reviewed the testing and
monitoring requirements of 40 CFR part 63, subpart MM and is proposing
the following change. The EPA is proposing to require facilities
complying with the standards for chemical recovery combustion sources
at kraft, soda, sulfite, and stand-alone semichemical pulp mills to
conduct periodic air emissions performance testing, with the first of
the periodic performance tests to be conducted within 3 years of the
effective date of the revised standards and thereafter before the
facilities renew their 40 CFR part 70 operating permits, but no longer
than 5 years following the previous performance test. Periodic
performance tests are already required by permitting authorities for
some facilities. Further, the EPA believes that requiring periodic
performance tests will help to ensure that control systems are properly
maintained over time, thereby reducing the potential for acute
emissions episodes. This proposal would require periodic air emissions
testing for filterable PM once every 5 years for existing and new kraft
and soda recovery furnaces, SDTs, and lime kilns and sulfite combustion
units. In addition, this proposal would require air emissions testing
for methanol once every 5 years for new kraft and soda recovery
furnaces. This proposal would also require periodic air emissions
testing for THC for existing and new semichemical combustion units.
3. Continuous Parameter Monitoring System (CPMS) Operating Limits
We are proposing to specify procedures for establishing operating
limits based on data recorded by CPMS. The 40 CFR part 63, subpart MM
emission standards are comprised of numerical emission limits, with
compliance demonstrated through periodic performance tests, and
operating limits such as opacity limits or continuously monitored
parameter limits used to demonstrate ongoing compliance in between
performance
[[Page 97079]]
tests. Currently, the subpart MM regulatory text refers extensively to
operating parameter ranges and is not as specific as more recent
NESHAPs in specifying how operating limits are to be determined.
Therefore, we are proposing language to clarify the procedures for
establishing parameter limits.
As noted previously, we are proposing ESP parameter monitoring
requirements for recovery furnaces and lime kilns with ESPs or combined
ESP and wet scrubber controls. This proposal would require ESP
parameters be recorded at least once every successive 15-minute period,
and the recorded readings be reduced to semiannual averages for ESPs
(i.e., where opacity monitoring requirements also apply) or 3-hour
averages for ESPs followed by a wet scrubber. Similarly, this proposal
would require wet scrubber parameters, including pressure drop across
the scrubber (or fan amperage for certain SDT scrubbers) and scrubbing
liquid flow rate, be recorded at least every 15-minutes and reduced to
3-hour averages. This proposal would require RTO temperature be
recorded every 15 minutes and reduced to a 1-hour average for purposes
of assessing when corrective action is required under 40 CFR
63.864(k)(1), and reduced to a 3-hour average under 40 CFR 63.864(k)(2)
for purposes of assessing violations.
We are proposing that the ESP and wet scrubber operating limits be
established as the average of the parameter values associated with each
performance test run. For example, the proposal would require the
recorded readings during each test run be averaged to arrive at the
parameter value associated with three test runs, and the three values
be averaged to arrive at the operating limit. The proposal would
require these revised procedures be used beginning with the first
periodic performance test proposed to be required under 40 CFR 63.865.
Wet scrubbers and ESPs have minimum operating limits, such that the EPA
would consider 3-hour average values below the minimum operating limit
to be a monitoring exceedance to be reported under 40 CFR 63.867(c).
Also, in the spirit of ensuring continuous compliance, we are proposing
to eliminate the language in 40 CFR 63.864(k)(3) that allowed no more
than one non-opacity monitoring exceedance to be attributed to any 24-
hour period.
4. Reporting Frequency
Subpart MM of 40 CFR part 63 currently requires owners and
operators of subpart MM facilities to submit quarterly excess emissions
reports for monitoring exceedances and periods of noncompliance and
semiannual reports when no excess emissions have occurred during the
reporting period. These excess emission reports are typically submitted
as a hard copy to the delegated authority, and reports in this form
usually are not readily available for the EPA and public to analyze.
The Agency is proposing that semiannual electronic reporting would
provide ample data to assess a facility's performance with regard to
the emission standards in subpart MM. The EPA is proposing that all
excess emissions reports be submitted on a semiannual basis, to conform
to the semiannual reporting frequency employed by the electronic
reporting system discussed in the following section. The EPA requests
comment on maintaining quarterly reporting for reports of monitoring
exceedances and periods of noncompliance.
5. Electronic Reporting
The EPA is proposing that owners and operators of 40 CFR part 63,
subpart MM facilities submit electronic copies of compliance reports,
which include performance test reports, semiannual reports, and
notifications, through the EPA's Central Data Exchange (CDX) using the
Compliance and Emissions Data Reporting Interface (CEDRI).
Specifically, we are proposing that owners and operators submit
performance test reports through the Electronic Reporting Tool (ERT)
and submit notifications and semiannual reports through CEDRI. The EPA
believes that the electronic submittal of the reports addressed in this
proposed rulemaking will increase the usefulness of the data contained
in those reports, is in keeping with current trends in data
availability, will further assist in the protection of public health
and the environment, and will ultimately result in less burden on the
regulated community. Under current requirements, paper reports are
often stored in filing cabinets or boxes, which make the reports more
difficult to obtain and use for data analysis and sharing. Electronic
storage of such reports would make data more accessible for review,
analyses, and sharing. Electronic reporting can also eliminate paper-
based, manual processes, thereby saving time and resources, simplifying
data entry, eliminating redundancies, minimizing data reporting errors
and providing data quickly and accurately to the affected facilities,
air agencies, the EPA, and the public.
In 2011, in response to Executive Order 13563, the EPA developed a
plan \41\ to periodically review its regulations to determine if they
should be modified, streamlined, expanded, or repealed in an effort to
make regulations more effective and less burdensome. The plan includes
replacing outdated paper reporting with electronic reporting. In
keeping with this plan and the White House's Digital Government
Strategy,\42\ in 2013 the EPA issued an agency-wide policy specifying
that new regulations will require reports to be electronic to the
maximum extent possible. By requiring electronic submission of
specified reports in this proposed rule, the EPA is taking steps to
implement this policy.
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\41\ Improving Our Regulations: Final Plan for Periodic
Retrospective Reviews of Existing Regulations, August 2011.
Available at https://www.epa.gov/sites/roduction/files/2015-09-/documents/eparetroreviewplan-aug2011_0.pdf.
\42\ Digital Government: Buildiing a 21st Century Platform to
Better Serve the American People, May 2012. Available at https://www.whitehouse.gov/sites/default/files/omb/egov/digital-government/digital-government-strategy/pdf.
---------------------------------------------------------------------------
The EPA Web site that stores the submitted electronic data,
WebFIRE, will be easily accessible to everyone and will provide a user-
friendly interface that any stakeholder could access. By making data
readily available, electronic reporting increases the amount of data
that can be used for many purposes. One example is the development of
emissions factors. An emissions factor is a representative value that
attempts to relate the quantity of a pollutant released to the
atmosphere with an activity associated with the release of that
pollutant (e.g., kilograms of particulate emitted per megagram of coal
burned). Such factors facilitate the estimation of emissions from
various sources of air pollution and are an important tool in
developing emissions inventories, which in turn are the basis for
numerous efforts, including trends analysis, regional, and local scale
air quality modeling, regulatory impact assessments, and human exposure
modeling. Emissions factors are also widely used in regulatory
applicability determinations and in permitting decisions.
The EPA has received feedback from stakeholders asserting that many
of the EPA's emissions factors are outdated or not representative of a
particular industry emission source. While the EPA believes that the
emissions factors are suitable for their intended purpose, we recognize
that the quality of emissions factors varies based on the extent and
quality of underlying data. We also recognize that emissions profiles
on different pieces of equipment can change over time due to
[[Page 97080]]
a number of factors (fuel changes, equipment improvements, industry
work practices), and it is important for emissions factors to be
updated to keep up with these changes. The EPA is currently pursuing
emissions factor development improvements that include procedures to
incorporate the source test data that we are proposing be submitted
electronically. By requiring the electronic submission of the reports
identified in this proposed action, the EPA would be able to access and
use the submitted data to update emissions factors more quickly and
efficiently, creating factors that are characteristic of what is
currently representative of the relevant industry sector. Likewise, an
increase in the number of test reports used to develop the emissions
factors will provide more confidence that the factor is of higher
quality and representative of the whole industry sector.
Additionally, by making the records, data and reports addressed in
this proposed rulemaking readily available, the EPA, the regulated
community and the public will benefit when the EPA conducts periodic
reviews of its rules. As a result of having performance test reports
and air emission reports readily accessible, our ability to carry out
comprehensive reviews will be increased and achieved within a shorter
period of time. These data will provide useful information on control
efficiencies being achieved and maintained in practice within a source
category and across source categories for regulated sources and
pollutants. These reports can also be used to inform the technology-
review process by providing information on improvements to add-on
control technology and new control technology.
Under an electronic reporting system, the EPA's Office of Air
Quality Planning and Standards (OAQPS) would have air emissions and
performance test data in hand; OAQPS would not have to collect these
data from the EPA Regional offices or from delegated authorities or
industry sources in cases where these reports are not submitted to the
EPA Regional offices. Thus, we anticipate fewer or less substantial
ICRs in conjunction with prospective CAA-required technology and risk-
based reviews may be needed. We expect this to result in a decrease in
time spent by industry to respond to data collection requests. We also
expect the ICRs to contain less extensive stack testing provisions, as
we will already have stack test data electronically. Reduced testing
requirements would be a cost savings to industry. The EPA should also
be able to conduct these required reviews more quickly, as OAQPS will
not have to include the ICR collection time in the process or spend
time collecting reports from the EPA Regional Offices. While the
regulated community may benefit from a reduced burden of ICRs, the
general public benefits from the Agency's ability to provide these
required reviews more quickly, resulting in increased public health and
environmental protection.
Electronic reporting could minimize submission of unnecessary or
duplicative reports in cases where facilities report to multiple
government agencies and the agencies opt to rely on the EPA's
electronic reporting system to view report submissions. Where delegated
authorities continue to require a paper copy of these reports and will
accept a hard copy of the electronic report, facilities will have the
option to print paper copies of the electronic reporting forms to
submit to the delegated authorities, and, thus, minimize the time spent
reporting to multiple agencies. Additionally, maintenance and storage
costs associated with retaining paper records could likewise be
minimized by replacing those records with electronic records of
electronically submitted data and reports.
Delegated authorities could benefit from more streamlined and
automated review of the electronically submitted data. For example,
because the performance test data would be readily-available in a
standard electronic format, delegated authorities would be able to
review reports and data electronically rather than having to conduct a
review of the reports and data manually. Having reports and associated
data in electronic format will facilitate review through the use of
software ``search'' options, as well as the downloading and analyzing
of data in spreadsheet format. Additionally, delegated authorities
would benefit from the reported data being accessible to them through
the EPA's electronic reporting system wherever and whenever they want
or need access (as long as they have access to the Internet). The
ability to access and review air emission report information
electronically will assist delegated authorities to more quickly and
accurately determine compliance with the applicable regulations,
potentially allowing a faster response to violations which could
minimize harmful air emissions. This benefits both delegated
authorities and the general public.
The proposed electronic reporting of data is consistent with
electronic data trends (e.g., electronic banking and income tax
filing). Electronic reporting of environmental data is already common
practice in many media offices at the EPA. The changes being proposed
in this rulemaking are needed to continue the EPA's transition to
electronic reporting.
As noted above, we are proposing that 40 CFR part 63, subpart MM
performance test reports be submitted through the EPA's ERT. All of the
test methods listed under subpart MM are currently supported by the
ERT, with the exception of Method 308 in 40 CFR part 63, appendix A.
