[Federal Register Volume 86, Number 221 (Friday, November 19, 2021)]
[Rules and Regulations]
[Pages 66045-66096]
From the Federal Register Online via the Government Publishing Office [www.gpo.gov]
[FR Doc No: 2021-24100]
[[Page 66045]]
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ENVIRONMENTAL PROTECTION AGENCY
40 CFR Part 63
[EPA-HQ-OAR-2020-0148; FRL-7527-02-OAR]
RIN 2060-AU67
National Emission Standards for Hazardous Air Pollutants:
Refractory Products Manufacturing Residual Risk and Technology Review
AGENCY: Environmental Protection Agency (EPA).
ACTION: Final rule.
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SUMMARY: This action finalizes the residual risk and technology review
(RTR) conducted for the Refractory Products Manufacturing source
category regulated under national emission standards for hazardous air
pollutants (NESHAP). The Environmental Protection Agency (EPA) found
the risks due to emissions of air toxics from this source category to
be acceptable and that the standards provide an ample margin of safety
to protect public health. As a result, the Agency is making no
revisions to the emission limits for this source category based on the
residual risk. In our technology review, after reviewing developments
in practices, processes, and control technologies, the EPA determined
that no revisions to the numeric emission limits is necessary. However,
the EPA is revising certain work practice provisions based on the
technology review. These final amendments also include new provisions
for certain hazardous air pollutants (HAP) and a revision of the
alternative fuel provisions. In addition, the Agency is taking final
action on the proposed amendments for the source category to address
emissions during periods of startup, shutdown, and malfunction (SSM);
emissions during periods of scheduled maintenance; electronic reporting
of notification of compliance status (NOCS) reports, performance test
results, and performance evaluation results; the addition of test
methods and guidance materials; updates to several test methods; and
other miscellaneous clarifying and technical corrections.
DATES: This final rule is effective on November 19, 2021. The
incorporation by reference (IBR) of certain publications listed in the
rule is approved by the Director of the Federal Register as of November
19, 2021.
ADDRESSES: The U.S. Environmental Protection Agency (EPA) has
established a docket for this action under Docket ID No. EPA-HQ-OAR-
2020-0148. All documents in the docket are listed on the https://www.regulations.gov/ website. Although listed, some information is not
publicly available, e.g., Confidential Business Information 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 form. Publicly
available docket materials are available either electronically through
https://www.regulations.gov/, or in hard copy at the EPA Docket Center,
WJC West Building, Room Number 3334, 1301 Constitution Ave. NW,
Washington, DC. The Public Reading Room hours of operation are 8:30
a.m. to 4:30 p.m. Eastern Standard Time (EST), Monday through Friday.
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.
FOR FURTHER INFORMATION CONTACT: For questions about this final action,
contact Ms. Paula Deselich Hirtz, Minerals and Manufacturing Group,
Sector Policies and Programs Division (D243-04), Office of Air Quality
Planning and Standards, U.S. Environmental Protection Agency, Research
Triangle Park, North Carolina 27711; telephone number: (919) 541-2618;
fax number: (919) 541-4991; and email address: [email protected]. For
specific information regarding the risk modeling methodology, contact
Mr. Chris Sarsony, Health and Environmental Impacts Division (C539-02),
Office of Air Quality Planning and Standards, U.S. Environmental
Protection Agency, Research Triangle Park, North Carolina 27711;
telephone number: (919) 541-4843; fax number: (919) 541-0840; and email
address: [email protected].
SUPPLEMENTARY INFORMATION: Preamble acronyms and abbreviations. The
Agency uses 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 below. Also, throughout this preamble the terms ``we,''
``us,'' or ``our'' mean the EPA.
BLD bag leak detection
CAA Clean Air Act
CRA Congressional Review Act
CDX Central Data Exchange
CEDRI Compliance and Emissions Data Reporting Interface
EJ Environmental Justice
EPA Environmental Protection Agency
ERT Electronic Reporting Tool
FTIR Fourier Transform Infrared
HAP hazardous air pollutants(s)
HQ hazard quotient
IBR incorporation by reference
ICR Information Collection Request
lb/hr pounds per hour
MACT maximum achievable control technology
HCl hydrogen chloride
HF hydrogen fluoride
Hg mercury
MIR maximum individual risk
NAAQS National Ambient Air Quality Standards
NACWA National Association of Clean Water Agencies
NEI National Emission Inventory
NESHAP national emission standards for hazardous air pollutants
NOCS notification of compliance status
OM&M operation, maintenance, and monitoring
OPL operating parameter limit
PDF portable document format
PM Particulate matter
POM polycyclic organic matter
ppmvd per million by volume, dry basis
RFA Regulatory Flexibility Act
RTO regenerative thermal oxidizer
RTR risk and technology review
SSI Sewage Sludge Incinerator
SSM startup, shutdown, and malfunction
THC total hydrocarbons
tpy tons per year
TOSHI target organ specific hazard index
UMRA Unfunded Mandates Reform Act
[mu]g/dscm micrograms per dry standard cubic meter
[mu]g/Nm\3\ micrograms per normal cubic meter
UPL upper prediction limit
VCS voluntary consensus standards
VE visible emissions
XML extensible markup language
Background information. On January 14, 2021, the EPA proposed
revisions to the Refractory Manufacturing Products NESHAP based on our
RTR (86 FR 3095, January 14, 2021). In this action, we are finalizing
decisions and revisions for the rule. We summarize some of the more
significant comments we timely received regarding the proposed rule and
provide our responses in this preamble. A summary of all other public
comments on the proposal and the EPA's responses to those comments is
available in the document titled Summary of Public Comments and
Responses on Proposed Rule: National Emission Standards for HAP from
Refractory Products Manufacturing (40 CFR part 63, subpart SSSSS)
Residual Risk and Technology Review, Final Amendments, located in
Docket ID No. EPA-HQ-OAR-2020-0148. A ``track changes'' version of the
regulatory language that incorporates the changes in this action is
available in the docket.
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Organization of this document. The information in this preamble is
organized as follows:
I. General Information
A. Does this action apply to me?
B. Where can I get a copy of this document and other related
information?
C. Judicial Review and Administrative Reconsideration
II. Background
A. What is the statutory authority for this action?
B. What is the Refractory Products Manufacturing source category
and how does the NESHAP regulate HAP emissions from the source
category?
C. What changes did we propose for the Refractory Products
Manufacturing source category in our January 14, 2021 RTR proposal?
III. What is included in this final rule?
A. What are the final rule amendments based on the risk review
for the Refractory Products Manufacturing source category?
B. What are the final rule amendments based on the technology
review for the Refractory Products Manufacturing source category?
C. What are the final rule amendments pursuant to CAA sections
112(d)(2) and (3) for the Refractory Products Manufacturing source
category?
D. What are the final rule amendments addressing emissions
during periods of startup, shutdown, and malfunction (SSM)?
E. What other changes have been made to the NESHAP?
F. What are the effective and compliance dates of the standards?
IV. What is the rationale for our final decisions and amendments for
the Refractory Products Manufacturing source category?
A. Residual Risk Review for the Refractory Products
Manufacturing Source Category
B. Technology Review for the Refractory Products Manufacturing
Source Category
C. CAA Sections 112(d)(2) and (3) Amendments for the Refractory
Products Manufacturing Source Category
D. SSM Amendments for the Refractory Products Manufacturing
Source Category
E. Electronic Reporting Amendments for the Refractory Products
Manufacturing Source Category
F. Technical Amendments for the Refractory Products
Manufacturing Source Category
V. Summary of Cost, Environmental, and Economic Impacts and
Additional Analyses Conducted
A. What are the affected facilities?
B. What are the air quality impacts?
C. What are the cost impacts?
D. What are the economic impacts?
E. What are the benefits?
F. What analysis of environmental justice did we conduct?
G. What analysis of children's environmental health did we
conduct?
VI. Statutory and Executive Order Reviews
A. Executive Orders 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 and 1 CFR
part 51
J. Executive Order 12898: Federal Actions To Address
Environmental Justice in Minority Populations and Low-Income
Populations
K. Congressional Review Act (CRA)
I. General Information
A. Does this action apply to me?
Regulated entities. Refractory Products Manufacturing, the source
category that is the subject of this final action, is regulated under
40 CFR part 63, subpart SSSSS. The North American Industry
Classification System codes for the refractory products industry are
327124 (clay) and 327125 (nonclay). We estimate that three major source
facilities engaged in refractory products manufacturing will be
affected by this final rule. To determine whether your facility is
affected, you should examine the applicability criteria in the
appropriate NESHAP. If you have any questions regarding the
applicability of any aspect of this NESHAP, please contact the
appropriate person listed in the preceding FOR FURTHER INFORMATION
CONTACT section of this preamble.
B. 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 final action will also be available on the internet. Following
signature by the EPA Administrator, the EPA will post a copy of this
final action at: https://www.epa.gov/stationary-sources-air-pollution/refractory-products-manufacturing-national-emissions-standards.
Following publication in the Federal Register, the EPA will post the
Federal Register version and key technical documents at this same
website.
Additional information is available on the RTR website at https://www.epa.gov/stationary-sources-air-pollution/risk-and-technology-review-national-emissions-standards-hazardous. This information
includes an overview of the RTR program and links to project websites
for the RTR source categories.
C. Judicial Review and Administrative Reconsideration
Under Clean Air Act (CAA) section 307(b)(1), judicial review of
this final action is available only by filing a petition for review in
the United States Court of Appeals for the District of Columbia Circuit
(the Court) by January 18, 2022. Under CAA section 307(b)(2), the
requirements established by this final rule may not be challenged
separately in any civil or criminal proceedings brought by the EPA to
enforce the requirements.
Section 307(d)(7)(B) of the CAA further provides that only an
objection to a rule or procedure which was raised with reasonable
specificity during the period for public comment (including any public
hearing) may be raised during judicial review. This section also
provides a mechanism for the EPA to reconsider the rule if the person
raising an objection can demonstrate to the Administrator that it was
impracticable to raise such objection within the period for public
comment or if the grounds for such objection arose after the period for
public comment (but within the time specified for judicial review) and
if such objection is of central relevance to the outcome of the rule.
Any person seeking to make such a demonstration should submit a
Petition for Reconsideration to the Office of the Administrator, U.S.
EPA, Room 3000, WJC South Building, 1200 Pennsylvania Ave. NW,
Washington, DC 20460, with a copy to both the person(s) listed in the
preceding FOR FURTHER INFORMATION CONTACT section, and the Associate
General Counsel for the Air and Radiation Law Office, Office of General
Counsel (Mail Code 2344A), U.S. EPA, 1200 Pennsylvania Ave. NW,
Washington, DC 20460.
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 HAP from stationary sources. In the first
stage, we must identify categories of sources emitting one or more of
the HAP listed in CAA section 112(b) and then promulgate technology-
based NESHAP for those sources. ``Major sources'' are those that emit,
or have the potential to emit, any single HAP at a rate of 10 tons per
year (tpy) or more, or 25 tpy or more of any combination of HAP. For
major sources, these standards are commonly referred
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to as maximum achievable control technology (MACT) standards and must
reflect the maximum degree of emission reductions of HAP achievable
(after considering cost, energy requirements, and non-air quality
health and environmental impacts). In developing MACT standards, CAA
section 112(d)(2) directs the EPA to consider the application of
measures, processes, methods, systems, or techniques, including, but
not limited to, those that reduce the volume of or eliminate HAP
emissions through process changes, substitution of materials, or other
modifications; enclose systems or processes to eliminate emissions;
collect, capture, or treat HAP when released from a process, stack,
storage, or fugitive emissions point; are design, equipment, work
practice, or operational standards; or any combination of the above.
For these MACT standards, the statute specifies certain minimum
stringency requirements, which are referred to as MACT floor
requirements, and which may not be based on cost considerations. See
CAA section 112(d)(3). For new sources, the MACT floor cannot be less
stringent than the emission control achieved in practice by the best-
controlled similar source. The MACT standards for existing sources can
be less stringent than floors for new sources, but they cannot be less
stringent than the average emission 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, we must also consider control options that are more
stringent than the floor under CAA section 112(d)(2). We may establish
standards more stringent than the floor, based on the consideration of
the cost of achieving the emissions reductions, any non-air quality
health and environmental impacts, and energy requirements.
In the second stage of the regulatory process, the CAA requires the
EPA to undertake two different analyses, which we refer to as the
technology review and the residual risk review. Under the technology
review, we must review the 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, pursuant to CAA section 112(d)(6). Under the residual risk
review, we must evaluate the risk to public health remaining after
application of the technology-based standards and revise the standards,
if necessary, to provide an ample margin of safety to protect public
health or to prevent, taking into consideration costs, energy, safety,
and other relevant factors, an adverse environmental effect. The
residual risk review is required within 8 years after promulgation of
the technology-based standards, pursuant to CAA section 112(f). In
conducting the residual risk review, if the EPA determines that the
current standards provide an ample margin of safety to protect public
health, it is not necessary to revise the MACT standards pursuant to
CAA section 112(f).\1\ For more information on the statutory authority
for this rule, see 86 FR 3097 (January 14, 2021).
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\1\ The Court has affirmed this approach of implementing CAA
section 112(f)(2)(A): 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.'').
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B. What is the Refractory Products Manufacturing source category and
how does the NESHAP regulate HAP emissions from the source category?
The EPA promulgated the Refractory Products Manufacturing NESHAP on
April 16, 2003 (68 FR 18730). The standards are codified at 40 CFR part
63, subpart SSSSS. The Refractory Products Manufacturing industry
consists of facilities that manufacture refractory products, such as
refractory bricks, refractory shapes, monolithics, kiln furniture,
crucibles, and other materials used for lining furnaces and other high
temperature process units. The source category covered by this NESHAP
includes three major source facilities.
The NESHAP groups refractory product manufacturing processes into
four subcategories: Clay refractories, nonclay refractories, chromium
refractories (nonclay) and pitch-impregnated refractories (nonclay).
The three major source facilities manufacture clay and/or nonclay
refractory products and can be grouped into the clay and nonclay
refractories subcategories. Chromium refractory products and pitch-
impregnated refractory products are not manufactured by any of the
three major source facilities.
The Refractory Products Manufacturing NESHAP specifies emission
limits, operating limits, and work practice standards for existing
affected thermal process units and for new and reconstructed affected
thermal process units that emit organic HAP according to refractory
product type. For existing clay refractory product kilns, the NESHAP
requires the use of natural gas or equivalent fuel at all times, except
during periods of natural gas supply interruption or curtailment, to
limit metal HAP, hydrogen fluoride (HF) and hydrogen chloride (HCl)
emissions. New clay refractory product kilns are required to meet
numeric limits for HF and HCl. For existing and new curing ovens, shape
dryers, and kilns that are used to process refractory products that use
organic HAP (i.e., nonclay refractory product sources), the NESHAP
provides the option of meeting a total hydrocarbon (THC) concentration
limit or reducing the THC mass emissions by at least 95 percent. The
NESHAP also establishes operating limits for thermal process sources
and control devices, which are based on operating parameters
established during performance testing. Additional detail on the
refractory product manufacturing source category and NESHAP
requirements are provided in the proposal preamble (86 FR 3083, January
14, 2021).
C. What changes did we propose for the Refractory Products
Manufacturing source category in our January 14, 2021 RTR proposal?
On January 14, 2021, the EPA published a proposed rule in the
Federal Register for the Refractory Products Manufacturing NESHAP, 40
CFR part 63, subpart SSSSS, that took into consideration the RTR
analyses (86 FR 3095). For this source category, we proposed that the
risks are acceptable, and that additional emission controls are not
necessary to provide an ample margin of safety. For the technology
review, we proposed improvements to the existing work practice standard
for affected continuous kilns using THC emission control devices. We
also proposed the following amendments: Standards for previously
unregulated HAP for affected sources in the clay and nonclay refractory
subcategories; the requirement that NOCS reports, performance test
results, and performance evaluation results be electronically
submitted; revisions to the SSM provisions of the rule; new test
methods and incorporation by reference (IBR) of alternative test
methods; and other minor technical and editorial revisions.
III. What is included in this final rule?
This action finalizes the EPA's determinations pursuant to the RTR
provisions of CAA section 112 for the Refractory Products Manufacturing
source category and amends the Refractory Products Manufacturing NESHAP
based on those determinations. This action also
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finalizes other changes to the NESHAP, including the proposed changes
described above, except we are finalizing a slightly modified version
of the proposed work practice standard for affected continuous kilns
using THC emission control devices, as explained in section IV.B.2 of
this preamble; and we are not finalizing the proposed allowance to use
alternative fuels during periods of natural gas supply curtailment or
interruption from the natural gas fuel requirement, as explained in
section IV.B.3 of this preamble. We are finalizing these requirements
as a result of the public comments we received on the proposed rule.
A. What are the final rule amendments based on the risk review for the
Refractory Products Manufacturing source category?
This section describes the final amendments to the Refractory
Products Manufacturing NESHAP (subpart SSSSS) being promulgated
pursuant to CAA section 112(f). In this action, we are finalizing our
proposed determination that risks from the Refractory Products
Manufacturing source category are acceptable, the standards provide an
ample margin of safety to protect public health, and additional
standards are not necessary to prevent an adverse environmental effect.
The EPA proposed no changes to the subpart based on the risk review
conducted pursuant to CAA section 112(f). The EPA received no new data
or other information during the comment period that would cause us to
change our proposed risk determination. Therefore, we are not requiring
additional controls or new requirements under CAA section 112(f)(2) for
subpart SSSSS in this action.
B. What are the final rule amendments based on the technology review
for the Refractory Products Manufacturing source category?
We determined that there was a development in practice that
warranted revision of the MACT standards for this source category.
Therefore, to satisfy the requirements of CAA section 112(d)(6), we
proposed revisions to the MACT standards to improve the existing work
practice standard for affected continuous kilns using emission control
devices. The proposed revisions were based on the best practices of one
facility and included:
Limitation of the work practice standard to THC emission
control devices only,
an annual limit on the number of hours for bypass of the
control device,
the requirement to process product containing lower
percentages of organic HAP content in the resins, binders and additives
(less than the average organic HAP mass fraction),
an allowance for the processing of five kiln cars per year
with greater than average organic HAP mass fraction, and
reporting of the mass of organic HAP emissions for bypass
periods in the semi-annual compliance report.
The EPA received additional data during the comment period that
caused us to change these proposed work practice requirements.
Therefore, in this action, we are finalizing the following requirements
under CAA section 112(d)(6) for subpart SSSSS:
The proposed limitation of the work practice standard to
THC emission control devices only,
the proposed annual limit on the number of hours for
bypass of the control device,
revised requirement to maintain the organic HAP processing
rate below whichever is lower, either (a) the average organic HAP
processing rate (i.e., the average organic HAP processing rate (pounds
per hour (lb/hr)) based on actual production on a 6-month rolling
basis, not to include periods of kiln shut down) or (b) the lowest
hourly organic HAP processing rate determined during the most recent
performance test,
removal of the proposed allowance for processing of five
kiln cars per year with greater than average organic HAP mass fraction
during control device maintenance and bypass,
revised reporting requirements for the semi-annual
compliance report, including:
[cir] The average organic HAP processing rate based on actual
production on a 6-month rolling basis (not to include periods of kiln
shut down) or the lowest hourly organic HAP processing rate from the
most recent performance test (whichever is lower), for bypass periods,
[cir] the actual organic HAP processing rate,
[cir] the amount of product produced and the mass of organic HAP in
the product produced,
[cir] the estimated THC emissions,
[cir] the number of hours the control device was bypassed during
the compliance period, and
[cir] the cumulative number of hours the control device was
bypassed over the last 12-month rolling period.
We are not finalizing the proposed allowance for processing of five
kiln cars per year with greater than average organic HAP mass fraction
during control device maintenance and bypass. For more information
regarding the final improvements to the work practice standard that
applies for continuous kilns with THC emissions control devices, see
section IV.B of this preamble.
In addition, the EPA received a comment during the comment period
that caused us to review the fuel combustion technology used by sources
in the source category and consequently revise the existing work
practice standard to require the use of natural gas (or equivalent
fuel) at all times. After consideration of the comment, under CAA
section 112(d)(6), we are removing the allowance to use alternative
fuels during periods of natural gas supply curtailment or interruption
from the natural gas fuel requirement as explained in section IV.B.3 of
this preamble. This finalized amendment applies to existing clay
refractory products kilns and new or existing chromium refractory
products kilns and reflects a development in our understanding of
refractory kiln fuel combustion technology since promulgation of the
original standard.
Finally, as part of the technology review, we identified regulatory
gaps (previously unregulated processes or pollutants) and are
establishing new standards to fill those gaps as described in section
III.C of this preamble.
C. What are the final rule amendments pursuant to CAA sections
112(d)(2) and (3) for the Refractory Products Manufacturing source
category?
We determined that there are previously unregulated HAP for
existing sources in the clay and nonclay refractory subcategories that
warrant revisions to the MACT standards for this source category.
Therefore, pursuant to the requirements of CAA section 112(d)(2) and
(3) we proposed revisions to the MACT standards to include the
following:
New emission limits for particulate matter (PM) as a
surrogate for non-mercury (non-Hg) metal HAP and mercury (Hg) for
existing clay refractory product kilns, and
the requirement to use natural gas as fuel, or an
equivalent fuel, as the kiln fuel for new and existing curing ovens,
shape dryers, and kilns that are used to process refractory products
that use organic HAP (i.e., nonclay refractory product sources), except
during periods of natural gas supply interruption or curtailment.
As noted in section III.B of this preamble, the EPA received a
comment during the comment period that caused us to review the fuel
combustion technology used for all refractory
[[Page 66049]]
products sources in the source category. Based on that review, we are
not finalizing the proposed allowance to use alternative fuels during
periods of natural gas supply interruption or curtailment from the
natural gas fuel requirement for new and existing nonclay sources.
Therefore, we are finalizing the new emission limits for PM (as a
surrogate for non-Hg metal HAP) and Hg for existing clay refractory
product kilns, as proposed, and we are finalizing a revised requirement
to use natural gas, or an equivalent fuel, as the fuel for new and
existing nonclay sources, as a result of comments, under CAA section
112(d)(2) and (3) for subpart SSSSS in this action.
D. What are the final rule amendments addressing emissions during
periods of startup, shutdown, and malfunction?
We are finalizing the proposed amendments to the Refractory
Products Manufacturing NESHAP to eliminate the SSM exemption.
Consistent with Sierra Club v. EPA, 551 F. 3d 1019 (D.C. Cir. 2008),
the EPA is establishing standards in these rules that apply at all
times. As detailed in section IV.E of the proposal preamble (86 FR
3099, January 14, 2021), Table 11 to subpart SSSSS of part 63 (General
Provisions applicability table) is being revised to change several
references related to the provisions that apply during periods of SSM.
We also eliminated or revised certain recordkeeping and reporting
requirements related to the eliminated SSM exemption. The EPA also made
other harmonizing changes to remove or modify inappropriate,
unnecessary, or redundant language in the absence of the SSM exemption.
We determined that facilities in this source category can meet the
applicable emission standards at all times, including periods of
startup and shutdown. Therefore, the EPA determined that no additional
standards are needed to address emissions during these periods. The
legal rationale and explanation of the changes for SSM periods are set
forth in the proposed rule. See 86 FR 3079, 3099-3102. Further, the EPA
did not propose and is not promulgating standards for malfunctions in
this final action. As discussed in section IV.E of the January 14,
2021, proposal preamble, 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, although the
EPA has the discretion to set standards for malfunctions where
feasible. For the Refractory Products Manufacturing source category, it
is unlikely that a malfunction would result in a violation of the
standards, and no comments or information were submitted during the
comment period that support a contrary conclusion. Refer to section
IV.E of the January 14, 2021 proposal preamble for further discussion
of the EPA's rationale for the decision not to set standards for
malfunction events, as well as a discussion of the actions a source
could take in the unlikely event that a source fails to comply with the
applicable CAA section 112(d) standards as a result of a malfunction
event, given that administrative and judicial procedures for addressing
exceedances of the standards fully recognize that violations may occur
despite good faith efforts to comply.
E. What other changes have been made to the NESHAP?
In addition to the changes described above we are finalizing other
proposed amendments for the Refractory Products Manufacturing NESHAP
related to electronic reporting, test methods and minor technical and
editorial revisions, as described below.
To increase the ease and efficiency of data submittal and data
accessibility, we are finalizing the proposed requirement that owners
and operators of facilities in the Refractory Products Manufacturing
source category submit electronic copies of required NOCS reports,
performance test results, and performance evaluation results through
the EPA's Central Data Exchange (CDX) website using an electronic
performance test report tool called the Electronic Reporting Tool
(ERT). We also are finalizing, as proposed, provisions that allow
facility operators the ability to seek extensions for submitting
electronic reports for circumstances beyond the control of the
facility, i.e., for a possible outage in the CDX or Compliance and
Emissions Data Reporting Interface (CEDRI) or for a force majeure event
in the time just prior to a report's due date, as well as the process
to assert such a claim.
We are also finalizing the proposed additional and updated test
methods and an EPA guidance document that are incorporated by
reference. In accordance with requirements of 1 CFR 51.5, the EPA is
incorporating by reference the following documents described in the
amendments to 40 CFR 63.14:
ANSI/ASME PTC 19.10-1981, Flue and Exhaust Gas Analyses
[Part 10, Instruments and Apparatus], issued August 31, 1981, IBR
approved for Table 4 to subpart SSSSS.
ASTM D6348-12e1, Standard Test Method for Determination of
Gaseous Compounds by Extractive Direct Interface Fourier Transform
Infrared (FTIR) Spectroscopy, Approved February 1, 2012, IBR approved
for Table 4 to subpart SSSSS.
ASTM D6784-16, ``Standard Test Method for Elemental,
Oxidized, Particle-Bound and Total Mercury in Flue Gas Generated from
Coal-Fired Stationary Sources (Ontario Hydro Method),'' (Approved March
1, 2016), IBR approved for Table 4 to subpart SSSSS.
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 63.9804(f)(1). This document provides
guidance on the use of triboelectric monitors as fabric filter bag leak
detectors.
In addition, we are finalizing the following proposed technical and
editorial corrections:
Revise 40 CFR 63.9824 and Table 4 to subpart SSSSS of part
63 to clarify the location in 40 CFR part 60 of applicable EPA test
methods; and
Revise 40 CFR 63.9814 and 63.9816 to include the
requirements to record and report information on failures to meet the
applicable standard.
Finally, although not addressed in the proposal, we are amending 40
CFR 63.9804(e)(1) to correct a spelling error.
F. What are the effective and compliance dates of the standards?
The revisions to the MACT standards for the Refractory Products
Manufacturing source category being promulgated in this action are
effective on November 19, 2021. New sources must comply with all of the
standards immediately upon the effective date of the standard, November
19, 2021, or upon startup, whichever is later.
The compliance dates for existing affected sources are listed
below. Existing affected sources must continue to meet the current
requirements of 40 CFR part 63, subpart SSSSS, until the applicable
compliance date.
The compliance date for existing affected nonclay sources to comply
with the work practice to use natural gas as fuel, or an equivalent
fuel, as the kiln fuel at all times, including periods of natural gas
supply interruption or curtailment is November 19, 2021. The compliance
date for existing affected sources to comply with the electronic
reporting requirement for NOCS reports, performance test results, and
performance evaluation results is May 19, 2022. The compliance date for
existing affected sources with continuous kilns using THC emission
control devices to comply with the amended work practice standards
(i.e., limit the total number of hours for
[[Page 66050]]
bypass of the control device for during scheduled maintenance to 750
hours per year per kiln; maintain the organic HAP processing rate below
the average rate based on production or below the lowest hourly rate
during the most recent performance test, whichever is lower; update the
operation, maintenance, and monitoring (OM&M) plan; include the
required information in the semi-annual compliance report) is May 19,
2022. The compliance date for existing affected clay refractory product
kilns to comply with the new limits for PM (as a surrogate for non-Hg
metal HAP) and Hg is November 20, 2022. The compliance date for
existing affected sources to comply with the SSM revisions, in
accordance with the SSM court decision, is May 19, 2022.
We determined that an immediate compliance date is practicable for
the natural gas requirement and is based on current practices and other
information provided by the facilities. We are finalizing the 181-day
compliance date for electronic reporting and the scheduled maintenance
work practice to require facilities to implement these changes as
expeditiously as practicable. For electronic reporting, our experience
with similar industries that are required to convert reporting
mechanisms to install necessary hardware and software, become familiar
with the process of submitting performance test results electronically
through the EPA's CEDRI, test these new electronic submission
capabilities, and reliably employ electronic reporting shows that a
time period of a minimum of 90 days, and, more typically, 180 days, is
generally necessary to successfully accomplish these revisions. For the
improved scheduled maintenance work practice, we expect facilities
would also need this time to seek approval from the Administrator
before taking the control device on the affected kiln out of service
for scheduled maintenance and update their operation, maintenance, and
monitoring plan to reflect the revised requirements. For the new PM (as
a surrogate for non-Hg metal HAP) and Hg requirements, we determined
the one-year compliance date would provide existing clay sources with
sufficient time to plan and schedule facility resources to meet the
notification and compliance demonstration testing requirements
associated with the new limits. For the SSM changes, excluding the
revised requirements for the SSM described above (40 CFR 63.6(f)(1)),
our experience with similar industries further shows that this sort of
regulated facility generally requires a time period of 181 days to read
and understand the amended rule requirements and make any necessary
operational adjustments, adjustments to recordkeeping and reporting
systems, and/or updates to OM&M plans to reflect the revised
requirements.
During proposal we requested information from sources in this
source category regarding specific actions that would need to be
undertaken to comply with the proposed amended requirements and the
time needed to make the adjustments for compliance with any of the
revised requirements. No comments or information were submitted during
the comment period that support a contrary conclusion; therefore, we
are finalizing these compliance dates as proposed.
IV. What is the rationale for our final decisions and amendments for
the Refractory Products Manufacturing source category?
For each issue, this section provides a description of what we
proposed and what we are finalizing for the issue, the EPA's rationale
for the final decisions and amendments, and a summary of key comments
and responses. For all comments not discussed in this preamble, comment
summaries and the EPA's responses can be found in the comment summary
and response document, Summary of Public Comments and Responses on
Proposed Rule: National Emission Standards for HAP for Refractory
Products Manufacturing (40 CFR part 63, subpart SSSSS), Residual Risk
and Technology Review, Final Amendments, available in the docket.
A. Residual Risk Review for the Refractory Products Manufacturing
Source Category
1. What did we propose pursuant to CAA section 112(f) for the
Refractory Products Manufacturing source category?
