(a)(1) At all times, each owner or operator must operate and maintain any affected source subject to the requirements of this subpart, including associated air pollution control equipment and monitoring equipment, in a manner consistent with safety and good air pollution control practices for minimizing emissions. The general duty to minimize emissions does not require the owner or operator to make any further efforts to reduce emissions if levels required by this standard have been achieved. Determination of whether such operation and maintenance procedures are being used will be based on information available to the Administrator which may include, but is not limited to, monitoring results, review of operation and maintenance procedures, review of operation and maintenance records, and inspection of the source.
(1) At all times, each owner or operator must operate and maintain any affected source subject to the requirements of this subpart, including associated air pollution control equipment and monitoring equipment, in a manner consistent with safety and good air pollution control practices for minimizing emissions. The general duty to minimize emissions does not require the owner or operator to make any further efforts to reduce emissions if levels required by this standard have been achieved. Determination of whether such operation and maintenance procedures are being used will be based on information available to the Administrator which may include, but is not limited to, monitoring results, review of operation and maintenance procedures, review of operation and maintenance records, and inspection of the source.
(2) Each owner or operator of an affected source subject to the provisions of this subpart shall comply with these requirements in this section on and after the compliance dates specified in Sec. 63.343(a). All affected sources are regulated by applying maximum achievable control technology.
(b) Applicability of emission limitations. (1) The emission limitations in this section apply during tank operation as defined in Sec. 63.341, and during periods of startup and shutdown as these are routine occurrences for affected sources subject to this subpart. In response to an action to enforce the standards set forth in this subpart, the owner or operator may assert a defense to a claim for civil penalties for violations of such standards that are caused by a malfunction, as defined in 40 CFR 63.2. Appropriate penalties may be assessed, however, if the owner or operator fails to meet the burden of proving all the requirements in the affirmative defense. The affirmative defense shall not be available for claims for injunctive relief.
(1) The emission limitations in this section apply during tank operation as defined in Sec. 63.341, and during periods of startup and shutdown as these are routine occurrences for affected sources subject to this subpart. In response to an action to enforce the standards set forth in this subpart, the owner or operator may assert a defense to a claim for civil penalties for violations of such standards that are caused by a malfunction, as defined in 40 CFR 63.2. Appropriate penalties may be assessed, however, if the owner or operator fails to meet the burden of proving all the requirements in the affirmative defense. The affirmative defense shall not be available for claims for injunctive relief.
(i) To establish the affirmative defense in any action to enforce such a standard, the owner or operator must timely meet the reporting requirements of paragraph (b)(1)(ii) of this section, and must prove by a preponderance of evidence that:
(A) The violation was caused by a sudden, infrequent, and unavoidable failure of air pollution control equipment, process equipment, or a process to operate in a normal and usual manner; and could not have been prevented through careful planning, proper design or better operation and maintenance practices; and did not stem from any activity or event that could have been foreseen and avoided, or planned for; and was not part of a recurring pattern indicative of inadequate design, operation, or maintenance; and
(B) Repairs were made as expeditiously as possible when exceeded violation occurred. Off-shift and overtime labor were used, to the extent practicable to make these repairs; and
(C) The frequency, amount and duration of the violation (including any bypass) were minimized to the maximum extent practicable; and
(D) If the violation resulted from a bypass of control equipment or a process, then the bypass was unavoidable to prevent loss of life, personal injury, or severe property damage; and
(E) All possible steps were taken to minimize the impact of the violation on ambient air quality, the environment, and human health; and
(F) All emissions monitoring and control systems were kept in operation if at all possible, consistent with safety and good air pollution control practices; and
(G) All of the actions in response to the violation were documented by properly signed, contemporaneous operating logs; and
(H) At all times, the affected sources were operated in a manner consistent with good practices for minimizing emissions; and
(I) A written root cause analysis was prepared, the purpose of which is to determine, correct, and eliminate the primary causes of the malfunction and the excess emissions resulting from the malfunction event at issue. The analysis shall also specify, using the best monitoring methods and engineering judgment, the amount of excess emissions that were the result of the malfunction.