The proposal would require that performance test results collected
using test methods that are not supported by the ERT as listed on the
EPA's ERT Web site at the time of the test be submitted in portable
document format (PDF) using the attachment module of the ERT.
In addition to electronically reporting the results of performance
tests, we are proposing the requirement to electronically submit
notifications and the semiannual excess emissions report and/or summary
report required in 40 CFR 63.867. The proposal would require the owner
or operator use the appropriate electronic form or spreadsheet template
in CEDRI for the subpart or an alternate electronic file format
consistent with the form's extensible markup language (XML) schema. If
neither the reporting form nor the spreadsheet template specific to the
subpart are available at the time that the report is due, the owner or
operator would upload an electronic copy of the report in CEDRI. The
owner or operator would begin submitting reports electronically using
the reporting form or spreadsheet template with the next report that is
due, once the electronic form or template has been available for at
least 90 days. The EPA is currently working to develop the forms and a
spreadsheet template for subpart MM. We are specifically taking comment
on the content, layout, and overall design of the forms and spreadsheet
template, which are discussed in a memorandum in the docket titled
Electronic Reporting for Subpart MM Excess Emission Reports.
As part of this review, we have specified in 40 CFR 63.867 the
reporting requirements from the 40 CFR part 63 General Provisions for
the excess emissions and summary reports. We believe that specifying
the General Provision reporting requirements for the proposed
semiannual reports in 40 CFR part 63, subpart MM, will help eliminate
confusion as to which report is submitted (e.g., full excess emissions
report or summary report) and the content of the required report. Based
on the criteria specified in the General Provisions, subpart MM
requires a full
[[Page 97081]]
excess emissions report under any of the following three conditions:
(1) The total duration of monitoring exceedances is one percent or more
of the total reporting period operating time, or (2) the total
continuous monitoring system (CMS) downtime is five percent or more of
the total reporting period operating time, or (3) any violations
according to 40 CFR 63.864(k)(2) occurred. Subpart MM requires only an
abbreviated summary report when none of the three conditions apply for
the semiannual reporting period.
As stated in 40 CFR 63.867(a), the proposal also requires that
notifications be reported electronically though CEDRI. Currently, there
are no templates for notifications in CEDRI for this subpart.
Therefore, the owner or operator must submit their notifications in
PDF. Examples of such notifications include (but are not limited to)
the following: Initial notifications, notifications of compliance
status, notifications of a performance test, notifications of CMS
performance evaluation, and notifications of opacity and visible
emissions observations.
6. Incorporation by Reference Under 1 CFR part 51
The EPA is proposing regulatory text that includes incorporation by
reference (IBR). In accordance with requirements of 1 CFR 51.5, the EPA
is proposing to incorporate by reference the following document
described in the amendments to 40 CFR 63.14:
EPA-454/R-98-015, Office of Air Quality Planning and
Standards (OAQPS), Fabric Filter Bag Leak Detection Guidance, September
1997, IBR approved for 40 CFR 63.864(e).
This document provides guidance on the use of triboelectric
monitors as fabric filter bag leak detectors. The document includes
fabric filter and monitoring system descriptions; guidance on monitor
selection, installation, setup, adjustment, and operation; and quality
assurance procedures. The EPA has made, and will continue to make, this
document generally available electronically through https://www.regulations.gov and/or in hard copy at the appropriate EPA office
(see the ADDRESSES section of this preamble for more information). In
addition, this document is available on the EPA Technical Air Pollution
Resources Emission Measurement Center Web page (https://www.epa.gov/emc) under Continuous Emission Monitoring.
7. Technical and Editorial Changes
The following lists additional changes that address technical and
editorial corrections:
Made revisions throughout 40 CFR part 63, subpart MM, to
clarify the location in 40 CFR part 60 of applicable EPA test methods;
Made revisions throughout 40 CFR part 63, subpart MM, to
update the facility name for Cosmo Specialty Fibers;
Revised the definitions section in 40 CFR 63.861 to:
[cir] Remove the definition for ``black liquor gasification'' and
remove reference to black liquor gasification in the definitions for
``kraft recovery furnace,'' ``recovery furnace,'' ``semichemical
combustion unit,'' and ``soda recovery furnace'';
[cir] Remove the SSM exemption from the definition for
``modification'';
[cir] Clarify that the definition for ``particulate matter'' refers
to filterable PM;
[cir] Removed reference to use of one-half of the method detection
limit for non-detect Method 29 measurements within the definition of
``hazardous air pollutant (HAP) metals'' because the full detection
limit in emission measurements is now typically used for compliance
determination in NESHAPs, with the limited exception of TEQ
determination for dioxins and furans; and
[cir] Remove the definition for ``startup'' that pertains to the
former black liquor gasification system at Georgia-Pacific's facility
in Big Island, Virginia.
Corrected misspelling in 40 CFR 63.862(c).
Revised multiple sections (40 CFR 63.863, 63.866, and
63.867) to remove reference to the former smelters and former black
liquor gasification system at Georgia-Pacific's facility in Big Island,
Virginia.
Revised the monitoring requirements section in 40 CFR
63.864 to:
[cir] Add reference to Performance Specification 1 (PS-1) in COMS
monitoring provisions;
[cir] Add IBR for bag leak detection systems;
[cir] Specify written procedures for CMS recording frequency and
reducing data into averages; and
[cir] Clarify ongoing compliance provisions to address startup and
shutdown periods when certain parameters cannot be met.
Revised the performance test requirements section in 40
CFR 63.865 to specify the conditions for conducting performance tests
and to revise the ambient O2 concentration in Equations 7
and 8 from 21 percent to 20.9 percent to bring 40 CFR part 63, subpart
MM, in line with the rest of the NESHAPs.
Revised the recordkeeping requirements section in 40 CFR
63.866 to include the requirement to record information on failures to
meet the applicable standard.
Revised the terminology in the delegation of authority
section in 40 CFR 63.868 to match the definitions in 40 CFR 63.90.
Revised the General Provisions applicability table (Table
1 to subpart MM of part 63) to align with those sections of the General
Provisions that have been amended or reserved over time.
E. What compliance dates are we proposing?
The compliance date for the revisions we are proposing here is 1
year after the date of publication of the final rule in the Federal
Register, with the exception of the following: (1) Facilities must
conduct the first of the 5-year periodic performance tests within 3
years of the effective date of the standards (that is, the date 3 years
after the date of publication of the final rule in the Federal
Register), and must conduct the subsequent periodic performance tests
before renewing the facility's 40 CFR part 70 operating permit, but no
longer than 5 years following the previous performance test; and (2)
facilities must submit performance test data through the ERT within 60
days after the date of completing each performance test.
V. Summary of Cost, Environmental, and Economic Impacts
A. What are the affected sources?
There are currently 108 major source pulp and paper mills operating
in the United States that conduct chemical recovery combustion
operations, including 97 kraft pulp mills, 1 soda pulp mill, 3 sulfite
pulp mills, and 7 stand-alone semichemical pulp mills. The 40 CFR part
63, subpart MM, affected source regulated at kraft or soda pulp mills
is each existing chemical recovery system, defined as all existing DCE
and NDCE recovery furnaces, SDTs, and lime kilns. The DCE recovery
furnace system is defined as the DCE recovery furnace and any BLO
system, if present, at the pulp mill. New affected sources at kraft or
soda pulp mills include each new NDCE or DCE recovery furnace and
associated SDT, and each new lime kiln. Subpart MM affected sources
also include each new or existing chemical recovery combustion unit
located at a sulfite pulp
[[Page 97082]]
mill or at a stand-alone semichemical pulp mill.
B. What are the air quality impacts?
At the current level of control, emissions of HAPs (HAP metals,
acid gases, and gaseous organic HAP) are approximately 11,600 tpy.
Current emissions of PM (a surrogate pollutant for HAP metals) and TRS
(emitted by the same mechanism as gaseous organic HAP) are
approximately 23,200 tpy and 3,600 tpy, respectively.
The proposed amendments will require an estimated 108 mills to
conduct periodic testing for their chemical recovery combustion
operations, 96 mills equipped with ESP controls to meet more stringent
opacity limits and monitoring allowances and conduct ESP parameter
monitoring, and all 108 major sources with equipment subject to the 40
CFR part 63, subpart MM standards to operate without the SSM exemption.
The EPA estimates that the proposed changes to the opacity limits and
monitoring allowances will reduce PM emissions by approximately 235 tpy
and PM2.5 emissions by approximately 112 tpy. We were unable
to quantify the specific emissions reductions associated with periodic
emissions testing or eliminating the SSM exemption, and we expect no
emissions reductions with ESP parameter monitoring. However, periodic
testing will tend to reduce emissions by providing incentive for
facilities to maintain their control systems and make periodic
adjustments to ensure peak performance. Eliminating the SSM exemption
will reduce emissions by requiring facilities to meet the applicable
standard during SSM periods.
Indirect or secondary air emissions impacts are impacts that would
result from the increased electricity usage associated with the
operation of control devices (i.e., increased secondary emissions of
criteria pollutants from power plants). Energy impacts consist of the
electricity and steam needed to operate control devices and other
equipment that would be required under this proposed rule. The EPA
estimates that the proposed changes to the opacity limits and
monitoring allowances will result in energy impacts of 106,000 million
British thermal units per year and criteria pollutant emissions of 29
tpy (which includes PM, carbon monoxide, nitrogen oxides, and sulfur
dioxide). The EPA expects no secondary air emissions impacts or energy
impacts from the other proposed requirements.
Section IV.C of this preamble presents estimates of the air quality
impacts associated with the regulatory options that were not selected
for inclusion in this proposed rule. For further information, see the
memorandum titled, Costs/Impacts of the Subpart MM Residual Risk and
Technology Review, in the docket for this action.
C. What are the cost impacts?
Subpart MM of 40 CFR part 63 mills will incur costs to meet more
stringent opacity limits and monitoring allowances, conduct periodic
testing, and perform new ESP parameter monitoring. Costs associated
with elimination of the startup and shutdown exemption were estimated
as part of the reporting and recordkeeping costs and include time for
re-evaluating previously developed SSM record systems. The EPA
estimates the nationwide capital costs associated with the new testing
and monitoring requirements to be $48 million. The EPA estimates the
total nationwide annualized costs associated with these new
requirements to be $13 million per year. Section IV.C of this preamble
presents cost estimates associated with the regulatory options that
were not selected for inclusion in this rule. For further information,
see the memorandum titled Costs/Impacts of the Subpart MM Residual Risk
and Technology Review, in the docket for this action.
D. What are the economic impacts?
The economic impact analysis is designed to inform decision makers
about the potential economic consequences of a regulatory action. For
the current proposal, the EPA performed a partial-equilibrium analysis
of national pulp and paper product markets to estimate potential paper
product market and consumer and producer welfare impacts of the
proposed regulatory options.
Across proposed regulatory options, the EPA estimates market-level
changes in the paper and paperboard markets to be insignificant. For
the proposed option, the EPA predicts national-level weighted average
paper and paperboard prices to increase about 0.01 percent, but
predicts total quantities to decrease less than 0.01 percent.
In addition, the EPA performed a screening analysis for impacts on
small businesses by comparing estimated annualized engineering
compliance costs at the firm-level to firm sales. The screening
analysis found that the ratio of compliance cost to firm revenue falls
below 1-percent for the three small companies likely to be affected by
the proposal. For small firms, the minimum and maximum cost-to-sales
ratios are less than 1 percent.
