National Emission Standards for Hazardous Air Pollutant Emissions: Hard and Decorative Chromium Electroplating and Chromium Anodizing Tanks; and Steel Pickling-HCl Process Facilities and Hydrochloric Acid Regeneration Plants, 6628-6656 [2012-2434]
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Federal Register / Vol. 77, No. 26 / Wednesday, February 8, 2012 / Proposed Rules
ENVIRONMENTAL PROTECTION
AGENCY
40 CFR Part 63
[EPA–HQ–OAR–2010–0600; FRL–9626–7]
RIN 2060–AQ60
National Emission Standards for
Hazardous Air Pollutant Emissions:
Hard and Decorative Chromium
Electroplating and Chromium
Anodizing Tanks; and Steel PicklingHCl Process Facilities and
Hydrochloric Acid Regeneration Plants
Environmental Protection
Agency (EPA).
ACTION: Supplemental notice of
proposed rulemaking.
AGENCY:
This action supplements our
proposed amendments to National
Emission Standards for Hazardous Air
Pollutant Emissions for Hard and
Decorative Chromium Electroplating
and Chromium Anodizing Tanks; and
Steel Pickling-HCl Process Facilities and
Hydrochloric Acid Regeneration Plants,
which were published on October 21,
2010 (75 FR 65068, October 21, 2010).
In that action, EPA proposed
amendments to these NESHAP under
section 112(d)(6) and (f)(2) of the Clean
Air Act. Specifically, this action
presents a new technology review and a
new residual risk analysis for chromium
electroplating and anodizing facilities
and proposes revisions to the NESHAP
based on those reviews. This action also
proposes to remove an alternative
compliance method for Steel Pickling
hydrochloric acid regeneration plants.
Finally, this action proposes to
incorporate electronic reporting
requirements into both NESHAP.
DATES: Comments must be received on
or before March 26, 2012. Under the
Paperwork Reduction Act, comments on
the information collection provisions
are best assured of having full effect if
the Office of Management and Budget
(OMB) receives a copy of your
comments on or before March 9, 2012.
Public Hearing. If anyone contacts the
EPA requesting to speak at a public
hearing by February 21, 2012, a public
hearing will be held on February 23,
2012.
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SUMMARY:
You may submit comments,
identified by Docket ID No. EPA–HQ–
OAR–2010–0600, by one of the
following methods:
• Federal eRulemaking Portal:
www.regulations.gov: Follow the
instructions for submitting comments.
• Email: a-and-r-docket@epa.gov.
Include Docket ID No. EPA–HQ–OAR–
ADDRESSES:
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2010–0600 in the subject line of the
message.
• Fax: (202) 566–9744. Attention
Docket ID No. EPA–HQ–OAR–2010–
0600.
• Mail: U.S. Postal Service, send
comments to: EPA Docket Center, EPA
West (Air Docket), Attention Docket ID
No. EPA–HQ–OAR–2010–0600, U.S.
Environmental Protection Agency,
Mailcode: 2822T, 1200 Pennsylvania
Ave. NW., Washington, DC 20460.
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, Office of
Management and Budget (OMB), Attn:
Desk Officer for EPA, 725 17th Street
NW., Washington, DC 20503.
• Hand Delivery: U.S. Environmental
Protection Agency, EPA West (Air
Docket), Room 3334, 1301 Constitution
Ave. NW., Washington, DC 20004.
Attention Docket ID No. EPA–HQ–
OAR–2010–0600. Such deliveries are
only accepted during the Docket’s
normal hours of operation, and special
arrangements should be made for
deliveries of boxed information.
Instructions. Direct your comments to
Docket ID No. EPA–HQ–OAR–2010–
0600. EPA’s policy is that all comments
received will be included in the public
docket without change and may be
made available online at
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 www.regulations.gov
or email. The www.regulations.gov Web
site is an ‘‘anonymous access’’ system,
which means EPA will not know your
identity or contact information unless
you provide it in the body of your
comment. If you send an email
comment directly to EPA without going
through 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, EPA recommends that you
include your name and other contact
information in the body of your
comment and with any disk or CD–ROM
you submit. If EPA cannot read your
comment due to technical difficulties
and cannot contact you for clarification,
EPA may not be able to consider your
comment. Electronic files should avoid
the use of special characters, any form
of encryption, and be free of any defects
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or viruses. For additional information
about EPA’s public docket, visit the EPA
Docket Center homepage at https://
www.epa.gov/epahome/dockets.htm.
Docket. The EPA has established a
docket for this rulemaking under Docket
ID No. EPA–HQ–OAR–2010–0600. All
documents in the docket are listed in
the 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, is not placed on
the Internet and will be publicly
available only in hard copy. Publicly
available docket materials are available
either electronically in
www.regulations.gov or in hard copy at
the EPA Docket Center, EPA West,
Room 3334, 1301 Constitution Ave.
NW., Washington, DC. The Public
Reading Room is open from 8:30 a.m. to
4:30 p.m., Monday through Friday,
excluding legal holidays. The telephone
number for the Public Reading Room is
(202) 566–1744, and the telephone
number for the EPA Docket Center is
(202) 566–1742.
FOR FURTHER INFORMATION CONTACT: For
questions about this proposed action,
contact Mr. Phil Mulrine, Sector
Policies and Programs Division (D243–
02), Office of Air Quality Planning and
Standards, U.S. Environmental
Protection Agency, Research Triangle
Park, NC 27711, telephone (919) 541–
5289; fax number: (919) 541–3207; and
email address: mulrine.phil@epa.gov.
For specific information regarding the
risk modeling methodology, contact Mr.
Mark Morris, Health and Environmental
Impacts Division (C539–02), Office of
Air Quality Planning and Standards,
U.S. Environmental Protection Agency,
Research Triangle Park, NC 27711;
telephone number: (919) 541–5416; fax
number: (919) 541–0840; and email
address: morris.mark@epa.gov.
SUPPLEMENTARY INFORMATION:
Organization of this Document. The
information in this preamble is
organized as follows:
I. General Information
A. Does this action apply to me?
B. Where can I get a copy of this document
and other related information?
C. What should I consider as I prepare my
comments for the EPA?
D. When would a public hearing occur?
II. Background Information
A. Overview of the Chromium
Electroplating and Chromium Anodizing
Source Categories
B. What is the history of the chromium
electroplating and chromium anodizing
risk and technology reviews?
C. Overview of the steel pickling source
category
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D. What is the history of the Steel Pickling
Risk and Technology Review?
E. What data collection activities were
conducted to support this action?
III. Analyses Performed
A. How did we perform the technology
review?
B. For purposes of this supplemental
proposal, how did we estimate the risk
posed by each of the three chromium
electroplating source categories?
IV. Analytical Results and Proposed
Decisions for the Three Chromium
Electroplating Source Categories
A. What are the results and proposed
decisions based on our technology
review?
B. What are the results of the risk
assessment?
C. What are our proposed decisions
regarding risk acceptability and ample
margin of safety?
D. Compliance Dates
V. What action are we proposing for the steel
pickling source category?
A. Elimination of an Alternative
Compliance Option
B. Compliance Dates
VI. What other actions are we proposing?
A. Electronic Reporting
VII. Summary of Cost, Environmental, and
Economic Impacts
A. What are the affected sources?
B. What are the emission reductions?
C. What are the cost impacts?
D. What are the economic impacts?
E. What are the benefits?
VIII. Request for Comments
IX. 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
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use
I. National Technology Transfer and
Advancement Act
J. Executive Order 12898: Federal Actions
To Address Environmental Justice in
Minority Populations and Low-Income
Populations
I. General Information
A. Does this action apply to me?
The regulated industrial source
categories that are the subject of this
proposal are listed in Table 1 to this
preamble. Table 1 is not intended to be
exhaustive, but rather provides a guide
for readers regarding entities likely to be
affected by the proposed action for the
source categories listed. These
standards, and any changes considered
in this rulemaking, would be directly
applicable to sources as a federal
program. Thus, federal, state, local, and
tribal government entities are not
affected by this proposed action. Table
1 shows the regulated categories
affected by this proposed action.
TABLE 1—NESHAP AND INDUSTRIAL SOURCE CATEGORIES AFFECTED BY THIS PROPOSED ACTION
NAICS code 1
NESHAP and source category
Chromium Electroplating NESHAP, Subpart N ..............
Chromium Anodizing Tanks ...........................................
Decorative Chromium Electroplating ..............................
Hard Chromium Electroplating .......................................
Steel Pickling—HCl Process Facilities And Hydrochloric Acid Regeneration Plants NESHAP, Subpart CCC
1 North
MACT code 2
332813
332813
332813
1607
1610
1615
3311, 3312
0310
American Industry Classification System.
Achievable Control Technology.
2 Maximum
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B. Where can I get a copy of this
document and other related
information?
In addition to being available in the
docket, an electronic copy of this
proposal will also be available on the
World Wide Web (WWW) through the
Technology Transfer Network (TTN).
Following signature by the EPA
Administrator, a copy of this proposed
action 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/atw/rrisk/rtrpg.html. The TTN
provides information and technology
exchange in various areas of air
pollution control.
Additional information is available on
the residual risk and technology review
(RTR) web page at https://www.epa.gov/
ttn/atw/rrisk/rtrpg.html. This
information includes source category
descriptions and detailed emissions and
other data that were used as inputs to
the risk assessments.
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C. What should I consider as I prepare
my comments for the EPA?
Submitting CBI. Do not submit
information containing CBI to the EPA
through https://www.regulations.gov or
email. Clearly mark the part or all of the
information that you claim to be CBI.
For CBI information on a disk or CD–
ROM that you mail to the EPA, mark the
outside of the disk or CD–ROM as CBI
and then identify electronically within
the disk or CD–ROM the specific
information that is claimed as CBI. In
addition to one complete version of the
comment that includes information
claimed as CBI, a copy of the comment
that does not contain the information
claimed as CBI must be submitted for
inclusion in the public docket. If you
submit a CD–ROM or disk that does not
contain CBI, mark the outside of the
disk or CD–ROM clearly that it does not
contain CBI. Information not marked as
CBI will be included in the public
docket and the EPA’s electronic public
docket without prior notice. Information
marked as CBI will not be disclosed
except in accordance with procedures
set forth in 40 CFR part 2. Send or
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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 Number
EPA–HQ–OAR–2010–0600.
D. When would a public hearing occur?
If a public hearing is held, it will be
held at 10:00 a.m. on February 23, 2012
and will be held at a location to be
determined. Persons interested in
presenting oral testimony at the hearing
should contact Mr. Phil Mulrine, Office
of Air Quality Planning and Standards,
Sector Policies and Programs Division
(D243–02), U.S. Environmental
Protection Agency, Research Triangle
Park, NC 27711, telephone (919) 541–
5289; fax number: (919) 541–3207;
email address: mulrine.phil@epa.gov.
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II. Background Information
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A. Overview of the Chromium
Electroplating and Chromium
Anodizing Source Categories
The Chromium Electroplating
NESHAP regulates emissions of
chromium compounds from three
source categories: hard chromium
electroplating, decorative chromium
electroplating, and chromium
anodizing. The NESHAP apply to both
major sources and area sources. The
NESHAP were promulgated on January
25, 1995 (60 FR 4963) and codified at
40 CFR part 63, subpart N. We proposed
amendments to the NESHAP on June 5,
2002 (67 FR 38810) to address issues
related to changes in control technology,
monitoring and implementation. The
amendments were promulgated on July
19, 2004 (69 FR 42885).
1. Hard Chromium Electroplating
The Hard Chromium Electroplating
source category consists of facilities that
plate base metals with a relatively thick
layer of chromium using an electrolytic
process. Hard chromium electroplating
provides a finish that is resistant to
wear, abrasion, heat, and corrosion.
These facilities plate large cylinders and
industrial rolls used in construction
equipment and printing presses,
hydraulic cylinders and rods, zinc die
castings, plastic molds, engine
components, and marine hardware.
The NESHAP distinguishes between
large hard chromium electroplating
facilities and small hard chromium
electroplating facilities. Large hard
chromium electroplating facilities are
defined as any such facility with a
cumulative annual rectifier capacity
equal to or greater than 60 million
ampere-hours per year (amp-hr/yr).
Small hard chromium electroplating
facilities are defined as any facility with
a cumulative annual rectifier capacity
less than 60 million amp-hr/yr. The
NESHAP requires all affected tanks
located at large hard chromium
electroplating facilities to meet an
emissions limit of 0.015 milligrams per
dry standard cubic meter (mg/dscm).
Alternatively, large hard chromium
facilities also can comply with the
NESHAP by maintaining the surface
tension limits in affected tanks equal to
or less than 45 dynes per centimeter
(dynes/cm), if measured using a
stalagmometer, or 35 dynes/cm, if
measured using a tensiometer.
The Chromium Electroplating
NESHAP requires affected tanks at
existing small hard chromium
electroplating facilities to meet an
emissions limit of 0.030 mg/dscm and
affected tanks at new small hard
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chromium electroplating facilities to
meet a limit of 0.015 mg/dscm.
Alternatively, these sources have the
option of complying with surface
tension limits equal to or less than 45
dynes per centimeter (dynes/cm), if
measured using a stalagmometer, or 35
dynes/cm, if measured using a
tensiometer. Under the current
NESHAP, any small hard chromium
electroplating tank for which
construction or reconstruction was
commenced on or before December 16,
1993 (i.e., the proposal date for the
original NESHAP) is subject to the
existing source standards and any small
hard chromium electroplating tank
constructed or reconstructed after
December 16, 1993 is subject to new
source standards.
We estimate that there currently are
approximately 230 large hard chromium
electroplating facilities and 450 small
hard chromium electroplating facilities
in operation. Of the 450 small hard
chromium electroplating facilities, we
estimate that 150 of these facilities have
one or more tanks that are subject to the
new source standards, and the affected
sources at the other 300 facilities are
subject to the existing source standards.
2. Decorative Chromium Electroplating
The Decorative Chromium
Electroplating source category consists
of facilities that plate base materials
such as brass, steel, aluminum, or
plastic with layers of copper and nickel,
followed by a relatively thin layer of
chromium to provide a bright, tarnishand wear-resistant surface. Decorative
chromium electroplating is used for
items such as automotive trim, metal
furniture, bicycles, hand tools, and
plumbing fixtures. We estimate that
there currently are approximately 590
decorative chromium electroplating
plants in operation. The NESHAP
requires all existing and new decorative
chromium electroplating sources to
meet an emissions limit of 0.01 mg/
dscm, or meet the surface tension limits
of 45 dynes/cm, if measured using a
stalagmometer, or 35 dynes/cm, if
measured using a tensiometer.
3. Chromium Anodizing
The Chromium Anodizing source
category consists of facilities that use
chromic acid to form an oxide layer on
aluminum to provide resistance to
corrosion. The chromium anodizing
process is used to coat aircraft parts
(such as wings and landing gears) as
well as architectural structures that are
subject to high stress and corrosive
conditions. We estimate that there
currently are about 180 chromium
anodizing plants in operation. The
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NESHAP requires all existing and new
chromium anodizing sources to meet an
emissions limit of 0.01 mg/dscm, or
meet the surface tension limits of 45
dynes/cm, if measured using a
stalagmometer, or 35 dynes/cm, if
measured using a tensiometer.
B. What is the history of the chromium
electroplating and chromium anodizing
risk and technology reviews?
Pursuant to section 112(f)(2) of the
CAA, we evaluated the residual risk
associated with the NESHAP in 2010. At
that time, we also conducted a
technology review, as required by
section 112(d)(6). Based on the results of
our initial residual risk and technology
reviews, we proposed on October 21,
2010 (75 FR 65071) that the risks due to
HAP emissions from these source
categories were acceptable and that no
additional controls were necessary to
provide an ample margin of safety to
protect public health because we had
not identified additional controls that
would reduce risk at reasonable costs.
Thus, we did not propose to revise the
NESHAP under 112(f)(2). However, as
explained in that proposal publication,
we were concerned about the potential
cancer risks due to emissions from this
category and asked for additional
information and comments on this
issue.
As a result of our technology review
in 2010, we proposed the following
amendments to the NESHAP to:
• Incorporate several housekeeping
practices into 40 CFR 63.342(f);
• phase out the use of wetting agent
fume suppressants (WAFS) based on
perfluorooctyl sulfonates (PFOS);
• revise the startup, shutdown, and
malfunction provisions (SSM) in the
rule;
• revise the monitoring and testing
requirements; and,
• make a few technical corrections to
the NESHAP.
The comment period for the October
21, 2010 proposal ended on December 6,
2010, and we are not re-opening the
comment period on those issues.
However, we will address the comments
we received during the October 21, 2010
to December 6, 2010 public comment
period at the time we take final action.
C. Overview of the Steel Pickling Source
Category
Steel pickling is a treatment process
in which the heavy oxide crust or mill
scale that develops on the steel surface
during hot forming or heat treating is
removed chemically in a bath of
aqueous acid solution. Pickling is a
process applied to metallic substances
that removes surface impurities, stains,
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or crusts to prepare the metal for
subsequent plating (e.g., with
chromium) or other treatment, such as
galvanization or painting. An acid
regeneration plant is defined in the rule
as the equipment and processes that
regenerate fresh hydrochloric acid
pickling solution from spent pickle
liquor using a thermal treatment
process. The HAP emission points from
the steel pickling process include steel
pickling baths, steel pickling sprays,
and tank vents. The HAP emission point
from acid regeneration plants is the
spray roaster.
We estimate that there are
approximately 80 facilities subject to the
MACT standards that are currently
performing steel pickling and/or acid
regeneration. Many of these facilities are
located adjacent to integrated iron and
steel manufacturing plants or electric
arc furnace steelmaking facilities
(minimills) that produce steel from
scrap. Facilities that regenerate HCl may
or may not be located at steel pickling
operations.
D. What is the history of the steel
pickling risk and technology review?
Pursuant to section 112(f)(2) of the
CAA, we evaluated the residual risk
associated with the NESHAP in 2010.
We also conducted a technology review,
as required by section 112(d)(6) of the
CAA. Based on the results of our
residual risk assessment, we proposed
on October 21, 2010 that the risks were
acceptable and that there were no
additional cost effective controls to
reduce risk further and that the
NESHAP provides an ample margin of
safety to protect public health and
prevented an adverse environmental
effect. In that notice, we also proposed
no changes based on the technology
review because we did not identify any
new, feasible technologies that
warranted changes to the NESHAP. We
are not taking comment on these
proposed determinations.
E. What data collection activities were
conducted to support this action?
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1. Chromium Electroplating and
Chromium Anodizing Source Categories
Several commenters expressed
concern that the data set used in the risk
assessment that was relied on for the
October 2010 proposal was not based on
actual data from an adequate number of
facilities and was not representative of
the current chromium electroplating
industry. In response to these
comments, we contacted 28 State and
local air pollution control agencies to
request information on the industry.
The requested information included
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facility data (name, location, number of
employees), process type, tank design
and operating parameters, annual hours
of operation, emission control
technology, control device operating
parameters, emission test data, and
other available supporting documents,
such as emission inventory reports and
operating permits. Agencies were asked
to provide data on the 5 to 10 facilities
that were likely to have the highest risk
based on either chromium emissions or
close proximity to sensitive receptors,
and any additional facilities for which
the data were readily available. The
agencies were also asked to review the
list of facilities we had in our
Chromium Electroplating Database and
update the list to the extent that they
had more recent information on plant
closings, new plants, or changes in
processes.
We received the most current data
available from a total of 24 agencies. We
supplemented the data provided by the
agencies with additional information we
obtained from operating permits and
other information downloaded from
State Web sites. We also received some
data from an industry organization (i.e.,
the National Association for Surface
Finishing, located in Washington, DC).
The updated data set included
information on 346 plants. After
eliminating redundancies in the data
and deleting data for facilities that were
no longer in operation or no longer
performing chromium electroplating or
anodizing, the new data set included
annual emissions for 301 plants
currently in operation. Of these,
approximately 128 plants were located
in California, and 173 plants were
located in other States. Finally, we
performed a quality control check of
plant geographic coordinates and
updated the coordinates for
approximately 400 plants, focusing on
those plants most likely to have high
emissions.
We believe the current data set to be
significantly better than the data set we
relied on for the 2010 proposal for a
number of reasons. The current data set
provides improved emissions estimates
for many facilities, based on actual
emissions test data; provides actual
emissions data for a larger number of
facilities than had been modeled for the
2010 proposal; includes an updated
plant list that accounts for facilities that
have opened recently and eliminates
nearly 200 plants that have recently
closed or have stopped performing
chromium electroplating; includes more
plant-specific data on numbers and
types of electroplating tanks, types of
emissions controls, and control system
operating parameters; and corrected
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geographic locations (latitudes,
longitudes) for hundreds of chromium
electroplating and anodizing facilities.
For the October 21, 2010, proposal we
used the actual emissions data available
at the time, which covered far fewer
plants, and, in many cases, were based
on general emission factors and other
data not specific to the plant in
question. To fill in data gaps for the
October 2010 proposal, we relied on
plant capacity, process design, process
operating, and control device data
collected during the development of the
original MACT standard in the early
1990’s to develop a series of model
plants for each process (hard chromium
electroplating, decorative chromium
electroplating, and chromium
anodizing). We used theoretical
emissions estimates for the model plants
to represent actual facilities in
operation. As we have collected much
more data on actual emissions from
facilities currently in operation, we now
realize that the emission estimates based
on pre-MACT data used for the October
proposal significantly overestimated
emissions. In addition, we modeled all
of the unknown facilities (i.e., the
facilities where we did not know the
type of plating) using the hard
chromium electroplating emission factor
developed from the model plants. Since
hard chromium electroplating facilities
have the highest emissions among the
three source categories this resulted in
very conservative estimates of emissions
for those unknown sources.
The list of plants in our current data
set much better reflects the current
status of the industry. First, it better
reflects the status because we have
greatly improved the locations of several
hundred plants, which is critical in
assessing risk. Second, the emissions
data in the current data set better reflect
actual emissions from facilities
currently in operation because it reflects
emission levels since implementation of
the NESHAP.
In addition, having more accurate
data on such things as the emission
controls in use, the number of affected
electroplating and anodizing tanks, tank
operating parameters, facility types,
stack parameters (such as exhaust flow
rates), and other information allowed us
to better estimate current nationwide
emissions and the cost and
environmental impacts associated with
the control options. More details on the
data collection activities for this
supplemental proposal are provided in
the technical document ‘‘Information on
Chromium Electroplating Facilities
Collected from State and Local Agencies
from January to March 2011,’’ which is
available in the docket for this action.
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Additional details on the industry data
collected are provided in the technical
document ‘‘Profile of Chromium
Electroplating Processes and
Emissions,’’ which is available in the
docket for this action.
2. Steel Pickling Source Category
We had sufficient emissions data for
this source category at the time of the
October 21, 2010 proposal for the risk
analysis. Nevertheless, subsequent to
the close of the comment period, we
gathered more data and information
regarding the status of facility processes
and controls, and we further evaluated
the MACT rule to determine if any
updates or corrections would be
appropriate.
III. Analyses Performed
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A. How did we perform the technology
review?
For our October 2010 proposal, we
performed several activities for
purposes of evaluating developments in
practices, processes, and control
technologies for the chromium
electroplating source categories: (1) We
reviewed comments received on the
proposed 2002 amendments to the
Chromium Electroplating NESHAP (67
FR 38810, June 5, 2002) to determine
whether they identified any
developments that warranted further
consideration; (2) we reviewed the
supporting documentation for the 2007
amendments to California’s Airborne
Toxic Control Measure (ATCM) for
Chromium Plating and Chromium
Anodizing Facilities; and (3) we
searched the RACT/BACT/LAER
Clearinghouse (RBLC) and the Internet
to identify other practices, processes, or
control technologies that could be
applied to chromium electroplating.
The October 21, 2010 proposal of the
Chromium Electroplating NESHAP
identified four developments in
practices, processes, and control
technologies that were considered for
the technology review: emission
elimination devices, high efficiency
particulate air (HEPA) filters, wetting
agent fume suppressants (WAFS), and
housekeeping practices. These
technologies and practices are described
in detail in the October 2010 proposal.
Furthermore, our initial analyses,
findings, and conclusions regarding
these developments are discussed in the
preamble to the October 2010 proposal.
The following paragraphs describe
additional analyses that were performed
for today’s supplemental proposal.
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1. Emissions Limits
a. Large Hard Chromium
Electroplating. Most large hard
chromium facilities currently have one
or more add-on control devices such as
packed bed scrubbers (PBS), composite
mesh pad (CMP) scrubbers, mesh pad
mist eliminators (MPMEs), high
efficiency scrubbers, or HEPA filters.
Some facilities use add-on controls plus
WAFS to limit emissions. However,
some facilities control their emissions
using only WAFS and have no add-on
control device.
To evaluate how effective the
emission control technologies currently
used on existing large hard chromium
electroplating sources are in reducing
emissions and meeting the emissions
limit, we compiled the available data on
emission concentration (mg/dscm) we
collected from the 24 State and local
agencies and ranked the data from
lowest to highest. We have data from 75
tanks located at 38 facilities. We then
reviewed the data to better understand
where existing sources operated with
respect to the emissions limit. That is,
we looked at the number of sources that
operated at or below various emission
levels, including 75 percent of the
emissions limit, 50 percent of the
emissions limit, and 40 percent of the
emissions limit.
The data indicate that most of these
sources operate well below the 0.015
mg/dscm emissions limit. For example,
approximately 88 percent of existing
sources operate at less than 75 percent
of the emissions limit (i.e., below 0.011
mg/dscm); 72 percent of sources operate
at less than 50 percent of the emissions
limit (i.e., below 0.0075 mg/dscm); and
about 67 percent of existing large hard
chromium electroplating sources
achieve emissions below 0.006 mg/
dscm. We then considered several
options for reducing the emissions and
weighed the costs and emissions
reductions associated with each option.
Further discussion of these options and
the proposed decisions are presented in
section IV below.
For purpose of addressing new large
chromium electroplating facilities, we
considered the feasibility of a more
stringent emissions limit. Specifically,
we examined what emission level could
be met using available add-on control
devices (such as with a CMP, MPME, or
high efficiency scrubber) or a
combination of add-on controls (such as
a CMP plus a HEPA filter or an MPME
plus a HEPA filter) and the emissions
concentrations that could be achieved
by using a combination of add-on
control technology and WAFS. The
results of this analysis and the proposed
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decisions are described in section IV
below.
b. Small Hard Chromium
Electroplating. For small hard
chromium electroplating facilities, we
performed the same type of analyses
described in the previous section for
large hard chromium electroplating. In
terms of emissions limits, the NESHAP
distinguishes between existing facilities,
which are subject to an emissions limit
of 0.030 mg/dscm, and new facilities,
which are subject to an emissions limit
of 0.015 mg/dscm. We compiled and
ranked the available data, which also
indicate that the large majority of
sources operate well below the current
emissions limits. We have data on
emissions concentrations for 73 tanks at
56 facilities located in States other than
California which were used for this
ranking. We estimate that there are a
total of 414 small hard chromium plants
located in States other than California.