Pursuant to CAA section 112(f), the EPA conducted a residual risk
review and presented the results of this review, along with our
proposed decisions regarding risk acceptability and ample margin of
safety, in section IV.B of the proposed rule preamble (86 FR 3095,
January 14, 2021). The results of this review are presented briefly
below in Table 1 of this preamble. Additional detail is provided in the
residual risk technical support document titled, Residual Risk
Assessment for the Refractory Products Manufacturing Source Category in
Support of the 2020 Risk and Technology Review Proposed Rule, which is
available in the Refractory Products Manufacturing docket (Docket Item
No. EPA-HQ-OAR-2020-0148-0013).
Table 1--Refractory Products Manufacturing Source Category Inhalation Risk Assessment Results
--------------------------------------------------------------------------------------------------------------------------------------------------------
Maximum individual Estimated population Estimated annual Maximum chronic Maximum screening
cancer risk (in 1 at increased risk of cancer incidence noncancer target organ acute noncancer HQ \2\
million) cancer >=1-in-1 (cases per year) specific hazard index -----------------------
------------------------ million ------------------------ (TOSHI) \1\
Risk assessment ------------------------ ------------------------
Based on Based on Based on Based on Based on Based on Based on Based on Based on actual
actual allowable actual allowable actual allowable actual allowable emissions
emissions emissions emissions emissions emissions emissions emissions emissions
--------------------------------------------------------------------------------------------------------------------------------------------------------
Source Category................. 0.7 0.7 0 0 0.0003 0.0003 0.04 0.04 HQREL = 0.09
Whole Facility.................. 0.7 .......... 0 .......... 0.0004 .......... 0.04 .......... ......................
--------------------------------------------------------------------------------------------------------------------------------------------------------
\1\ The TOSHI is the sum of the chronic noncancer hazard quotients (HQ) for substances that affect the same target organ or organ system.
\2\ The maximum estimated acute exposure concentration was divided by available short-term threshold values to develop HQ values.
The results of the proposed inhalation risk modeling, as shown in
Table 1 of this preamble, indicate that the maximum individual cancer
risk based on actual and allowable emissions (lifetime) is 0.7-in-1
million (driven by trace amounts of chromium, arsenic, nickel and
cadmium emissions from tunnel kilns), the maximum chronic noncancer
TOSHI value based on actual and allowable emissions is 0.04 (driven by
HF from tunnel kilns), and the maximum screening acute noncancer HQ
value (off-facility site) is 0.09 (driven by HF). At proposal, the
total annual cancer incidence (national) from these facilities based on
actual and allowable emission levels was estimated
[[Page 66051]]
to be 0.0003 excess cancer cases per year or one case every 3,333
years. The maximum individual cancer risk (lifetime) for the whole
facility was determined to be 0.7-in-1 million at proposal, driven by
chromium, arsenic, nickel and cadmium emissions from tunnel kilns. The
total estimated cancer incidence from the whole facility was determined
to be 0.0004 excess cancer cases per year, or one excess case in every
2,500 years. No people were estimated to have cancer risks above 1-in-1
million from exposure to HAP emitted from both MACT and non-MACT
sources at the three facilities in this source category. The maximum
facility-wide TOSHI for the source category was estimated to be 0.04,
driven by HF emissions from tunnel kilns.
We also evaluated multipathway human health risk from the five PB-
HAP that are emitted by sources within this source category (arsenic,
cadmium, POM, Hg (divalent Hg and methyl mercury), and lead). We
evaluated the cadmium emissions from these facilities and concluded
this HAP did not exceed the Tier 1 multipathway screening value of 1
for cancer or noncancer. We also evaluated the arsenic, methyl mercury,
and POM emissions and found these HAP caused an exceedance of the Tier
1 multipathway screening value of 1 for cancer. Therefore, we conducted
a Tier 2 screening assessment for these HAP and concluded that
emissions of arsenic, POM and methyl mercury from these facilities did
not exceed the Tier 2 multipathway screening value of 1 for cancer. A
Tier 2 noncancer screening assessment was also conducted for Hg
emissions and resulted in a screening value less than 1. Based upon the
results of the screening assessments no further screening or site-
specific assessments were conducted for this source category.
In evaluating the potential for multipathway effects from emissions
of lead, modeled maximum annual-average lead concentrations were
compared to the National Ambient Air Quality Standards (NAAQS) for lead
(0.15 [micro]g/m\3\). Results of this analysis confirmed that the NAAQS
for lead would not be exceeded by any facility.
To evaluate the potential for adverse environmental effects, the
EPA focuses on eight HAP, which are referred to as ``environmental
HAP,'' in its screening assessment: Six PB-HAP and two acid gases. The
PB-HAP emitted by sources in the category are arsenic compounds,
cadmium compounds, POM, mercury (both inorganic mercury and methyl
mercury), and lead compounds. The acid gases included in the screening
assessment and emitted from the category are HCl and HF. In the Tier 1
screening analysis for PB-HAP (other than lead, which was evaluated
differently), arsenic, cadmium, divalent mercury, and POM had no Tier 1
exceedances for any ecological benchmark. Methyl mercury emissions at
one facility had a Tier 1 exceedance for the surface soil no-observed-
adverse-effect-level (avian ground insectivores) by a maximum SV of 2.
A Tier 2 screening assessment was performed for methyl mercury. Methyl
mercury had no Tier 2 exceedances for any ecological benchmark. For
lead, we did not estimate any exceedances of the secondary lead NAAQS.
Two acid gases are emitted by sources within this source category:
HCl HF. We conducted a screening-level evaluation of the potential
adverse environmental effects associated with emissions of HCl and HF
and found that 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 (i.e., each off-site data
point in the modeling domain) was below the ecological benchmarks for
all facilities. For HF, the maximum facility screening value (based on
the average concentration of all off-site data points over the modeling
domain) was well below 1 (0.007) and the maximum area that exceeded the
ecological benchmark was only 0.002-percent of the modeled area. Based
on the results of the environmental risk screening evaluation, we do
not expect an adverse environmental effect as a result of HAP emissions
from this source category.
We weighed all health risk factors, including those shown in Table
1 of this preamble, in our risk acceptability determination and
proposed that the residual risks from the Refractory Products
Manufacturing source category are acceptable (section IV.C of the
proposed rule preamble, 86 FR 3095, January 14, 2021). We then
considered whether 40 CFR part 63, subpart SSSSS provides an ample
margin of safety to protect public health and prevents, taking into
consideration costs, energy, safety, and other relevant factors, an
adverse environmental effect. At proposal we determined there are no
individuals in the exposed population with lifetime cancer risks above
1-in-1 million as a result of actual or allowable emissions from this
category. In addition, in our risk analysis we did not identify a
potential for adverse chronic noncancer, acute noncancer, or
multipathway health effects. Therefore, we proposed the current
standards provide an ample margin of safety to protect public health
(section IV.C of the proposed rule preamble, 86 FR 3095, January 14,
2021).
2. How did the risk review change for the Refractory Products
Manufacturing source category?
We have not changed any aspect of the risk assessment for this
source category as a result of public comments received on the January
2021 proposal.
3. What key comments did we receive on the risk review, and what are
our responses?
We received comments in support of and against the proposed
residual risk review. Having carefully considered these comments, it is
our determination that no revisions are warranted under CAA section
112(f)(2) for the Refractory Products Manufacturing source category.
Generally, the comments that were not supportive of the risk review
determination suggested changes to the underlying risk assessment
methodology. For example, one commenter stated that the EPA should
account for the increased risks due to exposure to multiple sources of
HAP, use more health-protective dose-response values, and consider
increased risks in childhood and from prenatal exposure. After review
of all the comments received, we determined that no changes to our
Science Advisory Board-approved review process were necessary. The
comments and our specific responses can be found in the document,
Summary of Public Comments and Responses on Proposed Rule: National
Emission Standards for HAP for Refractory Products Manufacturing (40
CFR part 63, subpart SSSSS), Residual Risk and Technology Review, Final
Amendments, available in the docket for this action (Docket ID No. EPA-
HQ-OAR-2020-0148).
4. What is the rationale for our final approach and final decisions for
the risk review?
As noted in our proposal, 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 the maximum individual risk (MIR) of
``approximately 1-in-10 thousand'' (see 54 FR 38045, September 14,
1989). We weigh all health risk factors in our risk acceptability
determination, including the cancer MIR, cancer incidence, the maximum
cancer TOSHI, the maximum acute noncancer HQ, the extent of
[[Page 66052]]
noncancer risks, the distribution of cancer and noncancer risks in the
exposed population, and the risk estimation uncertainties.
Since proposal, neither the risk assessment nor our determinations
regarding risk acceptability, ample margin of safety, or adverse
environmental effects have changed. For the reasons explained in the
proposed rule, we have determined that the risks from the Refractory
Products Manufacturing source category are acceptable, and that the
current standards provide an ample margin of safety to protect public
health and prevent an adverse environmental effect. Therefore, we are
not revising the subpart to require additional controls pursuant to CAA
section 112(f)(2) based on the residual risk review, and we are
readopting the existing standards under CAA section 112(f)(2).
B. Technology Review for the Refractory Products Manufacturing Source
Category
1. What did we propose pursuant to CAA section 112(d)(6) for the
Refractory Products Manufacturing source category?
Based on our technology review, we proposed improvements to the
existing underlying work practices as required by CAA section 112(d)(6)
during scheduled maintenance of THC control devices. These revisions
are necessary to reflect technical developments in pollution control
practices since the promulgation of the original standard for this
source category and reflect the best practices of one affected
facility. Specifically, for affected continuous kilns using THC
emission control devices, we proposed to limit the number of hours for
bypass of the control device to conduct scheduled maintenance, schedule
the manufacture of product with binder applicability of the standard to
THC emission control devices, limit the number of hours for percentages
at the lower end of the range produced during periods of control device
bypass. We also proposed to include the THC emissions for these periods
in the semi-annual compliance report. A brief summary of the EPA's
findings in conducting the technology review of refractory products
manufacturing operations was included in the preamble to the proposed
rule (86 FR 3095, January 14, 2021), and a detailed discussion of the
EPA's technology review and findings was included in the memorandum,
Technology Review for the Refractory Products Manufacturing NESHAP,
available in the docket for this action (Docket Item No. EPA-HQ-OAR-
2020-0148-0008).
2. How did the technology review change for the Refractory Products
Manufacturing source category?
For the final rule, we revised aspects of two work practice
standards from the proposal, based on public comments. First, we are
finalizing slightly different improvements than proposed for the work
practice standard that applies when a continuous kiln THC control
device is bypassed for scheduled maintenance. In particular, to
demonstrate compliance with the requirement in 40 CFR 63.9792(e)(2) to
minimize HAP emissions during the period when the kiln is operating and
the control device is out of service, the owner or operator will be
required to maintain the organic HAP processing rate (lb/hr) below
either the average organic HAP processing rate based on the actual
production on a 6-month rolling basis (not to include periods of kiln
shut down) or the HAP processing rate (lb/hr) that coincides with the
lowest hour of the most recent 3-hour performance test, whichever is
lower. This requirement replaces the proposed limitation of five kiln
cars with products for which the mass fraction of organic HAP in the
resins, binders, and additives is greater than the average for the
year. Second, we are revising the work practice standard to use natural
gas, or equivalent, as the kiln fuel by removing the exception for
periods of natural gas curtailment or supply interruption.
3. What key comments did we receive on the technology review, and what
are our responses?
We received both supportive and adverse comments on various aspects
of our technology review for refractory products manufacturing. The key
comments and responses are provided in this section; summaries of
comments not discussed in this preamble and the EPA's responses can be
found in the comment summary and response document, available in the
docket.
Comment: One commenter provided technical comments on the specific
provisions that the EPA proposed to limit production during periods
when the THC control device is being bypassed for maintenance. The
proposed provisions would have required manufacturing mostly product in
the tunnel kiln that contains a mass fraction of organic HAP in the
resins, binders, and additives that is less than the average organic
HAP mass fraction of these constituents for the year (on a 12-month
rolling basis), and manufacture of the product with an organic HAP mass
fraction greater than the average for the year would be limited to only
five kiln cars during such maintenance periods.
The commenter explained that tunnel kilns comprise a preheating
zone, firing zone, and cooling zone in sequence with kiln cars passing
through the system containing pressed/formed refractory. Each kiln is
designed to hold a set number of kiln cars in the preheating zone
position and a separate set number of kiln cars in the firing zone
position. The type and amount of resins, binders, and additives in the
kiln are dictated by each product type's formulation. During drying in
the tunnel kilns, organic HAP in resins, binders, and additives is
volatilized and either destroyed in the tunnel kiln or exhausted to a
THC control device for destruction.
The commenter noted that according to the memorandum Technology
Review for the Refractory Products Manufacturing NESHAP, available in
the docket for this action (Docket Item No. EPA-HQ-OAR-2020-0148-0008),
these proposed provisions are based on the facility's specific internal
operation procedures for the regenerative thermal oxidizer (RTO) unit
that state that tunnel kiln batches exceeding 90 binder counts can only
be pushed in a train of ``five cars or less.'' The commenter asserted
that the EPA has catered the five-kiln car provision too specifically
to the facility's one tunnel kiln due to extremely limited data, as the
facility is the only U.S. nonclay refractory producer using organic
binder and a THC control device. The commenter further stated that
these procedures only address one of the two continuous kilns at the
facility. The commenter also stated that since kiln cars can hold a
variety of refractory products of varying dimensions and formulation,
the mass of organic HAP emissions from the resins, binders, and
additives from car to car is variable. The commenter noted that a new
nonclay refractory tunnel kiln could potentially be constructed with
larger kiln cars, such that each kiln car could be designed to hold a
greater mass of nonclay refractory and emit much more organic HAP while
still satisfying the proposed provisions during periods of control
device maintenance.
The commenter suggested that instead the proposed requirements that
apply during THC control device bypass for continuous kilns should be
amended to reflect a more universal operating parameter limit (OPL).
The OPL is established during performance testing in accordance with 40
CFR 63.9800 and Table 4 to subpart SSSSS. Each
[[Page 66053]]
continuous unit is required to establish a 3-hour block operating limit
for maximum allowable organic HAP processing rate, which is calculated
as the average organic HAP processing rate from performance testing
plus 10 percent in accordance with 40 CFR 63.9798(c) and EPA guidance.
The commenter suggested that the organic HAP processing rate during THC
control device bypass be limited to the average organic HAP processing
rate from the most recent performance test demonstration, as determined
on an hourly basis (i.e., 1-hour block average). The commenter also
provided suggested revisions to the regulatory language to implement
this suggestion.
Response: The EPA proposed an improved work practice standard to
further minimize emissions during periods of scheduled maintenance and
bypass of the thermal oxidizer as a result of the CAA section 112(d)(6)
technology review process. In addition to the current work practice to
minimize emissions during these periods, we proposed other measures
based on the best practices of one facility. These included: (1)
Limiting the applicability to THC control devices; (2) an annual limit
on the number of hours for bypass of the control device; (3) the
requirement to process product containing lower percentages of organic
HAP content in the resins, binders and additives (less than the average
organic HAP mass fraction); (4) an allowance for the processing of five
kiln cars per year with greater than average organic HAP mass fraction;
and (5) reporting of the mass of organic HAP emissions for bypass
periods in the semi-annual compliance report.
As a result of the comments regarding these proposed measures, we
learned we did not have full knowledge of the details of the facility's
internal operating procedures during scheduled maintenance and bypass
of the thermal oxidizer. As the commenter clarified, tunnel kiln
batches exceeding 90 binder counts (a measure of the volume of binder)
can only be pushed in a train of ``five cars or less'' during these
periods. The commenter also clarified this procedure applies to only
one of the two continuous tunnel kilns. We agree with the commenter
that using the ``kiln car'' limitation is an imprecise way of limiting
organic HAP emissions due to the potential variation in kiln car size.
However, the EPA found the facility's suggestion to set an operating
limit during bypass periods equal to the ``average organic HAP
processing rate from the most recent performance test, as determined on
an hourly basis (1-hour block average)'' and rule language edits to be
inconsistent with other rule requirements. Specifically, because
performance tests are required to be conducted while the source is
operating at the maximum organic HAP processing rate as defined in
Sec. 63.9824, we found this suggestion to be inconsistent with the
rule requirement to minimize emissions during control device bypass and
maintenance required by Sec. 63.9792(e)(2).
We are therefore finalizing revisions to the proposed revised work
practice standard that reflect additional improvements as a result of
these comments and follow-up discussions with the facility to clarify
their best practices. Specifically, we are revising the proposed work
practice to limit the organic HAP processing rate rather than the
organic HAP content during control device bypass and maintenance as
proposed. The proposed rule language that required the facility to
minimize HAP emissions during the period when the kiln is operating and
the control device is out of service by ``scheduling of the manufacture
of product for which the mass fraction of organic HAP in the resins,
binders, and additives is at the lower end of the range produced (i.e.,
below the typical average mass fraction of organic HAP in the resins,
binders, and additives)'' is revised to ``maintaining the organic HAP
processing rate (lb/hr) below the average organic HAP processing rate
based on actual production on a 6-month rolling basis (not to include
periods of kiln shut down) or below the organic HAP processing rate
(lb/hr) that coincides with the lowest hour of the most recent 3-hour
performance test, whichever is lower.'' We are then requiring sources
to demonstrate compliance with the requirement to minimize emissions by
maintaining the organic HAP processing rate (lb/hr) during control
device maintenance and bypass below lower of the two organic HAP
processing rates described above. We are also revising the proposed
reporting requirements to reflect these changes. In addition, we are
removing the allowance for the processing of five kiln cars per year
with greater than average organic HAP mass fraction from the work
practice. Changing the work practice requirement from the mass fraction
of organic HAP in the product to the HAP processing rate while also
removing the reference to kiln cars provides a clearer and more
consistent metric for demonstrating that HAP emissions have been
minimized and provides the facility with options for minimizing
emissions during the period when the kiln is operating and the control
device is out of service (e.g., loading kiln cars with products with
lower HAP contents, reducing the number of kiln cars pushed through the
kiln per hour).
In summary, the finalized work practice standard for periods of
control device maintenance and bypass includes: (1) The proposed limit
of the applicability to THC control devices; (2) the proposed annual
limit on the number of hours for bypass of the control device; (3) the
revised requirement to maintain the organic HAP processing rate below
the average organic HAP processing rate, determined as the lower of
either (a) the average organic HAP processing rate (lb/hr) based on
actual production on a 6-month rolling basis, not to include periods of
kiln shut down) or (b) the organic HAP processing rate determined
during the lowest hour of the most recent performance test; and (4)
semiannual compliance reporting of the following information: The
average organic HAP processing rate based on actual production on a 6-
month rolling basis (not to include periods of kiln shut down) or the
lowest hour from the most recent performance test (whichever is lower),
the actual organic HAP processing rate, the amount of product produced
and the mass of organic HAP in the product produced, the estimated THC
emissions, the number of hours the control device was bypassed during
the compliance period (as proposed), and the cumulative number of hours
the control device was bypassed over the last 12-month period (as
proposed). The final improvement of the work practice standard as a
result of the CAA section 112(d)(6) technology review process does not
include the proposed allowance for processing of five kiln cars per
year with greater than average organic HAP mass fraction during control
device maintenance and bypass.
Meeting minutes from the discussion with the facility and follow-up
emails are included in the rulemaking docket (Docket ID No. EPA-HQ-OAR-
2020-0148).
Comment: One commenter noted that the EPA proposed to limit the
number of hours during which a continuous kiln is operating and the THC
control device is bypassed for maintenance to 750 hours per year on a
12-month rolling basis. The commenter noted that the EPA identified
this provision as an improvement to the current standard since there is
no limit on the total amount of time the provision may be used other
than the requirement for the owner or operator to minimize the amount
of time for each bypass.
The commenter also noted that per proposed requirements in 40 CFR
[[Page 66054]]
63.9792(e) and 63.9812(g), kiln operation during bypass of the THC
control device requires advanced approval from the Administrator (86 FR
3079, 3099, January 14, 2021). The commenter noted that the EPA also
proposed that affected sources must document the planned maintenance
procedures in the OM&M plan, and the proposed requirement in 40 CFR
63.9814(c)(7) would require reporting in the semi-annual compliance
report for these periods, including a statement of whether or not the
control device maintenance was included in the approved request to
bypass the control device while scheduled maintenance is performed. The
EPA has proposed to allow 181 days for compliance with the proposed
revisions, noting that this time would be used to update the OM&M plans
and seek approval from the Administrator before taking the control
device on the affected kiln out of service for scheduled maintenance.
The commenter stated that the proposed requirement for
Administrator approval is based on its current state-issued title V
permit. The commenter noted that the state has delegated authority and
is the ``Administrator'' in regard to implementing and enforcing the
NESHAP requirements at 40 CFR part 63. The commenter clarified that the
current title V permit requires advance notification via email to the
state air quality inspector and to the Regional Air Quality staff that
the RTO will be out of service for scheduled maintenance, but the
permit does not include approval requirements. In addition, the
commenter stated that the EPA did not differentiate between THC control
device planned and unplanned maintenance and did not specify the scope
of maintenance (e.g., washdowns, bakeouts, media placement) to be
documented in the OM&M plan. Because the proposed provisions require
approval from the Administrator in advance, the commenter noted that it
appears kiln operation during unplanned maintenance events is not
addressed.
The commenter requested that the EPA amend 40 CFR 63.9792(e),
63.9812(g), 63.9814(c)(7), Table 3, and Table 9 to specify that kiln
operation during periods of control device maintenance requires
``Administrator notification'' and not ``Administrator approval.'' The
commenter suggested that the notification could include a telephone
call or email to the Administrator within 24 hours of a bypass event.
The commenter asserted that this provision would allow for unplanned/
emergency maintenance, which is common for continuous process units,
particularly where facilities operate 24 hours a day, 365 days a year.
Additionally, requiring notification rather than approval for each
bypass allows facilities to avoid complete shutdown of a process unit
if the Administrator cannot be reached for approval (e.g., control
device requires unplanned maintenance at 3 a.m. on Saturday and
Administrator cannot be reached until 9 a.m. Monday). The commenter
noted that the EPA's proposed recordkeeping and reporting requirements
related to the 750-hour (12-month rolling basis) limit on use of the
bypass provisions would still adequately qualify these bypasses with
Administrator notification versus approval. The commenter also asserted
that requiring notification instead of approval does not restore
``malfunction'' provisions, as the term is defined under 40 CFR 63.2,
as the bypass period is limited to 750 hours per year (12-month rolling
basis). Also, per U.S. Sugar Corp. v. EPA, 830 F.3d 579, 606-610
(2016), the Administrator may determine whether the facility took good
faith efforts to minimize resulting emissions including preventative
and corrective actions and whether excess emissions were caused by poor
maintenance or careless operation.
Response: The EPA disagrees with the commenter's characterization
of the proposed requirements in 40 CFR 63.9792(e) and 63.9812(g),
regarding kiln operation during bypass of the THC control device and
advanced approval from the Administrator (86 FR 3099, January 14,
2021). The EPA agrees these citations pertain to kiln operation during
bypass of the THC control device and advanced approval from the
Administrator, but these provisions are original rule requirements that
were not proposed to be amended. The original general requirements for
complying with subpart SSSSS are contained in 40 CFR 63.9792, and 40
CFR 63.9792(e) specifically permits the continued operation of a
continuous kiln during bypass and scheduled maintenance of the control
device for that kiln, provided the owner or operator meets the
requirements of the work practice standard and requests and receives
approval by the Administrator per 40 CFR 63.9792(e)(1), which requires
a separate request each time the owner or operator plans to bypass the
control device for scheduled maintenance. Similarly, the original
requirements for notifications for subpart SSSSS are contained in 40
CFR 63.9812, and 40 CFR 63.9812(g) specifically states that owner and
operators must request approval from the Administrator before bypassing
the control device, as specified in 40 CFR 63.9792(e), and that a
separate request must be submitted for approval each time.
We also disagree with the statement that the EPA proposed a new
requirement that affected sources must document the planned maintenance
procedures in the OM&M plan, as this requirement was also required in
the original rule at 40 CFR 63.9794(a)(6). The provisions in 40 CFR
63.9794(a)(6) pertain to any maintenance that requires use of the
bypass provisions. The provision includes ``procedures for the proper
operation and routine and long-term maintenance of each process unit
and [air pollution control device],'' which encompasses the more
specific types of maintenance described by the commenter (e.g.,
washdowns, bakeouts, media placement). Further, subpart SSSSS does not
include the terms ``planned maintenance'' or ``unplanned maintenance,''
nor does it define ``scheduled maintenance.'' However, as noted earlier
in this response, a request for Administrator approval must be
submitted each time the owner or operator plans to bypass the control
device for ``scheduled maintenance,'' and per Table 2 to subpart SSSSS,
the owner or operator must receive approval from the Administrator
before taking the control device on the affected kiln out of service
for scheduled maintenance.
After review of the commenter's request, we are not amending the
requirements to request Administrator approval, and we also disagree
with the comment that there is a need to differentiate between THC
control device ``planned and unplanned maintenance'' within subpart
SSSSS. The EPA did not propose to amend the requirement to request
Administrator approval each time an owner or operator plans to bypass
the control device, and we conclude that allowing notification rather
than approval would not be an improvement to the standard. In
particular, if owners and operators were allowed to comply with the
work practice standard during periods of maintenance that are only
``scheduled'' a few hours in advance of the control device bypass,
those owners and operators would likely find it very challenging to
comply with all the specific requirements that must be met during
bypass to demonstrate compliance with the requirement in 40 CFR
63.9792(e)(2) to minimize HAP emissions during the bypass. Therefore,
the work practice standard we are finalizing for periods of control
device bypass and scheduled maintenance applies to all THC control
device bypasses for scheduled maintenance for
[[Page 66055]]
which the owner or operator receives approval from the Administrator.
Most of the maintenance activities described by the commenter are
likely to be considered ``scheduled maintenance'' for which the owner
or operator will be able to request advanced approval from the
Administrator before the control device is bypassed. These maintenance
activities are the activities that should be documented in the OM&M
plan. Bypass of the control device without Administrator approval would
be considered a deviation from the standard.
Finally, the EPA agrees with the commenter that the state has
delegated authority and is the ``Administrator'' with regard to
implementing and enforcing the 40 CFR subpart SSSSS requirements.
However, the state does not have the authority to set standards less
stringent than those promulgated by the Administrator in accordance
with CAA section 112(l). Therefore, in order for the current title V
permit to satisfy the 40 CFR 63.9792(e) and 63.9812(g) requirements, it
must require advance approval by the Administrator and not the less
stringent notification requirements.
Comment: One commenter stated that the EPA must remove the
alternative fuel allowance provision. The commenter noted that the
existing standards contain a provision allowing for ``the use of
alternative fuels'' (such as fuel oil, propane, and pulverized coal)
during certain circumstances as an exception to the work practice
standard that requires use of natural gas as the core emission control
requirement. The commenter noted that the EPA has recognized this
provision allows for an exception from the standards in ``situations
analogous to malfunctions'' and explained in 2003 that its
justification for this provision was similar to the SSM exemption. At
the time, the EPA stated that, ``Just as an exceedance of emission
limits during a malfunction is not considered a violation, as indicated
in 40 CFR 63.6(f)(1) and (h)(1), we believe that using other fuels
during periods when natural gas is unavailable should also not be
considered a violation of the work practice standard for clay and
chromium refractory products kilns'' (68 FR 18740, April 16, 2003).
The commenter stated that to the extent that the EPA retains this
work practice standard as the sole or an additional control, it must
remove the illegal alternative fuel allowance provision. The commenter
further stated that including this provision means that the emission
standard (i.e., the fuel requirement) is not ``continuous'' and does
not apply at all times, which is a violation of CAA sections 302(k) and
112. The commenter asserted that the EPA should recognize this
allowance is as unlawful as the SSM exemption that it has recognized
the need to remove (Sierra Club, 551 F.3d at 1022), and therefore the
EPA should remove this specific malfunction exemption as well. Failing
to do so would violate CAA section 112(d)(6), by refusing to make a
``necessary'' revision to assure compliance with the CAA, and it would
be arbitrary because it would leave in place a harmful exemption that
allows the release of more pollution than CAA section 112 allows, based
on the illegal justification of a ``malfunction.'' In this instance,
the commenter noted, such a ``malfunction'' may simply be an increase
in natural gas prices, making this allowance particularly arbitrary
because it conflicts with the CAA's public health objective and the
floor requirement to assure emission standards based on the
``achieved'' emission reductions, without consideration of cost.
Response: The EPA agrees with the commenter that the existing
standards require the use of natural gas or equivalent fuel. It also
allows ``the use of alternative fuels'' during ``periods of natural gas
curtailment or supply interruption'' as defined in 40 CFR 63.9824.
Propane is considered to be a fuel that is equivalent to natural gas,
not an alternative fuel, as stated by the commenter.
The current rule requirements related to alternative fuel usage
state that procedures for alternative fuel usage must be included in
the OM&M plan per 40 CFR 63.9794(a)(10)(i), require notification of
alternative fuel usage within 48 hours of the declaration of a period
of natural gas curtailment or supply interruption per 40 CFR
63.9812(f), and reporting of termination of alternative fuel usage
within 10 working days per 40 CFR 63.9814. The ``period of natural gas
curtailment or supply interruption'' is defined in 40 CFR 63.9824 as
``the period of time during which the supply of natural gas to an
affected facility is halted for reasons beyond the control of the
facility. An increase in the cost or unit price of natural gas does not
constitute a period of natural gas curtailment or supply
interruption.''
The alternative fuel allowance was added to the rule as a result of
comments from the industry on the 2002 proposed rule, in which the EPA
proposed the use of natural gas or other such clean fuel to prohibit
the use of coal, fuel oil, waste oil, or equivalent fuels and the
resulting emissions of HF, HCl or HAP metals from existing clay
refractories (67 FR 42122, June 20, 2002). The EPA provided the
justification for the allowance referenced by the commenter in the memo
titled Summary of Public Comments and Responses on the Proposed NESHAP
for Refractory Products Manufacturing (Docket ID OAR-2002-0088, Item
No. V-C-01, page 12). Industry stakeholders opposed the 2002 proposed
work practice that required use of natural gas, stating that many kilns
were designed to use fuels other than natural gas and the need to use
these alternative fuels arises during natural gas shortages or price
increases. They also stated that during natural gas shortages,
residential users receive priority over industrial users of natural gas
and that prohibiting the use of alternative fuels could adversely
impact the viability of some refractory operations. After considering
those comments, the EPA finalized the alternative fuel allowance (73 FR
18736, April 16, 2003). The EPA did not consider a price increase to be
a justification for alternative fuel use at that time and omitted that
reason from the natural gas curtailment definition. Contrary to the
commenter's argument, this definition expressly states that an increase
in natural gas prices does not constitute a period of natural gas
curtailment or supply interruption, so the commenter's claim that such
a ``malfunction'' may simply be an increase in natural gas prices is
not valid.