(ii) Report. The owner or operator seeking to assert an affirmative defense shall submit a written report to the Administrator with all necessary supporting documentation, that it has met the requirements set forth in paragraph (i) of this section. This affirmative defense report shall be included in the first periodic compliance, deviation report or excess emission report otherwise required after the initial occurrence of the violation of the relevant standard (which may be the end of any applicable averaging period). If such compliance, deviation report or excess emission report is due less than 45 days after the initial occurrence of the violation, the affirmation defense report may be included in the second compliance, deviation report or excess emission report due after the initial occurrence of the violation of the relevant standard.
(2) If an owner or operator is controlling a group of tanks with a common add-on air pollution control device, the emission limitations of paragraphs (c), (d), and (e) of this section apply whenever any one affected source is operated. The emission limitation that applies to the group of affected sources is:
(i) The emission limitation identified in paragraphs (c), (d), and (e) of this section if the affected sources are performing the same type of operation (e.g., hard chromium electroplating), are subject to the same emission limitation, and are not controlled by an add-on air pollution control device also controlling nonaffected sources;
(ii) The emission limitation calculated according to Sec. 63.344(e)(3) if affected sources are performing the same type of operation, are subject to the same emission limitation, and are controlled with an add-on air pollution control device that is also controlling nonaffected sources; and
(iii) The emission limitation calculated according to Sec. 63.344(e)(4) if affected sources are performing different types of operations, or affected sources are performing the same operations but subject to different emission limitations, and are controlled with an add-on air pollution control device that may also be controlling emissions from nonaffected sources.
(c)(1) Standards for open surface hard chromium electroplating tanks. During tank operation, 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) Standards for open surface hard chromium electroplating tanks. During tank operation, 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:
(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 x 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 exceed 0.015 mg/dscm (6.6 x 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 x 10-3 pound-force per foot (lbf/ft)), as measured by a stalagmometer, or 33 dynes/cm (2.3 x 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 x 10-6 gr/dscf) for all open surface hard chromium electroplating tanks that are new affected sources; or
(v) After September 21, 2015, the owner or operator of an affected open surface hard chromium electroplating tank shall not add PFOS-based fume suppressants to any affected open surface hard chromium electroplating tank.
(2) Standards for enclosed hard chromium electroplating tanks. During tank operation, 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:
(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 x 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 x 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 x 10-3 lbf/ft), as measured by a stalagmometer, or 33 dynes/cm (2.3 x 10-3 lbf/ft), as measured by a tensiometer at any time during tank operation; or
(iv) Not allowing the mass rate of total chromium in the exhaust gas stream discharged to the atmosphere to exceed the maximum allowable mass emission rate determined by using the calculation procedure in Sec. 63.344(f)(1)(i) for all enclosed hard chromium electroplating tanks that are existing affected sources and are located at large hard chromium electroplating facilities; or
(v) Not allowing the mass rate of total chromium in the exhaust gas stream discharged to the atmosphere to exceed the maximum allowable mass emission rate determined by using the calculation procedure in Sec. 63.344(f)(1)(ii) if the enclosed hard chromium electroplating tank is an existing affected source and is located at a small, hard chromium electroplating facility.
(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 x 10-6 gr/dscf) for all enclosed hard chromium electroplating tanks that are new affected sources; or
(vii) Not allowing the mass rate of total chromium in the exhaust gas stream discharged to the atmosphere to exceed the maximum allowable mass emission rate determined by using the calculation procedure in Sec. 63.344(f)(1)(iii) if the enclosed hard chromium electroplating tank is a new affected source.
(viii) After September 21, 2015, the owner or operator of an affected enclosed hard chromium electroplating tank shall not add PFOS-based fume suppressants to any affected enclosed hard chromium electroplating tank.