We estimate that there are a total of 450
plants nationwide, with about 36 plants
located in California. We considered
different options for reducing the
emissions limits. We also considered
removing the existing distinction
between existing and new, as they are
currently defined in the NESHAP,
because many of the ‘‘new’’ facilities
have been in operation for more than 17
years and we were considering
proposing a more stringent new source
standard for all sources. We evaluated
the impacts, in terms of costs and
emissions reductions, that would result
for various potential proposed
emissions limits at or below 0.015 mg/
dscm. We did not evaluate potential
limits greater than 0.015 mg/dscm since
about one-third of the currently
operating small hard chromium sources
are already subject to an emissions limit
of 0.015 mg/dscm. Specifically, we
considered two main options: (1)
Propose that all small hard chromium
electroplating facilities currently in
operation meet an emissions limit of
0.015 mg/dscm, and (2) propose that all
small hard chromium electroplating
facilities currently in operation meet an
emissions limit of 0.010 mg/dscm. The
results of this analysis and the proposed
decisions are described in section IV
below.
We also considered revising the
definition of new small hard chromium
electroplating facilities, based on the
proposal date for this action, and
requiring those facilities to meet a more
stringent emissions limit. The results of
this analysis and the proposed decisions
are described in section IV below.
c. Decorative Chromium
Electroplating. For decorative chromium
electroplating, we intended to perform
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analyses similar to that performed for
hard chromium electroplating.
However, the data set for decorative
chromium electroplating was much
smaller (e.g., 20 data points for
decorative chromium electroplating vs.
75 data points for large hard chromium),
and we did not think the data were
adequate for considering several
different emissions reductions options.
The primary reason for the smaller data
set is that the most commonly used
method for controlling emissions from
decorative chromium electroplating is
adding WAFS to the electroplating tank
bath. Since sources that use WAFS and
comply with the surface tension limits
are not required to conduct an emission
test, there are limited test data available.
However, we did rank the available
data on existing sources in the
decorative chromium electroplating
source category by emissions level to
determine the typical level of emissions
performance and range of performance
among those sources to determine
options for revising these limits. All the
facilities for which we have data have
emissions concentrations less than
0.007 mg/dscm (i.e., at least 30 percent
below the applicable emissions limit of
0.010 mg/dscm). Further discussion of
this analysis and the proposed decisions
for existing and new decorative
chromium electroplating sources are
presented in section IV below.
d. Chromium Anodizing. In the case
of chromium anodizing, we had only a
single data point (0.0016 mg/dscm),
which is significantly below the current
emissions limit of 0.010 mg/dscm.
However, we concluded that the data on
decorative chromium electroplating was
relevant to determining the feasible
options for chromium anodizing. For
one, many chromium anodizing sources
(approximately 50 percent) are
controlled using only WAFS. It was for
this reason that the current NESHAP
specifies the same emissions limits of
0.010 mg/dscm for both chromium
anodizing and decorative chromium
electroplating sources. In addition,
chromium anodizing plants are
comparable to decorative chromium
electroplating plants with respect to the
relative magnitude of chromium
emissions. Finally, the feasibility and
options for controlling emissions from
chromium anodizing are similar to those
for decorative chromium. Further
discussion of this analysis and the
proposed decisions for existing and new
chromium anodizing sources are
presented in section IV below.
2. Surface Tension Limits
The NESHAP provides that affected
sources must either meet an emissions
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limit specified in the NESHAP or must
maintain the surface tension in
chromium electroplating or chromium
anodizing tanks below one of two
specified surface tension limits,
depending on the type of instrument
used to measure surface tension. Despite
the fact that the emissions limits for the
three chromium electroplating source
categories differ, the surface tension
limits in the current NESHAP are the
same for all three source categories and
are the same for existing and new
sources, as follows: if a stalagmometer is
used to measure surface tension, the
surface tension limit is 45 dynes/cm,
and, if a tensiometer is used, the surface
tension limit is 35 dynes/cm. The
available data, which are described in
detail in the technical document
‘‘Development of Revised Surface
Tension Limits for Chromium
Electroplating and Anodizing Tanks
Controlled with Wetting Agent Fume
Suppressants,’’ which is available in the
docket, indicate that maintaining the
surface tension below these limits
ensures that emissions are below 0.01
mg/dscm, which is the most stringent
limit currently in the NESHAP.
As part of the information collection
described in section II.E of this
preamble, we obtained test data for
several decorative and hard chromium
electroplating sources controlled using
only WAFS. These data on surface
tension and emission concentration
were evaluated to determine the
relationship between emissions and
surface tension. We analyzed these data
to evaluate the feasibility of requiring
lower surface tension limits and the
corresponding emissions levels. Further
details of this analysis and the results,
and the proposed decisions based on
this analysis, are presented below in
section IV.A.
B. For purposes of this supplemental
proposal, how did we estimate the risk
posed by each of the three chromium
electroplating source categories?
The EPA conducted a risk assessment
that provided estimates of the maximum
individual risk (MIR) posed by HAP
emissions from sources in the source
category and the hazard index (HI) for
chronic exposures to HAP with the
potential to cause noncancer health
effects. The assessment also provided
estimates of the distribution of cancer
risks within the exposed populations,
cancer incidence, and an evaluation of
the potential for adverse environmental
effects for each source category. The
docket for this rulemaking contains the
following document which provides
more information on the risk assessment
inputs and models: Residual Risk
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6633
Assessment for the Chromic Acid
Anodizing, Decorative Chromium
Electroplating, and Hard Chromium
Electroplating Source Categories. The
methods used to assess risks are
consistent with those peer-reviewed by
a panel of the EPA’s Science Advisory
Board (SAB) in 2009 and described in
their peer review report issued in
2010 1; they are also consistent with the
key recommendations contained in that
report.
1. Estimating Actual Emissions
As explained previously, the revised
data set for the Chromium
Electroplating NESHAP source
categories includes significantly
improved emissions data for many more
plants than the data set used for the
October 2010 proposal. However, to
assess nationwide residual risk, it was
still necessary to estimate emissions for
much of the industry. Rather than
estimate those emissions using the
model plant approach used for the
October 2010 proposal, we used a
Monte Carlo procedure to simulate
actual emissions for those plants for
which actual emissions data were not
available. The simulation model used
the pool of available data on actual
emissions concentrations, exhaust flow
rates, and annual operating hours for
each process type (hard chromium
electroplating, decorative chromium
electroplating, and chromium
anodizing). Actual emissions data
(lbs/yr) were fitted to a Weibull
distribution and emissions for plants for
which emissions were unknown were
simulated using the actual data for each
plant type. Because process-specific
data were used to simulate emissions for
each facility, it was necessary to identify
the process type for each of the plants.
Although the process type was known
for many plants, it was unknown for a
large number of other plants. By scaling
up the data on known plants, and using
other available data on the industry, the
profile of the current chromium
electroplating industry was estimated in
terms of the number of each type of
plant.
One of the primary goals in
simulating actual annual emissions was
to develop a data set of emissions
estimates that best represents chromium
electroplating plants operating in the
U.S. For this reason, a distinction was
made between chromium electroplating
plants located in California and plants
located elsewhere (i.e., the non1 U.S. EPA SAB. Risk and Technology Review
(RTR) Risk Assessment Methodologies: For Review
by the EPA’s Science Advisory Board with Case
Studies—MACT I Petroleum Refining Sources and
Portland Cement Manufacturing, May 2010.
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California plants). Because chromium
electroplating plants located in
California are subject to emissions limits
that are significantly more stringent
than the limits specified in the
NESHAP, they typically use multiple
emissions controls, including HEPA
filters in many cases, to reduce
emissions. Thus, emissions for
California plants are not representative
of emissions for non-California plants.
For this reason, the data on California
plants were not included in the data set
used to simulate emissions for plants
located in other States. However, the
data on actual emissions from plants
located in California were used to
estimate emissions for other plants in
California. Thus, we did not exclude the
California data from the overall analysis;
we treated the data from plants in
California differently. (Additional
details on the emissions data for the
California plants are provided below.)
Based on the total numbers of plants
nationwide, plant types were randomly
assigned to each of the unknown plants,
while ensuring that the total numbers of
each type of plants nationwide were
preserved. After assigning plant types,
emissions for each plant was simulated
5,000 times using only the data for that
specific type of plant (e.g., only data for
small hard chromium electroplating
plants were used to simulate emissions
for a small hard chromium
electroplating plant). Once all 5,000
simulations were completed, the mean
of the simulated values for each plant
was determined and that value was used
to populate the risk modeling file on
actual emissions.
Taking into account all of the new
emissions data collected following the
public comment period for the October
2010 proposal, plus the good quality
emissions data collected previously, the
data set included emissions estimates
for a total of 301 plants. Of these,
approximately 128 plants were located
in California, and 173 plants were
located in other States. A review of the
data indicated that emissions for the
California plants were significantly
lower than emissions for the nonCalifornia plants. For example,
emissions from the large hard chromium
electroplating plants in California
averaged 0.027 lbs/yr, whereas the
average for the non-California large hard
chromium plants was 2.62 lbs/yr. For
small hard chromium electroplating, the
California plants averaged 0.0095 lbs/yr
and the non-California plants averaged
0.56 lbs/yr. For decorative chromium
electroplating, the average emissions
were 0.00042 lbs/yr (California) and
0.55 lbs/yr (non-California). For
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chromium anodizing, the average
emissions were 0.00035 lbs/yr
(California) and 0.46 lbs/yr (nonCalifornia). These results clearly
indicated that the data for plants in
California were not representative of
plants located outside of California. For
this reason, all subsequent analyses
related to estimating emissions for
plants located outside of California were
performed using only data for nonCalifornia plants.
For the California plants we used the
emissions estimates as reported. For all
the plants outside of California, we used
actual emissions estimates if they were
available. For the other plants we used
the simulation model described above to
estimate emissions.
Overall, we believe that the resulting
emissions simulated by the model are
much more representative of actual
emissions on average and also are more
representative of the variability of
emissions from plant to plant.
Additional details on the simulation
approach can be found in the emissions
technical document ‘‘Simulation of
Actual and Allowable Emissions for
Chromium Electroplating Facilities,’’
which is available in the docket for this
rulemaking.
2. Estimating MACT-Allowable
Emissions
To estimate allowable annual
emissions (e.g., lbs/yr) for those plants
for which actual emissions
concentration data were available, we
calculated the allowable annual
emissions using the MACT emissions
limit. In other words, we scaled up
actual annual emissions for those plants
using the ratio of the emissions
concentration (measured during the
performance test) to the MACT limit.
For example, if the measured
concentration for a large hard chromium
plant was 0.0075 mg/dscm, which is
one-half of the 0.015 mg/dscm
emissions limit, we scaled up annual
emissions by a factor or 2. For those
plants for which we did not have actual
emissions data, we used the same
emissions simulation approach used to
estimate actual emissions, as described
previously. That is, data for California
plants were excluded from the analysis;
process types were assigned to each
plant for which the process was
unknown, while ensuring that the total
number of each type of plant matched
the estimated numbers of plants
nationwide; and a Monte Carlo
simulation model was developed using
the pool of available data on emissions
concentrations, exhaust flow rates, and
annual operating hours for each process
type to simulate allowable emissions for
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each plant. However, instead of using
the actual emissions concentration data
in the simulation model, we used the
corresponding MACT emissions limit.
Thus, we calculated the allowable
emissions by using the pool of available
data on exhaust flow rates and annual
operating hours for each process type
and assumed each source had emissions
concentrations equal to the MACT
emissions limit (i.e., we assumed they
were emitting at the maximum level
allowed by the MACT standard). For
example, to estimate the allowable
emissions for a large hard chromium
electroplating plant, data on large hard
chromium plant exhaust flow rates and
annual operating hours were used, along
with an emissions concentration of
0.015 mg/dscm, which is the emissions
limit specified in the NESHAP for large
hard chromium electroplating plants. As
was used for calculating actual
emissions estimates, 5,000 simulations
were performed for each plant, and the
average of simulated values was used to
represent allowable emissions for the
plant. Additional details on the
simulation approach can be found in the
emissions technical document
‘‘Simulation of Actual and Allowable
Emissions for Chromium Electroplating
Facilities,’’ which is available in the
docket for this rulemaking.
3. Conducting Dispersion Modeling,
Determining Inhalation Exposures, and
Estimating Individual and Population
Inhalation Risks
Both long-term and short-term
inhalation exposure concentrations and
health risks from the three chromium
electroplating source categories were
estimated using the Human Exposure
Model (HEM–3). The HEM–3 performs
three of the primary risk assessment
activities listed above: (1) Conducting
dispersion modeling to estimate the
concentrations of HAP in ambient air,
(2) estimating long-term and short-term
inhalation exposures to individuals
residing within 50 kilometers (km) of
the modeled sources, and (3) estimating
individual and population-level
inhalation risks using the exposure
estimates and quantitative doseresponse information.
The air dispersion model used by the
HEM–3 model (AERMOD) is one of the
EPA’s preferred models for assessing
pollutant concentrations from industrial
facilities.2 To perform the dispersion
modeling and to develop the
preliminary risk estimates, HEM–3
2 U.S. EPA. Revision to the Guideline on Air
Quality Models: Adoption of a Preferred General
Purpose (Flat and Complex Terrain) Dispersion
Model and Other Revisions (70 FR 68218,
November 9, 2005).
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draws on three data libraries. The first
is a library of meteorological data,
which is used for dispersion
calculations. This library includes 1
year of hourly surface and upper air
observations for approximately 200
meteorological stations, selected to
provide coverage of the United States
and Puerto Rico. A second library, of
United States Census Bureau census
block 3 internal point locations and
populations, provides the basis of
human exposure calculations (Census,
2010). In addition, for each census
block, the census library includes the
elevation and controlling hill height,
which are also used in dispersion
calculations. A third library of pollutant
unit risk factors and other health
benchmarks is used to estimate health
risks. These risk factors and health
benchmarks are the latest values
recommended by the EPA for HAP and
other toxic air pollutants. These values
are available at https://www.epa.gov/ttn/
atw/toxsource/summary.html and are
discussed in more detail later in this
section.
In developing the risk assessment for
chronic exposures, we used the
estimated annual average ambient air
concentrations of chromium emitted by
each source. The air concentrations at
each nearby census block centroid were
used as a surrogate for the chronic
inhalation exposure concentration for
all the people who reside in that census
block. We calculated the MIR for each
facility as the cancer risk associated
with a continuous lifetime (24 hours per
day, 7 days per week, and 52 weeks per
year for a 70-year period) exposure to
the maximum concentration at the
centroid of inhabited census blocks.
Individual cancer risks were calculated
by multiplying the estimated lifetime
exposure to the ambient concentration
of chromium (in micrograms per cubic
meter (mg/m3)) by its unit risk estimate
(URE), which is an upper bound
estimate of an individual’s probability
of contracting cancer over a lifetime of
exposure to a concentration of 1
microgram of the pollutant per cubic
meter of air. For residual risk
assessments, we generally use URE
values from the EPA’s Integrated Risk
Information System (IRIS). For
carcinogenic pollutants without the EPA
IRIS values, we look to other reputable
sources of cancer dose-response values,
often using California EPA (CalEPA)
URE values, where available. In cases
where new, scientifically credible dose
response values have been developed in
a manner consistent with the EPA
3 A census block is the smallest geographic area
for which census statistics are tabulated.
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guidelines and have undergone a peer
review process similar to that used by
the EPA, we may use such doseresponse values in place of, or in
addition to, other values, if appropriate.
Incremental individual lifetime
cancer risks were estimated as the sum
of the risks for each of the carcinogenic
HAP (including those classified as
carcinogenic to humans, likely to be
carcinogenic to humans, and suggestive
evidence of carcinogenic potential 4)
emitted by the modeled source. Cancer
incidence and the distribution of
individual cancer risks for the
population within 50 km of the sources
were also estimated for the source
category as part of this assessment by
summing individual risks. A distance of
50 km is consistent with both the
analysis supporting the 1989 Benzene
NESHAP (54 FR 38044) and the
limitations of Gaussian dispersion
models, including AERMOD.
To assess the risk of non-cancer
health effects from chronic exposures,
we summed the HQ for each of the HAP
that affects a common target organ
system to obtain the HI for that target
organ system (or target organ-specific
HI, TOSHI). The HQ is the estimated
exposure divided by the chronic
reference value, which is either the EPA
reference concentration (RfC), defined
as ‘‘an estimate (with uncertainty
spanning perhaps an order of
magnitude) of a continuous inhalation
exposure to the human population
(including sensitive subgroups) that is
likely to be without an appreciable risk
of deleterious effects during a lifetime,’’
or, in cases where an RfC from the
EPA’s IRIS database is not available, the
EPA will utilize the following
prioritized sources for our chronic doseresponse values: (1) The Agency for
Toxic Substances and Disease Registry
Minimum Risk Level, which is defined
as ‘‘an estimate of daily human
exposure to a substance that is likely to
be without an appreciable risk of
adverse effects (other than cancer) over
a specified duration of exposure’’; (2)
the CalEPA Chronic Reference Exposure
Level (REL), which is defined as ‘‘the
4 These classifications also coincide with the
terms ‘‘known carcinogen, probable carcinogen, and
possible carcinogen,’’ respectively, which are the
terms advocated in the EPA’s previous Guidelines
for Carcinogen Risk Assessment, published in 1986
(51 FR 33992, September 24, 1986). Summing the
risks of these individual compounds to obtain the
cumulative cancer risks is an approach that was
recommended by the EPA’s Science Advisory Board
(SAB) in their 2002 peer review of EPA’s National
Air Toxics Assessment (NATA) entitled, NATA—
Evaluating the National-scale Air Toxics
Assessment 1996 Data—an SAB Advisory, available
at: https://yosemite.epa.gov/sab/sabproduct.nsf/
214C6E915BB04E14852570CA007A682C/$File/
ecadv02001.pdf.
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concentration level at or below which
no adverse health effects are anticipated
for a specified exposure duration’’; and
(3), as noted above, in cases where
scientifically credible dose-response
values have been developed in a manner
consistent with the EPA guidelines and
have undergone a peer review process
similar to that used by the EPA, we may
use those dose-response values in place
of or in concert with other values.
4. Conducting Multipathway Exposure
and Risk Screening
As explained in the October 2010
proposal, chromium electroplating
facilities do not emit any of the 14 PB–
HAP compounds or compound classes
identified for the multipathway
screening in the EPA’s Air Toxics Risk
Assessment Library (available at https://
www.epa.gov/ttn/fera/
risk_atra_vol1.html). Because none of
these PB–HAP are emitted by sources in
the chromium electroplating source
categories, we concluded at the time of
the proposal that there is low potential
for significant non-inhalation human or
environmental risks for these source
categories. The data we received since
proposal continues to indicate that
chromium electroplating sources do not
emit any of those 14 PB–HAP
compounds or compound classes.
5. Conducting Other Analyses: FacilityWide Risk Assessments and
Demographic Analyses
a. Facility-Wide Risk
To put the source category risks in
context, we examined the risks from the
entire ‘‘facility,’’ where the facility
includes all HAP-emitting operations
within a contiguous area and under
common control. In other words, for
each facility that includes one or more
sources from a source category under
review, we examined the HAP
emissions not only from that source
category, but also emissions of HAP
from all other emission sources at the
facility. The emissions data for
generating these ‘‘facility-wide’’ risks
were obtained from the 2005 NEI. We
analyzed risks due to the inhalation of
HAP that are emitted ‘‘facility-wide’’ for
the populations residing within 50 km
of each facility, consistent with the
methods used for the source category
analysis described above. For these
facility-wide risk analyses, the modeled
source category risks were compared to
the facility-wide risks to determine the
portion of facility-wide risks that could
be attributed to each of the three
chromium electroplating source
categories. We specifically examined the
facility that was associated with the
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highest estimate of risk and determined
the percentage of that risk attributable to
the source category of interest. The risk
documentation available through the
docket for this action provides all
facility-wide risks and the percentage of
source category contribution for the
three chromium electroplating source
categories.
The methodology and results of the
facility-wide analyses for each source
category are included in the residual
risk documentation as referenced in
section IV of this preamble, which is
available in the docket for this action.
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b. Demographic Analysis
To examine the potential for any
environmental justice (EJ) issues that
might be associated with these source
categories, we performed demographic
analyses of the at-risk populations for
two of the three chromium
electroplating categories. We performed
these analyses for only these two source
categories because the chromium
anodizing source category is not
associated with significant populations
with estimated cancer risks above 1 in
a million. For the hard and decorative
chromium electroplating source
categories, we evaluated the percentages
of different social, demographic and
economic groups within the populations
living near the facilities who were
estimated to be subjected to cancer risks
greater than 1 in a million due to HAP
emissions from chromium
electroplating. We compared the
percentages of these demographic
groups to the total percentages of those
demographic groups nationwide. The
methodology and results of the
demographic analyses are included in
the technical reports: ‘‘Risk and
Technology Review—Analysis of SocioEconomic Factors for Populations
Living Near Hard Chromium
Electroplating Facilities’’; and ‘‘Risk and
Technology Review—Analysis of SocioEconomic Factors for Populations
Living Near Decorative Chromium
Electroplating Facilities.’’ These reports
are available in the docket for this
action.
6. Considering Uncertainties in Risk
Assessment
Uncertainty and the potential for bias
are inherent in all risk assessments,
including those performed for the
source category addressed in this
supplemental proposal. Although
uncertainty exists, we believe that our
approach, which used conservative
tools and assumptions, ensures that our
decisions are health-protective. A brief
discussion of the uncertainties in the
emissions data set, dispersion modeling,
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inhalation exposure estimates and doseresponse relationships follows below. A
more thorough discussion of these
uncertainties is included in the risk
assessment documentation available in
the docket for this action.
a. Uncertainties in the Emissions Data
Set
Although the development of the RTR
data sets involved quality assurance/
quality control processes, the accuracy
of emissions values will vary depending
on the source of the data, the degree to
which data are incomplete or missing,
the degree to which assumptions made
to complete the data sets are inaccurate,
errors in estimating emissions values,
and other factors.
The emission estimates considered in
this analysis generally are annual totals
for certain years that do not reflect
short-term fluctuations during the
course of a year or variations from year
to year. Additionally, although we
believe that we have good data for
hundreds of facilities in these source
categories in our RTR data set, our data
set does not include data for many other
existing facilities.
To simulate emissions estimates for
plants for which we did not have actual
emissions estimates, separate data sets
were compiled for each process type:
large hard chromium electroplating,
small hard chromium electroplating,
decorative chromium electroplating,
and chromium anodizing. The data sets
included combinations of actual data on
emissions concentrations, exhaust flow
rates, annual operating hours, and
hourly emission rates. In addition,
assumptions were used to fill in some
of the data gaps. For example, if, for a
specific facility, data on all parameters
except exhaust flow rate were known,
the exhaust flow rate was estimated
using average flow rate data for other
plants of similar process (e.g., large hard
chromium electroplating). A similar
procedure was used to estimate annual
operating hours if all data except for
annual operating hours were known.
The relative sizes of the data sets used
to simulate emissions also introduce
various levels of uncertainty in the
simulations: the smaller the data set, the
greater the variability in the analysis,
and the greater the uncertainty in the
emissions estimates. For example, the
data set for chromium anodizing was
the smallest and, therefore, is expected
to have the highest level of uncertainty;
the data set for large hard chromium
electroplating was the largest and is
expected to have the lowest degree of
uncertainty in the emissions
simulations.
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Moreover, even after collecting the
additional information, we still had
many sources in our data set for which
we did not know the type of facility
(e.g., hard chromium electroplating,
decorative chromium electroplating, or
chromium anodizing). To assign source
types to these unknown sources for the
model input file, we first determined
the percent of each of the type of
sources among the sources for which we
have data, then we assumed that the
remaining unknown sources (those for
which we did not know the source type)
would comprise the same percentages
for each type. Finally, we randomly
assigned a source type to each unknown
plant based on these percentages. For
further details on these data, the
simulation approach, and the associated
uncertainties, see the technical
document ‘‘Simulation of Actual and
Allowable Emissions for Chromium
Electroplating Facilities,’’ which is
available in the docket.
In terms of speciation, it was assumed
that emissions from all chromium
electroplating sources consisted of 98
percent hexavalent chromium and 2
percent trivalent chromium. The actual
speciation of chromium in exhaust
streams may vary slightly from source to
source. However, historical data
indicate that emissions from chromium
electroplating sources are almost
entirely comprised of hexavalent
chromium, and the 98%/2% assumed
speciation was believed to be
representative of sources on average.
b. Uncertainties in Dispersion Modeling
While the analysis employed the
EPA’s recommended regulatory
dispersion model, AERMOD, we
recognize that there is uncertainty in
ambient concentration estimates
associated with any model, including
AERMOD. In circumstances where we
had to choose between various model
options, where possible, model options
(e.g., rural/urban, plume depletion,
chemistry) were selected to provide an
overestimate of ambient air
concentrations of the HAP rather than
underestimates. However, because of
practicality and data limitation reasons,
some factors (e.g., meteorology, building
downwash) have the potential in some
situations to overestimate or
underestimate ambient impacts. For
example, meteorological data were
taken from a single year (1991) and
facility locations can be a significant
distance from the site where these data
were taken.
c. Uncertainties in Inhalation Exposure
The effects of human mobility on
exposures were not included in the
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assessment. Specifically, short-term
mobility and long-term mobility
between census blocks in the modeling
domain were not considered.5 The
assumption of not considering short or
long-term population mobility does not
bias the estimate of the theoretical MIR,
nor does it affect the estimate of cancer
incidence because the total population
number remains the same. It does,
however, affect the shape of the
distribution of individual risks across
the affected population, shifting it
toward higher estimated individual
risks at the upper end and reducing the
number of people estimated to be at
lower risks, thereby increasing the
estimated number of people at specific
high risk levels (e.g., one in 10,000 or
one in one million).
In addition, the assessment predicted
the chronic exposures at the centroid of
each populated census block as
surrogates for the exposure
concentrations for all people living in
that block. Using the census block
centroid to predict chronic exposures
tends to over-predict exposures for
people in the census block who live
farther from the facility and underpredict exposures for people in the
census block who live closer to the
facility. Thus, using the census block
centroid to predict chronic exposures
may lead to a potential understatement
or overstatement of the true maximum
impact, but is an unbiased estimate of
average risk and incidence.
The assessment evaluates the cancer
inhalation risks associated with
pollutant exposures over a 70-year
period, which is the assumed lifetime of
an individual. In reality, both the length
of time that modeled emissions sources
at facilities actually operate (i.e., more
or less than 70 years), and the domestic
growth or decline of the modeled
industry (i.e., the increase or decrease in
the number or size of United States
facilities), will influence the future risks
posed by a given source or source
category. Depending on the
characteristics of the industry, these
factors will, in most cases, result in an
overestimate both in individual risk
levels and in the total estimated number
of cancer cases. However, in rare cases,
where a facility maintains or increases
its emissions levels beyond 70 years,
residents live beyond 70 years at the
same location, and the residents spend
most of their days at that location, then
the risks could potentially be
underestimated. Annual cancer
5 Short-term mobility is movement from one
micro-environment to another over the course of
hours or days. Long-term mobility is movement
from one residence to another over the course of a
lifetime.
