flash emissions may be generated. You must select gasket material for
the hatch based on composition of the fluid in the storage vessel and
weather conditions.
    (c) Closed vent system requirements for storage vessel affected
facilities using a control device or routing emissions to a process.
(1) You must design the closed vent system to route all gases, vapors,
and fumes emitted from the material in the storage vessel to a control
device that meets the requirements specified in Sec.  60.5412a(c) and
(d), or to a process.
    (2) You must design and operate a closed vent system with no
detectable emissions, as determined using olfactory, visual and
auditory inspections. Each closed vent system that routes emissions to
a process must be operational 95 percent of the year or greater.
    (3) You must meet the requirements specified in paragraphs
(c)(3)(i) and (ii) of this section if the closed vent system contains
one or more bypass devices that could be used to divert all or a
portion of the gases, vapors, or fumes from entering the control device
or to a process.
    (i) Except as provided in paragraph (c)(3)(ii) of this section, you
must comply with either paragraph (c)(3)(i)(A) or (B) of this section
for each bypass device.
    (A) You must properly install, calibrate, maintain, and operate a
flow indicator at the inlet to the bypass device that could divert the
stream away from the control device or process to the atmosphere. Set
the flow indicator to trigger and audible and visible alarm, and
initiate notification via remote alarm to the nearest field office,
when the bypass device is open such that the stream is being, or could
be, diverted away from the control device or process to the atmosphere.
You must maintain records of each time the alarm is sounded according
to Sec.  60.5420a(c)(8).
    (B) You must secure the bypass device valve installed at the inlet
to the bypass device in the non-diverting position using a car-seal or
a lock-and-key type configuration.
    (ii) Low leg drains, high point bleeds, analyzer vents, open-ended
valves or lines, and safety devices are not subject to the requirements
of paragraph (c)(3)(i) of this section.

Sec.  60.5412a  What additional requirements must I meet for
determining initial compliance with control devices used to comply with
the emission standards for my centrifugal compressor, pneumatic pump
and storage vessel affected facilities?

    You must meet the applicable requirements of this section for each
control device used to comply with the emission standards for your
centrifugal compressor affected facility, pneumatic pump affected
facility, or storage vessel affected facility.
    (a) Each control device used to meet the emission reduction
standard in Sec.  60.5380a(a)(1) for your centrifugal compressor
affected facility or Sec.  60.5393a(b)(1) for your pneumatic pump must
be installed according to paragraphs (a)(1) through (3) of this
section. As an alternative, you may install a control device model
tested under Sec.  60.5413a(d), which meets the criteria in Sec.
60.5413a(d)(11) and Sec.  60.5413a(e).
    (1) Each combustion device (e.g., thermal vapor incinerator,
catalytic vapor incinerator, boiler, or process heater) must be
designed and operated in accordance with one of the performance
requirements specified in paragraphs (a)(1)(i) through (iv) of this
section.
    (i) You must reduce the mass content of methane and VOC in the
gases vented to the device by 95.0 percent by weight or greater as
determined in accordance with the requirements of Sec.  60.5413a.
    (ii) You must reduce the concentration of TOC in the exhaust gases
at the outlet to the device to a level equal to or less than 600 parts
per million by volume as propane on a dry basis corrected to 3 percent
oxygen as determined in accordance with the requirements of Sec.
60.5413a.
    (iii) You must operate at a minimum temperature of 760 [deg]C for a
control device that can demonstrate a uniform combustion zone
temperature during the performance test conducted under Sec.  60.5413a.
    (iv) If a boiler or process heater is used as the control device,
then you must introduce the vent stream into the flame zone of the
boiler or process heater.
    (2) Each vapor recovery device (e.g., carbon adsorption system or
condenser) or other non-destructive control device must be designed and
operated to reduce the mass content of methane and VOC in the gases
vented to the device by 95.0 percent by weight or greater as determined
in accordance with the requirements of Sec.  60.5413a. As an
alternative to the performance testing requirements, you may
demonstrate initial compliance by conducting a design analysis for
vapor recovery devices according to the requirements of Sec.
60.5413a(c).
    (3) You must design and operate a flare in accordance with the
requirements of Sec.  60.5413a(a)(1).
    (b) You must operate each control device installed on your
centrifugal compressor or pneumatic pump affected facility in
accordance with the requirements specified in paragraphs (b)(1) and (2)
of this section.
    (1) You must operate each control device used to comply with this
subpart at all times when gases, vapors, and fumes are vented from the
wet seal fluid degassing system affected facility as required under
Sec.  60.5380a(a), or from the pneumatic pump as required under Sec.
60.5393a(b)(1), through the closed vent system to the control device.
You may vent more than one affected facility to a control device used
to comply with this subpart.
    (2) For each control device monitored in accordance with the
requirements of Sec.  60.5417a(a) through (g), you must demonstrate
compliance according to the requirements of Sec.  60.5415a(b)(2), as
applicable.
    (c) For each carbon adsorption system used as a control device to
meet the requirements of paragraph (a)(2) or

(d)(2) of this section, you must manage the carbon in accordance with
the requirements specified in paragraphs (c)(1) or (2) of this section.
    (1) Following the initial startup of the control device, you must
replace all carbon in the control device with fresh carbon on a
regular, predetermined time interval that is no longer than the carbon
service life established according to Sec.  60.5413a(c)(2) or (3) or
according to the design required in paragraph (d)(2) of this section,
for the carbon adsorption system. You must maintain records identifying
the schedule for replacement and records of each carbon replacement as
required in Sec.  60.5420a(c)(10) and (12).
    (2) You must either regenerate, reactivate, or burn the spent
carbon removed from the carbon adsorption system in one of the units
specified in paragraphs (c)(2)(i) through (vii) of this section.
    (i) Regenerate or reactivate the spent carbon in a thermal
treatment unit for which you have been issued a final permit under 40
CFR part 270 that implements the requirements of 40 CFR part 264,
subpart X.
    (ii) Regenerate or reactivate the spent carbon in a thermal
treatment unit equipped with and operating air emission controls in
accordance with this section.
    (iii) Regenerate or reactivate the spent carbon in a thermal
treatment unit equipped with and operating organic air emission
controls in accordance with an emissions standard for VOC under another
subpart in 40 CFR part 60 or this part.
    (iv) Burn the spent carbon in a hazardous waste incinerator for
which the owner or operator has been issued a final permit under 40 CFR
part 270 that implements the requirements of 40 CFR part 264, subpart
O.
    (v) Burn the spent carbon in a hazardous waste incinerator which
you have designed and operated in accordance with the requirements of
40 CFR part 265, subpart O.
    (vi) Burn the spent carbon in a boiler or industrial furnace for
which you have been issued a final permit under 40 CFR part 270 that
implements the requirements of 40 CFR part 266, subpart H.
    (vii) Burn the spent carbon in a boiler or industrial furnace that
you have designed and operated in accordance with the interim status
requirements of 40 CFR part 266, subpart H.
    (d) Each control device used to meet the emission reduction
standard in Sec.  60.5395a(a) for your storage vessel affected facility
must be installed according to paragraphs (d)(1) through (3) of this
section, as applicable. As an alternative to paragraph (d)(1) of this
section, you may install a control device model tested under Sec.
60.5413a(d), which meets the criteria in Sec.  60.5413a(d)(11) and
Sec.  60.5413a(e).
    (1) For each enclosed combustion control device (e.g., thermal
vapor incinerator, catalytic vapor incinerator, boiler, or process
heater) you must meet the requirements in paragraphs (d)(1)(i) through
(iv) of this section.
    (i) Ensure that each enclosed combustion control device is
maintained in a leak free condition.
    (ii) Install and operate a continuous burning pilot flame.
    (iii) Operate the combustion control device with no visible
emissions, except for periods not to exceed a total of 1 minute during
any 15 minute period. A visible emissions test using section 11 of EPA
Method 22 of appendix A-7 of this part must be performed at least once
every calendar month, separated by at least 15 days between each test.
The observation period shall be 15 minutes. Devices failing the visible
emissions test must follow manufacturer's repair instructions, if
available, or best combustion engineering practice as outlined in the
unit inspection and maintenance plan, to return the unit to compliant
operation. All inspection, repair and maintenance activities for each
unit must be recorded in a maintenance and repair log and must be
available for inspection. Following return to operation from
maintenance or repair activity, each device must pass a Method 22 of
appendix A-7 of this part visual observation as described in this
paragraph.
    (iv) Each combustion control device (e.g., thermal vapor
incinerator, catalytic vapor incinerator, boiler, or process heater)
must be designed and operated in accordance with one of the performance
requirements specified in paragraphs (A) through (D) of this section.
    (A) You must reduce the mass content of methane and VOC in the
gases vented to the device by 95.0 percent by weight or greater as
determined in accordance with the requirements of Sec.  60.5413a.
    (B) You must reduce the concentration of TOC in the exhaust gases
at the outlet to the device to a level equal to or less than 600 parts
per million by volume as propane on a dry basis corrected to 3 percent
oxygen as determined in accordance with the requirements of Sec.
60.5413a.
    (C) You must operate at a minimum temperature of 760 [deg]C for a
control device that can demonstrate a uniform combustion zone
temperature during the performance test conducted under Sec.  60.5413a.
    (D) If a boiler or process heater is used as the control device,
then you must introduce the vent stream into the flame zone of the
boiler or process heater.
    (2) Each vapor recovery device (e.g., carbon adsorption system or
condenser) or other non-destructive control device must be designed and
operated to reduce the mass content of methane and VOC in the gases
vented to the device by 95.0 percent by weight or greater. A carbon
replacement schedule must be included in the design of the carbon
adsorption system.
    (3) You must operate each control device used to comply with this
subpart at all times when gases, vapors, and fumes are vented from the
storage vessel affected facility through the closed vent system to the
control device. You may vent more than one affected facility to a
control device used to comply with this subpart.

Sec.  60.5413a  What are the performance testing procedures for control
devices used to demonstrate compliance at my centrifugal compressor,
pneumatic pump and storage vessel affected facilities?

    This section applies to the performance testing of control devices
used to demonstrate compliance with the emissions standards for your
centrifugal compressor affected facility, pneumatic pump affected
facility, or storage vessel affected facility. You must demonstrate
that a control device achieves the performance requirements of Sec.
60.5412a(a) or (d) using the performance test methods and procedures
specified in this section. For condensers and carbon adsorbers, you may
use a design analysis as specified in paragraph (c) of this section in
lieu of complying with paragraph (b) of this section. In addition, this
section contains the requirements for enclosed combustion control
device performance tests conducted by the manufacturer applicable to
storage vessel, centrifugal compressor and pneumatic pump affected
facilities.
    (a) Performance test exemptions. You are exempt from the
requirements to conduct performance tests and design analyses if you
use any of the control devices described in paragraphs (a)(1) through
(7) of this section.
    (1) A flare that is designed and operated in accordance with Sec.
60.18(b). You must conduct the compliance determination using Method 22
of appendix A-7 of this part to determine visible emissions.
    (2) A boiler or process heater with a design heat input capacity of
44 megawatts or greater.

    (3) A boiler or process heater into which the vent stream is
introduced with the primary fuel or is used as the primary fuel.
    (4) A boiler or process heater burning hazardous waste for which
you have either been issued a final permit under 40 CFR part 270 and
comply with the requirements of 40 CFR part 266, subpart H; or you have
certified compliance with the interim status requirements of 40 CFR
part 266, subpart H.
    (5) A hazardous waste incinerator for which you have been issued a
final permit under 40 CFR part 270 and comply with the requirements of
40 CFR part 264, subpart O; or you have certified compliance with the
interim status requirements of 40 CFR part 265, subpart O.
    (6) A performance test is waived in accordance with Sec.  60.8(b).
    (7) A control device whose model can be demonstrated to meet the
performance requirements of Sec.  60.5412a(a) or (d) through a
performance test conducted by the manufacturer, as specified in
paragraph (d) of this section.
    (b) Test methods and procedures. You must use the test methods and
procedures specified in paragraphs (b)(1) through (5) of this section,
as applicable, for each performance test conducted to demonstrate that
a control device meets the requirements of Sec.  60.5412a(a) or (d).
You must conduct the initial and periodic performance tests according
to the schedule specified in paragraph (b)(5) of this section.
    (1) You must use Method 1 or 1A of appendix A-1 of this part, as
appropriate, to select the sampling sites specified in paragraphs
(b)(1)(i) and (ii) of this section. Any references to particulate
mentioned in Methods 1 and 1A do not apply to this section.
    (i) Sampling sites must be located at the inlet of the first
control device, and at the outlet of the final control device, to
determine compliance with the control device percent reduction
requirement specified in Sec.  60.5412a(a)(1)(i) or (a)(2).
    (ii) The sampling site must be located at the outlet of the
combustion device to determine compliance with the enclosed combustion
control device total TOC concentration limit specified in Sec.
60.5412a(a)(1)(ii).
    (2) You must determine the gas volumetric flowrate using Method 2,
2A, 2C, or 2D of appendix A-2 of this part, as appropriate.
    (3) To determine compliance with the control device percent
reduction performance requirement in Sec.  60.5412a(a)(1)(i), (a)(2) or
(d)(1)(i)(A), you must use Method 25A of appendix A-7 of this part. You
must use the procedures in paragraphs (b)(3)(i) through (iv) of this
section to calculate percent reduction efficiency.
    (i) For each run, you must take either an integrated sample or a
minimum of four grab samples per hour. If grab sampling is used, then
the samples must be taken at approximately equal intervals in time,
such as 15-minute intervals during the run.
    (ii) You must compute the mass rate of TOC (minus methane and
ethane) using the equations and procedures specified in paragraphs
(b)(3)(ii)(A) and (B) of this section.
    (A) You must use the following equations:
    [GRAPHIC] [TIFF OMITTED] TP18SE15.002

Where:

Ei, Eo = Mass rate of TOC (minus methane and
ethane) at the inlet and outlet of the control device, respectively,
dry basis, kilogram per hour.
K2 = Constant, 2.494 x 10-6 (parts per
million) (gram-mole per standard cubic meter) (kilogram/gram)
(minute/hour), where standard temperature (gram-mole per standard
cubic meter) is 20 [deg]C.
Cij, Coj = Concentration of sample component j
of the gas stream at the inlet and outlet of the control device,
respectively, dry basis, parts per million by volume.
Mij, Moj = Molecular weight of sample
component j of the gas stream at the inlet and outlet of the control
device, respectively, gram/gram-mole.
Qi, Qo = Flowrate of gas stream at the inlet
and outlet of the control device, respectively, dry standard cubic
meter per minute.
n = Number of components in sample.