(3)(i) An owner or operator may demonstrate the size of a hard chromium electroplating facility through the definitions in Sec. 63.341(a). Alternatively, an owner or operator of a facility with a maximum cumulative potential rectifier capacity of 60 million amp-hr/yr or more may be considered small if the actual cumulative rectifier capacity is less than 60 million amp-hr/yr as demonstrated using the following procedures:
(i) An owner or operator may demonstrate the size of a hard chromium electroplating facility through the definitions in Sec. 63.341(a). Alternatively, an owner or operator of a facility with a maximum cumulative potential rectifier capacity of 60 million amp-hr/yr or more may be considered small if the actual cumulative rectifier capacity is less than 60 million amp-hr/yr as demonstrated using the following procedures:
(A) If records show that the facility's previous annual actual rectifier capacity was less than 60 million amp-hr/yr, by using nonresettable ampere-hr meters and keeping monthly records of actual ampere-hr usage for each 12-month rolling period following the compliance date in accordance with Sec. 63.346(b)(12). The actual cumulative rectifier capacity for the previous 12-month rolling period shall be tabulated monthly by adding the capacity for the current month to the capacities for the previous 11 months; or
(B) By accepting a federally-enforceable limit on the maximum cumulative potential rectifier capacity of a hard chromium electroplating facility and by maintaining monthly records in accordance with Sec. 63.346(b)(12) to demonstrate that the limit has not been exceeded. The actual cumulative rectifier capacity for the previous 12-month rolling period shall be tabulated monthly by adding the capacity for the current month to the capacities for the previous 11 months.
(ii) Once the monthly records required to be kept by Sec. 63.346(b)(12) and by this paragraph (c)(3)(ii) show that the actual cumulative rectifier capacity over the previous 12-month rolling period corresponds to the large designation, the owner or operator is subject to the emission limitation identified in paragraph (c)(1)(i), (iii), (c)(2)(i), (iii), or (iv) of this section, in accordance with the compliance schedule of Sec. 63.343(a)(5).
(d) Standards for decorative chromium electroplating tanks using a chromic acid bath and chromium anodizing tanks. During tank operation, 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 x 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 (2.6x10-6 gr/dscf) for all new or reconstructed decorative chromium electroplating tanks using a chromic acid bath and all new or reconstructed chromium anodizing tanks; or
(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 x 10-3 lbf/ft), as measured by a stalagmometer or 33 dynes/cm (2.3 x 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; or
(4) After September 21, 2015, the owner or operator of an affected decorative chromium electroplating tank or an affected chromium anodizing tank shall not add PFOS-based fume suppressants to any affected decorative chromium electroplating tank or chromium anodizing tank.
(e) Standards for decorative chromium electroplating tanks using a trivalent chromium bath. (1) Each owner or operator of an existing, new, or reconstructed decorative chromium electroplating tank that uses a trivalent chromium bath that incorporates a wetting agent as a bath ingredient is subject to the recordkeeping and reporting requirements of Secs. 63.346(b)(14) and 63.347(i), but are not subject to the work practice requirements of paragraph (f) of this section, or the continuous compliance monitoring requirements in Sec. 63.343(c). The wetting agent must be an ingredient in the trivalent chromium bath components purchased as a package.
(1) Each owner or operator of an existing, new, or reconstructed decorative chromium electroplating tank that uses a trivalent chromium bath that incorporates a wetting agent as a bath ingredient is subject to the recordkeeping and reporting requirements of Secs. 63.346(b)(14) and 63.347(i), but are not subject to the work practice requirements of paragraph (f) of this section, or the continuous compliance monitoring requirements in Sec. 63.343(c). The wetting agent must be an ingredient in the trivalent chromium bath components purchased as a package.
(2) After September 21, 2015, the owner or operator of an affected decorative chromium electroplating tank using a trivalent chromium bath shall not add PFOS-based fume suppressants to any affected decorative chromium electroplating tank.
(3) Each owner or operator of an existing, new, or reconstructed decorative chromium electroplating tank that uses a trivalent chromium bath that does not incorporate a wetting agent as a bath ingredient is subject to the standards of paragraph (d) of this section.
(4) Each owner or operator of an existing, new, or reconstructed decorative chromium electroplating tank that had been using a trivalent chromium bath that incorporated a wetting agent and ceases using this type of bath must fulfill the reporting requirements of Sec. 63.347(i)(3) and comply with the applicable emission limitation within the timeframe specified in Sec. 63.343(a)(7).
(f) Operation and maintenance practices. All owners or operators subject to the standards in paragraphs (c) and (d) of this section are subject to these operation and maintenance practices.
