Reconsideration of Certain New Source and Startup/Shutdown Issues: National Emission Standards for Hazardous Air Pollutants From Coal- and Oil-Fired Electric Utility Steam Generating Units and Standards of Performance for Fossil-Fuel-Fired Electric Utility, Industrial-Commercial-Institutional, and Small Industrial-Commercial-Institutional Steam Generating Units, 71323-71344 [2012-28729]
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Federal Register / Vol. 77, No. 231 / Friday, November 30, 2012 / Rules and Regulations
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Issued in Washington, DC, this 20th day of
November, 2012.
Laricke Blanchard,
Deputy Director for Policy, Pension Benefit
Guaranty Corporation.
[FR Doc. 2012–28892 Filed 11–29–12; 8:45 am]
BILLING CODE 7709–01–P
ENVIRONMENTAL PROTECTION
AGENCY
40 CFR Parts 60 and 63
[EPA–HQ–OAR–2009–0234; EPA–HQ–OAR–
2011–0044; FRL–9733–2]
RIN 2060–AR62
Reconsideration of Certain New
Source and Startup/Shutdown Issues:
National Emission Standards for
Hazardous Air Pollutants From Coaland Oil-Fired Electric Utility Steam
Generating Units and Standards of
Performance for Fossil-Fuel-Fired
Electric Utility, Industrial-CommercialInstitutional, and Small IndustrialCommercial-Institutional Steam
Generating Units
Environmental Protection
Agency (EPA).
ACTION: Proposed rules; notice of public
hearing.
AGENCY:
On February 16, 2012,
pursuant to sections 111 and 112 of the
Clean Air Act (CAA), the EPA published
the final rules titled ‘‘National Emission
Standards for Hazardous Air Pollutants
from Coal- and Oil-fired Electric Utility
Steam Generating Units and Standards
of Performance for Fossil-Fuel-Fired
Electric Utility, Industrial-CommercialInstitutional, and Small IndustrialCommercial-Institutional Steam
Generating Units.’’ The National
Emission Standards for Hazardous Air
Pollutants (NESHAP) rule issued
pursuant to CAA section 112 is referred
to as the Mercury and Air Toxics
Standards (MATS), and the New Source
Performance Standards rule issued
pursuant to CAA section 111 is referred
to as the Utility NSPS. The
Administrator received petitions for
reconsideration of certain aspects of
MATS and the Utility NSPS. In this
notice, the EPA is announcing
reconsideration of certain new source
standards for MATS, the requirements
applicable during periods of startup and
shutdown for MATS, the startup and
shutdown provisions related to the
particulate matter (PM) standard in the
Utility NSPS, and certain revisions to
the definitional and monitoring
provisions of the Utility NSPS. We are
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SUMMARY:
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also proposing certain technical
corrections to both MATS and the
Utility NSPS.
We seek comment only on the aspects
of the final MATS and Utility NSPS
rules specifically identified in this
notice. We are not opening for
reconsideration any other provisions of
MATS or the Utility NSPS at this time.
DATES: Comments. Comments must be
received on or before December 31,
2012. Because of the need to resolve the
issues identified in this notice in a
timely manner, the EPA does not intend
to grant requests for extensions beyond
this date.
Public Hearing. If anyone contacts the
EPA by December 10, 2012 requesting to
speak at a public hearing, the EPA will
hold a public hearing on December 18,
2012. If a public hearing is held, it will
be held from 9:00 a.m. to 7:00 p.m.,
Eastern time, in Room 1153 EPA East
Hearing room, 1201 Constitution
Avenue NW., Washington, DC 20460,
(202) 564–1657. For further information
on the public hearing and requests to
speak, see the ADDRESSES section of this
preamble.
ADDRESSES: Comments. Submit your
comments, identified by Docket ID. No.
EPA–HQ–OAR–2011–0044 (NSPS
action) or Docket ID No. EPA–HQ–
OAR–2009–0234 (NESHAP/MATS
action), by one of the following
methods:
• https://www.regulations.gov. Follow
the instructions for submitting
comments.
• https://www.epa.gov/oar/
docket.html. Follow the instructions for
submitting comments on the EPA Air
and Radiation Docket Web Site.
• Email: Comments may be sent by
electronic mail (email) to a-and-rdocket@epa.gov, Attention EPA–HQ–
OAR–2011–0044 (NSPS action) or EPA–
HQ–OAR–2009–0234 (NESHAP/MATS
action).
• Fax: Fax your comments to: (202)
566–9744, Docket ID No. EPA–HQ–
OAR–2011–0044 (NSPS action) or
Docket ID No. EPA–HQ–OAR–2009–
0234 (NESHAP/MATS action).
• Mail: Send your comments on the
NESHAP/MATS action to: EPA Docket
Center (EPA/DC), Environmental
Protection Agency, Mailcode: 2822T,
1200 Pennsylvania Ave. NW.,
Washington, DC 20460, Docket ID No.
EPA–HQ–OAR–2009–0234. Send your
comments on the NSPS action to: EPA
Docket Center (EPA/DC), Environmental
Protection Agency, Mailcode: 2822T,
1200 Pennsylvania Ave. NW.,
Washington, DC 20460, Docket ID. EPA–
HQ–OAR–2011–0044. Please include a
total of two copies. In addition, please
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71323
mail a copy of your comments on the
information collection provisions to the
Office of Information and Regulatory
Affairs, OMB, Attn: Desk Officer for
EPA, 725 17th St. NW., Washington, DC
20503.
• Hand Delivery or Courier: Deliver
your comments to: EPA Docket Center,
EPA West, Room 3334, 1301
Constitution Ave. NW., Washington, DC
20460. Please include a total of two
copies. Such deliveries are only
accepted during the Docket’s normal
hours of operation (8:30 a.m. to 4:30
p.m., Monday through Friday, excluding
legal holiday), and special arrangements
should be made for deliveries of boxed
information.
Instructions. All submissions must
include agency name and respective
docket number or Regulatory
Information Number (RIN) for this
rulemaking. All comments will be
posted without change and may be
made available online at https://
www.regulations.gov, including any
personal information provided, unless
the comment includes information
claimed to be confidential business
information (CBI) or other information
whose disclosure is restricted by statute.
Do not submit information that you
consider to be CBI or otherwise
protected through https://
www.regulations.gov or email. The
https://www.regulations.gov Web site is
an ‘‘anonymous access’’ system, which
means the EPA will not know your
identity or contact information unless
you provide it in the body of your
comment. If you send an email
comment directly to the EPA without
going through https://
www.regulations.gov, your email
address will be automatically captured
and included as part of the comment
that is placed in the public docket and
made available on the Internet. If you
submit an electronic comment, the EPA
recommends that you include your
name and other contact information in
the body of your comment and with any
disk or CD–ROM you submit. If the EPA
cannot read your comment due to
technical difficulties and cannot contact
you for clarification, the EPA may not
be able to consider your comment.
Electronic files should avoid the use of
special characters, any form of
encryption, and be free of any defects or
viruses.
Public Hearing. If anyone contacts
EPA by December 10, 2012 requesting to
speak at a public hearing, the EPA will
hold a public hearing on December 18,
2012. If a public hearing is held, it will
be held from 9:00 a.m. to 7:00 p.m.,
Eastern time in Room 1153 EPA East
Hearing room, 1201 Constitution
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Avenue NW., Washington, DC 20460,
202–564–1657. A lunch break is
scheduled from 12:00 p.m.–1:00 p.m.
Visitors must go through a metal
detector, sign in with the security desk,
be accompanied by an employee and
show identification to enter the
building. Contact Pamela Garrett at
(919) 541–7966 or at
garrett.pamela@epa.gov to request a
hearing, to determine if a hearing will
be held and to register to speak if a
hearing is held. If no one contacts the
EPA requesting to speak at a public
hearing concerning this proposed rule
by December 10, 2012, the hearing will
be cancelled without further notice. If a
hearing is held, the last day to register
to present oral testimony in advance
will be Friday, December 14, 2012. The
public hearing will provide interested
parties the opportunity to present data,
views, or arguments concerning this
notice. The record for this action will
remain open for 30 days after the date
of the hearing to provide an opportunity
for submission of rebuttal and
supplementary information. We will
also specify the date and time of the
public hearings on https://www.epa.gov/
airquality/powerplanttoxics/
actions.html and https://www.epa.gov/
ttn/atw/utility/utilitypg.html.
Docket. All documents in the docket
are listed in the https://
www.regulations.gov index. Although
listed in the index, some information is
not publicly available (e.g., CBI or other
information whose disclosure is
restricted by statute). Certain other
material, such as copyrighted material,
will be publicly available only in hard
copy form. Publicly available docket
Category
Industry .....................................
Federal government .................
State/local/Tribal government ...
materials are available either
electronically in https://
www.regulations.gov or in hard copy at
the EPA Docket Center, Room 3334,
1301 Constitution Avenue NW.,
Washington, DC. The Public Reading
Room is open from 8:30 a.m. to 4:30
p.m., Monday through Friday, excluding
legal holidays. The telephone number
for the Public Reading Room is (202)
566–1744, and the telephone number for
the Air Docket is (202) 566–1742.
FOR FURTHER INFORMATION CONTACT: For
the NESHAP action: Mr. William
Maxwell, Energy Strategies Group,
Sector Policies and Programs Division,
(D243–01), Office of Air Quality
Planning and Standards, U.S.
Environmental Protection Agency,
Research Triangle Park, North Carolina
27711; Telephone number: (919) 541–
5430; Fax number (919) 541–5450;
Email address: maxwell.bill@epa.gov.
For the NSPS action: Mr. Christian
Fellner, Energy Strategies Group, Sector
Policies and Programs Division, (D243–
01), Office of Air Quality Planning and
Standards, U.S. Environmental
Protection Agency, Research Triangle
Park, North Carolina 27711; Telephone
number: (919) 541–4003; Fax number
(919) 541–5450; Email address:
fellner.christian@epa.gov.
SUPPLEMENTARY INFORMATION:
Outline. The information presented in
this preamble is organized as follows:
I. General Information
A. Does this reconsideration notice apply
to me?
B. What should I consider as I prepare my
comments to the EPA?
C. How do I obtain a copy of this document
and other related information?
II. Background
NAICS code 1
I. General Information
A. Does this reconsideration notice
apply to me?
Categories and entities potentially
affected by today’s notice include:
Examples of potentially regulated entities
221112
2 221122
2 221122
921150
1 North
III. Today’s Action
IV. Discussion of Provisions Subject to
Reconsideration—NESHAP/MATS
A. New Source MATS Emission Limits
B. Eligibility To Be a New Source
C. Startup and Shutdown Provisions
V. Discussion of Provisions Subject to
Reconsideration—Utility NSPS
VI. Technical Corrections and Clarifications
VII. Impacts of This Proposed Rule
A. What are the air impacts?
B. What are the energy impacts?
C. What are the compliance costs?
D. What are the economic and employment
impacts?
E. What are the benefits of the proposed
standards?
VIII. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory
Planning and Review and Executive
Order 13563: Improving Regulation and
Regulatory Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
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 That
Significantly Affect Energy Supply,
Distribution, or Use
I. National Technology Transfer and
Advancement Act
J. Executive Order 12898: Federal Actions
To Address Environmental Justice in
Minority Populations and Low-Income
Populations
Fossil
Fossil
Fossil
Fossil
fuel-fired
fuel-fired
fuel-fired
fuel-fired
electric
electric
electric
electric
utility
utility
utility
utility
steam
steam
steam
steam
generating
generating
generating
generating
units.
units owned by the Federal government.
units owned by municipalities.
units in Indian country.
American Industry Classification System.
State, or local government-owned and operated establishments are classified according to the activity in which they are engaged.
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2 Federal,
This table is not intended to be
exhaustive but rather to provide a guide
for readers regarding entities likely to be
affected by this action. To determine
whether your facility, company,
business, organization, etc. would be
regulated by this action, you should
examine the applicability criteria in 40
CFR 60.40, 60.40Da, or 60.40c or in 40
CFR 63.9982. If you have any questions
regarding the applicability of this action
to a particular entity, consult either the
air permitting authority for the entity or
your EPA regional representative as
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listed in 40 CFR 60.4 or 40 CFR 63.13
(General Provisions).
B. What should I consider as I prepare
my comments to the EPA?
Do not submit information containing
CBI to the EPA through https://
www.regulations.gov or email. Send or
deliver information identified as CBI
only to the following address: Roberto
Morales, OAQPS Document Control
Officer (C404–02), Office of Air Quality
Planning and Standards, U.S.
Environmental Protection Agency,
PO 00000
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Research Triangle Park, North Carolina
27711, Attention: Docket ID EPA–HQ–
OAR–2011–0044 (Utility NSPS) or
Docket ID EPA–HQ–OAR–2009–0234
(NESHAP/MATS). Clearly mark the part
or all of the information that you claim
to be CBI. For CBI information in a disk
or CD–ROM that you mail to the EPA,
mark the outside of the disk or CD–ROM
as CBI and then identify electronically
within the disk or CD–ROM the specific
information that is claimed as CBI. In
addition to one complete version of the
comment that includes information
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Federal Register / Vol. 77, No. 231 / Friday, November 30, 2012 / Rules and Regulations
claimed as CBI, a copy of the comment
that does not contain the information
claimed as CBI must be submitted for
inclusion in the public docket.
Information so marked will not be
disclosed except in accordance with
procedures set forth in 40 CFR part 2.
C. How do I obtain a copy of this
document and other related
information?
In addition to being available in the
docket, electronic copies of these
proposed rules will be available on the
Worldwide Web (WWW) through the
Technology Transfer Network (TTN).
Following signature, a copy of each
proposed rule will be posted on the
TTN’s policy and guidance page for
newly proposed or promulgated rules at
the following address: https://
www.epa.gov/ttn/oarpg/. The TTN
provides information and technology
exchange in various areas of air
pollution control.
II. Background
The Administrator signed MATS and
the Utility NSPS on December 16, 2011,
and the final rules were published in
the Federal Register at 77 FR 9304,
February 16, 2012. Following
promulgation of the final rules, the
Administrator received petitions for
reconsideration of numerous provisions
of both MATS and the Utility NSPS
pursuant to CAA section 307(d)(7)(B).
Copies of the MATS petitions are
provided in rulemaking docket EPA–
HQ–OAR–2009–0234. Copies of the
Utility NSPS petitions are provided in
rulemaking docket EPA–HQ–OAR–
2011–0044.
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III. Today’s Action
Today, we are granting
reconsideration of, proposing, and
requesting comment on the following
limited set of issues: (1) Certain revised
new source standards in MATS, (2)
requirements applicable during periods
of startup and shutdown in MATS, (3)
startup and shutdown provisions related
to the PM standard in the Utility NSPS,
and (4) definitional and monitoring
provisions in the Utility NSPS. We are
also proposing certain technical
corrections to both MATS and the
Utility NSPS.
This notice is limited to the specific
issues identified in this notice. We will
not respond to any comments
addressing any other provisions of
MATS or the Utility NSPS.1
1 The
recent decision by the U.S. Court of
Appeals for the D.C. Circuit regarding the Cross
State Air Pollution Rule (CSAPR) has no impact on
the issues being reconsidered in this action.
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The impacts of today’s proposed
revisions on the costs and the benefits
of the final rule are minor. We expect
that source owners and operators will
install and operate the same or similar
control technologies to meet the
proposed revised standards in this
notice as they would have chosen to
comply with the standards in the
February 2012 final rule.2
IV. Discussion of Provisions Subject to
Reconsideration—NESHAP/MATS
A. New Source MATS Emission Limits
The EPA received petitions requesting
reconsideration of aspects of the new
source emission limits in the final
MATS rule. We are granting
reconsideration of certain new source
emission limits, as discussed below, and
we invite comment on the proposed
provisions in today’s notice.
1. Certain New Source Limits—Use of
Data in the Record
The EPA received petitions for
reconsideration asserting that the
Agency did not use all the data in the
record from the best performing sources
in establishing certain final new source
emission limits for coal- and oil-fired
electric utility steam generating units
(EGUs). Specifically, the petitioners
maintained that the EPA did not
consider all of the data in the record
when establishing emission standards
for filterable PM and hydrogen chloride
(HCl) applicable to new coal-fired EGUs
and for filterable PM applicable to new
solid oil-derived fuel-fired EGUs.
In light of petitioners’ assertions, we
reviewed the available emissions
information in the record for all the new
source standards. We determined that
we did not use all the data in the record
in establishing the new source emission
limits for filterable PM and HCl
applicable to new coal-fired EGUs and
for filterable PM applicable to new solid
oil-derived fuel-fired EGUs. We also
identified a few additional new source
limits for which we did not use all of
the data in the record when setting the
standards in the final rule. We are
proposing to revise the sulfur dioxide
(SO2) limit applicable to solid oilderived fuel-fired EGUs, the filterable
PM limit applicable to continental
liquid oil-fired EGUs, and the lead and
selenium limits applicable to coal-fired
EGUs based on consideration of all the
data in the record from the best
performing sources for the pollutants at
2 Because, on an individual EGU-by-EGU basis we
anticipate very similar costs, any changes to the
baseline since we finalized MATS (e.g., potential
impacts of the CSAPR decision) would not impact
this determination.
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71325
issue. We solicit comment on the
revised standards. Additional details on
the proposed emission limits can be
found in the memo ‘‘Reconsideration of
the National Emission Standards for
Hazardous Air Pollutants (NESHAP)
Maximum Achievable Control
Technology (MACT) Floor Analysis for
Coal- and Oil-fired Electric Utility
Steam Generating Units, Proposed Rule’’
in rulemaking docket EPA–HQ–OAR–
2009–0234.
We also solicit comment on possible
revisions to the Hg limit applicable to
low rank virgin coal-fired EGUs based
on additional data in the record. See
‘‘Reconsideration of the National
Emission Standards for Hazardous Air
Pollutants (NESHAP) Maximum
Achievable Control Technology (MACT)
Floor Analysis for Coal- and Oil-fired
Electric Utility Steam Generating Units,
Proposed Rule’’ in rulemaking docket
EPA–HQ–OAR–2009–0234; ‘‘MATS
Reconsideration: Beyond-the-Floor
Memorandum’’ available in rulemaking
docket EPA–HQ–OAR–2009–0234.
The proposed revised new source
CAA section 112(d) emission standards
are presented in tables 1 and 2 of this
preamble. The Agency derived these
limits by first calculating the floor
standards and then assessing whether a
more stringent beyond-the-floor
standard is appropriate.3 As explained
further below, as to the standards we are
proposing to revise, we are proposing a
beyond-the-floor standard for HCl for
new coal-fired EGUs, but we are not
proposing beyond-the-floor standards
for the other pollutants and
subcategories.
2. SO2 Limit for New Coal-Fired EGUs—
Reliance on Industrial Boiler Emission
Data
We are also reconsidering the SO2
standard for new coal-fired EGUs. The
Agency received a petition asserting that
the final alternative SO2 emission limit
was developed using, as the best
performing source, a unit that is 25 MW
in capacity. In order to be classified as
an EGU, and thus subject to MATS, a
unit must be greater than 25 MW in
capacity. A unit that is 25 MW or less
is likely an industrial boiler and would
be subject to the Industrial-CommercialInstitutional Boiler NESHAP, not
MATS.
At the time of the final rule, we
believed the unit on which we based the
SO2 standard for new coal-fired EGUs
was an EGU. After we received the
petition for reconsideration, we re3 CAA section 112(d)(2) requires the EPA to
consider whether more stringent beyond-the-floor
standards should be established.
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examined the record and determined
that the unit was, in fact, an industrial
boiler and not an EGU.
As an initial matter, nothing in the
CAA precludes the EPA from
identifying a source in another source
category as the best controlled similar
source. However, we believe that it is
appropriate in this case, where we have
considerable data on EGUs, to base the
new source standard on the best
performing unit that is an EGU. This is
also consistent with our intent in the
final rule, as we thought the unit we had
selected was, in fact, an EGU. For these
reasons, we are reconsidering the SO2
standard for new coal-fired EGUs. We
have reviewed the emissions data and
identified the best performing EGU
upon which to base the proposed SO2
standard. The proposed limit is
presented in table 2 of this preamble.
We solicit comment on the revised limit
and the methods used to establish this
limit.
3. Hg Limit for New Coal-Fired EGUs
Designed for Coal ≥ 8300 Btu/lb—
Measurement Issues
The EPA is also reconsidering the
emission limit for Hg for new coal-fired
EGUs in the units designed for the coal
≥ 8300 Btu/lb (non-low rank virgin coal)
subcategory. Some petitioners asserted
that this limit, as finalized, was too low
for emissions to be reliably measured in
a manner that would allow sources to
operate their control technology in a
way that ensures compliance with the
standard. Specifically, petitioners
maintained that sorbent trap monitoring
systems could not provide sufficiently
timely Hg data at the new source level
for sources to make adjustments to the
EGUs and attendant air pollution
control devices (ACPDs) to ensure
compliance with the standard and that
Hg continuous emissions monitoring
systems (CEMS) were not capable of
measuring Hg at the new source limit.
The petitioners indicated that reliable
and frequent emission measurements
are needed to maintain the operation of
Hg control technology at performance
levels set in the final rule.
As we explained in the record to the
final rule, owners and operators of new
EGUs in the non-low rank virgin coal
subcategory could use the sorbent trap
monitoring systems to demonstrate
compliance with the new source Hg
standard because of the potential for a
longer sample collection period
associated with sorbent traps and their
inherent lower emissions detection
capability.
As described in the final rule, when
establishing emission limits for
pollutants, we calculated a
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representative detection limit (RDL) and
then compared the UPL-determined
emission floor with a value three times
the RDL (3 X RDL), and we set the final
limit at the higher of the two numbers.
We did not follow that procedure for
sorbent trap monitoring systems when
setting Hg emission limits as we did not
believe sorbent trap monitoring systems
were constrained by method detection
limits, since operators could increase
the sample collection time up to 14 days
to guarantee collection of a measurable
quantity of mercury with appropriate
accuracy. We continue to believe that
the promulgated Hg limit for the nonlow rank virgin coal subcategory is
measurable using a sorbent trap
monitoring system.
As noted, however, petitioners have
indicated that the long sorbent trap
sampling times that may be necessary to
measure at the final new source level do
not allow sufficiently frequent
emissions feedback such that a source
could take corrective action and avoid
violations of the emission limit within
the prescribed compliance time.
We understand that Hg emissions can
vary over time, and we acknowledge the
value of frequent feedback of emission
measurements. We also understand that
frequent feedback may be desirable and,
at times, necessary to optimize the
operation of generation or control
technology in order to maintain
emissions at or below the standard. The
sorbent trap monitoring method
required in the MATS rule allows
sampling for as long as 14 days. In the
final rule, we assumed that most sources
would leave the sorbent traps in as long
as needed—up to 14 days—to ensure
they had no measurement issues. Based
on the petitions for reconsideration, we
understand that sources will most likely
use a shorter sampling period, perhaps
as short as 30 minutes. The shorter
sampling periods will provide more
constant feedback on Hg emissions,
which will help the source ensure that
it is in compliance with the Hg emission
limit, for which compliance is
determined on a 30-day rolling average.
Given the petitioners’ stated need for
more frequent Hg emissions
information, we re-evaluated whether
detection level issues arise when shorter
sampling periods, such as 30 minutes,
are employed by sorbent trap
monitoring systems. Although the
shorter sampling period is adequate to
provide information needed to optimize
the operation of Hg control technology,
we believe the reduced sampling period
results in a reduced quantity of
collected Hg which constrains the
sorbent trap monitoring system by a
minimum detection limit. For
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Fmt 4700
Sfmt 4700
additional information, see
‘‘Determination of Representative
Detection Level (RDL) and 3 X RDL
Values for Mercury Measured Using
Sorbent Trap Technologies’’ in
rulemaking docket EPA–HQ–OAR–
2009–0234. Specifically, we believe
detection level issues may arise from
using a sorbent trap when short
sampling periods (e.g., 30 minutes) are
used, and that, as such, the
UPL-calculated floor value should be
compared against the 3 X RDL value to
account for the shorter sampling
periods. We solicit comment on this
proposed revised approach in light of
the information provided by petitioners
regarding the need for prompt Hg
emissions information.
Our review of the data in the record
shows that for reasonable, shorter
sampling conditions—30-minute
samples obtained at a sampling rate of
0.5 liter per minute—the
UPL-determined new source Hg limit is
less than the 3 X RDL value. Therefore,
we are proposing to set the Hg limit for
the non-low rank virgin coal
subcategory at the 3 X RDL value.
Although the value of the resulting
limit we are proposing today is higher
than that in the final rule, we do not
expect this change to alter the emission
control strategy of a new EGU, as both
emission limits result in Hg removal
efficiency in excess of 97 percent.
However, the proposed change will
improve EGU owners’ and operators’
ability to track emissions and take
preemptive actions to ensure
compliance. Based on information
provided by the petitioners, our
experience, and the National Institute of
Standards and Technology’s recently
confirmed capability to certify Hg
calibration gas generators down to 0.2
micrograms per cubic meter (mg/m3), the
proposed change in the Hg limit will
also allow the option of using a Hg
CEMS for process control and for
determining compliance.
Please refer to the memo ‘‘Data and
Procedure for Handling Below Detection
Level Data in Analyzing Various
Pollutant Emissions Databases for
MACT and RTR Emissions Limits’’
(docket entry EPA–HQ–OAR–2009–
0234–20062) for a discussion of the RDL
approach generally, and the memo
‘‘Determination of Representative
Detection Level (RDL) and 3 X RDL
Values for Mercury Measured Using
Sorbent Trap Technologies’’
(rulemaking docket EPA–HQ–OAR–
2009–0234) for a discussion of our
approach for establishing an RDL for Hg.
The proposed limit is presented in table
1 of this preamble.
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4. Limits for New IGCC EGUs—Use of
Permit Limits From Unconstructed
IGCC EGUs
We are granting reconsideration of the
finalized new source integrated
gasification combined cycle (IGCC)
limits. The EPA used the permit limits
from IGCC EGUs that are permitted but
not yet constructed as the basis for some
of the final new source IGCC emission
limits. Some petitioners asserted that
the EPA did not use this approach in the
notice of proposed rulemaking and that
they therefore were deprived of the
opportunity to comment on this
approach.
Although we indicated that we
considered establishing standards based
on IGCC permits at proposal, we are
granting reconsideration on the new
source IGCC limits so that the public
has an additional opportunity to
comment on the limits and the
approach.
Specifically, we request comment on
the proposed new source IGCC
standards, which are unchanged from
the final standards promulgated for
these units on February 16, 2012. These
proposed new source limits are
presented in tables 1 and 2 of this
preamble.
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5. Beyond-the-Floor Analysis
The MACT floor level of control for
new EGUs is based on the emission
control that is achieved in practice by
the best controlled similar source, as
determined by the Agency, of each HAP
for the different subcategories. After the
EPA establishes MACT floor levels,
CAA section 112(d)(2) requires the EPA
to consider whether more stringent
beyond-the-floor standards should be
established. Under that section, the
Agency must consider ‘‘the cost of
achieving such emission reduction, and
any non-air quality health and
environmental impacts and energy
requirements’’ before it may establish a
standard that is based on a beyond-thefloor level of control.
For most of the new source standards
addressed in this proposal, we have not
identified additional technologies or
HAP emission reduction approaches
that would achieve HAP reductions
greater than the new source floors for
the subcategories, other than multiple
controls in series (e.g., multiple
scrubbers in series or multiple PM
controls in series), which we consider to
be unreasonable from a cost perspective.
We are therefore proposing to adopt the
floor level of control for all but one of
these standards. We are proposing a
beyond-the-floor standard for HCl
emissions from coal-fired EGUs.
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Summaries of the EPA’s beyond-thefloor evaluations for the new source
standards addressed in this proposal are
provided below. Additional detail of
these analyses, including a discussion of
costs and non-air quality health and
environmental impacts, is provided in
the ‘‘MATS Reconsideration: Beyondthe-Floor Memorandum’’ available in
rulemaking docket EPA–HQ–OAR–
2009–0234. We request comment on all
aspects of our beyond-the-floor analysis.
Specifically, we solicit comment on
whether there are any control
technologies or HAP emission reduction
practices that have been demonstrated
to achieve HAP reductions at levels
lower than the standards proposed in
this notice consistently and in a costeffective manner. Comments should
include information on emissions,
pollutant control efficiencies,
operational reliability, current
demonstrated applications, and costs.
a. Beyond-the-floor analysis for PM
from coal-fired EGUs. It is commonly
accepted that a baghouse fabric filter
(FF) is the technology that provides the
best level of PM emission reduction for
coal-fired EGUs. Newly constructed
coal-fired EGUs will be expected to
install FFs to meet the new source
NESHAP PM limit that we are
proposing in this notice and the
applicable NSPS limit. We have
considered available options that would
allow a new source to achieve greater
emission reductions than those
achieved in practice by the best
controlled source. The EPA is aware
that some EGUs have installed
downstream secondary ‘‘polishing’’ PM
control devices to provide for
incremental PM reductions beyond
what is achieved by the primary PM
control device. However, those
‘‘polishing’’ PM control devices are
most often installed for one of two
purposes: (1) To augment the control of
an underperforming or undersized
primary control device or (2) to allow
for injection of activated carbon or other
powdered sorbent so that the fly ash and
the sorbent remain separated for
eventual storage, disposal, or re-use.
Given that a new coal-fired EGU would
have the opportunity to design the
primary PM control device to meet the
new source emission limit, we can see
no justification for including in the
design a secondary downstream
‘‘polishing’’ PM control device. Such a
device would add considerable cost to
the project, and the incremental costeffectiveness would not be reasonable.
See ‘‘MATS Reconsideration: Beyondthe-Floor Memorandum’’ in rulemaking
docket EPA–HQ–OAR–2009–0234.
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b. Beyond-the-floor analysis for Hg
from new coal-fired EGUs designed for
coal ≥ 8300 Btu/lb. The proposed new
source Hg emission limit for EGUs firing
non-low rank virgin coal is based on the
use of the 3 X RDL approach. As
explained above, there is concern that a
lower emission limit could not be
reliably measured with sufficient
frequency to allow consistent and
timely compliance. For this reason, we
are not proposing a limit based on a
beyond-the-floor level of control, and,
instead, we are proposing to establish
the standard at the MACT floor level.
c. Beyond-the-floor analysis for SO2
emissions from coal-fired EGUs. The
best performing source for SO2
emissions from a coal-fired EGU is a
circulating fluidized bed combustor
(CFB) with limestone injection for SO2
control and a downstream circulating
dry scrubber (CDS) for supplemental
SO2 control. Because the EGU already
employs a downstream ‘‘polishing’’ SO2
control device, we do not believe that
installation of an additional ‘‘polishing’’
control device would result in costeffective reduction (in $/ton of
incremental SO2 reduction) that would
justify setting a beyond-the-floor
emission limit. See ‘‘MATS
Reconsideration: Beyond-the-Floor
Memorandum’’ in rulemaking docket
EPA–HQ–OAR–2009–0234.
d. Beyond-the-floor analysis for PM
from solid oil-derived fuel-fired EGUs.
