(a) Each owner or
operator subject to the provisions of this subchapter shall comply with the
test methods and procedures requirements provided in this section.
(b) When a closed-vent system is tested for
compliance with no detectable emissions, as required in subsection
11-264-1033(1), the test shall comply with the following requirements:
(1) Monitoring shall comply with Reference
Method 21 in 40 CFR Part
60 .
(2)
The detection instrument shall meet the performance criteria of Reference
Method 21.
(3) The instrument shall
be calibrated before use on each day of its use by the procedures specified in
Reference Method 21.
(4)
Calibration gases shall be:
(i) Zero air
(less than ten ppm of hydrocarbon in air).
(ii) A mixture of methane or n-hexane and air
at a concentration of approximately, but less than, ten thousand ppm methane or
n-hexane.
(5) The
background level shall be determined as set forth in Reference Method
21.
(6) The instrument probe shall
be traversed around all potential leak interfaces as close to the interface as
possible as described in Reference Method 21.
(7) The arithmetic difference between the
maximum concentration indicated by the instrument and the background level is
compared with five-hundred ppm for determining compliance.
(c) Performance tests to determine compliance
with subsection
11-264-1032(a) and with the total organic compound
concentration limit of subsection
11-264-1033(c) shall comply with the
following:
(1) Performance tests to determine
total organic compound concentrations and mass flow rates entering and exiting
control devices shall be conducted and data reduced in accordance with the
following reference methods and calculation procedures:
(i) Method 2 in 40 CFR Part
60 for velocity
and volumetric flow rate.
(ii)
Method 18 in 40 CFR Part
60 for organic content.
(iii) Each performance test shall consist of
three separate runs; each run conducted for at least 1 hour under the
conditions that exist when the hazardous waste management unit is operating at
the highest load or capacity level reasonably expected to occur. For the
purpose of determining total organic compound concentrations and mass flow
rates, the average of results of all runs shall apply. The average shall be
computed on a time-weighted basis.
(iv) Total organic mass flow rates shall be
determined by the following equation:
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where:
Eh=Total organic mass flow rate,
kg/h;
Qsd=Volumetric flow rate of gases
entering or exiting control device, as determined by Method 2, dscm/h;
n=Number of organic compounds in the vent gas;
Ci=Organic concentration in ppm,
dry basis, of compound i in the vent gas, as determined by Method 18;
MWi=Molecular weight of organic
compound i in the vent gas, kg/kg-mol;
0.0416=Conversion factor for molar volume,
kg-mol/m3 (@ 293 K and 760 mm Hg);
10-6=Conversion from ppm,
ppm-1.
(v) The annual total organic emission rate
shall be determined by the following equation:
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Image
where:
EA=Total organic mass emission
rate, kg/y;
Eh=Total organic mass flow rate for
the process vent, kg/h;
H=Total annual hours of operations for the affected unit,
h.
(vi) Total organic
emissions from all affected process vents at the facility shall be determined
by summing the hourly total organic mass emission rates
(Eh, as determined in subparagraph (c) (1) (iv)) and by
summing the annual total organic mass emission rates
(EA, as determined in subparagraph (c) (1) (v)) for all
affected process vents at the facility.
(2) The owner or operator shall record such
process information as may be necessary to determine the conditions of the
performance tests. Operations during periods of startup, shutdown, and
malfunction shall not constitute representative conditions for the purpose of a
performance test.
(3) The owner or
operator of an affected facility shall provide, or cause to be provided,
performance testing facilities as follows:
(i) Sampling ports adequate for the test
methods specified in paragraph (c) (1).
(ii) Safe sampling platform(s).
(iii) Safe access to sampling
platform(s).
(iv) Utilities for
sampling and testing equipment.
(4) For the purpose of making compliance
determinations, the time-weighted average of the results of the three runs
shall apply. In the event that a sample is accidentally lost or conditions
occur in which one of the three runs must be discontinued because of forced
shutdown, failure of an irreplaceable portion of the sample train, extreme
meteorological conditions, or other circumstances beyond the owner or
operator's control, compliance may, upon the director's approval, be determined
using the average of the results of the two other runs.
(d) To show that a process vent associated
with a hazardous waste distillation, fractionation, thin-film evaporation,
solvent extraction, or air or steam stripping operation is not subject to the
requirements of this subchapter, the owner or operator must make an initial
determination that the time-weighted, annual average total organic
concentration of the waste managed by the waste management unit is less than
ten ppmw using one of the following two methods:
(1) Direct measurement of the organic
concentration of the waste using the following procedures:
(i) The owner or operator must take a minimum
of four grab samples of waste for each waste stream managed in the affected
unit under process conditions expected to cause the maximum waste organic
concentration.
(ii) For waste
generated onsite, the grab samples must be collected at a point before the
waste is exposed to the atmosphere such as in an enclosed pipe or other closed
system that is used to transfer the waste after generation to the first
affected distillation, fractionation, thin-film evaporation, solvent
extraction, or air or steam stripping operation. For waste generated offsite,
the grab samples must be collected at the inlet to the first waste management
unit that receives the waste provided the waste has been transferred to the
facility in a closed system such as a tank truck and the waste is not diluted
or mixed with other waste.
(iii)
Each sample shall be analyzed and the total organic concentration of the sample
shall be computed using Method 9060 or 8260 of SW-846 (incorporated by
reference under section
11-260-11).
(iv) The arithmetic mean of the results of
the analyses of the four samples shall apply for each waste stream managed in
the unit in determining the time-weighted, annual average total organic
concentration of the waste. The time-weighted average is to be calculated using
the annual quantity of each waste stream processed and the mean organic
concentration of each waste stream managed in the unit.
(2) Using knowledge of the waste to determine
that its total organic concentration is less than ten ppmw. Documentation of
the waste determination is required. Examples of documentation that shall be
used to support a determination under this provision include production process
information documenting that no organic compounds are used, information that
the waste is generated by a process that is identical to a process at the same
or another facility that has previously been demonstrated by direct measurement
to generate a waste stream having a total organic content less than ten ppmw,
or prior speciation analysis results on the same waste stream where it can also
be documented that no process changes have occurred since that analysis that
could affect the waste total organic concentration.
(e) The determination that distillation,
fractionation, thin-film evaporation, solvent extraction, or air or steam
stripping operations manage hazardous wastes with time-weighted, annual average
total organic concentrations less than ten ppmw shall be made as follows:
(1) By the effective date that the facility
becomes subject to the provisions of this subchapter or by the date when the
waste is first managed in a waste management unit, whichever is later,
and
(2) For continuously generated
waste, annually, or
(3) Whenever
there is a change in the waste being managed or a change in the process that
generates or treats the waste.
(f) When an owner or operator and the
director do not agree on whether a distillation, fractionation, thin-film
evaporation, solvent extraction, or air or steam stripping operation manages a
hazardous waste with organic concentrations of at least ten ppmw based on
knowledge of the waste, the procedures in Method 8260 of SW-846 (incorporated
by reference under section
11-260-11) may be used to resolve the
dispute.