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incidence estimates from exposures to
emissions from these sources would not
be affected by uncertainty in the length
of time emissions sources operate.
The exposure estimates used in these
analyses assume chronic exposures to
ambient levels of pollutants. Because
most people spend the majority of their
time indoors, actual exposures may not
be as high, depending on the
characteristics of the pollutants
modeled. For many of the HAP, indoor
levels are roughly equivalent to ambient
levels, but for very reactive pollutants or
larger particles, these levels are
typically lower. This factor has the
potential to result in an overstatement of
25 to 30 percent of exposures.6
In addition to the uncertainties
highlighted above, there are several
factors specific to the acute exposure
assessment that should be highlighted.
The accuracy of an acute inhalation
exposure assessment depends on the
simultaneous occurrence of
independent factors that may vary
greatly, such as hourly emissions rates,
meteorology, and human activity
patterns. In this assessment, we assume
that individuals remain for 1 hour at the
point of maximum ambient
concentration as determined by the cooccurrence of peak emissions and worstcase meteorological conditions. These
assumptions would tend to be worstcase actual exposures as it is unlikely
that a person would be located at the
point of maximum exposure during the
time of worst-case impact.
d. Uncertainties in Dose-Response
Relationships
There are uncertainties inherent in
the development of the dose-response
values used in our risk assessments for
cancer effects from chronic exposures
and non-cancer effects from both
chronic and acute exposures. Some
uncertainties may be considered
quantitatively, and others generally are
expressed in qualitative terms. We note
as a preface to this discussion a point on
dose-response uncertainty that is
brought out in the EPA’s 2005 Cancer
Guidelines; namely, that ‘‘the primary
goal of EPA actions is protection of
human health; accordingly, as an
Agency policy, risk assessment
procedures, including default options
that are used in the absence of scientific
data to the contrary, should be health
protective’’ (EPA 2005 Cancer
Guidelines, pages 1–7). This is the
approach followed here, as summarized
in the next several paragraphs. A
6 U.S. EPA. National-Scale Air Toxics Assessment
for 1996. (EPA 453/R–01–003; January 2001; page
85.)
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complete detailed discussion of
uncertainties and variability in doseresponse relationships is given in the
residual risk documentation which is
available in the docket for this action.
Cancer URE values used in our risk
assessments are those that have been
developed to generally provide an upper
bound estimate of risk. That is, they
represent a ‘‘plausible upper limit to the
true value of a quantity’’ (although this
is usually not a true statistical
confidence limit).7 In some
circumstances, the true risk could be as
low as zero; however, in other
circumstances the risk could be greater.8
When developing an upper bound
estimate of risk and to provide risk
values that do not underestimate risk,
health-protective default approaches are
generally used. To err on the side of
ensuring adequate health protection, the
EPA typically uses the upper bound
estimates rather than lower bound or
central tendency estimates in our risk
assessments, an approach that may have
limitations for other uses (e.g., prioritysetting or expected benefits analysis).
Chronic non-cancer reference
concentration (RfC) and reference dose
(RfD) values represent chronic exposure
levels that are intended to be healthprotective levels. Specifically, these
values provide an estimate (with
uncertainty spanning perhaps an order
of magnitude) of a continuous
inhalation exposure (RfC) or a daily oral
exposure (RfD) to the human population
(including sensitive subgroups) that is
likely to be without an appreciable risk
of deleterious effects during a lifetime.
To derive values that are intended to be
‘‘without appreciable risk,’’ the
methodology relies upon an uncertainty
factor (UF) approach, (U.S. EPA, 1993,
1994) which considers uncertainty,
variability and gaps in the available
data. The UF are applied to derive
reference values that are intended to
protect against appreciable risk of
deleterious effects. The UF are
commonly default values,9 e.g., factors of
7 IRIS glossary (https://www.epa.gov/NCEA/iris/
help_gloss.htm).
8 An exception to this is the URE for benzene,
which is considered to cover a range of values, each
end of which is considered to be equally plausible,
and which is based on maximum likelihood
estimates.
9 According to the NRC report, Science and
Judgment in Risk Assessment (NRC, 1994)
‘‘[Default] options are generic approaches, based on
general scientific knowledge and policy judgment,
that are applied to various elements of the risk
assessment process when the correct scientific
model is unknown or uncertain.’’ The 1983 NRC
report, Risk Assessment in the Federal Government:
Managing the Process, defined default option as
‘‘the option chosen on the basis of risk assessment
policy that appears to be the best choice in the
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10 or 3, used in the absence of
compound-specific data; where data are
available, UF may also be developed
using compound-specific information.
When data are limited, more
assumptions are needed and more UF
are used. Thus, there may be a greater
tendency to overestimate risk in the
sense that further study might support
development of reference values that are
higher (i.e., less potent) because fewer
default assumptions are needed.
However, for some pollutants, it is
possible that risks may be
underestimated.
While collectively termed ‘‘UF,’’ these
factors account for a number of different
quantitative considerations when using
observed animal (usually rodent) or
human toxicity data in the development
of the RfC. The UF are intended to
account for: (1) Variation in
susceptibility among the members of the
human population (i.e., inter-individual
variability); (2) uncertainty in
extrapolating from experimental animal
data to humans (i.e., interspecies
differences); (3) uncertainty in
extrapolating from data obtained in a
study with less-than-lifetime exposure
(i.e., extrapolating from sub-chronic to
chronic exposure); (4) uncertainty in
extrapolating the observed data to
obtain an estimate of the exposure
associated with no adverse effects; and
(5) uncertainty when the database is
incomplete or there are problems with
the applicability of available studies.
IV. Analytical Results and Proposed
Decisions for the Three Chromium
Electroplating Source Categories
A. What are the results and proposed
decisions based on our technology
review?
1. Emissions Limits for Large Hard
Chromium Electroplating
a. Emissions Limits for Existing Large
Hard Chromium Sources. As mentioned
above, the available data from 75 tanks
located at 38 facilities outside of
California indicate that approximately
88 percent of existing large hard
chromium electroplating sources
located outside of California have
emissions levels that are less than 75
percent of the current emissions limit
(i.e., below 0.011 mg/dscm); 72 percent
of these sources emit at less than 50
percent of the emissions limit (i.e.,
below 0.0075 mg/dscm); and about 60
percent of these sources achieve
emissions below 0.006 mg/dscm. There
are an additional 17 facilities located in
California, which on average have
considerably lower emissions compared
to plants in other States. These findings
demonstrate that the add-on emission
control technologies and/or the fume
suppressants used by the majority of
facilities in this source category are very
effective in reducing chromium
emissions and that most facilities have
emissions well below the current limit.
We considered three options to lower
the emissions limit. Table 2 summarizes
the emissions, costs, and cost
effectiveness for these options, which
are described further in the following
paragraphs.
TABLE 2—SUMMARY OF OPTIONS CONSIDERED FOR POTENTIAL REVISED EMISSIONS LIMITS FOR LARGE HARD CHROMIUM
ELECTROPLATING FACILITIES
Number of
plants
affected
Option
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Reduce emissions limit to 0.011 mg/dscm ......................
Reduce emissions limit to 0.0075 mg/dscm ....................
Reduce emissions limit to 0.006 mg/dscm ......................
Emissions
reductions,
lbs/yr
41
76
97
Capital costs,
$
121
169
180
$1,821,000
2,847,000
3,414,000
Annualized
costs, $/yr
$2,196,000
4,182,000
5,368,000
Cost
effectiveness,
$/lb
$18,100
24,700
29,900
The first option considered was to
propose that large hard chromium
electroplating plants meet an emissions
limit of 0.011 mg/dscm, which is
equivalent to a 25 percent reduction of
the current emission limit. The second
option evaluated was a limit of 0.006
mg/dscm since this is the level that
would be equivalent to the
concentration that can be achieved
(based on the 99 percent upper
tolerance limit) when WAFS are used to
control emissions and the surface
tension in the affected chromium
electroplating tank is maintained at the
level of the proposed revised surface
tension limits (described in section
IV.A.5). Finally, as a third option, we
selected an emissions limit of 0.0075
mg/dscm for large hard chromium
electroplating plants to provide an
intermediate option that is more
stringent than the first option of 0.011
mg/dscm, but less stringent than the
second option of 0.006 mg/dscm.
As noted above, we considered the
option of lowering the current emissions
limit by 25 percent, which would result
in a limit of 0.011 mg/dscm. Under this
option, we estimate that 26 plants (11
percent of the total plants nationwide)
would need to reduce emissions to
comply with this option because they
have emissions above 0.011 mg/dscm.
We also assume that an additional 15
plants (6 percent) that have emissions
close to this level (i.e., have emissions
concentrations greater than 0.009 mg/
dscm) would likely need to make
adjustments and reduce emissions to
ensure continuous compliance with a
limit of 0.011 mg/dscm. Therefore,
overall we estimate that 41 of the
existing large hard chromium facilities
(about 18 percent of the total) would
reduce emissions in order to ensure
compliance with a new emissions limit
of 0.011 mg/dscm. We assume that most
of these 41 facilities would achieve
these extra reductions with the addition
of fume suppressants. The available
data, which are described in the
technical document ‘‘Development of
Revised Surface Tension Limits for
Chromium Electroplating and
Anodizing Tanks Controlled with
Wetting Agent Fume Suppressants,’’
indicate that about 15 percent of sources
in the large hard chromium
electroplating industry outside of
California use fume suppressants to
supplement the level of control
achieved by an add-on control device;
for facilities located in California the
percentage is even higher. However, we
also assume that some facilities would
need to install new add-on control
devices or retrofit their existing controls
to meet the proposed limit. The only
costs for the other 192 facilities (82
absence of data to the contrary’’ (NRC, 1983a, p. 63).
Therefore, default options are not rules that bind
the Agency; rather, the Agency may depart from
them in evaluating the risks posed by a specific
substance when it believes this to be appropriate.
In keeping with EPA’s goal of protecting public
health and the environment, default assumptions
are used to ensure that risk to chemicals is not
underestimated (although defaults are not intended
to overtly overestimate risk). See EPA, 2004, An
Examination of EPA Risk Assessment Principles
and Practices, EPA/100/B–04/001 available at:
https://www.epa.gov/osa/pdfs/ratf-final.pdf.
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percent of the total) would be testing
and/or monitoring costs.
Based on this analysis, we estimate
that the total estimated capital costs for
all large hard chromium electroplating
sources to comply with this option (i.e.,
a limit of 0.011 mg/dscm) and conduct
the necessary testing and monitoring
would be $1.8 million and the average
capital costs per facility across all
facilities would be $8,300. The
estimated range of capital costs per
plant would be from $0 to $180,000.
The total annualized costs would be an
estimated $2.2 million, which includes
the costs for controls (WAFS and addon controls) plus testing. The average
annual cost per facility across all
facilities would be about $10,000. The
annualized costs per facility range from
$0 to $55,000. We estimate that these
requirements would reduce emissions of
chromium (mainly hexavalent
chromium) by 121 pounds per year (lbs/
yr), and that the cost-effectiveness
would be $18,100 per pound. The cost
estimates for the WAFS accounts for the
potential for slightly higher costs for
non-PFOS WAFS compared to PFOSbased WAFS and includes a
conservative assumption that the costs
for non-PFOS WAFS will be 15 percent
higher than the costs for PFOS-based
WAFS. The use of non-PFOS WAFS to
limit surface tension is described further
in section IV.A.5 below. More
information about the estimates of costs
and reductions and how they were
derived are provided in the technical
support document ‘‘Procedures for
Determining Control Costs and Cost
Effectiveness for Chromium
Electroplating Supplemental Proposal’’,
which is available in the docket for this
action.
Another option considered was to
lower the current emissions limit by 50
percent, which would result in a limit
of 0.0075 mg/dscm. Under this option,
and using a similar assumption (as that
used above) that facilities with
emissions close to this level (i.e., with
emissions greater than 0.006) would
make adjustments and reduce emissions
to ensure compliance with the revised
limit, we estimate that 76 of the existing
large hard chromium facilities (about 33
percent of the total) would reduce
emissions in order to ensure compliance
with an emissions limit of 0.0075 mg/
dscm. This would include the
approximately 28 percent of sources not
currently meeting this limit, as well as
sources (approximately 5 percent) that
are currently measuring close to this
limit and that would likely need to
make adjustments to ensure continuous
compliance with a limit of 0.0075 mg/
dscm. We assume that most of these 76
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facilities would achieve these extra
reductions with the addition of fume
suppressants. However, we also assume
that some facilities would need to
install new add-on control devices or
retrofit their existing controls to meet
the limit.
Based on this analysis, we estimate
that the total estimated capital costs for
all large hard chromium electroplating
sources to comply with this second
option (i.e., a limit of 0.0075 mg/dscm)
and conduct the necessary testing and
monitoring would be about $2.8 million,
and the average capital costs per facility
across all facilities would be about
$12,000. The total annualized costs are
estimated to be about $4.2 million, and
the estimated average annual cost per
facility across all facilities would be
about $19,000. We estimate that these
requirements would reduce emissions
by 169 lbs/yr, and that the costeffectiveness would be about $24,700
per pound. Moreover, the incremental
cost-effectiveness (i.e., the increased
costs per pound that result from
increasing the level of stringency from
option 1 to option 2) is estimated to be
about $41,800 per pound. This option
would also result in more facilities
needing to install or retrofit add-on
controls and would have more
significant impacts on small businesses
compared to the first option discussed
above.
We also considered the option of
lowering the limit by 60 percent, which
would result in a limit of 0.006 mg/
dscm. The option of reducing the
emissions limit to 0.006 mg/dscm was
evaluated because that concentration is
equivalent to the concentration that can
be achieved when WAFS are used to
control emissions and the surface
tension in the affected chromium
electroplating tank is maintained at
levels consistent with the surface
tension limits that are being proposed in
this action (as described in section
IV.A.5). However, the number of
facilities affected, the cost-effectiveness,
and incremental cost-effectiveness were
significantly higher than the estimated
costs and impacts for the two options
presented above (as shown in Table 2),
and would result in greater economic
impacts to small businesses.
We made the decision to consider
more stringent emissions limits than the
limit in the current NESHAP primarily
because the revised data set indicated
that most facilities were operating well
below the current emissions limit. This
indicated that more stringent emissions
limits could be implemented without
significant economic burden to the
industry.
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After considering the three options
described above for reducing the
emissions limit and after weighing the
costs and emissions reductions
associated with each option, we are
proposing to reduce the emissions limit
for affected tanks located at existing
large hard chromium electroplating
facilities to 0.011 mg/dscm. We
conclude this emissions limit would
achieve significant reductions in
emissions at a reasonable cost. This
option results in reductions from about
18 percent of the facilities. We project
that these facilities would generally be
the higher emitting facilities since they
would be the facilities with emissions
concentrations at the upper end (above
0.009 mg/dscm) compared to other
facilities; therefore, this lower limit will
achieve significant reductions. We did
not choose the other options for a
number of reasons, including the
following: those options would pose
greater economic burden, would be less
cost effective, would have significantly
higher incremental cost-effectiveness,
would have higher total annualized
costs and higher average costs per
facility, would impact substantially
more facilities, and would result in
greater impacts to a greater number of
small businesses.
Nevertheless, as an alternative to
meeting the proposed emissions limits,
we are proposing to allow existing large
hard chromium electroplating facilities
to meet the surface tension limits that
are also being proposed in this action.
The proposed surface tension limits
would be 40 dynes/cm, if measured
using a stalagmometer, and 33 dynes/
cm, if measured using a tensiometer.
Section IV.A.5 of this preamble
discusses the analyses performed and
the basis for these proposed surface
tension limits. As described in section
IV.A.5 of this preamble, we conclude
that maintaining surface tension at this
level would reflect a level of emissions
that is lower than the emissions limit (of
0.011 mg/dscm) proposed above.
b. Compliance Testing and
Monitoring. To demonstrate compliance,
we are proposing that each facility
would need to provide a new or
previous performance stack emissions
test that is representative of current
operations and current controls and is
conducted at the exit of the control
device to show they are in compliance
with the emissions limit. Or, as an
alternative, facilities could demonstrate
compliance with the MACT standard by
monitoring surface tension and
demonstrate that they maintain the
surface tension below the proposed
limits of 40 dynes/cm, if measured with
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a stalagmometer, and 33 dynes/cm, if
measured with a tensiometer.
c. Estimated Costs and Impacts for
Existing Large Hard Chromium
Facilities for the Proposed Option. We
estimate that 41 of the existing large
hard chromium facilities (about 18
percent of the total) would reduce
emissions in order to ensure compliance
with a new emissions limit of 0.011 mg/
dscm. This would include the
approximately 11 percent not currently
meeting this limit, as well as sources
(approximately 6 percent) that are
currently measuring close to this limit
and that would likely need to make
adjustments to ensure continuous
compliance with the proposed 0.011
mg/dscm level. We assume that most of
these 41 facilities would achieve these
extra reductions with the addition of
fume suppressants. However, we also
assume that some facilities would need
to install new add-on control devices or
retrofit their existing controls to meet
the limit. We estimate that 27 plants
would be required only to conduct
performance tests; and the remaining
plants would not be required to test or
add additional controls.
Based on this analysis, we estimate
that the total estimated capital costs for
all large hard chromium electroplating
sources to comply with the revised
limits and conduct the necessary testing
and monitoring is estimated to be $1.8
million and the average capital costs per
facility across all facilities are $8,300.
The total annualized costs are estimated
to be $2.2 million, and the average
annual cost per facility across all
facilities is estimated to $10,000. The
range for annualized costs per facility
range from $0 to $57,000. These costs
include the costs for controls (WAFS
and add-on controls) plus testing. We
estimate these requirements will reduce
chromium emissions (mainly
hexavalent chromium) by 121 pounds
per year, and that the cost-effectiveness
would be $18,100 per pound. We
conclude that these costs (e.g., total
capital and annualized costs, and the
costs per plant) and the cost
effectiveness are reasonable, particularly
since hexavalent chromium is a known
human carcinogen.
d. Emissions Limits for New Large
Hard Chromium Sources. We also
considered options for a more stringent
emissions limit for new sources. In
doing so, we recognized the need to redefine ‘‘new source’’ to help clarify
which facilities would be subject to the
new source standards being proposed in
this action. For purposes of the
revisions to the NESHAP being
proposed, a new facility would be one
that commences construction or
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reconstruction after February 8, 2012.
All other sources are considered
existing facilities for purposes of these
proposed amendments.
In evaluating options for a more
stringent emissions limit for new large
hard chromium electroplating facilities,
we considered the emissions
concentrations that could be achieved
using available add-on control devices
(such as with a CMP, MPME or high
efficiency scrubber) or a combination of
add-on controls (such as a CMP plus a
HEPA filter or an MPME plus a HEPA
filter) and the emissions concentrations
that could be achieved using WAFS. To
analyze the level of emissions that can
be achieved with add-on controls, we
evaluated available data on the
emissions concentrations that are
achieved by existing hard chromium
electroplating facilities that have
various add-on controls or combinations
of controls. Based on our analysis, we
conclude that the best available control
technology configurations, such as CMP
plus a HEPA filter, a MPME plus a
HEPA filter, or a high efficiency
scrubber, can achieve emissions
concentrations of approximately 0.003
mg/dscm or lower. We also considered
the costs associated with each of these
types of control configurations. We
estimate that the capital cost to install
a CMP plus a HEPA filter for a new large
hard chromium source is about
$306,400 and that the annualized costs
would be $109,300/yr. We also estimate
that the capital and annualized costs for
the other comparable control technology
configurations would be no greater than
these. We conclude that these costs are
reasonable for new sources that choose
one of these combinations of add-on
controls to minimize emissions.
Nevertheless, as discussed in section
IV.A.5 of this preamble, maintaining
affected tanks below the proposed
surface tension limits, which would be
a cost-effective compliance option for
new large hard chromium sources,
would limit chromium emissions
concentrations to less than 0.006 mg/
dscm. The combination of add-on
controls described above (e.g., CMP plus
HEPA filter or an MPME plus HEPA
filter or a high efficiency scrubber) can
reliably achieve emissions of 0.003 mg/
dscm or lower at a reasonable cost for
those new sources that choose to use
these add-on controls to comply with
the NESHAP instead of WAFS. The
available data indicate that all existing
hard chromium electroplating sources
that use these add-on controls (e.g.,
CMP plus HEPA filter or an MPME plus
HEPA filter) achieve emissions of 0.003
mg/dscm or lower, well below 0.006
mg/dscm. Moreover, based on the data
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that we have, 60 percent of all existing
large hard chromium facilities already
achieve emissions below 0.006
regardless of the type of controls they
use. For example, many facilities that
only have a CMP alone (without the
HEPA filter) have emissions below
0.006 mg/dscm. Therefore, we conclude
that some new facilities may be able to
achieve emissions below 0.006 mg/dscm
with only a CMP, which would be lower
costs than those costs mentioned above
for the combination of controls. Taking
into account an allowance for variability
in emission testing and control device
performance for those sources that
comply using add-on controls, and to
provide new facilities the flexibility to
use WAFS to minimize emissions to
comply with the emissions limit as an
alternative to add-on controls, we are
proposing an emissions limit of 0.006
mg/dscm for new sources. That is, we
are proposing to require affected tanks
at new large hard chromium
electroplating facilities to meet an
emissions limit of 0.006 mg/dscm.
Today’s action would also allow new
large hard chromium electroplating
sources the option of meeting the
proposed surface tension limits (40
dynes/cm by stalagmometer and 33
dynes/cm by tensiometer) as an
alternative to the proposed emissions
limit of 0.006 mg/dscm.
2. Emissions Limits for Small Hard
Chromium Electroplating
a. Emissions Limits for Small Hard
Chromium Sources. As we did for large
hard chromium electroplating,
described above to evaluate possible
options to reduce the emissions limits,
we compiled and ranked the available
data, which indicate that more than 80
percent of the currently operating small
hard chromium electroplating sources
have emissions concentrations below
the current emissions limit for new
small hard chromium electroplating
sources (i.e., 0.015 mg/dscm). We have
such data for 73 tanks at 56 facilities
located in States other than California.
We estimate that there are a total of 450
small hard chromium plants in the U.S.,
with 36 of those plants located in
California and 414 plants located in
other States. The plants located in
California have considerably lower
emissions on average compared to
plants in other States. We evaluated
three possible options for a more
stringent standard for these small hard
chromium electroplating sources,
considering the costs and emissions
reductions that would be achieved
under each of these options. Table 3
summarizes the emissions reductions,
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costs, and cost effectiveness associated
with these options.
TABLE 3—SUMMARY OF OPTIONS CONSIDERED FOR POTENTIAL REVISED EMISSIONS LIMITS FOR SMALL HARD CHROMIUM
ELECTROPLATING FACILITIES
Emissions
reductions,
lbs/yr
Numer of
plants
Option
Capital
costs, $
Annualized
costs, $/yr
Cost
effectiveness,
$/lb
Reduce emissions limit to 0.015 mg/dscm
Existing Small Hard Chromium ........................................
85
41
$1,445,000
$652,000
$15,800
140
34
64
7
2,447,000
571,000
1,225,000
243,000
19,200
36,000
171
80
81
35
3,161,000
1,268,000
1,585,000
653,000
19,700
18,800
Reduce emissions limit to 0.010 mg/dscm
Existing Small Hard Chromium ........................................
New * Small Hard Chromium ...........................................
Reduce emissions limit to 0.006 mg/dscm
Existing Small Hard Chromium ........................................
New * Small Hard Chromium ...........................................
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* The term ‘‘new’’ as used in this table refers to sources subject to the new source limit in the current NESHAP (i.e., sources that were constructed or reconstructed after December 16, 1993).
The first option evaluated was to
require existing small hard chromium
electroplating plants to meet the
emissions limit currently required for
new small hard chromium
electroplating plant (i.e., 0.015 mg/
dscm). As described above, the current
NESHAP (promulgated in 1995),
includes a limit of 0.03 for existing
sources and a limit of 0.015 for new
sources (those constructed or
reconstructed after December 16, 1993).
We decided that it was appropriate to
evaluate this option since many small
hard chromium plants (those
constructed or reconstructed since
December 16, 1993) are already subject
to this limit and because the vast
majority of currently operating small
hard chromium plants are achieving
emissions at or below this level.
We also considered a more stringent
option of proposing a limit of 0.006 mg/
dscm for the same reason described
previously for large hard chromium
electroplating. That is, an emissions
limit of 0.006 mg/dscm would be
equivalent to the concentration that can
be achieved when WAFS are used to
control emissions and the surface
tension in the affected chromium
electroplating tank is maintained by the
revised limits that are being proposed in
this action.
Finally, as a third option, we
evaluated a possible emissions limit of
0.010 mg/dscm for small hard
chromium electroplating plants to
provide an intermediate option that is
more stringent than the first option of
0.015 mg/dscm, but less stringent than
the second option of 0.006 mg/dscm.
These options are described in more
detail in the following paragraphs.
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As noted above, the first option we
considered was to propose that all
currently operating small hard
chromium facilities meet the new
source limit in the current NESHAP
(i.e., 0.015 mg/dscm). Under this option,
we estimate that 55 plants (12 percent
of the total small hard chromium plants
nationwide) would need to reduce
emissions to comply with this option
because they have emissions at or above
0.015 mg/dscm. We also assume that an
additional 30 plants (7 percent) that
have emissions close to this level (i.e.,
have emissions concentrations greater
than 0.012 mg/dscm) would likely need
to make adjustments and reduce
emissions to ensure continuous
compliance with a limit of 0.015 mg/
dscm. Under this option we estimate
that 85 small hard chromium facilities
(about 19 percent of the total) would
reduce emissions. We assume that most
of these 85 facilities would achieve
these extra reductions with the addition
of fume suppressants. However, we also
assume that some facilities would need
to install new add-on control devices or
retrofit their existing controls to meet
the limit.
The total estimated capital costs for
all small hard chromium electroplating
sources to comply with this option and
conduct the necessary testing and
monitoring would be $1.45 million, and
the average capital costs per facility
across all facilities would be $5,300.
The total annualized costs are estimated
to be $650,000, and the average annual
cost per facility across all facilities is
$2,400. These costs include the costs for
controls (WAFS and add-on controls)
plus testing. The annualized costs per
facility are estimated to range from $0
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to $22,000 per year. We estimate that
this option would reduce chromium
emissions by 41.3 pounds per year, and
that the cost-effectiveness would be
$15,800 per pound. More information
about the estimates of costs and
reductions and how they were derived
are provided in the technical document
‘‘Procedures for Determining Control
Costs and Cost Effectiveness for
Chromium Electroplating Supplemental
Proposal’’, which is available in the
docket for this action.
Another option evaluated was to
lower the limit for existing and new
sources to 0.01 mg/dscm. Under this
option we estimate that 174 small hard
chromium facilities (about 39 percent of
the total) would need to reduce
emissions. We assume that most of these
174 facilities would achieve these extra
reductions with the addition of fume
suppressants. However, we also assume
that several facilities would need to
install new add-on control devices or
retrofit their existing controls to meet
the limit.