(1)(i) At all times, including periods of startup, shutdown, and malfunction, owners or operators shall operate and maintain any affected source, including associated air pollution control devices and monitoring equipment, in a manner consistent with good air pollution control practices.
(i) At all times, including periods of startup, shutdown, and malfunction, owners or operators shall operate and maintain any affected source, including associated air pollution control devices and monitoring equipment, in a manner consistent with good air pollution control practices.
(ii) Malfunctions shall be corrected as soon as practicable after their occurrence.
(iii) Operation and maintenance requirements established pursuant to section 112 of the Act are enforceable independent of emissions limitations or other requirements in relevant standards.
(2)(i) Determination of whether acceptable operation and maintenance procedures are being used will be based on information available to the Administrator, which may include, but is not limited to, monitoring results; review of the operation and maintenance plan, procedures, and records; and inspection of the source.
(i) Determination of whether acceptable operation and maintenance procedures are being used will be based on information available to the Administrator, which may include, but is not limited to, monitoring results; review of the operation and maintenance plan, procedures, and records; and inspection of the source.
(ii) Based on the results of a determination made under paragraph (f)(2)(i) of this section, the Administrator may require that an owner or operator of an affected source make changes to the operation and maintenance plan required by paragraph (f)(3) of this section for that source. Revisions may be required if the Administrator finds that the plan:
(A) Does not address a malfunction that has occurred;
(B) Fails to provide for the proper operation of the affected source, the air pollution control techniques, or the control system and process monitoring equipment during a malfunction in a manner consistent with good air pollution control practices; or
(C) Does not provide adequate procedures for correcting malfunctioning process equipment, air pollution control techniques, or monitoring equipment as quickly as practicable.
(3) Operation and maintenance plan. (i) The owner or operator of an affected source subject to paragraph (f) of this section shall prepare an operation and maintenance plan no later than the compliance date, except for hard chromium electroplaters and the chromium anodizing operations in California which have until January 25, 1998. The plan shall be incorporated by reference into the source's title V permit, if and when a title V permit is required. The plan shall include the following elements:
(i) The owner or operator of an affected source subject to paragraph (f) of this section shall prepare an operation and maintenance plan no later than the compliance date, except for hard chromium electroplaters and the chromium anodizing operations in California which have until January 25, 1998. The plan shall be incorporated by reference into the source's title V permit, if and when a title V permit is required. The plan shall include the following elements:
(A) The plan shall specify the operation and maintenance criteria for the affected source, the add-on air pollution control device (if such a device is used to comply with the emission limits), and the process and control system monitoring equipment, and shall include a standardized checklist to document the operation and maintenance of this equipment;
(B) For sources using an add-on control device or monitoring equipment to comply with this subpart, the plan shall incorporate the operation and maintenance practices for that device or monitoring equipment, as identified in Table 1 of this section, if the specific equipment used is identified in Table 1 of this section;
(C) If the specific equipment used is not identified in Table 1 of this section, the plan shall incorporate proposed operation and maintenance practices. These proposed operation and maintenance practices shall be submitted for approval as part of the submittal required under Sec. 63.343(d);
(D) The plan shall specify procedures to be followed to ensure that equipment or process malfunctions due to poor maintenance or other preventable conditions do not occur; and
(E) The plan shall include a systematic procedure for identifying malfunctions of process equipment, add-on air pollution control devices, and process and control system monitoring equipment and for implementing corrective actions to address such malfunctions.
(F) The plan shall include housekeeping procedures, as specified in Table 2 of this section.
(ii) If the operation and maintenance plan fails to address or inadequately addresses an event that meets the characteristics of a malfunction at the time the plan is initially developed, the owner or operator shall revise the operation and maintenance plan within 45 days after such an event occurs. The revised plan shall include procedures for operating and maintaining the process equipment, add-on air pollution control device, or monitoring equipment during similar malfunction events, and a program for corrective action for such events.
(iii) Recordkeeping associated with the operation and maintenance plan is identified in Sec. 63.346(b). Reporting associated with the operation and maintenance plan is identified in Sec. 63.347 (g) and (h) and paragraph (f)(3)(iv) of this section.