    (B) When calculating the TOC mass rate, you must sum all organic
compounds (minus methane and ethane) measured by Method 25A of appendix
A-7 of this part using the equations in paragraph (b)(3)(ii)(A) of this
section.
    (iii) You must calculate the percent reduction in TOC (minus
methane and ethane) as follows:
[GRAPHIC] [TIFF OMITTED] TP18SE15.003

Where:

Rcd = Control efficiency of control device, percent.
Ei = Mass rate of TOC (minus methane and ethane) at the
inlet to the control device as calculated under paragraph (b)(3)(ii)
of this section, kilograms TOC per hour or kilograms HAP per hour.
Eo = Mass rate of TOC (minus methane and ethane) at the
outlet of the control device, as calculated under paragraph
(b)(3)(ii) of this section, kilograms TOC per hour per hour.

    (iv) If the vent stream entering a boiler or process heater with a
design capacity less than 44 megawatts is introduced with the
combustion air or as a secondary fuel, you must determine the weight-
percent reduction of total TOC (minus methane and ethane) across the
device by comparing the TOC (minus methane and ethane) in all combusted
vent streams and primary and secondary fuels with the TOC (minus
methane and ethane) exiting the device, respectively.
    (4) You must use Method 25A of appendix A-7 of this part to measure
TOC (minus methane and ethane) to determine compliance with the
enclosed combustion control device total VOC concentration limit
specified in Sec.  60.5412a(a)(1)(ii) or (d)(1)(iv)(B). You must
calculate parts per million by volume concentration and correct to 3
percent oxygen, using the procedures in paragraphs (b)(4)(i) through
(iii) of this section.
    (i) For each run, you must take either an integrated sample or a
minimum of four grab samples per hour. If grab sampling is used, then
the samples must be taken at approximately equal intervals in time,
such as 15-minute intervals during the run.
    (ii) You must calculate the TOC concentration for each run as
follows:
[GRAPHIC] [TIFF OMITTED] TP18SE15.004

Where:

CTOC = Concentration of total organic compounds minus
methane and ethane, dry basis, parts per million by volume.
Cji = Concentration of sample component j of sample i,
dry basis, parts per million by volume.
n = Number of components in the sample.
x = Number of samples in the sample run.

    (iii) You must correct the TOC concentration to 3 percent oxygen as
specified in paragraphs (b)(4)(iii)(A) and (B) of this section.
    (A) You must use the emission rate correction factor for excess
air, integrated sampling and analysis procedures of Method 3A or 3B of
appendix A-2 of this part, ASTM D6522-00 (Reapproved 2005), or ASME/

ANSI PTC 19.10-1981, Part 10 (manual portion only) (incorporated by
reference as specified in Sec.  60.17) to determine the oxygen
concentration. The samples must be taken during the same time that the
samples are taken for determining TOC concentration.
    (B) You must correct the TOC concentration for percent oxygen as
follows:
[GRAPHIC] [TIFF OMITTED] TP18SE15.005

Where:

Cc = TOC concentration corrected to 3 percent oxygen, dry
basis, parts per million by volume.
Cm = TOC concentration, dry basis, parts per million by
volume.
%O2d = Concentration of oxygen, dry basis, percent by
volume.

    (5) You must conduct performance tests according to the schedule
specified in paragraphs (b)(5)(i) and (ii) of this section.
    (i) You must conduct an initial performance test within 180 days
after initial startup for your affected facility. You must submit the
performance test results as required in Sec.  60.5420a(b)(9).
    (ii) You must conduct periodic performance tests for all control
devices required to conduct initial performance tests except as
specified in paragraphs (b)(5)(ii)(A) and (B) of this section. You must
conduct the first periodic performance test no later than 60 months
after the initial performance test required in paragraph (b)(5)(i) of
this section. You must conduct subsequent periodic performance tests at
intervals no longer than 60 months following the previous periodic
performance test or whenever you desire to establish a new operating
limit. You must submit the periodic performance test results as
specified in Sec.  60.5420a(b)(9). Combustion control devices meeting
the criteria in either paragraph (b)(5)(ii)(A) or (B) of this section
are not required to conduct periodic performance tests.
    (A) A control device whose model is tested under, and meets the
criteria of paragraph (d) of this section.
    (B) A combustion control device tested under paragraph (b) of this
section that meets the outlet TOC performance level specified in Sec.
60.5412a(a)(1)(ii) or (d)(1)(iv)(B) and that establishes a correlation
between firebox or combustion chamber temperature and the TOC
performance level.
    (c) Control device design analysis to meet the requirements of
Sec.  60.5412a(a)(2) or (d)(2). (1) For a condenser, the design
analysis must include an analysis of the vent stream composition,
constituent concentrations, flowrate, relative humidity, and
temperature, and must establish the design outlet organic compound
concentration level, design average temperature of the condenser
exhaust vent stream, and the design average temperatures of the coolant
fluid at the condenser inlet and outlet.
    (2) For a regenerable carbon adsorption system, the design analysis
shall include the vent stream composition, constituent concentrations,
flowrate, relative humidity, and temperature, and shall establish the
design exhaust vent stream organic compound concentration level,
adsorption cycle time, number and capacity of carbon beds, type and
working capacity of activated carbon used for the carbon beds, design
total regeneration stream flow over the period of each complete carbon
bed regeneration cycle, design carbon bed temperature after
regeneration, design carbon bed regeneration time, and design service
life of the carbon.
    (3) For a nonregenerable carbon adsorption system, such as a carbon
canister, the design analysis shall include the vent stream
composition, constituent concentrations, flowrate, relative humidity,
and temperature, and shall establish the design exhaust vent stream
organic compound concentration level, capacity of the carbon bed, type
and working capacity of activated carbon used for the carbon bed, and
design carbon replacement interval based on the total carbon working
capacity of the control device and source operating schedule. In
addition, these systems shall incorporate dual carbon canisters in case
of emission breakthrough occurring in one canister.
    (4) If you and the Administrator do not agree on a demonstration of
control device performance using a design analysis, then you must
perform a performance test in accordance with the requirements of
paragraph (b) of this section to resolve the disagreement. The
Administrator may choose to have an authorized representative observe
the performance test.
    (d) Performance testing for combustion control devices--
manufacturers' performance test. (1) This paragraph applies to the
performance testing of a combustion control device conducted by the
device manufacturer. The manufacturer must demonstrate that a specific
model of control device achieves the performance requirements in
paragraph (d)(11) of this section by conducting a performance test as
specified in paragraphs (d)(2) through (10) of this section. You must
submit a test report for each combustion control device in accordance
with the requirements in paragraph (d)(12) of this section.
    (2) Performance testing must consist of three 1-hour (or longer)
test runs for each of the four firing rate settings specified in
paragraphs (d)(2)(i) through (iv) of this section, making a total of 12
test runs per test. Propene (propylene) gas must be used for the
testing fuel. All fuel analyses must be performed by an independent
third-party laboratory (not affiliated with the control device
manufacturer or fuel supplier).
    (i) 90-100 percent of maximum design rate (fixed rate).
    (ii) 70-100-70 percent (ramp up, ramp down). Begin the test at 70
percent of the maximum design rate. During the first 5 minutes,
incrementally ramp the firing rate to 100 percent of the maximum design
rate. Hold at 100 percent for 5 minutes. In the 10-15 minute time
range, incrementally ramp back down to 70 percent of the maximum design
rate. Repeat three more times for a total of 60 minutes of sampling.
    (iii) 30-70-30 percent (ramp up, ramp down). Begin the test at 30
percent of the maximum design rate. During the first 5 minutes,
incrementally ramp the firing rate to 70 percent of the maximum design
rate. Hold at 70 percent for 5 minutes. In the 10-15 minute time range,
incrementally ramp back down to 30 percent of the maximum design rate.
Repeat three more times for a total of 60 minutes of sampling.
    (iv) 0-30-0 percent (ramp up, ramp down). Begin the test at the
minimum firing rate. During the first 5 minutes, incrementally ramp the
firing rate to 30 percent of the maximum design rate. Hold at 30
percent for 5 minutes. In the 10-15 minute time range, incrementally
ramp back down to the minimum firing rate. Repeat three more times for
a total of 60 minutes of sampling.
    (3) All models employing multiple enclosures must be tested
simultaneously and with all burners operational. Results must be
reported for each enclosure individually and for the average of the
emissions from all interconnected combustion enclosures/chambers.
Control device operating data must be collected continuously throughout
the performance test using an electronic Data Acquisition System. A
graphic presentation or strip chart of the control device operating
data and emissions test data must be included in the test report in
accordance with paragraph (d)(12) of this section. Inlet fuel meter
data may be manually recorded provided that all inlet fuel data
readings are included in the final report.

    (4) Inlet testing must be conducted as specified in paragraphs
(d)(4)(i) through (ii) of this section.
    (i) The inlet gas flow metering system must be located in
accordance with Method 2A of appendix A-1 of this part (or other
approved procedure) to measure inlet gas flow rate at the control
device inlet location. You must position the fitting for filling fuel
sample containers a minimum of eight pipe diameters upstream of any
inlet gas flow monitoring meter.
    (ii) Inlet flow rate must be determined using Method 2A of appendix
A-1 of this part. Record the start and stop reading for each 60-minute
THC test. Record the gas pressure and temperature at 5-minute intervals
throughout each 60-minute test.
    (5) Inlet gas sampling must be conducted as specified in paragraphs
(d)(5)(i) through (ii) of this section.
    (i) At the inlet gas sampling location, securely connect a
Silonite-coated stainless steel evacuated canister fitted with a flow
controller sufficient to fill the canister over a 3-hour period.
Filling must be conducted as specified in paragraphs (d)(5)(i)(A)
through (C) of this section.
    (A) Open the canister sampling valve at the beginning of each test
run, and close the canister at the end of each test run.
    (B) Fill one canister across the three test runs such that one
composite fuel sample exists for each test condition.
    (C) Label the canisters individually and record sample information
on a chain of custody form.
    (ii) Analyze each inlet gas sample using the methods in paragraphs
(d)(5)(ii)(A) through (C) of this section. You must include the results
in the test report required by paragraph (d)(12) of this section.
    (A) Hydrocarbon compounds containing between one and five atoms of
carbon plus benzene using ASTM D1945-03.
    (B) Hydrogen (H2), carbon monoxide (CO), carbon dioxide
(CO2), nitrogen (N2), oxygen (O2)
using ASTM D1945-03.
    (C) Higher heating value using ASTM D3588-98 or ASTM D4891-89.
    (6) Outlet testing must be conducted in accordance with the
criteria in paragraphs (d)(6)(i) through (v) of this section.
    (i) Sample and flow rate must be measured in accordance with
paragraphs (d)(6)(i)(A) through (B) of this section.
    (A) The outlet sampling location must be a minimum of four
equivalent stack diameters downstream from the highest peak flame or
any other flow disturbance, and a minimum of one equivalent stack
diameter upstream of the exit or any other flow disturbance. A minimum
of two sample ports must be used.
    (B) Flow rate must be measured using Method 1 of appendix A-1 of
this part for determining flow measurement traverse point location, and
Method 2 of appendix A-1 of this part for measuring duct velocity. If
low flow conditions are encountered (i.e., velocity pressure
differentials less than 0.05 inches of water) during the performance
test, a more sensitive manometer must be used to obtain an accurate
flow profile.
    (ii) Molecular weight and excess air must be determined as
specified in paragraph (d)(7) of this section.
    (iii) Carbon monoxide must be determined as specified in paragraph
(d)(8) of this section.
    (iv) THC must be determined as specified in paragraph (d)(9) of
this section.
    (v) Visible emissions must be determined as specified in paragraph
(d)(10) of this section.
    (7) Molecular weight and excess air determination must be performed
as specified in paragraphs (d)(7)(i) through (iii) of this section.
    (i) An integrated bag sample must be collected during the moisture
test required by Method 4 of appendix A-3 of this part following the
procedure specified in (d)(7)(i)(A) and (B) of this section. Analyze
the bag sample using a gas chromatograph-thermal conductivity detector
(GC-TCD) analysis meeting the criteria in paragraphs (d)(7)(i)(C) and
(D) of this section.
    (A) Collect the integrated sample throughout the entire test, and
collect representative volumes from each traverse location.
    (B) Purge the sampling line with stack gas before opening the valve
and beginning to fill the bag. Clearly label each bag and record sample
information on a chain of custody form.
    (C) The bag contents must be vigorously mixed prior to the gas
chromatograph analysis.
    (D) The GC-TCD calibration procedure in Method 3C of appendix A-2
of this part must be modified by using EPA Alt-045 as follows: For the
initial calibration, triplicate injections of any single concentration
must agree within 5 percent of their mean to be valid. The calibration
response factor for a single concentration re-check must be within 10
percent of the original calibration response factor for that
concentration. If this criterion is not met, repeat the initial
calibration using at least three concentration levels.
    (ii) Calculate and report the molecular weight of oxygen, carbon
dioxide, methane, and nitrogen in the integrated bag sample and include
in the test report specified in paragraph (d)(12) of this section.
Moisture must be determined using Method 4 of appendix A-3 of this
part. Traverse both ports with the sampling train required by Method 4
of appendix A-3 of this part during each test run. Ambient air must not
be introduced into the integrated bag sample required by Method 3C of
appendix A-2 of this part during the port change.
    (iii) Excess air must be determined using resultant data from the
EPA Method 3C tests and EPA Method 3B of appendix A-2 of this part,
equation 3B-1, or ASME/ANSI PTC 19.10-1981, Part 10 (manual portion
only) (incorporated by reference as specified in Sec.  60.17).
    (8) Carbon monoxide must be determined using Method 10 of appendix
A-4 of this part. Run the test simultaneously with Method 25A of
appendix A-7 of this part using the same sampling points. An instrument
range of 0-10 parts per million by volume-dry (ppmvd) is recommended.
    (9) Total hydrocarbon determination must be performed as specified
by in paragraphs (d)(9)(i) through (vii) of this section.
    (i) Conduct THC sampling using Method 25A of appendix A-7 of this
part, except that the option for locating the probe in the center 10
percent of the stack is not allowed. The THC probe must be traversed to
16.7 percent, 50 percent, and 83.3 percent of the stack diameter during
each test run.
    (ii) A valid test must consist of three Method 25A tests, each no
less than 60 minutes in duration.
    (iii) A 0-10 parts per million by volume-wet (ppmvw) (as propane)
measurement range is preferred; as an alternative a 0-30 ppmvw (as
carbon) measurement range may be used.
    (iv) Calibration gases must be propane in air and be certified
through EPA Protocol 1--``EPA Traceability Protocol for Assay and
Certification of Gaseous Calibration Standards,'' September 1997, as
amended August 25, 1999, EPA-600/R-97/121 (or more recent if updated
since 1999).
    (v) THC measurements must be reported in terms of ppmvw as propane.
    (vi) THC results must be corrected to 3 percent CO2, as
measured by Method 3C of appendix A-2 of this part. You must use the
following equation for this diluent concentration correction:
[GRAPHIC] [TIFF OMITTED] TP18SE15.006