More information and details of this analysis is provided in the
technical document titled Economic Impact Analysis for Proposed
Revisions to the National Emissions Standards for Hazardous Air
Pollutants, Subpart MM, for the Pulp and Paper Industry, which is
available in the docket for this proposed rule (Docket ID No. EPA-HQ-
OAR-2014-0741).
E. What are the benefits?
The EPA estimates the proposed changes to the opacity limits and
monitoring allowances at the 16 impacted mills will reduce PM emissions
by approximately 235 tpy and PM2.5 emissions by
approximately 112 tpy. Because these proposed amendments are not
considered economically significant, as defined by Executive Order
12866, we did not monetize the benefits of reducing these emissions.
This does not mean that there are no benefits associated with the
reduction in metal HAPs from this rule. We expect that these avoided
emissions will reduce health effects associated with exposure to air
pollution, and we provide below a qualitative description of benefits
associated with reducing PM2.5. In addition, we anticipate
the specific control technologies associated with these proposed
amendments will result in minor disbenefits from additional energy
consumption.
Directly emitted particles are precursors to secondary formation of
PM2.5. Controls installed to reduce HAP emissions would also
reduce ambient concentrations of PM2.5. Reducing exposure to
PM2.5 is associated with significant human health benefits,
including avoiding mortality and morbidity from cardiovascular and
respiratory illnesses. Researchers have associated PM2.5
exposure with adverse health effects in numerous toxicological,
clinical, and epidemiological studies (U.S. EPA, 2009).\43\ When
adequate data and resources are available and a regulatory impact
analysis is required, the EPA generally quantifies several health
effects associated with exposure to PM2.5 (e.g., U.S. EPA,
2012).\44\ These
[[Page 97083]]
health effects include premature mortality for adults and infants,
cardiovascular morbidities such as heart attacks, hospital admissions,
and respiratory morbidities such as asthma attacks, acute bronchitis,
hospital and emergency department visits, work loss days, restricted
activity days, and respiratory symptoms. The scientific literature also
suggests that exposure to PM2.5 is associated with adverse
effects on birth weight, pre-term births, pulmonary function, and other
cardiovascular and respiratory effects (U.S. EPA, 2009), but the EPA
has not quantified these impacts in its benefits analyses.
---------------------------------------------------------------------------
\43\ U.S. Environmental Protection agency (U.S. EPA). 2009.
Integrated Science Assessment for Particulate Matter (Final Report).
EPA-600-R-08-139F. National Center for Environmental Assessment--RTP
Division. Available on the Internet at https://cfpub.epa.gov/ncea/risk/recordisplay.cfm?deid=216546.
\44\ U.S. Environmental Protection Agency (U.S. EPA). 2012.
Regulatory Impact Analysis for the Final Revisions to the National
Ambient Air Quality Standards for Particulate Matter. Office of Air
and Radiation, Research Triange Park, NC. Available on the Internet
at https://www3.epa.gov/thn/ecas/regdata/RIAs/finalria.pdf and
https://www3.epa.gov/ttnecas1/regdata/RIAs/PMRIACombinedFile_Bookmarked.pdf.
---------------------------------------------------------------------------
VI. Request for Comments
We solicit comments on all aspects of this proposed action. In
addition to general comments on this proposed action, we are also
interested in additional data that may improve the risk assessments and
other analyses. We are specifically interested in receiving any
improvements to the data used in the site-specific emissions profiles
used for risk modeling. Such data should include supporting
documentation in sufficient detail to allow characterization of the
quality and representativeness of the data or information. Section VII
of this preamble provides more information on submitting data.
VII. Submitting Data Corrections
The site-specific emissions profiles used in the source category
risk and demographic analyses and instructions are available for
download on the RTR Web site at: https://www3.epa.gov/ttn/atw/rrisk/rtrpg.html. The data files include detailed information for each HAP
emissions release point for the facilities in the source category.
If you believe that the data are not representative or are
inaccurate, please identify the data in question, provide your reason
for concern, and provide any ``improved'' data that you have, if
available. When you submit data, we request that you provide
documentation of the basis for the revised values to support your
suggested changes. To submit comments on the data downloaded from the
RTR Web site, complete the following steps:
1. Within this downloaded file, enter suggested revisions to the
data fields appropriate for that information.
2. Fill in the commenter information fields for each suggested
revision (i.e., commenter name, commenter organization, commenter email
address, commenter phone number, and revision comments).
3. Gather documentation for any suggested emissions revisions
(e.g., performance test reports, material balance calculations, etc.).
4. Send the entire downloaded file with suggested revisions in
Microsoft[supreg] Access format and all accompanying documentation to
Docket ID No. EPA-HQ-OAR-2014-0741 (through one of the methods
described in the ADDRESSES section of this preamble).
5. If you are providing comments on a single facility or multiple
facilities, you need only submit one file for all facilities. The file
should contain all suggested changes for all sources at that facility.
We request that all data revision comments be submitted in the form of
updated Microsoft[supreg] Excel files that are generated by the
Microsoft[supreg] Access file. These files are provided on the RTR Web
site at: https://www3.epa.gov/ttn/atw/rrisk/rtrpg.html.
VIII. Statutory and Executive Order Reviews
Additional information about these statutes and Executive Orders
can be found at https://www.epa.gov/laws-regulations/laws-and-executive-orders.
A. Executive Order 12866: Regulatory Planning and Review and Executive
Order 13563: Improving Regulation and Regulatory Review
This action is not a significant regulatory action and was
therefore not submitted to OMB for review.
B. Paperwork Reduction Act (PRA)
The information collection activities in this proposed rule have
been submitted for approval to OMB under the PRA. The ICR document that
the EPA prepared has been assigned EPA ICR number 1805.08. You can find
a copy of the ICR in the docket for this rule, and it is briefly
summarized here.
The information collection requirements are not enforceable until
OMB approves them. The information requirements are based on
notification, recordkeeping, and reporting requirements in the NESHAP
General Provisions (40 CFR part 63, subpart A), which are essential in
determining compliance and mandatory for all operators subject to
national emissions standards. These recordkeeping and reporting
requirements are specifically authorized by CAA section 114 (42 U.S.C.
7414). All information submitted to the EPA pursuant to the
recordkeeping and reporting requirements for which a claim of
confidentiality is made is safeguarded according to Agency policies set
forth in 40 CFR part 2, subpart B.
We are proposing changes to the paperwork requirements for 40 CFR
part 63, subpart MM, in the form of eliminating the SSM reporting and
SSM plan requirements, adding periodic emissions testing for selected
process equipment, revising opacity monitoring provisions, adding
parameter monitoring for ESPs, changing the frequency of all excess
emissions reports to semiannual, and requiring electronic submittal of
all compliance reports (including performance test reports).
Respondents/affected entities: Respondents include chemical pulp
mills operating equipment subject to 40 CFR part 63, subpart MM.
Respondent's obligation to respond: Mandatory (authorized by
section 114 of the CAA).
Estimated number of respondents: 108.
Frequency of response: The frequency of responses varies depending
on the burden item. Responses include initial notifications, reports of
periodic performance tests, and semiannual compliance reports.
Total estimated burden: The annual recordkeeping and reporting
burden for this information collection, averaged over the first 3 years
of this ICR, is estimated to total 139,600 labor hours per year. Burden
is defined at 5 CFR 1320.3(b).
Total estimated cost: $17.7 million per year, including $14.4
million per year in labor costs and $3.29 million per year in
annualized capital and operation and maintenance costs.
An agency may not conduct or sponsor, and a person is not required
to respond to, a collection of information unless it displays a
currently valid OMB control number. The OMB control numbers for the
EPA's regulations in 40 CFR are listed in 40 CFR part 9.
Submit your comments on the Agency's need for this information, the
accuracy of the provided burden estimates, and any suggested methods
for minimizing respondent burden, to the EPA using the docket
identified at the beginning of this rule. You may also send your ICR-
related comments to OMB's Office of Information and Regulatory Affairs
via email to OIRA_submission@omb.eop.gov, Attention: Desk Officer for
the EPA. Since OMB is required to make a decision concerning the ICR
between 30 and 60 days after receipt, OMB must receive comments no
later than January 30, 2017. The EPA will respond to any ICR-related
comments in the final rule.
[[Page 97084]]
C. Regulatory Flexibility Act (RFA)
I certify that this action will not have a significant economic
impact on a substantial number of small entities under the RFA. In
making this determination, the impact of concern is any significant
adverse economic impact on small entities. An agency may certify that a
rule will not have a significant economic impact on a substantial
number of small entities if the rule relieves regulatory burden, has no
net burden or otherwise has a positive economic effect on the small
entities subject to the rule. The EPA estimates that all affected small
entities will have annualized costs of less than 1 percent of their
sales. We have, therefore, concluded that this action will have no net
regulatory burden for all directly regulated small entities. For more
information on the small entity impacts associated with this proposed
rule, please refer to the Economic Impact and Small Business Analyses
in the public docket.
D. Unfunded Mandates Reform Act (UMRA)
This action does not contain an unfunded mandate of $100 million or
more as described in UMRA, 2 U.S.C. 1531-1538, and does not
significantly or uniquely affect small governments. The action imposes
no enforceable duty on any state, local, or tribal governments or the
private sector.
E. Executive Order 13132: Federalism
This action 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.
F. Executive Order 13175: Consultation and Coordination With Indian
Tribal Governments
This action does not have tribal implications as specified in
Executive Order 13175. It will not have substantial direct effects on
tribal governments, on the relationship between the federal government
and Indian tribes, or on the distribution of power and responsibilities
between the federal government and Indian tribes, as specified in
Executive Order 13175. This rule imposes requirements on owners and
operators of kraft, soda, sulfite, and stand-alone semichemical pulp
mills and not tribal governments. The EPA does not know of any pulp
mills owned or operated by Indian tribal governments, or located within
tribal lands. However, if there are any, the effect of this rule on
communities of tribal governments would not be unique or
disproportionate to the effect on other communities. Thus, Executive
Order 13175 does not apply to this action.
G. Executive Order 13045: Protection of Children From Environmental
Health Risks and Safety Risks
This action is not subject to Executive Order 13045 because it is
not economically significant as defined in Executive Order 12866, and
because the EPA does not believe the environmental health or safety
risks addressed by this action present a disproportionate risk to
children. This action's health and risk assessments are contained in
sections III and IV of this preamble and further documented in the risk
report, titled Residual Risk Assessment for Pulp Mill Combustion
Sources in Support of the December 2016 Risk and Technology Review
Proposed Rule, in the docket for this action.
H. Executive Order 13211: Actions Concerning Regulations That
Significantly Affect Energy Supply, Distribution, or Use
This action is not subject to Executive Order 13211, because it is
not a significant regulatory action under Executive Order 12866.
I. National Technology Transfer and Advancement Act (NTTAA) and 1 CFR
part 51
This action involves technical standards. While the EPA identified
ASTM D6784-02 (Reapproved 2008), ``Standard Test Method for Elemental,
Oxidized, Particle-Bound and Total Mercury Gas Generated from Coal-
Fired Stationary Sources (Ontario Hydro Method)'' as being potentially
applicable, the Agency does not propose to use it. The use of this
voluntary consensus standard would be impractical because this standard
is only acceptable as an alternative to the portion of Method 29 for
mercury, and mercury is not regulated under 40 CFR part 63, subpart MM.