(iv) If actions taken by the owner or operator during periods of malfunction are inconsistent with the procedures specified in the operation and maintenance plan required by paragraph (f)(3)(i) of this section, the owner or operator shall record the actions taken for that event and shall report by phone such actions within 2 working days after commencing actions inconsistent with the plan. This report shall be followed by a letter within 7 working days after the end of the event, unless the owner or operator makes alternative reporting arrangements, in advance, with the Administrator.
(v) The owner or operator shall keep the written operation and maintenance plan on record after it is developed to be made available for inspection, upon request, by the Administrator for the life of the affected source or until the source is no longer subject to the provisions of this subpart. In addition, if the operation and maintenance plan is revised, the owner or operator shall keep previous (i.e., superseded) versions of the operation and maintenance plan on record to be made available for inspection, upon request, by the Administrator for a period of 5 years after each revision to the plan.
(vi) To satisfy the requirements of paragraph (f)(3) of this section, the owner or operator may use applicable standard operating procedure (SOP) manuals, Occupational Safety and Health Administration (OSHA) plans, or other existing plans, provided the alternative plans meet the requirements of this section.
(g) The standards in this section that apply to chromic acid baths shall not be met by using a reducing agent to change the form of chromium from hexavalent to trivalent.
Table 1 to Sec. 63.342--Summary of Operation and Maintenance Practices------------------------------------------------------------------------
Operation and
Control technique maintenance practices Frequency------------------------------------------------------------------------Composite mesh-pad (CMP) 1. Visually inspect 1. 1/quarter.
system. device to ensure there
is proper drainage, no
chronic acid buildup
on the pads, and no
evidence of chemical
attack on the
structural integrity
of the device.
2. Visually inspect 2. 1/quarter.
back portion of the
mesh pad closest to
the fan to ensure
there is no
breakthrough of
chromic acid mist.
3. Visually inspect 3. 1/quarter.
ductwork from tank to
the control device to
ensure there are no
leaks.
4. Perform washdown of 4. Per
the composite mesh- manufacturer.
pads in accordance
with manufacturers
recommendations.Packed-bed scrubber (PSB).... 1. Visually inspect 1. 1/quarter.
device to ensure there
is proper drainage, no
chromic acid buildup
on the packed beds,
and no evidence of
chemical attack on the
structural integrity
of the device.
2. Visually inspect 2. 1/quarter.
back portion of the
chevron blade mist
eliminator to ensure
that it is dry and
there is no
breakthrough of
chromic acid mist.
3. Same as number 3 3. 1/quarter.
above.
4. Add fresh makeup 4. Whenever
water to the top of makeup is
the packed bed \a b\. added.PBS/CMP system............... 1. Same as for CMP 1. 1/quarter.
system.
2. Same as for CMP 2. 1/quarter.
system.
3. Same as for CMP 3. 1/quarter.
system.
4. Same as for CMP 4. Per
system. manufacturer.Fiber-bed mist eliminator \c\ 1. Visually inspect 1. 1/quarter.
fiber-bed unit and
prefiltering device to
ensure there is proper
drainage, no chromic
acid buildup in the
units, and no evidence
of chemical attack on
the structural
integrity of the
devices.
2. Visually inspect 2. 1/quarter.
ductwork from tank or
tanks to the control
device to ensure there
are no leaks.
3. Perform washdown of 3. Per
fiber elements in manufacturer.
accordance with
manufacturers
recommendations.Air pollution control device To be proposed by the To be proposed
(APCD) not listed in rule. source for approval by by the source
the Administrator. for approval by
the
Administrator.------------------------------------------------------------------------
Monitoring Equipment------------------------------------------------------------------------Pitot tube................... Backflush with water, 1/quarter.
or remove from the
duct and rinse with
fresh water. Replace
in the duct and rotate
180 degrees to ensure
that the same zero
reading is obtained.
