40 CFR Part 264 -- STANDARDS FOR
OWNERS AND OPERATORS OF HAZARDOUS WASTE TREATMENT, STORAGE, AND DISPOSAL FACILITIES
§264.1035 Recordkeeping requirements.
(a)(1) Each owner or operator subject to the provisions of this subpart shall comply with
the recordkeeping requirements of this section.
(2) An owner or operator of more than one hazardous waste management unit subject to the
provisions of this subpart may comply with the recordkeeping requirements for these
hazardous waste management units in one recordkeeping system if the system identifies each
record by each hazardous waste management unit.
(b) Owners and operators must record the following information in the facility operating
record:
(1) For facilities that comply with the provisions of §264.1033(a)(2), an implementation
schedule that includes dates by which the closed-vent system and control device will be
installed and in operation. The schedule must also include a rationale of why the
installation cannot be completed at an earlier date. The implementation schedule must be
in the facility operating record by the effective date that the facility becomes subject
to the provisions of this subpart.
(2) Up-to-date documentation of compliance with the process vent standards in §264.1032,
including:
(i) Information and data identifying all affected process vents, annual throughput and
operating hours of each affected unit, estimated emission rates for each affected vent and
for the overall facility (i.e., the total emissions for all affected vents at the
facility), and the approximate location within the facility of each affected unit (e.g.,
identify the hazardous waste management units on a facility plot plan).
(ii) Information and data supporting determinations of vent emissions and emission
reductions achieved by add-on control devices based on engineering calculations or source
tests. For the purpose of determining compliance, determinations of vent emissions and
emission reductions must be made using operating parameter values (e.g., temperatures,
flow rates, or vent stream organic compounds and concentrations) that represent the
conditions that result in maximum organic emissions, such as when the waste management
unit is operating at the highest load or capacity level reasonably expected to occur. If
the owner or operator takes any action (e.g., managing a waste of different composition or
increasing operating hours of affected waste management units) that would result in an
increase in total organic emissions from affected process vents at the facility, then a
new determination is required.
(3) Where an owner or operator chooses to use test data to determine the organic removal
efficiency or total organic compound concentration achieved by the control device, a
performance test plan. The test plan must include:
(i) A description of how it is determined that the planned test is going to be conducted
when the hazardous waste management unit is operating at the highest load or capacity
level reasonably expected to occur. This shall include the estimated or design flow rate
and organic content of each vent stream and define the acceptable operating ranges of key
process and control device parameters during the test program.
(ii) A detailed engineering description of the closed-vent system and control device
including:
(A) Manufacturer's name and model number of control device.
(B) Type of control device.
(C) Dimensions of the control device.
(D) Capacity.
(E) Construction materials.
(iii) A detailed description of sampling and monitoring procedures, including sampling and
monitoring locations in the system, the equipment to be used, sampling and monitoring
frequency, and planned analytical procedures for sample analysis.
(4) Documentation of compliance with §264.1033 shall include the following information:
(i) A list of all information references and sources used in preparing the documentation.
(ii) Records, including the dates, of each compliance test required by §264.1033(k).
(iii) If engineering calculations are used, a design analysis, specifications, drawings,
schematics, and piping and instrumentation diagrams based on the appropriate sections of
"APTI Course 415: Control of Gaseous Emissions'' (incorporated by reference as
specified in §260.11) or other engineering texts acceptable to the Regional Administrator
that present basic control device design information. Documentation provided by the
control device manufacturer or vendor that describes the control device design in
accordance with paragraphs through (b)(4)(iii)(G) of this section may be used to comply
with this requirement. The design analysis shall address the vent stream characteristics
and control device operation parameters as specified below.
(A) For a thermal vapor incinerator, the design analysis shall consider the vent stream
composition, constituent concentrations, and flow rate. The design analysis shall also
establish the design minimum and average temperature in the combustion zone and the
combustion zone residence time.
(B) For a catalytic vapor incinerator, the design analysis shall consider the vent stream
composition, constituent concentrations, and flow rate. The design analysis shall also
establish the design minimum and average temperatures across the catalyst bed inlet and
outlet.
(C) For a boiler or process heater, the design analysis shall consider the vent stream
composition, constituent concentrations, and flow rate. The design analysis shall also
establish the design minimum and average flame zone temperatures, combustion zone
residence time, and description of method and location where the vent stream is introduced
into the combustion zone.