This analysis is very similar to that
which was presented earlier for PM
emissions from coal-fired EGUs. Given
that a new solid oil-derived fuel-fired
EGU would have the opportunity to
design the primary PM control device to
meet the new source emission limit, we
can see no justification for including in
the design a secondary downstream
‘‘polishing’’ PM control device. As with
the coal-fired source, such a device
would add considerable costs to the
project, and the incremental costeffectiveness would not be reasonable.
e. Beyond-the-floor analysis for SO2
from solid oil-derived fuel-fired EGUs.
The best performing source for SO2
emissions from solid oil-derived fuelfired EGUs is a CFB combustor with
limestone injection for SO2 control.
Additional SO2 control, beyond that
which is obtained by the best controlled
source, may be obtained by installing a
downstream SO2 control device such as
a spray drier absorber (SDA) or wet-flue
gas desulfurization (wet-FGD) scrubber
or, as was the case with the best
performing coal-fired unit, a CDS.
However, as stated earlier, we believe
that, in this case, the installation of
additional downstream ‘‘polishing’’
control technologies does not result in
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cost-effective control (in $/ton of
incremental SO2 reduction) that would
justify setting a beyond-the-floor
emission limit.
f. Beyond-the-floor analysis for PM
from continental liquid oil fuel-fired
EGUs. The proposed new source
filterable PM emission limit for
continental liquid oil-fired fuel is based
on an EGU which uses an electrostatic
precipitator (ESP). Distillate oil-fired
facilities do not need add-on PM
controls, as their emissions are
inherently low, and residual oil-fired
units cannot use FFs for PM control due
to concerns about bag contamination
and fire safety. ESPs are the best
filterable PM control technology for
liquid oil fuel-fired EGUs. Given that a
new continental liquid-oil fuel-fired
EGU would have the opportunity to
design the primary PM control device to
meet the new source emission limit, we
can see no justification for including in
the design a secondary downstream
‘‘polishing’’ PM control device. Such a
device would add considerable costs to
the project, and the incremental costeffectiveness would not be reasonable.
g. Beyond-the-floor analysis for HAP
emissions from IGCC EGUs. We have no
data upon which to assess whether or
not technologies exist that can provide
additional HAP control beyond the
proposed new source emission limits for
new IGCC units. Accordingly, we are
not proposing to establish beyond-thefloor emission limitations for these
pollutants for new IGCC units. We
request comment on whether the use of
any control technologies or practices
have been demonstrated to consistently
achieve in a cost-effective manner,
emission levels for similar sources that
are lower than those proposed for new
IGCC sources in this proposal.
Comments should include information
on emissions, pollutant control
efficiencies, operational reliability,
current demonstrated applications, and
costs.
h. Beyond-the-floor analysis for HCl
emissions from coal-fired EGUs. For
HCl, the EPA’s revised floor analysis for
coal units—discussed above—resulted
in a revised MACT floor of 2.0E–2
pound per megawatt-hour (lb/MWh).
We have estimated that a new coal-fired
EGU would need to remove HCl in the
range of 81.0 to 96.6 percent (depending
upon the initial chlorine (Cl) content of
the fuel) in order to meet this revised
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MACT floor level of control for HCl
emissions. We also note that it is
reasonable to expect that in most, if not
all, cases, advanced FGD control
technology (such as a wet-FGD scrubber
or a high efficiency SDA) would be
required as a result of other federal
requirements—specifically a prevention
of significant deterioration (PSD) best
available control technology (BACT)
analysis. More detailed discussion may
be found in the memo ‘‘MATS
Reconsideration: Control Technology
Needed to Meet New Source Limits’’
contained in rulemaking docket EPA–
HQ–OAR–2009–0234.
A high efficiency SDA is less costly
than a wet-FGD, and we think it likely
that some new sources will be able to
comply with PSD/BACT requirements
using that less expensive option.4 For
this reason, we believe that it is
reasonable to assume the minimum
level of performance for HCl control
from a new EGU will be equivalent to
that of a well-performing SDA for
purposes of the beyond-the-floor
analysis. We examined the level of HCl
control achieved by those EGUs from
the 2010 utility information collection
request (ICR) database that were
equipped with SDA and we determined
that those EGUs achieved HCl control in
a range of 90 to 98 percent (coal-tostack, depending on the coal Cl
content).5
We, therefore, are proposing to set a
beyond-the-floor HCl emission limit for
new coal-fired EGUs at 1.0E–2 lb/MWh.
We believe that a new EGU firing lower
Cl-content coal would need to achieve
a minimum of 90 percent control to
meet this proposed limit and that a new
EGU firing a higher Cl-content coal
would need to achieve a minimum of 98
4 New Source Review (NSR) permit requirements
include, among other things, the application of
BACT (best available control technology) under
PSD. BACT control technology determinations and
associated emission limit establishment involve
case-by-case analyses and, such analyses take into
account site-specific factors such as energy,
environmental and economic impacts. For that
reason, it is impossible to strictly predict the
outcome of such analyses. However, based on
recent BACT determinations for SO2 emissions from
coal-fired EGUs, it is reasonable to expect that in
most, if not all, cases, flue gas desulfurization
control technologies (such as wet-FGD scrubbers or
high efficiency spray drier absorbers) would be
required (see https://cfpub.epa.gov/RBLC/).
5 Note that the HCl emission levels achieved are
very similar for all EGUs. The difference observed
in level of control (percentage) is due to the
difference in chlorine levels seen in various coals.
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percent control to meet the limit. We
believe that this beyond-the-floor
emission limit is cost-effective because
it does not involve additional cost, as
we expect that any new unit will install
at least a high efficiency SDA to comply
with other CAA requirements.
We also considered a beyond-the-floor
emission limit by assuming installation
of a wet-FGD scrubber, which generally
achieves greater HCl reductions, but at
a greater cost, than a high efficiency
SDA. We understand that some new
coal-fired EGUs will likely be required
to install this type of advanced FGD
technology for SO2 control. However, if
the EGU is not required to install a wetFGD scrubber from the PSD BACT
determination for SO2, then the
additional costs beyond those for a high
efficiency SDA would be attributable to
the achievement of additional HCl
emission reductions, and the costeffectiveness would not be reasonable.
6. Proposed New Source Emission
Limits
For coal-fired EGUs, the final rule
regulates HCl as a surrogate for acid gas
HAP, with an alternative equivalent
standard for SO2 as a surrogate for acid
gas HAP for coal-fired EGUs with FGD
systems installed and operational;
filterable PM as a surrogate for nonmercury HAP metals, with total nonmercury HAP metals and individual
non-mercury HAP metals as alternative
equivalent standards; Hg; and organic
HAP. For oil-fired EGUs, the final rule
regulates HCl and HF; filterable PM as
a surrogate for total HAP metals, with
individual HAP metals as alternative
equivalent standards; and organic HAP.
The filterable PM, HCl, and Hg limits
that we are proposing to revise are
provided in table 1; the alternate limits
that we are proposing to revise are
provided in table 2. We are soliciting
comment on the revised new source
emission limits proposed in this action.6
6 Tables 1 and 2 in this preamble set forth the new
source limits the Agency is proposing to revise.
However, to comply with Federal Register
guidelines, ‘‘Table 1 to Subpart UUUUU of Part
63—Emission Limits for New or Reconstructed
EGUs’’ in the regulatory text includes all of the new
source limits, including the limits that are not
proposed to be revised and are not part of this
reconsideration action. The EPA is only accepting
comments on the new source limits that are set
forth in tables 1 and 2 of this preamble, which are
the limits that are the subject of this reconsideration
action.
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TABLE 1—PROPOSED EMISSION LIMITATIONS FOR NEW EGUS
Filterable particulate
matter
Subcategory
New—Unit not designed for low rank virgin coal ....................................
New—Unit designed for low rank virgin coal ..........................................
New—IGCC .............................................................................................
New—Solid oil-derived .............................................................................
New—Liquid oil—continental ...................................................................
9.0E–2
9.0E–2
7.0E–2
9.0E–2
3.0E–2
4.0E–1
lb/MWh ..........
lb/MWh ..........
lb/MWh b ........
lb/MWh c ........
lb/MWh ..........
lb/MWh ..........
Hydrogen chloride
Mercury
1.0E–2 lb/MWh a ........
1.0E–2 lb/MWh a ........
2.0E–3 lb/MWh d ........
3.0E–3 lb/GWh.
NR.
3.0E–3 lb/GWh.e
NR .............................
NR .............................
NR.
NR.
Note: lb/MWh = pounds pollutant per megawatt-hour electric output (gross).
lb/GWh = pounds pollutant per gigawatt-hour electric output (gross).
NR = limit not revised.
a Beyond-the-floor value.
b Duct burners on syngas; based on permit levels in comments received.
c Duct burners on natural gas; based on permit levels in comments received.
d Based on best-performing similar source.
e Based on permit levels in comments received.
TABLE 2—PROPOSED REVISED ALTERNATE EMISSION LIMITATIONS FOR NEW EGUS
Subcategory/pollutant
Coal-fired EGUs
IGCC a
SO2 ................................................
Total non-mercury metals ..............
Antimony, Sb .................................
Arsenic, As .....................................
Beryllium, Be ..................................
Cadmium, Cd .................................
Chromium, Cr .................................
Cobalt, Co ......................................
Lead, Pb ........................................
Mercury, Hg ...................................
Manganese, Mn .............................
Nickel, Ni ........................................
Selenium, Se .................................
1.0 lb/MWh ...................................
NR .................................................
NR .................................................
NR .................................................
NR .................................................
NR .................................................
NR .................................................
NR .................................................
3.0E–2 lb/GWh .............................
NA .................................................
NR .................................................
NR .................................................
5.0E–2 lb/GWh .............................
4.0E–1 lb/MWh b ...........................
4.0E–1 lb/GWh .............................
2.0E–2 lb/GWh .............................
2.0E–2 lb/GWh .............................
1.0E–3 lb/GWh .............................
2.0E–3 lb/GWh .............................
4.0E–2 lb/GWh .............................
4.0E–3 lb/GWh .............................
9.0E–3 lb/GWh .............................
NA .................................................
2.0E–2 lb/GWh .............................
7.0E–2 lb/GWh .............................
3.0E–1 lb/GWh .............................
Solid oil-derived
1.0 lb/MWh.
NR.
NR.
NR.
NR.
NR.
NR.
NR.
NR.
NR.
NR.
NR.
NR.
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NA = not applicable.
NR = limit not revised.
a Based on best-performing similar source unless otherwise noted.
b Based on DOE information.
7. Control Technologies To Meet
Proposed New Source Emission Limits
We have evaluated the levels of
control that would generally be needed
to meet the proposed emission limits for
new sources and have compared those
to the levels of control needed to meet
the new source emission limits in the
final MATS rule. We compared the level
of control needed by analyzing
requirements for a new hypothetical 500
MW facility. The comparison led us to
conclude that new EGUs would need to
be designed to use the same types of
emission control technologies to meet
the proposed new source limits as
would have been needed to meet the
final MATS new source limits. More
detailed discussion of this evaluation
may be found in the memo ‘‘MATS
Reconsideration: Control Technology
Needed to Meet New Source Limits’’
contained in rulemaking docket EPA–
HQ–OAR–2009–0234.
Nothing in the statute requires the
EPA to demonstrate that an existing
source is able to meet all of the new
source limits. Nevertheless, we note that
based on our review of the data EPA
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collected as part of the 2010 ICR
process, at least eight existing non-low
rank virgin coal-fired EGUs and one low
rank virgin coal-fired EGU have
reported short-term stack test data that
demonstrate that these EGUs have in
practice achieved the new source limits
proposed in this notice (considering all
of their submitted data). Furthermore,
for HCl (as well as the SO2 surrogate)
and filterable PM, the new source limits
proposed in this notice are consistent
with those in several permits for EGUs
that have not yet commenced
construction. For Hg, the new source
limits proposed in this notice are
consistent with the levels that a number
of control vendors have suggested in
their petitions for reconsideration are
achievable and capable of being
measured with an appropriate level of
accuracy.
8. Filterable PM Monitoring
We provided several monitoring
options for the filterable PM standard in
the final rule, including quarterly stack
testing, PM CEMS, and PM continuous
parameter monitoring system (PM
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CPMS) with annual testing. For many
reasons, including continued use of
already-installed instruments on some
EGUs, direct (as opposed to parametric)
measurement of the pollutant of
concern, and continuous feedback for
process control, we believe that many
EGU owners or operators will choose to
use PM CEMS to monitor the proposed
filterable PM limit.
We solicit comment on whether to
retain the quarterly stack testing
compliance option, as this option may
not be necessary because continuous,
direct measurement of filterable PM or
a correlated parameter is available and
likely to be used by most sources to
monitor compliance with the revised
standard.
With respect to the PM CPMS
compliance option for new EGUs, we
considered three approaches to establish
an operating limit based on emissions
testing. The first approach would allow
an EGU owner or operator to use the
highest parameter value obtained during
an individual emissions test when the
result of that individual test was below
the limit as the operating limit. The
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second approach would allow an EGU
owner or operator to use the average
parameter value obtained from all runs
pertaining to an individual emissions
test as the operating limit. The third
approach would allow an EGU owner or
operator whose PM emissions as
demonstrated during performance
testing do not exceed 75 percent of the
PM emissions limit to set his PM CPMS
operating limit by linearly scaling the
average operating value obtained during
all the runs to be equivalent to the value
at 75 percent of the limit; an EGU owner
or operator whose PM emissions as
demonstrated during performance
testing exceed 75 percent of the PM
emissions limit would establish his
operating limit as a 30-day rolling
average equal to the average PM CPMS
values recorded during performance
testing. Such an approach would
prevent unnecessary retests for EGUs
with low PM emissions. See ‘‘75 Percent
CPMS Operating Limit Approach—
MATS Reconsideration’’ in rulemaking
docket EPA–HQ–OAR–2009–0234.
Even though this rule proposes the
first approach, we solicit comments on
the appropriateness of any of the three
approaches to establish a PM CPMS
operating limit for new EGUs.
In addition, this rule proposes to
require emissions testing after each
exceedance of the operating limit for
new sources. This rule proposes a
number of consequences if the PM
monitoring parameter is exceeded. First,
the EGU owner or operator will have 48
hours to conduct an inspection of the
control device(s) and to take action to
restore the controls to proper operation,
if necessary, and 45 days to conduct a
Method 5 compliance test under the
same operating conditions to verify
ongoing compliance with the filterable
PM limit. Within 60 days, the EGU
owner or operator will have to complete
the emissions sampling, sample
analyses, and verification that the EGU
is in compliance with its emissions
limit, as well as having to determine an
operating limit based on the PM CPMS
data collected during the performance
test. The EGU owner or operator would
then compare the recalculated operating
limit with the existing operating limit
and, as appropriate, adjust the
numerical operating limit to reflect
compliance performance. Adjustments
could include applying the most
recently established value or combining
the data collected over multiple
performance tests to establish a more
representative value. The EGU owner or
operator would then apply the
reverified or adjusted operating limit
value from that time forward.
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Second, this rule proposes to limit the
number of exceedances of the sitespecific CPMS limit leading to followup performance tests in any 12 month
process operating period and that an
excess of this number be considered a
violation of the standard. This
presumption of violation could be
rebutted by the EGU owner or operator,
but would require more than a Method
5 test as a basis for the rebuttal (e.g.,
results of physical inspections would
also need to be included). This
additional information is necessary
since a Method 5 test could not be
conducted during or immediately
following the discovery of exceedances
and would not necessarily represent
conditions identical to those when the
exceedances occurred. The basis for this
part of the proposal is that the sitespecific CPMS operating limit reflects a
30-day average that should represent an
actual emissions level lower than the
three test run numerical emissions limit
since variability is mitigated over time.
Consequently, we believe that there
should be few, if any, exceedances from
the 30-day parametric limit and there is
a reasonable basis for presuming that
exceedances that lead to multiple
performance tests to represent poor
control device performance and to be a
violation of the standard. Therefore, this
rule proposes that PM CPMS
exceedances leading to more than four
required performance tests in a 12month process operating period is
presumed to be a violation of this
standard, subject to an EGU owner or
operator’s ability to rebut that
presumption about process and control
device operations in addition to the
Method 5 performance test results. We
solicit comment on this proposed
revised approach.
B. Eligibility To Be a New Source
The CAA section 112(a)(4) defines a
new source as a stationary source ‘‘the
construction or reconstruction of which
is commenced after the Administrator
first proposes regulations under this
section establishing an emissions
standard applicable to such source.’’
The EPA views the new source trigger
date (the date EPA ‘‘first proposes
regulations’’) to be the date EPA first
proposes standards under a particular
rulemaking record. (74 FR 21158). In
this case, EPA first proposed standards
for EGUs on May 3, 2011, and although
we are proposing revisions to certain
new source standards, the rulemaking
record remains the same. As such, we
are not proposing to revise the trigger
date for determining whether a source is
a new source. Any source which
commenced construction or
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reconstruction after May 3, 2011 is
subject to the new source standards.7
Furthermore, it is the EPA’s technical
judgment that new sources would need
to adopt the same or similar emissions
control strategies under the amended
standards as they would have under the
promulgated standards. The revised
standards remain stringent and can be
met, in our view, using the same or
similar control strategies as would have
been required to meet the standards in
the final rule.
C. Startup and Shutdown Provisions
The EPA received petitions asserting
that the public lacked an opportunity to
comment on the startup and shutdown
provisions in the final MATS.
Petitioners also assert that the
definitions of ‘‘startup’’ and
‘‘shutdown’’ in the final MATS and the
provisions for work practice standards
did not adequately address applicability
to certain types of units, fuels
considered ‘‘clean,’’ and operational
limitations for certain EGU types and/or
pollution control devices.
We proposed numerical standards for
startup and shutdown periods, and in
response to comments on the proposed
rule we changed those standards in the
final MATS to work practice standards.
Among other things, the work practice
standards required sources to combust
clean fuels during startup and shutdown
periods and required sources to engage
APCDs when coal or oil was fired in the
EGU. (See 77 FR 9380–83). We also
revised the definitions of ‘‘startup’’ and
‘‘shutdown’’ after considering
comments we received. Although we
revised these provisions in response to
comments, we are granting
reconsideration on this issue to provide
an opportunity for comment on the final
startup and shutdown standards and
those we have revised and propose
today. For further discussion of
petitioners’ concerns and these
proposed revisions, please refer to the
memo ‘‘Startup and shutdown
provisions’’ in rulemaking docket EPA–
HQ–OAR–2009–0234. Below we
summarize the startup and shutdown
revisions proposed today.
1. Definitions
We are proposing to revise the
definitions of startup and shutdown in
this reconsideration notice as set forth
in 40 CFR 63.10042. Petitioners asserted
that the final rule’s definitions of startup
and shutdown were not sufficiently
clear, should accommodate operation of
7 We are unaware of any new source that has
commenced construction or reconstruction since
May 3, 2011.
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cogeneration units, and did not
accurately reflect startup conditions for
all affected units, particularly
supercritical units. We have clarified
the definitions and added provisions
including useful thermal energy.8 We
believe that these changes address
petitioners’ concerns. For more
discussion, please refer to the memo
‘‘Startup and shutdown provisions’’ in
rulemaking docket EPA–HQ–OAR–
2009–0234.
2. Work Practice Standards
We are proposing several revisions to
the finalized work practice standards.
Petitioners asserted that the final rule’s
work practice standards should include
certain additional fuels as ‘‘clean fuels’’
and recognize operating limitations of
certain EGU types and APCDs.
Specifically, petitioners contend that
the list of clean fuels required for use
during startup in order to minimize
emissions should include synthetic
natural gas, syngas, and ultra-low sulfur
diesel (ULSD). The EPA has also been
informed since the final rule that
propane is used to startup some EGUs
and has been requested to consider it as
a clean fuel. Petitioners additionally
contend that the standards need to
recognize operating conditions for FBC
EGUs that inject limestone for acid gas
control, selective non-catalytic
reduction systems (SNCRs), selective
catalytic reduction systems (SCRs), and
other systems.
In this reconsideration notice, we are
proposing to add certain synthetic
natural gas, syngas, propane, and ULSD
to the list of clean fuels. We solicit
comment on our understanding of clean
fuels for startup and shutdown.
We are also proposing to require EGU
source owners and operators, when
firing coal, solid oil-derived fuel, or
residual oil in the EGU during startup
or shutdown, to vent emissions to the
main stack(s) and operate all control
devices necessary to meet the operating
standards that apply at all other times
under the final rule (with the exception
of limestone injection in FBC EGUs, dry
scrubbers, SNCRs, and SCRs). Owners
and operators of EGUs are responsible
for starting limestone injection in FBC
EGUs, dry scrubbers, SNCRs, and SCRs
as expeditiously as possible, but, in any
case, when necessary to comply with
other standards applicable to the source
that require operation of those control
devices.
Additionally, we are proposing to
revise the final rule’s work practice
requirements to recognize constraints of
certain EGUs and APCDs. The proposed
8 16
U.S.C. 796(18)(A) and 18 CFR 292.202(c).
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revised standards allow limestone
injection to start after appropriate
temperatures have been attained in FBC
EGUs that inject limestone for acid gas
control and allow SNCR, SCR, and dry
scrubber systems to start as soon as
technically feasible after the appropriate
temperature has been reached.
For more discussion of each of these
issues, please refer to the memo
‘‘Startup and shutdown provisions’’ in
rulemaking docket EPA–HQ–OAR–
2009–0234.
3. Treatment of IGCC EGU Syngas
The EPA understands that at an IGCC
EGU, syngas is generated in the gasifier
and combusted in the turbine. During
the startup and shutdown periods, some
or all of the syngas produced may not
be combusted in the turbine. We are
proposing two options for IGCC EGUs
for handling syngas not fired in the
combustion turbine: (1) syngas must be
flared, not vented or (2) syngas must be
routed to duct burners, which may need
to be installed, and the flue gas from the
duct burners must be routed to the heat
recovery steam generator. We are
soliciting comments on the need to flare
the unfired syngas, if it is more
appropriate to require routing of the
unfired syngas back into the system for
all IGCC EGUs, and on the costs of
adding duct burners, should they be
required.
We solicit comments on the proposed
revisions to the startup and shutdown
requirements set forth in this notice.
V. Discussion of Provisions Subject To
Reconsideration—Utility NSPS
Petitioners state that because the final
Utility NSPS rule contains a definition
of ‘‘natural gas’’ that was not included
in the proposed rule, they were not able
to comment on the definition. Further,
petitioners maintain that the definition
established in the final rule is not a
‘‘logical outgrowth’’ of the proposed
rule. Although the definition was
changed between proposal and final
based on public comment, we are reproposing the definition of natural gas
that was in the final Utility NSPS to
allow additional opportunity to
comment.
We are also proposing several
additional amendments so that
synthetic natural gas will receive similar
treatment as natural gas. We seek
comment on all aspects of these
additional amendments. First,
consistent with the NESHAP definition,
we are proposing to clarify the
definition of coal to include synthetic
natural gas derived from coal. As such,
we are also proposing to add synthetic
natural gas to the opacity exemption in
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paragraph 40 CFR 60.42Da(b)(2) since
facilities burning synthetic natural gas
would otherwise be subject to an
opacity standard. In addition, we are
also proposing to replace ‘‘natural gas’’
with ‘‘gaseous fuels’’ in 40 CFR
60.49Da(b) so facilities burning
desulfurized coal-derived synthetic
natural gas are not required to install an
SO2 CEMS. The proposed amendments
to the startup and shutdown
requirements in the NESHAP portion of
this proposal would also allow the use
of synthetic natural gas for the work
practice standards required for PM
emissions control during periods of
startup and shutdown.
Additional proposed amendments
include amending the definition of an
IGCC to be similar to the corresponding
NESHAP MATS definition. Potential
language is as follows:
Integrated gasification combined cycle
electric utility steam generating unit or IGCC
electric utility steam generating unit means
an electric utility combined cycle gas turbine
that burns a synthetic gas derived from coal
and/or solid oil-derived fuel for more than
10.0 percent of the average annual heat input
during any 3 consecutive calendar years or
for more than 15.0 percent of the annual heat
input during any one calendar year in a
combined-cycle gas turbine. No solid coal or
solid oil-derived fuel is directly burned in
the unit during operation.
We believe that this would address
the issue of IGCC facilities switching
applicability between the stationary
combustion turbine NSPS (40 CFR part
60, subpart KKKK) and the Utility
NSPS. However, we are specifically
requesting comment if it would be more
appropriate to maintain the existing
NSPS IGCC definition and add ‘‘startup
and commissioning, shutdown’’ as
suggested by one petitioner. Potential
language for the alternate definition is
as follows:
Integrated gasification combined cycle
electric utility steam generating unit or IGCC
electric utility steam generating unit means
an electric utility combined cycle gas turbine
that is designed to burn fuels containing 50
percent (by heat input) or more solid-derived
fuel not meeting the definition of natural gas.
The Administrator may waive the 50 percent
solid-derived fuel requirement during
periods of the gasification system
construction, startup and commissioning,
shutdown, or repair. No solid fuel is directly
burned in the unit during operation.
In addition, the rationale for the
filterable PM standard startup and
shutdown work practice provision
discussed in the NESHAP portion of
this notice also applies to the filterable
PM startup and shutdown standards in
the Utility NSPS. Therefore, we are
proposing to amend both the emissions
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rate calculation procedure and
monitoring requirements for PM to be
similar to the requirements specified in
the NESHAP for new facilities. Owners/
operators of EGUs subject to the Utility
NSPS would calculate the filterable PM
emissions rate as the average of the
measured hourly rates during the
applicable averaging period (instead of
as the sum of the emissions divided by
the sum of the output over the
applicable averaging period) and would
use either a PM CEMS, PM CPMS, or
quarterly performance testing to
demonstrate compliance with the
applicable standard.9
Finally, we are proposing to clarify
that owners/operators electing to use
PM CPMS to monitor PM emissions are
exempt from the requirement to install
a continuous opacity monitoring system
(COMS) and would be allowed to elect
to use alternate opacity monitoring
procedures currently allowed in the
Utility NSPS.
VI. Technical Corrections and
Clarifications
On April 19, 2012 (77 FR 23399), we
issued a technical corrections notice
addressing certain corrections to the
February 16, 2012 (77 FR 9304) MATS.
In this notice, we are proposing
several additional technical corrections.
These amendments are being proposed
to correct inaccuracies and other
inadvertent errors in the final rule and
to make the rule language consistent
with provisions addressed through this
reconsideration. We are soliciting
comment only on whether the proposed
changes provide the intended accuracy,
clarity and consistency. These proposed
technical changes are described in
tables 3 and 4 of this preamble. We
request comment on all of these
proposed changes.
TABLE 3—MISCELLANEOUS PROPOSED TECHNICAL CORRECTIONS TO 40 CFR PART 60, SUBPART DA
Section of subpart Da
Description of proposed correction
40 CFR 60.42Da(a) ..............
40 CFR 60.42Da(e)(1)(ii) .....
Correct the erroneous ‘‘0.030’’ to the correct ‘‘0.03.’’
Correct the erroneous conversion ‘‘13 ng/J (0.015 lb/MMBtu)’’ to the correct ‘‘6.4 ng/J (0.015 lb/MMBtu)’’ by
amending the regulatory text to specify that the requirements in 40 CFR 60.42Da(c) or (d), which includes two
additional alternative limits, are available compliance alternatives for modified facilities.
TABLE 4—MISCELLANEOUS PROPOSED TECHNICAL CORRECTIONS TO 40 CFR PART 63, SUBPART UUUUU
Section of subpart UUUUU
Description of proposed correction
40 CFR 63.9982(a) .............................................
40 CFR 63.9982(b) and (c) ................................
40 CFR 63.10005(d)(2)(ii) ..................................
Clarify the language to use the word ‘‘or’’ instead of ‘‘and.’’
Correct the discrepancy between 63.9982(b) and (c) and 63.9985(a).
Correct the typographical error by replacing the incorrect ‘‘corresponding’’ with the correct
‘‘corresponds.’’
Revise to clarify the determination and measurement of fuel moisture content.
40 CFR 63.10005(i)(4)(ii) and (i)(5) and add
63.10005(i)(6).
40 CFR 63.10006(c) ...........................................
Subpart
Correct the omission of solid oil-derived fuel- and coal-fired EGUs and IGCC EGUs and the
omission of section 10000(c).
Correct the omission of section 63.10023 from the list of sections to be followed in establishing
an operating limit.
Correct omission of the term ‘‘boiler operating’’ and clarify the term ‘‘Rti’’ in Equation 2a.
Correct omission of the term ‘‘system’’ and clarify the term ‘‘Rti’’ in Equation 3a.
Correct the typographical error to use the correct word ‘‘your’’ instead of ‘‘you.’’
Clarify the language to use the word ‘‘and’’ instead of ‘‘or’’ between the words ‘‘startup’’ and
‘‘shutdown.’’
Clarify the language to use the word ‘‘or’’ instead of ‘‘and’’ between the words ‘‘oil-fired’’ and
‘‘solid.’’
Clarify the affected-source language.
Change the period by which a Notification of Intent to conduct a performance test must be
submitted to conform to the General Provisions.
Revise the definition of ‘‘boiler operating day’’ to clarify that periods of startup or shutdown are
not included.
Correct the typographical error in the intended definition of ‘‘unit designed for coal ≥ 8,300 Btu/
lb subcategory’’ by replacing the erroneous ‘‘>’’ with the correct ‘‘≥.’’
Correct the typographical error in footnote 4 by replacing the erroneous ‘‘≥’’ with the correct
‘‘≤.’’
Clarify the applicability of the alternate 90-day average for Hg in item 1.
Revise item 3 in the table to clarify use of CMS for liquid oil-fired EGUs.
Correct the typographical error by replacing the incorrect citation to ‘‘§ 63.10005(g)’’ with the
correct ‘‘§ 63.9984(f).’’
Correct the typographical error by replacing the incorrect citation to ‘‘Table A–4’’ with the correct ‘‘Table A–2.’’
Correct the typographical error by replacing the erroneous ‘‘≥’’ with the correct ‘‘≤.’’