Where:

Cmeas = The measured concentration of the pollutant.
CO2meas = The measured concentration of the
CO2 diluent.
3 = The corrected reference concentration of CO2 diluent.
Ccorr = The corrected concentration of the pollutant.

    (vii) Subtraction of methane or ethane from the THC data is not
allowed in determining results.
    (10) Visible emissions must be determined using Method 22 of
appendix A-7 of this part. The test must be performed continuously
during each test run. A digital color photograph of the exhaust point,
taken from the position of the observer and annotated with date and
time, must be taken once per test run and the 12 photos included in the
test report specified in paragraph (d)(12) of this section.
    (11) Performance test criteria. (i) The control device model tested
must meet the criteria in paragraphs (d)(11)(i)(A) through (D) of this
section. These criteria must be reported in the test report required by
paragraph (d)(12) of this section.
    (A) Results from Method 22 of appendix A-7 of this part determined
under paragraph (d)(10) of this section with no indication of visible
emissions.
    (B) Average results from Method 25A of appendix A-7 of this part
determined under paragraph (d)(9) of this section equal to or less than
10.0 ppmvw THC as propane corrected to 3.0 percent CO2.
    (C) Average CO emissions determined under paragraph (d)(8) of this
section equal to or less than 10 parts ppmvd, corrected to 3.0 percent
CO2.
    (D) Excess air determined under paragraph (d)(7) of this section
equal to or greater than 150 percent.
    (ii) The manufacturer must determine a maximum inlet gas flow rate
which must not be exceeded for each control device model to achieve the
criteria in paragraph (d)(11)(iii) of this section. The maximum inlet
gas flow rate must be included in the test report required by paragraph
(d)(12) of this section.
    (iii) A control device meeting the criteria in paragraphs
(d)(11)(i)(A) through (D) of this section must demonstrate a
destruction efficiency of 95 percent for methane, if applicable, and
VOC regulated under this subpart.
    (12) The owner or operator of a combustion control device model
tested under this paragraph must submit the information listed in
paragraphs (d)(12)(i) through (vi) in the test report required by this
section in accordance with Sec.  60.5420a(b). Owners or operators who
claim that any of the performance test information being submitted is
confidential business information (CBI) must submit a complete file
including information claimed to be CBI, on a compact disc, flash
drive, or other commonly used electronic storage media to the EPA. The
electronic media must be clearly marked as CBI and mailed to Attn: CBI
Officer; OAQPS CBIO Room 521; 109 T.W. Alexander Drive; RTP, NC 27711.
The same file with the CBI omitted must be submitted to
<EMAIL_ADDRESS>    (i) A full schematic of the control device and dimensions of the
device components.
    (ii) The maximum net heating value of the device.
    (iii) The test fuel gas flow range (in both mass and volume).
Include the maximum allowable inlet gas flow rate.
    (iv) The air/stream injection/assist ranges, if used.
    (v) The test conditions listed in paragraphs (d)(12)(v)(A) through
(O) of this section, as applicable for the tested model.
    (A) Fuel gas delivery pressure and temperature.
    (B) Fuel gas moisture range.
    (C) Purge gas usage range.
    (D) Condensate (liquid fuel) separation range.
    (E) Combustion zone temperature range. This is required for all
devices that measure this parameter.
    (F) Excess air range.
    (G) Flame arrestor(s).
    (H) Burner manifold.
    (I) Pilot flame indicator.
    (J) Pilot flame design fuel and calculated or measured fuel usage.
    (K) Tip velocity range.
    (L) Momentum flux ratio.
    (M) Exit temperature range.
    (N) Exit flow rate.
    (O) Wind velocity and direction.
    (vi) The test report must include all calibration quality
assurance/quality control data, calibration gas values, gas cylinder
certification, strip charts, or other graphic presentations of the data
annotated with test times and calibration values.
    (e) Continuous compliance for combustion control devices tested by
the manufacturer in accordance with paragraph (d) of this section. This
paragraph applies to the demonstration of compliance for a combustion
control device tested under the provisions in paragraph (d) of this
section. Owners or operators must demonstrate that a control device
achieves the performance criteria in paragraph (d)(11) of this section
by installing a device tested under paragraph (d) of this section,
complying with the criteria specified in paragraphs (e)(1) through (7)
of this section, maintaining the records specified in 60.5420a(b) and
submitting the reports specified in 60.5420a(c).
    (1) The inlet gas flow rate must be equal to or less than the
maximum specified by the manufacturer.
    (2) A pilot flame must be present at all times of operation.
    (3) Devices must be operated with no visible emissions, except for
periods not to exceed a total of 1 minute during any 15-minute period.
A visible emissions test conducted according to section 11 of EPA
Method 22 of appendix A-7 of this part must be performed at least once
every calendar month, separated by at least 15 days between each test.
The observation period shall be 15 minutes.
    (4) Devices failing the visible emissions test must follow
manufacturer's repair instructions, if available, or best combustion
engineering practice as outlined in the unit inspection and maintenance
plan, to return the unit to compliant operation. All repairs and
maintenance activities for each unit must be recorded in a maintenance
and repair log and must be available for inspection.
    (5) Following return to operation from maintenance or repair
activity, each device must pass a visual observation according to EPA
Method 22 of appendix A-7 of this part as described in paragraph (e)(3)
of this section.
    (6) If the owner or operator operates a combustion control device
model tested under this section, an electronic copy of the performance
test results required by this section shall be submitted via email to
<EMAIL_ADDRESS>unless the test results for that model of
combustion control device are posted at the following Web site:
epa.gov/airquality/oilandgas/.
    (7) Ensure that each enclosed combustion control device is
maintained in a leak free condition.

Sec.  60.5415a  How do I demonstrate continuous compliance with the
standards for my well, centrifugal compressor, reciprocating
compressor, pneumatic controller, pneumatic pump, storage vessel,
collection of fugitive emissions components at a well site, and
collection of fugitive emissions components at a compressor station,
and affected facilities at onshore natural gas processing plants?

    (a) For each well affected facility, you must demonstrate
continuous compliance by submitting the reports required by Sec.
60.5420a(b) and maintaining the records for each completion operation
specified in Sec.  60.5420a(c)(1).
    (b) For each centrifugal compressor affected facility and each
pneumatic pump affected facility at a location with a control device on
site, you must

demonstrate continuous compliance according to paragraphs (b)(1)
through (3) of this section.
    (1) You must reduce methane and VOC emissions from the wet seal
fluid degassing system and from the pneumatic pump by 95.0 percent or
greater.
    (2) For each control device used to reduce emissions, you must
demonstrate continuous compliance with the performance requirements of
Sec.  60.5412a(a) using the procedures specified in paragraphs
(b)(2)(i) through (vii) of this section. If you use a condenser as the
control device to achieve the requirements specified in Sec.
60.5412a(a)(2), you must demonstrate compliance according to paragraph
(b)(2)(viii) of this section. You may switch between compliance with
paragraphs (b)(2)(i) through (vii) of this section and compliance with
paragraph (b)(2)(viii) of this section only after at least 1 year of
operation in compliance with the selected approach. You must provide
notification of such a change in the compliance method in the next
annual report, as required in Sec.  60.5420a(b), following the change.
    (i) You must operate below (or above) the site specific maximum (or
minimum) parameter value established according to the requirements of
Sec.  60.5417a(f)(1).
    (ii) You must calculate the daily average of the applicable
monitored parameter in accordance with Sec.  60.5417a(e) except that
the inlet gas flow rate to the control device must not be averaged.
    (iii) Compliance with the operating parameter limit is achieved
when the daily average of the monitoring parameter value calculated
under paragraph (b)(2)(ii) of this section is either equal to or
greater than the minimum monitoring value or equal to or less than the
maximum monitoring value established under paragraph (b)(2)(i) of this
section. When performance testing of a combustion control device is
conducted by the device manufacturer as specified in Sec.  60.5413a(d),
compliance with the operating parameter limit is achieved when the
criteria in Sec.  60.5413a(e) are met.
    (iv) You must operate the continuous monitoring system required in
Sec.  60.5417a at all times the affected source is operating, except
for periods of monitoring system malfunctions, repairs associated with
monitoring system malfunctions, and required monitoring system quality
assurance or quality control activities (including, as applicable,
system accuracy audits and required zero and span adjustments). A
monitoring system malfunction is any sudden, infrequent, not reasonably
preventable failure of the monitoring system to provide valid data.
Monitoring system failures that are caused in part by poor maintenance
or careless operation are not malfunctions. You are required to
complete monitoring system repairs in response to monitoring system
malfunctions and to return the monitoring system to operation as
expeditiously as practicable.
    (v) You may not use data recorded during monitoring system
malfunctions, repairs associated with monitoring system malfunctions,
or required monitoring system quality assurance or control activities
in calculations used to report emissions or operating levels. You must
use all the data collected during all other required data collection
periods to assess the operation of the control device and associated
control system.
    (vi) Failure to collect required data is a deviation of the
monitoring requirements, except for periods of monitoring system
malfunctions, repairs associated with monitoring system malfunctions,
and required quality monitoring system quality assurance or quality
control activities (including, as applicable, system accuracy audits
and required zero and span adjustments).
    (vii) If you use a combustion control device to meet the
requirements of Sec.  60.5412a(a) and you demonstrate compliance using
the test procedures specified in Sec.  60.5413a(b), you must comply
with paragraphs (b)(2)(vii)(A) through (D) of this section.
    (A) A pilot flame must be present at all times of operation.
    (B) Devices must be operated with no visible emissions, except for
periods not to exceed a total of 1 minute during any 15-minute period.
A visible emissions test conducted according to section 11 of EPA
Method 22, 40 CFR part 60, appendix A, must be performed at least once
every calendar month, separated by at least 15 days between each test.
The observation period shall be 15 minutes.
    (C) Devices failing the visible emissions test must follow
manufacturer's repair instructions, if available, or best combustion
engineering practice as outlined in the unit inspection and maintenance
plan, to return the unit to compliant operation. All repairs and
maintenance activities for each unit must be recorded in a maintenance
and repair log and must be available for inspection.
    (D) Following return to operation from maintenance or repair
activity, each device must pass a Method 22 of appendix A-7 of this
part visual observation as described in paragraph (b)(2)(vii)(B) of
this section.
    (viii) If you use a condenser as the control device to achieve the
percent reduction performance requirements specified in Sec.
60.5412a(a)(2), you must demonstrate compliance using the procedures in
paragraphs (b)(2)(viii)(A) through (E) of this section.
    (A) You must establish a site-specific condenser performance curve
according to Sec.  60.5417a(f)(2).
    (B) You must calculate the daily average condenser outlet
temperature in accordance with Sec.  60.5417a(e).
    (C) You must determine the condenser efficiency for the current
operating day using the daily average condenser outlet temperature
calculated under paragraph (b)(2)(viii)(B) of this section and the
condenser performance curve established under paragraph (b)(2)(viii)(A)
of this section.
    (D) Except as provided in paragraphs (b)(2)(viii)(D)(1) and (2) of
this section, at the end of each operating day, you must calculate the
365-day rolling average TOC emission reduction, as appropriate, from
the condenser efficiencies as determined in paragraph (b)(2)(viii)(C)
of this section.
    (1) After the compliance dates specified in Sec.  60.5370a, if you
have less than 120 days of data for determining average TOC emission
reduction, you must calculate the average TOC emission reduction for
the first 120 days of operation after the compliance date. You have
demonstrated compliance with the overall 95.0 percent reduction
requirement if the 120-day average TOC emission reduction is equal to
or greater than 95.0 percent.
    (2) After 120 days and no more than 364 days of operation after the
compliance date specified in Sec.  60.5370a, you must calculate the
average TOC emission reduction as the TOC emission reduction averaged
over the number of days between the current day and the applicable
compliance date. You have demonstrated compliance with the overall 95.0
percent reduction requirement if the average TOC emission reduction is
equal to or greater than 95.0 percent.
    (E) If you have data for 365 days or more of operation, you have
demonstrated compliance with the TOC emission reduction if the rolling
365-day average TOC emission reduction calculated in paragraph
(b)(2)(viii)(D) of this section is equal to or greater than 95.0
percent.
    (3) You must submit the annual report required by 60.5420a(b) and
maintain the records as specified in