We acknowledge much has changed since the original NESHAP was
promulgated in 2003. For this final action, the facilities in the
source category confirmed they use natural gas and propane during
normal operations in accordance with the NESHAP and state requirements.
In the event of a natural gas curtailment or supply interruption, they
indicated they would not switch to another fuel due to the fuel-
specific burner technology in use. They stated they would either
continue to use equivalent fuel (propane backup) or shut down and
retool their process units to use equivalent fuel (propane) or an
alternative fuel (fuel oil) since they have no back-up supply of
propane and it would likely also be curtailed due to demand. The EPA
document titled AP-42, Section 1.5 Liquified Petroleum Gas Combustion,
updated July 2008, further supports that response, explaining that
burner design technology is specific to fuel type and that retooling
may even be required when changing the fuel type from natural gas to
propane. Retooling may include replacement of fuel injector
[[Page 66056]]
tips and/or vaporizers to provide burners with the proper fuel to air
ratio. In addition, as noted previously in this preamble, there are no
facilities currently subject to subpart SSSSS that manufacture chromium
refractory products. Based on the changes in in kiln and burner design
technologies since 2003, and on the determination that propane backup
is available (or if retooling is required, retooling can be done for
propane instead of other alternative fuels) for all existing sources
subject to this standard and can be part of the design of new sources,
we are removing the alternative fuel usage allowance. As a result, the
use of alternative fuels will not be permitted and will be a deviation
from the work practice standard, which will apply during normal
operation as well as during periods of natural gas curtailment/supply
interruption. The removal of the natural gas alternative fuel allowance
and the requirement to use natural gas or equivalent fuels reflects a
development in our understanding of refractory kiln fuel combustion
technology since promulgation of the original standard.
4. What is the rationale for our final approach for the technology
review?
For the reasons explained in the preamble to the proposed rule (86
FR 3095, January 14, 2021), we proposed amendments to improve the work
practice standard that applies when a continuous kiln THC control
device is bypassed for maintenance to reflect technical developments in
pollution control practices since the promulgation of the original
standard. We evaluated all of the comments received on these
improvements and the EPA's proposed amendments, and for the reasons
explained in the comment responses in section IV.B.3 of this preamble,
we are finalizing amendments to the proposed work practice standard to
further improve the work practices based on the best practices of one
affected source in the source category. We are also finalizing
amendments to the existing work practice standard that permits the use
of alternative fuels when natural gas or equivalent fuel is not
available, after review of the fuel combustion technology used by
sources in the source category in response to public comments. Further
explanation is included in the comment responses in section IV.B.3 of
this preamble. The removal of the natural gas alternative fuel
allowance and the requirement to use natural gas or equivalent fuels
reflects a development in our understanding of refractory kiln fuel
combustion technology since promulgation of the original standard.
C. CAA Sections 112(d)(2) and (3) Amendments for the Refractory
Products Manufacturing Source Category
1. What amendments did we propose pursuant to 112(d)(2) and (3) for the
Refractory Products Manufacturing source category?
In the January 14, 2021 action, we proposed amendments to the
Refractory Products Manufacturing NESHAP to address previously
unregulated HAP for affected sources in the clay and nonclay refractory
subcategories pursuant to 112(d)(2) and (3).
a. Clay Refractory Sources
For new and existing clay refractory kilns, we proposed MACT floor
limits for Hg and for PM (as a surrogate for non-Hg metal HAP), in
addition to the current NESHAP requirements for clay refractory
sources, based on emissions test data for existing clay refractory
kilns. The emissions test data for existing clay kilns reviewed for
this action confirmed trace (but measurable) amounts of non-Hg metal
HAP and Hg emissions. As a result, we proposed MACT floor limits of 3.1
lb/hr for PM and 6.1 micrograms per dry standard cubic meter ([micro]g/
dscm), corrected to 18 percent oxygen, for Hg for each new kiln used to
produce clay refractory products. We proposed MACT floor limits of 9.5
lb/hr for PM and 18 [micro]g/dscm, corrected to 18 percent oxygen, for
Hg for each existing kiln used to produce clay refractory products.
Similar to other source categories, we proposed a limit for PM (as a
surrogate for non-Hg metal HAP) because the metal HAP are contained in
the PM and the control techniques that would be used to control PM will
equally control non-Hg metal HAP. To demonstrate compliance with the
emission limits, we proposed initial and repeat 5-year performance
testing for the regulated pollutants, continuous parameter monitoring,
and daily visible emissions (VE) checks. Owners and operators whose
clay refractory products kilns are equipped with a fabric filter to
reduce PM (as a surrogate for non-Hg metal HAP) have the option of
demonstrating compliance using a bag leak detection (BLD) system
instead of daily VE checks.
We also evaluated the beyond-the-floor option of requiring all
existing sources to meet the proposed new source MACT standards for Hg
and PM (as a surrogate for total non-Hg metal HAP). We concluded that
the costs of the necessary controls were not reasonable relative to the
level of emission reduction achieved for either the Hg or PM beyond-
the-floor options. In addition, these controls would create additional
solid waste, as there would be a need to dispose of the collected
metal-contaminated dust. Therefore, we did not propose beyond-the-floor
limits for Hg or PM. A brief discussion regarding the derivation of the
Hg and PM limits and the beyond-the-floor option was included in the
preamble to the proposed rule (86 FR 3095, January 14, 2021), and a
detailed discussion is included in the technical memorandum titled
Development of Proposed Standards and Impacts for the Refractory
Products Manufacturing NESHAP, located in the docket for this action
(Docket Item No. EPA-HQ-OAR-2020-0148-0014).
b. Nonclay Refractory Sources
For new and existing curing ovens, shape dryers, and kilns that are
used to process refractory products that use organic HAP (i.e., nonclay
refractory sources), we proposed a work practice standard to use
natural gas as fuel to limit metal HAP emissions (except during periods
of natural gas curtailment or supply interruption) as provided in CAA
section 112(h) in lieu of a numerical emissions standard, in addition
to the current NESHAP THC limits for new and existing nonclay
refractory sources. These sources currently employ the use of thermal
oxidizers, regenerative thermal oxidizers and catalytic oxidizers to
meet the THC limit, however, the NESHAP did not require sources to use
natural gas as fuel for sources in this subcategory because the metal
HAP emissions were determined to be below measurable quantities due to
the use of purified nonclay raw materials. Available HAP data for these
sources in the 2017 National Emission Inventory (NEI) were found to be
outdated and not reflective of current operating conditions. The 2017
NEI included measurable PM emissions for these existing nonclay
refractory sources, and the PM would be expected to have trace amounts
of metal HAP; however, we have no emission stack test data to indicate
measurable emissions of metal HAP for these existing nonclay refractory
sources.\2\ Therefore, as discussed in the preamble to the
[[Page 66057]]
proposed rule (86 FR 3095, January 14, 2021), we proposed a work
practice standard to use natural gas as fuel for new and existing
nonclay refractory sources to limit metal HAP emissions in lieu of a
numerical emissions standard in accordance with CAA section 112(h).
---------------------------------------------------------------------------
\2\ Thus, while we believe that there are metal HAP emissions,
the lack of data showing measurable emissions leads the EPA to
conclude that the application of measurement methodology to this
class of sources is not practicable due to technological and
economic limitations. See CAA 112(h)(2)(B).
---------------------------------------------------------------------------
2. How did the 112(d)(2) and (3) amendments change for the Refractory
Products Manufacturing source category?
We are making one change to the proposed CAA section 112(d)(2) and
(3) amendments. For each new kiln used to produce clay refractory
products, we are finalizing the proposed MACT floor limits of 3.1 lb/hr
for PM (as a surrogate for metal HAP) and 6.1 [micro]g/dscm, corrected
to 18 percent oxygen, for Hg. For each existing kiln used to produce
clay refractory products, we are finalizing the proposed MACT floor
limits of 9.5 lb/hr for PM (as a surrogate for metal HAP) and 18
[micro]g/dscm, corrected to 18 percent oxygen, for Hg. We are also
finalizing the proposed requirements for initial and repeat 5-year
performance testing, continuous parameter monitoring, daily VE checks,
and the option of demonstrating compliance using a BLD system instead
of daily VE checks for clay refractory products kilns equipped with a
fabric filter to reduce PM (as a surrogate for metal HAP). For each new
and existing affected source used to produce nonclay refractory
products, we are finalizing the work practice standard to use natural
gas as fuel to limit metal HAP emissions as provided in CAA section
112(h) in lieu of a numerical emissions standard generally as proposed.
However, based on the review of combustion technologies prompted by
public comments on the existing work practice standard to use natural
gas as fuel (see section IV.B.3 of this preamble), the finalized work
practice for new and existing sources used to produce nonclay
refractory products requires the use natural gas or an equivalent fuel
at all times, without an exception during periods when natural gas is
not available.
3. What key comments did we receive on the 112(d)(2) and (3) amendments
and what are our responses?
We received one general comment supporting the proposed CAA section
112(d)(2) and (3) amendments for refractory products manufacturing. The
comment letter also included recommendations for more stringent
standards under CAA section 112(d)(2) and (3) for this source category.
Comment: One commenter supported the EPA's proposed decision to set
numeric emission standards for Hg and for PM as a surrogate for non-Hg
metal HAP for existing clay refractory sources. The commenter noted
that setting limits for all unregulated sources of HAP emissions in
this category is required by CAA section 112(d)(6) (see LEAN v. EPA,
955 F.3d 1088). However, the commenter asserted that the proposed
limits are not strong enough to satisfy the CAA section 112(d)(2)-(3)
requirements and that the standards must reflect the maximum achievable
degree of emission limitation. First, the commenter stated that the
limits were set using insufficient data and that it is not clear why
the EPA did not use its authority under CAA section 114 to collect
additional emission data. Second, the commenter stated that the ``upper
prediction limit'' (UPL) methodology of setting standards is not
consistent with the statutory requirement of the floor as the ``average
emission limitation'' achieved by the best-performing sources, which
violates CAA section 112(d)(3) and is arbitrary. Therefore, the
commenter stated, the proposed standards do not come close to the
``maximum achievable'' degree of emission reduction.
Response: As courts have regularly upheld, the EPA has wide
latitude in determining the extent of data gathering necessary to solve
a problem and courts generally defer to the Agency's decision to
proceed on the basis of imperfect scientific information, rather than
to ``invest the resources to conduct the perfect study.'' Sierra Club
v. EPA, 167 F. 3d 658, 662 (D.C. Cir. 1999)) (``If EPA were required to
gather exhaustive data about a problem for which gathering such data is
not yet feasible, the agency would be unable to act even if such
inaction had potentially significant consequences . . . [A]n agency
must make a judgment in the face of a known risk of unknown degree.''
Mexichem Specialty Resins, Inc., 787 F.3d. 561 (D.C. Cir. 2015)).
Contrary to the commenter's assertion, the EPA had sufficient data
available from the two clay refractory products kilns at Whitacre-Greer
to calculate MACT floors, so additional data collection was not
necessary. In the case of PM, multiple sets of emissions test data were
available for each of the two kilns, allowing for a data set for each
kiln that was robust enough that the EPA did not need to evaluate the
uncertainty associated with a limited dataset for either kiln. Further,
as noted in the memorandum Emissions Data Used to Develop the
Refractory Products Manufacturing Risk and Technology Review (RTR) Risk
Modeling Input Files (Docket Item No. EPA-HQ-OAR-2020-0148-0006), St.
Gobain has three batch tunnel kilns and two continuous tunnel kilns
capable of producing both clay and nonclay refractories, so they would
be subject to the proposed standards for PM and Hg when producing clay
refractories. However, 40 CFR 63.9824 defines a clay refractory product
as ``a refractory product that contains at least 10 percent uncalcined
clay by weight prior to firing in a kiln'' and includes six
classifications of clay (ball clay, bentonite, common clay and shale,
fire clay, fuller's earth, and kaolin). Based on the 2017 raw material
information provided by St. Gobain when the EPA was developing the
inputs file for the risk modeling, the quantities of clay fired do not
meet the 10 percent threshold for the manufacture of clay refractories
and are more consistent with the use of clay as a binder, so these
kilns are expected to be subject to the clay refractory kiln standards
infrequently. Therefore, it is not clear that using the authority under
CAA section 114 for these kilns would have yielded any additional PM or
Hg data for clay refractory kilns. In other words, if the EPA had
requested emissions testing under CAA section 114 for these five kilns
when they manufacture clay refractories, the EPA would have had to wait
for the facility to change their product on each kiln, which may not
have been feasible.
Regarding the UPL approach, in August 2013, the D.C. Circuit issued
its decision in National Association. of Clean Water Agencies (NACWA)
v. EPA, which addressed challenges to the EPA's 2011 Sewage Sludge
Incinerator (SSI) rule, issued under section 129 of the CAA. In NACWA
v. EPA, the court remanded the EPA's use of the UPL methodology to the
Agency for further explanation of how the methodology reflected the
average emissions limitation achieved by the best-performing 12 percent
of sources (for existing sources) and the average emissions limitation
achieved by the best-performing similar source (for new sources). NACWA
v. EPA, 734 F.3d 1115, 1151. Because the UPL methodology used in the
SSI rule was the same as that used in the major source Boiler MACT (40
CFR part 63, subpart DDDDD), the EPA requested a remand of the record
in U.S. Sugar v. EPA in order to address the court's decision in NACWA
v. EPA. The EPA prepared a memorandum explaining the methodology for
the UPL. This memorandum, the EPA's Response to Remand of the Record
for Major Source Boilers, provides a detailed rationale to use the UPL
as the basis of setting a
[[Page 66058]]
MACT floor for new and existing sources, and the methodology and the
explanation in the memorandum were upheld by the D.C. Circuit in U.S.
Sugar v. EPA, 830 F.3d at 639. Following the UPL memorandum, the EPA
issued a subsequent memorandum specifically addressing the application
of the UPL methodology when setting MACT emission limits with limited
datasets, Approach for Applying the Upper Prediction Limit to Limited
Datasets. In that memorandum, the EPA concluded that there are
additional considerations when setting MACT floors for limited
datasets. The D.C. Circuit agreed that the EPA sufficiently explained
the general application of the UPL approach to small datasets in Sierra
Club v. EPA, 895 F.3d 1, 14 (D.C. Cir. 2018). The MACT floors were set
consistent with EPA guidance and with previous court decisions.
4. What is the rationale for our final approach for the 112(d)(2) and
(3) amendments?
For the reasons explained in the preamble to the proposed rule (86
FR 3095, January 14, 2021), and in the comment responses in sections
IV.B.3 and IV.C.3 of this preamble and the comment summary and response
document (available in the docket for this rulemaking), we are
finalizing a work practice requirement to use natural gas at all times
for new and existing clay refractory product sources, and we are making
no changes and are finalizing the proposed 112(d)(2) and (3) amendments
for clay refractory kilns in the Refractory Products Manufacturing
source category.
D. SSM Amendments for the Refractory Products Manufacturing Source
Category
1. What SSM amendments did we propose for the Refractory Products
Manufacturing source category?
We proposed amendments to the Refractory Products Manufacturing
NESHAP to remove and revise provisions related to SSM that are not
consistent with the 2008 court decision that the standards apply at all
times. More information concerning the elimination of SSM provisions is
provided in the preamble to the proposed rule (86 FR 3095, January 14,
2021).
2. How did the SSM amendments change for the Refractory Products
Manufacturing source category?
We are finalizing the SSM provisions as proposed with no changes
(86 FR 3095, January 14, 2021).
3. What key comments did we receive on the SSM amendments and what are
our responses?
We received one general comment supporting the proposed amendments
to the SSM provisions for refractory products manufacturing and three
comments requesting that the rule requirements for this source category
apply at all times, not just during periods of SSM.
4. What is the rationale for our final approach for the SSM provisions?
For the reasons explained in the proposed rule and after evaluation
of the comments on the proposed amendments to the SSM provisions for
the Refractory Products Manufacturing NESHAP, we are finalizing the
proposed amendments related to SSM that are not consistent with the
requirement that the standards apply at all times. More information
concerning the proposed amendments to the SSM provisions is in the
preamble to the proposed rule (86 FR 3095, January 14, 2021).
E. Electronic Reporting Amendments for the Refractory Products
Manufacturing Source Category
1. What electronic reporting amendments did we propose for the
Refractory Products Manufacturing source category?
In the January 14, 2021, notice we proposed amendments to subpart
SSSSS to require owners and operators of refractory product
manufacturing facilities to submit electronic copies of NOCS reports,
performance test results, and performance evaluation results through
the EPA's CDX using CEDRI.
The proposed amendments apply to the NOCS required by 40 CFR
63.7(b) and (c), 40 CFR 63.8(f)(4), 40 CFR 63.9(b) through (e) and (h)
and 40 CFR 63.9812, and performance test results and performance
evaluation results required by 40 CFR 63.9(h), 40 CFR 63.9800, and 40
CFR 63.9814. The proposal would require that all NOCS be submitted as
portable document format (PDF) files and uploaded to CEDRI. For
performance test and performance evaluation results, the proposal would
require test results that use test methods supported by the EPA's ERT
listed on the ERT website\1\ at the time of the test be submitted in
the format generated through the use of the ERT or an electronic file
consistent with the extensible markup language (XML) schema on the ERT
website. Performance test results using test methods that are not
supported by the ERT at the time of the test would be required to be
submitted as a PDF file using the attachment module of the ERT. In
addition, the proposal included two broad circumstances for electronic
reporting extensions. A description of the electronic data submission
process is provided in the memorandum Electronic Reporting Requirements
for New Source Performance Standards (NSPS) and National Emission
Standards for NESHAP Rules, available in the docket for this action
(Docket Item No. EPA-HQ-OAR-2020-0148-0003). The proposed rule
requirements would replace the current rule requirements to submit the
NOCS reports, performance test results, and performance evaluation
results to the Administrator at the appropriate address listed in 40
CFR 63.13. The proposed rule requirement would not affect submittals
required by state air agencies. The proposed compliance date for
existing affected sources to comply with the electronic reporting
requirements for NOCS reports, performance test results, and
performance evaluation results is 181 days after the final rule is
published to begin electronic reporting. New affected sources are
required to comply with the electronic reporting requirements for NOCS
reports, performance test results, and performance evaluation results
on the effective date of the standard or upon startup, whichever is
later.
2. How did the electronic reporting provisions change for the
Refractory Products Manufacturing source category?
No changes were made to the proposed electronic reporting
provisions.
3. What key comments did we receive on the electronic reporting
provisions and what are our responses?
We received one comment letter that addressed the proposed
electronic reporting provisions for refractory products manufacturing.
The commenter generally supported the proposed amendments except for
the proposed provisions of 40 CFR 63.9814(k) and (l) that would provide
instructions for affected sources unable to submit an electronic report
either due to a force majeure event or an outage of CEDRI.
4. What is the rationale for our final approach for the electronic
reporting requirements?
For the reasons explained in the preamble to the proposed rule (86
FR 3095, January 14, 2021) and the comment summary and response
document (available in the docket for this rulemaking), we are making
no
[[Page 66059]]
changes and are finalizing the electronic reporting provisions as
proposed.
F. Technical Amendments for the Refractory Products Manufacturing
Source Category
In the final rule, we are amending 40 CFR 63.9824 and Table 4 to
subpart SSSSS of part 63, as proposed, to clarify the location in 40
CFR part 60 of applicable EPA test methods. We are also amending 40 CFR
63.9814 and 63.9816 to include the requirements to record and report
information on failures to meet the applicable standard.
In the final rule, as proposed, we are adding and updating test
methods that are incorporated by reference. In accordance with
requirements of 1 CFR part 51.5, the EPA is incorporating by reference
the following voluntary consensus standards (VCS) described in the
amendments to 40 CFR 63.14:
ANSI/ASME PTC 19.10-1981, Flue and Exhaust Gas Analyses
[Part 10, Instruments and Apparatus], issued August 31, 1981, proposed
to be IBR approved for Table 4 to subpart SSSSS. This document
specifies methods, apparatus and calculations which are used to
determine quantitatively, the gaseous constituents of the exhausts
including oxygen and carbon dioxide resulting from station combustions
sources.
ASTM D6348-12e1, Standard Test Method for Determination of
Gaseous Compounds by Extractive Direct Interface Fourier Transform
Infrared (FTIR) Spectroscopy, Approved February 1, 2012, proposed to be
IBR approved for Table 4 to subpart SSSSS.
ASTM D6784-16, ``Standard Test Method for Elemental,
Oxidized, Particle-Bound and Total Mercury in Flue Gas Generated from
Coal-Fired Stationary Sources (Ontario Hydro Method),'' (Approved March
1, 2016), proposed to be IBR approved for Table 4 to subpart SSSSS.
EPA-454/R-98-015, Office of Air Quality Planning and
Standards (OAQPS), Fabric Filter Bag Leak Detection Guidance, September
1997, proposed to be IBR approved for 40 CFR 63.9804(f). 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.
V. Summary of Cost, Environmental, and Economic Impacts and Additional
Analyses Conducted
A. What are the affected facilities?
Currently, three major sources subject to the Refractory Products
Manufacturing NESHAP are operating in the United States. The NESHAP
applies to each new, reconstructed, and existing affected source
located at a refractory products manufacturing facility that is a major
source of HAP emissions, is located at a major source of HAP emissions,
or is part of a major source of HAP emissions. A refractory products
manufacturing facility is a plant site that manufactures refractory
products, such as refractory bricks, refractory shapes, monolithics,
kiln furniture, crucibles, and other materials used for lining furnaces
and other high temperature process units. Refractory products
manufacturing facilities typically process raw material by crushing,
grinding, and screening; mixing the processed raw materials with
binders and other additives; forming the refractory mix into shapes;
and drying and firing the shapes. The NESHAP lists the affected sources
for four subcategories across the industry as the shape dryers, curing
ovens, and kilns that are used to manufacture refractory products that
use organic HAP; shape preheaters, pitch working tanks, defumers, and
coking ovens that are used to produce pitch-impregnated refractory
products; kilns that are used to manufacture chromium refractory
products; and kilns that are used to manufacture clay refractory
products. The three major sources currently operating in the U.S. can
be grouped into two of the subcategories and use curing ovens and kilns
that are used to manufacture nonclay refractory products that use
organic HAP and kilns that are used to manufacture clay refractory
products.
B. What are the air quality impacts?
At the current level of control, the estimated emissions of HAP
from the Refractory Products Manufacturing source category are
approximately 40 tpy. The final amendments require that all three major
sources in the Refractory Products Manufacturing source category comply
with the relevant emission standards at all times, including periods of
SSM. The final amendments also limit the number of hours a continuous
kiln THC control device can be bypassed during scheduled maintenance
and require minimizing emissions of THC during bypass periods. We were
unable to quantify the emissions that occur during periods of SSM or
the specific emissions reductions that would occur as a result of this
action. However, eliminating the SSM exemption has the potential to
reduce emissions by requiring facilities to meet the applicable
standard during SSM periods. Requiring the use of natural gas as kiln
fuel at all times also ensures that PM (as a surrogate for non-Hg metal
HAP) and Hg will not be emitted from combustion of coal, fuel oil, or
waste-derived fuels.
Indirect or secondary air emissions impacts are impacts that would
result from the increased electricity usage associated with the
operation of control devices (e.g., 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. The final amendments would have no effect on the energy
needs of the affected facilities in this source category and would,
therefore, have no indirect or secondary air emissions impacts.
C. What are the cost impacts?
We estimate that each facility in this source category will
experience costs as a result of these final amendments. Estimates for
reporting and recordkeeping costs for each facility are associated with
the electronic reporting requirements, elimination of the SSM
exemption, and revision of the requirements that apply during times of
scheduled maintenance of continuous kiln control devices. The costs
associated with the electronic reporting requirements are attributed to
submittal of NOCS reports, performance test results, and performance
evaluation results using CEDRI and include time for becoming familiar
with CEDRI. The costs associated with the revised SSM requirements were
estimated for re-evaluating previously developed SSM record systems.
The costs associated with recordkeeping to document the frequency and
duration of scheduled maintenance of control devices for continuous
kilns were also estimated. The recordkeeping and reporting costs are
presented in section VI.C of this preamble.
We estimate the costs associated with this action are primarily due
to the new compliance testing requirements for the clay refractory
kilns in this action. Two of the major source refractory manufacturing
facilities manufacture clay refractory and are required to conduct
periodic compliance testing for PM as a surrogate for non-Hg metal HAP
and Hg once every 5 years. One clay refractory manufacturing facility
has two continuous kilns and the other has
[[Page 66060]]
two continuous kilns and three batch kilns. The costs associated with
conducting the combined PM and Hg test for each continuous kiln stack
are estimated to be about $23,600. The costs associated with conducting
the combined PM and Hg test for each batch kiln stack are estimated to
be about $31,800. We also assumed that tests for additional stacks at
the same facility would be conducted in the same trip, so the
additional cost is less due to reduced travel costs. The total costs
for the two facilities to test the seven kilns in a single year would
be $115,300. In addition to the testing costs, each facility performing
the testing will have an additional $6,900 in reporting costs per
facility in the year in which the test occurs.
For kilns that meet the limits without any controls, owners or
operators are required to conduct VE monitoring to demonstrate
compliance. One of the continuous kilns is controlled with a wet
scrubber, but the other six kilns are expected to need to conduct VE
monitoring. We estimate that the monitoring will cost $3,740 per year
per stack, for a total of $22,400 per year.
For further information on the potential testing and monitoring
costs, see the memorandum titled Development of Proposed Standards and
Impacts for the Refractory Products Manufacturing NESHAP, located in
the docket for this action (Docket Item No. EPA-HQ-OAR-2020-0148-0014).
D. What are the economic impacts?
The economic impact analysis is designed to inform decision makers
about the potential economic consequences of the compliance costs
outlined in section V.C of this preamble. To assess the maximum
potential impact, the largest cost expected to be experienced in any
one year is compared to the total sales for the ultimate owner of the
affected facilities to estimate the total burden for each owner. For
these final amendments, the total cost of testing, monitoring, and
recordkeeping and reporting is estimated to be $158,140. The total
annual costs associated with the requirements range from 0.00008 to
0.18 percent of annual sales revenue per ultimate owner. These costs
are not expected to result in a significant market impact, regardless
of whether they are passed on to customers or absorbed by the firms.
The EPA also prepared a small business screening assessment to
determine whether any of the identified affected facilities are small
entities, as defined by the U.S. Small Business Administration. One of
the facilities affected by these amendments is a small entity. However,
the annual cost associated with the requirements is 0.18 percent of
annual sales revenue for the owner of that facility. Therefore, there
are no significant economic impacts on a substantial number of small
entities from these amendments.
E. What are the benefits?
As stated above in section V.B. of this preamble, we were unable to
quantify the specific emissions reductions associated with eliminating
the SSM exemption, although this change has the potential to reduce
emissions of volatile organic HAP.
Because these final 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 potential reduction in volatile
organic HAP from this rule.
F. What analysis of environmental justice did we conduct?
Executive Order 12898 directs the EPA to identify the populations
of concern who are most likely to experience unequal burdens from
environmental harms; specifically, minority populations, low-income
populations, and indigenous peoples (59 FR 7629, February 16, 1994).
Additionally, Executive Order 13985 was signed to advance racial equity
and support underserved communities through Federal government actions
(86 FR 7009, January 20, 2021). The EPA defines environmental justice
(EJ) as the fair treatment and meaningful involvement of all people
regardless of race, color, national origin, or income with respect to
the development, implementation, and enforcement of environmental laws,
regulations, and policies. The EPA further defines the term fair
treatment to mean that ``no group of people should bear a
disproportionate burden of environmental harms and risks, including
those resulting from the negative environmental consequences of
industrial, governmental, and commercial operations or programs and
policies'' (https://www.epa.gov/environmentaljustice). In recognizing
that minority and low-income populations often bear an unequal burden
of environmental harms and risks, the EPA continues to consider ways of
protecting them from adverse public health and environmental effects of
air pollution.
Based on an analysis of exposed populations, the EPA determined
that the Refractory Products Manufacturing source category does not
pose a disproportionately high adverse health impact on minority
populations and/or low-income populations, as specified in Executive
Order 12898 (59 FR 7629, February 16, 1994) and referenced in Executive
Order 13985 (86 FR 7009, January 20, 2021). The EPA remains committed
to engaging with communities and stakeholders throughout the
development of air pollution regulations.
To examine the potential for any environmental justice issues that
might be associated with this source category, we performed a
demographic analysis, which is an assessment of risks to individual
demographic groups of the populations living within 5 km and within 50
km of the facilities. In the analysis, we also evaluated the
distribution of HAP-related cancer and noncancer risks from the
Refractory Products Manufacturing source category across different
demographic groups within the populations living near facilities.\3\
---------------------------------------------------------------------------
\3\ Demographic groups included in the analysis are: White,
African American, Native American, other races and multiracial,
Hispanic or Latino, children 17 years of age and under, adults 18 to
64 years of age, adults 65 years of age and over, adults without a
high school diploma, people living below the poverty level, people
living two times the poverty level, and linguistically isolated
people.
---------------------------------------------------------------------------
The results of the demographic analysis for the Refractory Products
Manufacturing source category indicates that no one is exposed to a
cancer risk at or above 1-in-1 million or to a chronic noncancer TOSHI
greater than 1. In addition, no percentages of the populations exposed
to emissions from the source category are higher than their respective
nationwide average percentages. Thus, the populations living near
refractory products manufacturing facilities are similar to the
national average in demographic characteristics, and we do not see a
disproportionately high exposure to the population groups indicated in
the Executive Orders. The methodology and the results of the
demographic analysis are presented in more detail in the technical
report titled Risk and Technology Review--Analysis of Demographic
Factors for Populations Living Near Refractory Products Manufacturing
Source Category Operations, September 2020, available in the docket for
this action (Docket Item No. EPA-HQ-OAR-2020-0148-0007).
G. What analysis of children's environmental health did we conduct?
This action is not subject to Executive Order 13045 because it is
not
[[Page 66061]]
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
section IV.A of this preamble and are further documented in the
Residual Risk Assessment for the Refractory Products Manufacturing
Source Category in Support of the 2020 Risk and Technology Review
Proposed Rule, available in the Refractory Products Manufacturing
docket (Docket Item No. EPA-HQ-OAR-2020-0148-0013).