UUUUU
Correct the section number from the incorrect ‘‘5.3.4’’ to the correct ‘‘5.3.3.’’
40 CFR 63.10007(c) ...........................................
40
40
40
40
CFR
CFR
CFR
CFR
63.10009(b)(2) ......................................
63.10009(b)(3) ......................................
63.10010(j)(1)(i) ....................................
63.10011(g) ...........................................
40 CFR 63.10030(b), (c), and (d) .......................
40 CFR Section 63.10042 ..................................
Table 5 to Subpart UUUUU of Part 63 ..............
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Table 7 to Subpart UUUUU of Part 63 ..............
Section 4.1 to Appendix A to Subpart
of Part 63.
Section 5.2.2.2 to Appendix A to
UUUUU of Part 63.
Section 3.1.2.1.3 to Appendix B to
UUUUU of Part 63.
Section 5.3.4 to Appendix B to Subpart
of Part 63.
UUUUU
Subpart
9 As discussed in the final Utility NSPS Response
to Comments document, because the amended NOX
and SO2 standards used CEMS data and included
all periods of operation when establishing the
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numerical values for those standards, we are not
proposing to amend how periods of startup and
shutdown are handled or how the emission rates
are calculated for the Utility NSPS NOX and SO2
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standards. See docket entry EPA–HQ–OAR–2011–
0044–5759, p. 7.
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VII. Impacts of This Proposed Rule
Summary of Emissions Impacts, Costs
and Benefits
Our analysis shows that new EGUs
would choose to install and operate the
same or similar air pollution control
technologies in order to meet the
revised emission limits as would have
been necessary to meet the previously
finalized standards. We project that this
rule will result in no significant change
in costs, emission reductions, or
benefits.10 Even if there were changes in
costs for these units, such changes
would likely be small relative to both
the overall costs of the individual
projects and the overall costs and
benefits of the final rule, which is
dominated by actions taken by existing
units. Further, as noted elsewhere in
this preamble, we believe that EGUs
would put on the same controls for this
proposed rule that they would have for
the original final, so there should not be
any incremental costs related to this
proposed revision.
A. What are the air impacts?
We believe that electric power
companies will install the same or
similar control technologies to comply
with the revised standards proposed in
this action as they would have installed
to comply with the previously finalized
standards. Accordingly, we believe that
this proposed rule will not result in
significant changes in emissions of any
of the regulated pollutants.
B. What are the energy impacts?
This proposed rule is not anticipated
to have an effect on the supply,
distribution, or use of energy. As
previously stated, we believe that
electric power companies would install
the same or similar control technologies
as they would have installed to comply
with the previously finalized standards.
C. What are the compliance costs?
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We believe there will be no significant
change in compliance costs as a result
of this proposed rule because electric
power companies would install the
same or similar control technologies as
they would have installed to comply
with the previously finalized standards.
10 See ‘‘Regulatory Impact Analysis for the Final
Mercury and Air Toxics Standards [EPA–452/R–11–
011]’’ (docket entry EPA–HQ–OAR–2009–0234–
20131) and the memo ‘‘Economic Impact Analysis
for the Proposed Reconsideration of the Mercury
and Air Toxics Standards’’ in rulemaking docket
EPA–HQ–OAR–2009–0234. As noted earlier,
because, on an individual EGU-by-EGU basis we
anticipate very similar costs, any changes to the
baseline since we finalized MATS (e.g., potential
impacts of the CSAPR decision) would not impact
this determination.
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Moreover, we find no additional
monitoring costs are necessary to
comply with the proposed rule;
however, as in any other rule, EGU
owners or operators may choose to
conduct additional monitoring (and
incur its expense) for their own
purposes.
units would choose to install the same
control technology in order to meet the
revised emission limits as would have
been necessary to meet the previously
finalized standard, we project that this
rule will result in no significant change
in costs, emission reductions, or
benefits.
D. What are the economic and
employment impacts?
B. Paperwork Reduction Act
This action does not impose any new
information collection burden. Today’s
notice of reconsideration does not
change the information collection
requirements previously finalized and,
as a result, does not impose any
additional burden on industry.
However, OMB has previously approved
the information collection requirements
contained in the existing regulations
(see 77FR 9304) under the provisions of
the Paperwork Reduction Act, 44 U.S.C.
3501 et seq. and has assigned OMB
control number 2060–0567). The OMB
control numbers for EPA’s regulations
are listed in 40 CFR part 9 and 48 CFR
chapter 15.
Because we expect that electric power
companies would install the same or
similar control technologies to meet the
standards proposed in this action as
they would have chosen to comply with
the previously finalized standards, we
do not anticipate that this proposed rule
will result in significant changes in
emissions, energy impacts, costs,
benefits, or economic impacts. Likewise,
we believe this rule will not have any
impacts on the price of electricity,
employment or labor markets, or the
U.S. economy.
E. What are the benefits of the proposed
standards?
As previously stated, the EPA
anticipates the power sector will not
incur significant compliance costs or
savings as a result of this proposal and
we do not anticipate any significant
emission changes resulting from this
rule. Therefore, there are no direct
monetized benefits or disbenefits
associated with this proposed rule.
VIII. Statutory and Executive Order
Reviews
A. Executive Order 12866: Regulatory
Planning and Review and Executive
Order 13563: Improving Regulation and
Regulatory Review
Under Executive Order (E.O.) 12866
(58 FR 51735, October 4, 1993), this
action is a ‘‘significant regulatory
action’’ because it ‘‘raises novel legal or
policy issues arising out of legal
mandates.’’ Accordingly, the EPA
submitted this action to the Office of
Management and Budget (OMB) for
review under Executive Orders 12866
and 13563 (76 FR 3821, January 21,
2011) and any changes made in
response to OMB recommendations
have been documented in the docket for
this action.
In addition, the EPA prepared an
analysis of the potential costs and
benefits associated with this action.
This analysis is contained in the
‘‘Economic Impact Analysis for the
Proposed Reconsideration of the
Mercury and Air Toxics Standards’’
found in rulemaking docket EPA–HQ–
OAR–2009–0234. Because our analysis
shows that new electricity generating
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C. Regulatory Flexibility Act
The Regulatory Flexibility Act
generally requires an agency to prepare
a regulatory flexibility analysis of any
rule subject to notice and comment
rulemaking requirements under the
Administrative Procedure Act or any
other statute unless the agency certifies
that the rule will not have a significant
economic impact on a substantial
number of small entities. Small entities
include small businesses, small not-forprofit enterprises, and small
governmental jurisdictions.
For purposes of assessing the impacts
of today’s notice of reconsideration on
small entities, a small entity is defined
as: (1) A small business as defined by
the Small Business Administration’s
(SBA) regulations at 13 CFR 121.201; (2)
a small governmental jurisdiction that is
a government of a city, county, town,
school district, or special district with a
population of less that 50,000; and (3)
a small organization that is any not-forprofit enterprise which is independently
owned and operated and is not
dominant in its field. Categories and
entities potentially regulated by the
final rule with applicable NAICS codes
are provided in the Supplementary
Information section of this action.
According to the SBA size standards
for NAICS code 221122 Utilities-Fossil
Fuel Electric Power Generation, a firm
is small if, including its affiliates, it is
primarily engaged in the generation,
transmission, and or distribution of
electric energy for sale and its total
electric output for the preceding fiscal
year did not exceed 4 million MWh.
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After considering the economic
impacts of today’s notice of
reconsideration on small entities, I
certify that the notice will not have a
significant economic impact on a
substantial number of small entities.
The EPA has determined that none of
the small entities will experience a
significant impact because the notice of
reconsideration imposes no additional
regulatory requirements on owners or
operators of affected sources. We have
therefore concluded that today’s notice
of reconsideration will not result in a
significant economic impact on a
substantial number of small entities. We
continue to be interested in the
potential impacts of the rule on small
entities and welcome comments on
issues related to such impacts.
D. Unfunded Mandates Reform Act
This action contains no Federal
mandates under the provisions of Title
II of the Unfunded Mandates Reform
Act of 1995 (UMRA), 2 U.S.C. 1531–
1538 for State, local, or tribal
governments or the private sector. The
action imposes no enforceable duty on
any state, local, or tribal governments or
the private sector. Therefore, this action
is not subject to the requirements of
UMRA sections 202 or 205.
This action is also not subject to the
requirements of UMRA section 203
because it contains no regulatory
requirements that might significantly or
uniquely affect small governments
because it contains no requirements that
apply to such governments or impose
obligations upon them.
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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, as specified in EO
13132. None of the affected facilities are
owned or operated by state
governments, and the requirements
discussed in today’s notice will not
supersede state regulations that are
more stringent. Thus, EO 13132 does
not apply to today’s notice of
reconsideration.
In the spirit of EO 13132, and
consistent with EPA policy to promote
communications between EPA and state
and local governments, EPA specifically
solicits comment on this notice of
reconsideration from state and local
officials.
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F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
This action does not have tribal
implications. It will not have substantial
direct effects on tribal governments, on
the relationship between the Federal
government and Indian tribes, or on the
distribution of power and
responsibilities between the Federal
government and Indian tribes, as
specified in EO 13175. No affected
facilities are owned or operated by
Indian tribal governments. Thus, EO
13175 does not apply to today’s notice
of reconsideration. The EPA specifically
solicits comment on this notice of
reconsideration from tribal officials.
G. Executive Order 13045: Protection of
Children From Environmental Health
Risks and Safety Risks
This action is not subject to EO 13045
(62 FR 19885, April 23, 1997) because
it is not economically significant as
defined in EO 12866. The EPA has
evaluated the environmental health or
safety effects of the final Mercury and
Air Toxics Standards on children. The
results of the evaluation are discussed
in that final rule (77 FR 9304; February
16, 2012) and are contained in
rulemaking docket EPA–HQ–OAR–
2009–0234.
The public is invited to submit
comments or identify peer-reviewed
studies and data that assess effects of
early life exposure to hazardous air
pollutants.
H. Executive Order 13211: Actions That
Significantly Affect Energy Supply,
Distribution, or Use
This action is not a ‘‘significant
energy action’’ as defined in EO 13211
(66 FR 28355; May 22, 2001) because it
is not likely to have a significant
adverse effect on the supply,
distribution, or use of energy. Further,
we conclude that today’s notice of
reconsideration is not likely to have any
adverse energy effects because it is not
expected to impose any additional
regulatory requirements on the owners
of affected facilities.
I. National Technology Transfer and
Advancement Act
Section 12(d) of the National
Technology Transfer and Advancement
Act (NTTAA) of 1995 (Pub. L. 104–113;
15 U.S.C. 272 note) directs EPA to use
voluntary consensus standards in their
regulatory and procurement activities
unless to do so would be inconsistent
with applicable law or otherwise
impracticable. Voluntary consensus
standards are technical standards (e.g.,
material specifications, test methods,
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sampling procedures, business
practices) developed or adopted by one
or more voluntary consensus bodies.
The NTTAA requires EPA to provide
Congress, through the OMB, with
explanations when EPA decides not to
use available and applicable voluntary
consensus standards.
During the development of the final
rule, EPA searched for voluntary
consensus standards that might be
applicable. The search identified three
voluntary consensus standards that
were considered practical alternatives to
the specified EPA test methods. An
assessment of these and other voluntary
consensus standards is presented in the
preamble to the final rule (77 FR 9441;
February 16, 2012). Today’s notice of
reconsideration does not propose the
use of any additional technical
standards beyond those cited in the
final rule. Therefore, EPA is not
considering the use of any additional
voluntary consensus standards for this
notice.
The EPA welcomes comments on this
aspect of this notice of reconsideration
and, specifically, invites the public to
identify potentially-applicable
voluntary consensus standards and to
explain why such standards should be
used in this regulation.
J. Executive Order 12898: Federal
Actions To Address Environmental
Justice in Minority Populations and
Low-Income Populations
Executive Order 12898 (59 FR 7629
(Feb. 16, 1994)) establishes federal
executive policy on environmental
justice. Its main provision directs
federal agencies, to the greatest extent
practicable and permitted by law, to
make environmental justice part of their
mission by identifying and addressing,
as appropriate, disproportionately high
and adverse human health or
environmental effects of their programs,
policies, and activities on minority
populations and low-income
populations in the United States.
The EPA has determined that this
notice of reconsideration will not have
disproportionately high and adverse
human health or environmental effects
on minority or low-income populations
because it does not affect the level of
protection provided to human health or
the environment. Our analysis shows
that new EGUs would choose to install
the same control technology in order to
meet the revised emission limits as
would have been necessary to meet the
previously finalized standard. Under the
relevant assumptions, we project that
this rule will result in no significant
change in emission reductions.
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List of Subjects in 40 CFR Parts 60 and
63
Environmental protection,
Administrative practice and procedure,
Air pollution control, Hazardous
substances, Intergovernmental relations,
Reporting and recordkeeping
requirements.
Dated: November 16, 2012.
Lisa P. Jackson,
Administrator.
For the reasons discussed in the
preamble, the EPA proposes to amend
40 CFR parts 60 and 63 to read as
follows:
PART 60—STANDARDS OF
PERFORMANCE FOR NEW
STATIONARY SOURCES
§ 60.42Da
(PM).
1. The authority citation for part 60
continues to read as follows:
■
Authority: 42 U.S.C. 7401 et seq.
2. Amend § 60.41Da by revising the
definitions of ‘‘coal’’ and ‘‘integrated
gasification combined cycle electric
utility steam generating unit,’’ and by
adding the definition of ‘‘natural gas’’ in
alphabetical order to read as follows:
■
§ 60.41Da
Definitions.
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Coal means all solid fuels classified as
anthracite, bituminous, subbituminous,
or lignite by the American Society of
Testing and Materials in ASTM D388
(incorporated by reference, see § 60.17)
and coal refuse. Synthetic fuels derived
from coal for the purpose of creating
useful heat, including but not limited to
solvent-refined coal, gasified coal, coaloil mixtures, and coal-water mixtures
are included in this definition for the
purposes of this subpart.
*
*
*
*
*
Integrated gasification combined
cycle electric utility steam generating
unit or IGCC electric utility steam
generating unit means an electric utility
combined cycle gas turbine that burns a
synthetic natural gas derived from coal
and/or solid oil-derived fuel for more
than 10.0 percent of the average annual
heat input during any 3 consecutive
calendar years or for more than 15.0
percent of the annual heat input during
any one calendar year in a combinedcycle gas turbine. No solid coal or solid
oil-derived fuel is directly burned in the
unit during operation.
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*
*
Natural gas means a fluid mixture of
hydrocarbons (e.g., methane, ethane, or
propane), composed of at least 70
percent methane by volume or that has
a gross calorific value between 35 and
41 megajoules (MJ) per dry standard
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cubic meter (950 and 1,100 Btu per dry
standard cubic foot), that maintains a
gaseous state under ISO conditions. In
addition, natural gas contains 20.0
grains or less of total sulfur per 100
standard cubic feet. Finally, natural gas
does not include the following gaseous
fuels: landfill gas, digester gas, refinery
gas, sour gas, blast furnace gas, coalderived gas, producer gas, coke oven
gas, or any gaseous fuel produced in a
process which might result in highly
variable sulfur content or heating value.
*
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*
■ 3. Amend § 60.42Da by revising
paragraphs (a), (b)(2), (e)(1) introductory
text, and (e)(1)(ii) to read as follows:
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Standards for particulate matter
(a) Except as provided in paragraph (f)
of this section, on and after the date on
which the initial performance test is
completed or required to be completed
under § 60.8, whichever date comes
first, an owner or operator of an affected
facility shall not cause to be discharged
into the atmosphere from any affected
facility for which construction,
reconstruction, or modification
commenced before March 1, 2005, any
gases that contain PM in excess of 13
ng/J (0.03 lb/MMBtu) heat input.
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*
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*
(b) * * *
(2) An owner or operator of an
affected facility that combusts only
natural gas and/or synthetic natural gas
that chemically meets the definition of
natural gas is exempt from the opacity
standard specified in paragraph (b) of
this section.
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*
(e) * * *
(1) On and after the date on which the
initial performance test is completed or
required to be completed under § 60.8,
whichever date comes first, the owner
or operator shall cause to be discharged
into the atmosphere from that affected
facility any gases that contain PM in
excess of the applicable emissions limit
specified in paragraphs (e)(1)(i) or (ii) of
this section.
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*
*
*
(ii) For an affected facility which
commenced modification, any gases that
contain PM in excess of the emission
limits specified in paragraphs (c) or (d)
of this section.
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*
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■ 4. Amend § 60.48Da by revising
paragraphs (a), (f), (o) introductory text,
(o)(1), (o)(2) introductory text, (o)(3)
introductory text, (o)(3)(i), and (o)(4)
introductory text to read as follows:
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§ 60.48Da
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Compliance provisions.
(a) For affected facilities for which
construction, modification, or
reconstruction commenced before May
4, 2011, the applicable PM emissions
limit and opacity standard under
§ 60.42Da, SO2 emissions limit under
§ 60.43Da, and NOX emissions limit
under § 60.44Da apply at all times
except during periods of startup,
shutdown, or malfunction. For affected
facilities for which construction,
modification, or reconstruction
commenced after May 3, 2011, the
applicable SO2 emissions limit under
§ 60.43Da, NOX emissions limit under
§ 60.44Da, and NOX plus CO emissions
limit under § 60.45Da apply at all times.
The applicable PM emissions limit and
opacity standard under § 60.42Da apply
at all times except during periods of
startup and shutdown; however, you are
required to meet the work practice
requirements as specified in
60.42Da(e)(2) of this subpart during
periods of startup and shutdown.
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*
*
(f) For affected facilities for which
construction, modification, or
reconstruction commenced before May
4, 2011, compliance with the applicable
daily average PM emissions limit is
determined by calculating the
arithmetic average of all hourly
emission rates each boiler operating
day, except for data obtained during
startup, shutdown, or malfunction
periods. Daily averages are only
calculated for boiler operating days that
have non-out-of-control data for at least
18 hours of unit operation during which
the standard applies. Instead, all of the
non-out-of-control hourly emission rates
of the operating day(s) not meeting the
minimum 18 hours non-out-of-control
data daily average requirement are
averaged with all of the non-out-ofcontrol hourly emission rates of the next
boiler operating day with 18 hours or
more of non-out-of-control PM CEMS
data to determine compliance. For
affected facilities for which
construction, modification, or
reconstruction commenced after May 3,
2011, compliance with the applicable
30-boiler operating day rolling average
PM emissions limit is determined by
calculating the arithmetic average of all
hourly PM emission rates for the 30
successive boiler operating days, except
for data obtained during periods of
startup or shutdown.
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(o) Compliance provisions for sources
subject to § 60.42Da(c)(2), (d), or
(e)(1)(ii). Except as provided for in
paragraph (p) of this section, the owner
or operator shall demonstrate
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compliance with each applicable
emissions limit according to the
requirements in paragraphs (o)(1)
through (o)(5) of this section.
(1) You must conduct a performance
test to demonstrate initial compliance
with the applicable PM emissions limit
in § 60.42Da by the applicable date
specified in § 60.8(a). Thereafter, you
must conduct each subsequent
performance test within 12 calendar
months following the date the previous
performance test was required to be
conducted. You must conduct each
performance test according to the
requirements in § 60.8 using the test
methods and procedures in § 60.50Da.
The owner or operator of an affected
facility that has not operated for 60
consecutive calendar days prior to the
date that the subsequent performance
test would have been required had the
unit been operating is not required to
perform the subsequent performance
test until 30 calendar days after the next
boiler operating day. Requests for
additional 30 day extensions shall be
granted by the relevant air division or
office director of the appropriate
Regional Office of the U.S. EPA.
(2) You must monitor the performance
of each electrostatic precipitator or
fabric filter (baghouse) operated to
comply with the applicable PM
emissions limit in § 60.42Da using a
continuous opacity monitoring system
(COMS) according to the requirements
in paragraphs (o)(2)(i) through (vi)
unless you elect to comply with one of
the alternatives provided in paragraphs
(o)(3) and (o)(4) of this section, as
applicable to your control device.
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*
(3) As an alternative to complying
with the requirements of paragraph
(o)(2) of this section, an owner or
operator may elect to monitor the
performance of an electrostatic
precipitator (ESP) operated to comply
with the applicable PM emissions limit
in § 60.42Da using an ESP predictive
model developed in accordance with
the requirements in paragraphs (o)(3)(i)
through (v) of this section.
(i) You must calibrate the ESP
predictive model with each PM control
device used to comply with the
applicable PM emissions limit in
§ 60.42Da operating under normal
conditions. In cases when a wet
scrubber is used in combination with an
ESP to comply with the PM emissions
limit, the wet scrubber must be
maintained and operated.
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(4) As an alternative to complying
with the requirements of paragraph
(o)(2) of this section, an owner or
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operator may elect to monitor the
performance of a fabric filter (baghouse)
operated to comply with the applicable
PM emissions limit in § 60.42Da by
using a bag leak detection system
according to the requirements in
paragraphs (o)(4)(i) through (v) of this
section.
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■ 5. Amend § 60.49Da by:
■ a. Revising paragraphs (a)
introductory text and (a)(2);
■ b. Adding paragraphs (a)(2)(v) and
(a)(3)(iv); and
■ c. Revising paragraphs (a)(4)
introductory text, (b) introductory text,
and (t).
The revised and added text reads as
follows:
§ 60.49Da
Emission monitoring.
(a) An owner or operator of an
affected facility subject to the opacity
standard in § 60.42Da shall monitor the
opacity of emissions discharged from
the affected facility to the atmosphere
according to the applicable
requirements in paragraphs (a)(1)
through (4) of this section.
*
*
*
*
*
(2) As an alternative to the monitoring
requirements in paragraph (a)(1) of this
section, an owner or operator of an
affected facility that meets the
conditions in either paragraph (a)(2)(i),
(ii), (iii), (iv), or (v) of this section may
elect to monitor opacity as specified in
paragraph (a)(3) of this section.
*
*
*
*
*
(v) The owner or operator of the
affected facility installs, calibrates,
operates, and maintains a particulate
matter continuous parametric
monitoring system (PM CPMS)
according to the requirements specified
in subpart UUUUU of part 63.
*
*
*
*
*
(3) * * *
(iv) If the maximum 6-minute opacity
is less than 10 percent during the most
recent Method 9 of appendix A–4 of this
part performance test, the owner or
operator may, as an alternative to
performing subsequent Method 9 of
appendix A–4 performance tests, elect
to perform subsequent monitoring using
a digital opacity compliance system
according to a site-specific monitoring
plan approved by the Administrator.
The observations shall be similar, but
not necessarily identical, to the
requirements in paragraph (a)(3)(iii) of
this section. For reference purposes in
preparing the monitoring plan, see
OAQPS ‘‘Determination of Visible
Emission Opacity from Stationary
Sources Using Computer-Based
Photographic Analysis Systems.’’ This
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document is available from the U.S.
Environmental Protection Agency (U.S.
EPA); Office of Air Quality and
Planning Standards; Sector Policies and
Programs Division; Measurement Policy
Group (D243–02), Research Triangle
Park, NC 27711. This document is also
available on the Technology Transfer
Network (TTN) under Emission
Measurement Center Preliminary
Methods.
*
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*
(4) An owner or operator of an
affected facility that is subject to an
opacity standard under § 60.42Da is not
required to operate a COMS provided
that the affected facility combusts only
gaseous and/or liquid fuels (excluding
residue oil) where the potential SO2
emissions rate of each fuel is no greater
than 26 ng/J (0.060 lb/MMBtu), and the
unit operates according to a written sitespecific monitoring plan approved by
the permitting authority. This
monitoring plan must include
procedures and criteria for establishing
and monitoring specific parameters for
the affected facility indicative of
compliance with the opacity standard.
For testing performed as part of this sitespecific monitoring plan, the permitting
authority may require as an alternative
to the notification and reporting
requirements specified in §§ 60.8 and
60.11 that the owner or operator submit
any exceedances with the excess
emissions report required under
§ 60.51Da(d).
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*
(b) The owner or operator of an
affected facility shall install, calibrate,
maintain, and operate a CEMS, and
record the output of the system, for
measuring SO2 emissions, except where
only gaseous and/or liquid fuels
(excluding residual oil) where the
potential SO2 emissions rate of each fuel
is 26 ng/J (0.060 lb/MMBtu) or less are
combusted, as follows:
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*
(t) The owner or operator of an
affected facility demonstrating
compliance with the output-based
emissions limit under § 60.42Da shall
either install, certify, operate, and
maintain a CEMS for measuring PM
emissions according to the requirements
of paragraph (v) of this section, install,
calibrate, operate, and maintain a PM
CPMS according to the requirements for
new facilities specified in subpart
UUUUU of part 63 of this chapter, or
conduct quarterly testing according to
the requirements for new facilities
specified in subpart UUUUU of part 63
of this chapter. An owner or operator of
an affected facility demonstrating
compliance with the input-based
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6. Revise § 60.50Da paragraph (f) to
read as follows:
■
§ 60.50Da Compliance determination
procedures and methods.
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(f) The owner or operator of an
electric utility combined cycle gas
turbines that does not meet the
definition of an IGCC shall conduct
performance tests for PM, SO2, and NOX
using the procedures of Method 19 of
appendix A–7 of this part. The SO2 and
NOX emission rates calculations from
the gas turbine used in Method 19 of
appendix A–7 of this part are
determined when the gas turbine is
performance tested under subpart GG of
this part. The potential uncontrolled PM
emission rate from a gas turbine is
defined as 17 ng/J (0.04 lb/MMBtu) heat
input.
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PART 63—NATIONAL EMISSION
STANDARDS FOR HAZARDOUS AIR
POLLUTANTS FOR SOURCE
CATEGORIES
7. The authority citation for 40 CFR
part 63 continues to read as follows:
■
Authority: 42 U.S.C. 7401, et seq.
8. In § 63.9982, revise paragraphs (a)
introductory text, (b), and (c) to read as
follows:
■
§ 63.9982 What is the affected source of
this subpart?
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(a) This subpart applies to each
individual or group of two or more new,
reconstructed, or existing affected
source(s) as described in paragraphs
(a)(1) and (2) of this section within a
contiguous area and under common
control.
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Where:
Heri = hourly emission rate (e.g., lb/MMBtu,
lb/MWh) from unit i’s CEMS for the
preceding 30-group boiler operating
days,
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(b) An EGU is new if you commence
construction of the coal- or oil-fired
EGU after May 3, 2011.
(c) An EGU is reconstructed if you
meet the reconstruction criteria as
defined in § 63.2, or if you commence
reconstruction after May 3, 2011.
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■ 9. In § 63.10005, revise paragraphs
(d)(2)(ii), (i)(4)(ii), and (i)(5) and add
paragraph (i)(6) to read as follows:
§ 63.10005 What are my initial compliance
requirements and by what date must I
conduct them?
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*
(d) * * *
(2) * * *
(ii) You must demonstrate continuous
compliance with the PM CPMS sitespecific operating limit that corresponds
to the results of the performance test
demonstrating compliance with the
emission limit with which you choose
to comply.
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*
*
(i) * * *
(4) * * *
(ii) ASTM D4006–11, ‘‘Standard Test
Method for Water in Crude Oil by
Distillation,’’ including Annex A1 and
Appendix A1.
(5) Use one of the following methods
to obtain fuel moisture samples:
(i) ASTM D4177–95 (Reapproved
2010), ‘‘Standard Practice for Automatic
Sampling of Petroleum and Petroleum
Products,’’ including Annexes A1
through A6 and Appendices X1 and X2,
or
(ii) ASTM D4057–06 (Reapproved
2011), ‘‘Standard Practice for Manual
Sampling of Petroleum and Petroleum
Products,’’ including Annex A1.
(6) Should the moisture in your liquid
fuel be more than 1.0 percent by weight,
you must
(i) Conduct HCl and HF emissions
testing quarterly (and monitor sitespecific operating parameters as
provided in § 63.10000(c)(2)(iii) or
(ii) Use an HCl CEMS and/or HF
CEMS.
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*
*
*
Rmi = hourly heat input or gross electrical
output from unit i for the preceding 30group boiler operating days,
p = number of EGUs in emissions averaging
group that rely on CEMS or sorbent trap
monitoring,
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10. In § 63.10006, revise paragraph (c)
to read as follows:
■
§ 63.10006 When must I conduct
subsequent performance tests or tune-ups?
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(c) Except where paragraphs (a) or (b)
of this section apply, or where you
install, certify, and operate a PM CEMS
to demonstrate compliance with a
filterable PM emissions limit, for liquid
oil-, solid oil-derived fuel-, and coalfired EGUs and IGCC EGUs, you must
conduct all applicable periodic
emissions tests for filterable PM, or
individual or total HAP metals
emissions according to Table 5 to this
subpart, § 63.10007, and § 63.10000(c),
except as otherwise provided in
§ 63.10021(d)(1).
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■ 11. In § 63.10007, revise paragraph (c)
to read as follows:
§ 63.10007 What methods and other
procedures must I use for the performance
tests?
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*
(c) If you choose to comply with the
filterable PM emission limit and
demonstrate continuous performance
using a PM CPMS for an applicable
emission limit as provided for in
§ 63.10000(c), you must also establish
an operating limit according to
§ 63.10011(b), § 63.10023, and Tables 4
and 6 to this subpart. Should you desire
to have operating limits that correspond
to loads other than maximum normal
operating load, you must conduct
testing at those other loads to determine
the additional operating limits.
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*
■ 12. In § 63.10009, revise paragraphs
(b)(2) and (b)(3) to read as follows:
§ 63.10009 May I use emissions averaging
to comply with this subpart?
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*
(b) * * *
(2) Weighted 30-boiler operating day
rolling average emissions rate equations
for pollutants other than Hg. Use
equation 2a or 2b to calculate the 30 day
rolling average emissions daily.
n = number of hourly rates collected over 30group boiler operating days,
Teri = Emissions rate from most recent
emissions test of unit i in terms of lb/
heat input or lb/gross electrical output,
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emissions limit in § 60.42Da may install,
certify, operate, and maintain a CEMS
for measuring PM emissions according
to the requirements of paragraph (v) of
this section.
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m = number of EGUs in emissions averaging
group that rely on emissions testing.
Where:
variables with similar names share the
descriptions for Equation 2a,
Smi = steam generation in units of pounds
from unit i that uses CEMS for the
preceding 30-group boiler operating
days,
Cfmi = conversion factor, calculated from the
most recent compliance test results, in
units of heat input per pound of steam
generated or gross electrical output per
pound of steam generated, from unit i
that uses CEMS from the preceding 30
group boiler operating days,
Sti = steam generation in units of pounds
from unit i that uses emissions testing,
and
Cfti = conversion factor, calculated from the
most recent compliance test results, in
units of heat input per pound of steam
generated or gross electrical output per
(3) Weighted 90-boiler operating day
rolling average emissions rate equations
for Hg emissions from EGUs in the
‘‘coal-fired unit not low rank virgin
coal’’ subcategory. Use equation 3a or 3b
to calculate the 90-day rolling average
emissions daily.