(D) For a flare, the design analysis shall consider the vent stream composition,
constituent concentrations, and flow rate. The design analysis shall also consider the
requirements specified in §264.1033(d).
(E) For a condenser, the design analysis shall consider the vent stream composition,
constituent concentrations, flow rate, relative humidity, and temperature. The design
analysis shall also establish the design outlet organic compound concentration level,
design average temperature of the condenser exhaust vent stream, and design average
temperatures of the coolant fluid at the condenser inlet and outlet.
(F) For a carbon adsorption system such as a fixed-bed adsorber that regenerates the
carbon bed directly onsite in the control device, the design analysis shall consider the
vent stream composition, constituent concentrations, flow rate, relative humidity, and
temperature. The design analysis shall also establish the design exhaust vent stream
organic compound concentration level, number and capacity of carbon beds, type and working
capacity of activated carbon used for carbon beds, design total steam flow over the period
of each complete carbon bed regeneration cycle, duration of the carbon bed steaming and
cooling/drying cycles, design carbon bed temperature after regeneration, design carbon bed
regeneration time, and design service life of carbon.
(G) For a carbon adsorption system such as a carbon canister that does not regenerate the
carbon bed directly onsite in the control device, the design analysis shall consider the
vent stream composition, constituent concentrations, flow rate, relative humidity, and
temperature. The design analysis shall also establish the design outlet organic
concentration level, capacity of carbon bed, type and working capacity of activated carbon
used for carbon bed, and design carbon replacement interval based on the total carbon
working capacity of the control device and source operating schedule.
(iv) A statement signed and dated by the owner or operator certifying that the operating
parameters used in the design analysis reasonably represent the conditions that exist when
the hazardous waste management unit is or would be operating at the highest load or
capacity level reasonably expected to occur.
(v) A statement signed and dated by the owner or operator certifying that the control
device is designed to operate at an efficiency of 95 percent or greater unless the total
organic concentration limit of §264.1032(a) is achieved at an efficiency less than 95
weight percent or the total organic emission limits of §264.1032(a) for affected process
vents at the facility can be attained by a control device involving vapor recovery at an
efficiency less than 95 weight percent. A statement provided by the control device
manufacturer or vendor certifying that the control equipment meets the design
specifications may be used to comply with this requirement.
(vi) If performance tests are used to demonstrate compliance, all test results.
(c) Design documentation and monitoring, operating, and inspection information for each
closed-vent system and control device required to comply with the provisions of this part
shall be recorded and kept up-to-date in the facility operating record. The information
shall include:
(1) Description and date of each modification that is made to the closed-vent system or
control device design.
(2) Identification of operating parameter, description of monitoring device, and diagram
of monitoring sensor location or locations used to comply with §§264.1033 (f)(1) and
(f)(2).
(3) Monitoring, operating, and inspection information required by paragraphs (f) through
(k) of §264.1033.
(4) Date, time, and duration of each period that occurs while the control device is
operating when any monitored parameter exceeds the value established in the control device
design analysis as specified below:
(i) For a thermal vapor incinerator designed to operate with a minimum residence time of
0.50 second at a minimum temperature of 760 C. period when the combustion temperature is
below 760 C.
(ii) For a thermal vapor incinerator designed to operate with an organic emission
reduction efficiency of 95 weight percent or greater period when the combustion zone
temperature is more than 28 C below the design average combustion zone temperature
established as a requirement of paragraph (b)(4)(iii)(A) of this section.
(iii) For a catalytic vapor incinerator, period when:
(A) Temperature of the vent stream at the catalyst bed inlet is more than 28 C below the
average temperature of the inlet vent stream established as a requirement of paragraph
(b)(4)(iii)(B) of this section, or
(B) Temperature difference across the catalyst bed is less than 80 percent of the design
average temperature difference established as a requirement of paragraph (b)(4)(iii)(B) of
this section.
(iv) For a boiler or process heater, period when:
(A) Flame zone temperature is more than 28 C below the design average flame zone
temperature established as a requirement of paragraph (b)(4)(iii)(C) of this section, or
(B) Position changes where the vent stream is introduced to the combustion zone from the
location established as a requirement of paragraph (b)(4)(iii)(C) of this section.