VI. 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 Orders 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 action have been
submitted for approval to OMB under the PRA. The Information Collection
Request (ICR) document that the EPA prepared has been assigned EPA ICR
number 2040.08. You can find a copy of the ICR in the Refractory
Products Manufacturing Docket (Docket ID No. EPA-HQ-OAR-2020-0148), and
it is briefly summarized here.
As part of the RTR for the Refractory Products Manufacturing
NESHAP, the EPA is not revising the existing emission limit
requirements but is adding new emission limit requirements for existing
clay refractory sources and is adding new work practices for existing
nonclay refractory sources. The EPA is also revising the SSM provisions
of the rule and is adding the use of electronic data reporting for
future performance test result and performance evaluation result
submittals, and NOCS reports. This information is being collected to
assure compliance with 40 CFR part 63, subpart SSSSS.
Respondents/affected entities: Facilities manufacturing refractory
products.
Respondent's obligation to respond: Mandatory (40 CFR part 63,
subpart SSSSS).
Estimated number of respondents: In the 3 years after the
amendments are final, approximately three respondents per year will be
subject to the NESHAP and no additional respondents are expected to
become subject to the NESHAP during that period.
Frequency of response: The total number of responses is 15 per
year.
Total estimated burden: The average annual burden to the three
refractory products manufacturing facilities over the 3 years after the
amendments are final is estimated to be 230 hours (per year). The
average annual burden to the Agency over the 3 years after the
amendments are final is estimated to be 202 hours (per year). Burden is
defined at 5 CFR 1320.3(b).
Total estimated cost: The average annual cost to the refractory
products manufacturing facilities is $27,100 in labor costs in the
first 3 years after the amendments are final. The average annual
capital and operation and maintenance (O&M) cost is $69,900. The total
average annual Agency cost over the first 3 years after the amendments
are final is estimated to be $9,990.
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.
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. The
annualized costs associated with the requirements in this action for
the affected small entities is described in section V.C. above.
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. While this action
creates an enforceable duty on the private sector, the cost does not
exceed $100 million or more.
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. No tribal facilities are known to be engaged in
any of the industries that would be affected by this action. In
addition, the EPA conducted a proximity analysis for this source
category and found that no refractory products manufacturing facilities
are located within 50 miles of tribal lands. 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
section IV.A of this preamble and are further documented in the
Refractory Products Manufacturing Docket.
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 and 1 CFR Part 51
This action involves technical standards. The EPA amended the
Refractory Products Manufacturing NESHAP in this action with two
methods that can be used as alternatives to the EPA methods in the
current NESHAP: ANSI/ASME PTC 19.10-1981, ``Flue and Exhaust Gas
Analyses'' and ASTM D6348-12e1, ``Determination of Gaseous Compounds by
Extractive Direct Interface Fourier Transform (FTIR) Spectroscopy''.
The EPA also amended the Refractory Products Manufacturing NESHAP in
this action with two new methods: EPA Method 29 (portion for Hg only)
and alternative method ASTM D6784-16, ``Standard Test Method for
Elemental, Oxidized, Particle-Bound and Total Mercury in Flue Gas
Generated from Coal-Fired Stationary Sources (Ontario Hydro Method)''.
The EPA also added new guidance to the NESHAP: EPA-454/R-98-015, Office
of Air Quality Planning and Standards (OAQPS), Fabric Filter Bag Leak
Detection Guidance, September 1997. The methods and guidance will be
incorporated by reference as described below.
The EPA is incorporating by reference the VCS ANSI/ASME PTC 19.10-
1981,
[[Page 66062]]
``Flue and Exhaust Gas Analyses.'' This method determines
quantitatively the gaseous constituents of exhausts resulting from
stationary combustion sources. The manual procedures (but not
instrumental procedures) of VCS ANSI/ASME PTC 19.10-1981--Part 10 may
be used as an alternative to EPA Method 3B for measuring the oxygen or
carbon dioxide content of the exhaust gas. The gases covered in ANSI/
ASME PTC 19.10-1981 are oxygen, carbon dioxide, carbon monoxide,
nitrogen, sulfur dioxide, sulfur trioxide, nitric oxide, nitrogen
dioxide, hydrogen sulfide, and hydrocarbons, however the use in this
rule is only applicable to oxygen and carbon dioxide and is an
acceptable alternative to the manual portion only and not the
instrumental portion.
The EPA is incorporating by reference the VCS ASTM D6348-12e1,
``Determination of Gaseous Compounds by Extractive Direct Interface
Fourier Transform (FTIR) Spectroscopy'' as an acceptable alternative to
EPA Method 320. ASTM D6348-03(2010) was determined to be equivalent to
EPA Method 320 with caveats. ASTM D6348-12e1 is a revised version of
ASTM D6348-03(2010) and includes a new section on accepting the results
from the direct measurement of a certified spike gas cylinder, but
lacks the caveats placed on the D6348-03(2010) version. The VCS ASTM
D6348-12e1 ``Determination of Gaseous Compounds by Extractive Direct
Interface Fourier Transform (FTIR) Spectroscopy'' is an extractive FTIR
field test method used to quantify gas phase concentrations of multiple
analytes from stationary source effluent and is an acceptable
alternative to EPA Method 320 at this time with caveats requiring
inclusion of selected annexes to the standard as mandatory. When using
ASTM D6348-12e1, the following conditions must be met:
(1) The test plan preparation and implementation in the Annexes to
ASTM D6348-03, sections A1 through A8 are mandatory; and
(2) In ASTM D6348-03 Annex A5 (Analyte Spiking Technique), the
percent (%) R must be determined for each target analyte (Equation
A5.5).
In order for the test data to be acceptable for a compound, %R must
be 70% >= R <= 130%. If the %R value does not meet this criterion for a
target compound, the test data is not acceptable for that compound and
the test must be repeated for that analyte (i.e., the sampling and/or
analytical procedure should be adjusted before a retest). The %R value
for each compound must be reported in the test report, and all field
measurements must be corrected with the calculated %R value for that
compound by using the following equation: Reported Results = ((Measured
Concentration in Stack))/(%R) x 100.
The EPA is also incorporating by reference the VCS ASTM D6784-16,
``Standard Test Method for Elemental, Oxidized, Particle-Bound and
Total Mercury in Flue Gas Generated from Coal-Fired Stationary Sources
(Ontario Hydro Method)'' as an acceptable alternative to EPA Method 29
(portion for Hg only) as a method for measuring elemental, oxidized,
particle-bound, and total Hg concentrations ranging from approximately
0.5-100 micrograms per normal cubic meter ([mu]g/Nm\3\). This test
method describes equipment and procedures for obtaining samples from
effluent ducts and stacks, equipment and procedures for laboratory
analysis, and procedures for calculating results. VCS ASTM D6784-16
allows for additional flexibility in the sampling and analytical
procedures for the earlier version of the same standard VCS ASTM D6784-
02 (Reapproved 2008).
The EPA is also incorporating by reference EPA-454/R-98-015, Office
of Air Quality Planning and Standards (OAQPS), Fabric Filter Bag Leak
Detection Guidance, September 1997, IBR for 40 CFR 63.9804(f). This
document provides guidance on the use of triboelectric monitors as
fabric filter bag leak detectors and includes fabric filter and
monitoring system descriptions; guidance on monitor selection,
installation, setup, adjustment, and operation; and quality assurance
procedures.
Guidance document EPA-454/R-98-015 and ASTM D6784-16 are 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). The ANSI/ASME document (ANSI/ASME PTC
19.10-1981) is available from the American Society of Mechanical
Engineers (ASME) at http://www.asme.org; by mail at Three Park Avenue,
New York, NY 10016-5990; or by telephone at (800) 843-2763. The ASTM
methods are available from ASTM International at https://www.astm.org;
by mail at 100 Barr Harbor Drive, Post Office Box C700, West
Conshohocken, PA 19428-2959; or by telephone at (610) 832-9585.
J. Executive Order 12898: Federal Actions To Address Environmental
Justice in Minority Populations and Low-Income Populations
The EPA believes that this action does not have 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 the technical report
titled Risk and Technology Review--Analysis of Demographic Factors for
Populations Living Near Refractory Products Manufacturing Source
Category Operations, September 2020, available in the Refractory
Products Manufacturing Docket for this action (Docket Item No. EPA-HQ-
OAR-2020-0148-0007).
The EPA provided opportunities to engage with the EPA on this
action. The Agency offered a public hearing and reached out to
communities in other ways, including meetings to exchange information
with stakeholders about this action. We did not receive a request for a
public hearing, and we did not receive feedback regarding EJ during the
meetings.
K. Congressional Review Act (CRA)
This action is subject to the CRA, and the EPA will submit a rule
report to each House of the Congress and to the Comptroller General of
the United States. This action is not a ``major rule'' as defined by 5
U.S.C. 804(2).
List of Subjects in 40 CFR Part 63
Environmental protection, Administrative practice and procedures,
Air pollution control, Hazardous substances, Incorporation by
reference, Intergovernmental relations, Reporting and recordkeeping
requirements.
Michael S. Regan,
Administrator.
For the reasons set out in the preamble, 40 CFR part 63 is amended
as follows:
PART 63--NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS
FOR SOURCE CATEGORIES
0
1. The authority citation for part 63 continues to read as follows:
Authority: 42 U.S.C. 7401 et seq.
Subpart A--General Provisions
0
2. Section 63.14 is amended by:
0
a. Revising paragraphs (e)(1) and (h)(86);
0
b. Redesignating paragraphs (h)(104) through (118) as paragraphs
(h)(105) through (119);
0
c. Adding new paragraph (h)(104); and
0
d. Revising paragraph (n)(4).
[[Page 66063]]
The revisions and additions read as follows:
Sec. 63.14 Incorporations by reference.
* * * * *
(e) * * *
(1) ANSI/ASME PTC 19.10-1981, Flue and Exhaust Gas Analyses [Part
10, Instruments and Apparatus], issued August 31, 1981, IBR approved
for Sec. Sec. 63.309(k), 63.457(k), 63.772(e) and (h), 63.865(b),
63.997(e), 63.1282(d) and (g), and 63.1625(b), table 5 to subpart EEEE,
Sec. Sec. 63.3166(a), 63.3360(e), 63.3545(a), 63.3555(a), 63.4166(a),
63.4362(a), 63.4766(a), 63.4965(a), and 63.5160(d), table 4 to subpart
UUUU, table 3 to subpart YYYY, Sec. Sec. 63.7822(b), 63.7824(e),
63.7825(b), 63.8000(d), 63.9307(c), 63.9323(a), 63.9621(b) and (c),
63.11148(e), 63.11155(e), 63.11162(f), 63.11163(g), 63.11410(j),
63.11551(a), 63.11646(a), and 63.11945, and table 4 to subpart AAAAA,
table 5 to subpart DDDDD, table 4 to subpart JJJJJ, table 4 to subpart
KKKKK, table 4 to subpart SSSSS, tables 4 and 5 of subpart UUUUU, table
1 to subpart ZZZZZ, and table 4 to subpart JJJJJJ.
* * * * *
(h) * * *
(86) ASTM D6348-12e1, Standard Test Method for Determination of
Gaseous Compounds by Extractive Direct Interface Fourier Transform
Infrared (FTIR) Spectroscopy, Approved February 1, 2012, IBR approved
for Sec. Sec. 63.997(e), 63.1571(a), and 63.2354(b), table 5 to
subpart EEEE, table 4 to subpart UUUU, Sec. Sec. 63.7142(a) and (b)
and 63.8000(d), and table 4 to subpart SSSSS.
* * * * *
(104) ASTM D6784-16, Standard Test Method for Elemental, Oxidized,
Particle-Bound and Total Mercury in Flue Gas Generated from Coal-Fired
Stationary Sources (Ontario Hydro Method), Approved March 1, 2016, IBR
approved for table 4 to subpart SSSSS.
* * * * *
(n) * * *
(4) EPA-454/R-98-015, Office of Air Quality Planning and Standards
(OAQPS), Fabric Filter Bag Leak Detection Guidance, September 1997,
https://nepis.epa.gov/Exe/ZyPDF.cgi?Dockey=2000D5T6.PDF, IBR approved
for Sec. Sec. 63.548(e), 63.864(e), 63.7525(j), 63.8450(e),
63.8600(e), 63.9632(a), 63.9804(f), and 63.11224(f).
* * * * *
Subpart SSSSS--National Emission Standards for Hazardous Air
Pollutants for Refractory Products Manufacturing
0
3. Section 63.9786 is amended by revising paragraphs (a), (b), and
(d)(2) to read as follows:
Sec. 63.9786 When do I have to comply with this subpart?
(a) If you have a new or reconstructed affected source, you must
comply with this subpart according to paragraphs (a)(1) and (2) of this
section.
(1) If the initial startup of your affected source is before April
16, 2003, then you must comply with the emission limitations for new
and reconstructed sources in this subpart no later than April 16, 2003,
except as otherwise specified in Sec. Sec. 63.9792, 63.9812(c) and
(e), and 63.9814(b)(6) and Tables 1 through 11 to this subpart.
(2) If the initial startup of your affected source is after April
16, 2003, then you must comply with the emission limitations for new
and reconstructed sources in this subpart upon initial startup of your
affected source, except as otherwise specified in Sec. Sec. 63.9792,
63.9812(c) and (e), and 63.9814(b)(6) and Tables 1 through 11 to this
subpart.
(b) If you have an existing affected source, you must comply with
the emission limitations for existing sources no later than April 17,
2006, except as otherwise specified in Sec. Sec. 63.9792, 63.9812(c)
and (e), and 63.9814(b)(6) and Tables 1 through 11 to this subpart.
* * * * *
(d) * * *
(2) All other parts of the existing facility must be in compliance
with this subpart by 3 years after the date the area source becomes a
major source, except as otherwise specified in Sec. Sec. 63.9792,
63.9812(c) and (e), and 63.9814(b)(6) and Tables 1 through 11 to this
subpart.
* * * * *
0
4. Section 63.9792 is amended by revising paragraph (a) introductory
text, paragraphs (b) and (c), paragraph (e) introductory text, and
paragraphs (e)(2) and (3) to read as follows:
Sec. 63.9792 What are my general requirements for complying with
this subpart?
(a) You must be in compliance with the emission limitations
(including operating limits and work practice standards) in this
subpart at all times, except during periods specified in paragraphs
(a)(1) and (2) of this section before May 19, 2022. You must be in
compliance with the emission limitations (including operating limits
and work practice standards) in this subpart at all times, on or after
May 19, 2022.
* * * * *
(b) Except as specified in paragraph (e) of this section, before
May 19, 2022, you must always operate and maintain your affected
source, including air pollution control and monitoring equipment,
according to the provisions in Sec. 63.6(e)(1)(i). During the period
between the compliance date specified for your affected source in Sec.
63.9786 and the date upon which continuous monitoring systems have been
installed and validated and any applicable operating limits have been
established, you must maintain a log detailing the operation and
maintenance of the process and emissions control equipment. On and
after May 19, 2022, at all times, you 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 you 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 that 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 affected source.
(c) Before May 19, 2022, you must develop a written startup,
shutdown, and malfunction plan (SSMP) according to the provisions in
Sec. 63.6(e)(3). On or after May 19, 2022, you are not required to
develop a written SSMP according to the provisions in Sec. 63.6(e)(3).
* * * * *
(e) If you own or operate an affected continuous kiln used to
manufacture refractory products that use organic HAP and you must
perform scheduled maintenance on the THC control device for that kiln,
you may bypass the kiln THC control device and continue operating the
kiln subject to the alternative standard established in this paragraph
upon approval by the Administrator, provided you satisfy the conditions
listed in paragraphs (e)(1) through (3) of this section.
* * * * *
(2) Before May 19, 2022, you must minimize HAP emissions during the
period when the kiln is operating, and the control device is out of
service. On
[[Page 66064]]
and after May 19, 2022, you must minimize HAP emissions during the
period when the kiln is operating and the control device is out of
service by complying with the applicable standard in Table 3 to this
subpart.
(3) You must minimize the time period during which the kiln is
operating and the control device is out of service. On and after May
19, 2022, the total time during which the kiln is operating and the
control device is out of service for each year on a 12-month rolling
basis must not exceed 750 hours.
* * * * *
0
5. Section 63.9794 is amended by revising paragraphs (a)(7), (8), (12),
and (13) and paragraph (b)(2) to read as follows:
Sec. 63.9794 What do I need to know about operation, maintenance,
and monitoring plans?
(a) * * *
(7) Before May 19, 2022, procedures for the proper operation and
maintenance of monitoring equipment consistent with the requirements in
Sec. Sec. 63.8(c)(1), (3), (4)(ii), (7), and (8), and 63.9804. On or
after May 19, 2022, procedures for the proper operation and maintenance
of monitoring equipment consistent with the requirements in Sec. Sec.
63.8(c)(3), (4)(ii), (7), and (8), and 63.9804.
(8) Before May 19, 2022, ongoing data quality assurance procedures
in accordance with the general requirements of Sec. 63.8(d). On or
after May 19, 2022, ongoing data quality assurance procedures
consistent with the requirements in Sec. 63.8(d)(1) and (2). You must
keep these written procedures 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, you must 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).
* * * * *
(12) Before Novermber 19, 2021, if you operate a kiln that is
subject to the limits on the type of fuel used, as specified in items 3
and 4 of Table 3 to subpart SSSSS, procedures for using alternative
fuels. On and after Novermber 19, 2021, you may not use a fuel other
than natural gas or equivalent to fire the affected kiln.
(13) If you operate an affected continuous kiln used to manufacture
refractory products that use organic HAP and you plan to take the kiln
THC control device out of service for scheduled maintenance, as
specified in Sec. 63.9792(e), the procedures specified in paragraphs
(a)(13)(i) and (ii) of this section.
(i) Procedures for minimizing HAP emissions from the kiln during
periods of scheduled maintenance of the kiln control device when the
kiln is operating and the control device is out of service. On or after
May 19, 2022, document the average organic HAP processing rate for that
kiln (i.e., the average organic HAP processing rate based on (a) the
actual production on a 6-month rolling basis (not to include periods of
kiln shut down) or (b) the HAP processing rate (lb/hr) that coincides
with the lowest hour of the most recent 3-hour performance test,
whichever is lower), the mass fraction of organic HAP in the resins,
binders, and additives for each product manufactured in the kiln and
procedures for ensuring that the actual organic HAP processing rate on
an hourly basis does not exceed the average organic HAP processing
rate.
(ii) Procedures for minimizing any period of scheduled maintenance
on the kiln control device when the kiln is operating and the control
device is out of service. On or after May 19, 2022, procedures for
ensuring that the total time during which the kiln is operating and the
control device is out of service does not exceed 750 hours for each
year on a 12-month rolling basis.
(b) * * *
(2) After completing the performance tests to demonstrate that
compliance with the emission limits can be achieved at the revised
operating limit parameter value, you must submit the summary of the
performance test results and the revised operating limits as part of
the Notification of Compliance Status required under Sec. 63.9(h) and
the complete test report according to Sec. 63.9814(h).
* * * * *
0
6. Section 63.9800 is amended by revising paragraphs (c) and (d) and
paragraph (g) introductory text and adding paragraph (g)(4) to read as
follows:
Sec. 63.9800 How do I conduct performance tests and establish
operating limits?
* * * * *
(c) Before May 19, 2022, each performance test must be conducted
according to the requirements in Sec. 63.7 and under the specific
conditions in Table 4 to this subpart. On or after May 19, 2022, each
performance test must be conducted under the specific conditions in
Table 4 to this subpart.
(d) Before May 19, 2022, you may not conduct performance tests
during periods of startup, shutdown, or malfunction, as specified in
Sec. 63.7(e)(1). On or after May 19, 2022, you may not conduct
performance tests during periods of malfunction. You also may not
conduct performance tests during periods of startup or shutdown. You
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.
You must make available to the Administrator such records as may be
necessary to determine the conditions of performance tests.
* * * * *
(g) You must use the data gathered during the performance test and
the equations in paragraphs (g)(1) through (4) of this section to
determine compliance with the emission limitations.
* * * * *
(4) To determine compliance with the Hg emission concentration
limit listed in Table 1 to this subpart, you must calculate your
emission concentration corrected to 18 percent oxygen for each test run
using Equation 4 of this section:
[GRAPHIC] [TIFF OMITTED] TR19NO21.573
Where:
CHg-C = Hg concentration, corrected to 18 percent oxygen,
micrograms per dry standard cubic meters ([micro]g/dscm)
CHg = Hg concentration (uncorrected), [micro]g/dscm
[[Page 66065]]
CO2 = oxygen concentration, percent.
* * * * *
0
7. Section 63.9804 is amended by revising paragraphs (a)(13), (e)(1),
and (f)(1) to read as follows:
Sec. 63.9804 What are my monitoring system installation, operation,
and maintenance requirements?
(a) * * *
(13) At all times, you must maintain your CPMS in accordance with
Sec. 63.9792(b), including, but not limited to, keeping the necessary
parts readily available for routine repairs of the CPMS.
* * * * *
(e) * * *
(1) Use a pH CPMS with a minimum accuracy of 0.2 pH
units.
* * * * *
(f) * * *
(1) Each triboelectric bag leak detection system must be installed,
calibrated, operated, and maintained according to the ``Fabric Filter
Bag Leak Detection Guidance'' (EPA-454/R-98-015, September 1997)
(incorporated by reference, see Sec. 63.14). Other types of bag leak
detection systems must be installed, operated, calibrated, and
maintained in a manner consistent with the manufacturer's written
specifications and recommendations.
* * * * *
0
8. Section 63.9806 is amended by revising paragraph (d) to read as
follows:
Sec. 63.9806 How do I demonstrate initial compliance with the
emission limits, operating limits, and work practice standards?
* * * * *
(d) You must submit the Notification of Compliance Status
containing the results of the initial compliance demonstration
according to the requirements in Sec. 63.9812(e). After Novermber 19,
2021 for affected sources that commence construction or reconstruction
after January 14, 2021, and on and after May 19, 2022 for all other
affected sources, you must submit the Notification of Compliance Status
containing the results of the initial compliance demonstration
according to the requirements in Sec. 63.9812(e) and 63.9814(j).
0
9. Section 63.9808 is amended by revising paragraph (b) to read as
follows:
Sec. 63.9808 How do I monitor and collect data to demonstrate
continuous compliance?
* * * * *
(b) At all times, you must maintain your monitoring systems in
accordance with Sec. 63.9792(b), including, but not limited to,
keeping the necessary parts readily available for routine repairs of
the monitoring equipment.
* * * * *
0
10. Section 63.9810 is amended by revising paragraph (e) and adding
paragraph (f) to read as follows:
Sec. 63.9810 How do I demonstrate continuous compliance with the
emission limits, operating limits, and work practice standards?
* * * * *
(e) Before May 19, 2022, you must report each instance in which you
did not meet each emission limit and each operating limit in this
subpart that applies to you. This includes periods of SSM. These
instances are deviations from the emission limitations in this subpart.
These deviations must be reported according to the requirements in
Sec. 63.9814. On or after May 19, 2022, you must report each instance
in which you did not meet each emission limit and each operating limit
in this subpart that applies to you. These instances are deviations
from the emission limitations in this subpart. These deviations must be
reported according to the requirements in Sec. 63.9814.
(1) [Reserved]
(2) Before May 19, 2022, consistent with Sec. Sec. 63.6(e) and
63.7(e)(1), deviations that occur during a period of startup, shutdown,
or malfunction are not violations if you demonstrate to the
Administrator's satisfaction that you were operating in accordance with
Sec. 63.6(e)(1) and your OM&M plan. The Administrator will determine
whether deviations that occur during a period of startup, shutdown, or
malfunction are violations, according to the provisions in Sec.
63.6(e). On or after May 19, 2022, consistent with Sec. Sec.
63.9792(b) and 63.9800(d), deviations are not violations if you
demonstrate to the Administrator's satisfaction that you were operating
in accordance with Sec. 63.9792(b) and your OM&M plan. The
Administrator will determine whether deviations are violations,
according to the provisions in Sec. 63.9792(b).
(f) You must demonstrate continuous compliance with the operating
limits in Table 2 to this subpart for visible emissions (VE) from clay
refractory products kilns that are uncontrolled or equipped with DLA,
dry lime injection fabric filter (DIFF), dry lime scrubber/fabric
filter (DLS/FF) or other dry control device as described in paragraph
(f)(1) or (2) of this section.
(1) VE testing. Monitoring VE at each kiln stack according to the
requirements in paragraphs (f)(1)(i) through (v) of this section.
(i) Perform daily VE observations of each kiln stack according to
the procedures of EPA Method 22 of 40 CFR part 60, appendix A-7. You
must conduct the EPA Method 22 test while the affected source is
operating under normal conditions. The duration of each EPA Method 22
test must be at least 15 minutes.
(ii) If VE are observed during any daily test conducted using EPA
Method 22 of 40 CFR part 60, appendix A-7, you must promptly conduct an
opacity test, according to the procedures of EPA Method 9 of 40 CFR
part 60, appendix A-4. If opacity greater than 10 percent is observed,
you must initiate and complete corrective actions according to your
OM&M plan.
(iii) You may decrease the frequency of EPA Method 22 testing from
daily to weekly for a kiln stack if one of the conditions in paragraph
(f)(1)(iii)(A) or (B) of this section is met.
(A) No VE are observed in 30 consecutive daily EPA Method 22 tests
for any kiln stack; or
(B) No opacity greater than 10 percent is observed during any of
the EPA Method 9 tests for any kiln stack.
(iv) If VE are observed during any weekly test and opacity greater
than 10 percent is observed in the subsequent EPA Method 9 test, you
must promptly initiate and complete corrective actions according to
your OM&M plan, resume testing of that kiln stack following EPA Method
22 of 40 CFR part 60, appendix A-7, on a daily basis, as described in
paragraph (f)(1)(i) of this section, and maintain that schedule until
one of the conditions in paragraph (f)(1)(iii)(A) or (B) of this
section is met, at which time you may again decrease the frequency of
EPA Method 22 testing to a weekly basis.
(v) If greater than 10 percent opacity is observed during any test
conducted using EPA Method 9 of 40 CFR part 60, appendix A-4, you must
report these deviations by following the requirements in Sec. 63.9814.
(2) Alternative to VE testing. In lieu of meeting the requirements
under paragraph (f)(1) of this section, you may conduct a PM test at
least once every year following the initial performance test, according
to the procedures of EPA Method 5 of 40 CFR part 60, appendix A-3, and
the provisions of Sec. 63.9800(e) and (f).
0
11. Section 63.9812 is amended by revising paragraphs (b) and (c),
paragraph (e) introductory text, paragraph (e)(1), paragraph (f)
introductory text, and paragraph (g) to read as follows:
[[Page 66066]]
Sec. 63.9812 What notifications must I submit and when?
* * * * *
(b) As specified in Sec. 63.9(b)(2) and (3), if you start up your
affected source before April 16, 2003, you must submit an Initial
Notification not later than 120 calendar days after April 16, 2003, or
no later than 120 days after the source becomes subject to this
subpart, whichever is later.
(c) As specified in Sec. 63.9(b)(3), if you start up your new or
reconstructed affected source on or after April 16, 2003, you must
submit an Initial Notification not later than 120 calendar days after
you become subject to this subpart. Initial Notifications required to
be submitted after November 19, 2021 for affected sources that commence
construction or reconstruction after January 14, 2021, and on and after
May 19, 2022 for all other affected sources submitting initial
notifications required in Sec. 63.9(b) must be submitted following the
procedure specified in Sec. 63.9814(h) through (l).
* * * * *
(e) If you are required to conduct a performance test, you must
submit a Notification of Compliance Status as specified in Sec.
63.9(h) and paragraphs (e)(1) and (2) of this section. After November
19, 2021 for affected sources that commence construction or
reconstruction after January 14, 2021, and on and after May 19, 2022
for all other affected sources, submit all subsequent Notifications of
Compliance Status following the procedure specified in Sec. 63.9814(h)
through (l).
(1) For each compliance demonstration that includes a performance
test conducted according to the requirements in Table 4 to this
subpart, you must submit the Notification of Compliance Status,
including the summary of the performance test results, before the close
of business on the 60th calendar day following the completion of the
performance test.
* * * * *
(f) Before November 19, 2021, if you operate a clay refractory
products kiln or a chromium refractory products kiln that is subject to
the work practice standard specified in item 3 or 4 of Table 3 to this
subpart, and you intend to use a fuel other than natural gas or
equivalent to fire the affected kiln, you must submit a notification of
alternative fuel use within 48 hours of the declaration of a period of
natural gas curtailment or supply interruption, as defined in Sec.
63.9824. The notification must include the information specified in
paragraphs (f)(1) through (5) of this section. On and after November
19, 2021, you may not use a fuel other than natural gas or equivalent
to fire the affected kiln.
* * * * *
(g) If you own or operate an affected continuous kiln used to
manufacture refractory products that use organic HAP and must perform
scheduled maintenance on the THC control device for that kiln, you must
request approval from the Administrator before bypassing the control
device, as specified in Sec. 63.9792(e). You must submit a separate
request for approval each time you plan to bypass the kiln control
device.
0
12. Section 63.9814 is amended by:
0
a. Revising paragraph (c) introductory text and paragraph (c)(4);
0
b. Adding paragraph (c)(7);
0
c. Revising paragraphs (d) and (e) and paragraph (g) introductory text;
and
0
d. Adding paragraphs (h) through (l).
The revisions and additions read as follows:
Sec. 63.9814 What reports must I submit and when?
* * * * *
(c) The compliance report must contain the information in
paragraphs (c)(1) through (7) of this section.
* * * * *
(4) Before May 19, 2022, if you had a startup, shutdown, or
malfunction during the reporting period, and you took actions
consistent with your SSMP and OM&M plan, the compliance report must
include the information specified in Sec. 63.10(d)(5)(i). On or after
May 19, 2022, if you had a deviation from any emission limitations
(emission limit, operating limit, or work practice standard) during the
reporting period that apply to you, and you took actions consistent
with your OM&M plan, the compliance report must include the information
specified in (d) and (e) of this section.
* * * * *
(7) For each period when an affected continuous kiln used to
manufacture refractory products that use organic HAP was operating
while the THC control device was out of service, the compliance report
must include a description of the control device maintenance performed,
including the information specified in paragraphs (c)(7)(i) through
(vi) of this section.
(i) The date and time when the control device was shut down and
restarted.
(ii) Identification of the kiln that was operating and the number
of hours that the kiln operated while the control device was out of
service.
(iii) A statement of whether or not the control device maintenance
was included in your approved request to bypass the control device
while scheduled maintenance is performed, developed as specified in
Sec. 63.9792(e).