The total estimated capital costs for
all small hard chromium electroplating
sources to comply with this option and
conduct the necessary testing and
monitoring would be $3.02 million and
the average capital costs per facility
across all facilities would be $17,400.
The total annualized costs are estimated
to be about $1.47 million, and the
average annual cost per facility across
all facilities would be about $8,400. We
estimate that this option would reduce
emissions by 71 pounds per year, and
that the cost-effectiveness would be
about $20,700 per pound. Moreover, the
incremental cost-effectiveness (i.e., the
increased costs per pound that result
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from increasing the level of stringency
from option 1 to option 2) is estimated
to be about $27,000 per pound. This
option would also result in more
facilities needing to install or retrofit
add-on controls and would have more
significant impacts on small businesses
compared to option 1.
We also considered the more stringent
option of lowering the limit to 0.006
mg/dscm, which would be consistent
with the emissions that can be achieved
using WAFS and maintaining the
surface tension below the limit being
proposed in this action. However, the
number of facilities affected, the costeffectiveness, and incremental costeffectiveness were significantly higher
than the estimated costs and impacts for
the two options presented above (as
indicated in Table 3), and would result
in greater economic impacts to small
businesses.
After considering the impacts of these
three options, we are proposing to
reduce the emissions limit for existing
small hard chromium electroplating
sources to 0.015 mg/dscm, which is
equal to the MACT limit we established
for new small hard chromium
electroplating sources when we first
promulgated the NESHAP (60 FR 4963,
January 25, 1995).
As an alternative to meeting the
proposed emissions limits, we are
proposing to allow existing small hard
chromium electroplating facilities to
meet the surface tension limits that are
also being proposed in this action. The
proposed surface tension limits would
be 40 dynes/cm, if measured using a
stalagmometer, and 33 dynes/cm, if
measured using a tensiometer. Section
IV.A.5 of this preamble discusses the
analyses performed and the basis for
these proposed surface tension limits.
As described in section IV.A.5 of this
preamble, we conclude that maintaining
surface tension at this level would
reflect a level of emissions that is lower
than the emissions limit (of 0.015 mg/
dscm) proposed above.
b. Compliance Testing and
Monitoring. To demonstrate compliance,
we are proposing that each facility
would need to provide a new or
previous performance stack emissions
test that is representative of current
operations and current controls and is
conducted at the exit of the control
device to show they are in compliance
with the emissions limit. Or, as an
alternative, facilities can demonstrate
compliance with the MACT standard by
monitoring surface tension and
demonstrate that they maintain the
surface tension below the proposed
limits of 40 dynes/cm, if measured with
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a stalagmometer, and 33 dynes/cm, if
measured with a tensiometer.
c. Estimated Costs and Impacts for
Small Hard Chromium Facilities.
We estimate that 85 small hard
chromium facilities (about 19 percent of
the total) would reduce emissions to
ensure compliance with the proposed
limit. We assume that most of these 85
facilities would achieve these extra
reductions with the addition of fume
suppressants. However, we also assume
that some facilities would need to
install new add-on control devices or
retrofit their existing controls to meet
the limit. We estimate that 26 plants
would be required only to conduct
performance tests; and the remaining
plants would not be required to test or
add additional controls.
The total estimated capital costs for
all small hard chromium electroplating
sources to comply with the proposed
revised limits and conduct the
necessary testing and monitoring is
estimated to be $1.45 million and the
average capital costs per facility are
$5,300. The total annualized costs are
estimated to be $650,000, and the
average annual cost per facility is
$2,400. We estimate that these
requirements will reduce chromium
emissions by 41.3 pounds per year, and
that the cost-effectiveness would be
$15,800 per pound. We conclude that
these costs (e.g., total capital and
annualized costs, and the costs per
plant) and the cost effectiveness are
reasonable, particularly since
hexavalent chromium is a known
human carcinogen.
d. Emissions Limits for New Small
Hard Chromium Sources.
For new small hard chromium
facilities, we considered options for a
more stringent emissions limit based on
the same type of analysis described
above for large hard chromium
electroplating sources. As is the case for
large hard chromium electroplating, we
are also proposing to re-define new
source as those sources, the
construction or reconstruction of which
commenced after February 8, 2012.
For the reasons described previously
(in section IV.A.1.d) for large hard
chromium electroplating facilities, we
are proposing to require new small hard
chromium electroplating facilities, to
limit emissions from affected tanks to
0.006 mg/dscm. Those reasons include
the findings that add-on controls (such
as a CMP plus HEPA filter) or WAFS
can achieve this level of emissions at
new hard chromium sources for a
reasonable cost. We estimate that
installing a combination of CMP with
HEPA filter on a new small hard
chromium electroplating source would
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result in capital costs of $127,000 and
annualized costs of $45,000 per year.
Furthermore, we believe that sources
could meet this level with other control
configurations or with WAFS alone for
lower costs. We conclude that any new
source should be able to achieve this
level of performance with typical addon control devices or with use of WAFS.
Today’s action would also allow new
small hard chromium electroplating
sources the option of meeting the
proposed surface tension limits (40
dynes/cm by stalagmometer and 33
dynes/cm by tensiometer) as an
alternative to the proposed emissions
limit of 0.006 mg/dscm.
3. Decorative Chromium Electroplating
a. Emissions Limits for Existing and
New Sources. As described above, the
current emissions limit for decorative
chromium electroplating is 0.010 mg/
dscm. We reviewed the available data
on existing sources in the decorative
chromium electroplating source
category to determine the typical level
of emissions performance and range of
performance among those sources to
assess options for revising the current
limit. We also reviewed the available
data on surface tension levels and the
relationship of surface tension to
emissions concentrations since most
decorative chromium electroplating
tanks rely primarily or entirely on
WAFS to limit emissions. WAFS are the
most common method for limiting
emissions from these facilities.
With regard to emissions
concentration data, we have data from
20 tanks at 17 facilities. Based on these
data, the emissions concentrations from
these 20 tanks are all less than 0.007.
The highest value is 0.0066 mg/dscm.
Two of these tanks (about 11 percent)
have emissions between 0.006 to 0.0066.
All the other tanks in this data set
(about 89 percent) have emissions
concentrations below 0.006 mg/dscm.
Some tanks have emissions much lower
than 0.006 mg/dscm.
With regard to our analysis of surface
tension and its relationship with
emissions concentrations, as described
in section IV.A.5 below (and in more
details in the ‘‘Development of Revised
Surface Tension Limits for Chromium
Electroplating and Anodizing Tanks
Controlled with Wetting Agent Fume
Suppressants,’’ which is available in the
docket for this action), we conclude that
maintaining surface tension to 40
dynes/cm (as measured by a
stalagmometer) and 33 dynes/cm (as
measured with a tensiometer) in
decorative chromium electroplating
baths would maintain emissions below
0.006 mg/dscm.
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After reviewing these data and
evaluating various regulatory options,
we are proposing to lower the limit for
existing decorative electroplating tanks
to 0.007 mg/dscm, which would be a 30
percent reduction from the current limit
of 0.01 mg/dscm. Our general approach
to choosing this option was similar to
that explained previously for hard
chromium electroplating. On the one
hand, the available data indicate that
most decorative chromium
electroplating sources have emissions
well below the current emissions limit
of 0.010 mg/dscm. As noted above, all
sources in our data set have emissions
concentrations below 0.007 mg/dscm.
Thus, we concluded that a more
stringent limit could achieve reductions
in emissions, particularly in terms of
allowable emissions, without imposing
a significant burden on the industry. On
the other hand, the large majority of
decorative chromium electroplating
tanks are controlled with WAFS, and
the available surface tension data
indicate that emissions from these
source are in the range of 0.004 to 0.006
mg/dscm (as described further in
section IV.A.5). We considered this
concentration range as a lower bound to
what could reasonably be required.
Therefore, we decided to select an
option between 0.006 and 0.01 mg/dscm
for further evaluation. Subsequently, we
chose to evaluate 0.007 mg/dscm for
this thorough evaluation since this is
the upper end of the emissions levels for
sources in our data set.
Although all facilities in our data set
that use an add-on control device have
emissions below 0.007 mg/dscm, we
realize that some sources (an estimated
8 facilities) currently have emissions
relatively close to this limit and
therefore would likely need to make
adjustments and achieve reductions to
ensure continuous compliance with the
proposed 0.007 mg/dscm level. Based
on the available emissions
concentration data, we estimate that
about 8 facilities may need to reduce
emissions to ensure compliance with
this limit. (See the technical support
document ‘‘Procedures for Determining
Control Costs and Cost Effectiveness for
Chromium Electroplating Supplemental
Proposal’’ which is available in the
docket for more details). However, it is
important to note that sources would
have the choice to comply with the
standard either by demonstrating
emissions are less than 0.007 mg/dscm
(with a stack test), or by maintaining
surface tension below 40 dynes/cm (as
measured by a stalagmometer) or 33
dynes/cm (as measured with the
tensiometer), as described further in
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section IV.A.5 below. We believe that
most of the decorative chromium
facilities would choose this surface
tension compliance approach.
Nevertheless, we estimate that by
lowering the limit to 0.007 mg/dscm
(and recognizing that plants would have
the option to demonstrate compliance
by meeting the surface tension limits),
the total capital costs for all decorative
chromium electroplating facilities to
comply with this option and to conduct
all the necessary testing and monitoring
would be $183,000, and the average
capital costs per facility would be $400.
The total annualized costs are estimated
to be $189,000, and the average annual
cost per facility is $390. We estimate
that this option would reduce emissions
by 39 pounds per year, and that the
cost-effectiveness would be $4,800 per
pound.
We also considered other options, but
we concluded that proposing a limit of
0.007 was the most appropriate option.
Therefore, we are proposing an
emissions limit of 0.007 mg/dscm for
existing decorative chromium
electroplating sources. We conclude that
this lower proposed limit would likely
require no costs for add-on controls for
these sources since all facilities for
which we have data are already
performing below this level with their
current controls and that all the other
facilities (that may need to achieve
reductions) will do so by adding fume
suppressants rather than installing addon controls or retrofitting their existing
controls.
This limit of 0.007 mg/dscm would
apply to any affected decorative
chromium electroplating source that is
controlled with an add-on emission
control device and chooses to
demonstrate compliance with a stack
emissions test.
As an alternative to meeting the
proposed emissions limit, we are
proposing to allow existing decorative
chromium electroplating facilities to
meet the surface tension limits that are
also being proposed in this action. The
proposed surface tension limits would
be 40 dynes/cm, if measured using a
stalagmometer, and 33 dynes/cm, if
measured using a tensiometer. Section
IV.A.5 of this preamble discusses the
analyses performed and the basis for
these proposed surface tension limits.
As described in section IV.A.5 of this
preamble, we conclude that maintaining
surface tension at this level would
reflect a level of emissions that is lower
than the emissions limit (of 0.007 mg/
dscm) proposed above.
With regard to new sources, we are
proposing to require new decorative
chromium electroplating tanks meet an
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emissions limit of 0.006 mg/dscm,
consistent with the proposed new
source limit for hard chromium
electroplating sources. As explained
previously, the available data indicate
that chromium electroplating plants that
use WAFS to control emissions and
maintain the surface tension below the
proposed limits would meet an
emissions concentration of 0.006 mg/
dscm. Furthermore, the data used to
develop these revised surface tension
limits indicate that WAFS are equally
effective in controlling emissions from
hard chromium electroplating tanks and
from decorative chromium
electroplating tanks. In addition, the
available data indicate that over 80
percent of existing decorative chromium
electroplating plants with add-on
controls already meet this proposed new
source emissions limit. Therefore, new
facilities should be able to achieve this
level of emissions at relatively low costs
by using WAFS or with the type of addon control devices used by existing
facilities in this source category. As an
alternative, we are proposing that new
sources can demonstrate compliance
with the MACT standards by
maintaining surface tension limits of 40
dynes/cm, if measured by
stalagmometer, and 33 dynes/cm, if
measured by tensiometer.
As is the case for hard chromium
electroplating, today’s action would redefine new sources to clarify which
emissions limits would apply to a
specific facility.
b. Compliance Testing and
Monitoring.
To demonstrate compliance, we are
proposing that each decorative
chromium electroplating source that
uses an add-on control device to control
emissions from affected tanks and
chooses to comply with the proposed
emissions limit, rather than the surface
tension limits, would need to provide a
new or previous performance stack
emissions test that is representative of
current operations and current controls
and is conducted at the exit of the
control device to show they are in
compliance with the emissions limit.
Facilities that elect the alternative
option to comply with the surface
tension limits would be required to
monitor surface tension, as currently
required by the NESHAP.
c. Costs and Impacts for Decorative
Chromium Electroplating.
The total estimated capital costs for
all decorative chromium electroplating
facilities to comply with these proposed
revised standards (i.e., lower surface
tension limits or lower emissions limits)
and to conduct all the necessary testing
and monitoring is estimated to be
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$183,000, and the average capital costs
per facility are $400. The total
annualized costs are estimated to be
$189,000, and the average annual cost
per facility across all facilities is $390.
The range for annualized costs per
facility are from $0 to $4,200. We
estimate that these requirements will
reduce emissions by 39 pounds per
year, and that the cost-effectiveness
would be $4,800 per pound.
4. Chromium Anodizing
a. Emissions Limits for Existing and
New Chromium Anodizing Sources. As
discussed in section III.B.1.d. of this
preamble, although we did not have the
data to perform a detailed analysis of
options for chromium anodizing
sources, there is a basis for concluding
that the same emissions limits being
proposed for decorative chromium
electroplating would also be appropriate
for chromium anodizing sources. In
terms of relative magnitude of
emissions, the types of emission
controls commonly used, and the
emissions limits in the current
NESHAP, these two source categories
are similar. With regard to emissions
levels, based on the available data, the
average emissions from chromium
anodizing plants are about 20 percent
lower than the average emissions from
decorative electroplating plants, with an
average of about 0.46 pounds per year
per facility for anodizing plants and
0.57 pounds per year per plant for
decorative chromium electroplating.
With regard to controls, the majority of
chromium anodizing and decorative
chromium electroplating plants rely
partly or entirely on WAFS to limit
emissions. Moreover, the tank sizes are
similar, with an average of about 1,020
gallons per tank for decorative
chromium electroplating plants and
1,380 gallons per tank for chromium
anodizing plants. Overall, we conclude
that chromium anodizing plants should
be able to limit emissions just as
effectively and to the same level as the
decorative plants, primarily using
WAFS, for about the same costs.
Consequently, we are proposing the
same emissions limits for new and
existing chromium anodizing sources as
are being proposed for decorative
chromium electroplating sources. That
is, we are proposing that existing
chromium anodizing sources would
have to meet an emissions limit of 0.007
mg/dscm, and new sources would have
to meet an emissions limit of 0.006 mg/
dscm. Sources would also have the
option of meeting the proposed surface
tension limits as an alternative to
meeting the proposed emissions limits.
As is the case for hard chromium
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electroplating, today’s action would redefine new sources to clarify which
emissions limits would apply to a
specific facility. Nevertheless, since we
have very limited data on chromium
anodizing plants, we specifically
request comments on these proposed
limits and we seek data and information
on emissions from these chromium
anodizing sources, including emissions
test results, emissions concentration
data, mass rate emissions (e.g., lbs per
year), flow rates, and other emissions
release information.
b. Compliance Testing and
Monitoring. To demonstrate compliance,
we are proposing that each chromium
anodizing facility that uses an add-on
control device to control emissions from
affected tanks and chooses to comply
with the proposed emissions limit,
rather than the surface tension limits,
would need to provide a new or
previous performance stack emissions
test that is representative of current
operations and current controls and is
conducted at the exit of the control
device to show they are in compliance
with the emissions limit. Facilities that
elect the alternative option to comply
with the surface tension limits would be
required to monitor surface tension, as
currently required by the NESHAP.
c. Costs and Impacts for Chromic
Acid Anodizing.
To meet the proposed lower
emissions limits and/or the lower
surface tension limits, we
conservatively assume that about 50
percent of facilities will need to use
additional WAFS, which would result
in increased annualized costs. Since
emissions are already quite low for
these facilities, we assume that no
facilities will need to install add-on
controls to meet the lower limits.
Therefore, the only capital costs will be
costs for testing.
The total estimated capital costs for
all chromic acid anodizing facilities to
comply with the revised limits, which is
completely for testing and monitoring,
is estimated to be $245,000 and the
average capital costs per facility are
$1,700. The total annualized costs,
which include costs for WAFS and
annualized costs for testing and
monitoring, are estimated to be $54,000
and the average annual cost per facility
across all facilities is $370. The range
for annualized costs per facility are from
$0 to $2,600. We estimate that these
requirements will reduce emissions by 6
pounds per year, and that the costeffectiveness would be $9,100 per
pound. More information about the
estimates of costs and reductions and
how they were derived are provided in
the technical support document
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‘‘Procedures for Determining Control
Costs and Cost Effectiveness for
Chromium Electroplating Supplemental
Proposal,’’ which is available in the
docket for this action.
5. Surface Tension Limits
As described in section III.A.2 of this
preamble, the available data on surface
tension and emission concentration
were evaluated in terms of upper
tolerance limits (UTLs) to help us better
understand the relationship between
surface tension and emissions. As a first
step, we categorized the data according
to the type of instrument used
(stalagmometer or tensiometer). We
discarded any data for which we could
not identify the measurement
instrument.
We analyzed the data for the purpose
of developing tolerance limits that could
be used to establish emissions
concentrations for specified surface
tension values. Statistical tolerance
limits are limits within which a stated
proportion of the population is expected
to lie. The UTL represents the value
below which it can be expected that the
specified percentage of the
measurements would fall for the
specified level of confidence in repeated
sampling. For example, the 95 percent
UTL with 99 percent confidence level is
the value for which we can conclude
with 99 percent certainty or confidence
that at least 95 percent of the data points
lie below. We used this UTL approach
in our analysis at these percent values
(i.e., the 95 percent UTL with 99 percent
confidence level).
To determine the UTL for various
surface tension limits, we divided the
surface tension data into intervals that
had enough data points to calculate the
mean and standard deviation. Separate
data sets and intervals were determined
for surface tension measurements using
stalagmometers and for measurements
using tensiometers. We then applied a
statistical procedure to develop UTLs
for each surface tension interval. We
evaluated the results to determine
appropriate intervals (i.e., surface
tension limits) that would be achievable
from a process operating perspective
and would achieve significant
reductions in chromium emissions. We
used these surface tension limits as the
basis for our proposed decisions
regarding surface tension. These
proposed decisions are described
previously in sections IV.A.1 through
IV.A.4. The results of the UTL analysis
indicate that maintaining the surface
tension below 40 dynes/cm, as
measured using a stalagmometer, would
limit emissions to no more than 0.0055
mg/dscm; and maintaining the surface
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tension below 32.5 dynes/cm, as
measured using a tensiometer, would
limit emissions to no more than 0.0047
mg/dscm. Recognizing that these
instruments measure surface tension in
integer increments, we rounded the
tensiometer limit to 33 dynes/cm and
concluded that maintaining these two
surface tension limits (40 dynes/cm by
stalagmometer and 33 dynes/cm by
tensiometer) in chromium electroplating
and anodizing baths would maintain
emissions below 0.006 mg/dscm.
Additional details on the analysis of the
surface tension data can be found in the
technical memorandum, ‘‘Development
of Revised Surface Tension Limits for
Chromium Electroplating and
Anodizing Tanks Controlled with
Wetting Agent Fume Suppressants,’’
which is available in the docket for this
action.
Based on available data, many
facilities that currently use WAFS
already achieve surface tensions well
below these levels (i.e., 40 dynes/cm
and 33 dynes/cm), and based on
available information, we conclude that
other facilities can easily achieve these
levels with a relatively small increase in
the use of fume suppressants. Therefore,
as an alternative to meeting the
proposed emissions limits, we are
proposing to allow new and existing
sources in all three source categories
(hard chromium electroplating,
decorative chromium electroplating,
and chromium anodizing) that use
WAFS to comply with the NESHAP to
meet these proposed lower surface
tension limits (40 dynes/cm as
measured with a stalagmometer and 33
dynes/cm as measured with a
tensiometer).
As mentioned above, in the October
21, 2010 Federal Register notice (75 FR
65068), we proposed phasing out the
use of wetting agent fume suppressants
(WAFS) that contain perfluorooctyl
sulfonates (PFOS). Based on available
information, we continue to believe that
non-PFOS WAFS are available that can
effectively limit surface tension for
about the same costs as PFOS-based
WAFS, and that these non-PFOS WAFS
can achieve surface tension levels below
the proposed surface tension limits
(described above).10,11 However, to be
conservative, we have assumed that the
costs for non-PFOS WAFS will be 15
percent higher than the PFOS based
WAFS and these additional costs have
been included in the costs presented in
today’s notice. More information about
the cost estimates for WAFS and how
they were derived are provided in the
technical support document
‘‘Procedures for Determining Control
Costs and Cost Effectiveness for
Chromium Electroplating Supplemental
Proposal,’’ which is available in the
docket for this action.
We are not re-opening the comment
period on the proposed phase out of the
use of PFOS-based WAFS. However, we
are soliciting comment and data on
whether the proposed surface tension
limits can be met through the use of
non-PFOS WAFS. We seek data and
information on the type of WAFS used,
what surface tensions have been
achieved, what hexavalent chromium
emissions reductions have been
achieved, fume suppressant costs, and
detailed information related to the
feasibility of using different types of
WAFS.
B. What are the results of the risk
assessment?
1. Inhalation Risk Assessment Results
Table 4 provides an overall summary
of the inhalation risk assessment results
for the source category.
TABLE 4—CHROMIUM ELECTROPLATING AND ANODIZING INHALATION RISK ASSESSMENT RESULTS
Maximum individual cancer
risk
(in 1 million) 2
Number of
facilities 1
Source category
Hard Chromium Electro-plating .........................
Decorative Chromium Electro-plating ...............
Chromic acid Anodizing ....................................
Actual
emissions
level
699
577
179
Allowable
emissions
level
20
10
5
50
70
60
Population
at risk
≥ 1-in-1
million 3
130,000
43,000
5,000
Maximum chronic non-cancer TOSHI 4
Annual
cancer
incidence
(cases per
year) 3
Actual
emissions
level
0.05
0.02
0.003
0.02
0.008
0.004
Allowable
emissions
level
0.04
0.06
0.05
Maximum
off-site
acute noncancer HQ
5 NA
5 NA
5 NA
1 Number
of facilities evaluated in the risk analysis.
individual excess lifetime cancer risk.
on actual emissions.
4 Maximum TOSHI. The target organ with the highest TOSHI for these source categories is the respiratory system.
5 NA = Not applicable. There are no HAP with acute dose-response benchmark values, so no acute HQ were calculated for these source categories.
2 Maximum
srobinson on DSK4SPTVN1PROD with PROPOSALS2
3 Based
As shown in Table 4, the results of the
inhalation risk assessment for the hard
chromium electroplating source
category indicate the maximum lifetime
individual cancer risk could be up to
20-in-1 million based on actual
emission levels of hexavalent
chromium, and the maximum chronic
noncancer TOSHI value could be up to
0.02. The total estimated national cancer
incidence from these facilities, based on
actual emission levels, is 0.05 excess
cancer cases per year, or one case in
every 20 years. In addition, we note that
approximately 1,100 people are
estimated to have cancer risks greater
than 10 in one million, and
approximately 130,000 people are
estimated to have risks greater than 1in-1 million based on estimates of actual
emissions. Based on allowable emission
levels, the maximum lifetime individual
cancer risk could be up to 50-in-1
million, and the maximum chronic
noncancer TOSHI value could be up to
0.04. Hexavalent chromium, which is a
known human carcinogen, is the only
HAP emitted by these sources and the
HAP driving all these risks.
The results of the inhalation risk
assessment for the decorative chromium
electroplating source category indicate
the maximum lifetime individual cancer
risk could be up to 10-in-1 million
based on actual emission levels, and the
maximum chronic noncancer TOSHI
value could be up to 0.008. The total
estimated national cancer incidence
from these facilities, based on actual
emission levels, is 0.02 excess cancer
cases per year, or one case in every 50
years. In addition, we note that
approximately 100 people are estimated
to have cancer risks greater than 10 in
10 Barlowe, G. and Patton, N., 2011. ‘‘Non-PFOS,
Permanent Mist Suppressants for Hard Chromium
Plating, Decorative Chromium Plating and Chromic
Etch Applications’’. March 1, 2011.
11 Danish, EPA. 2011. Substitution of PFOS for
use in non-decorative hard chrome plating. Pia
Brunn Poulsen, Lars K. Gram and Allan Astrup
Jensen. Danish Environmental Protection Agency.
Environmental Project No. 1371 2011.
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one million, and approximately 43,000
people are estimated to have risks
greater than 1-in-1 million based on
estimates of actual emissions. Based on
allowable emission levels, the
maximum lifetime individual cancer
risk could be up to 70-in-1 million, and
the maximum chronic noncancer TOSHI
value could be up to 0.06.
The results of the inhalation risk
assessment for the chromic acid
anodizing source category indicate the
maximum lifetime individual cancer
risk could be up to 5-in-1 million based
on actual emission levels, and the
maximum chronic noncancer TOSHI
value could be up to 0.004. The total
estimated national cancer incidence
from these facilities, based on actual
emission levels, is 0.003 excess cancer
cases per year, or one case in every 333
years. In addition, we note that no
people are estimated to have cancer
risks greater than 10-in-1 million, and
approximately 5,000 people are
estimated to have risks greater than 1in-1 million. Based on allowable
emission levels, the maximum lifetime
individual cancer risk could be up to
60-in-1 million, and the maximum
improved data set is described further in
section II.E of this preamble, and the
methodology is described in section
III.B.
For all three source categories, there
were no reported emissions of PB–HAP,
and chromium emissions are not known
to have any associated adverse
environmental impacts; therefore, we
conclude there is low potential for
human health multipathway risks or
adverse environmental impacts. Also,
because there are no HAP with acute
dose-response benchmark values, no
acute HQ were calculated for these
source categories, and we believe that
the potential for acute effects is low.
chronic noncancer TOSHI value could
be up to 0.05.
The cancer risk estimates for all of the
chromium electroplating source
categories, especially those based on
actual emissions, are considerably
different compared to the results that
were presented in the initial RTR
proposal on October 21, 2010, (75 FR
65071). The risks due to the estimates of
actual emissions presented above are
considerably lower than those presented
in the October 21, 2010 proposal FR
Notice for hard chromium and
decorative chromium plants. However,
the risks due to actual emissions for
chrome anodizing are about the same as
the October 2010 proposal. The revised
estimate of risks based on allowable
emissions presented above are lower for
hard chromium, about the same for
decorative, and considerably higher for
anodizing plants compared to the
October 2010 proposal. The main reason
for the difference is that we have
significantly improved data on
emissions and facility characteristics for
this supplemental proposal, and we
used a different methodology to
estimate emissions for facilities for
which we had incomplete data. This
2. Facility-Wide Risk Assessment
Results
Table 5 displays the results of the
facility-wide risk assessment. This
assessment was conducted based on
actual emission levels. For detailed
facility-specific results, see Appendix 5
of the ‘‘Residual Risk Assessment for the
Chromic Acid Anodizing, Decorative
Chromium Electroplating, and Hard
Chromium Electroplating Source
Categories’’ which is available in the
docket for this rulemaking.