J. Executive Order 12898: Federal Actions To Address Environmental
Justice in Minority Populations and Low-Income Populations
The EPA believes that this action will not have potential
disproportionately high and adverse human health or environmental
effects on minority populations, low-income populations, and/or
indigenous peoples, as specified in Executive Order 12898 (59 FR 7629,
February 16, 1994). The documentation for this decision is contained in
section IV.B of this preamble and the technical report titled Risk and
Technology Review--Analysis of Socio-Economic Factors for Populations
Living Near Pulp Mill Combustion Sources, which is located in the
public docket for this action.
We examined the potential for any EJ issues that might be
associated with the source category, by performing a demographic
analysis of the population close to the facilities. In this analysis,
we evaluated the distribution of HAP-related cancer and non-cancer
risks from the 40 CFR part 63, subpart MM source category across
different social, demographic, and economic groups within the
populations living near facilities identified as having the highest
risks. The methodology and the results of the demographic analyses are
included in a technical report, Risk and Technology Review--Analysis of
Socio-Economic Factors for Populations Living Near Pulp Mill Combustion
Sources, available in the docket for this action.
The results of the 40 CFR part 63, subpart MM source category
demographic analysis indicate that emissions from the source category
expose approximately 7,600 people to a cancer risk at or above 1-in-1
million and no one exposed to a chronic non-cancer TOSHI greater than
1. The specific demographic results indicate that the percentage of the
population potentially impacted by emissions is greater than its
corresponding national percentage for the minority population (33
percent for the source category compared to 28 percent nationwide), the
African American population (28 percent for the source category
compared to 13 percent nationwide) and for the population over age 25
without a high school diploma (18 percent for the source category
compared to 15 percent nationwide). The proximity results (irrespective
of risk) indicate that the population percentages for certain
demographic categories within 5 km of source category emissions are
greater than the corresponding national percentage for those same
demographics. The following demographic percentages for populations
residing within close proximity to facilities with pulp mill combustion
sources are higher than the corresponding nationwide percentage:
African American, ages 65 and up, over age 25 without a high school
diploma, and below the poverty level.
The risks due to HAP emissions from this source category are low
for all populations (e.g., inhalation cancer risks are less than 4-in-1
million for all populations and non-cancer hazard indices are less than
1). Furthermore, we do not expect this proposal to
[[Page 97085]]
achieve significant reductions in HAP emissions. Therefore, we conclude
that this proposal 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. However, this proposal, if
finalized, will provide additional benefits to these demographic groups
by improving the compliance, monitoring, and implementation of the
NESHAP.
List of Subjects in 40 CFR Part 63
Environmental protection, Administrative practice and procedure,
Air pollution control, Hazardous substances, Incorporation by
reference, Intergovernmental relations, Pulp and paper mills, Reporting
and recordkeeping requirements.
Dated: December 13, 2016.
Gina McCarthy,
Administrator.
For the reasons set out in the preamble, title 40, chapter I, part
63 of the Code of Federal Regulations is proposed to be amended as
follows:
PART 63--[AMENDED]
0
1. The authority citation for part 63 continues to read as follows:
Authority: 42 U.S.C. 7401 et seq.
Subpart A--[Amended]
0
2. Section 63.14 is amended by revising paragraph (m)(3) to read as
follows:
Sec. 63.14 Incorporations by reference.
* * * * *
(m) * * *
(3) EPA-454/R-98-015, Office of Air Quality Planning and Standards
(OAQPS), Fabric Filter Bag Leak Detection Guidance, September 1997, IBR
approved for Sec. Sec. 63.548(e), 63.864(e), 63.7525(j), 63.8450(e),
63.8600(e), and 63.11224(f).
Subpart MM--[Amended]
0
3. Section 63.860 is amended by revising paragraphs (b)(5) and (7) and
adding paragraph (d) to read as follows:
Sec. 63.860 Applicability and designation of affected source.
* * * * *
(b) * * *
(5) Each new or existing sulfite combustion unit located at a
sulfite pulp mill, except such existing units at Cosmo Specialty
Fibers' Cosmopolis, Washington facility (Emission Unit no. AP-10).
* * * * *
(7) The requirements of the alternative standard in Sec. 63.862(d)
apply to the hog fuel dryer at Cosmo Specialty Fibers' Cosmopolis,
Washington facility (Emission Unit no. HD-14).
* * * * *
(d) At all times, the owner or operator must operate and maintain
any affected source, including associated air pollution control
equipment and monitoring equipment, in a manner consistent with safety
and good air pollution control practices for minimizing emissions. The
general duty to minimize emissions does not require the owner or
operator to make any further efforts to reduce emissions if levels
required by the applicable standard have been achieved. Determination
of whether a source is operating in compliance with operation and
maintenance requirements will be based on information available to the
Administrator which may include, but is not limited to, monitoring
results, review of operation and maintenance procedures, review of
operation and maintenance records, and inspection of the source.
0
4. Section 63.861 is amended by:
0
a. Removing the definitions for ``Black liquor gasification'' and
``Startup'';
0
b. Revising the definitions for ``Hazardous air pollutants (HAP)
metals,'' ``Hog fuel dryer,'' ``Kraft recovery furnace,''
``Modification,'' ``Particulate matter (PM),'' ``Recovery furnace,''
``Semichemical combustion unit,'' ``Soda recovery furnace,'' and
``Total hydrocarbons (THC).''
The revisions read as follows:
Sec. 63.861 Definitions.
* * * * *
Hazardous air pollutants (HAP) metals means the sum of all
emissions of antimony, arsenic, beryllium, cadmium, chromium, cobalt,
lead, manganese, mercury, nickel, and selenium as measured by EPA
Method 29 (40 CFR part 60, appendix A-8).
Hog fuel dryer means the equipment that combusts fine particles of
wood waste (hog fuel) in a fluidized bed and directs the heated exhaust
stream to a rotary dryer containing wet hog fuel to be dried prior to
combustion in the hog fuel boiler at Cosmo Specialty Fibers'
Cosmopolis, Washington facility. The hog fuel dryer at Cosmo Specialty
Fibers' Cosmopolis, Washington facility is Emission Unit no. HD-14.
* * * * *
Kraft recovery furnace means a recovery furnace that is used to
burn black liquor produced by the kraft pulping process, as well as any
recovery furnace that burns black liquor produced from both the kraft
and semichemical pulping processes, and includes the direct contact
evaporator, if applicable.
* * * * *
Modification means, for the purposes of Sec.
63.862(a)(1)(ii)(E)(1), any physical change (excluding any routine part
replacement or maintenance) or operational change that is made to the
air pollution control device that could result in an increase in PM
emissions.
* * * * *
Particulate matter (PM) means total filterable particulate matter
as measured by EPA Method 5 (40 CFR part 60, appendix A-3), EPA Method
17 (Sec. 63.865(b)(1)) (40 CFR part 60, appendix A-6), or EPA Method
29 (40 CFR part 60, appendix A-8).
* * * * *
Recovery furnace means an enclosed combustion device where
concentrated black liquor produced by the kraft or soda pulping process
is burned to recover pulping chemicals and produce steam.
* * * * *
Semichemical combustion unit means any equipment used to combust or
pyrolyze black liquor at stand-alone semichemical pulp mills for the
purpose of chemical recovery.
* * * * *
Soda recovery furnace means a recovery furnace used to burn black
liquor produced by the soda pulping process and includes the direct
contact evaporator, if applicable.
* * * * *
Total hydrocarbons (THC) means the sum of organic compounds
measured as carbon using EPA Method 25A (40 CFR part 60, appendix A-7).
0
5. Section 63.862 is amended by revising paragraphs (c)(1) and (d) to
read as follows:
Sec. 63.862 Standards.
* * * * *
(c) Standards for gaseous organic HAP. (1) The owner or operator of
any new recovery furnace at a kraft or soda pulp mill must ensure that
the concentration or gaseous organic HAP, as measured by methanol,
discharged to the atmosphere is no greater than 0.012 kg/Mg (0.025 lb/
ton) of black liquor solids fired.
* * * * *
(d) Alternative standard. As an alternative to meeting the
requirements of paragraph (a)(2) of this section, the owner or operator
of the existing hog
[[Page 97086]]
fuel dryer at Cosmo Specialty Fibers' Cosmopolis, Washington facility
(Emission Unit no. HD-14) must ensure that the mass of PM in the
exhaust gases discharged to the atmosphere from the hog fuel dryer is
less than or equal to 4.535 kilograms per hour (kg/hr) (10.0 pounds per
hour (lb/hr)).
0
6. Section 63.863 is amended by revising paragraph (c) to read as
follows:
Sec. 63.863 Compliance dates.
* * * * *
(c) The owner or operator of an existing or new affected source or
process unit must comply with the revised requirements published on
[insert date of publication of final rule in the Federal Register] no
later than [insert date 1 year after date of publication of final rule
in the Federal Register], with the exception of the following:
(1) The first of the 5-year periodic performance tests must be
conducted within 3 years of the effective date of the revised
standards, by [insert date 3 years after date of publication of final
rule in the Federal Register], and thereafter before renewing the
facility's 40 CFR part 70 operating permit, but no longer than 5 years
following the previous performance test; and
(2) The date to submit performance test data through the ERT is
within 60 days after the date of completing each performance test.
0
7. Section 63.864 is revised to read as follows:
Sec. 63.864 Monitoring requirements.
(a)-(c) [Reserved]
(d) Continuous opacity monitoring system (COMS). The owner or
operator of each affected kraft or soda recovery furnace or lime kiln
equipped with an ESP must install, calibrate, maintain, and operate a
COMS in accordance with Performance Specification 1 (PS-1) in appendix
B to 40 CFR part 60 and the provisions in Sec. Sec. 63.6(h) and 63.8
and paragraphs (d)(1) through (5) of this section.
(1)-(2) [Reserved]
(3) As specified in Sec. 63.8(c)(4)(i), each COMS must complete a
minimum of one cycle of sampling and analyzing for each successive 10-
second period and one cycle of data recording for each successive 6-
minute period.
(4) As specified in Sec. 63.8(g)(2), each 6-minute COMS data
average must be calculated as the average of 36 or more data points,
equally spaced over each 6-minute period.
(5) As specified in Sec. 63.8(g)(4), each 6-minute COMS data
average should be rounded to the nearest 1-percent opacity.
(e) Continuous parameter monitoring system (CPMS). For each CPMS
required in this section, the owner or operator of each affected source
or process unit must meet the requirements in paragraphs (e)(1) through
(14) of this section.
(1) For any kraft or soda recovery furnace or lime kiln using an
ESP emission control device, the owner or operator must use the
continuous parameter monitoring devices specified in paragraphs
(e)(1)(i) and (ii) of this section to determine and record parameters
at least once every successive 15-minute period.
(i) A monitoring device for the continuous measurement of the
secondary voltage of each ESP collection field.
(ii) A monitoring device for the continuous measurement of the
secondary current of each ESP collection field.
(iii) Total secondary power may be calculated as the product of the
secondary voltage and secondary current measurements for each ESP
collection field and used to demonstrate compliance as an alternative
to the secondary voltage and secondary current measurements.
(2) For any kraft or soda recovery furnace or lime kiln using an
ESP followed by a wet scrubber, the owner or operator must use the
continuous parameter monitoring devices specified in paragraphs (e)(1)
and (10) of this section. The opacity monitoring system specified in
paragraph (d) of this section is not required for combination ESP/wet
scrubber control device systems.