(v) For a flare, period when the pilot flame is not ignited.
(vi) For a condenser that complies with §264.1033(f)(2)(vi)(A), period when the organic
compound concentration level or readings of organic compounds in the exhaust vent stream
from the condenser are more than 20 percent greater than the design outlet organic
compound concentration level established as a requirement of paragraph (b)(4)(iii)(E) of
this section.
(vii) For a condenser that complies with §264.1033(f)(2)(vi)(B), period when:
(A) Temperature of the exhaust vent stream from the condenser is more than 6 C above the
design average exhaust vent stream temperature established as a requirement of paragraph
(b)(4)(iii)(E) of this section; or
(B) Temperature of the coolant fluid exiting the condenser is more than 6 C above the
design average coolant fluid temperature at the condenser outlet established as a
requirement of paragraph (b)(4)(iii)(E) of this section.
(viii) For a carbon adsorption system such as a fixed-bed carbon adsorber that regenerates
the carbon bed directly onsite in the control device and complies with
§264.1033(f)(2)(vii)(A), period when the organic compound concentration level or readings
of organic compounds in the exhaust vent stream from the carbon bed are more than 20
percent greater than the design exhaust vent stream organic compound concentration level
established as a requirement of paragraph (b)(4)(iii)(F) of this section.
(ix) For a carbon adsorption system such as a fixed-bed carbon adsorber that regenerates
the carbon bed directly onsite in the control device and complies with
§264.1033(f)(2)(vii)(B), period when the vent stream continues to flow through the
control device beyond the predetermined carbon bed regeneration time established as a
requirement of paragraph (b)(4)(iii)(F) of this section.
(5) Explanation for each period recorded under paragraph (4) of the cause for control
device operating parameter exceeding the design value and the measures implemented to
correct the control device operation.
(6) For a carbon adsorption system operated subject to requirements specified in
§264.1033(g) or §264.1033(h)(2), date when existing carbon in the control device is
replaced with fresh carbon.
(7) For a carbon adsorption system operated subject to requirements specified in
§264.1033(h)(1), a log that records:
(i) Date and time when control device is monitored for carbon breakthrough and the
monitoring device reading.
(ii) Date when existing carbon in the control device is replaced with fresh carbon.
(8) Date of each control device startup and shutdown.
(d) Records of the monitoring, operating, and inspection information required by
paragraphs (c)(3)-(c)(8) of this section need be kept only 3 years.
(e) For a control device other than a thermal vapor incinerator, catalytic vapor
incinerator, flare, boiler, process heater, condenser, or carbon adsorption system, the
Regional Administrator will specify the appropriate recordkeeping requirements.
(f) Up-to-date information and data used to determine whether or not a process vent is
subject to the requirements in §264.1032 including supporting documentation as required
by §264.1034(d)(2) when application of the knowledge of the nature of the hazardous waste
stream or the process by which it was produced is used, shall be recorded in a log that is
kept in the facility operating record.
(Approved by the Office of Management and Budget under control number 2060-0195)
(55 FR 25494, June 21, 1990, as amended at 56 FR 19290, Apr. 26, 1991)
§264.1036 Reporting requirements.
(a) A semiannual report shall be submitted by owners and operators to the requirements of
this subpart to the Regional Administrator by dates specified by the Regional
Administrator. The report shall include the following information:
(1) The Environmental Protection Agency identification number, name, and address of the
facility.
(2) For each month during the semiannual reporting period, dates when the control device
exceeded or operated outside of the design specifications as defined in §264.1035(c)(4)
and as indicated by the control device monitoring required by §264.1033(f) and such
exceedances were not corrected within 24 hours, or that a flare operated with visible
emissions as defined in §264.1033(d) and as determined by Method 22 monitoring, the
duration and cause of each exceedance or visible emissions, and any corrective measures
taken.
(b) If, during the semiannual reporting period, the control device does not exceed or
operate outside of the design specifications as defined in §264.1035(c)(4) for more than
24 hours or a flare does not operate with visible emissions as defined in §264.1033(d), a
report to the Regional Administrator is not required.
(Approved by the Office of Management and Budget under control number 2060-0195)
§§264.1037 -- 264.1049 (Reserved)
Subpart BB -- Air Emission Standards for Equipment Leaks
§264.1050 Applicability.