TABLE 5—CHROMIUM ELECTROPLATING AND ANODIZING FACILITY–WIDE RISK ASSESSMENT RESULTS
Hard chromium
electroplating
Source category
Number of facilities analyzed ............................................................................
Decorative chromium electroplating
Chromium
anodizing
699
577
179
70
80
10
0
0
0
0
0
0
195
98
31
Cancer Risk:
Estimated maximum facility-wide individual cancer risk (in 1 million) ...............
Number of facilities with estimated facility-wide individual cancer risk of 100in-1 million or more ........................................................................................
Number of facilities at which the source category contributes 50 percent or
more to the facility-wide individual cancer risks of 100-in-1 million or more
Number of facilities at which the source category contributes 50 percent or
more to the facility-wide individual cancer risk of 1-in-1 million or more ......
Chronic Noncancer Risk:
srobinson on DSK4SPTVN1PROD with PROPOSALS2
Maximum facility-wide chronic noncancer TOSHI .............................................
Number of facilities with facility-wide maximum noncancer TOSHI greater
than 1 .............................................................................................................
Number of facilities at which the source category contributes 50 percent or
more to the facility-wide maximum noncancer TOSHI of 1 or more .............
2
7
0.1
1
2
0
0
0
0
The facility-wide MIR from all HAP
emissions at a facility that contains
sources subject to the hard chromium
electroplating MACT standards is
estimated to be 70-in-1 million, based
on actual emissions. Of the 699 facilities
included in this analysis, none have a
facility-wide MIR of 100-in-1 million or
greater. There are 206 facilities with
facility-wide MIR of 1-in-1 million or
greater, of which 195 have hard
chromium electroplating operations that
The facility-wide MIR from all HAP
emissions at a facility that contains
sources subject to the decorative
chromium electroplating MACT
standards is estimated to be 80-in-1
million, based on actual emissions. Of
the 577 facilities included in this
analysis, none have a facility-wide MIR
of 100-in-1 million or greater. There are
121 facilities with a facility-wide MIR of
1-in-1 million or greater, of which 98
have decorative chromium
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contribute greater than 50 percent to the
facility-wide risks. The facility-wide
maximum individual chronic noncancer
TOSHI value is estimated to be 2, based
on actual emissions, and there is 1
facility with a facility-wide maximum
individual chronic noncancer TOSHI
value greater than 1. Hard chromium
electroplating operations do not
contribute greater than 50 percent to the
facility-wide maximum chronic
noncancer TOSHI value at any facility.
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electroplating operations that contribute
greater than 50 percent to the facilitywide risks. The facility-wide maximum
individual chronic noncancer TOSHI
value is estimated to be 7, based on
actual emissions, and there are 2
facilities with facility-wide maximum
individual chronic noncancer TOSHI
values greater than one. Decorative
chromium electroplating operations do
not contribute greater than 50 percent to
the facility-wide maximum chronic
noncancer TOSHI value at any facility.
The facility-wide MIR from all HAP
emissions at a facility that contains
sources subject to the chromium
anodizing MACT standards is estimated
to be 10-in-1 million, based on actual
emissions. Of the 179 facilities included
in this analysis, none have a facilitywide MIR of 100-in-1 million or greater.
There are 35 facilities with a facilitywide MIR of 1-in-1 million or greater, of
which 31 have chromium anodizing
operations that contribute greater than
50 percent to the facility-wide risks. The
facility-wide maximum individual
chronic noncancer TOSHI value is
estimated to be 0.1.
3. Demographic Analysis Results
To examine the potential for any
environmental justice (EJ) issues that
might be associated with these source
categories, we performed demographic
analyses of the at-risk populations (i.e.,
the population with estimated lifetime
cancer risks greater than or equal to 1in-1 million due to emissions from
chromium electroplaters) for two of the
three chromium electroplating
categories. The results of the
demographic analyses are summarized
in Table 6. These results, for various
demographic groups, are based on the
estimated risks from actual emissions
levels for the population living within
50 km of the facilities.
TABLE 6—HARD AND DECORATIVE CHROMIUM ELECTROPLATING DEMOGRAPHIC RISK ANALYSIS RESULTS
Hard chromium
electroplating
Nationwide
Decorative chromium electroplating
Population with cancer risk at or above
1-in-1 Million
Total Population .........................................................................................................
312,900,000
131,000
43,000
72
28
59
41
48
52
72
13
1.1
14
59
21
0.8
20
48
21
0.8
30
17
83
34
66
26
74
14
86
21
79
24
76
10
90
27
73
24
76
Race by Percent
White ..........................................................................................................................
All Other Races .........................................................................................................
Race by Percent
White ..........................................................................................................................
African American .......................................................................................................
Native American ........................................................................................................
Other and Multiracial .................................................................................................
Ethnicity by Percent
Hispanic .....................................................................................................................
Non-Hispanic .............................................................................................................
Income by Percent
Below Poverty Level ..................................................................................................
Above Poverty Level ..................................................................................................
Education by Percent
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Over 25 and without High School Diploma ...............................................................
Over 25 and with a High School Diploma .................................................................
For hard chromium electroplating, the
results indicate that there are
approximately 131,000 people exposed
to a cancer risk at or above 1-in-1
million due to emissions from the
source category. For several
demographic groups, the percentage of
such groups in the at-risk population are
higher than their respective nationwide
percentages, including the African
American, Other and Multiracial,
Hispanic, Below the Poverty Level, and
Over 25 without a High School Diploma
demographic groups. These results
indicate that these demographic groups
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carry the potential to be
disproportionately exposed to emissions
and risks from this source category.
These groups therefore stand to benefit
the most from the emission reductions
achieved by this proposed rulemaking.
For decorative chromium
electroplating, the results indicate that
there are approximately 43,000 people
exposed to a cancer risk at or above 1in-1 million due to emissions from the
source category. The percentages of the
at-risk population in several
demographic groups are higher than
their respective nationwide percentages,
including the African American, Other
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and Multiracial, Hispanic, Below the
Poverty Level, and the Over 25 without
a High School Diploma demographic
groups. These results indicate that these
demographic groups carry the potential
to be disproportionately exposed to
emissions and risks from this source
category. These groups therefore stand
to benefit the most from the emission
reductions achieved by this proposed
rulemaking.
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C. What are our proposed decisions
regarding risk acceptability and ample
margin of safety?
1. Risk Acceptability
As noted in the preamble of the
October 2010 proposal (75 FR 65068),
we weigh all health risk factors in our
risk acceptability determination,
including the MIR, the numbers of
persons in various cancer and
noncancer risk ranges, cancer incidence,
the maximum noncancer HI, the
maximum acute noncancer hazard, the
extent of noncancer risks, the potential
for adverse environmental effects, and
risk estimation uncertainties (54 FR
38044, September 14, 1989).
For each of the three source
categories, the risk analysis we
performed indicates that the cancer risk
to the individual most exposed due to
actual emissions is well below 100-in-1
million (an MIR of 100-in-1 million is
generally considered the upper limit of
acceptable risk), and that the cancer
incidence is less than 0.05 cases per
year (about 1 case in every 20 years).
These risks are due to hexavalent
chromium emissions. Hexavalent
chromium is classified as a known
human carcinogen by U.S. EPA. While
the potential cancer risks due to
allowable emissions from each of the
three chromium electroplating
categories are higher, they are also less
than 100-in-1 million (with the highest
estimated MIR of 70-in-1 million for the
decorative chromium electroplating
category based on allowable emissions).
Specifically, for hard chromium
electroplating, the MIR due to actual
emissions is estimated to be 20-in-1
million, and the cancer incidence is
estimated to be 0.05 cases per year. The
MIR due to allowable emissions from
hard chromium electroplating facilities
is estimated to be 50-in-1 million, and
the cancer incidence is estimated to be
0.2. For decorative chromium
electroplating, the MIR due to actual
emissions is estimated to be 10-in-1
million, and the cancer incidence is
estimated to be 0.02 cases per year. The
MIR due to allowable emissions from
decorative chromium facilities is
estimated to be 70-in-1 million, and the
cancer incidence is estimated to be 0.08.
For chromium anodizing, the MIR due
to actual emissions is estimated to be 5in-1 million, and the cancer incidence is
estimated to be 0.003 cases per year.
The MIR due to allowable emissions
from chromium anodizing facilities is
estimated to be 60-in-1 million, and the
cancer incidence is estimated to be 0.08.
Our analysis also indicates that
chronic noncancer health risks,
potential acute impacts of concern,
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multipathway health risks and
environmental risks are all negligible
due to both actual and allowable
emissions for all three source categories.
Although the cancer risks are due to
emissions of a known human
carcinogen (hexavalent chromium),
since the cancer MIRs due to actual
emissions are well below 100-in-1
million, and because a number of the
other risk metrics do not indicate high
risk concerns, we are proposing to
determine that the risks due to HAP
emissions from each of the three source
categories are acceptable.
We note that the results of our
demographic analyses (which are
presented above) for hard and
decorative chromium electroplating
indicate that certain minority groups
and low-income populations may be
disproportionately exposed to emissions
from these categories and to any risks
that may result due to these emissions
because the communities most
proximate to facilities within these
categories have a higher proportion of
these groups than the national
demographic profile. We note that we
did not identify any vulnerability or
susceptibility to risks particular to
minority and low income populations
from pollutants emitted from this source
category. The Agency has determined
that the existing NESHAP for these
source categories provides an acceptable
level of risk for all proximate
populations, including minority and
low-income populations.
2. Ample Margin of Safety Analysis
We next considered whether the
existing MACT standard provides an
ample margin of safety (AMOS). Under
the ample margin of safety analysis, we
evaluate the cost and feasibility of
available control technologies and other
measures (including the controls,
measures, and costs reviewed under the
technology review) that could be
applied in each of the three source
categories to further reduce the risks (or
potential risks) due to emissions of HAP
identified in our risk assessment, along
with all of the health risks and other
health information considered in the
risk acceptability determination
described above.
Based on the fact that we have
determined the risks due to actual and
allowable emissions associated with
each of the three categories of sources
subject to the Chromium Electroplating
NESHAP to be acceptable, and after
evaluating the costs and feasibility of
possible options to reduce emissions in
our technology review, we are
proposing that the same emission and
surface tension limits that we are
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proposing under section 112(d)(6) of the
Clean Air Act, which are discussed
previously in section IV.A of this
preamble, will reduce health risks and
provide an ample margin of safety to
protect public health. As described
below, these proposed actions will
reduce the modeled estimated
maximum individual cancer risks and
the modeled population cancer risks for
the three source categories. Specifically,
under Section 112(f) of the Clean Air
Act, we are proposing the following
amendments to the NESHAP:
• Existing large hard chromium
electroplating facilities would be
required to meet an emissions limit of
0.011 mg/dscm or a surface tension
limit of 40 dynes/cm, if measured by
stalagmometer, or 33 dynes/cm, if
measured by tensiometer;
• New large hard chromium
electroplating facilities would be
required to meet an emissions limit of
0.006 mg/dscm or a surface tension
limit of 40 dynes/cm, if measured by
stalagmometer, or 33 dynes/cm, if
measured by tensiometer;
• Existing small hard chromium
electroplating facilities would be
required to meet an emissions limit of
0.015 mg/dscm or a surface tension
limit of 40 dynes/cm, if measured by
stalagmometer, or 33 dynes/cm, if
measured by tensiometer;
• New small hard chromium
electroplating facilities would be
required to meet an emissions limit of
0.006 mg/dscm or a surface tension
limit of 40 dynes/cm, if measured by
stalagmometer, or 33 dynes/cm, if
measured by tensiometer;
• Existing decorative chromium
electroplating and chromium anodizing
facilities would be required to meet an
emissions limit of 0.007 mg/dscm or a
surface tension limit of 40 dynes/cm, if
measured by stalagmometer, or 33
dynes/cm, if measured by tensiometer;
• New decorative chromium
electroplating and chromium anodizing
facilities would be required to meet an
emissions limit of 0.006 mg/dscm or a
surface tension limit of 40 dynes/cm, if
measured by stalagmometer, or 33
dynes/cm, if measured by tensiometer.
These proposed amendments to the
NESHAP would reduce the cancer risks
due to emissions of hexavalent
chromium from this industry for all
populations, including minority and
low-income populations. Specifically,
we estimate that the MIR based on
actual emissions for each of these
categories would be reduced by 25 to 50
percent, and the MIR based on
allowable emissions would also be
reduced by 25 to 50 percent. Cancer
incidence and the number of people
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exposed to risks greater than 1-in-1
million would also be reduced
significantly, by about 25 to 50 percent
each.
As described above, we estimate that
the total estimated capital costs for all
existing large hard chromium
electroplating sources to comply with
the proposed revised limits and conduct
the necessary testing and monitoring
would be $1.8 million. The total
annualized costs are estimated to be
$2.2 million. We estimate that these
proposed requirements would reduce
chromium emissions by 121 pounds per
year, and that the cost-effectiveness
would be $18,100 per pound.
The total estimated capital costs for
all existing small hard chromium
electroplating sources to comply with
the proposed revised limits and conduct
the necessary testing and monitoring is
estimated to be $1.45 million. The total
annualized costs are estimated to be
$652,000. We estimate that these
proposed requirements would reduce
chromium emissions by 41 pounds per
year, and that the cost-effectiveness
would be $15,800 per pound.
The total estimated capital costs for
all existing decorative chromium
electroplating facilities to comply with
these proposed revised standards (i.e.,
lower surface tension limits or lower
emissions limits) and to conduct all the
necessary testing and monitoring is
estimated to be $183,000. The total
annualized costs are estimated to be
$189,000. We estimate that these
proposed requirements would reduce
emissions by 39 pounds per year, and
that the cost-effectiveness would be
$4,800 per pound.
The total estimated capital costs for
all existing chromic acid anodizing
facilities to comply with the proposed
revised limits and conduct the
necessary testing and monitoring is
estimated to be $245,000. The total
annualized costs are estimated to be
$54,000. We estimate that these
proposed requirements would reduce
emissions by 6 pounds per year, and
that the cost-effectiveness would be
$9,100 per pound.
We conclude that the costs for all four
categories or subcategories described
above are reasonable given the risk
reductions that will be achieved.
Based on all the above information,
we propose that the NESHAP as revised
with these proposed requirements will
provide an ample margin of safety to
protect public health by lowering
emission levels and reducing cancer risk
for all populations, including minority
and low-income populations.
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D. Compliance Dates
We are proposing to require existing
facilities to comply with the proposed
revised emissions limits or revised
surface tension requirements no later
than 2 years after the date of publication
of the final rule. We believe this much
time is needed for facilities to determine
if they meet the proposed emissions
limits, which would likely require
conducting an emissions test.
Scheduling a compliance test,
conducting the test, and receiving the
results, could take as much as 4 to 6
months. At that time, affected facilities
that do not meet the proposed emissions
limit would have to perform an
engineering analysis to determine the
control options, decide on what
additional controls are needed, send out
a tender notice, evaluate the bids
received, and contract the installation
and testing of the new equipment. Since
most chromium electroplating facilities
do not have in-house engineering
expertise, they would likely have to hire
consultants to perform all of the above
work, and that would add to the time
required.
We are proposing that all new
facilities (newly constructed or
reconstructed) must comply with the
proposed revised emissions limits or
surface tension requirements upon
startup. We are proposing to require
compliance with the electronic
reporting requirements, which are
discussed in section VII below, upon
promulgation of the final rule.
V. What action are we proposing for the
steel pickling source category?
A. Elimination of an Alternative
Compliance Option
As a result of the review of the
NESHAP, we are proposing the
elimination of language in the NESHAP
that allows HCl regeneration facilities to
establish an alternative chlorine
concentration standard for existing acid
regeneration plants. The NESHAP
currently allows the owner or operator
to request approval for a source-specific
standard based on the maximum design
temperature and minimum excess air
that allows production of iron oxide of
acceptable quality if the source is
unable to meet the otherwise applicable
emissions limit for chlorine (Cl2) of 6
parts per million by volume (ppmv) (40
CFR subpart CCC). Upon review of this
provision, we believe that it does not
meet the requirements in section
112(d)(2) and (3) of the CAA. MACT
standards for existing sources cannot be
less stringent than the average emissions
limitation achieved by the bestperforming 12 percent of existing
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sources in the category or subcategory
(or the best-performing five sources for
categories or subcategories with fewer
than 30 sources). This is referred to as
the ‘‘MACT floor.’’ The promulgated
standard in 40 CFR part 63,
§ 63.1157(b)(2), subpart CCC, was
established in compliance with EPA’s
obligation to promulgate a standard
representing the MACT floor. We do not
have authority to allow a source to seek
an alternative standard if such a source
is unable to meet a standard which
reflects the MACT floor level of control.
Therefore, we are proposing to amend
the NESHAP by removing the language
in § 63.1157(b)(2) that currently allows
a source-specific standard for sources
that demonstrate they are unable to
meet the applicable standard and
removing the methods for establishing a
source-specific standard under
§ 63.1161(c)(2) of the NESHAP. This
action is being proposed under section
112(d)(2) and (3) of the CAA to ensure
that the NESHAP is consistent with
requirements of that section.
In addition to fulfilling the statutory
requirements of Sections 112(d)(2) and
(3), we note that this proposed action
also will reduce the emissions of
chlorine and HCl from this source
category, resulting in a reduction of the
Hazard Index (HI) from 2 due to HCl
(that was presented in the October 21,
2010 proposal) to an HI of less than one.
The one facility that posed the HI of 2
(in the October 21, 2010 proposal) will
need to improve controls and reduce
emissions by more than a factor of 2 to
comply with this proposed action.
B. Compliance Dates
We are proposing that the
amendments to § 63.1157(b)(2) and
§ 63.1161(c)(2) of the NESHAP would be
effective upon promulgation of the final
rule.
VI. What other actions are we
proposing?
A. Electronic Reporting
EPA must have performance test data
to conduct effective reviews of CAA
sections 112 and 129 standards, as well
as for many other purposes including
compliance determinations, emission
factor development, and annual
emission rate determinations. In
conducting these required reviews, EPA
has found it ineffective and time
consuming, not only for us, but also for
regulatory agencies and source owners
and operators, to locate, collect, and
submit performance test data because of
varied locations for data storage and
varied data storage methods. In recent
years, though, stack testing firms have
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typically collected performance test data
in electronic format, making it possible
to move to an electronic data submittal
system that would increase the ease and
efficiency of data submittal and improve
data accessibility.
Through this proposal, EPA is
presenting a step to increase the ease
and efficiency of data submittal and
improve data accessibility. Specifically,
EPA is proposing that owners and
operators of facilities in the Hard and
Decorative Chromium Electroplating
and Chromium Anodizing source
categories and the Steel Pickling—HCl
Process Facilities and Hydrochloric
Acid Regeneration Plants source
categories submit electronic copies of
required performance test reports to
EPA’s WebFIRE database. The WebFIRE
database was constructed to store
performance test data for use in
developing emission factors. A
description of the WebFIRE database is
available at https://cfpub.epa.gov/
oarweb/index.cfm?action=fire.main.
As proposed above, data entry would
be through an electronic emissions test
report structure called the Electronic
Reporting Tool (ERT). The ERT would
generate an electronic report which
would be submitted using the
Compliance and Emissions Data
Reporting Interface (CEDRI). The
submitted report would be transmitted
through EPA’s Central Data Exchange
(CDX) network for storage in the
WebFIRE database making submittal of
data very straightforward and easy. A
description of the ERT can be found at
https://www.epa.gov/ttn/chief/ert/
index.html and CEDRI can be accessed
through the CDX Web site
(www.epa.gov/cdx).
The proposal to submit performance
test data electronically to EPA would
apply only to those performance tests
conducted using test methods that will
be supported by the ERT. The ERT
contains a specific electronic data entry
form for most of the commonly used
EPA reference methods. A listing of the
pollutants and test methods supported
by the ERT is available at https://
www.epa.gov/ttn/chief/ert/.
We believe that industry would benefit
from this proposed approach to
electronic data submittal. Having these
data, EPA would be able to develop
improved emission factors, make fewer
information requests, and promulgate
better regulations.
One major advantage of the proposed
submittal of performance test data
through the ERT is a standardized
method to compile and store much of
the documentation required to be
reported by this rule. Another advantage
is that the ERT clearly states what
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testing information would be required.
Another important proposed benefit of
submitting these data to EPA at the time
the source test is conducted is that it
should substantially reduce the effort
involved in data collection activities in
the future. When EPA has performance
test data in hand, there will likely be
fewer or less substantial data collection
requests in conjunction with
prospective required residual risk
assessments or technology reviews. This
would result in a reduced burden on
both affected facilities (in terms of
reduced manpower to respond to data
collection requests) and EPA (in terms
of preparing and distributing data
collection requests and assessing the
results).
State, local, and tribal agencies could
also benefit from more streamlined and
accurate review of electronic data
submitted to them. The ERT would
allow for an electronic review process
rather than a manual data assessment
making review and evaluation of the
source provided data and calculations
easier and more efficient. Finally,
another benefit of the proposed data
submittal to WebFIRE electronically is
that these data would greatly improve
the overall quality of existing and new
emissions factors by supplementing the
pool of emissions test data for
establishing emissions factors and by
ensuring that the factors are more
representative of current industry
operational procedures. A common
complaint heard from industry and
regulators is that emission factors are
outdated or not representative of a
particular source category. With timely
receipt and incorporation of data from
most performance tests, EPA would be
able to ensure that emission factors,
when updated, represent the most
current range of operational practices. In
summary, in addition to supporting
regulation development, control strategy
development, and other air pollution
control activities, having an electronic
database populated with performance
test data would save industry, state,
local, tribal agencies, and EPA
significant time, money, and effort
while also improving the quality of
emission inventories and, as a result, air
quality regulations.
VII. Summary of Cost, Environmental,
and Economic Impacts
A. What are the affected sources?
1. Chromium Electroplating and
Chromium Anodizing
For the proposed amendments to the
Chromium Electroplating NESHAP, the
affected sources are each hard
chromium electroplating tank, each
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decorative chromium electroplating
tank, and each chromium anodizing
tank located at a facility that performs
hard chromium electroplating,
decorative chromium electroplating, or
chromium anodizing.
2. Steel Pickling
For the proposed amendments to the
Steel Pickling NESHAP, the affected
sources are hydrochloric acid
regeneration plants that are major
sources of HAP.
B. What are the emission reductions?
1. Chromium Electroplating and
Chromium Anodizing
Overall, the proposed amendments to
the Chromium Electroplating NESHAP
would reduce nationwide emissions of
chromium compounds by an estimated
208 pounds per year (lbs/yr) from the
current levels of 1,140 lbs/yr down to
930 lbs/yr. For large hard chromium
electroplating, the proposed
amendments would reduce chromium
compound emissions by about 121 lbs/
yr from 561 lbs/yr down to 440 pounds.
For small hard chromium electroplating,
the proposed amendments would
reduce chromium compound emissions
by an estimated 41 lbs/yr from 240 lbs/
yr to 199 lbs/yr. For decorative
chromium electroplating, the proposed
amendments would reduce chromium
compound emissions by an estimated 40
lbs/yr from 280 lbs/yr down to 240 lbs/
yr. For chromium anodizing, the
proposed amendments would reduce
chromium compound emissions by
about 6 lbs/yr from 66 lbs/yr down to
60 lbs/yr. The proposed amendments
would have negligible impacts on
secondary emissions because the
additional control equipment that
would be required would not
significantly impact energy use by the
affected facilities.
2. Steel Pickling
We estimate that the proposed
amendment to remove the alternative
compliance provision for hydrochloric
acid regeneration facilities would
reduce emissions of chlorine by 15 tpy.
C. What are the cost impacts?
1. Chromium Electroplating and
Chromium Anodizing
We estimate that these proposed
amendments would achieve 208 pounds
reductions in hexavalent chromium
emissions, and that the total capital and
total annualized cost for the proposed
amendments would be $3.7 million and
$3.1 million/yr, respectively. The
overall cost effectiveness would be
$14,900 per pound of hexavalent
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chromium emissions reductions. A
summary of the estimated costs and
reductions of hexavalent chromium
emissions are shown in Table 7.
TABLE 7—SUMMARY OF THE ESTIMATED COSTS, REDUCTIONS, AND COST EFFECTIVENESS FOR PROPOSED
REQUIREMENTS FOR CHROMIUM ELECTROPLATING AND ANODIZING SOURCE CATEGORIES
Capital costs
(controls +
WAFS + all
testing)
Source category or subcategory
Annualized costs
(controls +
WAFS + all
testing), $/yr
Emissions
reductions
(lbs/yr)
Cost
effectiveness
($/lb)
Large Hard Chromium Electroplating ..............................................
Small Hard Chromium Electroplating ..............................................
Decorative Chromium Electroplating ...............................................
Chromic Acid Anodizing ..................................................................
$1,821,000
1,445,000
183,000
245,000
$2,195,000
653,000
189,000
54,000
121
41
39
6
$18,100
15,800
4,800
9,100
Total ..........................................................................................
3,694,000
3,090,000
208
14,900
2. Steel Pickling
For HCl acid regeneration plants, we
estimate that the capital cost for the
proposed amendments would be
between $100,000 and $200,000,
depending on whether the existing
equipment can be upgraded or will need
to be replaced. The annualized cost are
estimated to be between $11,419 and
$22,837 per year. The estimated cost
effectiveness would be $761 to $1,522
per ton of HAP (mainly chlorine and
HCl).
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D. What are the economic impacts?
1. Chromium Electroplating and
Chromium Anodizing
EPA performed a screening analysis
for impacts on all affected small entities
by comparing compliance costs to
average sales revenues by employment
size category.12 This is known as the
cost-to-revenue or cost-to-sales ratio, or
the ‘‘sales test.’’ The ‘‘sales test’’ is the
impact methodology EPA primarily
employs in analyzing small entity
impacts as opposed to a ‘‘profits test,’’
in which annualized compliance costs
are calculated as a share of profits. The
sales test is frequently used because
revenues or sales data are commonly
available for entities impacted by EPA
regulations, and profits data normally
made available are often not the true
profit earned by firms because of
accounting and tax considerations. The
use of a ‘‘sales test’’ for estimating small
business impacts for a rulemaking is
consistent with guidance offered by EPA
on compliance with SBREFA 13 and is
consistent with guidance published by
the U.S. SBA’s Office of Advocacy that
12 https://www.census.gov/econ/susb/data/
susb2002.html.
13 The SBREFA compliance guidance to EPA
rulewriters regarding the types of small business
analysis that should be considered can be found at:
https://www.epa.gov/sbrefa/documents/GuidanceRegFlexAct.pdf. See Table 2 on page 36 for
guidance on interpretations of the magnitude of the
cost-to-sales numbers.