Where:
Heri = hourly emission rate from unit i’s
CEMS or Hg sorbent trap monitoring
system for the preceding 90-group boiler
operating days,
Rmi = hourly heat input or gross electrical
output from unit i for the preceding 90group boiler operating days,
p = number of EGUs in emissions averaging
group that rely on CEMS,
n = number of hourly rates collected over the
90-group boiler operating days,
Teri = Emissions rate from most recent
emissions test of unit i in terms of lb/
heat input or lb/gross electrical output,
Rti = Total heat input or gross electrical
output of unit i for the preceding 90boiler operating days, and
m = number of EGUs in emissions averaging
group that rely on emissions testing.
Where:
variables with similar names share the
descriptions for Equation 2a,
Smi = steam generation in units of pounds
from unit i that uses CEMS or a Hg
sorbent trap monitoring for the preceding
90-group boiler operating days,
Cfmi = conversion factor, calculated from the
most recent compliance test results, in
units of heat input per pound of steam
generated or gross electrical output per
pound of steam generated, from unit i
that uses CEMS or sorbent trap
monitoring from the preceding 90-group
boiler operating days,
Sti = steam generation in units of pounds
from unit i that uses emissions testing,
and
Cfti = conversion factor, calculated from the
most recent emissions test results, in
units of heat input per pound of steam
generated or gross electrical output per
pound of steam generated, from unit i
that uses emissions testing.
§ 63.10010 What are my monitoring,
installation, operation, and maintenance
requirements?
fuels: natural gas, synthetic natural gas,
propane, distillate oil, synthesis gas
(syngas), and ultra-low sulfur diesel
(ULSD).
(g) You must follow the startup and
shutdown requirements in Table 3 for
each coal-fired, liquid oil-fired, or solid
oil-derived fuel-fired EGU.
■ 15. Amend § 63.10021 by adding
paragraphs (c)(1) and (2) to read as
follows:
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13. In § 63.10010, revise paragraph
(j)(1)(i) to read as follows:
■
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(j) * * *
(1) * * *
(i) Install and certify your HAP metals
CEMS according to the procedures and
requirements in your approved sitespecific test plan as required in
§ 63.7(e). The reportable measurement
output from the HAP metals CEMS must
be expressed in units of the applicable
emissions limit (e.g., lb/MMBtu, lb/
MWh) and in the form of a 30-boiler
operating day rolling average.
*
*
*
*
*
■ 14. In § 63.10011, revise paragraphs (f)
and (g) to read as follows:
§ 63.10011 How do I demonstrate initial
compliance with the emissions limits and
work practice standards?
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*
(f) You must use during periods of
startup or shutdown any one or
combination of the following clean
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§ 63.10021 How do I demonstrate
continuous compliance with the emission
limitations, operating limits, and work
practice standards?
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(c) * * *
(1) For any exceedance of the 30boiler operating day PM CPMS average
value from the established operating
parameter limit for an EGU subject to
the emissions limits in Table 1 to this
subpart, you must:
(i) Within 48 hours of the exceedance,
visually inspect the air pollution control
device (APCD);
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pound of steam generated, from unit i
that uses emissions testing.
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(ii) If the inspection of the APCD
identifies the cause of the exceedance,
take corrective action as soon as
possible, and return the PM CPMS
measurement to within the established
value; and
(iii) Within 45 days of the exceedance
or at the time of the annual compliance
test, whichever comes first, conduct a
PM emissions compliance test to
determine compliance with the PM
emissions limit and to verify or reestablish the CPMS operating limit. You
are not required to conduct any
additional testing for any exceedances
that occur between the time of the
original exceedance and the PM
emissions compliance test required
under this paragraph.
(2) PM CPMS exceedances from the
operating limit for an EGU subject to the
emissions limits in Table 1 of this
subpart leading to more than four
required performance tests in a 12month period (rolling monthly)
constitute a separate violation of this
subpart.
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*
*
■ 16. In § 63.10023, revise paragraph (b)
to read as follows:
§ 63.10030 What notifications must I
submit and when?
*
*
*
*
*
(b) As specified in § 63.9(b)(2), if you
startup your EGU that is an affected
source before April 16, 2012, you must
submit an Initial Notification not later
than 120 days after April 16, 2012.
(c) As specified in § 63.9(b)(4) and
(b)(5), if you startup your new or
reconstructed EGU that is an affected
source on or after April 16, 2012, you
must submit an Initial Notification not
later than 15 days after the actual date
of startup of the EGU that is an affected
source.
(d) When you are required to conduct
a performance test, you must submit a
Notification of Intent to conduct a
performance test at least 60 days before
the performance test is scheduled to
begin.
*
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*
*
*
■ 18. Amend § 63.10042 by:
■ a. Revising the definitions of ‘‘Boiler
operating day,’’ ‘‘Shutdown’’, ‘‘Startup’’,
and ‘‘Unit designed for coal > 8,300 Btu/
lb subcategory’’; and
■ b. Adding, in alphabetical order, a
new definition of ‘‘Clean fuel’’.
The revised and added text reads as
follows:
§ 63.10023 How do I establish my PM
CPMS operating limit and determine
compliance with it?
§ 63.10042
subpart?
*
*
*
*
*
*
(b) Determine your operating limit as
provided in paragraph (b)(1) or (b)(2) of
this section. You must verify an existing
or establish a new operating limit after
each repeated performance test.
(1) For an existing EGU, determine
your operating limit based on the
highest 1-hour average PM CPMS output
value recorded during the performance
test.
(2) For a new EGU, determine your
operating limit based on the highest 1hour average PM CPMS output value
recorded during the performance test.
*
*
*
*
*
■ 17. In § 63.10030, revise paragraphs
(b), (c), and (d) to read as follows:
What definitions apply to this
*
*
*
*
Boiler operating day means a 24-hour
period that begins at midnight and ends
the following midnight during which
any fuel is combusted at any time in the
EGU, excluding periods of startup or
shutdown. It is not necessary for the
fuel to be combusted the entire 24-hour
period.
*
*
*
*
*
Clean fuel means natural gas,
synthetic natural gas that meets the
specification necessary for that gas to be
transported on a Federal Energy
Regulatory Commission (FERC)
regulated pipeline, propane, distillate
oil, synthesis gas (syngas), or ultra-lowsulfur diesel (ULSD).
*
*
*
*
*
1. Coal-fired unit not low rank virgin coal ......
wreier-aviles on DSK5TPTVN1PROD with
If your EGU is in this subcategory . . .
a. Filterable particulate
matter (PM).
OR
Total non-Hg HAP metals
OR
Individual HAP metals: .....
Antimony (Sb) ...........
Arsenic (As) ..............
Beryllium (Be) ...........
Cadmium (Cd) ..........
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Frm 00053
Shutdown means the period in which
cessation of operation of an EGU is
initiated for any purpose. Shutdown
begins when the EGU no longer
generates electricity or makes useful
thermal energy (such as heat or steam)
for industrial, commercial, heating, or
cooling purposes or when no coal,
liquid oil, syngas, or solid oil-derived
fuel is being fired in the EGU,
whichever is earlier. Shutdown ends
when the EGU no longer generates
electricity or makes useful thermal
energy (such as steam or heat) for
industrial, commercial, heating, or
cooling purposes, and no fuel is being
fired in the EGU.
Startup means the period in which
operation of an EGU is initiated for any
purpose. Startup begins with either the
first-ever firing of fuel in an EGU for the
purpose of producing electricity or
useful thermal energy (such as heat or
steam) for industrial, commercial,
heating, or cooling purposes or the
firing of fuel in an EGU for any purpose
after a shutdown event. Startup ends
when the EGU generates electricity that
is sold or used for any other purpose
(including on site use), or the EGU
makes useful thermal energy (such as
heat or steam) for industrial,
commercial, heating, or cooling
purposes (16 U.S.C. 796(18)(A) and 18
CFR 292.202(c)), whichever is earlier.
*
*
*
*
*
Unit designed for coal ≥ 8,300 Btu/lb
subcategory means any coal-fired EGU
that is not a coal-fired EGU in the ‘‘unit
designed for low rank virgin coal’’
subcategory.
*
*
*
*
*
19. Revise Table 1 to Subpart UUUUU
of Part 63 to read as follows:
■
Table 1 to Subpart UUUUU of Part 63—
Emission Limits for New or
Reconstructed EGUs
As stated in § 63.9991, you must
comply with the following applicable
emission limits:
You must meet the
following emission
limits and work
practice standards
. . .
For the following
pollutants . . .
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Fmt 4700
Using these requirements, as appropriate
(e.g., specified sampling volume or test run
duration) and limitations with the test
methods in Table 5 . . .
9.0E–2 lb/MWh 1 .......
Collect a minimum of 4 dscm per run.
OR
6.0E–2 lb/GWh .........
OR
...................................
8.0E–3 lb/GWh.
3.0E–3 lb/GWh.
6.0E–4 lb/GWh.
4.0E–4 lb/GWh.
Sfmt 4700
Collect a minimum of 4 dscm per run.
Collect a minimum of 3 dscm per run.
E:\FR\FM\30NOR1.SGM
30NOR1
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Federal Register / Vol. 77, No. 231 / Friday, November 30, 2012 / Rules and Regulations
For the following
pollutants . . .
Chromium (Cr) ..........
Cobalt (Co) ...............
Lead (Pb) ..................
Manganese (Mn) .......
Nickel (Ni) .................
Selenium (Se) ...........
b. Hydrogen chloride
(HCl).
2. Coal-fired units low rank virgin coal ...........
7.0E–3
2.0E–3
3.0E–2
4.0E–3
4.0E–2
5.0E–2
1.0E–2
OR
Sulfur dioxide (SO2) 3 .......
c. Mercury (Hg) ................
If your EGU is in this subcategory . . .
You must meet the
following emission
limits and work
practice standards
. . .
1.0 lb/MWh ................
3.0E–3 lb/GWh .........
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/MWh .........
9.0E–2 lb/MWh 1 .......
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1.0 lb/MWh ................
4.0E–2 lb/GWh .........
a. Filterable particulate
matter (PM).
OR
Total non-Hg HAP metals
OR
Individual HAP metals: .....
Antimony (Sb) ...........
Arsenic (As) ..............
Beryllium (Be) ...........
Cadmium (Cd) ..........
Chromium (Cr) ..........
Cobalt (Co) ...............
Lead (Pb) ..................
Manganese (Mn) .......
Nickel (Ni) .................
Selenium (Se) ...........
b. Hydrogen chloride
(HCl).
7.0E–2 lb/MWh 4 .......
9.0E–2 lb/MWh 5 .......
OR
4.0E–1 lb/GWh .........
OR
...................................
2.0E–2 lb/GWh.
2.0E–2 lb/GWh.
1.0E–3 lb/GWh.
2.0E–3 lb/GWh.
4.0E–2 lb/GWh.
4.0E–3 lb/GWh.
9.0E–3 lb/GWh.
2.0E–2 lb/GWh.
7.0E–2 lb/GWh.
3.0E–1 lb/GWh.
2.0E–3 lb/MWh .........
OR
Sulfur dioxide (SO2) 3 .......
c. Mercury (Hg) ................
4. Liquid oil-fired unit—continental (excluding
limited-use liquid oil-fired subcategory
units).
OR
6.0E–2 lb/GWh .........
OR
...................................
8.0E–3 lb/GWh.
3.0E–3 lb/GWh.
6.0E–4 lb/GWh.
4.0E–4 lb/GWh.
7.0E–3 lb/GWh.
2.0E–3 lb/GWh.
3.0E–2 lb/GWh.
4.0E–3 lb/GWh.
4.0E–2 lb/GWh.
5.0E–2 lb/GWh.
1.0E–2 lb/MWh .........
OR
Sulfur dioxide (SO2) 3 .......
c. Mercury (Hg) ................
3. IGCC unit ....................................................
a. Filterable particulate
matter (PM).
OR
Total non-Hg HAP metals
OR
Individual HAP metals: .....
Antimony (Sb) ...........
Arsenic (As) ..............
Beryllium (Be) ...........
Cadmium (Cd) ..........
Chromium (Cr) ..........
Cobalt (Co) ...............
Lead (Pb) ..................
Manganese (Mn) .......
Nickel (Ni) .................
Selenium (Se) ...........
b. Hydrogen chloride
(HCl).
4.0E–1 lb/MWh .........
3.0E–3 lb/GWh .........
a. Filterable particulate
matter (PM).
OR
Total HAP metals .............
OR
Individual HAP metals:
Antimony (Sb) ...........
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4.0E–1 lb/MWh 1 .......
OR
2.0E–4 lb/MWh .........
OR
...................................
1.0E–2 lb/GWh.
Sfmt 4700
Using these requirements, as appropriate
(e.g., specified sampling volume or test run
duration) and limitations with the test
methods in Table 5 . . .
For Method 26A, collect a minimum of 3
dscm per run.
For ASTM D6348–03 2 or Method 320,
sample for a minimum of 1 hour.
SO2 CEMS.
Hg CEMS or sorbent trap monitoring system only.
Collect a minimum of 4 dscm per run.
Collect a minimum of 4 dscm per run.
Collect a minimum of 3 dscm per run.
For Method 26A, collect a minimum of 3
dscm per run.
For ASTM D6348–03 2 or Method 320,
sample for a minimum of 1 hour.
SO2 CEMS.
Hg CEMS or sorbent trap monitoring system only.
Collect a minimum of 1 dscm per run.
Collect a minimum of 1 dscm per run.
Collect a minimum of 2 dscm per run.
For Method 26A, collect a minimum of 1
dscm per run; for Method 26, collect a
minimum of 120 liters per run.
For ASTM D6348–03 2 or Method 320,
sample for a minimum of 1 hour.
SO2 CEMS.
Hg CEMS or sorbent trap monitoring system only.
Collect a minimum of 1 dscm per run.
Collect a minimum of 2 dscm per run.
Collect a minimum of 2 dscm per run.
E:\FR\FM\30NOR1.SGM
30NOR1
Federal Register / Vol. 77, No. 231 / Friday, November 30, 2012 / Rules and Regulations
For the following
pollutants . . .
Arsenic (As) ..............
Beryllium (Be) ...........
Cadmium (Cd) ..........
Chromium (Cr) ..........
Cobalt (Co) ...............
Lead (Pb) ..................
Manganese (Mn) .......
Nickel (Ni) .................
Selenium (Se) ...........
Mercury (Hg) ....................
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a. Filterable particulate
matter (PM).
OR
Total HAP metals .............
OR
Individual HAP metals:
Antimony (Sb) ...........
Arsenic (As) ..............
Beryllium (Be) ...........
Cadmium (Cd) ..........
Chromium (Cr) ..........
Cobalt (Co) ...............
Lead (Pb) ..................
Manganese (Mn) .......
Nickel (Ni) .................
Selenium (Se) ...........
Mercury (Hg) ....................
2.0E–1 lb/MWh 1 .......
OR
7.0E–3 lb/MWh .........
OR
2.0E–3 lb/MWh .........
c. Hydrogen fluoride (HF)
VerDate Mar<15>2010
4.0E–4 lb/MWh .........
b. Hydrogen chloride
(HCl).
6. Solid oil-derived fuel-fired unit. ...................
4.0E–4 lb/MWh .........
c. Hydrogen fluoride (HF)
5. Liquid oil-fired unit—non-continental (excluding limited-use liquid oil-fired subcategory units).
3.0E–3
5.0E–4
2.0E–4
2.0E–2
3.0E–2
8.0E–3
2.0E–2
9.0E–2
2.0E–2
1.0E–4
b. Hydrogen chloride
(HCl).
If your EGU is in this subcategory . . .
You must meet the
following emission
limits and work
practice standards
. . .
5.0E–4 lb/MWh .........
a. Filterable particulate
matter (PM).
OR
Total non-Hg HAP metals
OR
Individual HAP metals: .....
Antimony (Sb) ...........
Arsenic (As) ..............
Beryllium (Be) ...........
Cadmium (Cd) ..........
Chromium (Cr) ..........
Cobalt (Co) ...............
Lead (Pb) ..................
Manganese (Mn) .......
Nickel (Ni) .................
Selenium (Se) ...........
b. Hydrogen chloride
(HCl).
3.0E–2 lb/MWh 1 .......
PO 00000
Frm 00055
Fmt 4700
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh.
lb/GWh .........
...................................
8.0E–3 lb/GWh.
6.0E–2 lb/GWh.
2.0E–3 lb/GWh.
2.0E–3 lb/GWh.
2.0E–2 lb/GWh.
3.0E–1 lb/GWh.
3.0E–2 lb/GWh.
1.0E–1 lb/GWh.
4.1E0 lb/GWh.
2.0E–2 lb/GWh.
4.0E–4 lb/GWh .........
OR
6.0E–1 lb/GWh .........
OR
...................................
8.0E–3 lb/GWh.
3.0E–3 lb/GWh.
6.0E–4 lb/GWh.
7.0E–4 lb/GWh.
6.0E–3 lb/GWh.
2.0E–3 lb/GWh.
2.0E–2 lb/GWh.
7.0E–3 lb/GWh.
4.0E–2 lb/GWh.
6.0E–3 lb/GWh.
4.0E–4 lb/MWh .........
Sfmt 4700
71341
Using these requirements, as appropriate
(e.g., specified sampling volume or test run
duration) and limitations with the test
methods in Table 5 . . .
For Method 30B sample volume determination (Section 8.2.4), the estimated Hg
concentration should nominally be <1⁄2
the standard.
For Method 26A, collect a minimum of 3
dscm per run.
For ASTM D6348–03 2 or Method 320,
sample for a minimum of 1 hour.
For Method 26A, collect a minimum of 3
dscm per run.
For ASTM D6348–03 2 or Method 320,
sample for a minimum of 1 hour.
Collect a minimum of 1 dscm per run.
Collect a minimum of 1 dscm per run.
Collect a minimum of 3 dscm per run.
For Method 30B sample volume determination (Section 8.2.4), the estimated Hg
concentration should nominally be <1⁄2
the standard.
For Method 26A, collect a minimum of 1
dscm per run; for Method 26, collect a
minimum of 120 liters per run.
For ASTM D6348–03 2 or Method 320,
sample for a minimum of 1 hour.
For Method 26A, collect a minimum of 3
dscm per run.
For ASTM D6348–03 2 or Method 320,
sample for a minimum of 1 hour.
Collect a minimum of 1 dscm per run.
Collect a minimum of 1 dscm per run.
Collect a minimum of 3 dscm per run.
For Method 26A, collect a minimum of 3
dscm per run.
For ASTM D6348–03 2 or Method 320,
sample for a minimum of 1 hour.
E:\FR\FM\30NOR1.SGM
30NOR1
71342
Federal Register / Vol. 77, No. 231 / Friday, November 30, 2012 / Rules and Regulations
For the following
pollutants . . .
Using these requirements, as appropriate
(e.g., specified sampling volume or test run
duration) and limitations with the test
methods in Table 5 . . .
OR
Sulfur dioxide (SO2) 3 .......
c. Mercury (Hg) ................
If your EGU is in this subcategory . . .
You must meet the
following emission
limits and work
practice standards
. . .
1.0 lb/MWh ................
2.0E–3 lb/GWh .........
SO2 CEMS.
Hg CEMS or Sorbent trap monitoring system only.
1 Gross
electric output.
by reference, see § 63.14.
3 You may not use the alternate SO limit if your EGU does not have some form of FGD system and SO CEMS installed.
2
2
4 Duct burners on syngas; gross electric output.
5 Duct burners on natural gas; gross electric output.
2 Incorporated
20. Revise Table 3 to Subpart UUUUU
of Part 63 to read as follows:
■
Table 3 to Subpart UUUUU of Part 63
— Work Practice Standards
As stated in §§ 63.9991, you must
comply with the following applicable
work practice standards:
If your EGU is . . .
You must meet the following . . .
1. An existing EGU .........................
Conduct a tune-up of the EGU burner and combustion controls at least each 36 calendar months, or each
48 calendar months if neural network combustion optimization software is employed, as specified in
§ 63.10021(e).
Conduct a tune-up of the EGU burner and combustion controls at least each 36 calendar months, or each
48 calendar months if neural network combustion optimization software is employed, as specified in
§ 63.10021(e).
You must operate all CMS during startup.
For startup of an EGU, you must use one or a combination of the following clean fuels: natural gas, synthetic natural gas, propane, distillate oil, syngas, and ultra-low sulfur diesel.
Once you start firing coal, residual oil, or solid oil-derived fuel, you must vent emissions to the main
stack(s) and engage all of the applicable control devices except limestone injection in FBC EGUs, dry
scrubber, SNCR, and SCR. You must start your limestone injection in FBC EGUs, dry scrubber, SNCR,
and SCR systems as expeditiously as possible, but, in any case, when necessary to comply with other
standards applicable to the source that require operation of the control devices.
Relative to the syngas not fired in the combustion turbine of an IGCC EGU during startup, you must either:
(1) Flare the syngas or (2) route the syngas to duct burners, which may need to be installed, and route
the flue gas from the duct burners to the heat recovery steam generator.
You must comply with all applicable emission limits at all times except for startup or shutdown periods conforming with this work practice. You must collect monitoring data during periods of startup, as specified
in § 63.10020(a). You must keep records during periods of startup. You must provide reports concerning
activities and periods of startup, as specified in § 63.10011(g) and § 63.10021(h) and (i).
You must operate all CMS during shutdown.
While firing coal, residual oil, or solid oil-derived fuel during shutdown, you must vent emissions to the
main stack(s) and operate all applicable control devices, except limestone injection in FBC EGUs, dry
scrubber, SNCR, and SCR. You must operate your limestone injection in FBC EGUs, dry scrubber,
SNCR, and SCR systems as expeditiously as possible, but, in any case, when necessary to comply with
other standards that apply to the source and that require operation of the control devices.
If, in addition to the fuel used prior to initiation of shutdown, another fuel must be used to support the shutdown process, that additional fuel must be one or a combination of the following clean fuels: Natural
gas, synthetic natural gas, propane, distillate oil, syngas, and ultra-low sulfur diesel.
Relative to the syngas not fired in the combustion turbine of an IGCC EGU during shutdown, you must either: (1) Flare the syngas or (2) route the syngas to duct burners, which may need to be installed, and
route the flue gas from the duct burners to the heat recovery steam generator.
You must comply with all applicable emission limits at all times except during startup and shutdown periods at which time you must meet this work practice. You must collect monitoring data during periods of
startup, as specified in § 63.10020(a). You must keep records during periods of startup. You must provide reports concerning activities and periods of startup, as specified in § 63.10011(g) and § 63.10021(h)
and (i).
2. A new or reconstructed EGU .....
3. A coal-fired, liquid oil-fired, or
solid oil-derived fuel-fired EGU
during startup.
4. A coal-fired, liquid oil-fired, or
solid oil-derived fuel-fired EGU
during shutdown.
21. Revise Table 4 to Subpart UUUUU
of Part 63 to read as follows:
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Table 4 to Subpart UUUUU of Part 63—
Operating Limits for EGUs
As stated in §§ 63.9991, you must
comply with the applicable operating
limits:
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71343
If you demonstrate compliance using . . .
You must meet these operating limits . . .
1. PM CPMS for an existing EGU.
Maintain the 30-boiler operating day rolling average PM CPMS output at or below the highest 1-hour average measured during the most recent performance test demonstrating compliance with the filterable PM, total non-mercury
HAP metals (total HAP metals, for liquid oil-fired units), or individual non-mercury HAP metals (individual HAP metals including Hg, for liquid oil-fired units) emissions limitation(s).
Maintain the 30-boiler operating day rolling average PM CPMS output at or below the highest 1-hour average PM
CPMS output value recorded during the most recent performance test run demonstrating compliance with the filterable PM, total non-mercury HAP metals (total HAP metals, for liquid oil-fired units), or individual non-mercury HAP
metals (individual HAP metals including Hg, for liquid oil-fired units) emissions limitation(s).
2. PM CPMS for a new
EGU.
22. Revise footnote 4 of Table 5 to
Subpart UUUUU of Part 63 to read as
follows:
■
Table 5 to Subpart UUUUU of Part 63—
Performance Testing Requirements
*
*
*
*
*
4 When
using ASTM D6348–03, 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; (2) For ASTM
D6348–03 Annex A5 (Analyte Spiking
Technique), the percent (%)R must be
determined for each target analyte (see
Equation A5.5); (3) For the ASTM D6348–03
test data to be acceptable for a target analyte,
%R must be 70% ≤ R ≤ 130%; and (4) The
%R value for each compound must be
reported in the test report and all field
measurements corrected with the calculated
%R value for that compound using the
following equation:
*
*
*
*
23. Revise Table 6 to Subpart UUUUU
of Part 63 to read as follows:
■
Table 6 to Subpart UUUUU of Part 63—
Establishing PM CPMS Operating
Limits
As stated in § 63.10007, you must
comply with the following requirements
for establishing operating limits:
*
If you have an applicable
emission limit for . . .
And you choose to establish PM CPMS operating
limits, you must . . .
And . . .
Using . . .
According to the following
procedures . . .
1. Filterable Particulate
matter (PM), total nonmercury HAP metals, individual non-mercury
HAP metals, total HAP
metals, or individual
HAP metals for an existing EGU.
Install, certify, maintain,
and operate a PM
CPMS for monitoring
emissions discharged to
the atmosphere according to § 63.10010(h)(1).
Establish a site-specific
operating limit in units of
PM CPMS output signal
(e.g., milliamps, mg/
acm, or other raw signal).
Data from the PM CPMS
and the PM or HAP metals performance tests.
2. Filterable Particulate
matter (PM), total nonmercury HAP metals, individual non-mercury
HAP metals, total HAP
metals, or individual
HAP metals for a new
EGU.
Install, certify, maintain,
and operate a PM
CPMS for monitoring
emissions discharged to
the atmosphere according to § 63.10010(h)(1).
Establish a site-specific
operating limit in units of
PM CPMS output signal
(e.g., milliamps, mg/
acm, or other raw signal).
Data from the PM CPMS
and the PM or HAP metals performance tests.
1. Collect PM CPMS output data during the entire period of the performance tests.
2. Record the average
hourly PM CPMS output
for each test run in the
three run performance
test.
3. Determine the highest
1-hour average PM
CPMS measured during
the performance test
demonstrating compliance with the filterable
PM or HAP metals emissions limitations.
1. Collect PM CPMS output data during the entire period of the performance tests.
2. Record the average
hourly PM CPMS output
for each test run in the
three run performance
test.
3. Determine the highest
1-hour average PM
CPMS measured during
the performance run
demonstrating compliance with the filterable
PM or HAP metals emissions limitations.
24. Revise Table 7 to Subpart UUUUU
of Part 63 to read as follows:
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Table 7 to Subpart UUUUU of Part 63—
Demonstrating Continuous Compliance
emission limitations for affected sources
according to the following:
As stated in § 63.10021, you must
show continuous compliance with the
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Federal Register / Vol. 77, No. 231 / Friday, November 30, 2012 / Rules and Regulations
If you use one of the following to meet applicable emissions
limits, operating limits, or work practice standards . . .
You demonstrate continuous compliance by . . .
1. CEMS to measure filterable PM, SO2, HCl, HF, or Hg
emissions, or using a sorbent trap monitoring system to
measure Hg.
Calculating the 30- (or 90-) boiler operating day rolling arithmetic average emissions rate in units of the applicable emissions standard basis at the end of
each boiler operating day using all of the quality assured hourly average
CEMS or sorbent trap data for the previous 30- (or 90-) boiler operating days,
excluding data recorded during periods of startup or shutdown.
Calculating the arithmetic 30- (or 90-) boiler operating day rolling average of all
of the quality assured hourly average PM CPMS output data (e.g., milliamps,
PM concentration, raw data signal) collected for all operating hours for the previous 30 boiler operating days, excluding data recorded during periods of startup or shutdown.
If applicable, by conducting the monitoring in accordance with an approved sitespecific monitoring plan.
Calculating the results of the testing in units of the applicable emissions standard.
2. PM CPMS to measure compliance with a parametric operating limit.
3. Site-specific monitoring using CMS for liquid oil-fired EGUs
for HCl and HF emission limit monitoring.
4. Quarterly performance testing for coal-fired, solid oil derived fired, or liquid oil-fired EGUs to measure compliance
with one or more applicable emissions limit in Table 1 or 2.
5. Conducting periodic performance tune-ups of your EGU(s)
6. Work practice standards for coal-fired, liquid oil-fired, or
solid oil-derived fuel-fired EGUs during startup.
7. Work practice standards for coal-fired, liquid oil-fired, or
solid oil-derived fuel-fired EGUs during shutdown.
Conducting periodic performance tune-ups of your EGU(s), as specified in
§ 63.10021(e).
Operating in accordance with Table 3.
Operating in accordance with Table 3.
25. Revise sections 4.1 and 5.2.2.2 to
Appendix A to Subpart UUUUU of Part
63 to read as follows:
ENVIRONMENTAL PROTECTION
AGENCY
Appendix A to Subpart UUUUU—Hg
Monitoring Provisions
[EPA–R06–RCRA–2012–0473; FRL–9745–1]
■
4.1 Certification Requirements. All Hg
CEMS and sorbent trap monitoring systems
and the additional monitoring systems used
to continuously measure Hg emissions in
units of the applicable emissions standard in
accordance with this appendix must be
certified in a timely manner, such that the
initial compliance demonstration is
completed no later than the applicable date
in § 63.9984(f).
*
*
*
*
*
5.2.2.2 The same RATA performance
criteria specified in Table A–2 for Hg CEMS
shall apply to the annual RATAs of the
sorbent trap monitoring system.
*
*
*
*
*
26. Revise section 3.1.2.1.3 and the
heading to section 5.3.4 to Appendix B
to Subpart UUUUU of Part 63 to read as
follows:
■
Appendix B to Subpart UUUUU—HCl
and HF Monitoring Provisions
3.1.2.1.3 For the ASTM D6348–03 test
data to be acceptable for a target analyte, %R
must be 70% ≤ R ≤ 130%; and
*
*
5.3.3
*
*
*
*
*
Conditional Data Validation
*
*
*
wreier-aviles on DSK5TPTVN1PROD with
[FR Doc. 2012–28729 Filed 11–29–12; 8:45 am]
BILLING CODE 6560–50–P
VerDate Mar<15>2010
14:04 Nov 29, 2012
Jkt 229001
40 CFR Parts 271 and 272
Texas: Final Authorization of Stateinitiated Changes and Incorporation by
Reference of State Hazardous Waste
Management Program
Environmental Protection
Agency (EPA).