(a) The regulations in this subpart apply to owners and operators of facilities that
treat, store, or dispose of hazardous wastes (except as provided in §264.1).
(b) Except as provided in §264.1064(k), this subpart applies to equipment that contains
or contacts hazardous wastes with organic concentrations of at least 10 percent by weight
that are managed in:
(1) Units that are subject to the permitting requirements of Part 270, or
(2) Hazardous waste recycling units that are located on hazardous waste management
facilities otherwise subject to the permitting requirements of Part 270.
(c) If the owner or operator of equipment subject to the requirements of §§264.1052
through 264.1065 has received a permit under section 3005 of RCRA prior to December 21,
1990, the requirements of §§264.1052 through 264.1065 must be incorporated when the
permit is reissued under§124.15 or reviewed under §270.50.
(d) Each piece of equipment to which this subpart applies shall be marked in such a manner
that it can be distinguished readily from other pieces of equipment.
(e) Equipment that is in vacuum service is excluded from the requirements of §§264.1052
to 264.1060 if it is identified as required in §264.1064(g)(5).
(Note: The requirements of §§264.1052 through 264.1065 apply to equipment associated
with hazardous waste recycling units previously exempt under §261.6(c)(1). Other
exemptions under §§261.4, 262.34, and 264.1(g) are not affected by these requirements.)
§264.1051 Definitions.
As used in this subpart, all terms shall have the meaning given them in §264.1031, the
Act, and Parts 260-266.
§264.1052 Standards: Pumps in light liquid service.
(a)(1) Each pump in light liquid service shall be monitored monthly to detect leaks by the
methods specified in §264.1063(b), except as provided in paragraphs (d), (e), and (f) of
this section.
(2) Each pump in light liquid service shall be checked by visual inspection each calendar
week for indications of liquids dripping from the pump seal.
(b)(1) If an instrument reading of 10,000 ppm or greater is measured, a leak is detected.
(2) If there are indications of liquids dripping from the pump seal, a leak is detected.
(c)(1) When a leak is detected, it shall be repaired as soon as practicable, but not later
than 15 calendar days after it is detected, except as provided in §264.1059.
(2) A first attempt at repair (e.g., tightening the packing gland) shall be made no later
than 5 calendar days after each leak is detected.
(d) Each pump equipped with a dual mechanical seal system that includes a barrier fluid
system is exempt from the requirements of paragraph (a) of this section, provided the
following requirements are met:
(1) Each dual mechanical seal system must be:
(i) Operated with the barrier fluid at a pressure that is at all times greater than the
pump stuffing box pressure, or
(ii) Equipped with a barrier fluid degassing reservoir that is connected by a closed-vent
system to a control device that complies with the requirements of §264.1060, or
(iii) Equipped with a system that purges the barrier fluid into a hazardous waste stream
with no detectable emissions to the atmosphere.
(2) The barrier fluid system must not be a hazardous waste with organic concentrations 10
percent or greater by weight.
(3) Each barrier fluid system must be equipped with a sensor that will detect failure of
the seal system, the barrier fluid system, or both.
(4) Each pump must be checked by visual inspection, each calendar week, for indications of
liquids dripping from the pump seals.
(5)(i) Each sensor as described in paragraph (d)(3) of this section must be checked daily
or be equipped with an audible alarm that must be checked monthly to ensure that it is
functioning properly.
(ii) The owner or operator must determine, based on design considerations and operating
experience, a criterion that indicates failure of the seal system, the barrier fluid
system, or both.
(6)(i) If there are indications of liquids dripping from the pump seal or the sensor
indicates failure of the seal system, the barrier fluid system, or both based on the
criterion determined in paragraph (d)(5)(ii) of this section, a leak is detected.
(ii) When a leak is detected, it shall be repaired as soon as practicable, but not later
than 15 calendar days after it is detected, except as provided in §264.1059.
(iii) A first attempt at repair (e.g., relapping the seal) shall be made no later than 5
calendar days after each leak is detected.
(e) Any pump that is designated, as described in §264.1064(g)(2), for no detectable
emissions, as indicated by an instrument reading of less than 500 ppm above background, is
exempt from the requirements of paragraphs (a), (c), and (d) of this section if the pump
meets the following requirements:
(1) Must have no externally actuated shaft penetrating the pump housing.