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suggests that cost as a percentage of total
revenues is a metric for evaluating cost
increases on small entities in relation to
increases on large entities (U.S. SBA,
2010).14
Based on the analysis, we estimate
that approximately 96 percent of all
affected facilities have a cost-to-sales
ratio of less than 1 percent. In addition,
for approximately 1 percent of all
affected facilities, or 9 facilities with
fewer than 20 employees, the potential
for cost-to-sales impacts may be
between 3 and 8 percent. All of these
facilities are in the hard chromium
electroplating category, with 2 of the
facilities in the small hard chromium
electroplating category and 7 in the
large hard chromium electroplating
category. For these categories, because
the average sales receipts used for the
analysis may understate sales for some
facilities and because these facilities are
likely to be able to pass cost increases
through to their customers, we do not
anticipate the regulatory proposal to
result in firm closures, significant price
increases, or substantial profit loss. We
conclude that this proposal will not
have a significant economic impact on
a substantial number of small entities.
More information and details of this
analysis are provided in the technical
document ‘‘Economic Impact Analysis
for Risk and Technology Review:
Chromium Electroplating,’’ which is
available in the docket for this proposed
rule.
2. Steel Pickling
Because only one of the
approximately 100 facilities incurs any
cost for controls and that cost is
estimated to be less than 1 percent of
sales, no significant price or
productivity impacts are anticipated.
14 U.S. SBA, Office of Advocacy. A Guide for
Government Agencies, How to Comply with the
Regulatory Flexibility Act, Implementing the
President’s Small Business Agenda and Executive
Order 13272, June 2010.
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E. What are the benefits?
1. Chromium Electroplating and
Chromium Anodizing
The estimated reductions in
chromium emissions that will be
achieved by this proposed rule will
provide benefits to public health. The
proposed limits will result in significant
reductions in the actual and allowable
emissions of hexavalent chromium
therefore will reduce the actual and
potential cancer risks due to emissions
of chromium from this source category.
2. Steel Pickling
The estimated reductions in hydrogen
chloride and chlorine emissions that
will result from this proposed action
will provide benefits to public health.
The proposed limits will result in
reductions in the potential for
noncancer health effects due to
emissions of these HAP.
VIII. Request for Comments
We are soliciting comments on all
aspects of this proposed action. All
comments received during the comment
period will be considered. In EPA’s
strive to continue to promote
sustainability in our protection of
human health and the environment, we
request comment on sustainability
related to the types of fume
suppressants and surfactants, depending
on their chemical properties, which may
have more or less potential for negative
health and environmental impacts
beyond the air emissions addressed by
this supplemental proposal. In addition
to general comments on this proposed
action, we are also soliciting additional
information and data (e.g., on emissions,
emissions concentrations results from
stack emissions tests, flow rates, facility
parameters, facility types, controls, test
reports, etc.) that may help to reduce the
uncertainties inherent in the risk
assessments and any additional data
that would inform the other analyses
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described in this preamble (such as the
analyses of the costs and reductions that
would result from the proposed
requirements). Because our current data
set includes test results for only one
chromium anodizing tank, we
specifically request additional
performance test data for chromium
anodizing sources, including emissions
concentration, exhaust flow rates,
rectifier output, and control device type.
Finally, we are requesting additional
information on the costs and feasibility
of using WAFS that do not contain
PFOS to meet the proposed surface
tension limits. Such data should include
supporting documentation in sufficient
detail to allow characterization of the
quality and representativeness of the
data or information. We are not reopening the public comment period for
the actions proposed in the October 21,
2010 notice.
IX. 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 12866 (58 FR
51735, October 4, 1993), this action is a
significant regulatory action because it
raises novel legal and policy issues.
Accordingly, 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.
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B. Paperwork Reduction Act
The information collection
requirements in this rule have been
submitted for approval to OMB under
the Paperwork Reduction Act, 44 U.S.C.
3501, et seq.
We are not proposing any new
paperwork requirements to the Steel
Pickling—HCl Process Facilities and
Hydrochloric Acid Regeneration Plants
MACT standards. Revisions and burden
associated with amendments to the
Hard and Decorative Chromium
Electroplating and Chromium
Anodizing Tanks are discussed in the
following paragraphs. The OMB has
previously approved the information
collection requirements contained in the
existing regulation being amended with
this proposed rule (i.e., 40 CFR part 63,
subparts N and CCC) under the
provisions of the Paperwork Reduction
Act, 44 U.S.C. 3501, et seq. The OMB
control numbers for EPA’s regulations
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in 40 CFR are listed in 40 CFR part 9.
Burden is defined at 5 CFR 1320.3(b).
The ICR document prepared by EPA
for the amendments to the Hard and
Decorative Chromium Electroplating
and Chromium Anodizing Tanks
NESHAP has been assigned EPA ICR
number 1611.08. Burden changes
associated with these amendments
would result from the emission testing
requirements and compliance
demonstrations being proposed with
today’s action. The estimated average
burden per response is 9 hours; the
frequency of response is one-time for all
respondents that must comply with the
rule’s reporting requirements and the
estimated average number of likely
respondents per year is 485. The cost
burden to respondents resulting from
the collection of information includes
the total capital cost annualized over the
equipment’s expected useful life
($100,958), a total operation and
maintenance component ($0 per year),
and a labor cost component (about
$152,116 per year).
An agency may not conduct or
sponsor, and a person is not required to
respond to a collection of information
unless it displays a currently valid OMB
control number.
To comment on the Agency’s need for
this information, the accuracy of the
provided burden estimates, and any
suggested methods for minimizing
respondent burden, EPA has established
a public docket for this rule, which
includes these ICR, under Docket ID
number EPA–HQ–OAR–2010–0600.
Submit any comments related to the ICR
to EPA and OMB. See ADDRESSES
section at the beginning of this notice
for where to submit comments to EPA.
Send comments to OMB at the Office of
Information and Regulatory Affairs,
Office of Management and Budget, 725
17th Street NW., Washington, DC 20503,
Attention: Desk Office for EPA. Since
OMB is required to make a decision
concerning the ICR between 30 and 60
days after February 8, 2012, a comment
to OMB is best assured of having its full
effect if OMB receives it by March 9,
2012. The final rule will respond to any
OMB or public comments on the
information collection requirements
contained in this proposal.
C. Regulatory Flexibility Act
The Regulatory Flexibility Act (RFA)
generally requires an agency to prepare
a regulatory flexibility analysis of any
rule subject to notice and comment
rulemaking requirements under the
Administrative Procedure Act or any
other statute unless the agency certifies
that the rule will not have a significant
economic impact on a substantial
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number of small entities. Small entities
include small businesses, small
organizations, and small governmental
jurisdictions.
For purposes of assessing the impacts
of today’s proposed rule on small
entities, small entity is defined as: (1) A
small business that is a small industrial
entity as defined by the Small Business
Administration’s (SBA) regulations at 13
CFR 121.201; (2) a small governmental
jurisdiction that is a government of a
city, county, town, school district or
special district with a population of less
than 50,000; and (3) a small
organization that is any not-for-profit
enterprise which is independently
owned and operated and is not
dominant in its field.
After considering the economic
impact of this supplemental proposed
rule on small entities, I certify that this
action will not have a significant
economic impact on a substantial
number of small entities. This proposed
rule would impose more stringent
emissions limits and lower surface
tension requirements. These new
proposed requirements and restrictions
to the hard and decorative chromium
electroplating and chromium anodizing
tanks MACT standard will impact small
entities, but those impacts have been
estimated to be nominal. The proposed
emissions limits reflect the level of
performance currently being achieved
by most facilities, and many facilities
currently have emissions that are far
below the proposed limits. With regard
to the remaining facilities (those that
will need to achieve emissions
reductions), most of these facilities can
achieve the proposed limits at low costs
(e.g., by using additional fume
suppressants).
The EPA’s analysis estimated that 96
percent of the affected entities will have
an annualized cost of less than 1 percent
of sales. In addition, approximately 1
percent of affected entities, or 9
facilities with fewer than 20 employees,
may have cost-to-sales ratios between 3
to 8 percent. All of these facilities are in
the hard chromium electroplating
category, with 2 of the facilities in the
small hard chromium electroplating
category and 7 in the large hard
chromium electroplating category.
Since our analysis indicates that a
small subset of facilities (about 1
percent) may have cost-to-sales ratios
greater than 3 percent, we have
conducted additional economic impact
analyses on this small subset of facilities
to better understand the potential
economic impacts for these facilities.
The additional analyses indicate the
estimates of costs-to-sales ratios in the
initial analyses are more likely to be
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overstated rather than understated
because the additional analyses indicate
that sales are typically higher for these
sources than the average value used in
the initial analysis.
Moreover, because of the nature of the
market, these facilities are likely to be
able to pass cost increases through to
their customers. As such, we do not
anticipate the proposal to result in firm
closures, or substantial profit loss. More
information and details of this analysis
are provided in the technical document
‘‘Economic Impact Analysis for Risk and
Technology Review: Chromium
Electroplating,’’ which is available in
the docket for this proposed rule.
Although this proposed rule will not
have a significant economic impact on
a substantial number of small entities,
EPA nonetheless has tried to reduce the
impact of this rule on small entities. We
continue to be interested in the
potential impacts of the proposed rule
on small entities and welcome
comments on issues related to such
impacts.
srobinson on DSK4SPTVN1PROD with PROPOSALS2
D. Unfunded Mandates Reform Act
This proposed rule does not contain
a Federal mandate 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
proposed rule would not result in
expenditures of $100 million or more
for State, local, and tribal governments,
in aggregate, or the private sector in any
1 year. The proposed rule imposes no
enforceable duties on any State, local, or
tribal governments or the private sector.
Thus, this proposed rule is not subject
to the requirements of sections 202 or
205 of the UMRA.
This proposed rule is also not subject
to the requirements of section 203 of
UMRA because it contains no regulatory
requirements that might significantly or
uniquely affect small governments. This
action contains no requirements that
apply to such governments nor does it
impose obligations upon them.
E. Executive Order 13132: Federalism
This proposed rule does not have
federalism implications. It will not have
substantial direct effects on the States,
on the relationship between the national
government and the States, or on the
distribution of power and
responsibilities among the various
levels of government, as specified in
Executive Order 13132. None of the
facilities subject to this action are
owned or operated by State
governments, and, because no new
requirements are being promulgated,
nothing in this proposal will supersede
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State regulations. Thus, Executive Order
13132 does not apply to this proposed
rule.
In the spirit of Executive Order 13132,
and consistent with EPA policy to
promote communications between EPA
and State and local governments, EPA
specifically solicits comment on this
proposed rule from State and local
officials.
F. Executive Order 13175: Consultation
and Coordination With Indian Tribal
Governments
This proposed rule will not have
tribal implications, as specified in
Executive Order 13175 (65 FR 67249,
November 9, 2000). It will not have
substantial direct effect on tribal
governments, on the relationship
between the Federal government and
Indian tribes, or on the distribution of
power and responsibilities between the
Federal government and Indian tribes,
as specified in Executive Order 13175.
Thus, Executive Order 13175 does not
apply to this action.
EPA specifically solicits additional
comment on this proposed action from
tribal officials.
G. Executive Order 13045: Protection of
Children From Environmental Health
Risks and Safety Risks
This proposed rule is not subject to
Executive Order 13045 (62 FR 19885,
April 23, 1997) because it is not
economically significant as defined in
Executive Order 12866, and because the
Agency does not believe the
environmental health or safety risks
addressed by this action present a
disproportionate risk to children. This
action would not relax the control
measures on existing regulated sources.
Nevertheless, this proposed action
would result in reductions in cancer
risks due to chromium emissions for
people of all ages, including children.
The EPA’s risk assessments (included in
the docket for this proposed rule)
demonstrate that these regulations, with
the amendments being proposed in
today’s action, will be health protective.
The public is invited to submit
comments or identify peer-reviewed
studies and data that assess effects of
early life exposure to hexavalent
chromium.
H. Executive Order 13211: Actions
Concerning Regulations That
Significantly Affect Energy Supply,
Distribution, or Use
This action is not a ‘‘significant
energy action’’ as defined under
Executive Order 13211 (66 FR 28355
(May 22, 2001)), because it is not likely
to have significant adverse effect on the
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supply, distribution, or use of energy.
This action will not create any new
requirements for sources in the energy
supply, distribution, or use sectors.
I. National Technology Transfer and
Advancement Act
Section 12(d) of the National
Technology Transfer and Advancement
Act of 1995 (NTTAA), Public Law 104–
113, 12(d) (15 U.S.C. 272 note) directs
EPA to use voluntary consensus
standards (VCS) in its regulatory
activities unless to do so would be
inconsistent with applicable law or
otherwise impractical. VCS are
technical standards (e.g., materials
specifications, test methods, sampling
procedures, and business practices) that
are developed or adopted by VCS
bodies. The NTTAA directs EPA to
provide Congress, through OMB,
explanations when the Agency decides
not to use available and applicable VCS.
This proposed rulemaking does not
involve technical standards. Therefore,
EPA is not considering the use of any
VCS.
J. Executive Order 12898: Federal
Actions To Address Environmental
Justice in Minority Populations and
Low-Income Populations
Executive Order 12898 (59 FR 7629,
February 16, 1994) establishes Federal
executive policy on environmental
justice. Its main provision directs
Federal agencies, to the greatest extent
practicable and permitted by law, to
make environmental justice part of their
mission by identifying and addressing,
as appropriate, disproportionately high
and adverse human health or
environmental effects of their programs,
policies, and activities on minority
populations and low-income
populations in the United States.
The EPA has determined that this
proposed rule will not have
disproportionately high and adverse
human health or environmental effects
on minority or low-income populations
because it maintains or increases the
level of environmental protection for all
affected populations without having any
disproportionately high and adverse
human health or environmental effects
on any population, including any
minority low-income, or indigenous
populations. Further, the EPA is
proposing that, after implementation of
the provisions of this rule, the public
health of all demographic groups will be
protected with an ample margin of
safety.
To examine the potential for any
environmental justice issues that might
be associated with two of the source
categories associated with today’s
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proposed rule (Hard Chromium
Electroplaters and Decorative
Chromium Electroplaters), we evaluated
the percentages of various social,
demographic, and economic groups
within the at-risk populations living
near the facilities where these source
categories are located and compared
them to national averages. We did not
conduct this type of analysis for the
chromic acid anodizing or steel pickling
categories because the numbers of
people subjected to cancer risks greater
than 1-in-1 million due to HAP
emissions from these source categories
were quite low. The development of
demographic analyses to inform the
consideration of environmental justice
issues in EPA rulemakings is an
evolving process. The EPA offers the
demographic analyses in this
rulemaking as examples of how such
analyses might be developed to inform
such consideration, and invites public
comment on the approaches used and
the interpretations made from the
results, with the hope that this will
support the refinement and improve
utility of such analyses for future
rulemakings.
Our analysis of the demographics of
the population with estimated risks
greater than 1-in-1 million indicates
potential disparities in risks between
demographic groups, including the
African American, Other and
Multiracial, Hispanic, Below the
Poverty Level, and the Over 25 without
a High School Diploma groups. These
groups stand to benefit the most from
the emission reductions achieved by
this proposed rulemaking.
EPA defines ‘‘Environmental Justice’’
to include meaningful involvement of
all people regardless of race, color,
national origin, or income with respect
to the development, implementation,
and enforcement of environmental laws,
regulations, and policies. To promote
meaningful involvement, after the rule
is proposed, EPA will be conducting a
webinar to inform the public about the
rule and to outline how to submit
written comments to the docket. Further
stakeholder and public input is
expected through public comment and
follow-up meetings with interested
stakeholders.
List of Subjects in 40 CFR Part 63
Environmental protection, Air
pollution control, Reporting and
recordkeeping requirements, Volatile
organic compounds.
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Dated: January 27, 2012.
Lisa P. Jackson,
Administrator.
For the reasons stated in the
preamble, part 63 of title 40, chapter I,
of the Code of Federal Regulations is
proposed to be amended as follows:
PART 63—[AMENDED]
1. The authority citation for part 63
continues to read as follows:
Authority: 42 U.S.C. 7401, et seq.
Subpart N—[Amended]
2. Section 63.341 is amended by
adding, in alphabetical order in
paragraph (a), definitions for existing
affected source and new affected source.
§ 63.341
Definitions and nomenclature.
(a) * * *
Existing affected source means an
affected hard chromium electroplating
tank, decorative chromium
electroplating tank, or chromium
anodizing tank, the construction or
reconstruction of which commenced on
or before February 8, 2012.
*
*
*
*
*
New affected source means an
affected hard chromium electroplating
tank, decorative chromium
electroplating tank, or chromium
anodizing tank, the construction or
reconstruction of which commenced
after February 8, 2012.
*
*
*
*
*
3. Section 63.342 is amended by:
a. Revising paragraphs (c)(1)(i),
(c)(1)(ii), and (c)(1)(iii);
b. Adding paragraph (c)(1)(iv);
c. Revising paragraphs (c)(2)(i),
(c)(2)(ii), and (c)(2)(iii);
d. Adding paragraph (c)(2)(vi);
e. Revising paragraphs (d)(1) and
(d)(2); and
f. Adding paragraph (d)(3) to read as
follows:
§ 63.342
Standards.
*
*
*
*
*
(c)(1) * * *
(i) Not allowing the concentration of
total chromium in the exhaust gas
stream discharged to the atmosphere to
exceed 0.011 milligrams of total
chromium per dry standard cubic meter
(mg/dscm) of ventilation air (4.8 × 10¥6
grains per dry standard cubic foot
(gr/dscf)) for all open surface hard
chromium electroplating tanks that are
existing affected sources and are located
at large hard chromium electroplating
facilities; or
(ii) Not allowing the concentration of
total chromium in the exhaust gas
stream discharged to the atmosphere to
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exceed 0.015 mg/dscm (6.6 × 10¥6
gr/dscf) for all open surface hard
chromium electroplating tanks that are
existing affected sources and are located
at small, hard chromium electroplating
facilities; or
(iii) If a chemical fume suppressant
containing a wetting agent is used, not
allowing the surface tension of the
electroplating or anodizing bath
contained within the affected tank to
exceed 40 dynes per centimeter (dynes/
cm) (2.8 × 10¥3 pound-force per foot
(lbf/ft)), as measured by a
stalagmometer, or 33 dynes/cm (2.3 ×
10¥3 lbf/ft), as measured by a
tensiometer at any time during tank
operation; or
(iv) Not allowing the concentration of
total chromium in the exhaust gas
stream discharged to the atmosphere to
exceed 0.006 mg/dscm of ventilation air
(2.6 × 10¥6 gr/dscf) for all open surface
hard chromium electroplating tanks that
are new affected sources.
*
*
*
*
*
(2) * * *
(i) Not allowing the concentration of
total chromium in the exhaust gas
stream discharged to the atmosphere to
exceed 0.011 mg/dscm of ventilation air
(4.8 × 10¥6 gr/dscf) for all enclosed hard
chromium electroplating tanks that are
existing affected sources and are located
at large hard chromium electroplating
facilities; or
(ii) Not allowing the concentration of
total chromium in the exhaust gas
stream discharged to the atmosphere to
exceed 0.015 mg/dscm (6.6 × 10¥6
gr/dscf) for all enclosed hard chromium
electroplating tanks that are existing
affected sources and are located at
small, hard chromium electroplating
facilities; or
(iii) If a chemical fume suppressant
containing a wetting agent is used, not
allowing the surface tension of the
electroplating or anodizing bath
contained within the affected tank to
exceed 40 dynes/cm (2.8 × 10¥3 lbf/ft),
as measured by a stalagmometer, or 33
dynes/cm (2.3 × 10¥3 lbf/ft), as
measured by a tensiometer at any time
during tank operation; or
*
*
*
*
*
(vi) Not allowing the concentration of
total chromium in the exhaust gas
stream discharged to the atmosphere to
exceed 0.006 mg/dscm of ventilation air
(2.6 × 10¥6 gr/dscf) for all enclosed hard
chromium electroplating tanks that are
new affected sources.
*
*
*
*
*
(d) Standards for decorative
chromium electroplating tanks using a
chromic acid bath and chromium
anodizing tanks. During tank operation,
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each owner or operator of an existing,
new, or reconstructed affected source
shall control chromium emissions
discharged to the atmosphere from that
affected source by either:
(1) Not allowing the concentration of
total chromium in the exhaust gas
stream discharged to the atmosphere to
exceed 0.007 mg/dscm (3.1 × 10¥6
gr/dscf) for all existing decorative
chromium electroplating tanks using a
chromic acid bath and all existing
chromium anodizing tanks; or
(2) Not allowing the concentration of
total chromium in the exhaust gas
stream discharged to the atmosphere to
exceed 0.006 mg/dscm (2.6 × 10¥6 gr/
dscf) for all new or reconstructed
decorative chromium electroplating
tanks using a chromic acid bath and all
new or reconstructed chromium
anodizing tanks;
(3) If a chemical fume suppressant
containing a wetting agent is used, not
allowing the surface tension of the
electroplating or anodizing bath
contained within the affected tank to
exceed 40 dynes/cm (2.8 × 10¥3 lbf/ft),
as measured by a stalagmometer or 33
dynes/cm (2.3 × 10¥3 lbf/ft), as
measured by a tensiometer at any time
during tank operation, for all existing,
new, or reconstructed decorative
chromium electroplating tanks using a
chromic acid bath and all existing, new,
or reconstructed chromium anodizing
tanks.
*
*
*
*
*
4. Section 63.343 is amended by:
a. Revising paragraphs (a)(1), (a)(2),
and (a)(4);
b. Revising paragraph (b)(1); and
c. Revising paragraphs (c)(1)(ii),
(c)(2)(ii), (c)(4)(ii), (c)(5)(i), (c)(5)(ii), and
(c)(6)(ii) to read as follows:
srobinson on DSK4SPTVN1PROD with PROPOSALS2
§ 63.343
Compliance provisions.
(a)(1) The owner or operator of an
existing affected source shall comply
with the emission limitations in
§ 63.342 no later than [DATE 2 YEARS
AFTER PUBLICATION OF FINAL RULE
IN Federal Register].
(2) The owner or operator of a new or
reconstructed affected source that has
an initial startup after [DATE OF
PUBLICATION OF FINAL RULE IN
THE Federal Register], shall comply
immediately upon startup of the source.
*
*
*
*
*
(4) The owner or operator of a new
area source (i.e., an area source for
which construction or reconstruction
was commenced after February 8, 2012)
that increases actual or potential
emissions of hazardous air pollutants
such that the area source becomes a
major source must comply with the
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provisions for new major sources,
immediately upon becoming a major
source.
*
*
*
*
*
(b) Methods to demonstrate initial
compliance. (1) Except as provided in
paragraphs (b)(2) and (b)(3) of this
section, an owner or operator of an
affected source subject to the
requirements of this subpart is required
to conduct an initial performance test as
required under § 63.7, using the
procedures and test methods listed in
§§ 63.7 and 63.344.
*
*
*
*
*
(c) * * *
(1) * * *
(ii) On and after the date on which the
initial performance test is required to be
completed under § 63.7, the owner or
operator of an affected source, or group
of affected sources under common
control, shall monitor and record the
pressure drop across the composite
mesh-pad system once each day that
any affected source is operating. To be
in compliance with the standards, the
composite mesh-pad system shall be
operated within ±2 inches of water
column of the pressure drop value
established during the initial
performance test, or shall be operated
within the range of compliant values for
pressure drop established during
multiple performance tests.
*
*
*
*
*
(2) * * *
(ii) On and after the date on which the
initial performance test is required to be
completed under § 63.7, the owner or
operator of an affected source, or group
of affected sources under common
control, shall monitor and record the
velocity pressure at the inlet to the
packed-bed system and the pressure
drop across the scrubber system once
each day that any affected source is
operating. To be in compliance with the
standards, the scrubber system shall be
operated within ±10 percent of the
velocity pressure value established
during the initial performance test, and
within ±1 inch of water column of the
pressure drop value established during
the initial performance test, or within
the range of compliant operating
parameter values established during
multiple performance tests.
*
*
*
*
*
(4) * * *
(ii) On and after the date on which the
initial performance test is required to be
completed under § 63.7, the owner or
operator of an affected source, or group
of affected sources under common
control, shall monitor and record the
pressure drop across the fiber-bed mist
eliminator, and the control device
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6655
installed upstream of the fiber bed to
prevent plugging, once each day that
any affected source is operating. To be
in compliance with the standards, the
fiber-bed mist eliminator and the
upstream control device shall be
operated within ±1 inch of water
column of the pressure drop value
established during the initial
performance test, or shall be operated
within the range of compliant values for
pressure drop established during
multiple performance tests.
*
*
*
*
*
(5) Wetting agent-type or combination
wetting agent-type/foam blanket fume
suppressants. (i) During the initial
performance test, the owner or operator
of an affected source complying with
the emission limitations in § 63.342
through the use of a wetting agent in the
electroplating or anodizing bath shall
determine the outlet chromium
concentration using the procedures in
§ 63.344(c). The owner or operator shall
establish as the site-specific operating
parameter the surface tension of the
bath using Method 306B, appendix A of
this part, setting the maximum value
that corresponds to compliance with the
applicable emission limitation. In lieu
of establishing the maximum surface
tension during the performance test, the
owner or operator may accept 40 dynes/
cm, as measured by a stalagmometer, or
33 dynes/cm, as measured by a
tensiometer, as the maximum surface
tension value that corresponds to
compliance with the applicable
emission limitation. However, the
owner or operator is exempt from
conducting a performance test only if
the criteria of paragraph (b)(2) of this
section are met.
(ii) On and after the date on which the
initial performance test is required to be
completed under § 63.7, the owner or
operator of an affected source shall
monitor the surface tension of the
electroplating or anodizing bath.
Operation of the affected source at a
surface tension greater than the value
established during the performance test,
or greater than 40 dynes/cm, as
measured by a stalagmometer, or 33
dynes/cm, as measured by a
tensiometer, if the owner or operator is
using this value in accordance with
paragraph (c)(5)(i) of this section, shall
constitute noncompliance with the
standards. The surface tension shall be
monitored according to the following
schedule:
*
*
*
*
*
(6) * * *
(ii) On and after the date on which the
initial performance test is required to be
completed under § 63.7, the owner or
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operator of an affected source shall
monitor the foam blanket thickness of
the electroplating or anodizing bath.
Operation of the affected source at a
foam blanket thickness less than the
value established during the
performance test, or less than 2.54 cm
(1 inch) if the owner or operator is using
this value in accordance with paragraph
(c)(6)(i) of this section, shall constitute
noncompliance with the standards. The
foam blanket thickness shall be
measured according to the following
schedule:
*
*
*
*
*
5. Section 63.344 is amended by:
a. Adding paragraphs (b)(1)(v) through
(b)(1)(viii); and
b. Deleting paragraph (b)(2); to read as
follows:
§ 63.344 Performance test requirements
and test methods.