ACTION: Direct final rule.
AGENCY:
During a review of Texas’
regulations, the EPA identified a variety
of State-initiated changes to its
hazardous waste program under the
Resource Conservation and Recovery
Act (RCRA). We have determined that
these changes are minor and satisfy all
requirements needed to qualify for Final
authorization and are authorizing the
State-initiated changes through this
Direct Final action.
The Solid Waste Disposal Act, as
amended, commonly referred to as the
Resource Conservation and Recovery
Act (RCRA), allows the Environmental
Protection Agency (EPA) to authorize
States to operate their hazardous waste
management programs in lieu of the
Federal program. The EPA uses the
regulations entitled ‘‘Approved State
Hazardous Waste Management
Programs’’ to provide notice of the
authorization status of State programs
and to incorporate by reference those
provisions of the State statutes and
regulations that will be subject to the
EPA’s inspection and enforcement. The
rule codifies in the regulations the prior
approval of Texas’ hazardous waste
management program and incorporates
SUMMARY:
PO 00000
Frm 00058
Fmt 4700
Sfmt 4700
by reference authorized provisions of
the State’s statutes and regulations.
DATES: This regulation is effective
January 29, 2013, unless the EPA
receives adverse written comment on
the codification of the Texas authorized
RCRA program by the close of business
December 31, 2012. If the EPA receives
such comments, it will publish a timely
withdrawal of this direct final rule in
the Federal Register informing the
public that this rule will not take effect.
The incorporation by reference of
authorized provisions in the Texas
statutes and regulations contained in
this rule is approved by the Director of
the Federal Register as of January 29,
2013 in accordance with 5 U.S.C. 552(a)
and 1 CFR part 51.
ADDRESSES: Submit your comments by
one of the following methods:
1. Federal eRulemaking Portal:
https://www.regulations.gov. Follow the
on-line instructions for submitting
comments.
2. Email: patterson.alima@epa.gov or
banks.julia@epa.gov.
3. Mail: Alima Patterson, Region 6,
Regional Authorization Coordinator, or
Julia Banks, Codification Coordinator,
State/Tribal Oversight Section (6PD–O),
Multimedia Planning and Permitting
Division, EPA Region 6, 1445 Ross
Avenue, Dallas, Texas 75202–2733.
4. Hand Delivery or Courier: Deliver
your comments to Alima Patterson,
Region 6, Regional Authorization
Coordinator, or Julia Banks, Codification
Coordinator, State/Tribal Oversight
Section (6PD–O), Multimedia Planning
and Permitting Division, EPA Region 6,
1445 Ross Avenue, Dallas, Texas 75202–
2733.
E:\FR\FM\30NOR1.SGM
30NOR1
Agencies
[Federal Register Volume 77, Number 231 (Friday, November 30, 2012)]
[Rules and Regulations]
[Pages 71323-71344]
From the Federal Register Online via the Government Printing Office [www.gpo.gov]
[FR Doc No: 2012-28729]
=======================================================================
-----------------------------------------------------------------------
ENVIRONMENTAL PROTECTION AGENCY
40 CFR Parts 60 and 63
[EPA-HQ-OAR-2009-0234; EPA-HQ-OAR-2011-0044; FRL-9733-2]
RIN 2060-AR62
Reconsideration of Certain New Source and Startup/Shutdown
Issues: National Emission Standards for Hazardous Air Pollutants From
Coal- and Oil-Fired Electric Utility Steam Generating Units and
Standards of Performance for Fossil-Fuel-Fired Electric Utility,
Industrial-Commercial-Institutional, and Small Industrial-Commercial-
Institutional Steam Generating Units
AGENCY: Environmental Protection Agency (EPA).
ACTION: Proposed rules; notice of public hearing.
-----------------------------------------------------------------------
SUMMARY: On February 16, 2012, pursuant to sections 111 and 112 of the
Clean Air Act (CAA), the EPA published the final rules titled
``National Emission Standards for Hazardous Air Pollutants from Coal-
and Oil-fired Electric Utility Steam Generating Units and Standards of
Performance for Fossil-Fuel-Fired Electric Utility, Industrial-
Commercial-Institutional, and Small Industrial-Commercial-Institutional
Steam Generating Units.'' The National Emission Standards for Hazardous
Air Pollutants (NESHAP) rule issued pursuant to CAA section 112 is
referred to as the Mercury and Air Toxics Standards (MATS), and the New
Source Performance Standards rule issued pursuant to CAA section 111 is
referred to as the Utility NSPS. The Administrator received petitions
for reconsideration of certain aspects of MATS and the Utility NSPS. In
this notice, the EPA is announcing reconsideration of certain new
source standards for MATS, the requirements applicable during periods
of startup and shutdown for MATS, the startup and shutdown provisions
related to the particulate matter (PM) standard in the Utility NSPS,
and certain revisions to the definitional and monitoring provisions of
the Utility NSPS. We are also proposing certain technical corrections
to both MATS and the Utility NSPS.
We seek comment only on the aspects of the final MATS and Utility
NSPS rules specifically identified in this notice. We are not opening
for reconsideration any other provisions of MATS or the Utility NSPS at
this time.
DATES: Comments. Comments must be received on or before December 31,
2012. Because of the need to resolve the issues identified in this
notice in a timely manner, the EPA does not intend to grant requests
for extensions beyond this date.
Public Hearing. If anyone contacts the EPA by December 10, 2012
requesting to speak at a public hearing, the EPA will hold a public
hearing on December 18, 2012. If a public hearing is held, it will be
held from 9:00 a.m. to 7:00 p.m., Eastern time, in Room 1153 EPA East
Hearing room, 1201 Constitution Avenue NW., Washington, DC 20460, (202)
564-1657. For further information on the public hearing and requests to
speak, see the ADDRESSES section of this preamble.
ADDRESSES: Comments. Submit your comments, identified by Docket ID. No.
EPA-HQ-OAR-2011-0044 (NSPS action) or Docket ID No. EPA-HQ-OAR-2009-
0234 (NESHAP/MATS action), by one of the following methods:
https://www.regulations.gov. Follow the instructions for
submitting comments.
https://www.epa.gov/oar/docket.html. Follow the
instructions for submitting comments on the EPA Air and Radiation
Docket Web Site.
Email: Comments may be sent by electronic mail (email) to
a-and-r-docket@epa.gov, Attention EPA-HQ-OAR-2011-0044 (NSPS action) or
EPA-HQ-OAR-2009-0234 (NESHAP/MATS action).
Fax: Fax your comments to: (202) 566-9744, Docket ID No.
EPA-HQ-OAR-2011-0044 (NSPS action) or Docket ID No. EPA-HQ-OAR-2009-
0234 (NESHAP/MATS action).
Mail: Send your comments on the NESHAP/MATS action to: EPA
Docket Center (EPA/DC), Environmental Protection Agency, Mailcode:
2822T, 1200 Pennsylvania Ave. NW., Washington, DC 20460, Docket ID No.
EPA-HQ-OAR-2009-0234. Send your comments on the NSPS action to: EPA
Docket Center (EPA/DC), Environmental Protection Agency, Mailcode:
2822T, 1200 Pennsylvania Ave. NW., Washington, DC 20460, Docket ID.
EPA-HQ-OAR-2011-0044. Please include a total of two copies. In
addition, please mail a copy of your comments on the information
collection provisions to the Office of Information and Regulatory
Affairs, OMB, Attn: Desk Officer for EPA, 725 17th St. NW., Washington,
DC 20503.
Hand Delivery or Courier: Deliver your comments to: EPA
Docket Center, EPA West, Room 3334, 1301 Constitution Ave. NW.,
Washington, DC 20460. Please include a total of two copies. Such
deliveries are only accepted during the Docket's normal hours of
operation (8:30 a.m. to 4:30 p.m., Monday through Friday, excluding
legal holiday), and special arrangements should be made for deliveries
of boxed information.
Instructions. All submissions must include agency name and
respective docket number or Regulatory Information Number (RIN) for
this rulemaking. All comments will be posted without change and may be
made available online at https://www.regulations.gov, including any
personal information provided, unless the comment includes information
claimed to be confidential business information (CBI) or other
information whose disclosure is restricted by statute. Do not submit
information that you consider to be CBI or otherwise protected through
https://www.regulations.gov or email. The https://www.regulations.gov Web
site is an ``anonymous access'' system, which means the EPA will not
know your identity or contact information unless you provide it in the
body of your comment. If you send an email comment directly to the EPA
without going through https://www.regulations.gov, your email address
will be automatically captured and included as part of the comment that
is placed in the public docket and made available on the Internet. If
you submit an electronic comment, the EPA recommends that you include
your name and other contact information in the body of your comment and
with any disk or CD-ROM you submit. If the EPA cannot read your comment
due to technical difficulties and cannot contact you for clarification,
the EPA may not be able to consider your comment. Electronic files
should avoid the use of special characters, any form of encryption, and
be free of any defects or viruses.
Public Hearing. If anyone contacts EPA by December 10, 2012
requesting to speak at a public hearing, the EPA will hold a public
hearing on December 18, 2012. If a public hearing is held, it will be
held from 9:00 a.m. to 7:00 p.m., Eastern time in Room 1153 EPA East
Hearing room, 1201 Constitution
[[Page 71324]]
Avenue NW., Washington, DC 20460, 202-564-1657. A lunch break is
scheduled from 12:00 p.m.-1:00 p.m. Visitors must go through a metal
detector, sign in with the security desk, be accompanied by an employee
and show identification to enter the building. Contact Pamela Garrett
at (919) 541-7966 or at garrett.pamela@epa.gov to request a hearing, to
determine if a hearing will be held and to register to speak if a
hearing is held. If no one contacts the EPA requesting to speak at a
public hearing concerning this proposed rule by December 10, 2012, the
hearing will be cancelled without further notice. If a hearing is held,
the last day to register to present oral testimony in advance will be
Friday, December 14, 2012. The public hearing will provide interested
parties the opportunity to present data, views, or arguments concerning
this notice. The record for this action will remain open for 30 days
after the date of the hearing to provide an opportunity for submission
of rebuttal and supplementary information. We will also specify the
date and time of the public hearings on https://www.epa.gov/airquality/powerplanttoxics/actions.html and https://www.epa.gov/ttn/atw/utility/utilitypg.html.
Docket. All documents in the docket are listed in the https://www.regulations.gov index. Although listed in the index, some
information is not publicly available (e.g., CBI or other information
whose disclosure is restricted by statute). Certain other material,
such as copyrighted material, will be publicly available only in hard
copy form. Publicly available docket materials are available either
electronically in https://www.regulations.gov or in hard copy at the EPA
Docket Center, Room 3334, 1301 Constitution Avenue NW., Washington, DC.
The Public Reading Room is open from 8:30 a.m. to 4:30 p.m., Monday
through Friday, excluding legal holidays. The telephone number for the
Public Reading Room is (202) 566-1744, and the telephone number for the
Air Docket is (202) 566-1742.
FOR FURTHER INFORMATION CONTACT: For the NESHAP action: Mr. William
Maxwell, Energy Strategies Group, Sector Policies and Programs
Division, (D243-01), Office of Air Quality Planning and Standards, U.S.
Environmental Protection Agency, Research Triangle Park, North Carolina
27711; Telephone number: (919) 541-5430; Fax number (919) 541-5450;
Email address: maxwell.bill@epa.gov. For the NSPS action: Mr. Christian
Fellner, Energy Strategies Group, Sector Policies and Programs
Division, (D243-01), Office of Air Quality Planning and Standards, U.S.
Environmental Protection Agency, Research Triangle Park, North Carolina
27711; Telephone number: (919) 541-4003; Fax number (919) 541-5450;
Email address: fellner.christian@epa.gov.
SUPPLEMENTARY INFORMATION:
Outline. The information presented in this preamble is organized as
follows:
I. General Information
A. Does this reconsideration notice apply to me?
B. What should I consider as I prepare my comments to the EPA?
C. How do I obtain a copy of this document and other related
information?
II. Background
III. Today's Action
IV. Discussion of Provisions Subject to Reconsideration--NESHAP/MATS
A. New Source MATS Emission Limits
B. Eligibility To Be a New Source
C. Startup and Shutdown Provisions
V. Discussion of Provisions Subject to Reconsideration--Utility NSPS
VI. Technical Corrections and Clarifications
VII. Impacts of This Proposed Rule
A. What are the air impacts?
B. What are the energy impacts?
C. What are the compliance costs?
D. What are the economic and employment impacts?
E. What are the benefits of the proposed standards?
VIII. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory Planning and Review and
Executive Order 13563: Improving Regulation and Regulatory Review
B. Paperwork Reduction Act
C. Regulatory Flexibility Act
D. Unfunded Mandates Reform Act
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 That Significantly Affect
Energy Supply, Distribution, or Use
I. National Technology Transfer and Advancement Act
J. Executive Order 12898: Federal Actions To Address
Environmental Justice in Minority Populations and Low-Income
Populations
I. General Information
A. Does this reconsideration notice apply to me?
Categories and entities potentially affected by today's notice
include:
----------------------------------------------------------------------------------------------------------------
Category NAICS code \1\ Examples of potentially regulated entities
----------------------------------------------------------------------------------------------------------------
Industry...................................... 221112 Fossil fuel-fired electric utility steam
generating units.
Federal government............................ \2\ 221122 Fossil fuel-fired electric utility steam
generating units owned by the Federal
government.
State/local/Tribal government................. \2\ 221122 Fossil fuel-fired electric utility steam
generating units owned by municipalities.
921150 Fossil fuel-fired electric utility steam
generating units in Indian country.
----------------------------------------------------------------------------------------------------------------
\1\ North American Industry Classification System.
\2\ Federal, State, or local government-owned and operated establishments are classified according to the
activity in which they are engaged.
This table is not intended to be exhaustive but rather to provide a
guide for readers regarding entities likely to be affected by this
action. To determine whether your facility, company, business,
organization, etc. would be regulated by this action, you should
examine the applicability criteria in 40 CFR 60.40, 60.40Da, or 60.40c
or in 40 CFR 63.9982. If you have any questions regarding the
applicability of this action to a particular entity, consult either the
air permitting authority for the entity or your EPA regional
representative as listed in 40 CFR 60.4 or 40 CFR 63.13 (General
Provisions).
B. What should I consider as I prepare my comments to the EPA?
Do not submit information containing CBI to the EPA through https://www.regulations.gov or email. Send or deliver information identified as
CBI only to the following address: Roberto Morales, OAQPS Document
Control Officer (C404-02), Office of Air Quality Planning and
Standards, U.S. Environmental Protection Agency, Research Triangle
Park, North Carolina 27711, Attention: Docket ID EPA-HQ-OAR-2011-0044
(Utility NSPS) or Docket ID EPA-HQ-OAR-2009-0234 (NESHAP/MATS). Clearly
mark the part or all of the information that you claim to be CBI. For
CBI information in a disk or CD-ROM that you mail to the EPA, mark the
outside of the disk or CD-ROM as CBI and then identify electronically
within the disk or CD-ROM the specific information that is claimed as
CBI. In addition to one complete version of the comment that includes
information
[[Page 71325]]
claimed as CBI, a copy of the comment that does not contain the
information claimed as CBI must be submitted for inclusion in the
public docket. Information so marked will not be disclosed except in
accordance with procedures set forth in 40 CFR part 2.
C. How do I obtain a copy of this document and other related
information?
In addition to being available in the docket, electronic copies of
these proposed rules will be available on the Worldwide Web (WWW)
through the Technology Transfer Network (TTN). Following signature, a
copy of each proposed rule will be posted on the TTN's policy and
guidance page for newly proposed or promulgated rules at the following
address: https://www.epa.gov/ttn/oarpg/. The TTN provides information
and technology exchange in various areas of air pollution control.
II. Background
The Administrator signed MATS and the Utility NSPS on December 16,
2011, and the final rules were published in the Federal Register at 77
FR 9304, February 16, 2012. Following promulgation of the final rules,
the Administrator received petitions for reconsideration of numerous
provisions of both MATS and the Utility NSPS pursuant to CAA section
307(d)(7)(B). Copies of the MATS petitions are provided in rulemaking
docket EPA-HQ-OAR-2009-0234. Copies of the Utility NSPS petitions are
provided in rulemaking docket EPA-HQ-OAR-2011-0044.
III. Today's Action
Today, we are granting reconsideration of, proposing, and
requesting comment on the following limited set of issues: (1) Certain
revised new source standards in MATS, (2) requirements applicable
during periods of startup and shutdown in MATS, (3) startup and
shutdown provisions related to the PM standard in the Utility NSPS, and
(4) definitional and monitoring provisions in the Utility NSPS. We are
also proposing certain technical corrections to both MATS and the
Utility NSPS.
This notice is limited to the specific issues identified in this
notice. We will not respond to any comments addressing any other
provisions of MATS or the Utility NSPS.\1\
---------------------------------------------------------------------------
\1\ The recent decision by the U.S. Court of Appeals for the
D.C. Circuit regarding the Cross State Air Pollution Rule (CSAPR)
has no impact on the issues being reconsidered in this action.
---------------------------------------------------------------------------
The impacts of today's proposed revisions on the costs and the
benefits of the final rule are minor. We expect that source owners and
operators will install and operate the same or similar control
technologies to meet the proposed revised standards in this notice as
they would have chosen to comply with the standards in the February
2012 final rule.\2\
---------------------------------------------------------------------------
\2\ Because, on an individual EGU-by-EGU basis we anticipate
very similar costs, any changes to the baseline since we finalized
MATS (e.g., potential impacts of the CSAPR decision) would not
impact this determination.
---------------------------------------------------------------------------
IV. Discussion of Provisions Subject to Reconsideration--NESHAP/MATS
A. New Source MATS Emission Limits
The EPA received petitions requesting reconsideration of aspects of
the new source emission limits in the final MATS rule. We are granting
reconsideration of certain new source emission limits, as discussed
below, and we invite comment on the proposed provisions in today's
notice.
1. Certain New Source Limits--Use of Data in the Record
The EPA received petitions for reconsideration asserting that the
Agency did not use all the data in the record from the best performing
sources in establishing certain final new source emission limits for
coal- and oil-fired electric utility steam generating units (EGUs).
Specifically, the petitioners maintained that the EPA did not consider
all of the data in the record when establishing emission standards for
filterable PM and hydrogen chloride (HCl) applicable to new coal-fired
EGUs and for filterable PM applicable to new solid oil-derived fuel-
fired EGUs.
In light of petitioners' assertions, we reviewed the available
emissions information in the record for all the new source standards.
We determined that we did not use all the data in the record in
establishing the new source emission limits for filterable PM and HCl
applicable to new coal-fired EGUs and for filterable PM applicable to
new solid oil-derived fuel-fired EGUs. We also identified a few
additional new source limits for which we did not use all of the data
in the record when setting the standards in the final rule. We are
proposing to revise the sulfur dioxide (SO2) limit
applicable to solid oil-derived fuel-fired EGUs, the filterable PM
limit applicable to continental liquid oil-fired EGUs, and the lead and
selenium limits applicable to coal-fired EGUs based on consideration of
all the data in the record from the best performing sources for the
pollutants at issue. We solicit comment on the revised standards.
Additional details on the proposed emission limits can be found in the
memo ``Reconsideration of the National Emission Standards for Hazardous
Air Pollutants (NESHAP) Maximum Achievable Control Technology (MACT)
Floor Analysis for Coal- and Oil-fired Electric Utility Steam
Generating Units, Proposed Rule'' in rulemaking docket EPA-HQ-OAR-2009-
0234.
We also solicit comment on possible revisions to the Hg limit
applicable to low rank virgin coal-fired EGUs based on additional data
in the record. See ``Reconsideration of the National Emission Standards
for Hazardous Air Pollutants (NESHAP) Maximum Achievable Control
Technology (MACT) Floor Analysis for Coal- and Oil-fired Electric
Utility Steam Generating Units, Proposed Rule'' in rulemaking docket
EPA-HQ-OAR-2009-0234; ``MATS Reconsideration: Beyond-the-Floor
Memorandum'' available in rulemaking docket EPA-HQ-OAR-2009-0234.
The proposed revised new source CAA section 112(d) emission
standards are presented in tables 1 and 2 of this preamble. The Agency
derived these limits by first calculating the floor standards and then
assessing whether a more stringent beyond-the-floor standard is
appropriate.\3\ As explained further below, as to the standards we are
proposing to revise, we are proposing a beyond-the-floor standard for
HCl for new coal-fired EGUs, but we are not proposing beyond-the-floor
standards for the other pollutants and subcategories.
---------------------------------------------------------------------------
\3\ CAA section 112(d)(2) requires the EPA to consider whether
more stringent beyond-the-floor standards should be established.
---------------------------------------------------------------------------
2. SO2 Limit for New Coal-Fired EGUs--Reliance on Industrial
Boiler Emission Data
We are also reconsidering the SO2 standard for new coal-
fired EGUs. The Agency received a petition asserting that the final
alternative SO2 emission limit was developed using, as the
best performing source, a unit that is 25 MW in capacity. In order to
be classified as an EGU, and thus subject to MATS, a unit must be
greater than 25 MW in capacity. A unit that is 25 MW or less is likely
an industrial boiler and would be subject to the Industrial-Commercial-
Institutional Boiler NESHAP, not MATS.
At the time of the final rule, we believed the unit on which we
based the SO2 standard for new coal-fired EGUs was an EGU.
After we received the petition for reconsideration, we re-
[[Page 71326]]
examined the record and determined that the unit was, in fact, an
industrial boiler and not an EGU.
As an initial matter, nothing in the CAA precludes the EPA from
identifying a source in another source category as the best controlled
similar source. However, we believe that it is appropriate in this
case, where we have considerable data on EGUs, to base the new source
standard on the best performing unit that is an EGU. This is also
consistent with our intent in the final rule, as we thought the unit we
had selected was, in fact, an EGU. For these reasons, we are
reconsidering the SO2 standard for new coal-fired EGUs. We
have reviewed the emissions data and identified the best performing EGU
upon which to base the proposed SO2 standard. The proposed
limit is presented in table 2 of this preamble. We solicit comment on
the revised limit and the methods used to establish this limit.
3. Hg Limit for New Coal-Fired EGUs Designed for Coal >= 8300 Btu/lb--
Measurement Issues
The EPA is also reconsidering the emission limit for Hg for new
coal-fired EGUs in the units designed for the coal >= 8300 Btu/lb (non-
low rank virgin coal) subcategory. Some petitioners asserted that this
limit, as finalized, was too low for emissions to be reliably measured
in a manner that would allow sources to operate their control
technology in a way that ensures compliance with the standard.
Specifically, petitioners maintained that sorbent trap monitoring
systems could not provide sufficiently timely Hg data at the new source
level for sources to make adjustments to the EGUs and attendant air
pollution control devices (ACPDs) to ensure compliance with the
standard and that Hg continuous emissions monitoring systems (CEMS)
were not capable of measuring Hg at the new source limit. The
petitioners indicated that reliable and frequent emission measurements
are needed to maintain the operation of Hg control technology at
performance levels set in the final rule.
As we explained in the record to the final rule, owners and
operators of new EGUs in the non-low rank virgin coal subcategory could
use the sorbent trap monitoring systems to demonstrate compliance with
the new source Hg standard because of the potential for a longer sample
collection period associated with sorbent traps and their inherent
lower emissions detection capability.
As described in the final rule, when establishing emission limits
for pollutants, we calculated a representative detection limit (RDL)
and then compared the UPL-determined emission floor with a value three
times the RDL (3 X RDL), and we set the final limit at the higher of
the two numbers. We did not follow that procedure for sorbent trap
monitoring systems when setting Hg emission limits as we did not
believe sorbent trap monitoring systems were constrained by method
detection limits, since operators could increase the sample collection
time up to 14 days to guarantee collection of a measurable quantity of
mercury with appropriate accuracy. We continue to believe that the
promulgated Hg limit for the non-low rank virgin coal subcategory is
measurable using a sorbent trap monitoring system.
As noted, however, petitioners have indicated that the long sorbent
trap sampling times that may be necessary to measure at the final new
source level do not allow sufficiently frequent emissions feedback such
that a source could take corrective action and avoid violations of the
emission limit within the prescribed compliance time.
We understand that Hg emissions can vary over time, and we
acknowledge the value of frequent feedback of emission measurements. We
also understand that frequent feedback may be desirable and, at times,
necessary to optimize the operation of generation or control technology
in order to maintain emissions at or below the standard. The sorbent
trap monitoring method required in the MATS rule allows sampling for as
long as 14 days. In the final rule, we assumed that most sources would
leave the sorbent traps in as long as needed--up to 14 days--to ensure
they had no measurement issues. Based on the petitions for
reconsideration, we understand that sources will most likely use a
shorter sampling period, perhaps as short as 30 minutes. The shorter
sampling periods will provide more constant feedback on Hg emissions,
which will help the source ensure that it is in compliance with the Hg
emission limit, for which compliance is determined on a 30-day rolling
average.
Given the petitioners' stated need for more frequent Hg emissions
information, we re-evaluated whether detection level issues arise when
shorter sampling periods, such as 30 minutes, are employed by sorbent
trap monitoring systems. Although the shorter sampling period is
adequate to provide information needed to optimize the operation of Hg
control technology, we believe the reduced sampling period results in a
reduced quantity of collected Hg which constrains the sorbent trap
monitoring system by a minimum detection limit. For additional
information, see ``Determination of Representative Detection Level
(RDL) and 3 X RDL Values for Mercury Measured Using Sorbent Trap
Technologies'' in rulemaking docket EPA-HQ-OAR-2009-0234. Specifically,
we believe detection level issues may arise from using a sorbent trap
when short sampling periods (e.g., 30 minutes) are used, and that, as
such, the UPL-calculated floor value should be compared against the 3 X
RDL value to account for the shorter sampling periods. We solicit
comment on this proposed revised approach in light of the information
provided by petitioners regarding the need for prompt Hg emissions
information.
Our review of the data in the record shows that for reasonable,
shorter sampling conditions--30-minute samples obtained at a sampling
rate of 0.5 liter per minute--the UPL-determined new source Hg limit is
less than the 3 X RDL value. Therefore, we are proposing to set the Hg
limit for the non-low rank virgin coal subcategory at the 3 X RDL
value.
Although the value of the resulting limit we are proposing today is
higher than that in the final rule, we do not expect this change to
alter the emission control strategy of a new EGU, as both emission
limits result in Hg removal efficiency in excess of 97 percent.
However, the proposed change will improve EGU owners' and operators'
ability to track emissions and take preemptive actions to ensure
compliance. Based on information provided by the petitioners, our
experience, and the National Institute of Standards and Technology's
recently confirmed capability to certify Hg calibration gas generators
down to 0.2 micrograms per cubic meter ([mu]g/m\3\), the proposed
change in the Hg limit will also allow the option of using a Hg CEMS
for process control and for determining compliance.
Please refer to the memo ``Data and Procedure for Handling Below
Detection Level Data in Analyzing Various Pollutant Emissions Databases
for MACT and RTR Emissions Limits'' (docket entry EPA-HQ-OAR-2009-0234-
20062) for a discussion of the RDL approach generally, and the memo
``Determination of Representative Detection Level (RDL) and 3 X RDL
Values for Mercury Measured Using Sorbent Trap Technologies''
(rulemaking docket EPA-HQ-OAR-2009-0234) for a discussion of our
approach for establishing an RDL for Hg. The proposed limit is
presented in table 1 of this preamble.
[[Page 71327]]
4. Limits for New IGCC EGUs--Use of Permit Limits From Unconstructed
IGCC EGUs
We are granting reconsideration of the finalized new source
integrated gasification combined cycle (IGCC) limits. The EPA used the
permit limits from IGCC EGUs that are permitted but not yet constructed
as the basis for some of the final new source IGCC emission limits.
Some petitioners asserted that the EPA did not use this approach in the
notice of proposed rulemaking and that they therefore were deprived of
the opportunity to comment on this approach.
Although we indicated that we considered establishing standards
based on IGCC permits at proposal, we are granting reconsideration on
the new source IGCC limits so that the public has an additional
opportunity to comment on the limits and the approach.
Specifically, we request comment on the proposed new source IGCC
standards, which are unchanged from the final standards promulgated for
these units on February 16, 2012. These proposed new source limits are
presented in tables 1 and 2 of this preamble.
5. Beyond-the-Floor Analysis
The MACT floor level of control for new EGUs is based on the
emission control that is achieved in practice by the best controlled
similar source, as determined by the Agency, of each HAP for the
different subcategories. After the EPA establishes MACT floor levels,
CAA section 112(d)(2) requires the EPA to consider whether more
stringent beyond-the-floor standards should be established. Under that
section, the Agency must consider ``the cost of achieving such emission
reduction, and any non-air quality health and environmental impacts and
energy requirements'' before it may establish a standard that is based
on a beyond-the-floor level of control.
For most of the new source standards addressed in this proposal, we
have not identified additional technologies or HAP emission reduction
approaches that would achieve HAP reductions greater than the new
source floors for the subcategories, other than multiple controls in
series (e.g., multiple scrubbers in series or multiple PM controls in
series), which we consider to be unreasonable from a cost perspective.
We are therefore proposing to adopt the floor level of control for all
but one of these standards. We are proposing a beyond-the-floor
standard for HCl emissions from coal-fired EGUs. Summaries of the EPA's
beyond-the-floor evaluations for the new source standards addressed in
this proposal are provided below. Additional detail of these analyses,
including a discussion of costs and non-air quality health and
environmental impacts, is provided in the ``MATS Reconsideration:
Beyond-the-Floor Memorandum'' available in rulemaking docket EPA-HQ-
OAR-2009-0234. We request comment on all aspects of our beyond-the-
floor analysis. Specifically, we solicit comment on whether there are
any control technologies or HAP emission reduction practices that have
been demonstrated to achieve HAP reductions at levels lower than the
standards proposed in this notice consistently and in a cost-effective
manner. Comments should include information on emissions, pollutant
control efficiencies, operational reliability, current demonstrated
applications, and costs.
a. Beyond-the-floor analysis for PM from coal-fired EGUs. It is
commonly accepted that a baghouse fabric filter (FF) is the technology
that provides the best level of PM emission reduction for coal-fired
EGUs. Newly constructed coal-fired EGUs will be expected to install FFs
to meet the new source NESHAP PM limit that we are proposing in this
notice and the applicable NSPS limit. We have considered available
options that would allow a new source to achieve greater emission
reductions than those achieved in practice by the best controlled
source. The EPA is aware that some EGUs have installed downstream
secondary ``polishing'' PM control devices to provide for incremental
PM reductions beyond what is achieved by the primary PM control device.