(iv) Before May 19, 2022, a statement of whether emissions were
minimized while the control device was out of service in accordance
with your OM&M plan. After May 19, 2022, a statement of whether
emissions were minimized while the control device was out of service in
accordance with your OM&M plan and the information specified in
paragraphs (c)(7)(iv)(A) through (C) of this section.
(A) The average organic HAP processing rate based on actual
production on a 6-month rolling basis (not to include periods of kiln
shut down) or the lowest hourly organic HAP processing rate from the
most recent performance test on that kiln, whichever is lower.
(B) The actual hourly organic HAP processing rate for the kiln
while the control device was out of service.
(C) The amount of product manufactured and the mass of organic HAP
in the product manufactured in the kiln while the control device was
out of service.
(v) After May 19, 2022, an estimate of the THC emissions from the
continuous kiln stack while the control device was out of service.
(vi) After May 19, 2022, the total number of hours that the kiln
has operated while the control device was out of service during the
last year on a 12-month rolling basis.
(d) Before May 19, 2022, for each deviation from an emission
limitation (emission limit, operating limit, or work practice standard)
that occurs at an affected source where you are not using a CPMS to
comply with the emission limitations in this subpart, the compliance
report must contain the information in paragraphs (c)(1) through (4)
and (d)(1) and (2) of this section. This includes periods of SSM. On or
after May 19, 2022, for each deviation from an emission limitation
(emission limit, operating limit, or work practice standard) that
occurs at an affected source where you are not using a CPMS to comply
with the emission limitations in this subpart, the compliance report
must contain the information in paragraphs (c)(1) through (4) and
(d)(1) through (3) of this section.
(1) The compliance report must include the total operating time of
each affected source during the reporting period.
(2) The compliance report must include information on the number,
[[Page 66067]]
duration in hours, and cause of deviations (including unknown cause, if
applicable) and the corrective action taken.
(3) The compliance report must include the date and time of each
deviation, a list of the affected sources or equipment, and an estimate
of each regulated pollutant emitted over the emission limit and a
description of the method used to estimate the emissions.
(e) Before May 19, 2022, for each deviation from an emission
limitation (emission limit, operating limit, or work practice standard)
occurring at an affected source where you are using a CPMS to comply
with the emission limitation in this subpart, the compliance report
must include the information in paragraphs (c)(1) through (4) and
(e)(1) through (13) of this section. This includes periods of SSM. On
or after May 19, 2022, for each deviation from an emission limitation
(emission limit, operating limit, or work practice standard) occurring
at an affected source where you are using a CPMS to comply with the
emission limitation in this subpart, the compliance report must include
the information in paragraphs (c)(1) through (4) and (e)(1) through
(13) of this section.
(1) The total operating time of each affected source during the
reporting period.
(2) Before May 19, 2022, the date and time that each startup,
shutdown, or malfunction started and stopped. On or after May 19, 2022,
the date and time that each startup, shutdown, or malfunction started
and stopped is not required.
(3) The date, time, and duration in hours that each CPMS was
inoperative.
(4) The date, time and duration in hours that each CPMS was out of
control, including the information in Sec. 63.8(c)(8), as required by
your OM&M plan.
(5) Before May 19, 2022, the date and time that each deviation from
an emission limitation (emission limit, operating limit, or work
practice standard) started and stopped, and whether each deviation
occurred during a period of startup, shutdown, or malfunction. On or
after May 19, 2022, for each deviation from an emission limitation
(emission limit, operating limit, or work practice standard), the date
and time that each deviation started and stopped, the duration in
hours, a list of the affected sources or equipment, an estimate of each
regulated pollutant emitted over the emission limit, and a description
of the method used to estimate the emissions.
(6) A description of corrective action taken in response to a
deviation.
(7) The total number of deviations during the reporting period, a
summary of the total duration in hours of the deviations during the
reporting period, and the total duration as a percentage of the total
source operating time during that reporting period.
(8) Before May 19, 2022, a breakdown of the total duration of the
deviations during the reporting period into those that are due to
startup, shutdown, control equipment problems, process problems, other
known causes, and other unknown causes. On or after May 19, 2022, a
breakdown of the total duration of the deviations during the reporting
period into those that are due to control equipment problems, process
problems, other known causes, and other unknown causes.
(9) A summary of the total duration in hours of CPMS downtime
during the reporting period and the total duration of CPMS downtime as
a percentage of the total source operating time during that reporting
period.
(10) A brief description of the process units.
(11) A brief description of the CPMS.
(12) The date of the latest CPMS initial validation or accuracy
audit.
(13) A description of any changes in CPMS, processes, or controls
since the last reporting period.
* * * * *
(g) Before November 19, 2021, if you operate a clay refractory
products kiln or a chromium refractory products kiln that is subject to
the work practice standard specified in item 3 or 4 of Table 3 to this
subpart, and you use a fuel other than natural gas or equivalent to
fire the affected kiln, you must submit a report of alternative fuel
use within 10 working days after terminating the use of the alternative
fuel. The report must include the information in paragraphs (g)(1)
through (6) of this section. On and after November 19, 2021, you may
not use a fuel other than natural gas or equivalent to fire the
affected kiln.
* * * * *
(h) Beginning on May 19, 2022, within 60 days after the date of
completing each performance test required by this subpart, you must
submit the results of the performance test following the procedures
specified in paragraphs (h)(1) through (3) of this section.
(1) Data collected using test methods supported by the EPA's
Electronic Reporting Tool (ERT) as listed on the EPA's ERT website
(https://www.epa.gov/electronic-reporting-air-emissions/electronic-reporting-tool-ert) at the time of the test. Submit the results of the
performance test to the EPA via the Compliance and Emissions Data
Reporting Interface (CEDRI), which can be accessed through the EPA's
CDX (https://cdx.epa.gov/). The data must be submitted in a file format
generated using the EPA's ERT. Alternatively, you may submit an
electronic file consistent with the extensible markup language (XML)
schema listed on the EPA's ERT website.
(2) Data collected using test methods that are not supported by the
EPA's ERT as listed on the EPA's ERT website at the time of the test.
The results of the performance test must be included as an attachment
in the ERT or an alternate electronic file consistent with the XML
schema listed on the EPA's ERT website. Submit the ERT generated
package or alternative file to the EPA via CEDRI.
(3) Confidential business information (CBI). Do not use CEDRI to
submit information you claim as CBI. Anything submitted using CEDRI
cannot later be claimed CBI. Although we do not expect persons to
assert a claim of CBI, if you wish to assert a CBI claim for some of
the information submitted under paragraph (h)(1) or (2) of this
section, you must submit a complete file, including information claimed
to be CBI, to the EPA. The file must be generated using the EPA's ERT
or an alternate electronic file consistent with the XML schema listed
on the EPA's ERT website. Submit the file on a compact disc, flash
drive, or other commonly used electronic storage medium and clearly
mark the medium as CBI. Mail the electronic medium 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 file with the
CBI omitted must be submitted to the EPA via the EPA's CDX as described
in paragraphs (h)(1) and (2) of this section. All CBI claims must be
asserted at the time of submission. Furthermore, under CAA section
114(c), emissions data is not entitled to confidential treatment, and
the EPA is required to make emissions data available to the public.
Thus, emissions data will not be protected as CBI and will be made
publicly available.
(i) Beginning on May 19, 2022, within 60 days after the date of
completing each continuous emissions monitoring system (CEMS)
performance evaluation (as defined in Sec. 63.2), you must submit the
results of the performance evaluation following the procedures
specified in paragraphs (i)(1) through (3) of this section.
[[Page 66068]]
(1) Performance evaluations of CEMS measuring relative accuracy
test audit (RATA) pollutants that are supported by the EPA's ERT as
listed on the EPA's ERT website at the time of the evaluation. Submit
the results of the performance evaluation to the EPA via CEDRI, which
can be accessed through the EPA's CDX. The data must be submitted in a
file format generated using the EPA's ERT. Alternatively, you may
submit an electronic file consistent with the XML schema listed on the
EPA's ERT website.
(2) Performance evaluations of CEMS measuring RATA pollutants that
are not supported by the EPA's ERT as listed on the EPA's ERT website
at the time of the evaluation. The results of the performance
evaluation must be included as an attachment in the ERT or an alternate
electronic file consistent with the XML schema listed on the EPA's ERT
website. Submit the ERT generated package or alternative file to the
EPA via CEDRI.
(3) CBI. Do not use CEDRI to submit information you claim as CBI.
Anything submitted using CEDRI cannot later be claimed CBI. Although we
do not expect persons to assert a claim of CBI, if you wish to assert a
CBI claim for some of the information submitted under paragraph (i)(1)
or (2) of this section, you must submit a complete file, including
information claimed to be CBI, to the EPA. The file must be generated
using the EPA's ERT or an alternate electronic file consistent with the
XML schema listed on the EPA's ERT website. Submit the file on a
compact disc, flash drive, or other commonly used electronic storage
medium and clearly mark the medium as CBI. Mail the electronic medium
to U.S. EPA/OAQPS/CORE CBI Office, Attention: Group Leader, Measurement
Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same
file with the CBI omitted must be submitted to the EPA via the EPA's
CDX as described in paragraphs (h)(1) and (2) of this section. All CBI
claims must be asserted at the time of submission. Furthermore, under
CAA section 114(c), emissions data is not entitled to confidential
treatment, and the EPA is required to make emissions data available to
the public. Thus, emissions data will not be protected as CBI and will
be made publicly available.
(j) Beginning May 19, 2022, you must submit all subsequent
Notification of Compliance Status reports in PDF format to the EPA via
CEDRI, which can be accessed through EPA's CDX (https://cdx.epa.gov/
).The EPA will make all the information submitted through CEDRI
available to the public without further notice to you. Do not use CEDRI
to submit information you claim as CBI. Anything submitted using CEDRI
cannot later be claimed CBI. Although we do not expect persons to
assert a claim of CBI, if you wish to assert a CBI claim, submit a
complete report, including information claimed to be CBI, to the EPA.
Submit the file on a compact disc, flash drive, or other commonly used
electronic storage medium and clearly mark the medium as CBI. Mail the
electronic medium to U.S. EPA/OAQPS/CORE CBI Office, Attention:
Refractory Lead MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The
same file with the CBI omitted must be submitted to the EPA via the
EPA's CDX as described earlier in this paragraph (j). All CBI claims
must be asserted at the time of submission. Furthermore, under CAA
section 114(c), emissions data is not entitled to confidential
treatment, and the EPA is required to make emissions data available to
the public. Thus, emissions data will not be protected as CBI and will
be made publicly available.
(k) If you are required to electronically submit a report through
CEDRI in the EPA's CDX, you may assert a claim of EPA system outage for
failure to timely comply with that reporting requirement. To assert a
claim of EPA system outage, you must meet the requirements outlined in
paragraphs (k)(1) through (7) of this section.
(1) You must have been or will be precluded from accessing CEDRI
and submitting a required report within the time prescribed due to an
outage of either the EPA's CEDRI or CDX systems.
(2) The outage must have occurred within the period of time
beginning five business days prior to the date that the submission is
due.
(3) The outage may be planned or unplanned.
(4) You must submit notification to the Administrator in writing as
soon as possible following the date you first knew, or through due
diligence should have known, that the event may cause or has caused a
delay in reporting.
(5) You must provide to the Administrator a written description
identifying:
(i) The date(s) and time(s) when CDX or CEDRI was accessed and the
system was unavailable;
(ii) A rationale for attributing the delay in reporting beyond the
regulatory deadline to EPA system outage;
(iii) A description of measures taken or to be taken to minimize
the delay in reporting; and
(iv) The date by which you propose to report, or if you have
already met the reporting requirement at the time of the notification,
the date you reported.
(6) The decision to accept the claim of EPA system outage and allow
an extension to the reporting deadline is solely within the discretion
of the Administrator.
(7) In any circumstance, the report must be submitted
electronically as soon as possible after the outage is resolved.
(l) If you are required to electronically submit a report through
CEDRI in the EPA's CDX, you may assert a claim of force majeure for
failure to timely comply with that reporting requirement. To assert a
claim of force majeure, you must meet the requirements outlined in
paragraphs (l)(1) through (5) of this section.
(1) You may submit a claim if a force majeure event is about to
occur, occurs, or has occurred or there are lingering effects from such
an event within the period of time beginning five business days prior
to the date the submission is due. For the purposes of this section, a
force majeure event is defined as an event that will be or has been
caused by circumstances beyond the control of the affected facility,
its contractors, or any entity controlled by the affected facility that
prevents you from complying with the requirement to submit a report
electronically within the time period prescribed. Examples of such
events are acts of nature (e.g., hurricanes, earthquakes, or floods),
acts of war or terrorism, or equipment failure or safety hazard beyond
the control of the affected facility (e.g., large scale power outage).
(2) You must submit notification to the Administrator in writing as
soon as possible following the date you first knew, or through due
diligence should have known, that the event may cause or has caused a
delay in reporting.
(3) You must provide to the Administrator:
(i) A written description of the force majeure event;
(ii) A rationale for attributing the delay in reporting beyond the
regulatory deadline to the force majeure event;
(iii) A description of measures taken or to be taken to minimize
the delay in reporting; and
(iv) The date by which you propose to report, or if you have
already met the reporting requirement at the time of the notification,
the date you reported.
(4) The decision to accept the claim of force majeure and allow an
extension to the reporting deadline is solely within the discretion of
the Administrator.
(5) In any circumstance, the reporting must occur as soon as
possible after the force majeure event occurs.
[[Page 66069]]
0
13. Section 63.9816 is amended by revising paragraph (a)(2) and
paragraphs (c)(5), (8), and (10) to read as follows:
Sec. 63.9816 What records must I keep?
(a) * * *
(2) Before May 19, 2022, the records in Sec. 63.6(e)(3)(iii)
through (v) related SSM.
* * * * *
(c) * * *
(5) For each deviation of an operating limit parameter value,
record the information in paragraphs (c)(5)(i) through (iv) of this
section.
(i) The date, time, and duration in hours of the deviation.
(ii) On or after May 19, 2022, a list of the affected sources or
equipment.
(iii) On or after May 19, 2022, an estimate of the quantity in
pounds of each regulated pollutant over any emission limit and a
description of the method used to estimate emissions.
(iv) Actions taken to minimize emissions in accordance with Sec.
63.9792(b), a brief explanation of the cause of the deviation, and the
corrective action taken to return the affected unit to its normal or
usual manner of operation.
* * * * *
(8) Records of maintenance activities and inspections performed on
control devices, including all records associated with the scheduled
maintenance of the THC control devices on continuous kilns used to
manufacture refractory products that use organic HAP, as specified in
Sec. 63.9792(e).
* * * * *
(10) Current copies of the OM&M plan, including any revisions and
records documenting conformance with those revisions.
0
14. Section 63.9820 is revised to read as follows:
Sec. 63.9820 What parts of the General Provisions apply to me?
Table 11 to this subpart shows which parts of the General
Provisions specified in Sec. Sec. 63.1 through 63.16 apply to you.
0
15. Section 63.9822 is amended by revising paragraph (c) introductory
text and adding paragraph (c)(5) to read as follows:
Sec. 63.9822 Who implements and enforces this subpart?
* * * * *
(c) The authorities that cannot be delegated to state, local, or
tribal agencies are as specified in paragraphs (c)(1) through (5) of
this section.
* * * * *
(5) Approval of an alternative to any electronic reporting to the
EPA required by this subpart.
0
16. Section 63.9824 is amended by revising the definition of
``Particulate matter (PM)'' to read as follows:
Sec. 63.9824 What definitions apply to this subpart?
* * * * *
Particulate matter (PM) means, for the purposes of this subpart,
emissions of particulate matter that serve as a measure of total
particulate emissions as measured by EPA Method 5 of 40 CFR part 60,
appendix A-3.
* * * * *
0
17. Table 1 to Subpart SSSSS is revised to read as follows:
Table 1 to Subpart SSSSS of Part 63--Emission Limits
As stated in Sec. 63.9788, you must comply with the emission
limits for affected sources in the following table:
------------------------------------------------------------------------
You must meet the following emission
For . . . limits . . .
------------------------------------------------------------------------
1. Each new or existing curing As specified in items 2 through 9 of
oven, shape dryer, and kiln that this table.
is used to process refractory
products that use organic HAP;
each new or existing coking oven
and defumer that is used to
produce pitch-impregnated
refractory products; each new
shape preheater that is used to
produce pitch-impregnated
refractory products; AND each new
or existing process unit that is
exhausted to a thermal or
catalytic oxidizer that also
controls emissions from an
affected shape preheater or pitch
working tank.
2. Continuous process units that a. The 3-hour block average THC
are controlled with a thermal or concentration must not exceed 20
catalytic oxidizer. parts per million by volume, dry
basis (ppmvd), corrected to 18
percent oxygen, at the outlet of
the control device; or
b. The 3-hour block average THC mass
emissions rate must be reduced by
at least 95 percent.
3. Continuous process units that a. The 3-hour block average THC
are equipped with a control concentration must not exceed 20
device other than a thermal or ppmvd, corrected to 18 percent
catalytic oxidizer. oxygen, at the outlet of the
control device; or
b. The 3-hour block average THC mass
emissions rate must be reduced by
at least 95 percent.
4. Continuous process units that The 3-hour block average THC
use process changes to reduce concentration must not exceed 20
organic HAP emissions. ppmvd, corrected to 18 percent
oxygen, at the outlet of the
process gas stream.
5. Continuous kilns that are not The 3-hour block average THC
equipped with a control device. concentration must not exceed 20
ppmvd, corrected to 18 percent
oxygen, at the outlet of the
process gas stream.
6. Batch process units that are a. The 2-run block average THC
controlled with a thermal or concentration for the 3-hour peak
catalytic oxidizer. emissions period must not exceed 20
ppmvd, corrected to 18 percent
oxygen, at the outlet of the
control device; or
b. The 2-run block average THC mass
emissions rate for the 3-hour peak
emissions period must be reduced by
at least 95 percent.
7. Batch process units that are a. The 2-run block average THC
equipped with a control device concentration for the 3-hour peak
other than a thermal or catalytic emissions period must not exceed 20
oxidizer. ppmvd, corrected to 18 percent
oxygen, at the outlet of the
control device; or
b. The 2-run block average THC mass
emissions rate for the 3-hour peak
emissions period must be reduced by
at least 95 percent.
[[Page 66070]]
8. Batch process units that use The 2-run block average THC
process changes to reduce organic concentration for the 3-hour peak
HAP emissions. emissions period must not exceed 20
ppmvd, corrected to 18 percent
oxygen, at the outlet of the
process gas stream.
9. Batch process kilns that are The 2-run block average THC
not equipped with a control concentration for the 3-hour peak
device. emissions period must not exceed 20
ppmvd, corrected to 18 percent
oxygen, at the outlet of the
process gas stream.
10. Each new continuous kiln that a. The 3-hour block average HF
is used to produce clay emissions must not exceed 0.019
refractory products. kilograms per megagram (kg/Mg)
(0.038 pounds per ton (lb/ton)) of
uncalcined clay processed, OR the 3-
hour block average HF mass
emissions rate must be reduced by
at least 90 percent; and
b. The 3-hour block average HCl
emissions must not exceed 0.091 kg/
Mg (0.18 lb/ton) of uncalcined clay
processed, OR the 3-hour block
average HCl mass emissions rate
must be reduced by at least 30
percent; and
c. The 3-hour block average PM
emissions must not exceed 1.4 kg/Mg
(3.1 lb/hr); and
d. The 3-hour block average Hg
concentration must not exceed 6.1
micrograms per dry standard cubic
meter ([micro]g/dscm), corrected to
18 percent oxygen, at the outlet of
the control device or the process
gas stream.
11. Each new batch process kiln a. The 2-run block average HF mass
that is used to produce clay emissions rate for the 3-hour peak
refractory products. emissions period must be reduced by
at least 90 percent; and
b. The 2-run block average HCl mass
emissions rate for the 3-hour peak
emissions period must be reduced by
at least 30 percent; and
c. The 2-run block average PM
emissions for the 3-hour peak
emissions period must not exceed
1.4 kg/Mg (3.1 lb/hr); and
d. The 2-run block average Hg
concentration for the 3-hour peak
emissions period must not exceed
6.1 [micro]g/dscm, corrected to 18
percent oxygen, at the outlet of
the control device or the process
gas stream.
12. Each existing continuous kiln a. The 3-hour block average PM
that is used to produce clay emissions must not exceed 4.3 kg/Mg
refractory products on and after (9.5 lb/hr); and
November 20, 2022. b. The 3-hour block average Hg
concentration must not exceed 18
[micro]g/dscm, corrected to 18
percent oxygen, at the outlet of
the control device or the process
gas stream.
13. Each existing batch kiln that a. The 2-run block average PM
is used to produce clay emissions for the 3-hour peak
refractory products on and after emissions period must not exceed
November 20, 2022. 4.3 kg/Mg (9.5 lb/hr); and
b. The 2-run block average Hg
concentration for the 3-hour peak
emissions period must not exceed 18
[micro]g/dscm, corrected to 18
percent oxygen, at the outlet of
the control device or the process
gas stream.
------------------------------------------------------------------------
0
18. Table 2 to Subpart SSSSS is revised to read as follows:
Table 2 to Subpart SSSSS of Part 63--Operating Limits
As stated in Sec. 63.9788, you must comply with the operating
limits for affected sources in the following table:
------------------------------------------------------------------------
For . . . You must . . .
------------------------------------------------------------------------
1. Each affected source listed in a. Operate all affected sources
Table 1 to this subpart. according to the requirements to
this subpart on and after the date
on which the initial performance
test is conducted or required to be
conducted, whichever date is
earlier; and
b. Capture emissions and vent them
through a closed system; and
c. Operate each control device that
is required to comply with this
subpart on each affected source
during all periods that the source
is operating, except where
specified in Sec. 63.9792(e),
item 2 of this table, item 5 of
Table 3 to this subpart, item 13 of
Table 4 to this subpart, and item 6
of Table 9 to this subpart for THC
control devices on continuous kilns
used to manufacture refractory
products that use organic HAP; and
d. Record all operating parameters
specified in Table 8 to this
subpart for the affected source;
and
e. Prepare and implement a written
OM&M plan as specified in Sec.
63.9792(d).
2. Each affected continuous kiln a. Receive approval from the
used to manufacture refractory Administrator before taking the
products that use organic HAP control device on the affected kiln
that is equipped with an emission out of service for scheduled
control device for THC. maintenance, as specified in Sec.
63.9792(e); and
b. Before May 19, 2022, minimize HAP
emissions from the affected kiln
during all periods of scheduled
maintenance of the kiln control
device when the kiln is operating
and the control device is out of
service; on and after May 19, 2022,
you must minimize HAP emissions
during the period when the kiln is
operating and the control device is
out of service by complying with
the applicable standard in Table 3
to this subpart; and
c. Minimize the duration of all
periods of scheduled maintenance of
the kiln control device when the
kiln is operating and the control
device is out of service. On and
after May 19, 2022, the total time
during which the kiln is operating
and the control device is out of
service for the each year on a 12-
month rolling basis must not exceed
750 hours.
[[Page 66071]]
3. Each new or existing curing Satisfy the applicable operating
oven, shape dryer, and kiln that limits specified in items 4 through
is used to process refractory 9 of this table.
products that use organic HAP;
each new or existing coking oven
and defumer that is used to
produce pitch-impregnated
refractory products; each new
shape preheater that is used to
produce pitch-impregnated
refractory products; AND each new
or existing process unit that is
exhausted to a thermal or
catalytic oxidizer that also
controls emissions from an
affected shape preheater or pitch
working tank.
4. Each affected continuous Maintain the 3-hour block average
process unit. organic HAP processing rate (pounds
per hour) at or below the maximum
organic HAP processing rate
established during the most recent
performance test.
5. Continuous process units that Maintain the 3-hour block average
are equipped with a thermal operating temperature in the
oxidizer. thermal oxidizer combustion chamber
at or above the minimum allowable
operating temperature for the
oxidizer established during the
most recent performance test.
6. Continuous process units that a. Maintain the 3-hour block average
are equipped with a catalytic operating temperature at the inlet
oxidizer. of the catalyst bed of the oxidizer
at or above the minimum allowable
operating temperature for the
oxidizer established during the
most recent performance test; and
b. Check the activity level of the
catalyst at least every 12 months.
7. Each affected batch process For each batch cycle, maintain the
unit. organic HAP processing rate (pounds
per batch) at or below the maximum
organic HAP processing rate
established during the most recent
performance test.
8. Batch process units that are a. From the start of each batch
equipped with a thermal oxidizer. cycle until 3 hours have passed
since the process unit reached
maximum temperature, maintain the
hourly average operating
temperature in the thermal oxidizer
combustion chamber at or above the
minimum allowable operating
temperature established for the
corresponding period during the
most recent performance test, as
determined according to item 11 of
Table 4 to this subpart; and
b. For each subsequent hour of the
batch cycle, maintain the hourly
average operating temperature in
the thermal oxidizer combustion
chamber at or above the minimum
allowable operating temperature
established for the corresponding
hour during the most recent
performance test, as specified in
item 13 of Table 4 to this subpart.
9. Batch process units that are a. From the start of each batch
equipped with a catalytic cycle until 3 hours have passed
oxidizer. since the process unit reached
maximum temperature, maintain the
hourly average operating
temperature at the inlet of the
catalyst bed at or above the
minimum allowable operating
temperature established for the
corresponding period during the
most recent performance test, as
determined according to item 12 of
Table 4 to this subpart; and
b. For each subsequent hour of the
batch cycle, maintain the hourly
average operating temperature at
the inlet of the catalyst bed at or
above the minimum allowable
operating temperature established
for the corresponding hour during
the most recent performance test,
as specified in item 13 of Table 4
to this subpart; and
c. Check the activity level of the
catalyst at least every 12 months.
10. Each new kiln that is used to Satisfy the applicable operating
process clay refractory products. limits specified in items 11
through 13 of this table.
11. Each affected kiln that is a. Maintain the 3-hour block average
equipped with a DLA. pressure drop across the DLA at or
above the minimum levels
established during the most recent
performance test; and
b. Maintain free-flowing limestone
in the feed hopper, silo, and DLA
at all times; and
c. Maintain the limestone feeder at
or above the level established
during the most recent performance
test; and
d. Use the same grade of limestone
from the same source as was used
during the most recent performance
test and maintain records of the
source and type of limestone used;
and
e. Maintain no VE from the stack.
12. Each affected kiln that is a. Initiate corrective action within
equipped with a DIFF or DLS/FF. 1 hour of a bag leak detection
system alarm and complete
corrective actions in accordance
with the OM&M plan; and
b. Verify at least once each 8-hour
shift that lime is free-flowing by
means of a visual check, checking
the output of a load cell, carrier
gas/lime flow indicator, or carrier
gas pressure drop measurement
system; and
c. Record the lime feeder setting
daily to verify that the feeder
setting is at or above the level
established during the most recent
performance test.
13. Each affected kiln that is a. Maintain the 3-hour block average
equipped with a wet scrubber. pressure drop across the scrubber,
liquid pH, and liquid flow rate at
or above the minimum levels
established during the most recent
performance test; and
b. If chemicals are added to the
scrubber liquid, maintain the 3-
hour block average chemical feed
rate at or above the minimum
chemical feed rate established
during the most recent performance
test.
14. Each new and existing kiln Maintain the average carbon flow
used to process clay refractory rate for each 3-hour block period
products that is equipped with an at or above the average carbon flow
activated carbon injection system. rate established during the Hg
performance test in which
compliance was demonstrated.
[[Page 66072]]
15. Each new and existing kiln Maintain no VE from the stack.
that is used to process clay
refractory products with no add-
on control and each existing kiln
that is equipped with a DLA.
16. Each existing kiln used to Initiate corrective action within 1
process clay refractory products hour of a bag leak detection system
that is equipped with a FF. alarm and complete corrective
actions in accordance with the OM&M
plan OR maintain no VE from the
stack.
17. Each existing kiln used to Maintain the 3-hour block average
process clay refractory products pressure drop across the scrubber
that is equipped with a wet and liquid flow rate at or above
scrubber. the minimum levels established
during the most recent performance
test.
------------------------------------------------------------------------
0
19. Table 3 to Subpart SSSSS is revised to read as follows:
Table 3 to Subpart SSSSS of Part 63--Work Practice Standards
As stated in Sec. 63.9788, you must comply with the work practice
standards for affected sources in the following table:
----------------------------------------------------------------------------------------------------------------
According to one of the following
For . . . You must . . . requirements . . .
----------------------------------------------------------------------------------------------------------------
1. Each basket or container that is used a. Control POM emissions i. At least every 10 preheating cycles,
for holding fired refractory shapes in from any affected shape clean the residual pitch from the
an existing shape preheater and preheater. surfaces of the basket or container by
autoclave during the pitch impregnation abrasive blasting prior to placing the
process. basket or container in the affected
shape preheater; or
ii. At least every 10 preheating cycles,
subject the basket or container to a
thermal process cycle that meets or
exceeds the operating temperature and
cycle time of the affected preheater,
AND is conducted in a process unit that
is exhausted to a thermal or catalytic
oxidizer that is comparable to the
control device used on an affected
defumer or coking oven; or
iii. Capture emissions from the affected
shape preheater and vent them to the
control device that is used to control
emissions from an affected defumer or
coking oven, or to a comparable thermal
or catalytic oxidizer.
2. Each new or existing pitch working Control POM emissions...... Capture emissions from the affected pitch
tank. working tank and vent them to the
control device that is used to control
emissions from an affected defumer or
coking oven, OR to a comparable thermal
or catalytic oxidizer.
3. Each new or existing chromium Minimize fuel-based HAP Before May 19, 2022, use natural gas, or
refractory products kiln. emissions. equivalent, as the kiln fuel, except
during periods of natural gas
curtailment or supply interruption, as
defined in Sec. 63.9824. On and after
May 19, 2022, use natural gas, or
equivalent, as the kiln fuel at all
times.
4. Each existing clay refractory Minimize fuel-based HAP Before May 19, 2022, use natural gas, or
products kiln. emissions. equivalent, as the kiln fuel, except
during periods of natural gas
curtailment or supply interruption, as
defined in Sec. 63.9824. On and after
May 19, 2022, use natural gas, or
equivalent, as the kiln fuel at all
times.