Check pitot tube ends
for damage. Replace
pitot tube if cracked
or fatigued.Stalagmometer................ Follow manufacturers
recommendations.------------------------------------------------------------------------\a\ If greater than 50 percent of the scrubber water is drained (e.g.,
for maintenance purposes), makeup water may be added to the scrubber
basin.\b\ For horizontal-flow scrubbers, top is defined as the section of the
unit directly above the packing media such that the makeup water would
flow perpendicular to the air flow through the packing. For vertical-
flow units, the top is defined as the area downstream of the packing
material such that the makeup water would flow countercurrent to the
air flow through the unit.\c\ Work practice standards for the control device installed upstream of
the fiber-bed mist eliminator to prevent plugging do not apply as long
as the work practice standards for the fiber-bed unit are followed.
Table 2 to Sec. 63.342--Housekeeping Practices------------------------------------------------------------------------
At this minimum
For You must: frequency------------------------------------------------------------------------1. Any substance used in an (a) Store the At all times, except
affected chromium substance in a when transferring
electroplating or chromium closed container in the substance to
anodizing tank that an enclosed storage and from the
contains hexavalent area or building; container.
chromium. AND Whenever
(b) Use a closed transporting
container when substance, except
transporting the when transferring
substance from the the substance to
enclosed storage and from the
area. container.2. Each affected tank, to (a) Install drip Prior to operating
minimize spills of bath trays that collect the tank.
solution that result from and return to the Whenever removing
dragout. Note: this measure tank any bath parts from an
does not require the return solution that drips affected tank.
of contaminated bath or drains from Whenever removing
solution to the tank. This parts as the parts parts from an
requirement applies only as are removed from affected tank.
the parts are removed from the tank; OR
the tank. Once away from (b) Contain and
the tank area, any spilled return to the tank
solution must be handled in any bath solution
accordance with Item 4 of that drains or
these housekeeping measures. drips from parts as
the parts are
removed from the
tank; OR.
(c) Collect and
treat in an onsite
wastewater
treatment plant any
bath solution that
drains or drips
from parts as the
parts are removed
from the tank.3. Each spraying operation Install a splash Prior to any such
for removing excess chromic guard to minimize spraying operation.
acid from parts removed overspray during
from, and occurring over, spraying operations
an affected tank. and to ensure that
any hexavalent
chromium laden
liquid captured by
the splash guard is
returned to the
affected chromium
electroplating or
anodizing tank.4. Each operation that Begin clean up, or Within 1 hour of the
involves the handling or otherwise contain, spill.
use of any substance used all spills of the
in an affected chromium substance. Note:
electroplating or chromium substances that
anodizing tank that fall or flow into
contains hexavalent drip trays, pans,
chromium. sumps, or other
containment areas
are not considered
spills.
5. Surfaces within the (a) Clean the At least once every
enclosed storage area, open surfaces using one 7 days if one or
floor area, walkways around or more of the more chromium
affected tanks contaminated following methods: electroplating or
with hexavalent chromium HEPA vacuuming; chromium anodizing
from an affected chromium Hand-wiping with a tanks were used, or
electroplating or chromium damp cloth; Wet at least after
anodizing tank. mopping; Hose down every 40 hours of
or rinse with operating time of
potable water that one or more
is collected in a affection chromium
wastewater electroplating or
collection system; chromium anodizing
Other cleaning tank, whichever is
method approved by later.
the permitting According to
authority; OR manufacturer's
(b) Apply a non- recommendations.
toxic chemical dust
suppressant to the
surfaces.6. All buffing, grinding, or Separate the Prior to beginning
polishing operations that operation from any the buffing,
are located in the same affected grinding, or
room as chromium electroplating or polishing
electroplating or chromium anodizing operation operation.
anodizing operations. by installing a
physical barrier;
the barrier may
take the form of
plastic strip
curtains.7. All chromium or chromium- Store, dispose, At all times.
containing wastes generated recover, or recycle
from housekeeping the wastes using
activities. practices that do
not lead to
fugitive dust and
in accordance with
hazardous waste
requirements.------------------------------------------------------------------------ [60 FR 4963, Jan. 25, 1995; 60 FR 33122, June 27, 1995, as amended at 61 FR 27787, June 3, 1996; 62 FR 42920, Aug. 11, 1997; 68 FR 37347, June 23, 2003; 69 FR 42894, July 19, 2004; 71 FR 20456, Apr. 20, 2006; 77 FR 58243, Sept. 19, 2012]