However, those ``polishing'' PM control devices are most often
installed for one of two purposes: (1) To augment the control of an
underperforming or undersized primary control device or (2) to allow
for injection of activated carbon or other powdered sorbent so that the
fly ash and the sorbent remain separated for eventual storage,
disposal, or re-use. Given that a new coal-fired EGU would have the
opportunity to design the primary PM control device to meet the new
source emission limit, we can see no justification for including in the
design a secondary downstream ``polishing'' PM control device. Such a
device would add considerable cost to the project, and the incremental
cost-effectiveness would not be reasonable. See ``MATS Reconsideration:
Beyond-the-Floor Memorandum'' in rulemaking docket EPA-HQ-OAR-2009-
0234.
b. Beyond-the-floor analysis for Hg from new coal-fired EGUs
designed for coal >= 8300 Btu/lb. The proposed new source Hg emission
limit for EGUs firing non-low rank virgin coal is based on the use of
the 3 X RDL approach. As explained above, there is concern that a lower
emission limit could not be reliably measured with sufficient frequency
to allow consistent and timely compliance. For this reason, we are not
proposing a limit based on a beyond-the-floor level of control, and,
instead, we are proposing to establish the standard at the MACT floor
level.
c. Beyond-the-floor analysis for SO2 emissions from
coal-fired EGUs. The best performing source for SO2
emissions from a coal-fired EGU is a circulating fluidized bed
combustor (CFB) with limestone injection for SO2 control and
a downstream circulating dry scrubber (CDS) for supplemental
SO2 control. Because the EGU already employs a downstream
``polishing'' SO2 control device, we do not believe that
installation of an additional ``polishing'' control device would result
in cost-effective reduction (in $/ton of incremental SO2
reduction) that would justify setting a beyond-the-floor emission
limit. See ``MATS Reconsideration: Beyond-the-Floor Memorandum'' in
rulemaking docket EPA-HQ-OAR-2009-0234.
d. Beyond-the-floor analysis for PM from solid oil-derived fuel-
fired EGUs. This analysis is very similar to that which was presented
earlier for PM emissions from coal-fired EGUs. Given that a new solid
oil-derived fuel-fired EGU would have the opportunity to design the
primary PM control device to meet the new source emission limit, we can
see no justification for including in the design a secondary downstream
``polishing'' PM control device. As with the coal-fired source, such a
device would add considerable costs to the project, and the incremental
cost-effectiveness would not be reasonable.
e. Beyond-the-floor analysis for SO2 from solid oil-
derived fuel-fired EGUs. The best performing source for SO2
emissions from solid oil-derived fuel-fired EGUs is a CFB combustor
with limestone injection for SO2 control. Additional
SO2 control, beyond that which is obtained by the best
controlled source, may be obtained by installing a downstream
SO2 control device such as a spray drier absorber (SDA) or
wet-flue gas desulfurization (wet-FGD) scrubber or, as was the case
with the best performing coal-fired unit, a CDS. However, as stated
earlier, we believe that, in this case, the installation of additional
downstream ``polishing'' control technologies does not result in
[[Page 71328]]
cost-effective control (in $/ton of incremental SO2
reduction) that would justify setting a beyond-the-floor emission
limit.
f. Beyond-the-floor analysis for PM from continental liquid oil
fuel-fired EGUs. The proposed new source filterable PM emission limit
for continental liquid oil-fired fuel is based on an EGU which uses an
electrostatic precipitator (ESP). Distillate oil-fired facilities do
not need add-on PM controls, as their emissions are inherently low, and
residual oil-fired units cannot use FFs for PM control due to concerns
about bag contamination and fire safety. ESPs are the best filterable
PM control technology for liquid oil fuel-fired EGUs. Given that a new
continental liquid-oil fuel-fired EGU would have the opportunity to
design the primary PM control device to meet the new source emission
limit, we can see no justification for including in the design a
secondary downstream ``polishing'' PM control device. Such a device
would add considerable costs to the project, and the incremental cost-
effectiveness would not be reasonable.
g. Beyond-the-floor analysis for HAP emissions from IGCC EGUs. We
have no data upon which to assess whether or not technologies exist
that can provide additional HAP control beyond the proposed new source
emission limits for new IGCC units. Accordingly, we are not proposing
to establish beyond-the-floor emission limitations for these pollutants
for new IGCC units. We request comment on whether the use of any
control technologies or practices have been demonstrated to
consistently achieve in a cost-effective manner, emission levels for
similar sources that are lower than those proposed for new IGCC sources
in this proposal. Comments should include information on emissions,
pollutant control efficiencies, operational reliability, current
demonstrated applications, and costs.
h. Beyond-the-floor analysis for HCl emissions from coal-fired
EGUs. For HCl, the EPA's revised floor analysis for coal units--
discussed above--resulted in a revised MACT floor of 2.0E-2 pound per
megawatt-hour (lb/MWh). We have estimated that a new coal-fired EGU
would need to remove HCl in the range of 81.0 to 96.6 percent
(depending upon the initial chlorine (Cl) content of the fuel) in order
to meet this revised MACT floor level of control for HCl emissions. We
also note that it is reasonable to expect that in most, if not all,
cases, advanced FGD control technology (such as a wet-FGD scrubber or a
high efficiency SDA) would be required as a result of other federal
requirements--specifically a prevention of significant deterioration
(PSD) best available control technology (BACT) analysis. More detailed
discussion may be found in the memo ``MATS Reconsideration: Control
Technology Needed to Meet New Source Limits'' contained in rulemaking
docket EPA-HQ-OAR-2009-0234.
A high efficiency SDA is less costly than a wet-FGD, and we think
it likely that some new sources will be able to comply with PSD/BACT
requirements using that less expensive option.\4\ For this reason, we
believe that it is reasonable to assume the minimum level of
performance for HCl control from a new EGU will be equivalent to that
of a well-performing SDA for purposes of the beyond-the-floor analysis.
We examined the level of HCl control achieved by those EGUs from the
2010 utility information collection request (ICR) database that were
equipped with SDA and we determined that those EGUs achieved HCl
control in a range of 90 to 98 percent (coal-to-stack, depending on the
coal Cl content).\5\
---------------------------------------------------------------------------
\4\ New Source Review (NSR) permit requirements include, among
other things, the application of BACT (best available control
technology) under PSD. BACT control technology determinations and
associated emission limit establishment involve case-by-case
analyses and, such analyses take into account site-specific factors
such as energy, environmental and economic impacts. For that reason,
it is impossible to strictly predict the outcome of such analyses.
However, based on recent BACT determinations for SO2
emissions from coal-fired EGUs, it is reasonable to expect that in
most, if not all, cases, flue gas desulfurization control
technologies (such as wet-FGD scrubbers or high efficiency spray
drier absorbers) would be required (see https://cfpub.epa.gov/RBLC/).
\5\ Note that the HCl emission levels achieved are very similar
for all EGUs. The difference observed in level of control
(percentage) is due to the difference in chlorine levels seen in
various coals.
---------------------------------------------------------------------------
We, therefore, are proposing to set a beyond-the-floor HCl emission
limit for new coal-fired EGUs at 1.0E-2 lb/MWh. We believe that a new
EGU firing lower Cl-content coal would need to achieve a minimum of 90
percent control to meet this proposed limit and that a new EGU firing a
higher Cl-content coal would need to achieve a minimum of 98 percent
control to meet the limit. We believe that this beyond-the-floor
emission limit is cost-effective because it does not involve additional
cost, as we expect that any new unit will install at least a high
efficiency SDA to comply with other CAA requirements.
We also considered a beyond-the-floor emission limit by assuming
installation of a wet-FGD scrubber, which generally achieves greater
HCl reductions, but at a greater cost, than a high efficiency SDA. We
understand that some new coal-fired EGUs will likely be required to
install this type of advanced FGD technology for SO2
control. However, if the EGU is not required to install a wet-FGD
scrubber from the PSD BACT determination for SO2, then the
additional costs beyond those for a high efficiency SDA would be
attributable to the achievement of additional HCl emission reductions,
and the cost-effectiveness would not be reasonable.
6. Proposed New Source Emission Limits
For coal-fired EGUs, the final rule regulates HCl as a surrogate
for acid gas HAP, with an alternative equivalent standard for
SO2 as a surrogate for acid gas HAP for coal-fired EGUs with
FGD systems installed and operational; filterable PM as a surrogate for
non-mercury HAP metals, with total non-mercury HAP metals and
individual non-mercury HAP metals as alternative equivalent standards;
Hg; and organic HAP. For oil-fired EGUs, the final rule regulates HCl
and HF; filterable PM as a surrogate for total HAP metals, with
individual HAP metals as alternative equivalent standards; and organic
HAP. The filterable PM, HCl, and Hg limits that we are proposing to
revise are provided in table 1; the alternate limits that we are
proposing to revise are provided in table 2. We are soliciting comment
on the revised new source emission limits proposed in this action.\6\
---------------------------------------------------------------------------
\6\ Tables 1 and 2 in this preamble set forth the new source
limits the Agency is proposing to revise. However, to comply with
Federal Register guidelines, ``Table 1 to Subpart UUUUU of Part 63--
Emission Limits for New or Reconstructed EGUs'' in the regulatory
text includes all of the new source limits, including the limits
that are not proposed to be revised and are not part of this
reconsideration action. The EPA is only accepting comments on the
new source limits that are set forth in tables 1 and 2 of this
preamble, which are the limits that are the subject of this
reconsideration action.
[[Page 71329]]
Table 1--Proposed Emission Limitations for New EGUs
----------------------------------------------------------------------------------------------------------------
Filterable particulate
Subcategory matter Hydrogen chloride Mercury
----------------------------------------------------------------------------------------------------------------
New--Unit not designed for 9.0E-2 lb/MWh............. 1.0E-2 lb/MWh \a\......... 3.0E-3 lb/GWh.
low rank virgin coal.
New--Unit designed for low 9.0E-2 lb/MWh............. 1.0E-2 lb/MWh \a\......... NR.
rank virgin coal.
New--IGCC................... 7.0E-2 lb/MWh \b\......... 2.0E-3 lb/MWh \d\......... 3.0E-3 lb/GWh.\e\
9.0E-2 lb/MWh \c\.........
New--Solid oil-derived...... 3.0E-2 lb/MWh............. NR........................ NR.
New--Liquid oil--continental 4.0E-1 lb/MWh............. NR........................ NR.
----------------------------------------------------------------------------------------------------------------
Note: lb/MWh = pounds pollutant per megawatt-hour electric output (gross).
lb/GWh = pounds pollutant per gigawatt-hour electric output (gross).
NR = limit not revised.
\a\ Beyond-the-floor value.
\b\ Duct burners on syngas; based on permit levels in comments received.
\c\ Duct burners on natural gas; based on permit levels in comments received.
\d\ Based on best-performing similar source.
\e\ Based on permit levels in comments received.
Table 2--Proposed Revised Alternate Emission Limitations for New EGUs
----------------------------------------------------------------------------------------------------------------
Subcategory/pollutant Coal-fired EGUs IGCC \a\ Solid oil-derived
----------------------------------------------------------------------------------------------------------------
SO2.................................. 1.0 lb/MWh............. 4.0E-1 lb/MWh \b\...... 1.0 lb/MWh.
Total non-mercury metals............. NR..................... 4.0E-1 lb/GWh.......... NR.
Antimony, Sb......................... NR..................... 2.0E-2 lb/GWh.......... NR.
Arsenic, As.......................... NR..................... 2.0E-2 lb/GWh.......... NR.
Beryllium, Be........................ NR..................... 1.0E-3 lb/GWh.......... NR.
Cadmium, Cd.......................... NR..................... 2.0E-3 lb/GWh.......... NR.
Chromium, Cr......................... NR..................... 4.0E-2 lb/GWh.......... NR.
Cobalt, Co........................... NR..................... 4.0E-3 lb/GWh.......... NR.
Lead, Pb............................. 3.0E-2 lb/GWh.......... 9.0E-3 lb/GWh.......... NR.
Mercury, Hg.......................... NA..................... NA..................... NR.
Manganese, Mn........................ NR..................... 2.0E-2 lb/GWh.......... NR.
Nickel, Ni........................... NR..................... 7.0E-2 lb/GWh.......... NR.
Selenium, Se......................... 5.0E-2 lb/GWh.......... 3.0E-1 lb/GWh.......... NR.
----------------------------------------------------------------------------------------------------------------
NA = not applicable.
NR = limit not revised.
\a\ Based on best-performing similar source unless otherwise noted.
\b\ Based on DOE information.
7. Control Technologies To Meet Proposed New Source Emission Limits
We have evaluated the levels of control that would generally be
needed to meet the proposed emission limits for new sources and have
compared those to the levels of control needed to meet the new source
emission limits in the final MATS rule. We compared the level of
control needed by analyzing requirements for a new hypothetical 500 MW
facility. The comparison led us to conclude that new EGUs would need to
be designed to use the same types of emission control technologies to
meet the proposed new source limits as would have been needed to meet
the final MATS new source limits. More detailed discussion of this
evaluation may be found in the memo ``MATS Reconsideration: Control
Technology Needed to Meet New Source Limits'' contained in rulemaking
docket EPA-HQ-OAR-2009-0234.
Nothing in the statute requires the EPA to demonstrate that an
existing source is able to meet all of the new source limits.
Nevertheless, we note that based on our review of the data EPA
collected as part of the 2010 ICR process, at least eight existing non-
low rank virgin coal-fired EGUs and one low rank virgin coal-fired EGU
have reported short-term stack test data that demonstrate that these
EGUs have in practice achieved the new source limits proposed in this
notice (considering all of their submitted data). Furthermore, for HCl
(as well as the SO2 surrogate) and filterable PM, the new
source limits proposed in this notice are consistent with those in
several permits for EGUs that have not yet commenced construction. For
Hg, the new source limits proposed in this notice are consistent with
the levels that a number of control vendors have suggested in their
petitions for reconsideration are achievable and capable of being
measured with an appropriate level of accuracy.
8. Filterable PM Monitoring
We provided several monitoring options for the filterable PM
standard in the final rule, including quarterly stack testing, PM CEMS,
and PM continuous parameter monitoring system (PM CPMS) with annual
testing. For many reasons, including continued use of already-installed
instruments on some EGUs, direct (as opposed to parametric) measurement
of the pollutant of concern, and continuous feedback for process
control, we believe that many EGU owners or operators will choose to
use PM CEMS to monitor the proposed filterable PM limit.
We solicit comment on whether to retain the quarterly stack testing
compliance option, as this option may not be necessary because
continuous, direct measurement of filterable PM or a correlated
parameter is available and likely to be used by most sources to monitor
compliance with the revised standard.
With respect to the PM CPMS compliance option for new EGUs, we
considered three approaches to establish an operating limit based on
emissions testing. The first approach would allow an EGU owner or
operator to use the highest parameter value obtained during an
individual emissions test when the result of that individual test was
below the limit as the operating limit. The
[[Page 71330]]
second approach would allow an EGU owner or operator to use the average
parameter value obtained from all runs pertaining to an individual
emissions test as the operating limit. The third approach would allow
an EGU owner or operator whose PM emissions as demonstrated during
performance testing do not exceed 75 percent of the PM emissions limit
to set his PM CPMS operating limit by linearly scaling the average
operating value obtained during all the runs to be equivalent to the
value at 75 percent of the limit; an EGU owner or operator whose PM
emissions as demonstrated during performance testing exceed 75 percent
of the PM emissions limit would establish his operating limit as a 30-
day rolling average equal to the average PM CPMS values recorded during
performance testing. Such an approach would prevent unnecessary retests
for EGUs with low PM emissions. See ``75 Percent CPMS Operating Limit
Approach--MATS Reconsideration'' in rulemaking docket EPA-HQ-OAR-2009-
0234.
Even though this rule proposes the first approach, we solicit
comments on the appropriateness of any of the three approaches to
establish a PM CPMS operating limit for new EGUs.
In addition, this rule proposes to require emissions testing after
each exceedance of the operating limit for new sources. This rule
proposes a number of consequences if the PM monitoring parameter is
exceeded. First, the EGU owner or operator will have 48 hours to
conduct an inspection of the control device(s) and to take action to
restore the controls to proper operation, if necessary, and 45 days to
conduct a Method 5 compliance test under the same operating conditions
to verify ongoing compliance with the filterable PM limit. Within 60
days, the EGU owner or operator will have to complete the emissions
sampling, sample analyses, and verification that the EGU is in
compliance with its emissions limit, as well as having to determine an
operating limit based on the PM CPMS data collected during the
performance test. The EGU owner or operator would then compare the
recalculated operating limit with the existing operating limit and, as
appropriate, adjust the numerical operating limit to reflect compliance
performance. Adjustments could include applying the most recently
established value or combining the data collected over multiple
performance tests to establish a more representative value. The EGU
owner or operator would then apply the reverified or adjusted operating
limit value from that time forward.
Second, this rule proposes to limit the number of exceedances of
the site-specific CPMS limit leading to follow-up performance tests in
any 12 month process operating period and that an excess of this number
be considered a violation of the standard. This presumption of
violation could be rebutted by the EGU owner or operator, but would
require more than a Method 5 test as a basis for the rebuttal (e.g.,
results of physical inspections would also need to be included). This
additional information is necessary since a Method 5 test could not be
conducted during or immediately following the discovery of exceedances
and would not necessarily represent conditions identical to those when
the exceedances occurred. The basis for this part of the proposal is
that the site-specific CPMS operating limit reflects a 30-day average
that should represent an actual emissions level lower than the three
test run numerical emissions limit since variability is mitigated over
time. Consequently, we believe that there should be few, if any,
exceedances from the 30-day parametric limit and there is a reasonable
basis for presuming that exceedances that lead to multiple performance
tests to represent poor control device performance and to be a
violation of the standard. Therefore, this rule proposes that PM CPMS
exceedances leading to more than four required performance tests in a
12-month process operating period is presumed to be a violation of this
standard, subject to an EGU owner or operator's ability to rebut that
presumption about process and control device operations in addition to
the Method 5 performance test results. We solicit comment on this
proposed revised approach.
B. Eligibility To Be a New Source
The CAA section 112(a)(4) defines a new source as a stationary
source ``the construction or reconstruction of which is commenced after
the Administrator first proposes regulations under this section
establishing an emissions standard applicable to such source.'' The EPA
views the new source trigger date (the date EPA ``first proposes
regulations'') to be the date EPA first proposes standards under a
particular rulemaking record. (74 FR 21158). In this case, EPA first
proposed standards for EGUs on May 3, 2011, and although we are
proposing revisions to certain new source standards, the rulemaking
record remains the same. As such, we are not proposing to revise the
trigger date for determining whether a source is a new source. Any
source which commenced construction or reconstruction after May 3, 2011
is subject to the new source standards.\7\
---------------------------------------------------------------------------
\7\ We are unaware of any new source that has commenced
construction or reconstruction since May 3, 2011.
---------------------------------------------------------------------------
Furthermore, it is the EPA's technical judgment that new sources
would need to adopt the same or similar emissions control strategies
under the amended standards as they would have under the promulgated
standards. The revised standards remain stringent and can be met, in
our view, using the same or similar control strategies as would have
been required to meet the standards in the final rule.
C. Startup and Shutdown Provisions
The EPA received petitions asserting that the public lacked an
opportunity to comment on the startup and shutdown provisions in the
final MATS. Petitioners also assert that the definitions of ``startup''
and ``shutdown'' in the final MATS and the provisions for work practice
standards did not adequately address applicability to certain types of
units, fuels considered ``clean,'' and operational limitations for
certain EGU types and/or pollution control devices.
We proposed numerical standards for startup and shutdown periods,
and in response to comments on the proposed rule we changed those
standards in the final MATS to work practice standards. Among other
things, the work practice standards required sources to combust clean
fuels during startup and shutdown periods and required sources to
engage APCDs when coal or oil was fired in the EGU. (See 77 FR 9380-
83). We also revised the definitions of ``startup'' and ``shutdown''
after considering comments we received. Although we revised these
provisions in response to comments, we are granting reconsideration on
this issue to provide an opportunity for comment on the final startup
and shutdown standards and those we have revised and propose today. For
further discussion of petitioners' concerns and these proposed
revisions, please refer to the memo ``Startup and shutdown provisions''
in rulemaking docket EPA-HQ-OAR-2009-0234. Below we summarize the
startup and shutdown revisions proposed today.
1. Definitions
We are proposing to revise the definitions of startup and shutdown
in this reconsideration notice as set forth in 40 CFR 63.10042.
Petitioners asserted that the final rule's definitions of startup and
shutdown were not sufficiently clear, should accommodate operation of
[[Page 71331]]
cogeneration units, and did not accurately reflect startup conditions
for all affected units, particularly supercritical units. We have
clarified the definitions and added provisions including useful thermal
energy.\8\ We believe that these changes address petitioners' concerns.
For more discussion, please refer to the memo ``Startup and shutdown
provisions'' in rulemaking docket EPA-HQ-OAR-2009-0234.
---------------------------------------------------------------------------
\8\ 16 U.S.C. 796(18)(A) and 18 CFR 292.202(c).
---------------------------------------------------------------------------
2. Work Practice Standards
We are proposing several revisions to the finalized work practice
standards. Petitioners asserted that the final rule's work practice
standards should include certain additional fuels as ``clean fuels''
and recognize operating limitations of certain EGU types and APCDs.
Specifically, petitioners contend that the list of clean fuels required
for use during startup in order to minimize emissions should include
synthetic natural gas, syngas, and ultra-low sulfur diesel (ULSD). The
EPA has also been informed since the final rule that propane is used to
startup some EGUs and has been requested to consider it as a clean
fuel. Petitioners additionally contend that the standards need to
recognize operating conditions for FBC EGUs that inject limestone for
acid gas control, selective non-catalytic reduction systems (SNCRs),
selective catalytic reduction systems (SCRs), and other systems.
In this reconsideration notice, we are proposing to add certain
synthetic natural gas, syngas, propane, and ULSD to the list of clean
fuels. We solicit comment on our understanding of clean fuels for
startup and shutdown.
We are also proposing to require EGU source owners and operators,
when firing coal, solid oil-derived fuel, or residual oil in the EGU
during startup or shutdown, to vent emissions to the main stack(s) and
operate all control devices necessary to meet the operating standards
that apply at all other times under the final rule (with the exception
of limestone injection in FBC EGUs, dry scrubbers, SNCRs, and SCRs).
Owners and operators of EGUs are responsible for starting limestone
injection in FBC EGUs, dry scrubbers, SNCRs, and SCRs as expeditiously
as possible, but, in any case, when necessary to comply with other
standards applicable to the source that require operation of those
control devices.
Additionally, we are proposing to revise the final rule's work
practice requirements to recognize constraints of certain EGUs and
APCDs. The proposed revised standards allow limestone injection to
start after appropriate temperatures have been attained in FBC EGUs
that inject limestone for acid gas control and allow SNCR, SCR, and dry
scrubber systems to start as soon as technically feasible after the
appropriate temperature has been reached.
For more discussion of each of these issues, please refer to the
memo ``Startup and shutdown provisions'' in rulemaking docket EPA-HQ-
OAR-2009-0234.
3. Treatment of IGCC EGU Syngas
The EPA understands that at an IGCC EGU, syngas is generated in the
gasifier and combusted in the turbine. During the startup and shutdown
periods, some or all of the syngas produced may not be combusted in the
turbine. We are proposing two options for IGCC EGUs for handling syngas
not fired in the combustion turbine: (1) syngas must be flared, not
vented or (2) syngas must be routed to duct burners, which may need to
be installed, and the flue gas from the duct burners must be routed to
the heat recovery steam generator. We are soliciting comments on the
need to flare the unfired syngas, if it is more appropriate to require
routing of the unfired syngas back into the system for all IGCC EGUs,
and on the costs of adding duct burners, should they be required.
We solicit comments on the proposed revisions to the startup and
shutdown requirements set forth in this notice.
V. Discussion of Provisions Subject To Reconsideration--Utility NSPS
Petitioners state that because the final Utility NSPS rule contains
a definition of ``natural gas'' that was not included in the proposed
rule, they were not able to comment on the definition. Further,
petitioners maintain that the definition established in the final rule
is not a ``logical outgrowth'' of the proposed rule. Although the
definition was changed between proposal and final based on public
comment, we are re-proposing the definition of natural gas that was in
the final Utility NSPS to allow additional opportunity to comment.
We are also proposing several additional amendments so that
synthetic natural gas will receive similar treatment as natural gas. We
seek comment on all aspects of these additional amendments. First,
consistent with the NESHAP definition, we are proposing to clarify the
definition of coal to include synthetic natural gas derived from coal.
As such, we are also proposing to add synthetic natural gas to the
opacity exemption in paragraph 40 CFR 60.42Da(b)(2) since facilities
burning synthetic natural gas would otherwise be subject to an opacity
standard. In addition, we are also proposing to replace ``natural gas''
with ``gaseous fuels'' in 40 CFR 60.49Da(b) so facilities burning
desulfurized coal-derived synthetic natural gas are not required to
install an SO2 CEMS. The proposed amendments to the startup
and shutdown requirements in the NESHAP portion of this proposal would
also allow the use of synthetic natural gas for the work practice
standards required for PM emissions control during periods of startup
and shutdown.
Additional proposed amendments include amending the definition of
an IGCC to be similar to the corresponding NESHAP MATS definition.
Potential language is as follows:
Integrated gasification combined cycle electric utility steam
generating unit or IGCC electric utility steam generating unit means
an electric utility combined cycle gas turbine that burns a
synthetic gas derived from coal and/or solid oil-derived fuel for
more than 10.0 percent of the average annual heat input during any 3
consecutive calendar years or for more than 15.0 percent of the
annual heat input during any one calendar year in a combined-cycle
gas turbine. No solid coal or solid oil-derived fuel is directly
burned in the unit during operation.
We believe that this would address the issue of IGCC facilities
switching applicability between the stationary combustion turbine NSPS
(40 CFR part 60, subpart KKKK) and the Utility NSPS. However, we are
specifically requesting comment if it would be more appropriate to
maintain the existing NSPS IGCC definition and add ``startup and
commissioning, shutdown'' as suggested by one petitioner. Potential
language for the alternate definition is as follows:
Integrated gasification combined cycle electric utility steam
generating unit or IGCC electric utility steam generating unit means
an electric utility combined cycle gas turbine that is designed to
burn fuels containing 50 percent (by heat input) or more solid-
derived fuel not meeting the definition of natural gas. The
Administrator may waive the 50 percent solid-derived fuel
requirement during periods of the gasification system construction,
startup and commissioning, shutdown, or repair. No solid fuel is
directly burned in the unit during operation.
In addition, the rationale for the filterable PM standard startup
and shutdown work practice provision discussed in the NESHAP portion of
this notice also applies to the filterable PM startup and shutdown
standards in the Utility NSPS. Therefore, we are proposing to amend
both the emissions
[[Page 71332]]
rate calculation procedure and monitoring requirements for PM to be
similar to the requirements specified in the NESHAP for new facilities.
Owners/operators of EGUs subject to the Utility NSPS would calculate
the filterable PM emissions rate as the average of the measured hourly
rates during the applicable averaging period (instead of as the sum of
the emissions divided by the sum of the output over the applicable
averaging period) and would use either a PM CEMS, PM CPMS, or quarterly
performance testing to demonstrate compliance with the applicable
standard.\9\
---------------------------------------------------------------------------
\9\ As discussed in the final Utility NSPS Response to Comments
document, because the amended NOX and SO2
standards used CEMS data and included all periods of operation when
establishing the numerical values for those standards, we are not
proposing to amend how periods of startup and shutdown are handled
or how the emission rates are calculated for the Utility NSPS
NOX and SO2 standards. See docket entry EPA-
HQ-OAR-2011-0044-5759, p. 7.
---------------------------------------------------------------------------
Finally, we are proposing to clarify that owners/operators electing
to use PM CPMS to monitor PM emissions are exempt from the requirement
to install a continuous opacity monitoring system (COMS) and would be
allowed to elect to use alternate opacity monitoring procedures
currently allowed in the Utility NSPS.
VI. Technical Corrections and Clarifications
On April 19, 2012 (77 FR 23399), we issued a technical corrections
notice addressing certain corrections to the February 16, 2012 (77 FR
9304) MATS.
In this notice, we are proposing several additional technical
corrections. These amendments are being proposed to correct
inaccuracies and other inadvertent errors in the final rule and to make
the rule language consistent with provisions addressed through this
reconsideration. We are soliciting comment only on whether the proposed
changes provide the intended accuracy, clarity and consistency. These
proposed technical changes are described in tables 3 and 4 of this
preamble. We request comment on all of these proposed changes.
Table 3--Miscellaneous Proposed Technical Corrections to 40 CFR Part 60,
Subpart Da
------------------------------------------------------------------------
Section of subpart Da Description of proposed correction
------------------------------------------------------------------------
40 CFR 60.42Da(a)............ Correct the erroneous ``0.030'' to the
correct ``0.03.''
40 CFR 60.42Da(e)(1)(ii)..... Correct the erroneous conversion ``13 ng/
J (0.015 lb/MMBtu)'' to the correct
``6.4 ng/J (0.015 lb/MMBtu)'' by
amending the regulatory text to specify
that the requirements in 40 CFR
60.42Da(c) or (d), which includes two
additional alternative limits, are
available compliance alternatives for
modified facilities.
------------------------------------------------------------------------
Table 4--Miscellaneous Proposed Technical Corrections to 40 CFR Part 63,
Subpart UUUUU
------------------------------------------------------------------------
Section of subpart UUUUU Description of proposed correction
------------------------------------------------------------------------
40 CFR 63.9982(a)............ Clarify the language to use the word
``or'' instead of ``and.''
40 CFR 63.9982(b) and (c).... Correct the discrepancy between
63.9982(b) and (c) and 63.9985(a).
40 CFR 63.10005(d)(2)(ii).... Correct the typographical error by
replacing the incorrect
``corresponding'' with the correct
``corresponds.''
40 CFR 63.10005(i)(4)(ii) and Revise to clarify the determination and
(i)(5) and add measurement of fuel moisture content.
63.10005(i)(6).
40 CFR 63.10006(c)........... Correct the omission of solid oil-derived
fuel- and coal-fired EGUs and IGCC EGUs
and the omission of section 10000(c).
40 CFR 63.10007(c)........... Correct the omission of section 63.10023
from the list of sections to be followed
in establishing an operating limit.