5. Each affected continuous kiln used to Minimize HAP emissions..... i. Before May 19, 2022, minimize HAP
manufacture refractory products that emissions from the affected kiln during
use organic HAP that is equipped with all periods of scheduled maintenance of
an emission control device for THC with the kiln control device when the kiln is
Administrator approval to take the operating and the control device is out
control device out of service for of service consistent with your OM&M
scheduled maintenance, as specified in plan and minimize the time period during
Sec. 63.9792(e). which the kiln is operating and the
control device is out of service; or
ii. On and after May 19, 2022, minimize
HAP emissions during the period when the
kiln is operating and the control device
is out of service by maintaining the
organic HAP processing rate (lb/hr)
below the average organic HAP processing
rate based on actual production on a 6-
month rolling basis (not to include
periods of kiln shut down) or below the
organic HAP processing rate (lb/hr) that
coincides with the lowest hour of the
most recent 3-hour performance test,
whichever is lower); and minimize the
time period during which the kiln is
operating and the control device is out
of service, not to exceed 750 hours for
the year (on a 12-month rolling basis).
6. Each new or existing curing oven, Minimize fuel-based HAP Use natural gas, or equivalent, as the
shape dryer, and kiln that is used to emissions. kiln fuel, at all times.
process refractory products that use
organic HAP, on and after Novermber 19,
2021.
----------------------------------------------------------------------------------------------------------------
[[Page 66073]]
0
20. Table 4 to Subpart SSSSS is revised to read as follows:
Table 4 to Subpart SSSSS to Part 63--Requirements for Performance Tests
As stated in Sec. 63.9800, you must comply with the requirements
for performance tests for affected sources in the following table:
----------------------------------------------------------------------------------------------------------------
According to the following
For . . . You must . . . Using . . . requirements . . .
----------------------------------------------------------------------------------------------------------------
1. Each affected source listed a. Conduct i. The requirements of (1) Record the date of the test;
in Table 1 to this subpart. performance tests. the general provisions and
in subpart A of this (2) Identify the emission source
part and the that is tested; and
requirements to this (3) Collect and record the
subpart. corresponding operating
parameter and emission test data
listed in this table for each
run of the performance test; and
(4) Repeat the performance test
at least every 5 years; and
(5) Repeat the performance test
before changing the parameter
value for any operating limit
specified in your OM&M plan; and
(6) If complying with the THC
concentration or THC percentage
reduction limits specified in
items 2 through 9 of Table 1 to
this subpart, repeat the
performance test under the
conditions specified in items
2.a.2. and 2.a.3. of this table;
and
(7) If complying with the
emission limits for new clay
refractory products kilns
specified in items 10 and 11 of
Table 1 to this subpart, repeat
the performance test under the
conditions specified in items
14.a.i.4. and 17.a.i.4. of this
table.
b. Select the i. Method 1 or 1A of 40 (1) To demonstrate compliance
locations of CFR part 60, appendix with the percentage reduction
sampling ports A-1. limits specified in items 2.b.,
and the number of 3.b., 6.b., 7.b., 10, and 11 of
traverse points. Table 1 to this subpart, locate
sampling sites at the inlet of
the control device and at either
the outlet of the control device
or at the stack prior to any
releases to the atmosphere; and
(2) To demonstrate compliance
with any other emission limit
specified in Table 1 to this
subpart, locate all sampling
sites at the outlet of the
control device or at the stack
prior to any releases to the
atmosphere.
c. Determine gas Method 2, 2A, 2C, 2D, Measure gas velocities and
velocity and 2F, or 2G of 40 CFR volumetric flow rates at 1-hour
volumetric flow part 60, appendix A-1 intervals throughout each test
rate. and A-2. run.
d. Conduct gas i. Method 3, 3A, or 3B As specified in the applicable
molecular weight of 40 CFR part 60, test method.
analysis. appendix A-2; or. You may use the manual procedures
ii. ASME PTC 19.10- (but not instrumental
1981--Part 10 \a\. procedures) of ASME PTC 19.10-
1981--Part 10 \a\ as an
alternative to EPA Method 3B.
e. Measure gas Method 4 of 40 CFR part As specified in the applicable
moisture content. 60, appendix A-3. test method.
[[Page 66074]]
2. Each new or existing curing a. Conduct ....................... (1) Conduct the performance test
oven, shape dryer, and kiln performance tests. while the source is operating at
that is used to process the maximum organic HAP
refractory products that use processing rate, as defined in
organic HAP; each new or Sec. 63.9824, reasonably
existing coking oven and expected to occur; and
defumer that is used to produce (2) Repeat the performance test
pitch-impregnated refractory before starting production of
products; each new shape any product for which the
preheater that is used to organic HAP processing rate is
produce pitch-impregnated likely to exceed the maximum
refractory products; AND each organic HAP processing rate
new or existing process unit established during the most
that is exhausted to a thermal recent performance test by more
or catalytic oxidizer that also than 10 percent, as specified in
controls emissions from an Sec. 63.9798(c); and
affected shape preheater or (3) Repeat the performance test
pitch working tank. on any affected uncontrolled
kiln following process changes
(e.g., shorter curing oven cycle
time) that could increase
organic HAP emissions from the
affected kiln, as specified in
Sec. 63.9798(d).
b. Satisfy the
applicable
requirements
listed in items 3
through 13 of
this table.
3. Each affected continuous a. Perform a The appropriate test Each test run must be at least 1
process unit. minimum of 3 test methods specified in hour in duration.
runs. items 1, 4, and 5 of
this table.
b. Establish the i. Method 311 of 40 CFR (1) Calculate and record the
operating limit part 63, appendix A, organic HAP content of all
for the maximum OR material safety refractory shapes that are
organic HAP data sheets (MSDS), OR processed during the performance
processing rate. product labels to test, based on the mass fraction
determine the mass of organic HAP in the resins,
fraction of organic binders, or additives; the mass
HAP in each resin, fraction of each resin, binder,
binder, or additive; or additive, in the product; and
and the process feed rate; and
ii. Product formulation (2) Calculate and record the
data that specify the organic HAP processing rate
mass fraction of each (pounds per hour) for each test
resin, binder, and run; and
additive in the
products that are
processed during the
performance test; and.
iii. Process feed rate (3) Calculate and record the
data (tons per hour). maximum organic HAP processing
rate as the average of the
organic HAP processing rates for
the three test runs.
c. Record the Process data........... During each test run and at least
operating once per hour, record the
temperature of operating temperature in the
the affected highest temperature zone of the
source. affected source.
4. Each continuous process unit a. Measure THC i. Method 25A of 40 CFR (1) Each minute, measure and
that is subject to the THC concentrations at part 60, appendix A-7. record the concentrations of THC
emission limit listed in item the outlet of the in the exhaust stream; and
2.a., 3.a., 4, or 5 of Table 1 control device or (2) Provide at least 50 1-minute
to this subpart. in the stack. measurements for each valid
hourly average THC
concentration.
b. Measure oxygen i. Method 3A of 40 CFR (1) Each minute, measure and
concentrations at part 60, appendix A-2. record the concentrations of
the outlet of the oxygen in the exhaust stream;
control device or and
in the stack. (2) Provide at least 50 1-minute
measurements for each valid
hourly average THC
concentration.
[[Page 66075]]
c. Determine the i. Equation 1 of Sec. (1) Calculate the hourly average
hourly average 63.9800(g)(1); and THC concentration for each hour
THC ii. The 1-minute THC of the performance test as the
concentration, and oxygen average of the 1-minute THC
corrected to 18 concentration data. measurements; and
percent oxygen. (2) Calculate the hourly average
oxygen concentration for each
hour of the performance test as
the average of the 1-minute
oxygen measurements; and
(3) Correct the hourly average
THC concentrations to 18 percent
oxygen using Equation 1 of Sec.
63.9800(g)(1).
d. Determine the 3- The hourly average Calculate the 3-hour block
hour block concentration of THC, average THC emission
average THC corrected to 18 concentration, corrected to 18
emission percent oxygen, for percent oxygen, as the average
concentration, each test run. of the hourly average THC
corrected to 18 emission concentrations,
percent oxygen. corrected to 18 percent oxygen.
5. Each continuous process unit a. Measure THC i. Method 25A of 40 CFR (1) Each minute, measure and
that is subject to the THC concentrations at part 60, appendix A-7. record the concentrations of THC
percentage reduction limit the inlet and at the inlet and outlet of the
listed in item 2.b. or 3.b. of outlet of the control device; and
Table 1 to this subpart. control device. (2) Provide at least 50 1-minute
measurements for each valid
hourly average THC concentration
at the control device inlet and
outlet.
b. Determine the i. The 1-minute THC Calculate the hourly THC mass
hourly THC mass concentration data at emissions rates at the control
emissions rates the control device device inlet and outlet for each
at the inlet and inlet and outlet; and hour of the performance test.
outlet of the ii. The volumetric flow
control device. rates at the control
device inlet and
outlet.
c. Determine the 3- i. The hourly THC mass (1) Calculate the hourly THC
hour block emissions rates at the percentage reduction for each
average THC inlet and outlet of hour of the performance test
percentage the control device. using Equation 2 of Sec.
reduction. 63.9800(g)(1); and
(2) Calculate the 3-hour block
average THC percentage
reduction.
6. Each continuous process unit a. Establish the i. Continuous recording (1) At least every 15 minutes,
that is equipped with a thermal operating limit of the output of the measure and record the thermal
oxidizer. for the minimum combustion chamber oxidizer combustion chamber
allowable thermal temperature temperature; and
oxidizer measurement device. (2) Provide at least one
combustion measurement during at least
chamber three 15-minute periods per hour
temperature. of testing; and
(3) Calculate the hourly average
thermal oxidizer combustion
chamber temperature for each
hour of the performance test;
and
(4) Calculate the minimum
allowable combustion chamber
temperature as the average of
the combustion chamber
temperatures for the three test
runs, minus 14 [deg]C (25
[deg]F).
7. Each continuous process unit a. Establish the i. Continuous recording (1) At least every 15 minutes,
that is equipped with a operating limit of the output of the measure and record the
catalytic oxidizer. for the minimum temperature temperature at the inlet of the
allowable measurement device. catalyst bed; and
temperature at (2) Provide at least one catalyst
the inlet of the bed inlet temperature
catalyst bed. measurement during at least
three 15-minute periods per hour
of testing; and
(3) Calculate the hourly average
catalyst bed inlet temperature
for each hour of the performance
test; and
(4) Calculate the minimum
allowable catalyst bed inlet
temperature as the average of
the catalyst bed inlet
temperatures for the three test
runs, minus 14 [deg]C (25
[deg]F).
8. Each affected batch process a. Perform a i. The appropriate test (1) Each test run must be
unit. minimum of two methods specified in conducted over a separate batch
test runs. items 1, 9, and 10 of cycle unless you satisfy the
this table. requirements of Sec.
63.9800(f)(3) and (4); and
(2) Each test run must begin with
the start of a batch cycle,
except as specified in item
8.a.i.4. of this table; and
(3) Each test run must continue
until the end of the batch
cycle, except as specified in
items 8.a.i.4. and 8.a.i.5. of
this table; and
(4) If you develop an emissions
profile, as described in Sec.
63.9802(a), AND for sources
equipped with a thermal or
catalytic oxidizer, you do not
reduce the oxidizer operating
temperature, as specified in
item 13 of this table, you can
limit each test run to the 3-
hour peak THC emissions period;
and
[[Page 66076]]
(5) If you do not develop an
emissions profile, a test run
can be stopped, and the results
of that run considered complete,
if you measure emissions
continuously until at least 3
hours after the affected process
unit has reached maximum
temperature, AND the hourly
average THC mass emissions rate
has not increased during the 3-
hour period since maximum
process temperature was reached,
and the hourly average
concentrations of THC at the
inlet of the control device have
not exceeded 20 ppmvd, corrected
to 18 percent oxygen, during the
3-hour period since maximum
process temperature was reached
or the hourly average THC
percentage reduction has been at
least 95 percent during the 3-
hour period since maximum
process temperature was reached,
AND, for sources equipped with a
thermal or catalytic oxidizer,
at least 1 hour has passed since
any reduction in the operating
temperature of the oxidizer, as
specified in item 13 of this
table.
b. Establish the i. Method 311 of 40 CFR (1) Calculate and record the
operating limit part 63, appendix A, organic HAP content of all
for the maximum OR MSDS, OR product refractory shapes that are
organic HAP labels to determine processed during the performance
processing rate. the mass fraction of test, based on the mass fraction
organic HAP in each of HAP in the resins, binders,
resin, binder, or or additives; the mass fraction
additive; and of each resin, binder, or
additive, in the product, and
the batch weight prior to
processing; and
ii. Product formulation (2) Calculate and record the
data that specify the organic HAP processing rate
mass fraction of each (pounds per batch) for each test
resin, binder, and run; and
additive in the (3) Calculate and record the
products that are maximum organic HAP processing
processed during the rate as the average of the
performance test; and. organic HAP processing rates for
iii. Batch weight the two test runs.
(tons).
c. Record the Process data........... Record the total elapsed time
batch cycle time. from the start to the completion
of the batch cycle.
d. Record the Process data........... Record the operating temperature
operating of the affected source at least
temperature of once every hour from the start
the affected to the completion of the batch
source. cycle.
9. Each batch process unit that a. Measure THC i. Method 25A of 40 CFR (1) Each minute, measure and
is subject to the THC emission concentrations at part 60, appendix A-7. record the concentrations of THC
limit listed in item 6.a., the outlet of the in the exhaust stream; and
7.a., 8, or 9 of Table 1 to control device or (2) Provide at least 50 1-minute
this subpart. in the stack. measurements for each valid
hourly average THC
concentration.
b. Measure oxygen i. Method 3A of 40 CFR (1) Each minute, measure and
concentrations at part 60, appendix A-2. record the concentrations of
the outlet of the oxygen in the exhaust stream;
control device or and
in the stack. (2) Provide at least 50 1-minute
measurements for each valid
hourly average oxygen
concentration.
c. Determine the i. Equation 1 of Sec. (1) Calculate the hourly average
hourly average 63.9800(g)(1); and THC concentration for each hour
THC ii. The 1-minute THC of the performance test as the
concentration, and oxygen average of the 1-minute THC
corrected to 18 concentration data. measurements; and
percent oxygen. (2) Calculate the hourly average
oxygen concentration for each
hour of the performance test as
the average of the 1-minute
oxygen measurements; and
(3) Correct the hourly average
THC concentrations to 18 percent
oxygen using Equation 1 of Sec.
63.9800(g)(1).
d. Determine the 3- The hourly average THC Select the period of 3
hour peak THC concentrations, consecutive hours over which the
emissions period corrected to 18 sum of the hourly average THC
for each test run. percent oxygen. concentrations, corrected to 18
percent oxygen, is greater than
the sum of the hourly average
THC emission concentrations,
corrected to 18 percent oxygen,
for any other period of 3
consecutive hours during the
test run.
e. Determine the The hourly average THC Calculate the average of the
average THC emission hourly average THC
concentration, concentrations, concentrations, corrected to 18
corrected to 18 corrected to 18 percent oxygen, for the 3 hours
percent oxygen, percent oxygen, for of the peak emissions period for
for each test run. the 3-hour peak THC each test run.
emissions period.
[[Page 66077]]
f. Determine the 2- The average THC Calculate the average of the
run block average concentration, average THC concentrations,
THC corrected to 18 corrected to 18 percent oxygen,
concentration, percent oxygen, for for each run.
corrected to 18 each test run.
percent oxygen,
for the emission
test.
10. Each batch process unit that a. Measure THC i. Method 25A of 40 CFR (1) Each minute, measure and
is subject to the THC concentrations at part 60, appendix A-7. record the concentrations of THC
percentage reduction limit the inlet and at the control device inlet and
listed in item 6.b. or 7.b. of outlet of the outlet; and
Table 1 to this subpart. control device. (2) Provide at least 50 1-minute
measurements for each valid
hourly average THC concentration
at the control device inlet and
outlet.
b. Determine the i. The 1-minute THC (1) Calculate the hourly mass
hourly THC mass concentration data at emissions rates at the control
emissions rates the control device device inlet and outlet for each
at the control inlet and outlet; and hour of the performance test.
device inlet and ii. The volumetric flow
outlet. rates at the control
device inlet and
outlet.
c. Determine the 3- The hourly THC mass Select the period of 3
hour peak THC emissions rates at the consecutive hours over which the
emissions period control device inlet. sum of the hourly THC mass
for each test run. emissions rates at the control
device inlet is greater than the
sum of the hourly THC mass
emissions rates at the control
device inlet for any other
period of 3 consecutive hours
during the test run.
d. Determine the i. Equation 2 of Sec. Calculate the average THC
average THC 63.9800(g)(2); and percentage reduction for each
percentage ii. The hourly THC mass test run using Equation 2 of
reduction for emissions rates at the Sec. 63.9800(g)(2).
each test run. control device inlet
and outlet for the 3-
hour peak THC
emissions period.
e. Determine the 2- The average THC Calculate the average of the
run block average percentage reduction average THC percentage
THC percentage for each test run. reductions for each test run.
reduction for the
emission test.
11. Each batch process unit that a. Establish the i. Continuous recording (1) At least every 15 minutes,
is equipped with a thermal operating limit of the output of the measure and record the thermal
oxidizer. for the minimum combustion chamber oxidizer combustion chamber
thermal oxidizer temperature temperature; and
combustion measurement device. (2) Provide at least one
chamber temperature measurement during
temperature. at least three 15-minute periods
per hour of testing; and
(3) Calculate the hourly average
combustion chamber temperature
for each hour of the 3-hour peak
emissions period, as defined in
item 9.d. or 10.c. of this
table, whichever applies; and
(4) Calculate the minimum
allowable thermal oxidizer
combustion chamber operating
temperature as the average of
the hourly combustion chamber
temperatures for the 3-hour peak
emissions period, minus 14
[deg]C (25 [deg]F).
12. Each batch process unit that a. Establish the i. Continuous recording (1) At least every 15 minutes,
is equipped with a catalytic operating limit of the output of the measure and record the
oxidizer. for the minimum temperature temperature at the inlet of the
temperature at measurement device. catalyst bed; and
the inlet of the (2) Provide at least one catalyst
catalyst bed. bed inlet temperature
measurement during at least
three 15-minute periods per hour
of testing; and
(3) Calculate the hourly average
catalyst bed inlet temperature
for each hour of the 3-hour peak
emissions period, as defined in
item 9.d. or 10.c. of this
table, whichever applies; and
(4) Calculate the minimum
allowable catalytic oxidizer
catalyst bed inlet temperature
as the average of the hourly
catalyst bed inlet temperatures
for the 3-hour peak emissions
period, minus 14 [deg]C (25
[deg]F).
[[Page 66078]]
13. Each batch process unit that a. During each ....................... (1) The oxidizer can be shut off
is equipped with a thermal or test run, or the oxidizer operating
catalytic oxidizer. maintain the temperature can be reduced if
applicable you do not use an emission
operating profile to limit testing to the
temperature of 3-hour peak emissions period, as
the oxidizer specified in item 8.a.i.4. of
until emission this table; and
levels allow the (2) At least 3 hours have passed
oxidizer to be since the affected process unit
shut off or the reached maximum temperature; and
operating (3) The applicable emission limit
temperature of specified in item 6.a. or 6.b.
the oxidizer to of Table 1 to this subpart was
be reduced. met during each of the previous
three 1-hour periods; and
(4) The hourly average THC mass
emissions rate did not increase
during the 3-hour period since
maximum process temperature was
reached; and
(5) The applicable emission limit
specified in item 6.a. and 6.b.
of Table 1 to this subpart was
met during each of the four 15-
minute periods immediately
following the oxidizer
temperature reduction; and
(6) If the applicable emission
limit specified in item 6.a. or
6.b. of Table 1 to this subpart
was not met during any of the
four 15-minute periods
immediately following the
oxidizer temperature reduction,
you must return the oxidizer to
its normal operating temperature
as soon as possible and maintain
that temperature for at least 1
hour; and
(7) Continue the test run until
the applicable emission limit
specified in items 6.a. and 6.b.
of Table 1 to this subpart is
met for at least four
consecutive 15-minute periods
that immediately follow the
temperature reduction; and
(8) Calculate the hourly average
oxidizer operating temperature
for each hour of the performance
test since the affected process
unit reached maximum
temperature.
14. Each new continuous kiln a. Measure i. Method 26A of 40 CFR (1) Conduct the test while the
that is used to process clay emissions of HF part 60, appendix A-8; kiln is operating at the maximum
refractory products. and HCl. or. production level; and
ii. Method 26 of 40 CFR (2) You may use EPA Method 26 of
part 60, appendix A-8; 40 CFR part 60, appendix A-8,
or. only if no acid PM (e.g., HF or
iii. Method 320 of 40 HCl dissolved in water droplets
CFR part 63, appendix emitted by sources controlled by
A. a wet scrubber) is present; and
(3) If you use EPA Method 320 of
40 CFR part 63, appendix A, you
must follow the analyte spiking
procedures of Section 13 of EPA
Method 320 unless you can
demonstrate that the complete
spiking procedure has been
conducted at a similar source.
ASTM D6348-12e1 \a\ may be used
as an alternative to EPA Method
320 if the test plan preparation
and implementation in Annexes A1-
A8 are mandatory and the %R in
Annex A5 is determined for each
target analyte and is equal or
greater than 70 percent and less
than or equal to 130 percent;
and
(4) Repeat the performance test
if the affected source is
controlled with a DLA and you
change the source of the
limestone used in the DLA.
b. Perform a The appropriate test Each test run must be at least 1
minimum of 3 test methods specified in hour in duration.
runs. items 1 and 14.a. of
this table.
15. Each new continuous kiln a. Record the i. Production data; and (1) Record the production rate
that is subject to the uncalcined clay ii. Product formulation (tons per hour of fired
production-based HF and HCl processing rate. data that specify the product); and
emission limits specified in mass fraction of (2) Calculate and record the
items 10.a. and 10.b. of Table uncalcined clay in the average rate at which uncalcined
1 to this subpart. products that are clay is processed (tons per
processed during the hour) for each test run; and
performance test. (3) Calculate and record the 3-
run average uncalcined clay
processing rate as the average
of the average uncalcined clay
processing rates for each test
run.
b. Determine the i. Method 26A of 40 CFR Calculate the HF mass emissions
HF mass emissions part 60, appendix A-8; rate for each test.
rate at the or. ASTM D6348-12e1 \a\ may be used
outlet of the ii. Method 26 of 40 CFR as an alternative to EPA Method
control device or part 60, appendix A-8; 320 if the test plan preparation
in the stack. or. and implementation in Annexes A1-
iii. Method 320 of 40 A8 are mandatory and the %R in
CFR part 63, appendix Annex A5 is determined for each
A. target analyte and is equal or
greater than 70 percent and less
than or equal to 130 percent.
[[Page 66079]]
c. Determine the 3- i. The HF mass (1) Calculate the hourly
hour block emissions rate for production-based HF emissions
average each test run; and. rate for each test run using
production-based ii. The average Equation 3 of Sec.
HF emissions rate. uncalcined clay 63.9800(g)(3); and
processing rate. (2) Calculate the 3-hour block
average production-based HF
emissions rate as the average of
the hourly production-based HF
emissions rates for each test
run.
d. Determine the i. Method 26A of 40 CFR Calculate the HCl mass emissions
HCl mass part 60, appendix A-8; rate for each test run.
emissions rate at or. ASTM D6348-12e1 \a\ may be used
the outlet of the ii. Method 26 of 40 CFR as an alternative to EPA Method
control device or part 60, appendix A-8; 320 if the test plan preparation
in the stack. or. and implementation in Annexes A1-
iii. Method 320 of 40 A8 are mandatory and the %R in
CFR part 63, appendix Annex A5 is determined for each
A. target analyte and is equal or
greater than 70 percent and less
than or equal to 130 percent.
e. Determine the 3- i. The HCl mass (1) Calculate the hourly
hour block emissions rate for production-based HCl emissions
average each test run; and. rate for each test run using
production-based ii. The average Equation 3 of Sec.
HCl emissions uncalcined clay 63.9800(g)(3); and
rate. processing rate. (2) Calculate the 3-hour block
average production-based HCl
emissions rate as the average of
the production-based HCl
emissions rates for each test
run.
16. Each new continuous kiln a. Measure the HF i. Method 26A of 40 CFR Calculate the HF mass emissions
that is subject to the HF and mass emissions part 60, appendix A-8; rates at the control device
HCl percentage reduction limits rates at the or. inlet and outlet for each test
specified in items 10.a. and inlet and outlet ii. Method 26 of 40 CFR run.
10.b. of Table 1 to this of the control part 60, appendix A-8; ASTM D6348-12e1 \a\ may be used
subpart. device. or. as an alternative to EPA Method
iii. Method 320 of 40 320 if the test plan preparation
CFR part 63, appendix and implementation in Annexes A1-
A. A8 are mandatory and the %R in
Annex A5 is determined for each
target analyte and is equal or
greater than 70 percent and less
than or equal to 130 percent.
b. Determine the 3- i. The HF mass (1) Calculate the hourly HF
hour block emissions rates at the percentage reduction using
average HF inlet and outlet of Equation 2 of Sec.
percentage the control device for 63.9800(g)(2); and
reduction. each test run. (2) Calculate the 3-hour block
average HF percentage reduction
as the average of the HF
percentage reductions for each
test run.
c. Measure the HCl i. Method 26A of 40 CFR Calculate the HCl mass emissions
mass emissions part 60, appendix A-8; rates at the control device
rates at the or. inlet and outlet for each test
inlet and outlet ii. Method 26 of 40 CFR run.
of the control part 60, appendix A-8; ASTM D6348-12e1 \a\ may be used
device. or. as an alternative to EPA Method
iii. Method 320 of 40 320 if the test plan preparation
CFR part 63, appendix and implementation in Annexes A1-
A. A8 are mandatory and the %R in
Annex A5 is determined for each
target analyte and is equal or
greater than 70 percent and less
than or equal to 130 percent.
d. Determine the 3- i. The HCl mass (1) Calculate the hourly HCl
hour block emissions rates at the percentage reduction using
average HCl inlet and outlet of Equation 2 of Sec.
percentage the control device for 63.9800(g)(2); and
reduction.. each test run. (2) Calculate the 3-hour block
average HCl percentage reduction
as the average of HCl percentage
reductions for each test run.
17. Each new batch process kiln a. Measure i. Method 26A of 40 CFR (1) Conduct the test while the
that is used to process clay emissions of HF part 60, appendix A-8; kiln is operating at the maximum
refractory products. and HCl at the or. production level; and
inlet and outlet ii. Method 26 of 40 CFR (2) You may use EPA Method 26 of
of the control part 60, appendix A-8; 40 CFR part 60, appendix A, only
device. or. if no acid PM (e.g., HF or HCl
iii. Method 320 of 40 dissolved in water droplets
CFR part 63, appendix emitted by sources controlled by
A. a wet scrubber) is present; and
(3) If you use EPA Method 320 of
40 CFR part 63, you must follow
the analyte spiking procedures
of Section 13 of EPA Method 320
unless you can demonstrate that
the complete spiking procedure
has been conducted at a similar
source
ASTM D6348-12e1 \a\ may be used
as an alternative to EPA Method
320 if the test plan preparation
and implementation in Annexes A1-
A8 are mandatory and the %R in
Annex A5 is determined for each
target analyte and is equal or
greater than 70 percent and less
than or equal to 130 percent.;
and
(4) Repeat the performance test
if the affected source is
controlled with a DLA and you
change the source of the
limestone used in the DLA.
b. Perform a i. The appropriate test (1) Each test run must be
minimum of 2 test methods specified in conducted over a separate batch
runs. items 1 and 17.a. of cycle unless you satisfy the
this table. requirements of Sec.
63.9800(f)(3) and (4); and
(2) Each test run must consist of
a series of 1-hour runs at the
inlet and outlet of the control
device, beginning with the start
of a batch cycle, except as
specified in item 17.b.i.4. of
this table; and
[[Page 66080]]
(3) Each test run must continue
until the end of the batch
cycle, except as specified in
item 17.b.i.4. of this table;
and
(4) If you develop an emissions
profile, as described in Sec.
63.9802(b), you can limit each
test run to the 3-hour peak HF
emissions period.
c. Determine the i. The appropriate test Determine the hourly mass HF and
hourly HF and HCl methods specified in HCl emissions rates at the inlet
mass emissions items 1 and 17.a. of and outlet of the control device
rates at the this table. for each hour of each test run.
inlet and outlet
of the control
device.
d. Determine the 3- The hourly HF mass Select the period of 3
hour peak HF emissions rates at the consecutive hours over which the
emissions period. inlet of the control sum of the hourly HF mass
device. emissions rates at the control
device inlet is greater than the
sum of the hourly HF mass
emissions rates at the control
device inlet for any other
period of 3 consecutive hours
during the test run.
e. Determine the 2- i. The hourly average (1) Calculate the HF percentage
run block average HF emissions rates at reduction for each hour of the 3-
HF percentage the inlet and outlet hour peak HF emissions period
reduction for the of the control device. using Equation 2 of Sec.
emissions test. 63.9800(g)(2); and
(2) Calculate the average HF
percentage reduction for each
test run as the average of the
hourly HF percentage reductions
for the 3-hour peak HF emissions
period for that run; and
(3) Calculate the 2-run block
average HF percentage reduction
for the emission test as the
average of the average HF
percentage reductions for the
two test runs.
f. Determine the 2- i. The hourly average (1) Calculate the HCl percentage
run block average HCl emissions rates at reduction for each hour of the 3-
HCl percentage the inlet and outlet hour peak HF emissions period
reduction for the of the control device. using Equation 2 Sec.
emission test. 63.9800(g)(2); and
(2) Calculate the average HCl
percentage reduction for each
test run as the average of the
hourly HCl percentage reductions
for the 3-hour peak HF emissions
period for that run; and
(3) Calculate the 2-run block
average HCl percentage reduction
for the emission test as the
average of the average HCl
percentage reductions for the
two test runs.
18. Each new kiln that is used a. Establish the Data from the pressure (1) At least every 15 minutes,
to process clay refractory operating limit drop measurement measure the pressure drop across
products and is equipped with a for the minimum device during the the DLA; and
DLA. pressure drop performance test. (2) Provide at least one pressure
across the DLA. drop measurement during at least
three 15-minute periods per hour
of testing; and
(3) Calculate the hourly average
pressure drop across the DLA for
each hour of the performance
test; and
(4) Calculate and record the
minimum pressure drop as the
average of the hourly average
pressure drops across the DLA
for the two or three test runs,
whichever applies.
b. Establish the Data from the limestone (1) Ensure that limestone in the
operating limit feeder during the feed hopper, silo, and DLA is
for the limestone performance test. free-flowing at all times during
feeder setting. the performance test; and
(2) Establish the limestone
feeder setting 1 week prior to
the performance test; and
(3) Record and maintain the
feeder setting for the 1-week
period that precedes the
performance test and during the
performance test.