(3)-(9) [Reserved]
(10) The owner or operator of each affected kraft or soda recovery
furnace, kraft or soda lime kiln, sulfite combustion unit, or kraft or
soda smelt dissolving tank equipped with a wet scrubber must install,
calibrate, maintain, and operate a CPMS that can be used to determine
and record the pressure drop across the scrubber and the scrubbing
liquid flow rate at least once every successive 15-minute period using
the procedures in Sec. 63.8(c), as well as the procedures in
paragraphs (e)(10)(i) and (ii) of this section:
(i) A monitoring device used for the continuous measurement of the
pressure drop of the gas stream across the scrubber must be certified
by the manufacturer to be accurate to within a gage pressure of 500 pascals (2 inches of water gage pressure); and
(ii) A monitoring device used for continuous measurement of the
scrubbing liquid flow rate must be certified by the manufacturer to be
accurate within 5 percent of the design scrubbing liquid
flow rate.
(iii) As an alternative to pressure drop measurement under
paragraph (e)(3)(i) of this section, a monitoring device for
measurement of fan amperage may be used for smelt dissolving tank
dynamic scrubbers that operate at ambient pressure or for low-energy
entrainment scrubbers where the fan speed does not vary.
(11) The owner or operator of each affected semichemical combustion
unit equipped with an RTO must install, calibrate, maintain, and
operate a CPMS that can be used to determine and record the operating
temperature of the RTO at least once every successive 15-minute period
using the procedures in Sec. 63.8(c). The monitor must compute and
record the operating temperature at the point of incineration of
effluent gases that are emitted using a temperature monitor accurate to
within 1 percent of the temperature being measured.
(12) The owner or operator of the affected hog fuel dryer at Cosmo
Specialty Fibers' Cosmopolis, Washington facility (Emission Unit no.
HD-14) must meet the requirements in paragraphs (e)(12)(i) through (xi)
of this section for each bag leak detection system.
(i) The owner or operator must install, calibrate, maintain, and
operate each triboelectric bag leak detection system according to EPA-
454/R-98-015, ``Fabric Filter Bag Leak Detection Guidance''
(incorporated by reference--see Sec. 63.14). This document is
available from the U.S. Environmental Protection Agency (U.S. EPA);
Office of Air Quality Planning and Standards; Emissions, Monitoring and
Analysis Division; Emission Measurement Center, MD-D205-02, Research
Triangle Park, NC 27711. This document is also available on the EPA
Technical Air Pollution Resources Emission Measurement Center Web page
under Continuous Emission Monitoring. The owner or operator must
install, calibrate, maintain, and operate other types of bag leak
detection systems in a manner consistent with the manufacturer's
written specifications and recommendations.
(ii) The bag leak detection system must be certified by the
manufacturer to be capable of detecting PM emissions at concentrations
of 10 milligrams per actual cubic meter (0.0044 grains per actual cubic
foot) or less.
(iii) The bag leak detection system sensor must provide an output
of relative PM loadings.
(iv) The bag leak detection system must be equipped with a device
to
[[Page 97087]]
continuously record the output signal from the sensor.
(v) The bag leak detection system must be equipped with an audible
alarm system that will sound automatically when an increase in relative
PM emissions over a preset level is detected. The alarm must be located
where it is easily heard by plant operating personnel.
(vi) For positive pressure fabric filter systems, a bag leak
detector must be installed in each baghouse compartment or cell.
(vii) For negative pressure or induced air fabric filters, the bag
leak detector must be installed downstream of the fabric filter.
(viii) Where multiple detectors are required, the system's
instrumentation and alarm may be shared among detectors.
(ix) The baseline output must be established by adjusting the range
and the averaging period of the device and establishing the alarm set
points and the alarm delay time according to section 5.0 of the
``Fabric Filter Bag Leak Detection Guidance'' (incorporated by
reference--see Sec. 63.14).
(x) Following initial adjustment of the system, the sensitivity or
range, averaging period, alarm set points, or alarm delay time may not
be adjusted except as detailed in the site-specific monitoring plan. In
no case may the sensitivity be increased by more than 100 percent or
decreased more than 50 percent over a 365-day period unless such
adjustment follows a complete fabric filter inspection which
demonstrates that the fabric filter is in good operating condition, as
defined in section 5.2 of the ``Fabric Filter Bag Leak Detection
Guidance,'' (incorporated by reference--see Sec. 63.14). Record each
adjustment.
(xi) The owner or operator must record the results of each
inspection, calibration, and validation check.
(13) The owner or operator of each affected source or process unit
that uses an ESP, wet scrubber, RTO, or fabric filter may monitor
alternative control device operating parameters subject to prior
written approval by the Administrator. The request for approval must
also include the manner in which the parameter operating limit is to be
set.
(14) The owner or operator of each affected source or process unit
that uses an air pollution control system other than an ESP, wet
scrubber, RTO, or fabric filter must provide to the Administrator an
alternative monitoring request that includes the site-specific
monitoring plan described in paragraph (a) of this section, a
description of the control device, test results verifying the
performance of the control device, the appropriate operating parameters
that will be monitored, how the operating limit is to be set, and the
frequency of measuring and recording to establish continuous compliance
with the standards. The alternative monitoring request is subject to
the Administrator's approval. The owner or operator of the affected
source or process unit must install, calibrate, operate, and maintain
the monitor(s) in accordance with the alternative monitoring request
approved by the Administrator. The owner or operator must include in
the information submitted to the Administrator proposed performance
specifications and quality assurance procedures for the monitors. The
Administrator may request further information and will approve
acceptable test methods and procedures. The owner or operator must
monitor the parameters as approved by the Administrator using the
methods and procedures in the alternative monitoring request.
(f) Data quality assurance. The owner or operator shall keep CMS
data quality assurance procedures consistent with the requirements in
Sec. 63.8(d)(1) and (2) on record for the life of the affected source
or until the affected source is no longer subject to the provisions of
this part, to be made available for inspection, upon request, by the
Administrator. If the performance evaluation plan in Sec. 63.8(d)(2)
is revised, the owner or operator shall keep previous (i.e.,
superseded) versions of the performance evaluation plan on record to be
made available for inspection, upon request, by the Administrator, for
a period of 5 years after each revision to the plan. The program of
corrective action should be included in the plan required under Sec.
63.8(d)(2).
(g) Gaseous organic HAP. The owner or operator of each affected
source or process unit complying with the gaseous organic HAP standard
of Sec. 63.862(c)(1) through the use of an NDCE recovery furnace
equipped with a dry ESP system is not required to conduct any
continuous monitoring to demonstrate compliance with the gaseous
organic HAP standard.
(h) Monitoring data. As specified in Sec. 63.8(g)(5), monitoring
data recorded during periods of unavoidable CMS breakdowns, out-of-
control periods, repairs, maintenance periods, calibration checks, and
zero (low-level) and high level adjustments must not be included in any
data average computed under this part.
(i) [Reserved]
(j) Determination of operating limits. (1) During the initial or
periodic performance test required in Sec. 63.865, the owner or
operator of any affected source or process unit must establish
operating limits for the monitoring parameters in paragraphs (e)(1) and
(2) and (e)(10) through (14) of this section, as appropriate; or
(2) The owner or operator may base operating limits on values
recorded during previous performance tests or conduct additional
performance tests for the specific purpose of establishing operating
limits, provided that test data used to establish the operating limits
are or have been obtained using the test methods required in this
subpart. The owner or operator of the affected source or process unit
must certify that all control techniques and processes have not been
modified subsequent to the testing upon which the data used to
establish the operating parameter limits were obtained.
(3) The owner or operator of an affected source or process unit may
establish expanded or replacement operating limits for the monitoring
parameters listed in paragraphs (e)(1) and (2) and (e)(10) through (14)
of this section and established in paragraph (j)(1) or (2) of this
section during subsequent performance tests using the test methods in
Sec. 63.865.
(4) The owner or operator of the affected source or process unit
must continuously monitor each parameter and determine the arithmetic
average value of each parameter during each performance test. Multiple
performance tests may be conducted to establish a range of parameter
values.
(5) New, expanded, or replacement operating limits for the
monitoring parameter values listed in paragraphs (e)(1) and (2) and
(e)(10) through (14) of this section should be determined as described
in paragraphs (j)(5)(i) through (iii) below.
(i) The owner or operator of an affected source or process unit
that uses a wet scrubber must set a minimum scrubber pressure drop
operating limit as the average of the pressure drop values associated
with each test run.
(A) For a smelt dissolving tank dynamic wet scrubber operating at
ambient pressure or for low-energy entrainment scrubbers where fan
speed does not vary, the minimum fan amperage operating limit must be
set as the average of the fan amperage values associated with each test
run.
(B) [Reserved]
(ii) The owner operator of an affected source equipped with an ESP
must set the minimum operating secondary current and secondary voltage
as the
[[Page 97088]]
average of the values associated with each test run.
(iii) The owner operator of an affected source equipped with an RTO
must set the minimum operating temperature of the RTO as the average of
the values associated with each test run.
(6) [Reserved]
(k) On-going compliance provisions. (1) Following the compliance
date, owners or operators of all affected sources or process units are
required to implement corrective action if the monitoring exceedances
in paragraphs (k)(1)(ii) through (vii) of this section occur during
times when spent pulping liquor or lime mud is fired (as applicable).
Corrective action can include completion of transient startup and
shutdown conditions as expediently as possible.
(i) [Reserved]
(ii) For a new or existing kraft or soda recovery furnace, kraft or
soda smelt dissolving tank, kraft or soda lime kiln, or sulfite
combustion unit equipped with a wet scrubber, when any 3-hour average
parameter value is below the minimum operating limit established in
paragraph (j) of this section, with the exception of pressure drop
during periods of startup and shutdown.
(iii) For a new or existing kraft or soda recovery furnace or lime
kiln equipped with an ESP followed by a wet scrubber, when:
(A) Any 3-hour average scrubber parameter value is below the
minimum operating limit established in paragraph (j) of this section,
with the exception of pressure drop during periods of startup and
shutdown; and
(B) Any 3-hour average ESP secondary voltage and secondary current
(or total secondary power) values are below the minimum operating
limits established during performance testing, with the exception of
secondary current (or total secondary power) during periods of startup
and shutdown.
(iv) For a new or existing semichemical combustion unit equipped
with an RTO, when any 1-hour average temperature falls below the
minimum temperature operating limit established in paragraph (j) of
this section.
(v) For the hog fuel dryer at Cosmo Specialty Fibers' Cosmopolis,
Washington facility (Emission Unit no. HD-14), when the bag leak
detection system alarm sounds.
(vi) For an affected source or process unit equipped with an ESP,
wet scrubber, RTO, or fabric filter and monitoring alternative
operating parameters established in paragraph (e)(13) of this section,
when any 3-hour average value does not meet the operating limit
established in paragraph (j) of this section.
(vii) For an affected source or process unit equipped with an
alternative air pollution control system and monitoring operating
parameters approved by the Administrator as established in paragraph
(e)(14) of this section, when any 3-hour average value does not meet
the operating limit established in paragraph (j) of this section.