40 CFR 63.10009(b)(2)........ Correct omission of the term ``boiler
operating'' and clarify the term ``Rti''
in Equation 2a.
40 CFR 63.10009(b)(3)........ Correct omission of the term ``system''
and clarify the term ``Rti'' in Equation
3a.
40 CFR 63.10010(j)(1)(i)..... Correct the typographical error to use
the correct word ``your'' instead of
``you.''
40 CFR 63.10011(g)........... Clarify the language to use the word
``and'' instead of ``or'' between the
words ``startup'' and ``shutdown.''
Clarify the language to use the word
``or'' instead of ``and'' between the
words ``oil-fired'' and ``solid.''
40 CFR 63.10030(b), (c), and Clarify the affected-source language.
(d).
Change the period by which a Notification
of Intent to conduct a performance test
must be submitted to conform to the
General Provisions.
40 CFR Section 63.10042...... Revise the definition of ``boiler
operating day'' to clarify that periods
of startup or shutdown are not included.
Correct the typographical error in the
intended definition of ``unit designed
for coal >= 8,300 Btu/lb subcategory''
by replacing the erroneous ``>'' with
the correct ``>=.''
Table 5 to Subpart UUUUU of Correct the typographical error in
Part 63. footnote 4 by replacing the erroneous
``>='' with the correct ``<=.''
Table 7 to Subpart UUUUU of Clarify the applicability of the
Part 63. alternate 90-day average for Hg in item
1.
Revise item 3 in the table to clarify use
of CMS for liquid oil-fired EGUs.
Section 4.1 to Appendix A to Correct the typographical error by
Subpart UUUUU of Part 63. replacing the incorrect citation to
``Sec. 63.10005(g)'' with the correct
``Sec. 63.9984(f).''
Section 5.2.2.2 to Appendix A Correct the typographical error by
to Subpart UUUUU of Part 63. replacing the incorrect citation to
``Table A-4'' with the correct ``Table A-
2.''
Section 3.1.2.1.3 to Appendix Correct the typographical error by
B to Subpart UUUUU of Part replacing the erroneous ``>='' with the
63. correct ``<=.''
Section 5.3.4 to Appendix B Correct the section number from the
to Subpart UUUUU of Part 63. incorrect ``5.3.4'' to the correct
``5.3.3.''
------------------------------------------------------------------------
[[Page 71333]]
VII. Impacts of This Proposed Rule
Summary of Emissions Impacts, Costs and Benefits
Our analysis shows that new EGUs would choose to install and
operate the same or similar air pollution control technologies in order
to meet the revised emission limits as would have been necessary to
meet the previously finalized standards. We project that this rule will
result in no significant change in costs, emission reductions, or
benefits.\10\ Even if there were changes in costs for these units, such
changes would likely be small relative to both the overall costs of the
individual projects and the overall costs and benefits of the final
rule, which is dominated by actions taken by existing units. Further,
as noted elsewhere in this preamble, we believe that EGUs would put on
the same controls for this proposed rule that they would have for the
original final, so there should not be any incremental costs related to
this proposed revision.
---------------------------------------------------------------------------
\10\ See ``Regulatory Impact Analysis for the Final Mercury and
Air Toxics Standards [EPA-452/R-11-011]'' (docket entry EPA-HQ-OAR-
2009-0234-20131) and the memo ``Economic Impact Analysis for the
Proposed Reconsideration of the Mercury and Air Toxics Standards''
in rulemaking docket EPA-HQ-OAR-2009-0234. As noted earlier,
because, on an individual EGU-by-EGU basis we anticipate very
similar costs, any changes to the baseline since we finalized MATS
(e.g., potential impacts of the CSAPR decision) would not impact
this determination.
---------------------------------------------------------------------------
A. What are the air impacts?
We believe that electric power companies will install the same or
similar control technologies to comply with the revised standards
proposed in this action as they would have installed to comply with the
previously finalized standards. Accordingly, we believe that this
proposed rule will not result in significant changes in emissions of
any of the regulated pollutants.
B. What are the energy impacts?
This proposed rule is not anticipated to have an effect on the
supply, distribution, or use of energy. As previously stated, we
believe that electric power companies would install the same or similar
control technologies as they would have installed to comply with the
previously finalized standards.
C. What are the compliance costs?
We believe there will be no significant change in compliance costs
as a result of this proposed rule because electric power companies
would install the same or similar control technologies as they would
have installed to comply with the previously finalized standards.
Moreover, we find no additional monitoring costs are necessary to
comply with the proposed rule; however, as in any other rule, EGU
owners or operators may choose to conduct additional monitoring (and
incur its expense) for their own purposes.
D. What are the economic and employment impacts?
Because we expect that electric power companies would install the
same or similar control technologies to meet the standards proposed in
this action as they would have chosen to comply with the previously
finalized standards, we do not anticipate that this proposed rule will
result in significant changes in emissions, energy impacts, costs,
benefits, or economic impacts. Likewise, we believe this rule will not
have any impacts on the price of electricity, employment or labor
markets, or the U.S. economy.
E. What are the benefits of the proposed standards?
As previously stated, the EPA anticipates the power sector will not
incur significant compliance costs or savings as a result of this
proposal and we do not anticipate any significant emission changes
resulting from this rule. Therefore, there are no direct monetized
benefits or disbenefits associated with this proposed rule.
VIII. Statutory and Executive Order Reviews
A. Executive Order 12866: Regulatory Planning and Review and Executive
Order 13563: Improving Regulation and Regulatory Review
Under Executive Order (E.O.) 12866 (58 FR 51735, October 4, 1993),
this action is a ``significant regulatory action'' because it ``raises
novel legal or policy issues arising out of legal mandates.''
Accordingly, the EPA submitted this action to the Office of Management
and Budget (OMB) for review under Executive Orders 12866 and 13563 (76
FR 3821, January 21, 2011) and any changes made in response to OMB
recommendations have been documented in the docket for this action.
In addition, the EPA prepared an analysis of the potential costs
and benefits associated with this action. This analysis is contained in
the ``Economic Impact Analysis for the Proposed Reconsideration of the
Mercury and Air Toxics Standards'' found in rulemaking docket EPA-HQ-
OAR-2009-0234. Because our analysis shows that new electricity
generating units would choose to install the same control technology in
order to meet the revised emission limits as would have been necessary
to meet the previously finalized standard, we project that this rule
will result in no significant change in costs, emission reductions, or
benefits.
B. Paperwork Reduction Act
This action does not impose any new information collection burden.
Today's notice of reconsideration does not change the information
collection requirements previously finalized and, as a result, does not
impose any additional burden on industry. However, OMB has previously
approved the information collection requirements contained in the
existing regulations (see 77FR 9304) under the provisions of the
Paperwork Reduction Act, 44 U.S.C. 3501 et seq. and has assigned OMB
control number 2060-0567). The OMB control numbers for EPA's
regulations are listed in 40 CFR part 9 and 48 CFR chapter 15.
C. Regulatory Flexibility Act
The Regulatory Flexibility Act generally requires an agency to
prepare a regulatory flexibility analysis of any rule subject to notice
and comment rulemaking requirements under the Administrative Procedure
Act or any other statute unless the agency certifies that the rule will
not have a significant economic impact on a substantial number of small
entities. Small entities include small businesses, small not-for-profit
enterprises, and small governmental jurisdictions.
For purposes of assessing the impacts of today's notice of
reconsideration on small entities, a small entity is defined as: (1) A
small business as defined by the Small Business Administration's (SBA)
regulations at 13 CFR 121.201; (2) a small governmental jurisdiction
that is a government of a city, county, town, school district, or
special district with a population of less that 50,000; and (3) a small
organization that is any not-for-profit enterprise which is
independently owned and operated and is not dominant in its field.
Categories and entities potentially regulated by the final rule with
applicable NAICS codes are provided in the Supplementary Information
section of this action.
According to the SBA size standards for NAICS code 221122
Utilities-Fossil Fuel Electric Power Generation, a firm is small if,
including its affiliates, it is primarily engaged in the generation,
transmission, and or distribution of electric energy for sale and its
total electric output for the preceding fiscal year did not exceed 4
million MWh.
[[Page 71334]]
After considering the economic impacts of today's notice of
reconsideration on small entities, I certify that the notice will not
have a significant economic impact on a substantial number of small
entities.
The EPA has determined that none of the small entities will
experience a significant impact because the notice of reconsideration
imposes no additional regulatory requirements on owners or operators of
affected sources. We have therefore concluded that today's notice of
reconsideration will not result in a significant economic impact on a
substantial number of small entities. We continue to be interested in
the potential impacts of the rule on small entities and welcome
comments on issues related to such impacts.
D. Unfunded Mandates Reform Act
This action contains no Federal mandates under the provisions of
Title II of the Unfunded Mandates Reform Act of 1995 (UMRA), 2 U.S.C.
1531-1538 for State, local, or tribal governments or the private
sector. The action imposes no enforceable duty on any state, local, or
tribal governments or the private sector. Therefore, this action is not
subject to the requirements of UMRA sections 202 or 205.
This action is also not subject to the requirements of UMRA section
203 because it contains no regulatory requirements that might
significantly or uniquely affect small governments because it contains
no requirements that apply to such governments or impose obligations
upon them.
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, as
specified in EO 13132. None of the affected facilities are owned or
operated by state governments, and the requirements discussed in
today's notice will not supersede state regulations that are more
stringent. Thus, EO 13132 does not apply to today's notice of
reconsideration.
In the spirit of EO 13132, and consistent with EPA policy to
promote communications between EPA and state and local governments, EPA
specifically solicits comment on this notice of reconsideration from
state and local officials.
F. Executive Order 13175: Consultation and Coordination With Indian
Tribal Governments
This action does not have tribal implications. It will not have
substantial direct effects on tribal governments, on the relationship
between the Federal government and Indian tribes, or on the
distribution of power and responsibilities between the Federal
government and Indian tribes, as specified in EO 13175. No affected
facilities are owned or operated by Indian tribal governments. Thus, EO
13175 does not apply to today's notice of reconsideration. The EPA
specifically solicits comment on this notice of reconsideration from
tribal officials.
G. Executive Order 13045: Protection of Children From Environmental
Health Risks and Safety Risks
This action is not subject to EO 13045 (62 FR 19885, April 23,
1997) because it is not economically significant as defined in EO
12866. The EPA has evaluated the environmental health or safety effects
of the final Mercury and Air Toxics Standards on children. The results
of the evaluation are discussed in that final rule (77 FR 9304;
February 16, 2012) and are contained in rulemaking docket EPA-HQ-OAR-
2009-0234.
The public is invited to submit comments or identify peer-reviewed
studies and data that assess effects of early life exposure to
hazardous air pollutants.
H. Executive Order 13211: Actions That Significantly Affect Energy
Supply, Distribution, or Use
This action is not a ``significant energy action'' as defined in EO
13211 (66 FR 28355; May 22, 2001) because it is not likely to have a
significant adverse effect on the supply, distribution, or use of
energy. Further, we conclude that today's notice of reconsideration is
not likely to have any adverse energy effects because it is not
expected to impose any additional regulatory requirements on the owners
of affected facilities.
I. National Technology Transfer and Advancement Act
Section 12(d) of the National Technology Transfer and Advancement
Act (NTTAA) of 1995 (Pub. L. 104-113; 15 U.S.C. 272 note) directs EPA
to use voluntary consensus standards in their regulatory and
procurement activities unless to do so would be inconsistent with
applicable law or otherwise impracticable. Voluntary consensus
standards are technical standards (e.g., material specifications, test
methods, sampling procedures, business practices) developed or adopted
by one or more voluntary consensus bodies. The NTTAA requires EPA to
provide Congress, through the OMB, with explanations when EPA decides
not to use available and applicable voluntary consensus standards.
During the development of the final rule, EPA searched for
voluntary consensus standards that might be applicable. The search
identified three voluntary consensus standards that were considered
practical alternatives to the specified EPA test methods. An assessment
of these and other voluntary consensus standards is presented in the
preamble to the final rule (77 FR 9441; February 16, 2012). Today's
notice of reconsideration does not propose the use of any additional
technical standards beyond those cited in the final rule. Therefore,
EPA is not considering the use of any additional voluntary consensus
standards for this notice.
The EPA welcomes comments on this aspect of this notice of
reconsideration and, specifically, invites the public to identify
potentially-applicable voluntary consensus standards and to explain why
such standards should be used in this regulation.
J. Executive Order 12898: Federal Actions To Address Environmental
Justice in Minority Populations and Low-Income Populations
Executive Order 12898 (59 FR 7629 (Feb. 16, 1994)) establishes
federal executive policy on environmental justice. Its main provision
directs federal agencies, to the greatest extent practicable and
permitted by law, to make environmental justice part of their mission
by identifying and addressing, as appropriate, disproportionately high
and adverse human health or environmental effects of their programs,
policies, and activities on minority populations and low-income
populations in the United States.
The EPA has determined that this notice of reconsideration will not
have disproportionately high and adverse human health or environmental
effects on minority or low-income populations because it does not
affect the level of protection provided to human health or the
environment. Our analysis shows that new EGUs would choose to install
the same control technology in order to meet the revised emission
limits as would have been necessary to meet the previously finalized
standard. Under the relevant assumptions, we project that this rule
will result in no significant change in emission reductions.
[[Page 71335]]
List of Subjects in 40 CFR Parts 60 and 63
Environmental protection, Administrative practice and procedure,
Air pollution control, Hazardous substances, Intergovernmental
relations, Reporting and recordkeeping requirements.
Dated: November 16, 2012.
Lisa P. Jackson,
Administrator.
For the reasons discussed in the preamble, the EPA proposes to
amend 40 CFR parts 60 and 63 to read as follows:
PART 60--STANDARDS OF PERFORMANCE FOR NEW STATIONARY SOURCES
0
1. The authority citation for part 60 continues to read as follows:
Authority: 42 U.S.C. 7401 et seq.
0
2. Amend Sec. 60.41Da by revising the definitions of ``coal'' and
``integrated gasification combined cycle electric utility steam
generating unit,'' and by adding the definition of ``natural gas'' in
alphabetical order to read as follows:
Sec. 60.41Da Definitions.
* * * * *
Coal means all solid fuels classified as anthracite, bituminous,
subbituminous, or lignite by the American Society of Testing and
Materials in ASTM D388 (incorporated by reference, see Sec. 60.17) and
coal refuse. Synthetic fuels derived from coal for the purpose of
creating useful heat, including but not limited to solvent-refined
coal, gasified coal, coal-oil mixtures, and coal-water mixtures are
included in this definition for the purposes of this subpart.
* * * * *
Integrated gasification combined cycle electric utility steam
generating unit or IGCC electric utility steam generating unit means an
electric utility combined cycle gas turbine that burns a synthetic
natural gas derived from coal and/or solid oil-derived fuel for more
than 10.0 percent of the average annual heat input during any 3
consecutive calendar years or for more than 15.0 percent of the annual
heat input during any one calendar year in a combined-cycle gas
turbine. No solid coal or solid oil-derived fuel is directly burned in
the unit during operation.
* * * * *
Natural gas means a fluid mixture of hydrocarbons (e.g., methane,
ethane, or propane), composed of at least 70 percent methane by volume
or that has a gross calorific value between 35 and 41 megajoules (MJ)
per dry standard cubic meter (950 and 1,100 Btu per dry standard cubic
foot), that maintains a gaseous state under ISO conditions. In
addition, natural gas contains 20.0 grains or less of total sulfur per
100 standard cubic feet. Finally, natural gas does not include the
following gaseous fuels: landfill gas, digester gas, refinery gas, sour
gas, blast furnace gas, coal-derived gas, producer gas, coke oven gas,
or any gaseous fuel produced in a process which might result in highly
variable sulfur content or heating value.
* * * * *
0
3. Amend Sec. 60.42Da by revising paragraphs (a), (b)(2), (e)(1)
introductory text, and (e)(1)(ii) to read as follows:
Sec. 60.42Da Standards for particulate matter (PM).
(a) Except as provided in paragraph (f) of this section, on and
after the date on which the initial performance test is completed or
required to be completed under Sec. 60.8, whichever date comes first,
an owner or operator of an affected facility shall not cause to be
discharged into the atmosphere from any affected facility for which
construction, reconstruction, or modification commenced before March 1,
2005, any gases that contain PM in excess of 13 ng/J (0.03 lb/MMBtu)
heat input.
* * * * *
(b) * * *
(2) An owner or operator of an affected facility that combusts only
natural gas and/or synthetic natural gas that chemically meets the
definition of natural gas is exempt from the opacity standard specified
in paragraph (b) of this section.
* * * * *
(e) * * *
(1) On and after the date on which the initial performance test is
completed or required to be completed under Sec. 60.8, whichever date
comes first, the owner or operator shall cause to be discharged into
the atmosphere from that affected facility any gases that contain PM in
excess of the applicable emissions limit specified in paragraphs
(e)(1)(i) or (ii) of this section.
* * * * *
(ii) For an affected facility which commenced modification, any
gases that contain PM in excess of the emission limits specified in
paragraphs (c) or (d) of this section.
* * * * *
0
4. Amend Sec. 60.48Da by revising paragraphs (a), (f), (o)
introductory text, (o)(1), (o)(2) introductory text, (o)(3)
introductory text, (o)(3)(i), and (o)(4) introductory text to read as
follows:
Sec. 60.48Da Compliance provisions.
(a) For affected facilities for which construction, modification,
or reconstruction commenced before May 4, 2011, the applicable PM
emissions limit and opacity standard under Sec. 60.42Da,
SO2 emissions limit under Sec. 60.43Da, and NOX
emissions limit under Sec. 60.44Da apply at all times except during
periods of startup, shutdown, or malfunction. For affected facilities
for which construction, modification, or reconstruction commenced after
May 3, 2011, the applicable SO2 emissions limit under Sec.
60.43Da, NOX emissions limit under Sec. 60.44Da, and
NOX plus CO emissions limit under Sec. 60.45Da apply at all
times. The applicable PM emissions limit and opacity standard under
Sec. 60.42Da apply at all times except during periods of startup and
shutdown; however, you are required to meet the work practice
requirements as specified in 60.42Da(e)(2) of this subpart during
periods of startup and shutdown.
* * * * *
(f) For affected facilities for which construction, modification,
or reconstruction commenced before May 4, 2011, compliance with the
applicable daily average PM emissions limit is determined by
calculating the arithmetic average of all hourly emission rates each
boiler operating day, except for data obtained during startup,
shutdown, or malfunction periods. Daily averages are only calculated
for boiler operating days that have non-out-of-control data for at
least 18 hours of unit operation during which the standard applies.
Instead, all of the non-out-of-control hourly emission rates of the
operating day(s) not meeting the minimum 18 hours non-out-of-control
data daily average requirement are averaged with all of the non-out-of-
control hourly emission rates of the next boiler operating day with 18
hours or more of non-out-of-control PM CEMS data to determine
compliance. For affected facilities for which construction,
modification, or reconstruction commenced after May 3, 2011, compliance
with the applicable 30-boiler operating day rolling average PM
emissions limit is determined by calculating the arithmetic average of
all hourly PM emission rates for the 30 successive boiler operating
days, except for data obtained during periods of startup or shutdown.
* * * * *
(o) Compliance provisions for sources subject to Sec.
60.42Da(c)(2), (d), or (e)(1)(ii). Except as provided for in paragraph
(p) of this section, the owner or operator shall demonstrate
[[Page 71336]]
compliance with each applicable emissions limit according to the
requirements in paragraphs (o)(1) through (o)(5) of this section.
(1) You must conduct a performance test to demonstrate initial
compliance with the applicable PM emissions limit in Sec. 60.42Da by
the applicable date specified in Sec. 60.8(a). Thereafter, you must
conduct each subsequent performance test within 12 calendar months
following the date the previous performance test was required to be
conducted. You must conduct each performance test according to the
requirements in Sec. 60.8 using the test methods and procedures in
Sec. 60.50Da. The owner or operator of an affected facility that has
not operated for 60 consecutive calendar days prior to the date that
the subsequent performance test would have been required had the unit
been operating is not required to perform the subsequent performance
test until 30 calendar days after the next boiler operating day.
Requests for additional 30 day extensions shall be granted by the
relevant air division or office director of the appropriate Regional
Office of the U.S. EPA.
(2) You must monitor the performance of each electrostatic
precipitator or fabric filter (baghouse) operated to comply with the
applicable PM emissions limit in Sec. 60.42Da using a continuous
opacity monitoring system (COMS) according to the requirements in
paragraphs (o)(2)(i) through (vi) unless you elect to comply with one
of the alternatives provided in paragraphs (o)(3) and (o)(4) of this
section, as applicable to your control device.
* * * * *
(3) As an alternative to complying with the requirements of
paragraph (o)(2) of this section, an owner or operator may elect to
monitor the performance of an electrostatic precipitator (ESP) operated
to comply with the applicable PM emissions limit in Sec. 60.42Da using
an ESP predictive model developed in accordance with the requirements
in paragraphs (o)(3)(i) through (v) of this section.
(i) You must calibrate the ESP predictive model with each PM
control device used to comply with the applicable PM emissions limit in
Sec. 60.42Da operating under normal conditions. In cases when a wet
scrubber is used in combination with an ESP to comply with the PM
emissions limit, the wet scrubber must be maintained and operated.
* * * * *
(4) As an alternative to complying with the requirements of
paragraph (o)(2) of this section, an owner or operator may elect to
monitor the performance of a fabric filter (baghouse) operated to
comply with the applicable PM emissions limit in Sec. 60.42Da by using
a bag leak detection system according to the requirements in paragraphs
(o)(4)(i) through (v) of this section.
* * * * *
0
5. Amend Sec. 60.49Da by:
0
a. Revising paragraphs (a) introductory text and (a)(2);
0
b. Adding paragraphs (a)(2)(v) and (a)(3)(iv); and
0
c. Revising paragraphs (a)(4) introductory text, (b) introductory text,
and (t).
The revised and added text reads as follows:
Sec. 60.49Da Emission monitoring.
(a) An owner or operator of an affected facility subject to the
opacity standard in Sec. 60.42Da shall monitor the opacity of
emissions discharged from the affected facility to the atmosphere
according to the applicable requirements in paragraphs (a)(1) through
(4) of this section.
* * * * *
(2) As an alternative to the monitoring requirements in paragraph
(a)(1) of this section, an owner or operator of an affected facility
that meets the conditions in either paragraph (a)(2)(i), (ii), (iii),
(iv), or (v) of this section may elect to monitor opacity as specified
in paragraph (a)(3) of this section.
* * * * *
(v) The owner or operator of the affected facility installs,
calibrates, operates, and maintains a particulate matter continuous
parametric monitoring system (PM CPMS) according to the requirements
specified in subpart UUUUU of part 63.
* * * * *
(3) * * *
(iv) If the maximum 6-minute opacity is less than 10 percent during
the most recent Method 9 of appendix A-4 of this part performance test,
the owner or operator may, as an alternative to performing subsequent
Method 9 of appendix A-4 performance tests, elect to perform subsequent
monitoring using a digital opacity compliance system according to a
site-specific monitoring plan approved by the Administrator. The
observations shall be similar, but not necessarily identical, to the
requirements in paragraph (a)(3)(iii) of this section. For reference
purposes in preparing the monitoring plan, see OAQPS ``Determination of
Visible Emission Opacity from Stationary Sources Using Computer-Based
Photographic Analysis Systems.'' This document is available from the
U.S. Environmental Protection Agency (U.S. EPA); Office of Air Quality
and Planning Standards; Sector Policies and Programs Division;
Measurement Policy Group (D243-02), Research Triangle Park, NC 27711.
This document is also available on the Technology Transfer Network
(TTN) under Emission Measurement Center Preliminary Methods.
* * * * *
(4) An owner or operator of an affected facility that is subject to
an opacity standard under Sec. 60.42Da is not required to operate a
COMS provided that the affected facility combusts only gaseous and/or
liquid fuels (excluding residue oil) where the potential SO2
emissions rate of each fuel is no greater than 26 ng/J (0.060 lb/
MMBtu), and the unit operates according to a written site-specific
monitoring plan approved by the permitting authority. This monitoring
plan must include procedures and criteria for establishing and
monitoring specific parameters for the affected facility indicative of
compliance with the opacity standard. For testing performed as part of
this site-specific monitoring plan, the permitting authority may
require as an alternative to the notification and reporting
requirements specified in Sec. Sec. 60.8 and 60.11 that the owner or
operator submit any exceedances with the excess emissions report
required under Sec. 60.51Da(d).
* * * * *
(b) The owner or operator of an affected facility shall install,
calibrate, maintain, and operate a CEMS, and record the output of the
system, for measuring SO2 emissions, except where only
gaseous and/or liquid fuels (excluding residual oil) where the
potential SO2 emissions rate of each fuel is 26 ng/J (0.060
lb/MMBtu) or less are combusted, as follows:
* * * * *
(t) The owner or operator of an affected facility demonstrating
compliance with the output-based emissions limit under Sec. 60.42Da
shall either install, certify, operate, and maintain a CEMS for
measuring PM emissions according to the requirements of paragraph (v)
of this section, install, calibrate, operate, and maintain a PM CPMS
according to the requirements for new facilities specified in subpart
UUUUU of part 63 of this chapter, or conduct quarterly testing
according to the requirements for new facilities specified in subpart
UUUUU of part 63 of this chapter. An owner or operator of an affected
facility demonstrating compliance with the input-based
[[Page 71337]]
emissions limit in Sec. 60.42Da may install, certify, operate, and
maintain a CEMS for measuring PM emissions according to the
requirements of paragraph (v) of this section.
* * * * *
0
6. Revise Sec. 60.50Da paragraph (f) to read as follows:
Sec. 60.50Da Compliance determination procedures and methods.
* * * * *
(f) The owner or operator of an electric utility combined cycle gas
turbines that does not meet the definition of an IGCC shall conduct
performance tests for PM, SO2, and NOX using the
procedures of Method 19 of appendix A-7 of this part. The
SO2 and NOX emission rates calculations from the
gas turbine used in Method 19 of appendix A-7 of this part are
determined when the gas turbine is performance tested under subpart GG
of this part. The potential uncontrolled PM emission rate from a gas
turbine is defined as 17 ng/J (0.04 lb/MMBtu) heat input.
* * * * *
PART 63--NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS
FOR SOURCE CATEGORIES
0
7. The authority citation for 40 CFR part 63 continues to read as
follows:
Authority: 42 U.S.C. 7401, et seq.
0
8. In Sec. 63.9982, revise paragraphs (a) introductory text, (b), and
(c) to read as follows:
Sec. 63.9982 What is the affected source of this subpart?
* * * * *
(a) This subpart applies to each individual or group of two or more
new, reconstructed, or existing affected source(s) as described in
paragraphs (a)(1) and (2) of this section within a contiguous area and
under common control.
* * * * *
(b) An EGU is new if you commence construction of the coal- or oil-
fired EGU after May 3, 2011.
(c) An EGU is reconstructed if you meet the reconstruction criteria
as defined in Sec. 63.2, or if you commence reconstruction after May
3, 2011.
* * * * *
0
9. In Sec. 63.10005, revise paragraphs (d)(2)(ii), (i)(4)(ii), and
(i)(5) and add paragraph (i)(6) to read as follows:
Sec. 63.10005 What are my initial compliance requirements and by what
date must I conduct them?
* * * * *
(d) * * *
(2) * * *
(ii) You must demonstrate continuous compliance with the PM CPMS
site-specific operating limit that corresponds to the results of the
performance test demonstrating compliance with the emission limit with
which you choose to comply.
* * * * *
(i) * * *
(4) * * *
(ii) ASTM D4006-11, ``Standard Test Method for Water in Crude Oil
by Distillation,'' including Annex A1 and Appendix A1.
(5) Use one of the following methods to obtain fuel moisture
samples:
(i) ASTM D4177-95 (Reapproved 2010), ``Standard Practice for
Automatic Sampling of Petroleum and Petroleum Products,'' including
Annexes A1 through A6 and Appendices X1 and X2, or
(ii) ASTM D4057-06 (Reapproved 2011), ``Standard Practice for
Manual Sampling of Petroleum and Petroleum Products,'' including Annex
A1.
(6) Should the moisture in your liquid fuel be more than 1.0
percent by weight, you must
(i) Conduct HCl and HF emissions testing quarterly (and monitor
site-specific operating parameters as provided in Sec.
63.10000(c)(2)(iii) or
(ii) Use an HCl CEMS and/or HF CEMS.
* * * * *
0
10. In Sec. 63.10006, revise paragraph (c) to read as follows:
Sec. 63.10006 When must I conduct subsequent performance tests or
tune-ups?
* * * * *
(c) Except where paragraphs (a) or (b) of this section apply, or
where you install, certify, and operate a PM CEMS to demonstrate
compliance with a filterable PM emissions limit, for liquid oil-, solid
oil-derived fuel-, and coal-fired EGUs and IGCC EGUs, you must conduct
all applicable periodic emissions tests for filterable PM, or
individual or total HAP metals emissions according to Table 5 to this
subpart, Sec. 63.10007, and Sec. 63.10000(c), except as otherwise
provided in Sec. 63.10021(d)(1).
* * * * *
0
11. In Sec. 63.10007, revise paragraph (c) to read as follows:
Sec. 63.10007 What methods and other procedures must I use for the
performance tests?
* * * * *
(c) If you choose to comply with the filterable PM emission limit
and demonstrate continuous performance using a PM CPMS for an
applicable emission limit as provided for in Sec. 63.10000(c), you
must also establish an operating limit according to Sec. 63.10011(b),
Sec. 63.10023, and Tables 4 and 6 to this subpart. Should you desire
to have operating limits that correspond to loads other than maximum
normal operating load, you must conduct testing at those other loads to
determine the additional operating limits.
* * * * *
0
12. In Sec. 63.10009, revise paragraphs (b)(2) and (b)(3) to read as
follows:
Sec. 63.10009 May I use emissions averaging to comply with this
subpart?
* * * * *
(b) * * *
(2) Weighted 30-boiler operating day rolling average emissions rate
equations for pollutants other than Hg. Use equation 2a or 2b to
calculate the 30 day rolling average emissions daily.
[GRAPHIC] [TIFF OMITTED] TR30NO12.001
Where:
Heri = hourly emission rate (e.g., lb/MMBtu, lb/MWh) from
unit i's CEMS for the preceding 30-group boiler operating days,
Rmi = hourly heat input or gross electrical output from
unit i for the preceding 30-group boiler operating days,
p = number of EGUs in emissions averaging group that rely on CEMS or
sorbent trap monitoring,
n = number of hourly rates collected over 30-group boiler operating
days,
Teri = Emissions rate from most recent emissions test of
unit i in terms of lb/heat input or lb/gross electrical output,
[[Page 71338]]
Rti = Total heat input or gross electrical output of unit
i for the preceding 30-boiler operating days, and
m = number of EGUs in emissions averaging group that rely on
emissions testing.