19. Each new kiln that is used a. Document Data from the Submit analyses and supporting
to process clay refractory conformance with installation and documentation demonstrating
products and is equipped with a specifications calibration of the bag conformance with EPA guidance
DIFF or DLS/FF. and requirements leak detection system. and specifications for bag leak
of the bag leak detection systems as part of the
detection system. Notification of Compliance
Status.
b. Establish the i. Data from the lime (1) For continuous lime injection
operating limit feeder during the systems, ensure that lime in the
for the lime performance test. feed hopper or silo is free-
feeder setting. flowing at all times during the
performance test; and
(2) Record the feeder setting for
the three test runs; and
(3) If the feed rate setting
varies during the three test
runs, calculate and record the
average feed rate for the two or
three test runs, whichever
applies.
[[Page 66081]]
20. Each new kiln that is used a. Establish the i. Data from the (1) At least every 15 minutes,
to process clay refractory operating limit pressure drop measure the pressure drop across
products and is equipped with a for the minimum measurement device the scrubber; and
wet scrubber. scrubber pressure during the performance (2) Provide at least one pressure
drop. test. drop measurement during at least
three 15-minute periods per hour
of testing; and
(3) Calculate the hourly average
pressure drop across the
scrubber for each hour of the
performance test; and
(4) Calculate and record the
minimum pressure drop as the
average of the hourly average
pressure drops across the
scrubber for the two or three
test runs, whichever applies.
b. Establish the i. Data from the pH (1) At least every 15 minutes,
operating limit measurement device measure scrubber liquid pH; and
for the minimum during the performance (2) Provide at least one pH
scrubber liquid test. measurement during at least
pH. three 15-minute periods per hour
of testing; and
(3) Calculate the hourly average
pH values for each hour of the
performance test; and
(4) Calculate and record the
minimum liquid pH as the average
of the hourly average pH
measurements for the two or
three test runs, whichever
applies.
c. Establish the i. Data from the flow (1) At least every 15 minutes,
operating limit rate measurement measure the scrubber liquid flow
for the minimum device during the rate; and
scrubber liquid performance test. (2) Provide at least one flow
flow rate. rate measurement during at least
three 15-minute periods per hour
of testing; and
(3) Calculate the hourly average
liquid flow rate for each hour
of the performance test; and
(4) Calculate and record the
minimum liquid flow rate as the
average of the hourly average
liquid flow rates for the two or
three test runs, whichever
applies.
d. If chemicals i. Data from the (1) At least every 15 minutes,
are added to the chemical feed rate measure the scrubber chemical
scrubber liquid, measurement device feed rate; and
establish the during the performance (2) Provide at least one chemical
operating limit test. feed rate measurement during at
for the minimum least three 15-minute periods
scrubber chemical per hour of testing; and
feed rate. (3) Calculate the hourly average
chemical feed rate for each hour
of the performance test; and
(4) Calculate and record the
minimum chemical feed rate as
the average of the hourly
average chemical feed rates for
the two or three test runs,
whichever applies.
21. Each new and existing kiln Measure PM Method 5 of 40 CFR part
that is used to process clay emissions. 60, appendix A-3.
refractory products that is
subject to the PM limits
specified in items 10.c. 11.c,
12.a, and 13.a of Table 1 to
this subpart.
22. Each new and existing kiln Measure Hg Method 29 of 40 CFR ASTM D6784-16 \a\ may be used as
that is used to process clay emissions. part 60, appendix A-8. an alternative to EPA Method 29
refractory products that is (portion for Hg only).
subject to the Hg limits
specified in items 10.d. 11.d,
12.b, and 13.b of Table 1 to
this subpart.
23. Each new and existing kiln Establish the Data from the carbon You must measure the carbon flow
that is used to process clay operating limit flow rate measurement rate during each test run,
refractory products and is for the average conducted during the determine and record the block
equipped with an activated carbon flow rate. Hg performance test. average carbon flow rate values
carbon injection system. for the three test runs, and
determine and record the 3-hour
block average of the recorded
carbon flow rate measurements
for the three test runs. The
average of the three test runs
establishes your minimum site-
specific activated carbon flow
rate operating limit.
[[Page 66082]]
24. Each existing kiln that is Document Data from the Submit analyses and supporting
used to process clay refractory conformance with installation and documentation demonstrating
products and is equipped with a specifications calibration of the bag conformance with EPA guidance
FF and a bag leak detection and requirements leak detection system. and specifications for bag leak
system. of the bag leak detection systems as part of the
detection system. Notification of Compliance
Status.
25. Each existing kiln that is a. Establish the i. Data from the (1) At least every 15 minutes,
used to process clay refractory operating limit pressure drop measure the pressure drop across
products and is equipped with a for the minimum measurement device the scrubber; and
wet scrubber. scrubber pressure during the performance (2) Provide at least one pressure
drop. test. drop measurement during at least
three 15-minute periods per hour
of testing; and
(3) Calculate the hourly average
pressure drop across the
scrubber for each hour of the
performance test; and
(4) Calculate and record the
minimum pressure drop as the
average of the hourly average
pressure drops across the
scrubber for the two or three
test runs, whichever applies.
b. Establish the i. Data from the flow (1) At least every 15 minutes,
operating limit rate measurement measure the scrubber liquid flow
for the minimum device during the rate; and
scrubber liquid performance test. (2) Provide at least one flow
flow rate. rate measurement during at least
three 15-minute periods per hour
of testing; and
(3) Calculate the hourly average
liquid flow rate for each hour
of the performance test; and
(4) Calculate and record the
minimum liquid flow rate as the
average of the hourly average
liquid flow rates for the two or
three test runs, whichever
applies.
----------------------------------------------------------------------------------------------------------------
\a\ Incorporated by reference, see Sec. 63.14.
0
21. Table 5 to Subpart SSSSS is revised to read as follows:
Table 5 to Subpart SSSSS of Part 63--Initial Compliance With Emission
Limits
As stated in Sec. 63.9806, you must show initial compliance with
the emission limits for affected sources according to the following
table:
------------------------------------------------------------------------
For the following
emission limit . You have demonstrated
For . . . . . compliance if . . .
------------------------------------------------------------------------
1. Each affected source listed a. Each i. Emissions measured
in Table 1 to this subpart. applicable using the test
emission limit methods specified in
listed in Table Table 4 to this
1 to this subpart satisfy the
subpart. applicable emission
limits specified in
Table 1 to this
subpart; and
ii. You establish and
have a record of the
operating limits
listed in Table 2 to
this subpart over
the performance test
period; and
iii. You report the
results of the
performance test in
the Notification of
Compliance Status,
as specified by Sec.
63.9812(e)(1) and
(2).
2. Each new or existing curing As specified in You have satisfied
oven, shape dryer, and kiln items 3 through the applicable
that is used to process 8 of this table. requirements
refractory products that use specified in items 3
organic HAP; each new or through 8 of this
existing coking oven and table.
defumer that is used to
produce pitch-impregnated
refractory products; each new
shape preheater that is used
to produce pitch-impregnated
refractory products; AND each
new or existing process unit
that is exhausted to a
thermal or catalytic oxidizer
that also controls emissions
from an affected shape
preheater or pitch working
tank.
3. Each affected continuous The average THC The 3-hour block
process unit that is subject concentration average THC emission
to the THC emission must not exceed concentration
concentration limit listed in 20 ppmvd, measured during the
item 2.a., 3.a., 4, or 5 of corrected to 18 performance test
Table 1 to this subpart. percent oxygen. using EPA Methods
25A and 3A is equal
to or less than 20
ppmvd, corrected to
18 percent oxygen.
[[Page 66083]]
4. Each affected continuous The average THC The 3-hour block
process unit that is subject percentage average THC
to the THC percentage reduction must percentage reduction
reduction limit listed in equal or exceed measured during the
item 2.b. or 3.b. of Table 1 95 percent. performance test
to this subpart. using EPA Method 25A
is equal to or
greater than 95
percent.
5. Each affected batch process The average THC The 2-run block
unit that is subject to the concentration average THC emission
THC emission concentration must not exceed concentration for
limit listed in item 6.a., 20 ppmvd, the 3-hour peak
7.a., 8, or 9 of Table 1 to corrected to 18 emissions period
this subpart. percent oxygen. measured during the
performance test
using EPA Methods
25A and 3A is equal
to or less than 20
ppmvd, corrected to
18 percent oxygen.
6. Each affected batch process The average THC The 2-run block
unit that is subject to the percentage average THC
THC percentage reduction reduction must percentage reduction
limit listed in item 6.b. or equal or exceed for the 3-hour peak
7.b. of Table 1 to this 95 percent. emissions period
subpart. measured during the
performance test
using EPA Method 25A
is equal to or
exceeds 95 percent.
7. Each affected continuous or a. The average i. You have installed
batch process unit that is THC a THC CEMS at the
equipped with a control concentration outlet of the
device other than a thermal must not exceed control device or in
or catalytic oxidizer and is 20 ppmvd, the stack of the
subject to the emission limit corrected to 18 affected source; and
listed in item 3 or 7 of percent oxygen; ii. You have
Table 1 to this subpart. or satisfied the
b. The average requirements of PS-8
THC percentage of 40 CFR part 60,
reduction must appendix B.
equal or exceed
95 percent.
8. Each affected continuous or The average THC i. You have installed
batch process unit that uses concentration a THC CEMS at the
process changes to reduce must not exceed outlet of the
organic HAP emissions and is 20 ppmvd, control device or in
subject to the emission limit corrected to 18 the stack of the
listed in item 4 or 8 of percent oxygen. affected source; and
Table 1 to this subpart. ii. You have
satisfied the
requirements of PS-8
of 40 CFR part 60,
appendix B.
9. Each new continuous kiln a. The average HF i. The 3-hour block
that is used to process clay emissions must average production-
refractory products. not exceed 0.019 based HF emissions
kg/Mg (0.038 lb/ rate measured during
ton) of the performance test
uncalcined clay using one of the
processed; OR methods specified in
the average item 14.a.i. of
uncontrolled HF Table 4 to this
emissions must subpart is equal to
be reduced by at or less than 0.019
least 90 percent. kg/Mg (0.038 lb/ton)
of uncalcined clay
processed; or
The 3-hour block
average HF emissions
reduction measured
during the
performance test is
equal to or greater
than 90 percent.
b. The average i. The 3-hour block
HCl emissions average production-
must not exceed based HCl emissions
0.091 kg/Mg rate measured during
(0.18 lb/ton) of the performance test
uncalcined clay using one of the
processed; OR methods specified in
the average item 14.a.i. of
uncontrolled HCl Table 4 to this
emissions must subpart is equal to
be reduced by at or less than 0.091
least 30 percent. kg/Mg (0.18 lb/ton)
of uncalcined clay
processed; or
ii. The 3-hour block
average HCl
emissions reduction
measured during the
performance test is
equal to or greater
than 30 percent.
c. The average PM i. The 3-hour block
emissions must average PM emissions
not exceed 1.4 measured during the
kg/Mg (3.1 lb/ performance test
hr). using one of the
methods specified in
item 21 of Table 4
to this subpart is
equal to or less
than 1.4 kg/Mg (3.1
lb/hr).
d. The average Hg i. The 3-hour block
emissions must average Hg emissions
not exceed 6.1 measured during the
[micro]g/dscm at performance test
18 percent using one of the
oxygen. methods specified in
item 22 of Table 4
to this subpart is
equal to or less
than 6.1 [micro]g/
dscm at 18 percent
oxygen.
10. Each new batch process a. The average The 2-run block
kiln that is used to process uncontrolled HF average HF emission
clay refractory products. emissions must reduction measured
be reduced by at during the
least 90 percent. performance test is
equal to or greater
than 90 percent.
b. The average The 2-run block
uncontrolled HCl average HCl
emissions must emissions reduction
be reduced by at measured during the
least 30 percent. performance test is
equal to or greater
than 30 percent.
c. The average PM i. The 2-run block
emissions must average PM emissions
not exceed 1.4 measured during the
kg/Mg (3.1 lb/ performance test
hr). using one of the
methods specified in
item 21 of Table 4
to this subpart is
equal to or less
than 1.4 kg/Mg (3.1
lb/hr).
d. The average Hg i. The 2-run block
emissions must average Hg emissions
not exceed 6.1 measured during the
[micro]g/dscm at performance test
18 percent using one of the
oxygen. methods specified in
item 22 of Table 4
to this subpart is
equal to or less
than 6.1 [micro]g/
dscm at 18 percent
oxygen.
11. Each existing continuous a. The average PM i. The 3-hour block
kiln that is used to produce emissions must average PM emissions
clay refractory products on not exceed 4.3 measured during the
and after November 20, 2022. kg/Mg (9.5 lb/ performance test
hr). using one of the
methods specified in
item 21 of Table 4
to this subpart is
equal to or less
than 4.3 kg/Mg (9.5
lb/hr).
[[Page 66084]]
b. The average Hg i. The 3-hour block
emissions must average Hg emissions
not exceed 18 measured during the
[micro]g/dscm at performance test
18 percent using one of the
oxygen. methods specified in
item 22 of Table 4
to this subpart is
equal to or less
than 18 [micro]g/
dscm at 18 percent
oxygen.
12. Each existing batch kiln a. The average PM i. The 2-run block
that is used to produce clay emissions must average PM emissions
refractory products on and not exceed 4.3 measured during the
after November 20, 2022. kg/Mg (9.5 lb/ performance test
hr). using one of the
methods specified in
item 21 of Table 4
to this subpart is
equal to or less
than 4.3 kg/Mg (9.5
lb/hr).
b. The average Hg i. The 2-run block
emissions must average Hg emissions
not exceed 18 measured during the
[mu]g/dscm at 18 performance test
percent oxygen. using one of the
methods specified in
item 22 of Table 4
to this subpart is
equal to or less
than 18 [micro]g/
dscm at 18 percent
oxygen.
------------------------------------------------------------------------
0
22. Table 6 to Subpart SSSSS is revised to read as follows:
Table 6 to Subpart SSSSS of Part 63--Initial Compliance With Work
Practice Standards
As stated in Sec. 63.9806, you must show initial compliance with
the work practice standards for affected sources according to the
following table:
------------------------------------------------------------------------
For the following You have demonstrated
For each . . . standard . . . initial compliance if
. . .
------------------------------------------------------------------------
1. Each affected source listed a. Each i. You have selected
in Table 3 to this subpart. applicable work a method for
practice performing each of
standard listed the applicable work
in Table 3 to practice standards
this subpart. listed in Table 3 to
this subpart; and
ii. You have included
in your Initial
Notification a
description of the
method selected for
complying with each
applicable work
practice standard,
as required by Sec.
63.9(b); and
iii. You submit a
signed statement
with the
Notification of
Compliance Status
that you have
implemented the
applicable work
practice standard
listed in Table 3 to
this subpart; and
iv. You have
described in your
OM&M plan the method
for complying with
each applicable work
practice standard
specified in Table 3
to this subpart.
2. Each basket or container a. Control POM i. You have
that is used for holding emissions from implemented at least
fired refractory shapes in an any affected one of the work
existing shape preheater and shape preheater. practice standards
autoclave during the pitch listed in item 1 of
impregnation process. Table 3 to this
subpart; and
ii. You have
established a system
for recording the
date and cleaning
method for each time
you clean an
affected basket or
container.
3. Each affected new or Control POM You have captured and
existing pitch working tank. emissions. vented emissions
from the affected
pitch working tank
to the device that
is used to control
emissions from an
affected defumer or
coking oven, or to a
thermal or catalytic
oxidizer that is
comparable to the
control device used
on an affected
defumer or coking
oven.
4. Each new or existing Minimize fuel- You use natural gas,
chromium refractory products based HAP or equivalent, as
kiln. emissions. the kiln fuel.
5. Each existing clay Minimize fuel- You use natural gas,
refractory products kiln. based HAP or equivalent, as
emissions. the kiln fuel.
6. Each new or existing curing Minimize fuel- You use natural gas,
oven, shape dryer, and kiln based HAP or equivalent, as
that is used to process emissions. the kiln fuel.
refractory products that use
organic HAP, on and after
November 19, 2021.
------------------------------------------------------------------------
0
23. Table 7 to Subpart SSSSS is revised to read as follows:
Table 7 to Subpart SSSSS of Part 63--Continuous Compliance With
Emission Limits
As stated in Sec. 63.9810, you must show continuous compliance
with the emission limits for affected sources according to the
following table:
------------------------------------------------------------------------
For the following
emission limit . You must demonstrate
For . . . . . continuous compliance
by . . .
------------------------------------------------------------------------
1. Each affected source listed a. Each i. Collecting and
in Table 1 to this subpart. applicable recording the
emission limit monitoring and
listed in Table process data listed
1 to this in Table 2
subpart. (operating limits)
to this subpart; and
ii. Reducing the
monitoring and
process data
associated with the
operating limits
specified in Table 2
to this subpart; and
iii. Recording the
results of any
control device
inspections; and
[[Page 66085]]
iv. Reporting, in
accordance with Sec.
63.9814(e), any
deviation from the
applicable operating
limits specified in
Table 2 to this
subpart.
2. Each new or existing curing As specified in Satisfying the
oven, shape dryer, and kiln items 3 through applicable
that is used to process 7 of this table. requirements
refractory products that use specified in items 3
organic HAP; each new or through 7 of this
existing coking oven and table.
defumer that is used to
produce pitch-impregnated
refractory products; each new
shape preheater that is used
to produce pitch-impregnated
refractory products; AND each
new or existing process unit
that is exhausted to a
thermal or catalytic oxidizer
that also controls emissions
from an affected shape
preheater or pitch working
tank.
3. Each affected process unit a. The average i. Collecting the
that is equipped with a THC applicable data
thermal or catalytic oxidizer. concentration measured by the
must not exceed control device
20 ppmvd, temperature
corrected to 18 monitoring system,
percent oxygen; as specified in
OR the average items 5, 6, 8, and 9
THC percentage of Table 8 to this
reduction must subpart; and
equal or exceed ii. Reducing the
95 percent. applicable data
measured by the
control device
temperature
monitoring system,
as specified in
items 5, 6, 8, and 9
of Table 8 to this
subpart; and
iii. Maintaining the
average control
device operating
temperature for the
applicable averaging
period specified in
items 5, 6, 8, and 9
of Table 2 to this
subpart at or above
the minimum
allowable operating
temperature
established during
the most recent
performance test.
4. Each affected process unit The average THC Operating and
that is equipped with a concentration maintaining a THC
control device other than a must not exceed CEMS at the outlet
thermal or catalytic oxidizer. 20 ppmvd, of the control
corrected to 18 device or in the
percent oxygen; stack of the
OR the average affected source,
THC performance according to the
reduction must requirements of
equal or exceed Procedure 1 of 40
95 percent. CFR part 60,
appendix F.
5. Each affected process unit The average THC Operating and
that uses process changes to concentration maintaining a THC
meet the applicable emission must not exceed CEMS at the outlet
limit. 20 ppmvd, of the control
corrected to 18 device or in the
percent oxygen. stack of the
affected source,
according to the
requirements of
Procedure 1 of 40
CFR part 60,
appendix F.
6. Each affected continuous The average THC Recording the organic
process unit. concentration HAP processing rate
must not exceed (pounds per hour)
20 ppmvd, and the operating
corrected to 18 temperature of the
percent oxygen; affected source, as
OR the average specified in items
THC percentage 3.b. and 3.c. of
reduction must Table 4 to this
equal or exceed subpart.
95 percent.
7. Each affected batch process The average THC Recording the organic
unit. concentration HAP processing rate
must not exceed (pounds per batch);
20 ppmvd, and process cycle
corrected to 18 time for each batch
percent oxygen; cycle; and hourly
OR the average average operating
THC percentage temperature of the
reduction must affected source, as
equal or exceed specified in items
95 percent. 8.b. through 8.d. of
Table 4 to this
subpart.
8. Each new kiln that is used As specified in Satisfying the
to process clay refractory items 9 through applicable
products. 11 of this table. requirements
specified in items 9
through 11 of this
table.
9. Each new affected kiln that a. The average HF i. Maintaining the
is equipped with a DLA. emissions must pressure drop across
not exceed 0.019 the DLA at or above
kg/Mg (0.038 lb/ the minimum levels
ton) of established during
uncalcined clay the most recent
processed, OR performance test;
the average and
uncontrolled HF ii. Verifying that
emissions must the limestone hopper
be reduced by at contains an adequate
least 90 amount of free-
percent; and flowing limestone by
b. The average performing a daily
HCl emissions visual check of the
must not exceed limestone in the
0.091 kg/Mg feed hopper; and
(0.18 lb/ton) of iii. Recording the
uncalcined clay limestone feeder
processed, or setting daily to
the average verify that the
uncontrolled HCl feeder setting is at
emissions must or above the level
be reduced by at established during
least 30 percent. the most recent
performance test;
and
iv. Using the same
grade of limestone
as was used during
the most recent
performance test and
maintaining records
of the source and
grade of limestone.
[[Page 66086]]
c. The average PM i. Performing VE
emissions must observations of the
not exceed 1.4 stack at the
kg/Mg (3.1 lb/ frequency specified
hr); and in Sec. 63.9810(f)
d. The average Hg using EPA Method 22
emissions must of 40 CFR part 60,
not exceed 6.1 appendix A-7;
[micro]g/dscm, maintaining no VE
corrected to 18 from the stack.
percent oxygen.
10. Each new affected kiln a. The average HF i. Verifying at least
that is equipped with a DIFF emissions must once each 8-hour
or DLS/FF. not exceed 0.019 shift that lime is
kg/Mg (0.038 lb/ free-flowing by
ton) of means of a visual
uncalcined clay check, checking the
processed; OR output of a load
the average cell, carrier gas/
uncontrolled HF lime flow indicator,
emissions must or carrier gas
be reduced by at pressure drop
least 90 measurement system;
percent; and and
b. The average ii. Recording feeder
HCl emissions setting daily to
must not exceed verify that the
0.091 kg/Mg feeder setting is at
(0.18 lb/ton) of or above the level
uncalcined clay established during
processed; OR the most recent
the average performance test;
uncontrolled HCl and
emissions must iii. Initiating
be reduced by at corrective action
least 30 within 1 hour of a
percent; and. bag leak detection
c. The average PM system alarm AND
emissions must completing
not exceed 1.4 corrective actions
kg/Mg (3.1 lb/ in accordance with
hr); and. the OM&M plan, AND
d. The average Hg operating and
emissions must maintaining the
not exceed 6.1 fabric filter such
[micro]g/dscm, that the alarm does
corrected to 18 not engage for more
percent oxygen. than 5 percent of
the total operating
time in a 6-month
block reporting
period.
11. Each new affected kiln a. The average HF i. Maintaining the
that is equipped with a wet emissions must pressure drop across
scrubber. not exceed 0.019 the scrubber, liquid
kg/Mg (0.038 lb/ pH, and liquid flow
ton) of rate at or above the
uncalcined clay minimum levels
processed; OR established during
the average the most recent
uncontrolled HF performance test;
emissions must and
be reduced by at ii. If chemicals are
least 90 added to the
percent; and scrubber liquid,
b. The average maintaining the
HCl emissions average chemical
must not exceed feed rate at or
0.091 kg/Mg above the minimum
(0.18 lb/ton) of chemical feed rate
uncalcined clay established during
processed; OR the most recent
the average performance test.
uncontrolled HCl
emissions must
be reduced by at
least 30
percent; and.
c. The average PM
emissions must
not exceed 1.4
kg/Mg (3.1 lb/
hr); and.
d. The average Hg
emissions must
not exceed 6.1
[micro]g/dscm,
corrected to 18
percent oxygen.
12. Each new affected kiln The average Hg Collecting the carbon
that is equipped with an emissions must flow rate data
activated carbon injection not exceed 6.1 according to Sec.
system. [micro]g/dscm, 63.9804(a); reducing
corrected to 18 the carbon flow rate
percent oxygen. data to 3-hour block
averages according
to Sec.
63.9804(a);
maintaining the
average carbon flow
rate for each 3-hour
block period at or
above the average
carbon flow rate
established during
the Hg performance
test in which
compliance was
demonstrated.
13. Each existing affected a. The average PM i. Performing VE
kiln that is equipped with a emissions must observations of the
DLA or no add-on control. not exceed 4.3 stack at the
kg/Mg (9.5 lb/ frequency specified
hr); and. in Sec. 63.9810(f)
b. The average Hg using EPA Method 22
emissions must of 40 CFR part 60,
not exceed 18 appendix A-7;
[micro]g/dscm, maintaining no VE
corrected to 18 from the stack.
percent oxygen.
14. Each existing affected a. The average PM i. If you use a bag
kiln that is equipped with a emissions must leak detection
DIFF or DLS/FF. not exceed 4.3 system, as
kg/Mg (9.5 lb/ prescribed in Sec.
hr). 63.9804(f),
initiating
corrective action
within 1 hour of a
bag leak detection
system alarm AND
completing
corrective actions
in accordance with
the OM&M plan, AND
operating and
maintaining the
fabric filter such
that the alarm does
not engage for more
than 5 percent of
the total operating
time in a 6-month
block reporting
period; OR
ii. Performing VE
observations of the
stack at the
frequency specified
in Sec. 63.9810(f)
using EPA Method 22
of 40 CFR part 60,
appendix A-7;
maintaining no VE
from the stack.
[[Page 66087]]
15. Each existing affected a. The average PM i. Maintaining the
kiln that is equipped with a emissions must pressure drop across
wet scrubber. not exceed 4.3 the scrubber and
kg/Mg (9.5 lb/ liquid flow rate at
hr); and or above the minimum
b. The average Hg levels established
emissions must during the most
not exceed 18 recent performance
[micro]g/dscm, test.
corrected to 18
percent oxygen.
16. Each existing affected The average Hg Collecting the carbon
kiln that is equipped with an emissions must flow rate data
activated carbon injection not exceed 18 according to Sec.
system. [micro]g/dscm, 63.9804(a); reducing
corrected to 18 the carbon flow rate
percent oxygen. data to 3-hour block
averages according
to Sec.
63.9804(a);
maintaining the
average carbon flow
rate for each 3-hour
block period at or
above the average
carbon flow rate
established during
the Hg performance
test in which
compliance was
demonstrated.
------------------------------------------------------------------------
0
24. Table 8 to Subpart SSSSS is revised to read as follows:
Table 8 to Subpart SSSSS of Part 63--Continuous Compliance With
Operating Limits
As stated in Sec. 63.9810, you must show continuous compliance
with the operating limits for affected sources according to the
following table:
------------------------------------------------------------------------
For the following
operating limit . You must demonstrate
For . . . . . continuous compliance
by . . .
------------------------------------------------------------------------
1. Each affected source listed a. Each i. Maintaining all
in Table 2 to this subpart. applicable applicable process
operating limit and control device
listed in Table operating parameters
2 to this within the limits
subpart. established during
the most recent
performance test;
and
ii. Conducting
annually an
inspection of all
duct work, vents,
and capture devices
to verify that no
leaks exist and that
the capture device
is operating such
that all emissions
are properly vented
to the control
device in accordance
with the OM&M plan.
2. Each affected continuous a. The operating i. Operating the
kiln used to manufacture limits specified control device on
refractory products that use in items 2.a. the affected kiln
organic HAP that is equipped through 2.c. of during all times
with a THC control device. Table 2 to this except during
subpart. periods of approved
scheduled
maintenance, as
specified in Sec.
63.9792(e); and
ii. Before May 19,
2022, minimizing HAP
emissions from the
affected kiln during
all periods of
scheduled
maintenance of the
kiln control device
when the kiln is
operating and the
control device is
out of service; on
and after May 19,
2022, minimizing HAP
emissions during the
period when the kiln
is operating and the
control device is
out of service by
complying with the
applicable standard
in Table 3 to this
subpart; and
iii. Minimizing the
duration of all
periods of scheduled
maintenance of the
kiln control device
when the kiln is
operating and the
control device is
out of service; on
and after May 19,
2022, the total time
during which the
kiln is operating
and the control
device is out of
service for the each
year on a 12-month
rolling basis must
not exceed 750
hours.
3. Each new or existing curing As specified in Satisfying the
oven, shape dryer, and kiln items 4 through applicable
that is used to process 9 of this table. requirements
refractory products that use specified in items 4
organic HAP; each new or through 9 of this
existing coking oven and table.
defumer that is used to
produce pitch-impregnated
refractory products; each new
shape preheater that is used
to produce pitch-impregnated
refractory products; AND each
new or existing process unit
that is exhausted to a
thermal or catalytic oxidizer
that also controls emissions
from an affected shape
preheater or pitch working
tank.
4. Each affected continuous Maintain process i. Recording the
process unit. operating organic HAP
parameters processing rate
within the (pounds per hour);
limits and
established ii. Recording the
during the most operating
recent temperature of the
performance test. affected source at
least hourly; and
iii. Maintaining the
3-hour block average
organic HAP
processing rate at
or below the maximum
organic HAP
processing rate
established during
the most recent
performance test.
[[Page 66088]]
5. Continuous process units Maintain the 3- i. Measuring and
that are equipped with a hour block recording the
thermal oxidizer. average thermal oxidizer
operating combustion chamber
temperature in temperature at least
the thermal every 15 minutes;
oxidizer and
combustion ii. Calculating the
chamber at or hourly average
above the thermal oxidizer
minimum combustion chamber
allowable temperature; and
operating
temperature
established
during the most
recent
performance test.
iii. Maintaining the
3-hour block average
thermal oxidizer
combustion chamber
temperature at or
above the minimum
allowable operating
temperature
established during
the most recent
performance test;
and
iv. Reporting, in
accordance with Sec.
63.9814(e), any 3-
hour block average
operating
temperature
measurements below
the minimum
allowable thermal
oxidizer combustion
chamber operating
temperature
established during
the most recent
performance test.
6. Continuous process units a. Maintain the 3- i. Measuring and
that are equipped with a hour block recording the
catalytic oxidizer. average temperature at the
temperature at inlet of the
the inlet of the catalyst bed at
catalyst bed at least every 15
or above the minutes; and
minimum ii. Calculating the
allowable hourly average
catalyst bed temperature at the
inlet inlet of the
temperature catalyst bed; and
established
during the most
recent
performance test.
iii. Maintaining the
3-hour block average
temperature at the
inlet of the
catalyst bed at or
above the minimum
allowable catalyst
bed inlet
temperature
established during
the most recent
performance test;
and
iv. Reporting, in
accordance with Sec.
63.9814(e), any 3-
hour block average
catalyst bed inlet
temperature
measurements below
the minimum
allowable catalyst
bed inlet
temperature
established during
the most recent
performance; and
v. Checking the
activity level of
the catalyst at
least every 12
months and taking
any necessary
corrective action,
such as replacing
the catalyst, to
ensure that the
catalyst is
performing as
designed.