*
claim that some of the information being
submitted for performance tests is
confidential business information (CBI)
must submit a complete ERT file
including information claimed to be CBI
on a compact disk or other commonly
used electronic storage media
(including, but not limited to, flash
drives) to EPA. The electronic media
must be clearly marked as CBI and
mailed to U.S. EPA/OAPQS/CORE CBI
Office, Attention: WebFIRE
Administrator, MD C404–02, 4930 Old
Page Rd., Durham, NC 27703. The same
ERT file with the CBI omitted must be
submitted to EPA via CDX as described
earlier in this paragraph. At the
discretion of the delegated authority,
you must also submit these reports,
including the confidential business
information, to the delegated authority
in the format specified by the delegated
authority.
(ii) All reports required by this
subpart not subject to the requirements
in paragraphs (3)(i) of this section must
be sent to the Administrator at the
appropriate address listed in § 63.13.
The Administrator or the delegated
authority may request a report in any
form suitable for the specific case (e.g.,
by commonly used electronic media
such as Excel spreadsheet, on CD or
hard copy). The Administrator retains
the right to require submittal of reports
subject to paragraph (3)(i) of this section
in paper format.
*
*
*
*
*
*
*
*
*
(b)(1) * * *
(v) The performance test was
conducted after January 25, 1995;
(vi) As of [DATE OF PUBLICATION
OF FINAL RULE IN Federal Register],
the source was using the same
emissions controls that were used
during the compliance test; and
(vii) As of [INSERT DATE OF
PUBLICATION OF FINAL RULE IN
Federal Register], the source was
operating under conditions that are
representative of the conditions under
which the source was operating during
the compliance test; and
(viii) Based on approval from the
permitting authority.
*
*
*
*
*
6. Section 63.347 is amended by
adding paragraph (f)(3) to read as
follows:
§ 63.1157
sources.
§ 63.347
*
Reporting requirements.
srobinson on DSK4SPTVN1PROD with PROPOSALS2
*
*
*
*
*
(f)(3)(i) Within 90 days after the date
of completing each performance test
(defined in § 63.2) as required by this
subpart, you must submit the results of
the performance tests required by this
subpart to EPA’s WebFIRE database by
using the Compliance and Emissions
Data Reporting Interface (CEDRI) that is
accessed through EPA’s Central Data
Exchange (CDX) (www.epa.gov/cdx).
Performance test data must be submitted
in the file format generated through use
of EPA’s Electronic Reporting Tool
(ERT) (see https://www.epa.gov/ttn/chief/
ert/). Only data collected
using test methods on the ERT Web site
are subject to this requirement for
submitting reports electronically to
WebFIRE. Owners or operators who
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Subpart CCC—[Amended]
7. Section 63.1157 is amended by
revising (b)(2) to read as follows:
Emission standards for existing
*
*
*
*
(b) * * *
(2) In addition to the requirement of
paragraph (b)(1) of this section, no
owner or operator of an existing plant
shall cause or allow to be discharged
into the atmosphere from the affected
plant any gases that contain chlorine
(Cl2) in a concentration in excess of 6
ppmv.
*
*
*
*
*
§ 63.1161
[Amended]
8. Section 63.1161 is amended by
deleting paragraph (c)(2).
9. Section 63.1164 is amended by
revising (a) to read as follows:
§ 63.1164
Reporting requirements.
(a) Reporting results of performance
tests. As required by § 63.10(d)(2) of
subpart A of this part, the owner or
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operator of an affected source shall
report the results of any performance
test required by this paragraph to EPA’s
WebFIRE database by using the
Compliance and Emissions Data
Reporting Interface (CEDRI) that is
accessed through EPA’s Central Data
Exchange (CDX) (www.epa.gov/cdx).
Performance test data shall be submitted
in the file format generated through use
of EPA’s Electronic Reporting Tool
(ERT) (see https://www.epa.gov/ttn/chief/
ert/). Only data collected
using test methods listed on the ERT
Web site are subject to this requirement
for submitting reports electronically to
WebFIRE. Owners or operators who
claim that some of the performance test
information being submitted is
confidential business information (CBI)
shall submit a complete ERT file
including information claimed to be CBI
on a compact disk or other commonly
used electronic storage media
(including, but not limited to, flash
drives) by registered letter to EPA and
the same ERT file with the CBI omitted
to EPA via CDX as described earlier in
this paragraph. The compact disk shall
be clearly marked as CBI and mailed to
U.S. EPA/OAPQS/CORE CBI Office,
Attention: WebFIRE Administrator, MD
C404–02, 4930 Old Page Rd., Durham,
NC 27703. At the discretion of the
delegated authority, owners or operators
shall also submit these reports to the
delegated authority in the format
specified by the delegated authority.
*
*
*
*
*
Appendix A—[Amended]
10. Appendix A to part 63, Method
306–B is amended revising paragraph
11.2.1.3 to read as follows:
METHOD 306B—SURFACE TENSION
MEASUREMENT FOR TANKS USED AT
CHROMIUM ELECTROPLATING AND
CHROMIUM ANODIZING FACILITIES
*
*
11.0
*
*
*
*
Analytical Procedure
*
*
*
*
11.2.1.3 If a measurement of the surface
tension of the solution is above the 40 dynes
per centimeter limit, as measured using a
stalagmometer, or above the 33 dynes per
centimeter limit, as measured using a
tensiometer, or above an alternate surface
tension limit established during the
performance test, the time interval shall
revert back to the original monitoring
schedule of once every 4 hours. A subsequent
decrease in frequency would then be allowed
according to Section 11.2.1.
*
*
*
*
*
[FR Doc. 2012–2434 Filed 2–7–12; 8:45 am]
BILLING CODE 6560–50–P
E:\FR\FM\08FEP2.SGM
08FEP2
Agencies
[Federal Register Volume 77, Number 26 (Wednesday, February 8, 2012)]
[Proposed Rules]
[Pages 6628-6656]
From the Federal Register Online via the Government Printing Office [www.gpo.gov]
[FR Doc No: 2012-2434]
[[Page 6627]]
Vol. 77
Wednesday,
No. 26
February 8, 2012
Part II
Environmental Protection Agency
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40 CFR Part 63
National Emission Standards for Hazardous Air Pollutant Emissions: Hard
and Decorative Chromium Electroplating and Chromium Anodizing Tanks;
and Steel Pickling-HCl Process Facilities and Hydrochloric Acid
Regeneration Plants; Proposed Rule
Federal Register / Vol. 77, No. 26 / Wednesday, February 8, 2012 /
Proposed Rules
[[Page 6628]]
-----------------------------------------------------------------------
ENVIRONMENTAL PROTECTION AGENCY
40 CFR Part 63
[EPA-HQ-OAR-2010-0600; FRL-9626-7]
RIN 2060-AQ60
National Emission Standards for Hazardous Air Pollutant
Emissions: Hard and Decorative Chromium Electroplating and Chromium
Anodizing Tanks; and Steel Pickling-HCl Process Facilities and
Hydrochloric Acid Regeneration Plants
AGENCY: Environmental Protection Agency (EPA).
ACTION: Supplemental notice of proposed rulemaking.
-----------------------------------------------------------------------
SUMMARY: This action supplements our proposed amendments to National
Emission Standards for Hazardous Air Pollutant Emissions for Hard and
Decorative Chromium Electroplating and Chromium Anodizing Tanks; and
Steel Pickling-HCl Process Facilities and Hydrochloric Acid
Regeneration Plants, which were published on October 21, 2010 (75 FR
65068, October 21, 2010). In that action, EPA proposed amendments to
these NESHAP under section 112(d)(6) and (f)(2) of the Clean Air Act.
Specifically, this action presents a new technology review and a new
residual risk analysis for chromium electroplating and anodizing
facilities and proposes revisions to the NESHAP based on those reviews.
This action also proposes to remove an alternative compliance method
for Steel Pickling hydrochloric acid regeneration plants. Finally, this
action proposes to incorporate electronic reporting requirements into
both NESHAP.
DATES: Comments must be received on or before March 26, 2012. Under the
Paperwork Reduction Act, comments on the information collection
provisions are best assured of having full effect if the Office of
Management and Budget (OMB) receives a copy of your comments on or
before March 9, 2012.
Public Hearing. If anyone contacts the EPA requesting to speak at a
public hearing by February 21, 2012, a public hearing will be held on
February 23, 2012.
ADDRESSES: You may submit comments, identified by Docket ID No. EPA-HQ-
OAR-2010-0600, by one of the following methods:
Federal eRulemaking Portal: www.regulations.gov: Follow
the instructions for submitting comments.
Email: a-and-r-docket@epa.gov. Include Docket ID No. EPA-
HQ-OAR-2010-0600 in the subject line of the message.
Fax: (202) 566-9744. Attention Docket ID No. EPA-HQ-OAR-
2010-0600.
Mail: U.S. Postal Service, send comments to: EPA Docket
Center, EPA West (Air Docket), Attention Docket ID No. EPA-HQ-OAR-2010-
0600, U.S. Environmental Protection Agency, Mailcode: 2822T, 1200
Pennsylvania Ave. NW., Washington, DC 20460. 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, Office of Management and Budget (OMB), Attn: Desk
Officer for EPA, 725 17th Street NW., Washington, DC 20503.
Hand Delivery: U.S. Environmental Protection Agency, EPA
West (Air Docket), Room 3334, 1301 Constitution Ave. NW., Washington,
DC 20004. Attention Docket ID No. EPA-HQ-OAR-2010-0600. Such deliveries
are only accepted during the Docket's normal hours of operation, and
special arrangements should be made for deliveries of boxed
information.
Instructions. Direct your comments to Docket ID No. EPA-HQ-OAR-
2010-0600. EPA's policy is that all comments received will be included
in the public docket without change and may be made available online at
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 www.regulations.gov or email. The
www.regulations.gov Web site is an ``anonymous access'' system, which
means EPA will not know your identity or contact information unless you
provide it in the body of your comment. If you send an email comment
directly to EPA without going through 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, EPA recommends that you
include your name and other contact information in the body of your
comment and with any disk or CD-ROM you submit. If EPA cannot read your
comment due to technical difficulties and cannot contact you for
clarification, EPA may not be able to consider your comment. Electronic
files should avoid the use of special characters, any form of
encryption, and be free of any defects or viruses. For additional
information about EPA's public docket, visit the EPA Docket Center
homepage at https://www.epa.gov/epahome/dockets.htm.
Docket. The EPA has established a docket for this rulemaking under
Docket ID No. EPA-HQ-OAR-2010-0600. All documents in the docket are
listed in the 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, is not placed on the Internet
and will be publicly available only in hard copy. Publicly available
docket materials are available either electronically in
www.regulations.gov or in hard copy at the EPA Docket Center, EPA West,
Room 3334, 1301 Constitution Ave. NW., Washington, DC. The Public
Reading Room is open from 8:30 a.m. to 4:30 p.m., Monday through
Friday, excluding legal holidays. The telephone number for the Public
Reading Room is (202) 566-1744, and the telephone number for the EPA
Docket Center is (202) 566-1742.
FOR FURTHER INFORMATION CONTACT: For questions about this proposed
action, contact Mr. Phil Mulrine, Sector Policies and Programs Division
(D243-02), Office of Air Quality Planning and Standards, U.S.
Environmental Protection Agency, Research Triangle Park, NC 27711,
telephone (919) 541-5289; fax number: (919) 541-3207; and email
address: mulrine.phil@epa.gov. For specific information regarding the
risk modeling methodology, contact Mr. Mark Morris, Health and
Environmental Impacts Division (C539-02), Office of Air Quality
Planning and Standards, U.S. Environmental Protection Agency, Research
Triangle Park, NC 27711; telephone number: (919) 541-5416; fax number:
(919) 541-0840; and email address: morris.mark@epa.gov.
SUPPLEMENTARY INFORMATION:
Organization of this Document. The information in this preamble is
organized as follows:
I. General Information
A. Does this action apply to me?
B. Where can I get a copy of this document and other related
information?
C. What should I consider as I prepare my comments for the EPA?
D. When would a public hearing occur?
II. Background Information
A. Overview of the Chromium Electroplating and Chromium
Anodizing Source Categories
B. What is the history of the chromium electroplating and
chromium anodizing risk and technology reviews?
C. Overview of the steel pickling source category
[[Page 6629]]
D. What is the history of the Steel Pickling Risk and Technology
Review?
E. What data collection activities were conducted to support
this action?
III. Analyses Performed
A. How did we perform the technology review?
B. For purposes of this supplemental proposal, how did we
estimate the risk posed by each of the three chromium electroplating
source categories?
IV. Analytical Results and Proposed Decisions for the Three Chromium
Electroplating Source Categories
A. What are the results and proposed decisions based on our
technology review?
B. What are the results of the risk assessment?
C. What are our proposed decisions regarding risk acceptability
and ample margin of safety?
D. Compliance Dates
V. What action are we proposing for the steel pickling source
category?
A. Elimination of an Alternative Compliance Option
B. Compliance Dates
VI. What other actions are we proposing?
A. Electronic Reporting
VII. Summary of Cost, Environmental, and Economic Impacts
A. What are the affected sources?
B. What are the emission reductions?
C. What are the cost impacts?
D. What are the economic impacts?
E. What are the benefits?
VIII. Request for Comments
IX. 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 Concerning Regulations That
Significantly Affect Energy Supply, Distribution, or Use
I. National Technology Transfer and Advancement Act
J. Executive Order 12898: Federal Actions To Address
Environmental Justice in Minority Populations and Low-Income
Populations
I. General Information
A. Does this action apply to me?
The regulated industrial source categories that are the subject of
this proposal are listed in Table 1 to this preamble. Table 1 is not
intended to be exhaustive, but rather provides a guide for readers
regarding entities likely to be affected by the proposed action for the
source categories listed. These standards, and any changes considered
in this rulemaking, would be directly applicable to sources as a
federal program. Thus, federal, state, local, and tribal government
entities are not affected by this proposed action. Table 1 shows the
regulated categories affected by this proposed action.
Table 1--NESHAP and Industrial Source Categories Affected by This Proposed Action
----------------------------------------------------------------------------------------------------------------
----------------------------------------------------------------------------------------------------------------
NESHAP and source category NAICS code MACT code
\1\ \2\
----------------------------------------------------------------------------------------------------------------
Chromium Electroplating NESHAP, Subpart N.... Chromium Anodizing Tanks............. 332813 1607
Decorative Chromium Electroplating... 332813 1610
Hard Chromium Electroplating......... 332813 1615
------------------------------------------------------------------------------------- -------------
Steel Pickling--HCl Process Facilities And Hydrochloric Acid Regeneration Plants 3311, 3312 0310
NESHAP, Subpart CCC
----------------------------------------------------------------------------------------------------------------
\1\ North American Industry Classification System.
\2\ Maximum Achievable Control Technology.
B. Where can I get a copy of this document and other related
information?
In addition to being available in the docket, an electronic copy of
this proposal will also be available on the World Wide Web (WWW)
through the Technology Transfer Network (TTN). Following signature by
the EPA Administrator, a copy of this proposed action 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/atw/rrisk/rtrpg.html. The TTN provides information and technology exchange in
various areas of air pollution control.
Additional information is available on the residual risk and
technology review (RTR) web page at https://www.epa.gov/ttn/atw/rrisk/rtrpg.html. This information includes source category descriptions and
detailed emissions and other data that were used as inputs to the risk
assessments.
C. What should I consider as I prepare my comments for the EPA?
Submitting CBI. Do not submit information containing CBI to the EPA
through https://www.regulations.gov or email. Clearly mark the part or
all of the information that you claim to be CBI. For CBI information on
a disk or CD-ROM that you mail to the EPA, mark the outside of the disk
or CD-ROM as CBI and then identify electronically within the disk or
CD-ROM the specific information that is claimed as CBI. In addition to
one complete version of the comment that includes information claimed
as CBI, a copy of the comment that does not contain the information
claimed as CBI must be submitted for inclusion in the public docket. If
you submit a CD-ROM or disk that does not contain CBI, mark the outside
of the disk or CD-ROM clearly that it does not contain CBI. Information
not marked as CBI will be included in the public docket and the EPA's
electronic public docket without prior notice. Information marked as
CBI will not be disclosed except in accordance with procedures set
forth in 40 CFR part 2. Send or deliver information identified as CBI
only to the following address: 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 Number EPA-HQ-OAR-2010-0600.
D. When would a public hearing occur?
If a public hearing is held, it will be held at 10:00 a.m. on
February 23, 2012 and will be held at a location to be determined.
Persons interested in presenting oral testimony at the hearing should
contact Mr. Phil Mulrine, Office of Air Quality Planning and Standards,
Sector Policies and Programs Division (D243-02), U.S. Environmental
Protection Agency, Research Triangle Park, NC 27711, telephone (919)
541-5289; fax number: (919) 541-3207; email address:
mulrine.phil@epa.gov.
[[Page 6630]]
II. Background Information
A. Overview of the Chromium Electroplating and Chromium Anodizing
Source Categories
The Chromium Electroplating NESHAP regulates emissions of chromium
compounds from three source categories: hard chromium electroplating,
decorative chromium electroplating, and chromium anodizing. The NESHAP
apply to both major sources and area sources. The NESHAP were
promulgated on January 25, 1995 (60 FR 4963) and codified at 40 CFR
part 63, subpart N. We proposed amendments to the NESHAP on June 5,
2002 (67 FR 38810) to address issues related to changes in control
technology, monitoring and implementation. The amendments were
promulgated on July 19, 2004 (69 FR 42885).
1. Hard Chromium Electroplating
The Hard Chromium Electroplating source category consists of
facilities that plate base metals with a relatively thick layer of
chromium using an electrolytic process. Hard chromium electroplating
provides a finish that is resistant to wear, abrasion, heat, and
corrosion. These facilities plate large cylinders and industrial rolls
used in construction equipment and printing presses, hydraulic
cylinders and rods, zinc die castings, plastic molds, engine
components, and marine hardware.
The NESHAP distinguishes between large hard chromium electroplating
facilities and small hard chromium electroplating facilities. Large
hard chromium electroplating facilities are defined as any such
facility with a cumulative annual rectifier capacity equal to or
greater than 60 million ampere-hours per year (amp-hr/yr). Small hard
chromium electroplating facilities are defined as any facility with a
cumulative annual rectifier capacity less than 60 million amp-hr/yr.
The NESHAP requires all affected tanks located at large hard chromium
electroplating facilities to meet an emissions limit of 0.015
milligrams per dry standard cubic meter (mg/dscm). Alternatively, large
hard chromium facilities also can comply with the NESHAP by maintaining
the surface tension limits in affected tanks equal to or less than 45
dynes per centimeter (dynes/cm), if measured using a stalagmometer, or
35 dynes/cm, if measured using a tensiometer.
The Chromium Electroplating NESHAP requires affected tanks at
existing small hard chromium electroplating facilities to meet an
emissions limit of 0.030 mg/dscm and affected tanks at new small hard
chromium electroplating facilities to meet a limit of 0.015 mg/dscm.
Alternatively, these sources have the option of complying with surface
tension limits equal to or less than 45 dynes per centimeter (dynes/
cm), if measured using a stalagmometer, or 35 dynes/cm, if measured
using a tensiometer. Under the current NESHAP, any small hard chromium
electroplating tank for which construction or reconstruction was
commenced on or before December 16, 1993 (i.e., the proposal date for
the original NESHAP) is subject to the existing source standards and
any small hard chromium electroplating tank constructed or
reconstructed after December 16, 1993 is subject to new source
standards.
We estimate that there currently are approximately 230 large hard
chromium electroplating facilities and 450 small hard chromium
electroplating facilities in operation. Of the 450 small hard chromium
electroplating facilities, we estimate that 150 of these facilities
have one or more tanks that are subject to the new source standards,
and the affected sources at the other 300 facilities are subject to the
existing source standards.
2. Decorative Chromium Electroplating
The Decorative Chromium Electroplating source category consists of
facilities that plate base materials such as brass, steel, aluminum, or
plastic with layers of copper and nickel, followed by a relatively thin
layer of chromium to provide a bright, tarnish- and wear-resistant
surface. Decorative chromium electroplating is used for items such as
automotive trim, metal furniture, bicycles, hand tools, and plumbing
fixtures. We estimate that there currently are approximately 590
decorative chromium electroplating plants in operation. The NESHAP
requires all existing and new decorative chromium electroplating
sources to meet an emissions limit of 0.01 mg/dscm, or meet the surface
tension limits of 45 dynes/cm, if measured using a stalagmometer, or 35
dynes/cm, if measured using a tensiometer.
3. Chromium Anodizing
The Chromium Anodizing source category consists of facilities that
use chromic acid to form an oxide layer on aluminum to provide
resistance to corrosion. The chromium anodizing process is used to coat
aircraft parts (such as wings and landing gears) as well as
architectural structures that are subject to high stress and corrosive
conditions. We estimate that there currently are about 180 chromium
anodizing plants in operation. The NESHAP requires all existing and new
chromium anodizing sources to meet an emissions limit of 0.01 mg/dscm,
or meet the surface tension limits of 45 dynes/cm, if measured using a
stalagmometer, or 35 dynes/cm, if measured using a tensiometer.
B. What is the history of the chromium electroplating and chromium
anodizing risk and technology reviews?
Pursuant to section 112(f)(2) of the CAA, we evaluated the residual
risk associated with the NESHAP in 2010. At that time, we also
conducted a technology review, as required by section 112(d)(6). Based
on the results of our initial residual risk and technology reviews, we
proposed on October 21, 2010 (75 FR 65071) that the risks due to HAP
emissions from these source categories were acceptable and that no
additional controls were necessary to provide an ample margin of safety
to protect public health because we had not identified additional
controls that would reduce risk at reasonable costs. Thus, we did not
propose to revise the NESHAP under 112(f)(2). However, as explained in
that proposal publication, we were concerned about the potential cancer
risks due to emissions from this category and asked for additional
information and comments on this issue.
As a result of our technology review in 2010, we proposed the
following amendments to the NESHAP to:
Incorporate several housekeeping practices into 40 CFR
63.342(f);
phase out the use of wetting agent fume suppressants
(WAFS) based on perfluorooctyl sulfonates (PFOS);
revise the startup, shutdown, and malfunction provisions
(SSM) in the rule;
revise the monitoring and testing requirements; and,
make a few technical corrections to the NESHAP.
The comment period for the October 21, 2010 proposal ended on
December 6, 2010, and we are not re-opening the comment period on those
issues. However, we will address the comments we received during the
October 21, 2010 to December 6, 2010 public comment period at the time
we take final action.
C. Overview of the Steel Pickling Source Category
Steel pickling is a treatment process in which the heavy oxide
crust or mill scale that develops on the steel surface during hot
forming or heat treating is removed chemically in a bath of aqueous
acid solution. Pickling is a process applied to metallic substances
that removes surface impurities, stains,
[[Page 6631]]
or crusts to prepare the metal for subsequent plating (e.g., with
chromium) or other treatment, such as galvanization or painting. An
acid regeneration plant is defined in the rule as the equipment and
processes that regenerate fresh hydrochloric acid pickling solution
from spent pickle liquor using a thermal treatment process. The HAP
emission points from the steel pickling process include steel pickling
baths, steel pickling sprays, and tank vents. The HAP emission point
from acid regeneration plants is the spray roaster.
We estimate that there are approximately 80 facilities subject to
the MACT standards that are currently performing steel pickling and/or
acid regeneration. Many of these facilities are located adjacent to
integrated iron and steel manufacturing plants or electric arc furnace
steelmaking facilities (minimills) that produce steel from scrap.
Facilities that regenerate HCl may or may not be located at steel
pickling operations.
D. What is the history of the steel pickling risk and technology
review?
Pursuant to section 112(f)(2) of the CAA, we evaluated the residual
risk associated with the NESHAP in 2010. We also conducted a technology
review, as required by section 112(d)(6) of the CAA. Based on the
results of our residual risk assessment, we proposed on October 21,
2010 that the risks were acceptable and that there were no additional
cost effective controls to reduce risk further and that the NESHAP
provides an ample margin of safety to protect public health and
prevented an adverse environmental effect. In that notice, we also
proposed no changes based on the technology review because we did not
identify any new, feasible technologies that warranted changes to the
NESHAP. We are not taking comment on these proposed determinations.
E. What data collection activities were conducted to support this
action?
1. Chromium Electroplating and Chromium Anodizing Source Categories
Several commenters expressed concern that the data set used in the
risk assessment that was relied on for the October 2010 proposal was
not based on actual data from an adequate number of facilities and was
not representative of the current chromium electroplating industry. In
response to these comments, we contacted 28 State and local air
pollution control agencies to request information on the industry. The
requested information included facility data (name, location, number of
employees), process type, tank design and operating parameters, annual
hours of operation, emission control technology, control device
operating parameters, emission test data, and other available
supporting documents, such as emission inventory reports and operating
permits. Agencies were asked to provide data on the 5 to 10 facilities
that were likely to have the highest risk based on either chromium
emissions or close proximity to sensitive receptors, and any additional
facilities for which the data were readily available. The agencies were
also asked to review the list of facilities we had in our Chromium
Electroplating Database and update the list to the extent that they had
more recent information on plant closings, new plants, or changes in
processes.
We received the most current data available from a total of 24
agencies. We supplemented the data provided by the agencies with
additional information we obtained from operating permits and other
information downloaded from State Web sites. We also received some data
from an industry organization (i.e., the National Association for
Surface Finishing, located in Washington, DC). The updated data set
included information on 346 plants. After eliminating redundancies in
the data and deleting data for facilities that were no longer in
operation or no longer performing chromium electroplating or anodizing,
the new data set included annual emissions for 301 plants currently in
operation. Of these, approximately 128 plants were located in
California, and 173 plants were located in other States. Finally, we
performed a quality control check of plant geographic coordinates and
updated the coordinates for approximately 400 plants, focusing on those
plants most likely to have high emissions.
We believe the current data set to be significantly better than the
data set we relied on for the 2010 proposal for a number of reasons.
The current data set provides improved emissions estimates for many
facilities, based on actual emissions test data; provides actual
emissions data for a larger number of facilities than had been modeled
for the 2010 proposal; includes an updated plant list that accounts for
facilities that have opened recently and eliminates nearly 200 plants
that have recently closed or have stopped performing chromium
electroplating; includes more plant-specific data on numbers and types
of electroplating tanks, types of emissions controls, and control
system operating parameters; and corrected geographic locations
(latitudes, longitudes) for hundreds of chromium electroplating and
anodizing facilities.
For the October 21, 2010, proposal we used the actual emissions
data available at the time, which covered far fewer plants, and, in
many cases, were based on general emission factors and other data not
specific to the plant in question. To fill in data gaps for the October
2010 proposal, we relied on plant capacity, process design, process
operating, and control device data collected during the development of
the original MACT standard in the early 1990's to develop a series of
model plants for each process (hard chromium electroplating, decorative
chromium electroplating, and chromium anodizing). We used theoretical
emissions estimates for the model plants to represent actual facilities
in operation. As we have collected much more data on actual emissions
from facilities currently in operation, we now realize that the
emission estimates based on pre-MACT data used for the October proposal
significantly overestimated emissions. In addition, we modeled all of
the unknown facilities (i.e., the facilities where we did not know the
type of plating) using the hard chromium electroplating emission factor
developed from the model plants. Since hard chromium electroplating
facilities have the highest emissions among the three source categories
this resulted in very conservative estimates of emissions for those
unknown sources.