[GRAPHIC] [TIFF OMITTED] TR30NO12.002
Where:
variables with similar names share the descriptions for Equation 2a,
Smi = steam generation in units of pounds from unit i
that uses CEMS for the preceding 30-group boiler operating days,
Cfmi = conversion factor, calculated from the most recent
compliance test results, in units of heat input per pound of steam
generated or gross electrical output per pound of steam generated,
from unit i that uses CEMS from the preceding 30 group boiler
operating days,
Sti = steam generation in units of pounds from unit i
that uses emissions testing, and
Cfti = conversion factor, calculated from the most recent
compliance test results, in units of heat input per pound of steam
generated or gross electrical output per pound of steam generated,
from unit i that uses emissions testing.
(3) Weighted 90-boiler operating day rolling average emissions rate
equations for Hg emissions from EGUs in the ``coal-fired unit not low
rank virgin coal'' subcategory. Use equation 3a or 3b to calculate the
90-day rolling average emissions daily.
[GRAPHIC] [TIFF OMITTED] TR30NO12.003
Where:
Heri = hourly emission rate from unit i's CEMS or Hg
sorbent trap monitoring system for the preceding 90-group boiler
operating days,
Rmi = hourly heat input or gross electrical output from
unit i for the preceding 90-group boiler operating days,
p = number of EGUs in emissions averaging group that rely on CEMS,
n = number of hourly rates collected over the 90-group boiler
operating days,
Teri = Emissions rate from most recent emissions test of
unit i in terms of lb/heat input or lb/gross electrical output,
Rti = Total heat input or gross electrical output of unit
i for the preceding 90-boiler operating days, and
m = number of EGUs in emissions averaging group that rely on
emissions testing.
[GRAPHIC] [TIFF OMITTED] TR30NO12.004
Where:
variables with similar names share the descriptions for Equation 2a,
Smi = steam generation in units of pounds from unit i
that uses CEMS or a Hg sorbent trap monitoring for the preceding 90-
group boiler operating days,
Cfmi = conversion factor, calculated from the most recent
compliance test results, in units of heat input per pound of steam
generated or gross electrical output per pound of steam generated,
from unit i that uses CEMS or sorbent trap monitoring from the
preceding 90-group boiler operating days,
Sti = steam generation in units of pounds from unit i
that uses emissions testing, and
Cfti = conversion factor, calculated from the most recent
emissions test results, in units of heat input per pound of steam
generated or gross electrical output per pound of steam generated,
from unit i that uses emissions testing.
* * * * *
0
13. In Sec. 63.10010, revise paragraph (j)(1)(i) to read as follows:
Sec. 63.10010 What are my monitoring, installation, operation, and
maintenance requirements?
* * * * *
(j) * * *
(1) * * *
(i) Install and certify your HAP metals CEMS according to the
procedures and requirements in your approved site-specific test plan as
required in Sec. 63.7(e). The reportable measurement output from the
HAP metals CEMS must be expressed in units of the applicable emissions
limit (e.g., lb/MMBtu, lb/MWh) and in the form of a 30-boiler operating
day rolling average.
* * * * *
0
14. In Sec. 63.10011, revise paragraphs (f) and (g) to read as
follows:
Sec. 63.10011 How do I demonstrate initial compliance with the
emissions limits and work practice standards?
* * * * *
(f) You must use during periods of startup or shutdown any one or
combination of the following clean fuels: natural gas, synthetic
natural gas, propane, distillate oil, synthesis gas (syngas), and
ultra-low sulfur diesel (ULSD).
(g) You must follow the startup and shutdown requirements in Table
3 for each coal-fired, liquid oil-fired, or solid oil-derived fuel-
fired EGU.
0
15. Amend Sec. 63.10021 by adding paragraphs (c)(1) and (2) to read as
follows:
Sec. 63.10021 How do I demonstrate continuous compliance with the
emission limitations, operating limits, and work practice standards?
* * * * *
(c) * * *
(1) For any exceedance of the 30-boiler operating day PM CPMS
average value from the established operating parameter limit for an EGU
subject to the emissions limits in Table 1 to this subpart, you must:
(i) Within 48 hours of the exceedance, visually inspect the air
pollution control device (APCD);
[[Page 71339]]
(ii) If the inspection of the APCD identifies the cause of the
exceedance, take corrective action as soon as possible, and return the
PM CPMS measurement to within the established value; and
(iii) Within 45 days of the exceedance or at the time of the annual
compliance test, whichever comes first, conduct a PM emissions
compliance test to determine compliance with the PM emissions limit and
to verify or re-establish the CPMS operating limit. You are not
required to conduct any additional testing for any exceedances that
occur between the time of the original exceedance and the PM emissions
compliance test required under this paragraph.
(2) PM CPMS exceedances from the operating limit for an EGU subject
to the emissions limits in Table 1 of this subpart leading to more than
four required performance tests in a 12-month period (rolling monthly)
constitute a separate violation of this subpart.
* * * * *
0
16. In Sec. 63.10023, revise paragraph (b) to read as follows:
Sec. 63.10023 How do I establish my PM CPMS operating limit and
determine compliance with it?
* * * * *
(b) Determine your operating limit as provided in paragraph (b)(1)
or (b)(2) of this section. You must verify an existing or establish a
new operating limit after each repeated performance test.
(1) For an existing EGU, determine your operating limit based on
the highest 1-hour average PM CPMS output value recorded during the
performance test.
(2) For a new EGU, determine your operating limit based on the
highest 1-hour average PM CPMS output value recorded during the
performance test.
* * * * *
0
17. In Sec. 63.10030, revise paragraphs (b), (c), and (d) to read as
follows:
Sec. 63.10030 What notifications must I submit and when?
* * * * *
(b) As specified in Sec. 63.9(b)(2), if you startup your EGU that
is an affected source before April 16, 2012, you must submit an Initial
Notification not later than 120 days after April 16, 2012.
(c) As specified in Sec. 63.9(b)(4) and (b)(5), if you startup
your new or reconstructed EGU that is an affected source on or after
April 16, 2012, you must submit an Initial Notification not later than
15 days after the actual date of startup of the EGU that is an affected
source.
(d) When you are required to conduct a performance test, you must
submit a Notification of Intent to conduct a performance test at least
60 days before the performance test is scheduled to begin.
* * * * *
0
18. Amend Sec. 63.10042 by:
0
a. Revising the definitions of ``Boiler operating day,'' ``Shutdown'',
``Startup'', and ``Unit designed for coal > 8,300 Btu/lb subcategory'';
and
0
b. Adding, in alphabetical order, a new definition of ``Clean fuel''.
The revised and added text reads as follows:
Sec. 63.10042 What definitions apply to this subpart?
* * * * *
Boiler operating day means a 24-hour period that begins at midnight
and ends the following midnight during which any fuel is combusted at
any time in the EGU, excluding periods of startup or shutdown. It is
not necessary for the fuel to be combusted the entire 24-hour period.
* * * * *
Clean fuel means natural gas, synthetic natural gas that meets the
specification necessary for that gas to be transported on a Federal
Energy Regulatory Commission (FERC) regulated pipeline, propane,
distillate oil, synthesis gas (syngas), or ultra-low-sulfur diesel
(ULSD).
* * * * *
Shutdown means the period in which cessation of operation of an EGU
is initiated for any purpose. Shutdown begins when the EGU no longer
generates electricity or makes useful thermal energy (such as heat or
steam) for industrial, commercial, heating, or cooling purposes or when
no coal, liquid oil, syngas, or solid oil-derived fuel is being fired
in the EGU, whichever is earlier. Shutdown ends when the EGU no longer
generates electricity or makes useful thermal energy (such as steam or
heat) for industrial, commercial, heating, or cooling purposes, and no
fuel is being fired in the EGU.
Startup means the period in which operation of an EGU is initiated
for any purpose. Startup begins with either the first-ever firing of
fuel in an EGU for the purpose of producing electricity or useful
thermal energy (such as heat or steam) for industrial, commercial,
heating, or cooling purposes or the firing of fuel in an EGU for any
purpose after a shutdown event. Startup ends when the EGU generates
electricity that is sold or used for any other purpose (including on
site use), or the EGU makes useful thermal energy (such as heat or
steam) for industrial, commercial, heating, or cooling purposes (16
U.S.C. 796(18)(A) and 18 CFR 292.202(c)), whichever is earlier.
* * * * *
Unit designed for coal = 8,300 Btu/lb subcategory means
any coal-fired EGU that is not a coal-fired EGU in the ``unit designed
for low rank virgin coal'' subcategory.
* * * * *
0
19. Revise Table 1 to Subpart UUUUU of Part 63 to read as follows:
Table 1 to Subpart UUUUU of Part 63--Emission Limits for New or
Reconstructed EGUs
As stated in Sec. 63.9991, you must comply with the following
applicable emission limits:
----------------------------------------------------------------------------------------------------------------
Using these requirements,
You must meet the as appropriate (e.g.,
If your EGU is in this subcategory For the following following emission specified sampling volume
. . . pollutants . . . limits and work or test run duration) and
practice standards . . limitations with the test
. methods in Table 5 . . .
----------------------------------------------------------------------------------------------------------------
1. Coal-fired unit not low rank a. Filterable 9.0E-2 lb/MWh \1\..... Collect a minimum of 4 dscm
virgin coal. particulate matter per run.
(PM).
OR OR
Total non-Hg HAP 6.0E-2 lb/GWh......... Collect a minimum of 4 dscm
metals. per run.
OR OR
Individual HAP metals: ...................... Collect a minimum of 3 dscm
per run.
Antimony (Sb)...... 8.0E-3 lb/GWh.
Arsenic (As)....... 3.0E-3 lb/GWh.
Beryllium (Be)..... 6.0E-4 lb/GWh.
Cadmium (Cd)....... 4.0E-4 lb/GWh.
[[Page 71340]]
Chromium (Cr)...... 7.0E-3 lb/GWh.
Cobalt (Co)........ 2.0E-3 lb/GWh.
Lead (Pb).......... 3.0E-2 lb/GWh.
Manganese (Mn)..... 4.0E-3 lb/GWh.
Nickel (Ni)........ 4.0E-2 lb/GWh.
Selenium (Se)...... 5.0E-2 lb/GWh.
b. Hydrogen chloride 1.0E-2 lb/MWh......... For Method 26A, collect a
(HCl). minimum of 3 dscm per run.
For ASTM D6348-03 \2\ or
Method 320, sample for a
minimum of 1 hour.
OR
Sulfur dioxide (SO2) 1.0 lb/MWh............ SO2 CEMS.
\3\.
c. Mercury (Hg)....... 3.0E-3 lb/GWh......... Hg CEMS or sorbent trap
monitoring system only.
2. Coal-fired units low rank virgin a. Filterable 9.0E-2 lb/MWh \1\..... Collect a minimum of 4 dscm
coal. particulate matter per run.
(PM).
OR OR
Total non-Hg HAP 6.0E-2 lb/GWh......... Collect a minimum of 4 dscm
metals. per run.
OR OR
Individual HAP metals: ...................... Collect a minimum of 3 dscm
per run.
Antimony (Sb)...... 8.0E-3 lb/GWh.
Arsenic (As)....... 3.0E-3 lb/GWh.
Beryllium (Be)..... 6.0E-4 lb/GWh.
Cadmium (Cd)....... 4.0E-4 lb/GWh.
Chromium (Cr)...... 7.0E-3 lb/GWh.
Cobalt (Co)........ 2.0E-3 lb/GWh.
Lead (Pb).......... 3.0E-2 lb/GWh.
Manganese (Mn)..... 4.0E-3 lb/GWh.
Nickel (Ni)........ 4.0E-2 lb/GWh.
Selenium (Se)...... 5.0E-2 lb/GWh.
b. Hydrogen chloride 1.0E-2 lb/MWh......... For Method 26A, collect a
(HCl). minimum of 3 dscm per run.
For ASTM D6348-03 \2\ or
Method 320, sample for a
minimum of 1 hour.
OR
Sulfur dioxide (SO2) 1.0 lb/MWh............ SO2 CEMS.
\3\.
c. Mercury (Hg)....... 4.0E-2 lb/GWh......... Hg CEMS or sorbent trap
monitoring system only.
3. IGCC unit....................... a. Filterable 7.0E-2 lb/MWh \4\..... Collect a minimum of 1 dscm
particulate matter 9.0E-2 lb/MWh \5\..... per run.
(PM).
OR OR
Total non-Hg HAP 4.0E-1 lb/GWh......... Collect a minimum of 1 dscm
metals. per run.
OR OR
Individual HAP metals: ...................... Collect a minimum of 2 dscm
per run.
Antimony (Sb)...... 2.0E-2 lb/GWh.
Arsenic (As)....... 2.0E-2 lb/GWh.
Beryllium (Be)..... 1.0E-3 lb/GWh.
Cadmium (Cd)....... 2.0E-3 lb/GWh.
Chromium (Cr)...... 4.0E-2 lb/GWh.
Cobalt (Co)........ 4.0E-3 lb/GWh.
Lead (Pb).......... 9.0E-3 lb/GWh.
Manganese (Mn)..... 2.0E-2 lb/GWh.
Nickel (Ni)........ 7.0E-2 lb/GWh.
Selenium (Se)...... 3.0E-1 lb/GWh.
b. Hydrogen chloride 2.0E-3 lb/MWh......... For Method 26A, collect a
(HCl). minimum of 1 dscm per run;
for Method 26, collect a
minimum of 120 liters per
run.
For ASTM D6348-03 \2\ or
Method 320, sample for a
minimum of 1 hour.
OR
Sulfur dioxide (SO2) 4.0E-1 lb/MWh......... SO2 CEMS.
\3\.
c. Mercury (Hg)....... 3.0E-3 lb/GWh......... Hg CEMS or sorbent trap
monitoring system only.
4. Liquid oil-fired unit-- a. Filterable 4.0E-1 lb/MWh \1\..... Collect a minimum of 1 dscm
continental (excluding limited-use particulate matter OR.................... per run.
liquid oil-fired subcategory (PM). 2.0E-4 lb/MWh......... Collect a minimum of 2 dscm
units). OR.................... OR.................... per run.
Total HAP metals......
OR....................
Individual HAP metals: ...................... Collect a minimum of 2 dscm
per run.
Antimony (Sb)...... 1.0E-2 lb/GWh.
[[Page 71341]]
Arsenic (As)....... 3.0E-3 lb/GWh.
Beryllium (Be)..... 5.0E-4 lb/GWh.
Cadmium (Cd)....... 2.0E-4 lb/GWh.
Chromium (Cr)...... 2.0E-2 lb/GWh.
Cobalt (Co)........ 3.0E-2 lb/GWh.
Lead (Pb).......... 8.0E-3 lb/GWh.
Manganese (Mn)..... 2.0E-2 lb/GWh.
Nickel (Ni)........ 9.0E-2 lb/GWh.
Selenium (Se)...... 2.0E-2 lb/GWh.
Mercury (Hg).......... 1.0E-4 lb/GWh......... For Method 30B sample
volume determination
(Section 8.2.4), the
estimated Hg concentration
should nominally be <\1/2\
the standard.
b. Hydrogen chloride 4.0E-4 lb/MWh......... For Method 26A, collect a
(HCl). minimum of 3 dscm per run.
For ASTM D6348-03 \2\ or
Method 320, sample for a
minimum of 1 hour.
c. Hydrogen fluoride 4.0E-4 lb/MWh......... For Method 26A, collect a
(HF). minimum of 3 dscm per run.
For ASTM D6348-03 \2\ or
Method 320, sample for a
minimum of 1 hour.
5. Liquid oil-fired unit--non- a. Filterable 2.0E-1 lb/MWh \1\..... Collect a minimum of 1 dscm
continental (excluding limited-use particulate matter OR.................... per run.
liquid oil-fired subcategory (PM). 7.0E-3 lb/MWh......... Collect a minimum of 1 dscm
units). OR.................... OR.................... per run.
Total HAP metals......
OR....................
Individual HAP metals: ...................... Collect a minimum of 3 dscm
per run.
Antimony (Sb)...... 8.0E-3 lb/GWh.
Arsenic (As)....... 6.0E-2 lb/GWh.
Beryllium (Be)..... 2.0E-3 lb/GWh.
Cadmium (Cd)....... 2.0E-3 lb/GWh.
Chromium (Cr)...... 2.0E-2 lb/GWh.
Cobalt (Co)........ 3.0E-1 lb/GWh.
Lead (Pb).......... 3.0E-2 lb/GWh.
Manganese (Mn)..... 1.0E-1 lb/GWh.
Nickel (Ni)........ 4.1E0 lb/GWh.
Selenium (Se)...... 2.0E-2 lb/GWh.
Mercury (Hg).......... 4.0E-4 lb/GWh......... For Method 30B sample
volume determination
(Section 8.2.4), the
estimated Hg concentration
should nominally be <\1/2\
the standard.
b. Hydrogen chloride 2.0E-3 lb/MWh......... For Method 26A, collect a
(HCl). minimum of 1 dscm per run;
for Method 26, collect a
minimum of 120 liters per
run.
For ASTM D6348-03 \2\ or
Method 320, sample for a
minimum of 1 hour.
c. Hydrogen fluoride 5.0E-4 lb/MWh......... For Method 26A, collect a
(HF). minimum of 3 dscm per run.
For ASTM D6348-03 \2\ or
Method 320, sample for a
minimum of 1 hour.
6. Solid oil-derived fuel-fired a. Filterable 3.0E-2 lb/MWh \1\..... Collect a minimum of 1 dscm
unit.. particulate matter per run.
(PM).
OR OR
Total non-Hg HAP 6.0E-1 lb/GWh......... Collect a minimum of 1 dscm
metals. per run.
OR OR
Individual HAP metals: ...................... Collect a minimum of 3 dscm
per run.
Antimony (Sb)...... 8.0E-3 lb/GWh.
Arsenic (As)....... 3.0E-3 lb/GWh.
Beryllium (Be)..... 6.0E-4 lb/GWh.
Cadmium (Cd)....... 7.0E-4 lb/GWh.
Chromium (Cr)...... 6.0E-3 lb/GWh.
Cobalt (Co)........ 2.0E-3 lb/GWh.
Lead (Pb).......... 2.0E-2 lb/GWh.
Manganese (Mn)..... 7.0E-3 lb/GWh.
Nickel (Ni)........ 4.0E-2 lb/GWh.
Selenium (Se)...... 6.0E-3 lb/GWh.
b. Hydrogen chloride 4.0E-4 lb/MWh......... For Method 26A, collect a
(HCl). minimum of 3 dscm per run.
For ASTM D6348-03 \2\ or
Method 320, sample for a
minimum of 1 hour.
[[Page 71342]]
OR
Sulfur dioxide (SO2) 1.0 lb/MWh............ SO2 CEMS.
\3\.
c. Mercury (Hg)....... 2.0E-3 lb/GWh......... Hg CEMS or Sorbent trap
monitoring system only.
----------------------------------------------------------------------------------------------------------------
\1\ Gross electric output.
\2\ Incorporated by reference, see Sec. 63.14.
\3\ You may not use the alternate SO2 limit if your EGU does not have some form of FGD system and SO2 CEMS
installed.
\4\ Duct burners on syngas; gross electric output.
\5\ Duct burners on natural gas; gross electric output.
0
20. Revise Table 3 to Subpart UUUUU of Part 63 to read as follows:
Table 3 to Subpart UUUUU of Part 63 -- Work Practice Standards
As stated in Sec. Sec. 63.9991, you must comply with the following
applicable work practice standards:
----------------------------------------------------------------------------------------------------------------
If your EGU is . . . You must meet the following . . .
----------------------------------------------------------------------------------------------------------------
1. An existing EGU..................... Conduct a tune-up of the EGU burner and combustion controls at least
each 36 calendar months, or each 48 calendar months if neural network
combustion optimization software is employed, as specified in Sec.
63.10021(e).
2. A new or reconstructed EGU.......... Conduct a tune-up of the EGU burner and combustion controls at least
each 36 calendar months, or each 48 calendar months if neural network
combustion optimization software is employed, as specified in Sec.
63.10021(e).
3. A coal-fired, liquid oil-fired, or You must operate all CMS during startup.
solid oil-derived fuel-fired EGU For startup of an EGU, you must use one or a combination of the
during startup. following clean fuels: natural gas, synthetic natural gas, propane,
distillate oil, syngas, and ultra-low sulfur diesel.
Once you start firing coal, residual oil, or solid oil-derived fuel,
you must vent emissions to the main stack(s) and engage all of the
applicable control devices except limestone injection in FBC EGUs, dry
scrubber, SNCR, and SCR. You must start your limestone injection in
FBC EGUs, dry scrubber, SNCR, and SCR systems as expeditiously as
possible, but, in any case, when necessary to comply with other
standards applicable to the source that require operation of the
control devices.
Relative to the syngas not fired in the combustion turbine of an IGCC
EGU during startup, you must either: (1) Flare the syngas or (2) route
the syngas to duct burners, which may need to be installed, and route
the flue gas from the duct burners to the heat recovery steam
generator.
You must comply with all applicable emission limits at all times except
for startup or shutdown periods conforming with this work practice.
You must collect monitoring data during periods of startup, as
specified in Sec. 63.10020(a). You must keep records during periods
of startup. You must provide reports concerning activities and periods
of startup, as specified in Sec. 63.10011(g) and Sec. 63.10021(h)
and (i).
4. A coal-fired, liquid oil-fired, or You must operate all CMS during shutdown.
solid oil-derived fuel-fired EGU While firing coal, residual oil, or solid oil-derived fuel during
during shutdown. shutdown, you must vent emissions to the main stack(s) and operate all
applicable control devices, except limestone injection in FBC EGUs,
dry scrubber, SNCR, and SCR. You must operate your limestone injection
in FBC EGUs, dry scrubber, SNCR, and SCR systems as expeditiously as
possible, but, in any case, when necessary to comply with other
standards that apply to the source and that require operation of the
control devices.
If, in addition to the fuel used prior to initiation of shutdown,
another fuel must be used to support the shutdown process, that
additional fuel must be one or a combination of the following clean
fuels: Natural gas, synthetic natural gas, propane, distillate oil,
syngas, and ultra-low sulfur diesel.
Relative to the syngas not fired in the combustion turbine of an IGCC
EGU during shutdown, you must either: (1) Flare the syngas or (2)
route the syngas to duct burners, which may need to be installed, and
route the flue gas from the duct burners to the heat recovery steam
generator.
You must comply with all applicable emission limits at all times except
during startup and shutdown periods at which time you must meet this
work practice. You must collect monitoring data during periods of
startup, as specified in Sec. 63.10020(a). You must keep records
during periods of startup. You must provide reports concerning
activities and periods of startup, as specified in Sec. 63.10011(g)
and Sec. 63.10021(h) and (i).
----------------------------------------------------------------------------------------------------------------
0
21. Revise Table 4 to Subpart UUUUU of Part 63 to read as follows:
Table 4 to Subpart UUUUU of Part 63--Operating Limits for EGUs
As stated in Sec. Sec. 63.9991, you must comply with the
applicable operating limits:
[[Page 71343]]
----------------------------------------------------------------------------------------------------------------
If you demonstrate compliance using . . . You must meet these operating limits . . .
----------------------------------------------------------------------------------------------------------------
1. PM CPMS for an existing EGU.............. Maintain the 30-boiler operating day rolling average PM CPMS
output at or below the highest 1-hour average measured during the
most recent performance test demonstrating compliance with the
filterable PM, total non-mercury HAP metals (total HAP metals,
for liquid oil-fired units), or individual non-mercury HAP metals
(individual HAP metals including Hg, for liquid oil-fired units)
emissions limitation(s).
2. PM CPMS for a new EGU.................... Maintain the 30-boiler operating day rolling average PM CPMS
output at or below the highest 1-hour average PM CPMS output
value recorded during the most recent performance test run
demonstrating compliance with the filterable PM, total non-
mercury HAP metals (total HAP metals, for liquid oil-fired
units), or individual non-mercury HAP metals (individual HAP
metals including Hg, for liquid oil-fired units) emissions
limitation(s).
----------------------------------------------------------------------------------------------------------------
0
22. Revise footnote 4 of Table 5 to Subpart UUUUU of Part 63 to read as
follows:
Table 5 to Subpart UUUUU of Part 63--Performance Testing Requirements
* * * * *
\4\ When using ASTM D6348-03, 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; (2) For ASTM
D6348-03 Annex A5 (Analyte Spiking Technique), the percent (%)R must
be determined for each target analyte (see Equation A5.5); (3) For
the ASTM D6348-03 test data to be acceptable for a target analyte,
%R must be 70% <= R <= 130%; and (4) The %R value for each compound
must be reported in the test report and all field measurements
corrected with the calculated %R value for that compound using the
following equation:
* * * * *
0
23. Revise Table 6 to Subpart UUUUU of Part 63 to read as follows:
Table 6 to Subpart UUUUU of Part 63--Establishing PM CPMS Operating
Limits
As stated in Sec. 63.10007, you must comply with the following
requirements for establishing operating limits:
----------------------------------------------------------------------------------------------------------------
And you choose to
If you have an applicable establish PM CPMS According to the
emission limit for . . . operating limits, And . . . Using . . . following
you must . . . procedures . . .
----------------------------------------------------------------------------------------------------------------
1. Filterable Particulate matter Install, certify, Establish a site- Data from the PM 1. Collect PM CPMS
(PM), total non-mercury HAP maintain, and specific CPMS and the PM output data
metals, individual non-mercury operate a PM CPMS operating limit or HAP metals during the entire
HAP metals, total HAP metals, for monitoring in units of PM performance tests. period of the
or individual HAP metals for an emissions CPMS output performance
existing EGU. discharged to the signal (e.g., tests.
atmosphere milliamps, mg/ 2. Record the
according to Sec. acm, or other raw average hourly PM
63.10010(h)(1). signal). CPMS output for
each test run in
the three run
performance test.
3. Determine the
highest 1-hour
average PM CPMS
measured during
the performance
test
demonstrating
compliance with
the filterable PM
or HAP metals
emissions
limitations.
2. Filterable Particulate matter Install, certify, Establish a site- Data from the PM 1. Collect PM CPMS
(PM), total non-mercury HAP maintain, and specific CPMS and the PM output data
metals, individual non-mercury operate a PM CPMS operating limit or HAP metals during the entire
HAP metals, total HAP metals, for monitoring in units of PM performance tests. period of the
or individual HAP metals for a emissions CPMS output performance
new EGU. discharged to the signal (e.g., tests.
atmosphere milliamps, mg/ 2. Record the
according to Sec. acm, or other raw average hourly PM
63.10010(h)(1). signal). CPMS output for
each test run in
the three run
performance test.
3. Determine the
highest 1-hour
average PM CPMS
measured during
the performance
run demonstrating
compliance with
the filterable PM
or HAP metals
emissions
limitations.
----------------------------------------------------------------------------------------------------------------
0
24. Revise Table 7 to Subpart UUUUU of Part 63 to read as follows:
Table 7 to Subpart UUUUU of Part 63--Demonstrating Continuous
Compliance
As stated in Sec. 63.10021, you must show continuous compliance
with the emission limitations for affected sources according to the
following:
[[Page 71344]]
------------------------------------------------------------------------
If you use one of the following to meet
applicable emissions limits, operating You demonstrate continuous
limits, or work practice standards . . compliance by . . .
.
------------------------------------------------------------------------
1. CEMS to measure filterable PM, SO2, Calculating the 30- (or 90-)
HCl, HF, or Hg emissions, or using a boiler operating day rolling
sorbent trap monitoring system to arithmetic average emissions
measure Hg. rate in units of the
applicable emissions standard
basis at the end of each
boiler operating day using all
of the quality assured hourly
average CEMS or sorbent trap
data for the previous 30- (or
90-) boiler operating days,
excluding data recorded during
periods of startup or
shutdown.
2. PM CPMS to measure compliance with a Calculating the arithmetic 30-
parametric operating limit. (or 90-) boiler operating day
rolling average of all of the
quality assured hourly average
PM CPMS output data (e.g.,
milliamps, PM concentration,
raw data signal) collected for
all operating hours for the
previous 30 boiler operating
days, excluding data recorded
during periods of startup or
shutdown.
3. Site-specific monitoring using CMS If applicable, by conducting
for liquid oil-fired EGUs for HCl and the monitoring in accordance
HF emission limit monitoring. with an approved site-specific
monitoring plan.
4. Quarterly performance testing for Calculating the results of the
coal-fired, solid oil derived fired, testing in units of the
or liquid oil-fired EGUs to measure applicable emissions standard.
compliance with one or more applicable
emissions limit in Table 1 or 2.
5. Conducting periodic performance tune- Conducting periodic performance
ups of your EGU(s). tune-ups of your EGU(s), as
specified in Sec.
63.10021(e).
6. Work practice standards for coal- Operating in accordance with
fired, liquid oil-fired, or solid oil- Table 3.
derived fuel-fired EGUs during startup.
7. Work practice standards for coal- Operating in accordance with
fired, liquid oil-fired, or solid oil- Table 3.
derived fuel-fired EGUs during
shutdown.
------------------------------------------------------------------------
0
25. Revise sections 4.1 and 5.2.2.2 to Appendix A to Subpart UUUUU of
Part 63 to read as follows:
Appendix A to Subpart UUUUU--Hg Monitoring Provisions
4.1 Certification Requirements. All Hg CEMS and sorbent trap
monitoring systems and the additional monitoring systems used to
continuously measure Hg emissions in units of the applicable
emissions standard in accordance with this appendix must be
certified in a timely manner, such that the initial compliance
demonstration is completed no later than the applicable date in
Sec. 63.9984(f).
* * * * *
5.2.2.2 The same RATA performance criteria specified in Table A-
2 for Hg CEMS shall apply to the annual RATAs of the sorbent trap
monitoring system.
* * * * *
0
26. Revise section 3.1.2.1.3 and the heading to section 5.3.4 to
Appendix B to Subpart UUUUU of Part 63 to read as follows:
Appendix B to Subpart UUUUU--HCl and HF Monitoring Provisions
3.1.2.1.3 For the ASTM D6348-03 test data to be acceptable for a
target analyte, %R must be 70% <= R <= 130%; and
* * * * *
5.3.3 Conditional Data Validation
* * * * *
[FR Doc. 2012-28729 Filed 11-29-12; 8:45 am]
BILLING CODE 6560-50-P