(2) Following the compliance date, owners or operators of all
affected sources or process units are in violation of the standards of
Sec. 63.862 if the monitoring exceedances in paragraphs (k)(2)(i)
through (ix) of this section occur during times when spent pulping
liquor or lime mud is fired (as applicable):
(i) For a new or existing kraft or soda recovery furnace equipped
with an ESP, when opacity is greater than 20 percent for 2 percent or
more of the operating time within any semiannual period;
(ii) For a new or existing kraft or soda lime kiln equipped with an
ESP, when opacity is greater than 20 percent for 1 percent or more of
the operating time within any semiannual period;
(iii) For a new or existing kraft or soda recovery furnace or lime
kiln equipped with an ESP, when the ESP secondary voltage and secondary
current (or total secondary power) averaged over the semiannual period
are below the minimum operating limits established during the
performance test, with the exception of secondary current (or total
secondary power) during periods of startup and shutdown;
(iv) For a new or existing kraft or soda recovery furnace, kraft or
soda smelt dissolving tank, kraft or soda lime kiln, or sulfite
combustion unit equipped with a wet scrubber, when six or more 3-hour
average parameter values within any 6-month reporting period are below
the minimum operating limits established in paragraph (j) of this
section, with the exception of pressure drop during periods of startup
and shutdown;
(v) For a new or existing kraft or soda recovery furnace or lime
kiln equipped with an ESP followed by a wet scrubber, when:
(A) Six or more 3-hour average scrubber parameter values within any
6-month reporting period are outside the range of values established in
paragraph (j) of this section, with the exception of pressure drop
during periods of startup and shutdown; and
(B) Six or more 3-hour average ESP secondary voltage and secondary
current (or total secondary power) values within any 6-month reporting
period are below the minimum operating limits established during
performance testing, with the exception of secondary current (or total
secondary power) during periods of startup and shutdown;
(vi) For a new or existing semichemical combustion unit equipped
with an RTO, when any 3-hour average temperature falls below the
temperature established in paragraph (j) of this section;
(vii) For the hog fuel dryer at Cosmo Specialty Fibers' Cosmopolis,
Washington facility (Emission Unit no. HD-14), when corrective action
is not initiated within 1 hour of a bag leak detection system alarm and
the alarm is engaged for more than 5 percent of the total operating
time in a 6-month block reporting period. In calculating the operating
time fraction, if inspection of the fabric filter demonstrates that no
corrective action is required, no alarm time is counted; if corrective
action is required, each alarm is counted as a minimum of 1 hour; if
corrective action is not initiated within 1 hour, the alarm time is
counted as the actual amount of time taken to initiate corrective
action;
(viii) For an affected source or process unit equipped with an ESP,
wet scrubber, RTO, or fabric filter and monitoring alternative
operating parameters established in paragraph (e)(13) of this section,
when six or more 3-hour average values within any 6-month reporting
period do not meet the operating limits established in paragraph (j) of
this section; and
(ix) For an affected source or process unit equipped with an
alternative air pollution control system and monitoring operating
parameters approved by the Administrator as established in paragraph
(e)(14) of this section, when six or more 3-hour average values within
any 6-month reporting period do not meet the operating limits
established in paragraph (j) of this section.
(3) [Reserved]
0
8. Section 63.865 is amended by revising the introductory text and
paragraphs (b)(1) through (5), (c)(1), and (d)introductory text to read
as follows:
Sec. 63.865 Performance test requirements and test methods.
The owner or operator of each affected source or process unit
subject to the requirements of this subpart is required to conduct an
initial performance test and periodic performance tests using the test
methods and procedures listed in Sec. 63.7 and paragraph (b) of this
section. The owner or operator must conduct the first of the periodic
performance tests within 3 years of the effective date of the
[[Page 97089]]
revised standards and thereafter before renewing their 40 CFR part 70
operating permit but at intervals no longer than 5 years following the
previous performance test. Performance tests shall be conducted under
such conditions as the Administrator specifies to the owner or operator
based on representative performance of the affected source for the
period being tested. Representative conditions exclude periods of
startup and shutdown. The owner or operator may not conduct performance
tests during periods of malfunction. The owner or operator must record
the process information that is necessary to document operating
conditions during the test and include in such record an explanation to
support that such conditions represent normal operation. Upon request,
the owner or operator shall make available to the Administrator such
records as may be necessary to determine the conditions of performance
tests.
* * * * *
(b) * * *
(1) For purposes of determining the concentration or mass of PM
emitted from each kraft or soda recovery furnace, sulfite combustion
unit, smelt dissolving tank, lime kiln, or the hog fuel dryer at Cosmo
Specialty Fibers' Cosmopolis, Washington facility (Emission Unit no.
HD-14), Method 5 in appendix A-3 of 40 CFR part 60 or Method 29 in
appendix A-8 of 40 CFR part 60 must be used, except that Method 17 in
appendix A-6 of 40 CFR part 60 may be used in lieu of Method 5 or
Method 29 if a constant value of 0.009 g/dscm (0.004 gr/dscf) is added
to the results of Method 17, and the stack temperature is no greater
than 205 [deg]C (400 [deg]F). For Methods 5, 29, and 17, the sampling
time and sample volume for each run must be at least 60 minutes and
0.90 dscm (31.8 dscf), and water must be used as the cleanup solvent
instead of acetone in the sample recovery procedure.
(2) For sources complying with Sec. 63.862(a) or (b), the PM
concentration must be corrected to the appropriate oxygen concentration
using Equation 7 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TP30DE16.036
Where:
Ccorr = the measured concentration corrected for oxygen,
g/dscm (gr/dscf);
Cmeas = the measured concentration uncorrected for
oxygen, g/dscm (gr/dscf);
X = the corrected volumetric oxygen concentration (8 percent for
kraft or soda recovery furnaces and sulfite combustion units and 10
percent for kraft or soda lime kilns); and
Y = the measured average volumetric oxygen concentration.
(3) Method 3A or 3B in appendix A-2 of 40 CFR part 60 must be used
to determine the oxygen concentration. The voluntary consensus standard
ANSI/ASME PTC 19.10-1981--Part 10 (incorporated by reference--see Sec.
63.14) may be used as an alternative to using Method 3B. The gas sample
must be taken at the same time and at the same traverse points as the
particulate sample.
(4) For purposes of complying with of Sec. 63.862(a)(1)(ii)(A),
the volumetric gas flow rate must be corrected to the appropriate
oxygen concentration using Equation 8 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TP30DE16.037
Where:
Qcorr = the measured volumetric gas flow rate corrected
for oxygen, dscm/min (dscf/min).
Qmeas = the measured volumetric gas flow rate uncorrected
for oxygen, dscm/min (dscf/min).
Y = the measured average volumetric oxygen concentration.
X = the corrected volumetric oxygen concentration (8 percent for
kraft or soda recovery furnaces and 10 percent for kraft or soda
lime kilns).
(5)(i) For purposes of selecting sampling port location and number
of traverse points, Method 1 or 1A in appendix A-1 of 40 CFR part 60
must be used;
(ii) For purposes of determining stack gas velocity and volumetric
flow rate, Method 2, 2A, 2C, 2D, or 2F in appendix A-1 of 40 CFR part
60 or Method 2G in appendix A-2 of 40 CFR part 60 must be used;
(iii) For purposes of conducting gas analysis, Method 3, 3A, or 3B
in appendix A-2 of 40 CFR part 60 must be used. The voluntary consensus
standard ANSI/ASME PTC 19.10-1981--Part 10 (incorporated by reference--
see Sec. 63.14) may be used as an alternative to using Method 3B; and
(iv) For purposes of determining moisture content of stack gas,
Method 4 in appendix A-3 of 40 CFR part 60 must be used.
* * * * *
(c) * * *
(1) The owner or operator complying through the use of an NDCE
recovery furnace equipped with a dry ESP system is required to conduct
periodic performance testing using Method 308 in appendix A of this
part, as well as the methods listed in paragraphs (b)(5)(i) through
(iv) of this section to demonstrate compliance with the gaseous organic
HAP standard. The requirements and equations in paragraph (b)(2) of
this section must be met and utilized, respectively.
* * * * *
(d) The owner or operator seeking to determine compliance with the
gaseous organic HAP standards in Sec. 63.862(c)(2) for semichemical
combustion units must use Method 25A in appendix A-7 of 40 CFR part 60,
as well as the methods listed in paragraphs (b)(5)(i) through (iv) of
this section. The sampling time for each Method 25A run must be at
least 60 minutes. The calibration gas for each Method 25A run must be
propane.
* * * * *
0
9. Section 63.866 is revised to read as follows:
Sec. 63.866 Recordkeeping requirements.
(a) [Reserved]
(b) The owner or operator of an affected source or process unit
must maintain records of any occurrence when corrective action is
required under Sec. 63.864(k)(1), and when a violation is noted under
Sec. 63.864(k)(2). Record the time corrective action was initiated and
completed, and the corrective action taken.
(c) In addition to the general records required by Sec.
63.10(b)(2)(iii) and (vi) through (xiv), the owner or operator must
maintain records of the information in paragraphs (c)(1) through (8) of
this section:
(1) Records of black liquor solids firing rates in units of Mg/d or
ton/d for
[[Page 97090]]
all recovery furnaces and semichemical combustion units;
(2) Records of CaO production rates in units of Mg/d or ton/d for
all lime kilns;
(3) Records of parameter monitoring data required under Sec.
63.864, including any period when the operating parameter levels were
inconsistent with the levels established during the performance test;
(4) Records and documentation of supporting calculations for
compliance determinations made under Sec. 63.865(a) through (d);
(5) Records of parameter operating limits established for each
affected source or process unit;
(6) Records certifying that an NDCE recovery furnace equipped with
a dry ESP system is used to comply with the gaseous organic HAP
standard in Sec. 63.862(c)(1);
(7) For the bag leak detection system on the hog fuel dryer fabric
filter at Cosmo Specialty Fibers' Cosmopolis, Washington facility
(Emission Unit no. HD-14), records of each alarm, the time of the
alarm, the time corrective action was initiated and completed, and a
brief description of the cause of the alarm and the corrective action
taken; and
(8) Records of the date, time, and duration of each startup and/or
shutdown period, recording the periods when the affected source was
subject to the standard applicable to startup and shutdown.
(d)(1) In the event that an affected unit fails to meet an
applicable standard, including any emission limit or operating limit,
record the number of failures. For each failure record the date, start
time, and duration of each failure along with a brief explanation of
the cause.
(2) For each failure to meet an applicable standard, record and
retain a list of the affected sources or equipment, an estimate of the
quantity of each regulated pollutant emitted over any emission limit
and a description of the method used to estimate the emissions.
(3) Record actions taken to minimize emissions in accordance with
Sec. 63.860(d) and any corrective actions taken to return the affected
unit to its normal or usual manner of operation.
0
10. Section 63.867 is revised to read as follows:
Sec. 63.867 Reporting requirements.
(a) Notifications. (1) The owner or operator of any affected source
or process unit must submit the applicable notifications from subpart A
of this part, as specified in Table 1 of this subpart.
(2) [Reserved]
(3) In addition to the requirements in subpart A of this part, the
owner or operator of the hog fuel dryer at Cosmo Specialty Fibers'
Cosmopolis, Washington, facility (Emission Unit no. HD-14) must include
analysis and supporting documentation demonstrating conformance with
EPA guidance and specifications for bag leak detection systems in Sec.
63.864(e)(12) in the Notification of Compliance Status.
(b) Additional reporting requirements for HAP metals standards. (1)
Any owner or operator of a group of process units in a chemical
recovery system at a mill complying with the PM emissions limits in
Sec. 63.862(a)(1)(ii) must submit the PM emissions limits determined
in Sec. 63.865(a) for each affected kraft or soda recovery furnace,
smelt dissolving tank, and lime kiln to the Administrator for approval.
The emissions limits must be submitted as part of the notification of
compliance status required under subpart A of this part.
(2) Any owner or operator of a group of process units in a chemical
recovery system at a mill complying with the PM emissions limits in
Sec. 63.862(a)(1)(ii) must submit the calculations and supporting
documentation used in Sec. 63.865(a)(1) and (2) to the Administrator
as part of the notification of compliance status required under subpart
A of this part.