Sec.  60.5420a(c)(2), (6) through (11), and (16), as applicable.
    (c) For each reciprocating compressor affected facility complying
with Sec.  60.5385a(a)(1) or (2), you must demonstrate continuous
compliance according to paragraphs (c)(1) through (3) of this section.
For each reciprocating compressor affected facility complying with
Sec.  60.5385a(a)(3), you must demonstrate continuous compliance
according to paragraph (c)(4) of this section.
    (1) You must continuously monitor the number of hours of operation
for each reciprocating compressor affected facility or track the number
of months since initial startup, or [date 60 days after publication of
final rule in Federal Register], or the date of the most recent
reciprocating compressor rod packing replacement, whichever is later.
    (2) You must submit the annual report as required in Sec.
60.5420a(b) and maintain records as required in Sec.  60.5420a(c)(3).
    (3) You must replace the reciprocating compressor rod packing
before the total number of hours of operation reaches 26,000 hours or
the number of months since the most recent rod packing replacement
reaches 36 months.
    (4) You must operate the rod packing emissions collection system
under negative pressure and continuously comply with the closed vent
requirements in Sec.  60.5411a(a).
    (d) For each pneumatic controller affected facility, you must
demonstrate continuous compliance according to paragraphs (d)(1)
through (3) of this section.
    (1) You must continuously operate the pneumatic controllers as
required in Sec.  60.5390a(a), (b), or (c).
    (2) You must submit the annual report as required in Sec.
60.5420a(b).
    (3) You must maintain records as required in Sec.  60.5420a(c)(4).
    (e) You must demonstrate continuous compliance according to
paragraph (e)(3) of this section for each storage vessel affected
facility, for which you are using a control device or routing emissions
to a process to meet the requirement of Sec.  60.5395a(a)(2).
    (1)-(2) [Reserved]
    (3) For each storage vessel affected facility, you must comply with
paragraphs (e)(3)(i) and (ii) of this section.
    (i) You must reduce methane and VOC emissions as specified in Sec.
60.5395a(a).
    (ii) For each control device installed to meet the requirements of
Sec.  60.5395a(a), you must demonstrate continuous compliance with the
performance requirements of Sec.  60.5412a(d) for each storage vessel
affected facility using the procedure specified in paragraph
(e)(3)(ii)(A) and either (e)(3)(ii)(B) or (e)(3)(ii)(C) of this
section.
    (A) You must comply with Sec.  60.5416a(c) for each cover and
closed vent system.
    (B) You must comply with Sec.  60.5417a(h) for each control device.
    (C) Each closed vent system that routes emissions to a process must
be operated as specified in Sec.  60.5411a(c)(2).
    (f) For affected facilities at onshore natural gas processing
plants, continuous compliance with methane and VOC requirements is
demonstrated if you are in compliance with the requirements of Sec.
60.5400a.
    (g) For each sweetening unit affected facility at onshore natural
gas processing plants, you must demonstrate continuous compliance with
the standards for SO2 specified in Sec.  60.5405a(b)
according to paragraphs (g)(1) and (2) of this section.
    (1) The minimum required SO2 emission reduction
efficiency (Zc) is compared to the emission reduction
efficiency (R) achieved by the sulfur recovery technology.
    (i) If R >= Zc, your affected facility is in compliance.
    (ii) If R < Zc, your affected facility is not in
compliance.
    (2) The emission reduction efficiency (R) achieved by the sulfur
reduction technology must be determined using the procedures in Sec.
60.5406a(c)(1).
    (h) For each collection of fugitive emissions components at a well
site and each collection of fugitive emissions components at a
compressor station, you must demonstrate continuous compliance with the
fugitive emission standards specified in Sec.  60.5397a according to
paragraphs (h)(1) through (4) of this section.
    (1) You must conduct periodic monitoring surveys as required in
Sec.  60.5397a(f) through (i).
    (2) You must repair or replace each identified source of fugitive
emissions as required in Sec.  60.5397a(j).
    (3) You must maintain records as specified in Sec.
60.5420a(c)(15).
    (4) You must submit annual reports for collection of fugitive
emissions components at a well site and each collection of fugitive
emissions components at a compressor station as required in Sec.
60.5420a(b).

Sec.  60.5416a  What are the initial and continuous cover and closed
vent system inspection and monitoring requirements for my centrifugal
compressor, reciprocating compressor, pneumatic pump and storage vessel
affected facilities?

    For each closed vent system or cover at your storage vessel,
centrifugal compressor, reciprocating compressor and pneumatic pump
affected facilities, you must comply with the applicable requirements
of paragraphs (a) through (c) of this section.
    (a) Inspections for closed vent systems and covers installed on
each centrifugal compressor, reciprocating compressor or pneumatic pump
affected facility. Except as provided in paragraphs (b)(11) and (12) of
this section, you must inspect each closed vent system according to the
procedures and schedule specified in paragraphs (a)(1) and (2) of this
section, inspect each cover according to the procedures and schedule
specified in paragraph (a)(3) of this section, and inspect each bypass
device according to the procedures of paragraph (a)(4) of this section.
    (1) For each closed vent system joint, seam, or other connection
that is permanently or semi-permanently sealed (e.g., a welded joint
between two sections of hard piping or a bolted and gasketed ducting
flange), you must meet the requirements specified in paragraphs
(a)(1)(i) and (ii) of this section.
    (i) Conduct an initial inspection according to the test methods and
procedures specified in paragraph (b) of this section to demonstrate
that the closed vent system operates with no detectable emissions. You
must maintain records of the inspection results as specified in Sec.
60.5420a(c)(6).
    (ii) Conduct annual visual inspections for defects that could
result in air emissions. Defects include, but are not limited to,
visible cracks, holes, or gaps in piping; loose connections; liquid
leaks; or broken or missing caps or other closure devices. You must
monitor a component or connection using the test methods and procedures
in paragraph (b) of this section to demonstrate that it operates with
no detectable emissions following any time the component is repaired or
replaced or the connection is unsealed. You must maintain records of
the inspection results as specified in Sec.  60.5420a(c)(6).
    (2) For closed vent system components other than those specified in
paragraph (a)(1) of this section, you must meet the requirements of
paragraphs (a)(2)(i) through (iii) of this section.
    (i) Conduct an initial inspection according to the test methods and

procedures specified in paragraph (b) of this section to demonstrate
that the closed vent system operates with no detectable emissions. You
must maintain records of the inspection results as specified in Sec.
60.5420a(c)(6).
    (ii) Conduct annual inspections according to the test methods and
procedures specified in paragraph (b) of this section to demonstrate
that the components or connections operate with no detectable
emissions. You must maintain records of the inspection results as
specified in Sec.  60.5420a(c)(6).
    (iii) Conduct annual visual inspections for defects that could
result in air emissions. Defects include, but are not limited to,
visible cracks, holes, or gaps in ductwork; loose connections; liquid
leaks; or broken or missing caps or other closure devices. You must
maintain records of the inspection results as specified in Sec.
60.5420a(c)(6).
    (3) For each cover, you must meet the requirements in paragraphs
(a)(3)(i) and (ii) of this section.
    (i) Conduct visual inspections for defects that could result in air
emissions. Defects include, but are not limited to, visible cracks,
holes, or gaps in the cover, or between the cover and the separator
wall; broken, cracked, or otherwise damaged seals or gaskets on closure
devices; and broken or missing hatches, access covers, caps, or other
closure devices. In the case where the storage vessel is buried
partially or entirely underground, you must inspect only those portions
of the cover that extend to or above the ground surface, and those
connections that are on such portions of the cover (e.g., fill ports,
access hatches, gauge wells, etc.) and can be opened to the atmosphere.
    (ii) You must initially conduct the inspections specified in
paragraph (a)(3)(i) of this section following the installation of the
cover. Thereafter, you must perform the inspection at least once every
calendar year, except as provided in paragraphs (b)(11) and (12) of
this section. You must maintain records of the inspection results as
specified in Sec.  60.5420a(c)(7).
    (4) For each bypass device, except as provided for in Sec.
60.5411a, you must meet the requirements of paragraphs (a)(4)(i) or
(ii) of this section.
    (i) Set the flow indicator to take a reading at least once every 15
minutes at the inlet to the bypass device that could divert the steam
away from the control device to the atmosphere.
    (ii) If the bypass device valve installed at the inlet to the
bypass device is secured in the non-diverting position using a car-seal
or a lock-and-key type configuration, visually inspect the seal or
closure mechanism at least once every month to verify that the valve is
maintained in the non-diverting position and the vent stream is not
diverted through the bypass device. You must maintain records of the
inspections according to Sec.  60.5420a(c)(8).
    (b) No detectable emissions test methods and procedures. If you are
required to conduct an inspection of a closed vent system or cover at
your centrifugal compressor, reciprocating compressor, or pneumatic
pump affected facility as specified in paragraphs (a)(1), (2), or (3)
of this section, you must meet the requirements of paragraphs (b)(1)
through (13) of this section.
    (1) You must conduct the no detectable emissions test procedure in
accordance with Method 21 of appendix A-7 of this part.
    (2) The detection instrument must meet the performance criteria of
Method 21 of appendix A-7 of this part, except that the instrument
response factor criteria in section 8.1.1 of Method 21 must be for the
average composition of the fluid and not for each individual organic
compound in the stream.
    (3) You must calibrate the detection instrument before use on each
day of its use by the procedures specified in Method 21 of appendix A-7
of this part.
    (4) Calibration gases must be as specified in paragraphs (b)(4)(i)
and (ii) of this section.
    (i) Zero air (less than 10 parts per million by volume hydrocarbon
in air).
    (ii) A mixture of methane in air at a concentration less than
10,000 parts per million by volume.
    (5) You may choose to adjust or not adjust the detection instrument
readings to account for the background organic concentration level. If
you choose to adjust the instrument readings for the background level,
you must determine the background level value according to the
procedures in Method 21 of appendix A-7 of this part.
    (6) Your detection instrument must meet the performance criteria
specified in paragraphs (b)(6)(i) and (ii) of this section.
    (i) Except as provided in paragraph (b)(6)(ii) of this section, the
detection instrument must meet the performance criteria of Method 21 of
appendix A-7 of this part, except the instrument response factor
criteria in section 8.1.1 of Method 21 must be for the average
composition of the process fluid, not each individual volatile organic
compound in the stream. For process streams that contain nitrogen, air,
or other inerts that are not organic hazardous air pollutants or
volatile organic compounds, you must calculate the average stream
response factor on an inert-free basis.
    (ii) If no instrument is available that will meet the performance
criteria specified in paragraph (b)(6)(i) of this section, you may
adjust the instrument readings by multiplying by the average response
factor of the process fluid, calculated on an inert-free basis, as
described in paragraph (b)(6)(i) of this section.
    (7) You must determine if a potential leak interface operates with
no detectable emissions using the applicable procedure specified in
paragraph (b)(7)(i) or (ii) of this section.
    (i) If you choose not to adjust the detection instrument readings
for the background organic concentration level, then you must directly
compare the maximum organic concentration value measured by the
detection instrument to the applicable value for the potential leak
interface as specified in paragraph (b)(8) of this section.
    (ii) If you choose to adjust the detection instrument readings for
the background organic concentration level, you must compare the value
of the arithmetic difference between the maximum organic concentration
value measured by the instrument and the background organic
concentration value as determined in paragraph (b)(5) of this section
with the applicable value for the potential leak interface as specified
in paragraph (b)(8) of this section.
    (8) A potential leak interface is determined to operate with no
detectable organic emissions if the organic concentration value
determined in paragraph (b)(7) of this section is less than 500 parts
per million by volume.
    (9) Repairs. In the event that a leak or defect is detected, you
must repair the leak or defect as soon as practicable according to the
requirements of paragraphs (b)(9)(i) and (ii) of this section, except
as provided in paragraph (b)(10) of this section.
    (i) A first attempt at repair must be made no later than 5 calendar
days after the leak is detected.
    (ii) Repair must be completed no later than 15 calendar days after
the leak is detected.
    (10) Delay of repair. Delay of repair of a closed vent system or
cover for which leaks or defects have been detected is allowed if the
repair is technically infeasible without a shutdown, or if you
determine that emissions resulting from immediate repair would be
greater than the fugitive emissions likely to result from delay of
repair. You must complete repair of such equipment by the end of the
next shutdown.
    (11) Unsafe to inspect requirements. You may designate any parts of
the