The list of plants in our current data set much better reflects the
current status of the industry. First, it better reflects the status
because we have greatly improved the locations of several hundred
plants, which is critical in assessing risk. Second, the emissions data
in the current data set better reflect actual emissions from facilities
currently in operation because it reflects emission levels since
implementation of the NESHAP.
In addition, having more accurate data on such things as the
emission controls in use, the number of affected electroplating and
anodizing tanks, tank operating parameters, facility types, stack
parameters (such as exhaust flow rates), and other information allowed
us to better estimate current nationwide emissions and the cost and
environmental impacts associated with the control options. More details
on the data collection activities for this supplemental proposal are
provided in the technical document ``Information on Chromium
Electroplating Facilities Collected from State and Local Agencies from
January to March 2011,'' which is available in the docket for this
action.
[[Page 6632]]
Additional details on the industry data collected are provided in the
technical document ``Profile of Chromium Electroplating Processes and
Emissions,'' which is available in the docket for this action.
2. Steel Pickling Source Category
We had sufficient emissions data for this source category at the
time of the October 21, 2010 proposal for the risk analysis.
Nevertheless, subsequent to the close of the comment period, we
gathered more data and information regarding the status of facility
processes and controls, and we further evaluated the MACT rule to
determine if any updates or corrections would be appropriate.
III. Analyses Performed
A. How did we perform the technology review?
For our October 2010 proposal, we performed several activities for
purposes of evaluating developments in practices, processes, and
control technologies for the chromium electroplating source categories:
(1) We reviewed comments received on the proposed 2002 amendments to
the Chromium Electroplating NESHAP (67 FR 38810, June 5, 2002) to
determine whether they identified any developments that warranted
further consideration; (2) we reviewed the supporting documentation for
the 2007 amendments to California's Airborne Toxic Control Measure
(ATCM) for Chromium Plating and Chromium Anodizing Facilities; and (3)
we searched the RACT/BACT/LAER Clearinghouse (RBLC) and the Internet to
identify other practices, processes, or control technologies that could
be applied to chromium electroplating.
The October 21, 2010 proposal of the Chromium Electroplating NESHAP
identified four developments in practices, processes, and control
technologies that were considered for the technology review: emission
elimination devices, high efficiency particulate air (HEPA) filters,
wetting agent fume suppressants (WAFS), and housekeeping practices.
These technologies and practices are described in detail in the October
2010 proposal. Furthermore, our initial analyses, findings, and
conclusions regarding these developments are discussed in the preamble
to the October 2010 proposal. The following paragraphs describe
additional analyses that were performed for today's supplemental
proposal.
1. Emissions Limits
a. Large Hard Chromium Electroplating. Most large hard chromium
facilities currently have one or more add-on control devices such as
packed bed scrubbers (PBS), composite mesh pad (CMP) scrubbers, mesh
pad mist eliminators (MPMEs), high efficiency scrubbers, or HEPA
filters. Some facilities use add-on controls plus WAFS to limit
emissions. However, some facilities control their emissions using only
WAFS and have no add-on control device.
To evaluate how effective the emission control technologies
currently used on existing large hard chromium electroplating sources
are in reducing emissions and meeting the emissions limit, we compiled
the available data on emission concentration (mg/dscm) we collected
from the 24 State and local agencies and ranked the data from lowest to
highest. We have data from 75 tanks located at 38 facilities. We then
reviewed the data to better understand where existing sources operated
with respect to the emissions limit. That is, we looked at the number
of sources that operated at or below various emission levels, including
75 percent of the emissions limit, 50 percent of the emissions limit,
and 40 percent of the emissions limit.
The data indicate that most of these sources operate well below the
0.015 mg/dscm emissions limit. For example, approximately 88 percent of
existing sources operate at less than 75 percent of the emissions limit
(i.e., below 0.011 mg/dscm); 72 percent of sources operate at less than
50 percent of the emissions limit (i.e., below 0.0075 mg/dscm); and
about 67 percent of existing large hard chromium electroplating sources
achieve emissions below 0.006 mg/dscm. We then considered several
options for reducing the emissions and weighed the costs and emissions
reductions associated with each option. Further discussion of these
options and the proposed decisions are presented in section IV below.
For purpose of addressing new large chromium electroplating
facilities, we considered the feasibility of a more stringent emissions
limit. Specifically, we examined what emission level could be met using
available add-on control devices (such as with a CMP, MPME, or high
efficiency scrubber) or a combination of add-on controls (such as a CMP
plus a HEPA filter or an MPME plus a HEPA filter) and the emissions
concentrations that could be achieved by using a combination of add-on
control technology and WAFS. The results of this analysis and the
proposed decisions are described in section IV below.
b. Small Hard Chromium Electroplating. For small hard chromium
electroplating facilities, we performed the same type of analyses
described in the previous section for large hard chromium
electroplating. In terms of emissions limits, the NESHAP distinguishes
between existing facilities, which are subject to an emissions limit of
0.030 mg/dscm, and new facilities, which are subject to an emissions
limit of 0.015 mg/dscm. We compiled and ranked the available data,
which also indicate that the large majority of sources operate well
below the current emissions limits. We have data on emissions
concentrations for 73 tanks at 56 facilities located in States other
than California which were used for this ranking. We estimate that
there are a total of 414 small hard chromium plants located in States
other than California. We estimate that there are a total of 450 plants
nationwide, with about 36 plants located in California. We considered
different options for reducing the emissions limits. We also considered
removing the existing distinction between existing and new, as they are
currently defined in the NESHAP, because many of the ``new'' facilities
have been in operation for more than 17 years and we were considering
proposing a more stringent new source standard for all sources. We
evaluated the impacts, in terms of costs and emissions reductions, that
would result for various potential proposed emissions limits at or
below 0.015 mg/dscm. We did not evaluate potential limits greater than
0.015 mg/dscm since about one-third of the currently operating small
hard chromium sources are already subject to an emissions limit of
0.015 mg/dscm. Specifically, we considered two main options: (1)
Propose that all small hard chromium electroplating facilities
currently in operation meet an emissions limit of 0.015 mg/dscm, and
(2) propose that all small hard chromium electroplating facilities
currently in operation meet an emissions limit of 0.010 mg/dscm. The
results of this analysis and the proposed decisions are described in
section IV below.
We also considered revising the definition of new small hard
chromium electroplating facilities, based on the proposal date for this
action, and requiring those facilities to meet a more stringent
emissions limit. The results of this analysis and the proposed
decisions are described in section IV below.
c. Decorative Chromium Electroplating. For decorative chromium
electroplating, we intended to perform
[[Page 6633]]
analyses similar to that performed for hard chromium electroplating.
However, the data set for decorative chromium electroplating was much
smaller (e.g., 20 data points for decorative chromium electroplating
vs. 75 data points for large hard chromium), and we did not think the
data were adequate for considering several different emissions
reductions options. The primary reason for the smaller data set is that
the most commonly used method for controlling emissions from decorative
chromium electroplating is adding WAFS to the electroplating tank bath.
Since sources that use WAFS and comply with the surface tension limits
are not required to conduct an emission test, there are limited test
data available.
However, we did rank the available data on existing sources in the
decorative chromium electroplating source category by emissions level
to determine the typical level of emissions performance and range of
performance among those sources to determine options for revising these
limits. All the facilities for which we have data have emissions
concentrations less than 0.007 mg/dscm (i.e., at least 30 percent below
the applicable emissions limit of 0.010 mg/dscm). Further discussion of
this analysis and the proposed decisions for existing and new
decorative chromium electroplating sources are presented in section IV
below.
d. Chromium Anodizing. In the case of chromium anodizing, we had
only a single data point (0.0016 mg/dscm), which is significantly below
the current emissions limit of 0.010 mg/dscm. However, we concluded
that the data on decorative chromium electroplating was relevant to
determining the feasible options for chromium anodizing. For one, many
chromium anodizing sources (approximately 50 percent) are controlled
using only WAFS. It was for this reason that the current NESHAP
specifies the same emissions limits of 0.010 mg/dscm for both chromium
anodizing and decorative chromium electroplating sources. In addition,
chromium anodizing plants are comparable to decorative chromium
electroplating plants with respect to the relative magnitude of
chromium emissions. Finally, the feasibility and options for
controlling emissions from chromium anodizing are similar to those for
decorative chromium. Further discussion of this analysis and the
proposed decisions for existing and new chromium anodizing sources are
presented in section IV below.
2. Surface Tension Limits
The NESHAP provides that affected sources must either meet an
emissions limit specified in the NESHAP or must maintain the surface
tension in chromium electroplating or chromium anodizing tanks below
one of two specified surface tension limits, depending on the type of
instrument used to measure surface tension. Despite the fact that the
emissions limits for the three chromium electroplating source
categories differ, the surface tension limits in the current NESHAP are
the same for all three source categories and are the same for existing
and new sources, as follows: if a stalagmometer is used to measure
surface tension, the surface tension limit is 45 dynes/cm, and, if a
tensiometer is used, the surface tension limit is 35 dynes/cm. The
available data, which are described in detail in the technical document
``Development of Revised Surface Tension Limits for Chromium
Electroplating and Anodizing Tanks Controlled with Wetting Agent Fume
Suppressants,'' which is available in the docket, indicate that
maintaining the surface tension below these limits ensures that
emissions are below 0.01 mg/dscm, which is the most stringent limit
currently in the NESHAP.
As part of the information collection described in section II.E of
this preamble, we obtained test data for several decorative and hard
chromium electroplating sources controlled using only WAFS. These data
on surface tension and emission concentration were evaluated to
determine the relationship between emissions and surface tension. We
analyzed these data to evaluate the feasibility of requiring lower
surface tension limits and the corresponding emissions levels. Further
details of this analysis and the results, and the proposed decisions
based on this analysis, are presented below in section IV.A.
B. For purposes of this supplemental proposal, how did we estimate the
risk posed by each of the three chromium electroplating source
categories?
The EPA conducted a risk assessment that provided estimates of the
maximum individual risk (MIR) posed by HAP emissions from sources in
the source category and the hazard index (HI) for chronic exposures to
HAP with the potential to cause noncancer health effects. The
assessment also provided estimates of the distribution of cancer risks
within the exposed populations, cancer incidence, and an evaluation of
the potential for adverse environmental effects for each source
category. The docket for this rulemaking contains the following
document which provides more information on the risk assessment inputs
and models: Residual Risk Assessment for the Chromic Acid Anodizing,
Decorative Chromium Electroplating, and Hard Chromium Electroplating
Source Categories. The methods used to assess risks are consistent with
those peer-reviewed by a panel of the EPA's Science Advisory Board
(SAB) in 2009 and described in their peer review report issued in 2010
\1\; they are also consistent with the key recommendations contained in
that report.
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\1\ U.S. EPA SAB. Risk and Technology Review (RTR) Risk
Assessment Methodologies: For Review by the EPA's Science Advisory
Board with Case Studies--MACT I Petroleum Refining Sources and
Portland Cement Manufacturing, May 2010.
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1. Estimating Actual Emissions
As explained previously, the revised data set for the Chromium
Electroplating NESHAP source categories includes significantly improved
emissions data for many more plants than the data set used for the
October 2010 proposal. However, to assess nationwide residual risk, it
was still necessary to estimate emissions for much of the industry.
Rather than estimate those emissions using the model plant approach
used for the October 2010 proposal, we used a Monte Carlo procedure to
simulate actual emissions for those plants for which actual emissions
data were not available. The simulation model used the pool of
available data on actual emissions concentrations, exhaust flow rates,
and annual operating hours for each process type (hard chromium
electroplating, decorative chromium electroplating, and chromium
anodizing). Actual emissions data (lbs/yr) were fitted to a Weibull
distribution and emissions for plants for which emissions were unknown
were simulated using the actual data for each plant type. Because
process-specific data were used to simulate emissions for each
facility, it was necessary to identify the process type for each of the
plants. Although the process type was known for many plants, it was
unknown for a large number of other plants. By scaling up the data on
known plants, and using other available data on the industry, the
profile of the current chromium electroplating industry was estimated
in terms of the number of each type of plant.
One of the primary goals in simulating actual annual emissions was
to develop a data set of emissions estimates that best represents
chromium electroplating plants operating in the U.S. For this reason, a
distinction was made between chromium electroplating plants located in
California and plants located elsewhere (i.e., the non-
[[Page 6634]]
California plants). Because chromium electroplating plants located in
California are subject to emissions limits that are significantly more
stringent than the limits specified in the NESHAP, they typically use
multiple emissions controls, including HEPA filters in many cases, to
reduce emissions. Thus, emissions for California plants are not
representative of emissions for non-California plants. For this reason,
the data on California plants were not included in the data set used to
simulate emissions for plants located in other States. However, the
data on actual emissions from plants located in California were used to
estimate emissions for other plants in California. Thus, we did not
exclude the California data from the overall analysis; we treated the
data from plants in California differently. (Additional details on the
emissions data for the California plants are provided below.) Based on
the total numbers of plants nationwide, plant types were randomly
assigned to each of the unknown plants, while ensuring that the total
numbers of each type of plants nationwide were preserved. After
assigning plant types, emissions for each plant was simulated 5,000
times using only the data for that specific type of plant (e.g., only
data for small hard chromium electroplating plants were used to
simulate emissions for a small hard chromium electroplating plant).
Once all 5,000 simulations were completed, the mean of the simulated
values for each plant was determined and that value was used to
populate the risk modeling file on actual emissions.
Taking into account all of the new emissions data collected
following the public comment period for the October 2010 proposal, plus
the good quality emissions data collected previously, the data set
included emissions estimates for a total of 301 plants. Of these,
approximately 128 plants were located in California, and 173 plants
were located in other States. A review of the data indicated that
emissions for the California plants were significantly lower than
emissions for the non-California plants. For example, emissions from
the large hard chromium electroplating plants in California averaged
0.027 lbs/yr, whereas the average for the non-California large hard
chromium plants was 2.62 lbs/yr. For small hard chromium
electroplating, the California plants averaged 0.0095 lbs/yr and the
non-California plants averaged 0.56 lbs/yr. For decorative chromium
electroplating, the average emissions were 0.00042 lbs/yr (California)
and 0.55 lbs/yr (non-California). For chromium anodizing, the average
emissions were 0.00035 lbs/yr (California) and 0.46 lbs/yr (non-
California). These results clearly indicated that the data for plants
in California were not representative of plants located outside of
California. For this reason, all subsequent analyses related to
estimating emissions for plants located outside of California were
performed using only data for non-California plants.
For the California plants we used the emissions estimates as
reported. For all the plants outside of California, we used actual
emissions estimates if they were available. For the other plants we
used the simulation model described above to estimate emissions.
Overall, we believe that the resulting emissions simulated by the
model are much more representative of actual emissions on average and
also are more representative of the variability of emissions from plant
to plant. Additional details on the simulation approach can be found in
the emissions technical document ``Simulation of Actual and Allowable
Emissions for Chromium Electroplating Facilities,'' which is available
in the docket for this rulemaking.
2. Estimating MACT-Allowable Emissions
To estimate allowable annual emissions (e.g., lbs/yr) for those
plants for which actual emissions concentration data were available, we
calculated the allowable annual emissions using the MACT emissions
limit. In other words, we scaled up actual annual emissions for those
plants using the ratio of the emissions concentration (measured during
the performance test) to the MACT limit. For example, if the measured
concentration for a large hard chromium plant was 0.0075 mg/dscm, which
is one-half of the 0.015 mg/dscm emissions limit, we scaled up annual
emissions by a factor or 2. For those plants for which we did not have
actual emissions data, we used the same emissions simulation approach
used to estimate actual emissions, as described previously. That is,
data for California plants were excluded from the analysis; process
types were assigned to each plant for which the process was unknown,
while ensuring that the total number of each type of plant matched the
estimated numbers of plants nationwide; and a Monte Carlo simulation
model was developed using the pool of available data on emissions
concentrations, exhaust flow rates, and annual operating hours for each
process type to simulate allowable emissions for each plant. However,
instead of using the actual emissions concentration data in the
simulation model, we used the corresponding MACT emissions limit. Thus,
we calculated the allowable emissions by using the pool of available
data on exhaust flow rates and annual operating hours for each process
type and assumed each source had emissions concentrations equal to the
MACT emissions limit (i.e., we assumed they were emitting at the
maximum level allowed by the MACT standard). For example, to estimate
the allowable emissions for a large hard chromium electroplating plant,
data on large hard chromium plant exhaust flow rates and annual
operating hours were used, along with an emissions concentration of
0.015 mg/dscm, which is the emissions limit specified in the NESHAP for
large hard chromium electroplating plants. As was used for calculating
actual emissions estimates, 5,000 simulations were performed for each
plant, and the average of simulated values was used to represent
allowable emissions for the plant. Additional details on the simulation
approach can be found in the emissions technical document ``Simulation
of Actual and Allowable Emissions for Chromium Electroplating
Facilities,'' which is available in the docket for this rulemaking.
3. Conducting Dispersion Modeling, Determining Inhalation Exposures,
and Estimating Individual and Population Inhalation Risks
Both long-term and short-term inhalation exposure concentrations
and health risks from the three chromium electroplating source
categories were estimated using the Human Exposure Model (HEM-3). The
HEM-3 performs three of the primary risk assessment activities listed
above: (1) Conducting dispersion modeling to estimate the
concentrations of HAP in ambient air, (2) estimating long-term and
short-term inhalation exposures to individuals residing within 50
kilometers (km) of the modeled sources, and (3) estimating individual
and population-level inhalation risks using the exposure estimates and
quantitative dose-response information.
The air dispersion model used by the HEM-3 model (AERMOD) is one of
the EPA's preferred models for assessing pollutant concentrations from
industrial facilities.\2\ To perform the dispersion modeling and to
develop the preliminary risk estimates, HEM-3
[[Page 6635]]
draws on three data libraries. The first is a library of meteorological
data, which is used for dispersion calculations. This library includes
1 year of hourly surface and upper air observations for approximately
200 meteorological stations, selected to provide coverage of the United
States and Puerto Rico. A second library, of United States Census
Bureau census block \3\ internal point locations and populations,
provides the basis of human exposure calculations (Census, 2010). In
addition, for each census block, the census library includes the
elevation and controlling hill height, which are also used in
dispersion calculations. A third library of pollutant unit risk factors
and other health benchmarks is used to estimate health risks. These
risk factors and health benchmarks are the latest values recommended by
the EPA for HAP and other toxic air pollutants. These values are
available at https://www.epa.gov/ttn/atw/toxsource/summary.html and are
discussed in more detail later in this section.
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\2\ U.S. EPA. Revision to the Guideline on Air Quality Models:
Adoption of a Preferred General Purpose (Flat and Complex Terrain)
Dispersion Model and Other Revisions (70 FR 68218, November 9,
2005).
\3\ A census block is the smallest geographic area for which
census statistics are tabulated.
---------------------------------------------------------------------------
In developing the risk assessment for chronic exposures, we used
the estimated annual average ambient air concentrations of chromium
emitted by each source. The air concentrations at each nearby census
block centroid were used as a surrogate for the chronic inhalation
exposure concentration for all the people who reside in that census
block. We calculated the MIR for each facility as the cancer risk
associated with a continuous lifetime (24 hours per day, 7 days per
week, and 52 weeks per year for a 70-year period) exposure to the
maximum concentration at the centroid of inhabited census blocks.
Individual cancer risks were calculated by multiplying the estimated
lifetime exposure to the ambient concentration of chromium (in
micrograms per cubic meter ([mu]g/m\3\)) by its unit risk estimate
(URE), which is an upper bound estimate of an individual's probability
of contracting cancer over a lifetime of exposure to a concentration of
1 microgram of the pollutant per cubic meter of air. For residual risk
assessments, we generally use URE values from the EPA's Integrated Risk
Information System (IRIS). For carcinogenic pollutants without the EPA
IRIS values, we look to other reputable sources of cancer dose-response
values, often using California EPA (CalEPA) URE values, where
available. In cases where new, scientifically credible dose response
values have been developed in a manner consistent with the EPA
guidelines and have undergone a peer review process similar to that
used by the EPA, we may use such dose-response values in place of, or
in addition to, other values, if appropriate.
Incremental individual lifetime cancer risks were estimated as the
sum of the risks for each of the carcinogenic HAP (including those
classified as carcinogenic to humans, likely to be carcinogenic to
humans, and suggestive evidence of carcinogenic potential \4\) emitted
by the modeled source. Cancer incidence and the distribution of
individual cancer risks for the population within 50 km of the sources
were also estimated for the source category as part of this assessment
by summing individual risks. A distance of 50 km is consistent with
both the analysis supporting the 1989 Benzene NESHAP (54 FR 38044) and
the limitations of Gaussian dispersion models, including AERMOD.
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\4\ These classifications also coincide with the terms ``known
carcinogen, probable carcinogen, and possible carcinogen,''
respectively, which are the terms advocated in the EPA's previous
Guidelines for Carcinogen Risk Assessment, published in 1986 (51 FR
33992, September 24, 1986). Summing the risks of these individual
compounds to obtain the cumulative cancer risks is an approach that
was recommended by the EPA's Science Advisory Board (SAB) in their
2002 peer review of EPA's National Air Toxics Assessment (NATA)
entitled, NATA--Evaluating the National-scale Air Toxics Assessment
1996 Data--an SAB Advisory, available at: https://yosemite.epa.gov/
sab/sabproduct.nsf/214C6E915BB04E14852570CA007A682C/$File/
ecadv02001.pdf.
---------------------------------------------------------------------------
To assess the risk of non-cancer health effects from chronic
exposures, we summed the HQ for each of the HAP that affects a common
target organ system to obtain the HI for that target organ system (or
target organ-specific HI, TOSHI). The HQ is the estimated exposure
divided by the chronic reference value, which is either the EPA
reference concentration (RfC), defined as ``an estimate (with
uncertainty spanning perhaps an order of magnitude) of a continuous
inhalation exposure to the human population (including sensitive
subgroups) that is likely to be without an appreciable risk of
deleterious effects during a lifetime,'' or, in cases where an RfC from
the EPA's IRIS database is not available, the EPA will utilize the
following prioritized sources for our chronic dose-response values: (1)
The Agency for Toxic Substances and Disease Registry Minimum Risk
Level, which is defined as ``an estimate of daily human exposure to a
substance that is likely to be without an appreciable risk of adverse
effects (other than cancer) over a specified duration of exposure'';
(2) the CalEPA Chronic Reference Exposure Level (REL), which is defined
as ``the concentration level at or below which no adverse health
effects are anticipated for a specified exposure duration''; and (3),
as noted above, in cases where scientifically credible dose-response
values have been developed in a manner consistent with the EPA
guidelines and have undergone a peer review process similar to that
used by the EPA, we may use those dose-response values in place of or
in concert with other values.
4. Conducting Multipathway Exposure and Risk Screening
As explained in the October 2010 proposal, chromium electroplating
facilities do not emit any of the 14 PB-HAP compounds or compound
classes identified for the multipathway screening in the EPA's Air
Toxics Risk Assessment Library (available at https://www.epa.gov/ttn/fera/risk_atra_vol1.html). Because none of these PB-HAP are emitted
by sources in the chromium electroplating source categories, we
concluded at the time of the proposal that there is low potential for
significant non-inhalation human or environmental risks for these
source categories. The data we received since proposal continues to
indicate that chromium electroplating sources do not emit any of those
14 PB-HAP compounds or compound classes.
5. Conducting Other Analyses: Facility-Wide Risk Assessments and
Demographic Analyses
a. Facility-Wide Risk
To put the source category risks in context, we examined the risks
from the entire ``facility,'' where the facility includes all HAP-
emitting operations within a contiguous area and under common control.
In other words, for each facility that includes one or more sources
from a source category under review, we examined the HAP emissions not
only from that source category, but also emissions of HAP from all
other emission sources at the facility. The emissions data for
generating these ``facility-wide'' risks were obtained from the 2005
NEI. We analyzed risks due to the inhalation of HAP that are emitted
``facility-wide'' for the populations residing within 50 km of each
facility, consistent with the methods used for the source category
analysis described above. For these facility-wide risk analyses, the
modeled source category risks were compared to the facility-wide risks
to determine the portion of facility-wide risks that could be
attributed to each of the three chromium electroplating source
categories. We specifically examined the facility that was associated
with the
[[Page 6636]]
highest estimate of risk and determined the percentage of that risk
attributable to the source category of interest. The risk documentation
available through the docket for this action provides all facility-wide
risks and the percentage of source category contribution for the three
chromium electroplating source categories.
The methodology and results of the facility-wide analyses for each
source category are included in the residual risk documentation as
referenced in section IV of this preamble, which is available in the
docket for this action.
b. Demographic Analysis
To examine the potential for any environmental justice (EJ) issues
that might be associated with these source categories, we performed
demographic analyses of the at-risk populations for two of the three
chromium electroplating categories. We performed these analyses for
only these two source categories because the chromium anodizing source
category is not associated with significant populations with estimated
cancer risks above 1 in a million. For the hard and decorative chromium
electroplating source categories, we evaluated the percentages of
different social, demographic and economic groups within the
populations living near the facilities who were estimated to be
subjected to cancer risks greater than 1 in a million due to HAP
emissions from chromium electroplating. We compared the percentages of
these demographic groups to the total percentages of those demographic
groups nationwide. The methodology and results of the demographic
analyses are included in the technical reports: ``Risk and Technology
Review--Analysis of Socio-Economic Factors for Populations Living Near
Hard Chromium Electroplating Facilities''; and ``Risk and Technology
Review--Analysis of Socio-Economic Factors for Populations Living Near
Decorative Chromium Electroplating Facilities.'' These reports are
available in the docket for this action.
6. Considering Uncertainties in Risk Assessment
Uncertainty and the potential for bias are inherent in all risk
assessments, including those performed for the source category
addressed in this supplemental proposal. Although uncertainty exists,
we believe that our approach, which used conservative tools and
assumptions, ensures that our decisions are health-protective. A brief
discussion of the uncertainties in the emissions data set, dispersion
modeling, inhalation exposure estimates and dose-response relationships
follows below. A more thorough discussion of these uncertainties is
included in the risk assessment documentation available in the docket
for this action.
a. Uncertainties in the Emissions Data Set
Although the development of the RTR data sets involved quality
assurance/quality control processes, the accuracy of emissions values
will vary depending on the source of the data, the degree to which data
are incomplete or missing, the degree to which assumptions made to
complete the data sets are inaccurate, errors in estimating emissions
values, and other factors.
The emission estimates considered in this analysis generally are
annual totals for certain years that do not reflect short-term
fluctuations during the course of a year or variations from year to
year. Additionally, although we believe that we have good data for
hundreds of facilities in these source categories in our RTR data set,
our data set does not include data for many other existing facilities.
To simulate emissions estimates for plants for which we did not
have actual emissions estimates, separate data sets were compiled for
each process type: large hard chromium electroplating, small hard
chromium electroplating, decorative chromium electroplating, and
chromium anodizing. The data sets included combinations of actual data
on emissions concentrations, exhaust flow rates, annual o