(3) After the Administrator has approved the emissions limits for
any process unit, the owner or operator of a process unit must notify
the Administrator before any of the actions in paragraphs (b)(3)(i)
through (iv) of this section are taken:
(i) The air pollution control system for any process unit is
modified or replaced;
(ii) Any kraft or soda recovery furnace, smelt dissolving tank, or
lime kiln in a chemical recovery system at a kraft or soda pulp mill
complying with the PM emissions limits in Sec. 63.862(a)(1)(ii) is
shut down for more than 60 consecutive days;
(iii) A continuous monitoring parameter or the value or range of
values of a continuous monitoring parameter for any process unit is
changed; or
(iv) The black liquor solids firing rate for any kraft or soda
recovery furnace during any 24-hour averaging period is increased by
more than 10 percent above the level measured during the most recent
performance test.
(4) An owner or operator of a group of process units in a chemical
recovery system at a mill complying with the PM emissions limits in
Sec. 63.862(a)(1)(ii) and seeking to perform the actions in paragraph
(b)(3)(i) or (ii) of this section must recalculate the overall PM
emissions limit for the group of process units and resubmit the
documentation required in paragraph (b)(2) of this section to the
Administrator. All modified PM emissions limits are subject to approval
by the Administrator.
(c) Excess emissions report. The owner or operator must submit
semiannual excess emissions reports containing the information
specified in paragraphs (c)(1) through (5) of this section. The owner
or operator must submit semiannual excess emission reports following
the procedure specified in paragraph (d)(2) of this section.
(1) If the total duration of excess emissions or process control
system parameter exceedances for the reporting period is less than 1-
percent of the total reporting period operating time, and CMS downtime
is less than 5-percent of the total reporting period operating time,
only the summary report is required to be submitted in accordance with
Sec. 63.10(e)(3)(vii). This report will be titled ``Summary Report--
Gaseous and Opacity Excess Emissions and Continuous Monitoring System
Performance'' in accordance with Sec. 63.10(e)(3)(vi) and must contain
the information required in Sec. 63.10(e)(3), as specified in
paragraphs (c)(1)(i) through (x) of this section. When no exceedances
of parameters have occurred, the owner or operator must submit the
summary report stating that no excess emissions occurred during the
reporting period. In addition to a statement verifying that no excess
emissions occurred during the reporting period, this report must
contain the information required in Sec. 63.10(e)(3) only as specified
in paragraphs (c)(1)(i) through (x) of this section. The summary report
must be submitted following the procedure specified in paragraph (d)(2)
of this section.
(i) The company name and address and name of the affected facility.
(ii) Beginning and ending dates of the reporting period.
(iii) An identification of each process unit with the corresponding
air pollution control device, being included in the semiannual report,
including the pollutants monitored at each process unit, and the total
operating time for each process unit.
(iv) An identification of the applicable emission limits, operating
parameter limits, and averaging times.
(v) An identification of the monitoring equipment used for each
process unit and the corresponding model number.
(vi) Date of the last CMS certification or audit.
(vii) An emission data summary, including the total duration of
excess
[[Page 97091]]
emissions (recorded in minutes for opacity and hours for gases), the
duration of excess emissions expressed as a percent of operating time,
and reason for the excess emissions (e.g., startup/shutdown, control
equipment problems, other known reasons, or other unknown reasons).
(viii) A CMS performance summary, including the total duration of
CMS downtime, the duration of downtime expressed as a percent of
operating time, and reason for the downtime (e.g., monitoring equipment
malfunction, non-monitoring equipment malfunction, quality assurance,
quality control calibrations, other known causes, or other unknown
causes).
(ix) A description of changes to CMS, processes, or controls since
last reporting period.
(x) A certification by a certifying official of truth, accuracy and
completeness. This will state that, based on information and belief
formed after reasonable inquiry, the statements and information in the
document are true, accurate, and complete.
(2) [Reserved]
(3) If measured parameters meet any of the conditions specified in
Sec. 63.864(k)(1) or (2), the owner or operator of the affected source
must submit a semiannual report describing the excess emissions that
occurred. If the total duration of monitoring exceedances for the
reporting period is 1-percent or greater of the total reporting period
operating time, or the total CMS downtime for the reporting period is
5-percent or greater of the total reporting period operating time, or
any violations according to Sec. 63.864(k)(2) occurred, information
from both the summary report and the excess emissions and continuous
monitoring system performance report must be submitted. This report
will be titled ``Excess Emissions and Continuous Monitoring System
Performance Report'' and must contain the information specified in
paragraphs (c)(1)(i) through (x) of this section, in addition to the
information required in Sec. 63.10(c)(5) through (14), as specified in
paragraphs (c)(3)(i) through (vi) of this section. Reporting monitoring
exceedances does not constitute a violation of the applicable standard
unless the criteria in Sec. 63.864(k)(2) are reached.
(i) An identification of the date and time identifying each period
during which the CMS was inoperative except for zero (low-level) and
high-level checks.
(ii) An identification of the date and time identifying each period
during which the CMS was out of control, as defined in Sec.
63.8(c)(7).
(iii) The specific identification of each period of excess
emissions and parameter monitoring exceedances as described in
paragraphs (c)(3)(iii)(A) through (C) of this section.
(A) For opacity:
(1) The total number of 6-minute averages in the reporting period
(excluding process unit downtime).
(2) The number of 6-minute averages in the reporting period removed
due to invalid readings.
(3) The number of 6-minute averages in the reporting period that
exceeded the 20-percent opacity limit.
(4) The percent of 6-minute averages in the reporting period that
exceed the 20-percent opacity limit.
(5) An identification of each exceedance by start time, date, and
cause of exceedance (including startup/shutdown, control equipment
problems, other known reasons, or other unknown reasons).
(B) For ESP operating parameters:
(1) The type of operating parameters monitored for compliance
(total secondary power, or secondary voltage and secondary current).
(2) The operating limits established during the performance test.
(3) For systems only controlled with an ESP, the operating
parameters averaged over the semiannual reporting period.
(4) For combined ESP and wet scrubber control systems, the number
of 3-hour ESP and wet scrubber parameter averages below the minimum
operating limit established during the performance test.
(5) An identification of each exceedance by start time, date, and
cause of exceedance (including startup/shutdown, control equipment
problems, other known reasons, or other unknown reasons).
(C) For wet scrubber operating parameters:
(1) The operating limits established during the performance test
for scrubbing liquid flow rate and pressure drop across the scrubber
(or fan amperage if used for smelt dissolving tank scrubbers).
(2) The number of 3-hour wet scrubber parameter averages below the
minimum operating limit established during the performance test, if
applicable.
(3) An identification of each exceedance by start time, date, and
cause of exceedance (including startup/shutdown, control equipment
problems, other known reasons, or other unknown reasons).
(D) For RTO operating temperature:
(1) The operating limit established during the performance test.
(2) The number of 1-hour and 3-hour temperature averages below the
minimum operating limit established during the performance test.
(3) An identification of each exceedance by start time, date, and
cause of exceedance including startup/shutdown, control equipment
problems, other known reasons, or other unknown reasons).
(iv) The nature and cause of any malfunction (if known).
(v) The corrective action taken or preventative measures adopted.
(vi) The nature of repairs and adjustments to the CMS that was
inoperative or out of control.
(4) If a source fails to meet an applicable standard, report such
events in the semiannual excess emissions report. Report the number of
failures to meet an applicable standard. For each instance, report the
date, time and duration of each failure. For each failure the report
must include a list of the affected sources or equipment, an estimate
of the quantity of each regulated pollutant emitted over any emission
limit, and a description of the method used to estimate the emissions.
(5) The owner or operator of an affected source or process unit
subject to the requirements of this subpart and subpart S of this part
may combine excess emissions and/or summary reports for the mill.
(d) Electronic reporting. (1) Within 60 days after the date of
completing each performance test (as defined in Sec. 63.2) required by
this subpart, the owner or operator must submit the results of the
performance test following the procedure specified in either paragraph
(d)(1)(i) or (ii) of this section.
(i) For data collected using test methods supported by the EPA's
Electronic Reporting Tool (ERT) as listed on the EPA's ERT Web site
(https://www.epa.gov/electronic-reporting-air-emissions/electronic-reporting-tool-ert) at the time of the test, the owner or operator must
submit the results of the performance test to the EPA via the
Compliance and Emissions Data Reporting Interface (CEDRI). (CEDRI can
be accessed through the EPA's Central Data Exchange (CDX) (https://cdx.epa.gov/).) Performance test data must be submitted in a file
format generated through the use of the EPA's ERT or an alternate
electronic file format consistent with the extensible markup language
(XML) schema listed on the EPA's ERT Web site. If the owner or operator
claims that some of the performance test information being submitted is
confidential business information (CBI), the owner or operator must
submit a complete file generated
[[Page 97092]]
through the use of the EPA's ERT or an alternate electronic file
consistent with the XML schema listed on the EPA's ERT Web site,
including information claimed to be CBI, on a compact disc, flash
drive, or other commonly used electronic storage media to the EPA. The
electronic media must be clearly marked as CBI and mailed to U.S. EPA/
OAPQS/CORE CBI Office, Attention: Group Leader, Measurement Policy
Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same ERT or
alternate file with the CBI omitted must be submitted to the EPA via
the EPA's CDX as described earlier in this paragraph (d)(1)(i).
(ii) For data collected using test methods that are not supported
by the EPA's ERT as listed on the EPA's ERT Web site at the time of the
test, the owner or operator must attach an electronic copy of the
complete performance test report containing the methods not included in
the ERT in the attachment module of the ERT in portable document format
(PDF) and submit the results of the performance test to the EPA via
CEDRI.
(2) The owner or operator must submit notification and semiannual
reports to the EPA via the CEDRI. (CEDRI can be accessed through the
EPA's CDX (https://cdx.epa.gov).) The owner or operator must use the
appropriate electronic report in CEDRI for this subpart or an
alternative electronic file format consistent with the XML schema
listed on the CEDRI Web site (https://www.epa.gov/electronic-reporting-air-emissions/compliance-and-emissions-data-reporting-interface-cedri).
If neither the reporting form nor the spreadsheet template specific to
this subpart are available in CEDRI at the time that the report is due,
you must upload an electronic copy of the report in CEDRI. Once the
form or spreadsheet template has been available in CEDRI for at least
90 calendar days, you must begin submitting all subsequent reports via
CEDRI using the form or spreadsheet template. The reports must be
submitted by the deadlines specified in this subpart, regardless of the
method in which the reports are submitted.
0
11. Section 63.868 is amended by revising paragraphs (b)(2) through (4)
to read as follows:
Sec. 63.868 Delegation of authority.
* * * * *
(b) * * *
(2) Approval of a major change to test method under Sec.
63.7(e)(2)(ii) and (f) and as defined in Sec. 63.90.
(3) Approval of a major change to monitoring under Sec. 63.8(f)
and as defined in Sec. 63.90.
(4) Approval of a major change to recordkeeping/reporting under
Sec. 63.10(f) and as defined in Sec. 63.90.
0
12. Table 1 to subpart MM of part 63 is revised to read as follows:
Table 1 to Subpart MM of Part 63--General Provisions Applicability to Subpart MM
----------------------------------------------------------------------------------------------------------------
General provisions reference Summary of requirements Applies to subpart MM Explanation
----------------------------------------------------------------------------------------------------------------
63.1(a)(1)........................ General applicability of Yes.................. Additional terms defined
the General Provisions. in Sec. 63.861; when
overlap between subparts
A and MM of this part,
subpart MM takes
precedence.
63.1(a)(2)-(14)................... General applicability of Yes..................
the General Provisions.
63.1(b)(1)........................ Initial applicability No................... Subpart MM specifies the
determination. applicability in Sec.