closed vent system or cover as unsafe to inspect if the requirements in
paragraphs (b)(11)(i) and (ii) of this section are met. Unsafe to
inspect parts are exempt from the inspection requirements of paragraphs
(a)(1) through (3) of this section.
    (i) You determine that the equipment is unsafe to inspect because
inspecting personnel would be exposed to an imminent or potential
danger as a consequence of complying with paragraphs (a)(1), (2), or
(3) of this section.
    (ii) You have a written plan that requires inspection of the
equipment as frequently as practicable during safe-to-inspect times.
    (12) Difficult to inspect requirements. You may designate any parts
of the closed vent system or cover as difficult to inspect, if the
requirements in paragraphs (b)(12)(i) and (ii) of this section are met.
Difficult to inspect parts are exempt from the inspection requirements
of paragraphs (a)(1) through (3) of this section.
    (i) You determine that the equipment cannot be inspected without
elevating the inspecting personnel more than 2 meters above a support
surface.
    (ii) You have a written plan that requires inspection of the
equipment at least once every 5 years.
    (13) Records. Records shall be maintained as specified in this
section and in Sec.  60.5420a(c)(9).
    (c) Cover and closed vent system inspections for storage vessel
affected facilities. If you install a control device or route emissions
to a process, you must inspect each closed vent system according to the
procedures and schedule specified in paragraphs (c)(1) of this section,
inspect each cover according to the procedures and schedule specified
in paragraph (c)(2) of this section, and inspect each bypass device
according to the procedures of paragraph (c)(3) of this section. You
must also comply with the requirements of (c)(4) through (7) of this
section.
    (1) For each closed vent system, you must conduct an inspection at
least once every calendar month as specified in paragraphs (c)(1)(i)
through (iii) of this section.
    (i) You must maintain records of the inspection results as
specified in Sec.  60.5420a(c)(6).
    (ii) Conduct olfactory, visual and auditory inspections for defects
that could result in air emissions. Defects include, but are not
limited to, visible cracks, holes, or gaps in piping; loose
connections; liquid leaks; or broken or missing caps or other closure
devices.
    (iii) Monthly inspections must be separated by at least 14 calendar
days.
    (2) For each cover, you must conduct inspections at least once
every calendar month as specified in paragraphs (c)(2)(i) through (iii)
of this section.
    (i) You must maintain records of the inspection results as
specified in Sec.  60.5420a(c)(7).
    (ii) Conduct olfactory, visual and auditory inspections for defects
that could result in air emissions. Defects include, but are not
limited to, visible cracks, holes, or gaps in the cover, or between the
cover and the separator wall; broken, cracked, or otherwise damaged
seals or gaskets on closure devices; and broken or missing hatches,
access covers, caps, or other closure devices. In the case where the
storage vessel is buried partially or entirely underground, you must
inspect only those portions of the cover that extend to or above the
ground surface, and those connections that are on such portions of the
cover (e.g., fill ports, access hatches, gauge wells, etc.) and can be
opened to the atmosphere.
    (iii) Monthly inspections must be separated by at least 14 calendar
days.
    (3) For each bypass device, except as provided for in Sec.
60.5411a(c)(3)(ii), you must meet the requirements of paragraphs
(c)(3)(i) or (ii) of this section.
    (i) You must properly install, calibrate and maintain a flow
indicator at the inlet to the bypass device that could divert the
stream away from the control device or process to the atmosphere. Set
the flow indicator to trigger an audible and visible alarm, and
initiate notification via remote alarm to the nearest field office,
when the bypass device is open such that the stream is being, or could
be, diverted away from the control device or process to the atmosphere.
You must maintain records of each time the alarm is sounded according
to Sec.  60.5420a(c)(8).
    (ii) If the bypass device valve installed at the inlet to the
bypass device is secured in the non-diverting position using a car-seal
or a lock-and-key type configuration, visually inspect the seal or
closure mechanism at least once every month to verify that the valve is
maintained in the non-diverting position and the vent stream is not
diverted through the bypass device. You must maintain records of the
inspections and records of each time the key is checked out, if
applicable, according to Sec.  60.5420a(c)(8).
    (4) Repairs. In the event that a leak or defect is detected, you
must repair the leak or defect as soon as practicable according to the
requirements of paragraphs (c)(4)(i) through (iii) of this section,
except as provided in paragraph (c)(5) of this section.
    (i) A first attempt at repair must be made no later than 5 calendar
days after the leak is detected.
    (ii) Repair must be completed no later than 30 calendar days after
the leak is detected.
    (iii) Grease or another applicable substance must be applied to
deteriorating or cracked gaskets to improve the seal while awaiting
repair.
    (5) Delay of repair. Delay of repair of a closed vent system or
cover for which leaks or defects have been detected is allowed if the
repair is technically infeasible without a shutdown, or if you
determine that emissions resulting from immediate repair would be
greater than the fugitive emissions likely to result from delay of
repair. You must complete repair of such equipment by the end of the
next shutdown.
    (6) Unsafe to inspect requirements. You may designate any parts of
the closed vent system or cover as unsafe to inspect if the
requirements in paragraphs (c)(6)(i) and (ii) of this section are met.
Unsafe to inspect parts are exempt from the inspection requirements of
paragraphs (c)(1) and (2) of this section.
    (i) You determine that the equipment is unsafe to inspect because
inspecting personnel would be exposed to an imminent or potential
danger as a consequence of complying with paragraphs (c)(1) or (2) of
this section.
    (ii) You have a written plan that requires inspection of the
equipment as frequently as practicable during safe-to-inspect times.
    (7) Difficult to inspect requirements. You may designate any parts
of the closed vent system or cover as difficult to inspect, if the
requirements in paragraphs (c)(7)(i) and (ii) of this section are met.
Difficult to inspect parts are exempt from the inspection requirements
of paragraphs (c)(1) and (2) of this section.
    (i) You determine that the equipment cannot be inspected without
elevating the inspecting personnel more than 2 meters above a support
surface.
    (ii) You have a written plan that requires inspection of the
equipment at least once every 5 years.

Sec.  60.5417a  What are the continuous control device monitoring
requirements for my centrifugal compressor, pneumatic pump, and storage
vessel affected facilities?

    You must meet the applicable requirements of this section to
demonstrate continuous compliance for each control device used to meet
emission standards for your storage vessel, centrifugal compressor or
pneumatic pump affected facility.

    (a) For each control device used to comply with the emission
reduction standard for centrifugal compressor affected facilities in
Sec.  60.5380a(a)(1) or the emission reduction standard for pneumatic
pumps affected facilities in Sec.  60.5393a(b)(1), you must install and
operate a continuous parameter monitoring system for each control
device as specified in paragraphs (c) through (g) of this section,
except as provided for in paragraph (b) of this section. If you install
and operate a flare in accordance with Sec.  60.5412a(a)(3), you are
exempt from the requirements of paragraphs (e) and (f) of this section.
    (b) You are exempt from the monitoring requirements specified in
paragraphs (c) through (g) of this section for the control devices
listed in paragraphs (b)(1) and (2) of this section.
    (1) A boiler or process heater in which all vent streams are
introduced with the primary fuel or are used as the primary fuel.
    (2) A boiler or process heater with a design heat input capacity
equal to or greater than 44 megawatts.
    (c) If you are required to install a continuous parameter
monitoring system, you must meet the specifications and requirements in
paragraphs (c)(1) through (4) of this section.
    (1) Each continuous parameter monitoring system must measure data
values at least once every hour and record the parameters in paragraphs
(c)(1)(i) or (ii) of this section.
    (i) Each measured data value.
    (ii) Each block average value for each 1-hour period or shorter
periods calculated from all measured data values during each period. If
values are measured more frequently than once per minute, a single
value for each minute may be used to calculate the hourly (or shorter
period) block average instead of all measured values.
    (2) You must prepare a site-specific monitoring plan that addresses
the monitoring system design, data collection, and the quality
assurance and quality control elements outlined in paragraphs (c)(2)(i)
through (v) of this section. You must install, calibrate, operate, and
maintain each continuous parameter monitoring system in accordance with
the procedures in your approved site-specific monitoring plan.
    (i) The performance criteria and design specifications for the
monitoring system equipment, including the sample interface, detector
signal analyzer, and data acquisition and calculations.
    (ii) Sampling interface (e.g., thermocouple) location such that the
monitoring system will provide representative measurements.
    (iii) Equipment performance checks, system accuracy audits, or
other audit procedures.
    (iv) Ongoing operation and maintenance procedures in accordance
with provisions in Sec.  60.13(b).
    (v) Ongoing reporting and recordkeeping procedures in accordance
with provisions in Sec.  60.7(c), (d), and (f).
    (3) You must conduct the continuous parameter monitoring system
equipment performance checks, system accuracy audits, or other audit
procedures specified in the site-specific monitoring plan at least once
every 12 months.
    (4) You must conduct a performance evaluation of each continuous
parameter monitoring system in accordance with the site-specific
monitoring plan.
    (d) You must install, calibrate, operate, and maintain a device
equipped with a continuous recorder to measure the values of operating
parameters appropriate for the control device as specified in paragraph
(d)(1), (2), or (3) of this section.
    (1) A continuous monitoring system that measures the operating
parameters in paragraphs (d)(1)(i) through (viii) of this section, as
applicable.
    (i) For a thermal vapor incinerator that demonstrates during the
performance test conducted under Sec.  60.5413a that combustion zone
temperature is an accurate indicator of performance, a temperature
monitoring device equipped with a continuous recorder. The monitoring
device must have a minimum accuracy of 1 percent of the
temperature being monitored in [deg]C, or 2.5 [deg]C,
whichever value is greater. You must install the temperature sensor at
a location representative of the combustion zone temperature.
    (ii) For a catalytic vapor incinerator, a temperature monitoring
device equipped with a continuous recorder. The device must be capable
of monitoring temperature at two locations and have a minimum accuracy
of 1 percent of the temperature being monitored in [deg]C,
or 2.5 [deg]C, whichever value is greater. You must install
one temperature sensor in the vent stream at the nearest feasible point
to the catalyst bed inlet, and you must install a second temperature
sensor in the vent stream at the nearest feasible point to the catalyst
bed outlet.
    (iii) For a flare, a heat sensing monitoring device equipped with a
continuous recorder that indicates the continuous ignition of the pilot
flame.
    (iv) For a boiler or process heater, a temperature monitoring
device equipped with a continuous recorder. The temperature monitoring
device must have a minimum accuracy of 1 percent of the
temperature being monitored in [deg]C, or 2.5 [deg]C,
whichever value is greater. You must install the temperature sensor at
a location representative of the combustion zone temperature.
    (v) For a condenser, a temperature monitoring device equipped with
a continuous recorder. The temperature monitoring device must have a
minimum accuracy of 1 percent of the temperature being
monitored in [deg]C, or 2.5 [deg]C, whichever value is
greater. You must install the temperature sensor at a location in the
exhaust vent stream from the condenser.
    (vi) For a regenerative-type carbon adsorption system, a continuous
monitoring system that meets the specifications in paragraphs
(d)(1)(vi)(A) and (B) of this section.
    (A) The continuous parameter monitoring system must measure and
record the average total regeneration stream mass flow or volumetric
flow during each carbon bed regeneration cycle. The flow sensor must
have a measurement sensitivity of 5 percent of the flow rate or 10
cubic feet per minute, whichever is greater. You must check the
mechanical connections for leakage at least every month, and you must
perform a visual inspection at least every 3 months of all components
of the flow continuous parameter monitoring system for physical and
operational integrity and all electrical connections for oxidation and
galvanic corrosion if your flow continuous parameter monitoring system
is not equipped with a redundant flow sensor; and
    (B) The continuous parameter monitoring system must measure and
record the average carbon bed temperature for the duration of the
carbon bed steaming cycle and measure the actual carbon bed temperature
after regeneration and within 15 minutes of completing the cooling
cycle. The temperature monitoring device must have a minimum accuracy
of 1 percent of the temperature being monitored in [deg]C,
or 2.5 [deg]C, whichever value is greater.
    (vii) For a nonregenerative-type carbon adsorption system, you must
monitor the design carbon replacement interval established using a
design analysis performed as specified in Sec.  60.5413a(c)(3). The
design carbon replacement interval must be based on the total carbon
working capacity of the control device and source operating schedule.
    (viii) For a combustion control device whose model is tested under
Sec.  60.5413a(d), a continuous monitoring system meeting the
requirements of