(2) Must operate with no detectable emissions as indicated by an instrument reading of
less than 500 ppm above background as measured by the methods specified in §264.1063(c).
(3) Must be tested for compliance with paragraph (e)(2) of this section initially upon
designation, annually, and at other times as requested by the Regional Administrator.
(f) If any pump is equipped with a closed-vent system capable of capturing and
transporting any leakage from the seal or seals to a control device that complies with the
requirements of 264.1060, it is exempt from the requirements of paragraphs (a) through (e)
of this section.
(55 FR 25501, June 21, 1990, as amended at 56 FR 19290, Apr. 26, 1991)
§264.1053 Standards: Compressors.
(a) Each compressor shall be equipped with a seal system that includes a barrier fluid
system and that prevents leakage of total organic emissions to the atmosphere, except as
provided in paragraphs (h) and (i) of this section.
(b) Each compressor seal system as required in paragraph (a) of this section shall be:
(1) Operated with the barrier fluid at a pressure that is at all times greater than the
compressor stuffing box pressure, or
(2) Equipped with a barrier fluid system that is connected by a closed-vent system to a
control device that complies with the requirements of §264.1060, or
(3) Equipped with a system that purges the barrier fluid into a hazardous waste stream
with no detectable emissions to atmosphere.
(c) The barrier fluid must not be a hazardous waste with organic concentrations 10 percent
or greater by weight.
(d) Each barrier fluid system as described in paragraphs (a) through (c) of this section
shall be equipped with a sensor that will detect failure of the seal system, barrier fluid
system, or both.
(e)(1) Each sensor as required in paragraph (d) of this section shall be checked daily or
shall be equipped with an audible alarm that must be checked monthly to ensure that it is
functioning properly unless the compressor is located within the boundary of an unmanned
plant site, in which case the sensor must be checked daily.
(2) The owner or operator shall determine, based on design considerations and operating
experience, a criterion that indicates failure of the seal system, the barrier fluid
system, or both.
(f) If the sensor indicates failure of the seal system, the barrier fluid system, or both
based on the criterion determined under paragraph (e)(2) of this section, a leak is
detected.
(g)(1) When a leak is detected, it shall be repaired as soon as practicable, but not later
than 15 calendar days after it is detected, except as provided in §264.1059.
(2) A first attempt at repair (e.g., tightening the packing gland) shall be made no later
than 5 calendar days after each leak is detected.
(h) A compressor is exempt from the requirements of paragraphs (a) and (b) of this section
if it is equipped with a closed-vent system capable of capturing and transporting any
leakage from the seal to a control device that complies with the requirements of
§264.1060, except as provided in paragraph (i) of this section.
(i) Any compressor that is designated, as described in §264.1064(g)(2), for no detectable
emissions as indicated by an instrument reading of less than 500 ppm above background is
exempt from the requirements of paragraphs (a) through (h) of this section if the
compressor:
(1) Is determined to be operating with no detectable emissions, as indicated by an
instrument reading of less than 500 ppm above background, as measured by the method
specified in §264.1063(c).
(2) Is tested for compliance with paragraph (i)(1) of this section initially upon
designation, annually, and at other times as requested by the Regional Administrator.
§264.1054 Standards: Pressure relief devices in gas/vapor service.
(a) Except during pressure releases, each pressure relief device in gas/vapor service
shall be operated with no detectable emissions, as indicated by an instrument reading of
less than 500 ppm above background, as measured by the method specified in §264.1063(c).
(b)(1) After each pressure release, the pressure relief device shall be returned to a
condition of no detectable emissions, as indicated by an instrument reading of less than
500 ppm above background, as soon as practicable, but no later than 5 calendar days after
each pressure release, except as provided in §264.1059.
(2) No later than 5 calendar days after the pressure release, the pressure relief device
shall be monitored to confirm the condition of no detectable emissions, as indicated by an
instrument reading of less than 500 ppm above background, as measured by the method
specified in §264.1063(c).
(c) Any pressure relief device that is equipped with a closed-vent system capable of
capturing and transporting leakage from the pressure relief device to a control device as
described in §264.1060 is exempt from the requirements of paragraphs (a) and (b) of this
section.