63.860.
63.1(b)(2)........................ Title V operating permit-- Yes.................. All major affected
see 40 CFR part 70. sources are required to
obtain a title V permit.
63.1(b)(3)........................ Record of the No................... All affected sources are
applicability subject to subpart MM
determination. according to the
applicability definition
of subpart MM.
63.1(c)(1)........................ Applicability of subpart A Yes.................. Subpart MM clarifies the
of this part after a applicability of each
relevant standard has paragraph of subpart A
been set. of this part to sources
subject to subpart MM.
63.1(c)(2)........................ Title V permit requirement Yes.................. All major affected
sources are required to
obtain a title V permit.
There are no area
sources in the pulp and
paper mill source
category.
63.1(c)(3)........................ [Reserved]................ No...................
63.1(c)(4)........................ Requirements for existing Yes..................
source that obtains an
extension of compliance.
63.1(c)(5)........................ Notification requirements Yes..................
for an area source that
increases HAP emissions
to major source levels.
63.1(d)........................... [Reserved]................ No...................
63.1(e)........................... Applicability of permit Yes..................
program before a relevant
standard has been set.
63.2.............................. Definitions............... Yes.................. Additional terms defined
in Sec. 63.861; when
overlap between subparts
A and MM of this part
occurs, subpart MM takes
precedence.
63.3.............................. Units and abbreviations... Yes..................
63.4.............................. Prohibited activities and Yes..................
circumvention.
63.5(a)........................... Construction and Yes..................
reconstruction--applicabi
lity.
63.5(b)(1)........................ Upon construction, Yes..................
relevant standards for
new sources.
63.5(b)(2)........................ [Reserved]................ No...................
63.5(b)(3)........................ New construction/ Yes..................
reconstruction.
63.5(b)(4)........................ Construction/ Yes..................
reconstruction
notification.
63.5(b)(5)........................ Construction/ Yes..................
reconstruction compliance.
63.5(b)(6)........................ Equipment addition or Yes..................
process change.
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63.5(c)........................... [Reserved]................ No...................
63.5(d)........................... Application for approval Yes..................
of construction/
reconstruction.
63.5(e)........................... Construction/ Yes..................
reconstruction approval.
63.5(f)........................... Construction/ Yes..................
reconstruction approval
based on prior State
preconstruction review.
63.6(a)(1)........................ Compliance with standards Yes..................
and maintenance
requirements--applicabili
ty.
63.6(a)(2)........................ Requirements for area Yes..................
source that increases
emissions to become major.
63.6(b)........................... Compliance dates for new Yes..................
and reconstructed sources.
63.6(c)........................... Compliance dates for Yes, except for Subpart MM specifically
existing sources. sources granted stipulates the
extensions under compliance schedule for
Sec. 63.863(c). existing sources.
63.6(d)........................... [Reserved]................ No...................
63.6(e)(1)(i)..................... General duty to minimize No................... See Sec. 63.860(d) for
emissions. general duty
requirement.
63.6(e)(1)(ii).................... Requirement to correct No...................
malfunctions ASAP.
63.6(e)(1)(iii)................... Operation and maintenance Yes..................
requirements enforceable
independent of emissions
limitations.
63.6(e)(2)........................ [Reserved]................ No...................
63.6(e)(3)........................ Startup, shutdown, and No...................
malfunction plan (SSMP).
63.6(f)(1)........................ Compliance with nonopacity No...................
emissions standards
except during SSM.
63.6(f)(2)-(3).................... Methods for determining Yes..................
compliance with
nonopacity emissions
standards.
63.6(g)........................... Compliance with Yes..................
alternative nonopacity
emissions standards.
63.6(h)(1)........................ Compliance with opacity No...................
and visible emissions
(VE) standards except
during SSM.
63.6(h)(2)-(9).................... Compliance with opacity Yes.................. Subpart MM does not
and VE standards. contain any opacity or
VE standards; however,
Sec. 63.864 specifies
opacity monitoring
requirements.
63.6(i)........................... Extension of compliance Yes..................
with emission standards.
63.6(j)........................... Exemption from compliance Yes..................
with emissions standards.
63.7(a)(1)........................ Performance testing Yes..................
requirements--applicabili
ty.
63.7(a)(2)........................ Performance test dates.... Yes..................
63.7(a)(3)........................ Performance test requests Yes..................
by Administrator under
CAA section 114.
63.7(a)(4)........................ Notification of delay in Yes..................
performance testing due
to force majeure.
63.7(b)(1)........................ Notification of Yes..................
performance test.
63.7(b)(2)........................ Notification of delay in Yes..................
conducting a scheduled
performance test.
63.7(c)........................... Quality assurance program. Yes..................
63.7(d)........................... Performance testing Yes..................
facilities.
63.7(e)(1)........................ Conduct of performance No................... See Sec. 63.865.
tests.
63.7(e)(2)-(3).................... Conduct of performance Yes..................
tests.
63.7(e)(4)........................ Testing under section 114. Yes..................
63.7(f)........................... Use of an alternative test Yes..................
method.
63.7(g)........................... Data analysis, Yes..................
recordkeeping, and
reporting.
63.7(h)........................... Waiver of performance Yes.................. Sec. 63.865(c)(1)
tests. specifies the only
exemption from
performance testing
allowed under subpart
MM.
63.8(a)(1)........................ Monitoring requirements-- Yes.................. See Sec. 63.864.
applicability.
63.8(a)(2)........................ Performance Specifications Yes..................
63.8(a)(3)........................ [Reserved]................ No...................
63.8(a)(4)........................ Monitoring with flares.... No................... The use of flares to meet
the standards in subpart
MM is not anticipated.
63.8(b)(1)........................ Conduct of monitoring..... Yes.................. See Sec. 63.864.
63.8(b)(2)-(3).................... Specific requirements for Yes..................
installing and reporting
on monitoring systems.
63.8(c)(1)........................ Operation and maintenance Yes.................. See Sec. 63.864.
of CMS.
63.8(c)(1)(i)..................... General duty to minimize No...................
emissions and CMS
operation.
[[Page 97094]]
63.8(c)(1)(ii).................... Reporting requirements for Yes..................
SSM when action not
described in SSMP.
63.8(c)(1)(iii)................... Requirement to develop SSM No...................
plan for CMS.
63.8(c)(2)-(3).................... Monitoring system Yes..................
installation.
63.8(c)(4)........................ CMS requirements.......... Yes..................
63.8(c)(5)........................ Continuous opacity Yes..................
monitoring system (COMS)
minimum procedures.
63.8(c)(6)........................ Zero and high level Yes..................
calibration check
requirements.
63.8(c)(7)-(8).................... Out-of-control periods.... Yes..................
63.8(d)(1)-(2).................... CMS quality control Yes.................. See Sec. 63.864.
program.
63.8(d)(3)........................ Written procedures for CMS No................... See Sec. 63.864(f).
63.8(e)(1)........................ Performance evaluation of Yes..................
CMS.
63.8(e)(2)........................ Notification of Yes..................
performance evaluation.
63.8(e)(3)........................ Submission of site- Yes..................
specific performance
evaluation test plan.
63.8(e)(4)........................ Conduct of performance Yes..................
evaluation and
performance evaluation
dates.
63.8(e)(5)........................ Reporting performance Yes..................
evaluation results.
63.8(f)........................... Use of an alternative Yes..................
monitoring method.
63.8(g)........................... Reduction of monitoring Yes..................
data.
63.9(a)........................... Notification requirements-- Yes..................
applicability and general
information.
63.9(b)........................... Initial notifications..... Yes..................
63.9(c)........................... Request for extension of Yes..................
compliance.
63.9(d)........................... Notification that source Yes..................
subject to special
compliance requirements.
63.9(e)........................... Notification of Yes..................
performance test.
63.9(f)........................... Notification of opacity Yes.................. Subpart MM does not
and VE observations. contain any opacity or
VE standards; however,
Sec. 63.864 specifies
opacity monitoring
requirements.
63.9(g)(1)........................ Additional notification Yes..................
requirements for sources
with CMS.
63.9(g)(2)........................ Notification of compliance Yes.................. Subpart MM does not
with opacity emissions contain any opacity or
standard. VE emissions standards;
however, Sec. 63.864
specifies opacity
monitoring requirements.
63.9(g)(3)........................ Notification that Yes..................
criterion to continue use
of alternative to
relative accuracy testing
has been exceeded.
63.9(h)........................... Notification of compliance Yes..................
status.
63.9(i)........................... Adjustment to time periods Yes..................
or postmark deadlines for
submittal and review of
required communications.
63.9(j)........................... Change in information Yes..................
already provided.
63.10(a).......................... Recordkeeping Yes.................. See Sec. 63.866.
requirements--applicabili
ty and general
information.
63.10(b)(1)....................... Records retention......... Yes..................
63.10(b)(2)(i).................... Recordkeeping of No................... See Sec. 63.866(c)(8)
occurrence and duration for recordkeeping of the
of startups and shutdowns. date, time, and duration
of each startup and/or
shutdown period.
63.10(b)(2)(ii)................... Recordkeeping of failures No................... See Sec. 63.866(d) for
to meet a standard. recordkeeping of (1)
date, time and duration;
(2) listing of affected
source or equipment, and
an estimate of the
quantity of each
regulated pollutant
emitted over the
standard; and (3)
actions to minimize
emissions and correct
the failure.
63.10(b)(2)(iii).................. Maintenance records....... Yes..................
63.10(b)(2)(iv)-(v)............... Actions taken to minimize No...................
emissions during SSM.
63.10(b)(2)(vi)................... Recordkeeping for CMS Yes..................
malfunctions.
63.10(b)(2)(vii)-(xiv)............ Other CMS requirements.... Yes..................
63.10(b)(3)....................... Records retention for Yes.................. Applicability
sources not subject to requirements are given
relevant standard. in Sec. 63.860.
63.10(c)(1)-(14).................. Additional recordkeeping Yes..................
requirements for sources
with CMS..
63.10(c)(15)...................... Use of SSM plan........... No...................
63.10(d)(1)....................... General reporting Yes..................
requirements.
63.10(d)(2)....................... Reporting results of Yes..................
performance tests.
[[Page 97095]]
63.10(d)(3)....................... Reporting results of Yes.................. Subpart MM does not
opacity or VE include any opacity or
observations. VE standards; however,
Sec. 63.864 specifies
opacity monitoring
requirements.
63.10(d)(4)....................... Progress reports.......... Yes..................
63.10(d)(5)(i).................... Periodic startup, No................... See Sec. 63.867(c)(3)
shutdown, and malfunction for malfunction
reports. reporting requirements.
63.10(d)(5)(ii)................... Immediate startup, No................... See Sec. 63.867(c)(3)
shutdown, and malfunction for malfunction
reports. reporting requirements.
63.10(e).......................... Additional reporting Yes..................
requirements for sources
with CMS.
63.10(f).......................... Waiver of recordkeeping Yes..................
and reporting
requirements.
63.11............................. Control device No................... The use of flares to meet
requirements for flares. the standards in subpart
MM is not anticipated.
63.12............................. State authority and Yes..................
delegations.
63.13............................. Addresses of State air Yes..................
pollution control
agencies and EPA Regional
Offices.
63.14............................. Incorporations by Yes..................
reference.
63.15............................. Availability of Yes..................
information and
confidentiality.
63.16............................. Requirements for Yes..................
Performance Track member
facilities.
----------------------------------------------------------------------------------------------------------------
[FR Doc. 2016-30758 Filed 12-29-16; 8:45 am]
BILLING CODE 6560-50-P