paragraphs (d)(1)(viii)(A) and (B) of this section.
    (A) The continuous monitoring system must measure gas flow rate at
the inlet to the control device. The monitoring instrument must have an
accuracy of 2 percent or better. The flow rate at the inlet
to the combustion device must not exceed the maximum or be less than
the minimum flow rate determined by the manufacturer.
    (B) A monitoring device that continuously indicates the presence of
the pilot flame while emissions are routed to the control device.
    (2) An organic monitoring device equipped with a continuous
recorder that measures the concentration level of organic compounds in
the exhaust vent stream from the control device. The monitor must meet
the requirements of Performance Specification 8 or 9 of appendix B of
this part. You must install, calibrate, and maintain the monitor
according to the manufacturer's specifications.
    (3) A continuous monitoring system that measures operating
parameters other than those specified in paragraph (d)(1) or (2) of
this section, upon approval of the Administrator as specified in Sec.
60.13(i).
    (e) You must calculate the daily average value for each monitored
operating parameter for each operating day, using the data recorded by
the monitoring system, except for inlet gas flow rate. If the emissions
unit operation is continuous, the operating day is a 24-hour period. If
the emissions unit operation is not continuous, the operating day is
the total number of hours of control device operation per 24-hour
period. Valid data points must be available for 75 percent of the
operating hours in an operating day to compute the daily average.
    (f) For each operating parameter monitor installed in accordance
with the requirements of paragraph (d) of this section, you must comply
with paragraph (f)(1) of this section for all control devices. When
condensers are installed, you must also comply with paragraph (f)(2) of
this section.
    (1) You must establish a minimum operating parameter value or a
maximum operating parameter value, as appropriate for the control
device, to define the conditions at which the control device must be
operated to continuously achieve the applicable performance
requirements of Sec.  60.5412a(a). You must establish each minimum or
maximum operating parameter value as specified in paragraphs (f)(1)(i)
through (iii) of this section.
    (i) If you conduct performance tests in accordance with the
requirements of Sec.  60.5413a(b) to demonstrate that the control
device achieves the applicable performance requirements specified in
Sec.  60.5412a(a), then you must establish the minimum operating
parameter value or the maximum operating parameter value based on
values measured during the performance test and supplemented, as
necessary, by a condenser design analysis or control device
manufacturer recommendations or a combination of both.
    (ii) If you use a condenser design analysis in accordance with the
requirements of Sec.  60.5413a(c) to demonstrate that the control
device achieves the applicable performance requirements specified in
Sec.  60.5412a(a), then you must establish the minimum operating
parameter value or the maximum operating parameter value based on the
condenser design analysis and supplemented, as necessary, by the
condenser manufacturer's recommendations.
    (iii) If you operate a control device where the performance test
requirement was met under Sec.  60.5413a(d) to demonstrate that the
control device achieves the applicable performance requirements
specified in Sec.  60.5412a(a), then your control device inlet gas flow
rate must not exceed the maximum or be less than the minimum inlet gas
flow rate determined by the manufacturer.
    (2) If you use a condenser as specified in paragraph (d)(1)(v) of
this section, you must establish a condenser performance curve showing
the relationship between condenser outlet temperature and condenser
control efficiency, according to the requirements of paragraphs
(f)(2)(i) and (ii) of this section.
    (i) If you conduct a performance test in accordance with the
requirements of Sec.  60.5413a(b) to demonstrate that the condenser
achieves the applicable performance requirements in Sec.  60.5412a(a),
then the condenser performance curve must be based on values measured
during the performance test and supplemented as necessary by control
device design analysis, or control device manufacturer's
recommendations, or a combination or both.
    (ii) If you use a control device design analysis in accordance with
the requirements of Sec.  60.5413a(c)(1) to demonstrate that the
condenser achieves the applicable performance requirements specified in
Sec.  60.5412a(a), then the condenser performance curve must be based
on the condenser design analysis and supplemented, as necessary, by the
control device manufacturer's recommendations.
    (g) A deviation for a given control device is determined to have
occurred when the monitoring data or lack of monitoring data result in
any one of the criteria specified in paragraphs (g)(1) through (g)(6)
of this section being met. If you monitor multiple operating parameters
for the same control device during the same operating day and more than
one of these operating parameters meets a deviation criterion specified
in paragraphs (g)(1) through (6) of this section, then a single
excursion is determined to have occurred for the control device for
that operating day.
    (1) A deviation occurs when the daily average value of a monitored
operating parameter is less than the minimum operating parameter limit
(or, if applicable, greater than the maximum operating parameter limit)
established in paragraph (f)(1) of this section.
    (2) If you are subject to Sec.  60.5412a(a)(2), a deviation occurs
when the 365-day average condenser efficiency calculated according to
the requirements specified in Sec.  60.5415a(b)(2)(viii)(D) is less
than 95.0 percent.
    (3) If you are subject to Sec.  60.5412a(a)(2) and you have less
than 365 days of data, a deviation occurs when the average condenser
efficiency calculated according to the procedures specified in Sec.
60.5415a(b)(2)(viii)(D)(1) or (2) is less than 95.0 percent.
    (4) A deviation occurs when the monitoring data are not available
for at least 75 percent of the operating hours in a day.
    (5) If the closed vent system contains one or more bypass devices
that could be used to divert all or a portion of the gases, vapors, or
fumes from entering the control device, a deviation occurs when the
requirements of paragraph (g)(5)(i) or (ii) of this section are met.
    (i) For each bypass line subject to Sec.  60.5411a(a)(3)(i)(A), the
flow indicator indicates that flow has been detected and that the
stream has been diverted away from the control device to the
atmosphere.
    (ii) For each bypass line subject to Sec.  60.5411a(a)(3)(i)(B), if
the seal or closure mechanism has been broken, the bypass line valve
position has changed, the key for the lock-and-key type lock has been
checked out, or the car-seal has broken.
    (6) For a combustion control device whose model is tested under
Sec.  60.5413a(d), a deviation occurs when the conditions of paragraphs
(g)(6)(i) or (ii) are met.

    (i) The inlet gas flow rate exceeds the maximum established during
the test conducted under Sec.  60.5413a(d).
    (ii) Failure of the monthly visible emissions test conducted under
Sec.  60.5413a(e)(3) occurs.
    (h) For each control device used to comply with the emission
reduction standard in Sec.  60.5395a(a)(2) for your storage vessel
affected facility, you must demonstrate continuous compliance according
to paragraphs (h)(1) through (h)(4) of this section. You are exempt
from the requirements of this paragraph if you install a control device
model tested in accordance with Sec.  60.5413a(d)(2) through (10),
which meets the criteria in Sec.  60.5413a(d)(11), the reporting
requirement in Sec.  60.5413a(d)(12), and meet the continuous
compliance requirement in Sec.  60.5413a(e).
    (1) For each combustion device you must conduct inspections at
least once every calendar month according to paragraphs (h)(1)(i)
through (iv) of this section. Monthly inspections must be separated by
at least 14 calendar days.
    (i) Conduct visual inspections to confirm that the pilot is lit
when vapors are being routed to the combustion device and that the
continuous burning pilot flame is operating properly.
    (ii) Conduct inspections to monitor for visible emissions from the
combustion device using section 11 of EPA Method 22 of appendix A of
this part. The observation period shall be 15 minutes. Devices must be
operated with no visible emissions, except for periods not to exceed a
total of 1 minute during any 15 minute period.
    (iii) Conduct olfactory, visual and auditory inspections of all
equipment associated with the combustion device to ensure system
integrity.
    (iv) For any absence of the pilot flame, or other indication of
smoking or improper equipment operation (e.g., visual, audible, or
olfactory), you must ensure the equipment is returned to proper
operation as soon as practicable after the event occurs. At a minimum,
you must perform the procedures specified in paragraphs (h)(1)(iv)(A)
and (B) of this section.
    (A) You must check the air vent for obstruction. If an obstruction
is observed, you must clear the obstruction as soon as practicable.
    (B) You must check for liquid reaching the combustor.
    (2) For each vapor recovery device, you must conduct inspections at
least once every calendar month to ensure physical integrity of the
control device according to the manufacturer's instructions. Monthly
inspections must be separated by at least 14 calendar days.
    (3) Each control device must be operated following the
manufacturer's written operating instructions, procedures and
maintenance schedule to ensure good air pollution control practices for
minimizing emissions. Records of the manufacturer's written operating
instructions, procedures, and maintenance schedule must be available
for inspection as specified in Sec.  60.5420a(c)(13).
    (4) Conduct a periodic performance test no later than 60 months
after the initial performance test as specified in Sec.
60.5413a(b)(5)(ii) and conduct subsequent periodic performance tests at
intervals no longer than 60 months following the previous periodic
performance test.

Sec.  60.5420a  What are my notification, reporting, and recordkeeping
requirements?

    (a) You must submit the notifications according to paragraphs
(a)(1) and (2) of this section if you own or operate one or more of the
affected facilities specified in Sec.  60.5365a that was constructed,
modified, or reconstructed during the reporting period.
    (1) If you own or operate a well, centrifugal compressor,
reciprocating compressor, pneumatic controller, pneumatic pump, storage
vessel, or collection of fugitive emissions components at a well site
or collection of fugitive emissions components at a compressor station
you are not required to submit the notifications required in Sec.
60.7(a)(1), (3), and (4).
    (2)(i) If you own or operate a well affected facility, you must
submit a notification to the Administrator no later than 2 days prior
to the commencement of each well completion operation listing the
anticipated date of the well completion operation. The notification
shall include contact information for the owner or operator; the API
well number; the latitude and longitude coordinates for each well in
decimal degrees to an accuracy and precision of five (5) decimals of a
degree using the North American Datum of 1983; and the planned date of
the beginning of flowback. You may submit the notification in writing
or in electronic format.
    (ii) If you are subject to state regulations that require advance
notification of well completions and you have met those notification
requirements, then you are considered to have met the advance
notification requirements of paragraph (a)(2)(i) of this section.
    (b) Reporting requirements. You must submit annual reports
containing the information specified in paragraphs (b)(1) through (8)
of this section and performance test reports as specified in paragraph
(b)(9) or (10) of this section. You must submit annual reports
following the procedure specified in paragraph (b)(11). The initial
annual report is due no later than 90 days after the end of the initial
compliance period as determined according to Sec.  60.5410a. Subsequent
annual reports are due no later than same date each year as the initial
annual report. If you own or operate more than one affected facility,
you may submit one report for multiple affected facilities provided the
report contains all of the information required as specified in
paragraphs (b)(1) through (10) of this section. Annual reports may
coincide with title V reports as long as all the required elements of
the annual report are included. You may arrange with the Administrator
a common schedule on which reports required by this part may be
submitted as long as the schedule does not extend the reporting period.
    (1) The general information specified in paragraphs (b)(1)(i)
through (iv) of this section for all reports.
    (i) The company name and address of the affected facility.
    (ii) An identification of each affected facility being included in
the annual report.
    (iii) Beginning and ending dates of the reporting period.
    (iv) A certification by a certifying official of truth, accuracy,
and completeness. This certification shall state that, based on
information and belief formed after reasonable inquiry, the statements
and information in the document are true, accurate, and complete.
    (2) For each well affected facility, the information in paragraphs
(b)(2)(i) and (ii) of this section.
    (i) Records of each well completion operation as specified in
paragraph (c)(1)(i) through (iv) of this section for each well affected
facility conducted during the reporting period. In lieu of submitting
the records specified in paragraph (c)(1)(i) through (iv), the owner or
operator may submit a list of the well completions with hydraulic
fracturing completed during the reporting period and the records
required by paragraph (c)(1)(v) of this section for each well
completion.
    (ii) Records of deviations specified in paragraph (c)(1)(ii) of
this section that occurred during the reporting period.
    (3) For each centrifugal compressor affected facility, the
information