7. Each affected batch process Maintain process i. Recording the
unit. operating organic HAP
parameters processing rate
within the (pounds per batch);
limits and
established ii. Recording the
during the most hourly average
recent operating
performance test. temperature of the
affected source; and
iii. Recording the
process cycle time
for each batch
cycle; and
iv. Maintaining the
organic HAP
processing rate at
or below the maximum
organic HAP
processing rate
established during
the most recent
performance test.
8. Batch process units that Maintain the i. Measuring and
are equipped with a thermal hourly average recording the
oxidizer. temperature in thermal oxidizer
the thermal combustion chamber
oxidizer temperature at least
combustion every 15 minutes;
chamber at or and
above the hourly ii. Calculating the
average hourly average
temperature thermal oxidizer
established for combustion chamber
the temperature; and
corresponding 1-
hour period of
the cycle during
the most recent
performance test.
iii. From the start
of each batch cycle
until 3 hours have
passed since the
process unit reached
maximum temperature,
maintaining the
hourly average
operating
temperature in the
thermal oxidizer
combustion chamber
at or above the
minimum allowable
operating
temperature
established for the
corresponding period
during the most
recent performance
test, as determined
according to item 11
of Table 4 to this
subpart; and
iv. For each
subsequent hour of
the batch cycle,
maintaining the
hourly average
operating
temperature in the
thermal oxidizer
combustion chamber
at or above the
minimum allowable
operating
temperature
established for the
corresponding hour
during the most
recent performance
test, as specified
in item 13 of Table
4 to this subpart;
and
v. Reporting, in
accordance with Sec.
63.9814(e), any
temperature
measurements below
the minimum
allowable thermal
oxidizer combustion
chamber temperature
measured during the
most recent
performance test.
[[Page 66089]]
9. Batch process units that Maintain the i. Measuring and
are equipped with a catalytic hourly average recording
oxidizer. temperature at temperatures at the
the inlet of the inlet of the
catalyst bed at catalyst bed at
or above the least every 15
corresponding minutes; and
hourly average ii. Calculating the
temperature hourly average
established for temperature at the
the inlet of the
corresponding 1- catalyst bed; and
hour period of
the cycle during
the most recent
performance test.
iii. From the start
of each batch cycle
until 3 hours have
passed since the
process unit reached
maximum temperature,
maintaining the
hourly average
operating
temperature at the
inlet of the
catalyst bed at or
above the minimum
allowable bed inlet
temperature
established for the
corresponding period
during the most
recent performance
test, as determined
according to item 12
of Table 4 to this
subpart; and
iv. For each
subsequent hour of
the batch cycle,
maintaining the
hourly average
operating
temperature at the
inlet of the
catalyst bed at or
above the minimum
allowable bed inlet
temperature
established for the
corresponding hour
during the most
recent performance
test, as specified
in item 13 of Table
4 to this subpart;
and
v. Reporting, in
accordance with Sec.
63.9814(e), any
catalyst bed inlet
temperature
measurements below
the minimum
allowable bed inlet
temperature measured
during the most
recent performance
test; and
vi. Checking the
activity level of
the catalyst at
least every 12
months and taking
any necessary
corrective action,
such as replacing
the catalyst, to
ensure that the
catalyst is
performing as
designed.
10. Each new kiln that is used As specified in Satisfying the
to process clay refractory items 11 through applicable
products. 13 of this table. requirements
specified in items
11 through 13 of
this table.
11. Each new kiln that is a. Maintain the i. Collecting the DLA
equipped a DLA. average pressure pressure drop data,
drop across the as specified in item
DLA for each 3- 18.a. of Table 4 to
hour block this subpart; and
period at or ii. Reducing the DLA
above the pressure drop data
minimum pressure to 1-hour and 3-hour
drop established block averages; and
during the most
recent
performance test.
iii. Maintaining the
3-hour block average
pressure drop across
the DLA at or above
the minimum pressure
drop established
during the most
recent performance
test.
b. Maintain free- Verifying that the
flowing limestone hopper has
limestone in the an adequate amount
feed hopper, of free-flowing
silo, and DLA. limestone by
performing a daily
visual check of the
limestone hopper.
c. Maintain the Recording the
limestone feeder limestone feeder
setting at or setting at least
above the level daily to verify that
established the feeder setting
during the most is being maintained
recent at or above the
performance test. level established
during the most
recent performance
test.
d. Use the same Using the same grade
grade of of limestone as was
limestone from used during the most
the same source recent performance
as was used test and maintaining
during the most records of the
recent source and grade of
performance test. limestone.
e. Maintain no VE i. Performing VE
from the stack. observations of the
stack at the
frequency specified
in Sec. 63.9810(f)
using EPA Method 22
of 40 CFR part 60,
appendix A-7; and
ii. Maintaining no VE
from the stack.
12. Each new kiln that is a. Initiate i. Initiating
equipped with a DIFF or DLS/ corrective corrective action
FF. action within 1 within 1 hour of a
hour of a bag bag leak detection
leak detection system alarm and
system alarm and completing
complete corrective actions
corrective in accordance with
actions in the OM&M plan; and
accordance with >ii. Operating and
the OM&M plan; maintaining the
AND operate and fabric filter such
maintain the that the alarm does
fabric filter not engage for more
such that the than 5 percent of
alarm does not the total operating
engage for more time in a 6-month
than 5 percent block reporting
of the total period; in
operating time calculating this
in a 6-month operating time
block reporting fraction, if
period. inspection of the
fabric filter
demonstrates that no
corrective action is
required, no alarm
time is counted; if
corrective action is
required, each alarm
shall be counted as
a minimum of 1 hour;
if you take longer
than 1 hour to
initiate corrective
action, the alarm
time shall be
counted as the
actual amount of
time taken by you to
initiate corrective
action.
[[Page 66090]]
b. Maintain free- i. Verifying at least
flowing lime in once each 8-hour
the feed hopper shift that lime is
or silo at all free-flowing via a
times for load cell, carrier
continuous gas/lime flow
injection indicator, carrier
systems; AND gas pressure drop
maintain feeder measurement system,
setting at or or other system;
above the level recording all
established monitor or sensor
during the most output, and if lime
recent is found not to be
performance test free flowing,
for continuous promptly initiating
injection and completing
systems. corrective actions;
and
ii. Recording the
feeder setting once
each day of
operation to verify
that the feeder
setting is being
maintained at or
above the level
established during
the most recent
performance test.
13. Each new kiln that is used a. Maintain the i. Collecting the
to process clay refractory average pressure scrubber pressure
products and is equipped with drop across the drop data, as
a wet scrubber. scrubber for specified in item
each 3-hour 20.a. of Table 4 to
block period at this subpart; and
or above the ii. Reducing the
minimum pressure scrubber pressure
drop established drop data to 1-hour
during the most and 3-hour block
recent averages; and
performance test.
iii. Maintaining the
3-hour block average
scrubber pressure
drop at or above the
minimum pressure
drop established
during the most
recent performance
test.
b. Maintain the i. Collecting the
average scrubber scrubber liquid pH
liquid pH for data, as specified
each 3-hour in item 20.b. of
block period at Table 4 to this
or above the subpart; and
minimum scrubber ii. Reducing the
liquid pH scrubber liquid pH
established data to 1-hour and 3-
during the most hour block averages;
recent and
performance test.
iii. Maintaining the
3-hour block average
scrubber liquid pH
at or above the
minimum scrubber
liquid pH
established during
the most recent
performance test.
c. Maintain the i. Collecting the
average scrubber scrubber liquid flow
liquid flow rate rate data, as
for each 3-hour specified in item
block period at 20.c. of Table 4 to
or above the this subpart; and
minimum scrubber ii. Reducing the
liquid flow rate scrubber liquid flow
established rate data to 1-hour
during the most and 3-hour block
recent averages; and
performance test.
iii. Maintaining the
3-hour block average
scrubber liquid flow
rate at or above the
minimum scrubber
liquid flow rate
established during
the most recent
performance test.
d. If chemicals i. Collecting the
are added to the scrubber chemical
scrubber liquid, feed rate data, as
maintain the specified in item
average scrubber 20.d. of Table 4 to
chemical feed this subpart; and
rate for each 3- ii. Reducing the
hour block scrubber chemical
period at or feed rate data to 1-
above the hour and 3-hour
minimum scrubber block averages; and
chemical feed
rate established
during the most
recent
performance test.
iii. Maintaining the
3-hour block average
scrubber chemical
feed rate at or
above the minimum
scrubber chemical
feed rate
established during
the most recent
performance test.
14. Each new and existing a. Maintain the i. Collecting the
affected kiln that is average carbon carbon flow rate
equipped with an activated flow rate for data, as specified
carbon injection system. each 3-hour in item 23 of Table
block period at 4 to this subpart;
or above the and
average carbon ii. Reducing the
flow rate carbon flow rate
established data to 3-hour block
during the Hg averages; and
performance test
in which
compliance was
demonstrated.
iii. Maintaining the
average carbon flow
rate for each 3-hour
block period at or
above the average
carbon flow rate
established during
the Hg performance
test in which
compliance was
demonstrated.
15. Each existing affected a. Maintain no VE i. Performing VE
kiln that is equipped with a from the stack. observations of the
DLA or no add-on control. stack at the
frequency specified
in Sec. 63.9810(f)
using EPA Method 22
of 40 CFR part 60,
appendix A-7; and
ii. Maintaining no VE
from the stack.
16. Each existing affected a. Maintain no VE i. Performing VE
kiln that is equipped with a from the stack; observations of the
FF. OR. stack at the
frequency specified
in Sec. 63.9810(f)
using EPA Method 22
of 40 CFR part 60,
appendix A-7; and
ii. Maintaining no VE
from the stack.
[[Page 66091]]
b. Initiate i. Initiating
corrective corrective action
action within 1 within 1 hour of a
hour of a bag bag leak detection
leak detection system alarm and
system alarm and completing
complete corrective actions
corrective in accordance with
actions in the OM&M plan; and
accordance with ii. Operating and
the OM&M plan; maintaining the
AND operate and fabric filter such
maintain the that the alarm does
fabric filter not engage for more
such that the than 5 percent of
alarm does not the total operating
engage for more time in a 6-month
than 5 percent block reporting
of the total period; in
operating time calculating this
in a 6-month operating time
block reporting fraction, if
period. inspection of the
fabric filter
demonstrates that no
corrective action is
required, no alarm
time is counted; if
corrective action is
required, each alarm
shall be counted as
a minimum of 1 hour;
if you take longer
than 1 hour to
initiate corrective
action, the alarm
time shall be
counted as the
actual amount of
time taken by you to
initiate corrective
action.
17. Each existing affected a. Maintain the i. Collecting the
kiln that is equipped with a average pressure scrubber pressure
wet scrubber. drop across the drop data, as
scrubber for specified in item
each 3-hour 25.a of Table 4 to
block period at this subpart; and
or above the ii. Reducing the
minimum pressure scrubber pressure
drop established drop data to 1-hour
during the most and 3-hour block
recent averages; and
performance test.
iii. Maintaining the
3-hour block average
scrubber pressure
drop at or above the
minimum pressure
drop established
during the most
recent performance
test.
b. Maintain the i. Collecting the
average scrubber scrubber liquid flow
liquid flow rate rate data, as
for each 3-hour specified in item
block period at 25.b. of Table 4 to
or above the this subpart; and
minimum scrubber ii. Reducing the
liquid flow rate scrubber liquid flow
established rate data to 1-hour
during the most and 3-hour block
recent averages; and
performance test.
iii. Maintaining the
3-hour block average
scrubber liquid flow
rate at or above the
minimum scrubber
liquid flow rate
established during
the most recent
performance test.
------------------------------------------------------------------------
0
25. Table 9 to Subpart SSSSS is revised to read as follows:
Table 9 to Subpart SSSSS of Part 63--Continuous Compliance With Work
Practice Standards
As stated in Sec. 63.9810, you must show continuous compliance
with the work practice standards for affected sources according to the
following table:
------------------------------------------------------------------------
For the following
work practice You must demonstrate
For . . . standard . . . continuous compliance
by . . .
------------------------------------------------------------------------
1. Each affected source listed Each applicable i. Performing each
in Table 3 to this subpart. work practice applicable work
requirement practice standard
listed in Table listed in Table 3 to
3 to this this subpart; and
subpart. ii. Maintaining
records that
document the method
and frequency for
complying with each
applicable work
practice standard
listed in Table 3 to
this subpart, as
required by Sec.
Sec. 63.10(b) and
63.9816(c)(2).
2. Each basket or container Control POM i. Controlling
that is used for holding emissions from emissions from the
fired refractory shapes in an any affected volatilization of
existing shape preheater and shape preheater. residual pitch by
autoclave during the pitch implementing one of
impregnation process. the work practice
standards listed in
item 1 of Table 3 to
this subpart; and
ii. Recording the
date and cleaning
method each time you
clean an affected
basket or container.
3. Each new or existing pitch Control POM Capturing and venting
working tank. emissions. emissions from the
affected pitch
working tank to the
control device that
is used to control
emissions from an
affected defumer or
coking oven, or to a
thermal or catalytic
oxidizer that is
comparable to the
control device used
on an affected
defumer or coking
oven.
4. Each new or existing Minimize fuel- i. Before November
chromium refractory products based HAP 19, 2021, using
kiln. emissions. natural gas, or
equivalent, as the
kiln fuel at all
times except during
periods of natural
gas curtailment or
supply interruption;
on and after
November 19, 2021,
using natural gas,
or equivalent, as
the kiln fuel at all
times; and
ii. Before November
19, 2021, if you
intend to use an
alternative fuel,
submitting a
notification of
alternative fuel use
within 48 hours of
the declaration of a
period of natural
gas curtailment or
supply interruption,
as defined in Sec.
63.9824; and
iii. Before November
19, 2021, submitting
a report of
alternative fuel use
within 10 working
days after
terminating the use
of the alternative
fuel, as specified
in Sec.
63.9814(g).
[[Page 66092]]
5. Each existing clay Minimize fuel- i. Before November
refractory products kiln. based HAP 19, 2021, using
emissions. natural gas, or
equivalent, as the
kiln fuel at all
times except during
periods of natural
gas curtailment or
supply interruption;
on and after
November 19, 2021,
using natural gas,
or equivalent, as
the kiln fuel at all
times; and
ii. Before November
19, 2021, if you
intend to use an
alternative fuel,
submitting a
notification of
alternative fuel use
within 48 hours of
the declaration of a
period of natural
gas curtailment or
supply interruption,
as defined in Sec.
63.9824; and
iii. Before November
19, 2021, submitting
a report of
alternative fuel use
within 10 working
days after
terminating the use
of the alternative
fuel, as specified
in Sec.
63.9814(g).
6. Each affected continuous Minimize organic i. Operating the
kiln used to manufacture HAP emissions. control device at
refractory products that use all times unless you
organic HAP that is equipped receive
with an emission control Administrator
device for THC. approval to take the
control device out
of service for
scheduled
maintenance, as
specified in Sec.
63.9792(e); and
ii. Minimizing HAP
emissions during the
period when the kiln
is operating and the
control device is
out of service as
specified in item 5
of Table 3 to this
subpart; and
iii. On and after
November 19, 2021,
recording the actual
hourly organic HAP
processing rate for
the kiln while the
control device was
out of service and
the amount of
product manufactured
in the kiln while
the control device
was out of service;
and
iv. Recording the
duration of each
period when the kiln
is operating and the
control device is
out of service and,
on and after
November 19, 2021,
the total amount of
time per year on a
12-month rolling
basis that the kiln
has operated and the
control device has
been out of service.
7. Each new or existing curing Minimize fuel- Using natural gas, or
oven, shape dryer, and kiln based HAP equivalent, as the
that is used to process emissions. kiln fuel at all
refractory products that use times.
organic HAP, on and after
November 19, 2021.
------------------------------------------------------------------------
0
26. Table 10 to Subpart SSSSS is revised to read as follows:
Table 10 to Subpart SSSSS of Part 63--Requirements for Reports
As stated in Sec. 63.9814, you must comply with the requirements
for reports in the following table:
------------------------------------------------------------------------
The report must You must submit the
You must submit a(n) . . . contain . . . report . . .
------------------------------------------------------------------------
1. Compliance report.......... The information Semiannually
in Sec. according to the
63.9814(c) requirements in Sec.
through (f). 63.9814(a) through
(f).
2. Before May 19, 2022, a. Actions taken By fax or telephone
immediate SSM report if you for the event. within 2 working
had a startup, shutdown, or days after starting
malfunction during the actions inconsistent
reporting period that is not with the plan.
consistent with your SSMP, on
and after May 19, 2022,
immediate SSM report is not
required.
b. The By letter within 7
information in working days after
Sec. the end of the event
63.10(d)(5)(ii). unless you have made
alternative
arrangements with
the permitting
authority.
3. Before May 19, 2022, report The information If you are subject to
of alternative fuel use. in Sec. the work practice
63.9814(g) and standard specified
items 4 and 5 of in item 3 or 4 of
Table 9 to this Table 3 to this
subpart. subpart, and you use
an alternative fuel
in the affected
kiln, by letter
within 10 working
days after
terminating the use
of the alternative
fuel.
4. Performance test report.... The information According to the
in Sec. requirements of Sec.
63.7(g). 63.9814(h).
5. CMS performance evaluation, The information According to the
as required for CEMS. in Sec. requirements of Sec.
63.7(g). 63.9814(i).
------------------------------------------------------------------------
0
27. Table 11 to Subpart SSSSS is revised to read as follows:
Table 11 to Subpart SSSSS of Part 63--Applicability of General
Provisions to Subpart SSSSS
As stated in Sec. 63.9820, you must comply with the applicable
General Provisions requirements according to the following table:
[[Page 66093]]
----------------------------------------------------------------------------------------------------------------
Applies to subpart
Citation Subject Brief description SSSSS
----------------------------------------------------------------------------------------------------------------
Sec. 63.1........................ Applicability......... ........................... Yes.
Sec. 63.2........................ Definitions........... ........................... Yes.
Sec. 63.3........................ Units and ........................... Yes.
Abbreviations.
Sec. 63.4........................ Prohibited Activities. Compliance date; Yes.
circumvention,
severability.
Sec. 63.5........................ Construction/ Applicability; Yes.
Reconstruction. applications; approvals.
Sec. 63.6(a)..................... Applicability......... General Provisions (GP) Yes.
apply unless compliance
extension; GP apply to
area sources that become
major.
Sec. 63.6(b)(1)-(4).............. Compliance Dates for Standards apply at Yes.
New and Reconstructed effective date; 3 years
Sources. after effective date; upon
startup; 10 years after
construction or
reconstruction commences
for section 112(f).
Sec. 63.6(b)(5).................. Notification.......... ........................... Yes.
Sec. 63.6(b)(6).................. [Reserved]............
Sec. 63.6(b)(7).................. Compliance Dates for Area sources that become Yes.
New and Reconstructed major must comply with
Area Sources That major source standards
Become Major. immediately upon becoming
major, regardless of
whether required to comply
when they were area
sources.
Sec. 63.6(c)(1)-(2).............. Compliance Dates for Comply according to date in Yes.
Existing Sources. subpart, which must be no
later than 3 years after
effective date; for
section 112(f) standards,
comply within 90 days of
effective date unless
compliance extension.
Sec. 63.6(c)(3)-(4).............. [Reserved]............
Sec. 63.6(c)(5).................. Compliance Dates for Area sources that become Yes.
Existing Area Sources major must comply with
That Become Major. major source standards by
date indicated in subpart
or by equivalent time
period (for example, 3
years).
Sec. 63.6(d)..................... [Reserved]............
Sec. 63.6(e)(1)-(2).............. Operation & Operate to minimize Yes before May 19,
Maintenance. emissions at all times; 2022. No on and after
correct malfunctions as May 19, 2022.
soon as practicable;
requirements independently
enforceable; information
Administrator will use to
determine if operation and
maintenance requirements
were met; see Sec.
63.9792(b) for general
duty requirement..
Sec. 63.6(e)(3).................. SSMP requirements..... ........................... Yes before May 19,
2022. No on and after
May 19, 2022.
Sec. 63.6(f)(1).................. Compliance Except You must comply with No.
During SSM. emission standards at all
times except during SSM.
Sec. 63.6(f)(2)-(3).............. Methods for Compliance based on Yes.
Determining performance test,
Compliance. operation and maintenance
plans, records, inspection.
Sec. 63.6(g)(1)-(3).............. Alternative Standard.. Procedures for getting an Yes.
alternative standard..
Sec. 63.6(h)(1)-(9).............. Opacity/Visible ........................... Not applicable.
Emission (VE)
Standards.
Sec. 63.6(i)(1)-(14)............. Compliance Extension.. Procedures and criteria for Yes.
Administrator to grant
compliance extension.
Sec. 63.6(j)..................... Presidential President may exempt source Yes.
Compliance Exemption. category.
Sec. 63.7(a)(1)-(2).............. Performance Test Dates Dates for conducting Yes.
initial performance
testing and other
compliance demonstrations;
must conduct 180 days
after first subject to
rule.
Sec. 63.7(a)(3).................. Section 114 Authority. Administrator may require a Yes.
performance test under CAA
section 114 at any time.
Sec. 63.7(b)(1).................. Notification of Must notify Administrator Yes.
Performance Test. 60 days before the test.
Sec. 63.7(b)(2).................. Notification of Must notify Administrator 5 Yes.
Rescheduling. days before scheduled date
and provide rescheduled
date.
Sec. 63.7(c)..................... Quality Assurance/Test Requirements; test plan Yes.
Plan. approval procedures;
performance audit
requirements; internal and
external QA procedures for
testing.
Sec. 63.7(d)..................... Testing Facilities.... ........................... Yes.
Sec. 63.7(e)(1).................. Conditions for See Sec. 63.9800......... No, Sec. 63.9800
Conducting specifies
Performance Tests. requirements.
Sec. 63.7(e)(2).................. Conditions for Must conduct according to Yes.
Conducting subpart and EPA test
Performance Tests. methods unless
Administrator approves
alternative.
Sec. 63.7(e)(3).................. Test Run Duration..... Must have three test runs Yes; Yes, except where
of at least 1 hour each; specified in Sec.
compliance is based on 63.9800 for batch
arithmetic mean of three process sources; Yes.
runs; conditions when data
from an additional test
run can be used.
Sec. 63.7(f)..................... Alternative Test ........................... Yes.
Method.
Sec. 63.7(g)..................... Performance Test Data ........................... Yes, except this
Analysis. subpart specifies how
and when the
performance test and
performance
evaluation results
are reported.
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Sec. 63.7(h)..................... Waiver of Test........ ........................... Yes.
Sec. 63.8(a)(1).................. Applicability of ........................... Yes.
Monitoring
Requirements.
Sec. 63.8(a)(2).................. Performance Performance Specifications Yes.
Specifications. in appendix B of 40 CFR
part 60 apply.
Sec. 63.8(a)(3).................. [Reserved]............
Sec. 63.8(a)(4).................. Monitoring with Flares ........................... Not applicable.
Sec. 63.8(b)(1).................. Monitoring............ Must conduct monitoring Yes.
according to standard
unless Administrator
approves alternative.
Sec. 63.8(b)(2)-(3).............. Multiple Effluents and Specific requirements for Yes.
Multiple Monitoring installing and reporting
Systems. on monitoring systems.
Sec. 63.8(c)(1).................. Continuous Monitoring Maintenance consistent with Yes before May 19,
System Operation and good air pollution control 2022. No on and after
Maintenance. practices. May 19, 2022.
Sec. 63.8(c)(2)-(3).............. Monitoring System Must install to get Yes.
Installation. representative emission
and parameter measurements.
Sec. 63.8(c)(4).................. CMS Requirements...... ........................... No, Sec. 63.9808
specifies
requirements.
Sec. 63.8(c)(5).................. COMS Minimum ........................... Not applicable.
Procedures.
Sec. 63.8(c)(6).................. CMS Requirements...... ........................... Applies only to
sources required to
install and operate a
THC CEMS.
Sec. 63.8(c)(7)(i)(A)............ CMS Requirements...... ........................... Applies only to
sources required to
install and operate a
THC CEMS.
Sec. 63.8(c)(7)(i)(B)............ CMS Requirements...... ........................... Applies only to
sources required to
install and operate a
THC CEMS.
Sec. 63.8(c)(7)(i)(C)............ CMS Requirements...... ........................... Not applicable.
Sec. 63.8(c)(7)(ii).............. CMS Requirements...... Corrective action required Yes.
when CMS is out of control.
Sec. 63.8(c)(8).................. CMS Requirements...... ........................... Yes.
Sec. 63.8(d)(1) and (2).......... CMS Quality Control... ........................... Yes.
Sec. 63.8(d)(3).................. Written procedures for ........................... No, Sec.
CMS. 63.9794(a)(8)
specifies
requirements.
Sec. 63.8(e)..................... CMS Performance ........................... Applies only to
Evaluation. sources required to
install and operate a
THC CEMS, except this
subpart specifies how
and when the
performance
evaluation results
are reported.
Sec. 63.8(f)(1)-(5).............. Alternative Monitoring ........................... Yes.
Method.
Sec. 63.8(f)(6).................. Alternative to ........................... Yes.
Relative Accuracy
Test.
Sec. 63.8(g)..................... Data Reduction........ ........................... Applies only to
sources required to
install and operate a
THC CEMS.
Sec. 63.9(a)..................... Notification ........................... Yes.
Requirements.
Sec. 63.9(b)(1)-(5).............. Initial Notifications. ........................... Yes.
Sec. 63.9(c)..................... Request for Compliance ........................... Yes.
Extension.
Sec. 63.9(d)..................... Notification of ........................... Yes.
Special Compliance
Requirements for New
Source.
Sec. 63.9(e)..................... Notification of Notify Administrator 60 Yes.
Performance Test. days prior.
Sec. 63.9(f)..................... Notification of VE/ ........................... Not applicable.
Opacity Test.
Sec. 63.9(g)..................... Additional ........................... Applies only to
Notifications When sources required to
Using CMS. install and operate a
THC CEMS.
Sec. 63.9(h)..................... Notification of ........................... Yes.
Compliance Status.
Sec. 63.9(i)..................... Adjustment of ........................... Yes.
Submittal Deadlines.
Sec. 63.9(j)..................... Change in Previous ........................... Yes.
Information.
Sec. 63.9(k)..................... Notifications......... Electronic reporting Yes, only as specified
procedures. in Sec. 63.9(j).
Sec. 63.10(a).................... Recordkeeping/ ........................... Yes.
Reporting.
Sec. 63.10(b)(1)................. General Recordkeeping ........................... Yes.
Requirements.
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Sec. 63.10(b)(2)(i)-(ii)......... Recordkeeping of See Sec. 63.9816......... Yes before May 19,
Occurrence and 2022. No on and after
Duration of Startups May 19, 2022.
and Shutdowns and
Failures to Meet
Standards.
Sec. 63.10(b)(2)(iii)............ Recordkeeping Relevant ........................... Yes.
to Maintenance of Air
Pollution Control and
Monitoring Equipment.
Sec. 63.10(b)(2)(iv)-(v)......... Actions Taken to ........................... Yes before May 19,
Minimize Emissions 2022. No on and after
during SSM. May 19, 2022.
Sec. 63.10(b)(2)(vi)............. Recordkeeping for CMS See Sec. 63.9816(c)(5)... Yes before May 19,
Malfunctions. 2022. No on and after
May 19, 2022.
Sec. 63.10(b)(2)(vii)-(xi)....... Records............... Measurements to demonstrate Yes.
compliance with emission
limitations; performance
test, performance
evaluation, and visible
emission observation
results; measurements to
determine conditions of
performance tests and
performance evaluations.
Sec. 63.10(b)(2)(xii)............ Records............... Records when under waiver.. Yes.
Sec. 63.10(b)(2)(xiii)........... Records............... Records when using Not applicable.
alternative to relative
accuracy test.
Sec. 63.10(b)(2)(xiv)............ Records............... All documentation Yes.
supporting Initial
Notification and
Notification of Compliance
Status.
Sec. 63.10(b)(3)................. Records............... Applicability Yes.
Determinations.
Sec. 63.10(c)(1), (c)(5)-(6)..... Additional Records for ........................... Yes.
CMS.
Sec. 63.10(c)(2)-(4)............. Records............... Additional Records for CMS. Not applicable.
Sec. 63.10(c)(7)-(8)............. Records of excess Sec. 63.9816 specifies No.
emissions and requirements..
parameter monitoring
exceedances for CMS.
Sec. 63.10(c)(9)................. Records............... Additional Records for CMS. Not applicable.
Sec. 63.10(c)(10)-(14)........... Additional Records for ........................... Yes.
CMS.
Sec. 63.10(c)(15)................ Records Regarding the ........................... Yes before May 19,
SSMP. 2022. No on and after
May 19, 2022.
Sec. 63.10(d)(1)................. General Reporting Requirements for reporting. Yes.
Requirements.
Sec. 63.10(d)(2)................. Report of Performance When to submit to Federal No. This subpart
Test Results. or State authority. specifies how and
when the performance
test results are
reported.
Sec. 63.10(d)(3)................. Reporting Opacity or ........................... Not applicable.
VE Observations.
Sec. 63.10(d)(4)................. Progress Reports...... Must submit progress Yes.
reports on schedule if
under compliance extension.
Sec. 63.10(d)(5)................. SSM Reports........... Contents and submission See Yes before May 19,
Sec. 63.9814 (d) and (e) 2022. No on and after
for malfunction reporting May 19, 2022.
requirements..
Sec. 63.10(e)(1)-(2)............. Additional CMS Reports ........................... Applies only to
sources required to
install and operate a
THC CEMS, except this
subpart specifies how
and when the
performance
evaluation results
are reported.
Sec. 63.10(e)(3)................. Reports............... ........................... No, Sec. 63.9814
specifies
requirements.
Sec. 63.10(e)(4)................. Reporting COMS data... ........................... Not applicable.
Sec. 63.10(f).................... Waiver for ........................... Yes.
Recordkeeping/
Reporting.
Sec. 63.11....................... Flares................ ........................... Not applicable.
Sec. 63.12....................... Delegation............ ........................... Yes.
Sec. 63.13....................... Addresses............. ........................... Yes.
Sec. 63.14....................... Incorporation by ........................... Yes.
Reference.
Sec. 63.15....................... Availability of ........................... Yes.
Information and
Confidentiality.
Sec. 63.16....................... Performance Track ........................... Yes.
Provisions.
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[[Page 66096]]
[FR Doc. 2021-24100 Filed 11-18-21; 8:45 am]
BILLING CODE 6560-50-P