specified in paragraphs (b)(3)(i) through (iv) of this section.
    (i) An identification of each centrifugal compressor using a wet
seal system constructed, modified or reconstructed during the reporting
period.
    (ii) Records of deviations specified in paragraph (c)(2) of this
section that occurred during the reporting period.
    (iii) If required to comply with Sec.  60.5380a(a)(2), the records
specified in paragraphs (c)(6) through (11) of this section.
    (iv) If complying with Sec.  60.5380a(a)(1) with a control device
tested under Sec.  60.5413a(d) which meets the criteria in Sec.
60.5413a(d)(11) and Sec.  60.5413a(e), records specified in paragraph
(c)(2)(i) through (c)(2)(vii) of this section for each centrifugal
compressor using a wet seal system constructed, modified or
reconstructed during the reporting period.
    (4) For each reciprocating compressor affected facility, the
information specified in paragraphs (b)(4)(i) and (ii) of this section.
    (i) The cumulative number of hours of operation or the number of
months since initial startup, since [date 60 days after publication of
final rule in the Federal Register], or since the previous
reciprocating compressor rod packing replacement, whichever is later.
    (ii) Records of deviations specified in paragraph (c)(3)(iii) of
this section that occurred during the reporting period.
    (5) For each pneumatic controller affected facility, the
information specified in paragraphs (b)(5)(i) through (iii) of this
section.
    (i) An identification of each pneumatic controller constructed,
modified or reconstructed during the reporting period, including the
identification information specified in Sec.  60.5390a(b)(2) or (c)(2).
    (ii) If applicable, documentation that the use of pneumatic
controller affected facilities with a natural gas bleed rate greater
than 6 standard cubic feet per hour are required and the reasons why.
    (iii) Records of deviations specified in paragraph (c)(4)(v) of
this section that occurred during the reporting period.
    (6) For each storage vessel affected facility, the information in
paragraphs (b)(6)(i) through (vii) of this section.
    (i) An identification, including the location, of each storage
vessel affected facility for which construction, modification or
reconstruction commenced during the reporting period. The location of
the storage vessel shall be in latitude and longitude coordinates in
decimal degrees to an accuracy and precision of five (5) decimals of a
degree using the North American Datum of 1983.
    (ii) Documentation of the VOC emission rate determination according
to Sec.  60.5365a(e) for each storage vessel that became an affected
facility during the reporting period or is returned to service during
the reporting period.
    (iii) Records of deviations specified in paragraph (c)(5)(iii) of
this section that occurred during the reporting period.
    (iv) A statement that you have met the requirements specified in
Sec.  60.5410a(h)(2) and (3).
    (v) You must identify each storage vessel affected facility that is
removed from service during the reporting period as specified in Sec.
60.5395a(c)(1)(ii), including the date the storage vessel affected
facility was removed from service.
    (vi) You must identify each storage vessel affected facility
returned to service during the reporting period as specified in Sec.
60.5395a(c)(3), including the date the storage vessel affected facility
was returned to service.
    (vii) If complying with Sec.  60.5395a(a)(2) with a control device
tested under Sec.  60.5413a(d) which meets the criteria in Sec.
60.5413a(d)(11) and Sec.  60.5413a(e), records specified in paragraphs
(c)(5)(vi)(A) through (G) of this section for each storage vessel
constructed, modified, reconstructed or returned to service during the
reporting period.
    (7) For the collection of fugitive emissions components at a well
site and the collection of fugitive emissions components at a
compressor station, the records of each monitoring survey conducted
during the year:
    (i) Date of the survey.
    (ii) Beginning and end time of the survey.
    (iii) Name of operator(s) performing survey. If the survey is
performed by optical gas imaging, you must note the training and
experience of the operator.
    (iv) Ambient temperature, sky conditions, and maximum wind speed at
the time of the survey.
    (v) Any deviations from the monitoring plan or a statement that
there were no deviations from the monitoring plan.
    (vi) Documentation of each fugitive emission, including the
information specified in paragraphs (b)(7)(vi)(A) through (C) of this
section
    (A) Location.
    (B) One or more digital photographs of each required monitoring
survey being performed. The digital photograph must include the date
the photograph was taken and the latitude and longitude of the
collection of fugitive emissions components at a well site or
collection of fugitive emissions components at a compressor station
imbedded within or stored with the digital file. As an alternative to
imbedded latitude and longitude within the digital photograph, the
digital photograph may consist of a photograph of the monitoring survey
being performed with a photograph of a separately operating GIS device
within the same digital picture, provided the latitude and longitude
output of the GIS unit can be clearly read in the digital photograph.
    (C) The date of successful repair of the fugitive emissions
component.
    (D) Type of instrument used to resurvey a repaired fugitive
emissions component that could not be repaired during the initial
fugitive emissions finding.
    (8) For each pneumatic pump affected facility, the information
specified in paragraphs (b)(8)(i) through (v) of this section.
    (i) In the initial annual report, a certification that there is no
control device on site, if applicable.
    (ii) An identification of each pneumatic pump constructed, modified
or reconstructed during the reporting period, including the
identification information specified in Sec.  60.5393a(a)(2) or (b)(2).
    (iii) An identification of any sites which contain natural
pneumatic pumps and which installed a control device during the
reporting period, where there was no control device previously at the
site.
    (iv) Records of deviations specified in paragraph (c)(16)(ii) of
this section that occurred during the reporting period.
    (v) If complying with Sec.  60.5393a(b)(1) with a control device
tested under Sec.  60.5413(d), which meets the criteria in Sec.
60.5413(d)(11) and Sec.  60.5413(e), records specified in paragraphs
(c)(16)(iv)(A) through (G) of this section for each pneumatic pump
constructed, modified or reconstructed during the reporting period.
    (9) Within 60 days after the date of completing each performance
test (see Sec.  60.8) required by this subpart, except testing
conducted by the manufacturer as specified in Sec.  60.5413a(d), you
must submit the results of the performance test following the procedure
specified in either paragraph (b)(9)(i) or (ii) of this section.
    (i) For data collected using test methods supported by the EPA's
Electronic Reporting Tool (ERT) as listed on the EPA's ERT Web site
(http://www.epa.gov/ttn/chief/ert/index.html) at the time of the test,
you must submit the results of the performance test to the EPA via the

Compliance and Emissions Data Reporting Interface (CEDRI). (CEDRI can
be accessed through the EPA's Central Data Exchange (CDX) (https://cdx.epa.gov/).) Performance test data must be submitted in a file
format generated through the use of the EPA's ERT or an alternate
electronic file format consistent with the extensible markup language
(XML) schema listed on the EPA's ERT Web site. If you claim that some
of the performance test information being submitted is confidential
business information (CBI), you must submit a complete file generated
through the use of the EPA's ERT or an alternate electronic file
consistent with the XML schema listed on the EPA's ERT Web site,
including information claimed to be CBI, on a compact disc, flash
drive, or other commonly used electronic storage media to the EPA. The
electronic media must be clearly marked as CBI and mailed to U.S. EPA/
OAQPS/CORE CBI Office, Attention: Group Leader, Measurement Policy
Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same ERT or
alternate file with the CBI omitted must be submitted to the EPA via
the EPA's CDX as described earlier in this paragraph.
    (ii) For data collected using test methods that are not supported
by the EPA's ERT as listed on the EPA's ERT Web site at the time of the
test, you must submit the results of the performance test to the
Administrator at the appropriate address listed in Sec.  60.4.
    (10) For combustion control devices tested by the manufacturer in
accordance with Sec.  60.5413a(d), an electronic copy of the
performance test results required by Sec.  60.5413a(d) shall be
submitted via email to<EMAIL_ADDRESS>unless the test results
for that model of combustion control device are posted at the following
Web site: epa.gov/airquality/oilandgas/.
    (11) You must submit reports to the EPA via the CEDRI. (CEDRI can
be accessed through the EPA's CDX (https://cdx.epa.gov/).) You must use
the appropriate electronic report in CEDRI for this subpart or an
alternate electronic file format consistent with the extensible markup
language (XML) schema listed on the CEDRI Web site (http://www.epa.gov/ttn/chief/cedri/index.html). If the reporting form specific to this
subpart is not available in CEDRI at the time that the report is due,
you must submit the report to the Administrator at the appropriate
address listed in Sec.  60.4. You must begin submitting reports via
CEDRI no later than 90 days after the form becomes available in CEDRI.
The reports must be submitted by the deadlines specified in this
subpart, regardless of the method in which the reports are submitted.
    (c) Recordkeeping requirements. You must maintain the records
identified as specified in Sec.  60.7(f) and in paragraphs (c)(1)
through (16) of this section. All records required by this subpart must
be maintained either onsite or at the nearest local field office for at
least 5 years. Any records required to be maintained by this subpart
that are submitted electronically via the EPA's CDX may be maintained
in electronic format.
    (1) The records for each well affected facility as specified in
paragraphs (c)(1)(i) through (v) of this section.
    (i) Records identifying each well completion operation for each
well affected facility;
    (ii) Records of deviations in cases where well completion
operations with hydraulic fracturing were not performed in compliance
with the requirements specified in Sec.  60.5375a.
    (iii) Records required in Sec.  60.5375a(b) or (f) for each well
completion operation conducted for each well affected facility that
occurred during the reporting period. You must maintain the records
specified in paragraphs (c)(1)(iii)(A) and (B) of this section.
    (A) For each well affected facility required to comply with the
requirements of Sec.  60.5375a(a), you must record: The location of the
well; the API well number; the date and time of the onset of flowback
following hydraulic fracturing or refracturing; the date and time of
each attempt to direct flowback to a separator as required in Sec.
60.5375a(a)(1)(ii); the date and time of each occurrence of returning
to the initial flowback stage under Sec.  60.5375a(a)(1)(i); and the
date and time that the well was shut in and the flowback equipment was
permanently disconnected, or the startup of production; the duration of
flowback; duration of recovery to the flow line; duration of
combustion; duration of venting; and specific reasons for venting in
lieu of capture or combustion. The duration must be specified in hours.
    (B) For each well affected facility required to comply with the
requirements of Sec.  60.5375a(f), you must maintain the records
specified in paragraph (c)(1)(iii)(A) of this section except that you
do not have to record the duration of recovery to the flow line.
    (iv) For each well affected facility for which you claim an
exception under Sec.  60.5375a(a)(3), you must record: The location of
the well; the API well number; the specific exception claimed; the
starting date and ending date for the period the well operated under
the exception; and an explanation of why the well meets the claimed
exception.
    (v) For each well affected facility required to comply with both
Sec.  60.5375a(a)(1) and (3), if you are using a digital photograph in
lieu of the records required in paragraphs (c)(1)(i) through (iv) of
this section, you must retain the records of the digital photograph as
specified in Sec.  60.5410a(a)(4).
    (2) For each centrifugal compressor affected facility, you must
maintain records of deviations in cases where the centrifugal
compressor was not operated in compliance with the requirements
specified in Sec.  60.5380a. Except as specified in paragraph
(c)(2)(vii) of this section, you must maintain the records in
paragraphs (c)(2)(i) through (vi) of this section for each control
device tested under Sec.  60.5413a(d) which meets the criteria in Sec.
60.5413a(d)(11) and Sec.  60.5413a(e) and used to comply with Sec.
60.5380a(a)(1) for each centrifugal compressor.
    (i) Make, model and serial number of purchased device.
    (ii) Date of purchase.
    (iii) Copy of purchase order.
    (iv) Location of the centrifugal compressor and control device in
latitude and longitude coordinates in decimal degrees to an accuracy
and precision of five (5) decimals of a degree using the North American
Datum of 1983.
    (v) Inlet gas flow rate.
    (vi) Records of continuous compliance requirements in Sec.
60.5413a(e) as specified in paragraphs (c)(2)(vi)(A) through (D) of
this section.
    (A) Records that the pilot flame is present at all times of
operation.
    (B) Records that the device was operated with no visible emissions
except for periods not to exceed a total of 2 minutes during any hour.
    (C) Records of the maintenance and repair log.
    (D) Records of the visible emissions test following return to
operation from a maintenance or repair activity.
    (vii) As an alternative to the requirements of paragraph (c)(2)(iv)
of this section, you may maintain records of one or more digital
photographs with the date the photograph was taken and the latitude and
longitude of the centrifugal compressor and control device imbedded
within or stored with the digital file. As an alternative to imbedded
latitude and longitude within the digital photograph, the digital
photograph may consist of a photograph of the centrifugal compressor
and control device with a photograph of a separately operating GIS
device within the same digital picture, provided the

latitude and longitude output of the GIS unit can be clearly read in
the digital photograph.
    (3) For each reciprocating compressor affected facility, you must
maintain the records in paragraphs (c)(3)(i) through (iii) of this
section.
    (i) Records of the cumulative number of hours of operation or
number of months since initial startup or [date 60 days after
publication of final rule in the Federal Register], or the previous
replacement of the reciprocating compressor rod packing, whichever is
later.
    (ii) Records of the date and time of each reciprocating compressor
rod packing replacement, or date of installation of a rod packing
emissions collection system and closed vent system as specified in
Sec.  60.5385a(a)(3).
    (iii) Records of deviations in cases where the reciprocating
compressor was not operated in compliance with the requirements
specified in Sec.  60.5385a.
    (4) For each pneumatic controller affected facility, you must
maintain the records identified in paragraphs (c)(4)(i) through (v) of
this section, as applicable.
    (i) Records of the date, location and manufacturer specifications
for each pneumatic controller constructed, modified or reconstructed.
    (ii) Records of the demonstration that the use of pneumatic
controller affected facilities with a natural gas bleed rate greater
than the applicable standard are required and the reasons why.
    (iii) If the pneumatic controller is not located at a natural gas
processing plant, records of the manufacturer's specifications
indicating that the controller is designed such that natural gas bleed
rate is less than or equal to 6 standard cubic feet per hour.
    (iv) If the pneumatic controller is located at a natural gas
processing plant, records of the documentation that the natural gas
bleed rate is zero.
    (v) Records of deviations in cases where the pneumatic controller
was not operated in compliance with the requirements specified in Sec.
60.5390a.
    (5) For each storage vessel affected facility, you must maintain
the records identified in paragraphs (c)(5)(i) through (vi) of this
section.
    (i) If required to reduce emissions by complying with Sec.
60.5395a(a)(2), the records specified in Sec. Sec.  60.5420a(c)(6)
through (8), 60.5416a(c)(6)(ii), and 60.5416a(c)(7)(ii). You must
maintain the records in paragraph (c)(5)(vi) of this part for each
control device tested under Sec.  60.5413a(d) which meets the criteria
in Sec.  60.5413a(d)(11) and Sec.  60.5413a(e) and used to comply with
Sec.  60.5395a(a)(2) for each storage vessel.
    (ii) Records of each VOC emissions determination for each storage
vessel affected facility made under Sec.  60.5365a(e) including
identification of the model or calculation methodology used to
calculate the VOC emission rate.
    (iii) Records of deviations in cases where the storage vessel was
not operated in compliance with the requirements specified in
Sec. Sec.  60.5395a, 60.5411a, 60.5412a, and 60.5413a, as applicable.
    (iv) For storage vessels that are skid-mounted or permanently
attached to something that is mobile (such as trucks, railcars, barges
or ships), records indicating the number of consecutive days that the
vessel is located at a site in the oil and natural gas production
segment, natural gas processing segment or natural gas transmission and
storage segment. If a storage vessel is removed from a site and, within
30 days, is either returned to the site or replaced by another storage
vessel at the site to serve the same or similar function, then the
entire period since the original storage vessel was first located at
the site, including the days when the storage vessel was removed, will
be added to the count towards the number of consecutive days.
    (v) You must maintain records of the identification and location of
each storage vessel affected facility.
    (vi) Except as specified in paragraph (c)(5)(vi)(G) of this
section, you must maintain the records specified in paragraphs
(c)(5)(vi)(A) through (F) of this section for each control device
tested under Sec.  60.5413a(d) which meets the criteria in Sec.
60.5413a(d)(11) and Sec.  60.5413a(e) and used to comply with Sec.
60.5395a(a)(2) for each storage vessel.
    (A) Make, model and serial number of purchased device.
    (B) Date of purchase.
    (C) Copy of purchase order.
    (D) Location of the control device in latitude and longitude
coordinates in decimal degrees to an accuracy and precision of five (5)
decimals of a degree using the North American Datum of 1983.
    (E) Inlet gas flow rate.
    (F) Records of continuous compliance requirements in Sec.
60.5413a(e) as specified in paragraphs (c)(5)(vi)(F)(1) through (4).
    (1) Records that the pilot flame is present at all times of
operation.
    (2) Records that the device was operated with no visible emissions
except for periods not to exceed a total of 2 minutes during any hour.
    (3) Records of the maintenance and repair log.
    (4) Records of the visible emissions test following return to
operation from a maintenance or repair activity.
    (G) As an alternative to the requirements of paragraph
(c)(5)(vi)(D) of this section, you may maintain records of one or more
digital photographs with the date the photograph was taken and the
latitude and longitude of the storage vessel and control device
imbedded within or stored with the digital file. As an alternative to
imbedded latitude and longitude within the digital photograph, the
digital photograph may consist of a photograph of the storage vessel
and control device with a photograph of a separately operating GIS
device within the same digital picture, provided the latitude and
longitude output of the GIS unit can be clearly read in the digital
photograph.
    (6) Records of each closed vent system inspection required under
Sec.  60.5416a(a)(1) and (a)(2) for centrifugal compressors,
reciprocating compressors and pneumatic pumps, or Sec.  60.5416a(c)(1)
for storage vessels.
    (7) A record of each cover inspection required under Sec.
60.5416a(a)(3) for centrifugal or reciprocating compressors or Sec.
60.5416a(c)(2) for storage vessels.
    (8) If you are subject to the bypass requirements of Sec.
60.5416a(a)(4) for centrifugal compressors, reciprocating compressors
or pneumatic pumps, or Sec.  60.5416a(c)(3) for storage vessels, a
record of each inspection or a record of each time the key is checked
out or a record of each time the alarm is sounded.
    (9) If you are subject to the closed vent system no detectable
emissions requirements of Sec.  60.5416a(b) for centrifugal
compressors, reciprocating compressors or pneumatic pumps, a record of
the monitoring conducted in accordance with Sec.  60.5416a(b).
    (10) For each centrifugal compressor or pneumatic pump affected
facility, records of the schedule for carbon replacement (as determined
by the design analysis requirements of Sec.  60.5413a(c)(2) or (3)) and
records of each carbon replacement as specified in Sec.
60.5412a(c)(1).
    (11) For each centrifugal compressor or pneumatic pump affected
facility subject to the control device requirements of Sec.
60.5412a(a), (b), and (c), records of minimum and maximum operating
parameter values, continuous parameter monitoring system data,
calculated averages of continuous parameter monitoring system data,
results of all compliance calculations, and results of all inspections.
    (12) For each carbon adsorber installed on storage vessel affected

facilities, records of the schedule for carbon replacement (as
determined by the design analysis requirements of Sec.  60.5412a(d)(2))
and records of each carbon replacement as specified in Sec.
60.5412a(c)(1).
    (13) For each storage vessel affected facility subject to the
control device requirements of Sec.  60.5412a(c) and (d), you must
maintain records of the inspections, including any corrective actions
taken, the manufacturers' operating instructions, procedures and
maintenance schedule as specified in Sec.  60.5417a(h)(3). You must
maintain records of EPA Method 22 of appendix A-7 of this part, section
11 results, which include: Company, location, company representative
(name of the person performing the observation), sky conditions,
process unit (type of control device), clock start time, observation
period duration (in minutes and seconds), accumulated emission time (in
minutes and seconds), and clock end time. You may create your own form
including the above information or use Figure 22-1 in EPA Method 22 of
appendix A-7 of this part. Manufacturer's operating instructions,
procedures and maintenance schedule must be available for inspection.
    (14) A log of records as specified in Sec. Sec.
60.5412a(d)(1)(iii), for all inspection, repair and maintenance
activities for each control device failing the visible emissions test.
    (15) For each collection of fugitive emissions components at a well
site and each collection of fugitive emissions components at a
compressor station, the records identified in paragraphs (c)(15)(i) and
(ii) of this section.
    (i) The fugitive emissions monitoring plan for each collection of
fugitive emissions components at a well site and each collection of
fugitive emissions components at a compressor station as required in
Sec.  60.5397a(a).
    (ii) The records of each monitoring survey as specified in
paragraphs (c)(15)(ii)(A) through (F) of this section.
    (A) Date of the survey.
    (B) Beginning and end time of the survey.
    (C) Name of operator(s) performing survey. You must note the
training and experience of the operator.
    (D) Ambient temperature, sky conditions, and maximum wind speed at
the time of the survey.
    (E) Any deviations from the monitoring plan or a statement that
there were no deviations from the monitoring plan.
    (F) Documentation of each fugitive emission, including the
information specified in paragraphs (c)(15)(ii)(F)(1) through (2) of
this section.
    (1) Location.
    (2) One or more digital photographs of each required monitoring
survey being performed. The digital photograph must include the date
the photograph was taken and the latitude and longitude of the
collection of fugitive emissions components at a well site or
collection of fugitive emissions components at a compressor station
imbedded within or stored with the digital file. As an alternative to
imbedded latitude and longitude within the digital photograph, the
digital photograph may consist of a photograph of the monitoring survey
being performed with a photograph of a separately operating GIS device
within the same digital picture, provided the latitude and longitude
output of the GIS unit can be clearly read in the digital photograph.
    (3) The date of successful repair of the fugitive emissions
component.
    (4) Instrumentation used to resurvey a repaired fugitive emissions
component that could not be repaired during the initial fugitive
emissions finding.
    (16) For each pneumatic pump affected facility, you must maintain
the records identified in paragraphs (c)(16)(i) through (iv) of this
section.
    (i) Records of the date, location and manufacturer specifications
for each pneumatic pump constructed, modified or reconstructed.
    (ii) Records of deviations in cases where the pneumatic pump was
not operated in compliance with the requirements specified in Sec.
60.5393a.
    (iii) Records of the control device installation date and the
location of sites containing pneumatic pumps at which a control device
was installed, where previously there was no control device at the
site.
    (iv) Except as specified in paragraph (c)(16)(iv)(G) of this
section, records for each control device tested under Sec.  60.5413a(d)
which meets the criteria in Sec.  60.5413a(d)(11) and Sec.  60.5413a(e)
and used to comply with Sec.  60.5393a(b)(1) for each pneumatic pump.
    (A) Make, model and serial number of purchased device.
    (B) Date of purchase.
    (C) Copy of purchase order.
    (D) Location of the pneumatic pump and control device in latitude
and longitude coordinates in decimal degrees to an accuracy and
precision of five (5) decimals of a degree using the North American
Datum of 1983.
    (E) Inlet gas flow rate.
    (F) Records of continuous compliance requirements in Sec.
60.5413a(e) as specified in paragraphs (c)(16)(iv)(F)(1) through (4) of
this section.
    (1) Records that the pilot flame is present at all times of
operation.
    (2) Records that the device was operated with no visible emissions
except for periods not to exceed a total of 2 minutes during any hour.
    (3) Records of the maintenance and repair log.
    (4) Records of the visible emissions test following return to
operation from a maintenance or repair activity.
    (G) As an alternative to the requirements of paragraph
(c)(16)(iv)(D) of this part, you may maintain records of one or more
digital photographs with the date the photograph was taken and the
latitude and longitude of the pneumatic pump and control device
imbedded within or stored with the digital file. As an alternative to
imbedded latitude and longitude within the digital photograph, the
digital photograph may consist of a photograph of the pneumatic pump
and control device with a photograph of a separately operating GIS
device within the same digital picture, provided the latitude and
longitude output of the GIS unit can be clearly read in the digital
photograph.

Sec.  60.5421a  What are my additional recordkeeping requirements for
my affected facility subject to methane and VOC requirements for
onshore natural gas processing plants?

    (a) You must comply with the requirements of paragraph (b) of this
section in addition to the requirements of Sec.  60.486a.
    (b) The following recordkeeping requirements apply to pressure
relief devices subject to the requirements of Sec.  60.5401a(b)(1) of
this subpart.
    (1) When each leak is detected as specified in Sec.
60.5401a(b)(2), a weatherproof and readily visible identification,
marked with the equipment identification number, must be attached to
the leaking equipment. The identification on the pressure relief device
may be removed after it has been repaired.
    (2) When each leak is detected as specified in Sec.
60.5401a(b)(2), the information specified in paragraphs (b)(2)(i)
through (x) of this section must be recorded in a log and shall be kept
for 2 years in a readily accessible location:
    (i) The instrument and operator identification numbers and the
equipment identification number.
    (ii) The date the leak was detected and the dates of each attempt
to repair the leak.
    (iii) Repair methods applied in each attempt to repair the leak.
    (iv) ``Above 500 ppm'' if the maximum instrument reading measured

by the methods specified in Sec.  60.5400a(d) after each repair attempt
is 500 ppm or greater.
    (v) ``Repair delayed'' and the reason for the delay if a leak is
not repaired within 15 calendar days after discovery of the leak.
    (vi) The signature of the owner or operator (or designate) whose
decision it was that repair could not be effected without a process
shutdown.
    (vii) The expected date of successful repair of the leak if a leak
is not repaired within 15 days.
    (viii) Dates of process unit shutdowns that occur while the
equipment is unrepaired.
    (ix) The date of successful repair of the leak.
    (x) A list of identification numbers for equipment that are
designated for no detectable emissions under the provisions of Sec.
60.482-4a(a). The designation of equipment subject to the provisions of
Sec.  60.482-4a(a) must be signed by the owner or operator.

Sec.  60.5422a  What are my additional reporting requirements for my
affected facility subject to methane and VOC requirements for onshore
natural gas processing plants?

    (a) You must comply with the requirements of paragraphs (b) and (c)
of this section in addition to the requirements of Sec.  60.487a(a),
(b), (c)(2)(i) through (iv), and (c)(2)(vii) through (viii). You must
submit semiannual reports to the EPA via the Compliance and Emissions
Data Reporting Interface (CEDRI). (CEDRI can be accessed through the
EPA's Central Data Exchange (CDX) (https://cdx.epa.gov/).) Use the
appropriate electronic report in CEDRI for this subpart or an alternate
electronic file format consistent with the extensible markup language
(XML) schema listed on the CEDRI Web site (http://www.epa.gov/ttn/chief/cedri/index.html). If the reporting form specific to this subpart
is not available in CEDRI at the time that the report is due, submit
the report to the Administrator at the appropriate address listed in
Sec.  60.4. You must begin submitting reports via CEDRI no later than
90 days after the form becomes available in CEDRI. The report must be
submitted by the deadline specified in this subpart, regardless of the
method in which the report is submitted.
    (b) An owner or operator must include the following information in
the initial semiannual report in addition to the information required
in Sec.  60.487a(b)(1) through (4): Number of pressure relief devices
subject to the requirements of Sec.  60.5401a(b) except for those
pressure relief devices designated for no detectable emissions under
the provisions of Sec.  60.482-4a(a) and those pressure relief devices
complying with Sec.  60.482-4a(c).
    (c) An owner or operator must include the information specified in
paragraphs (c)(1) and (2) of this section in all semiannual reports in
addition to the information required in Sec.  60.487a(c)(2)(i) through
(vi):
    (1) Number of pressure relief devices for which leaks were detected
as required in Sec.  60.5401a(b)(2); and
    (2) Number of pressure relief devices for which leaks were not
repaired as required in Sec.  60.5401a(b)(3).

Sec.  60.5423a  What additional recordkeeping and reporting
requirements apply to my sweetening unit affected facilities at onshore
natural gas processing plants?

    (a) You must retain records of the calculations and measurements
required in Sec.  60.5405a(a) and (b) and Sec.  60.5407a(a) through (g)