Tenn. Comp. R. & Regs. 1200-03-18-.40

Current through December 26, 2024

Section 1200-03-18-.40 - AIR OXIDATION PROCESSES IN THE SYNTHETIC ORGANIC CHEMICAL MANUFACTURING INDUSTRY

(1) Applicability of this rule is as follows:

(a) This rule applies to the following air oxidation facilities in Davidson, Rutherford, Shelby, Sumner, Williamson, and Wilson Counties in the synthetic organic chemical manufacturing industry:

1. Each air oxidation reactor not discharging its vent stream into a recovery system;

2. Each combination of an air oxidation reactor and the recovery system into which its vent stream is discharged; and

3. Each combination of two or more air oxidation reactors and the common recovery system into which their vent streams are discharged.

(b) Any air oxidation reactor vent stream that has a total resource effectiveness (TRE) index value greater than 1.0 is exempt from all provisions of this rule except the requirements in Paragraph (3) and Subparagraphs (5)(b) and (6)(j) of this rule.

(2) For the purpose of this rule, the following definitions apply:

"Air oxidation facility" means a product recovery system and all associated air oxidation process reactors discharging directly into that system or any such reactors discharging directly into the atmosphere.

"Air oxidation process" means a reactor in which air is used as an oxidizing agent to produce an organic chemical.

"Air oxidation reactor" means any device or process vessel in which one or more organic reactants are combined with air or a combination of air and oxygen to produce one or more organic compounds. Ammoxidation and oxychlorination are included in this definition.

"Air oxidation reactor recovery train" means an individual recovery system receiving the vent stream from at least one air oxidation reactor, along with all air oxidation reactors feeding vent streams into this system.

"Product recovery system" means any equipment used to collect volatile organic compounds (VOC's) for use, reuse, or sale. Such equipment includes, but is not limited to, absorbers, adsorbers, condensers, and devices that recover non-VOC's such as ammonia and HCl.

"Synthetic organic chemical manufacturing industry" means the industry that produces, as intermediates or final products, one or more of the chemicals listed at 40 C.F.R. 60.489, as of July 1, 1991.

"Total resource effectiveness index value," or TRE index value, means a measure of the supplemental total resource requirement per unit of VOC emission reduction associated with an individual air oxidation vent stream, based on vent stream flow rate, emission rate of VOC, net heating value, and corrosive properties, as quantified by the equation given under Subparagraph (4)(a) of this rule.

"Vent stream" means any gas stream containing nitrogen that was introduced as air to the air oxidation reactor, released to the atmosphere directly from any air oxidation reactor recovery train or indirectly, after diversion through other process equipment.

(3) For each vent stream from an air oxidation reactor or combination air oxidation reactor and recovery train subject to this rule, the owner or operator shall comply with Subparagraph (a), (b), or (c) as follows:

(a) Reduce total VOC emissions by 98 weight percent or to 20 parts per million volumetric (ppmv) on a dry basis corrected to 3 percent oxygen, whichever is less stringent. If a boiler or process heater is used to comply with this subparagraph, the vent stream shall be introduced into the flame zone of the boiler or process heater;

(b) Combust the emissions in a flare that meets the requirements of 40 C.F.R. 60.18, as of July 1, 1991, except that, for a hydrogen fueled flare serving a hydrogen cyanide process at a facility in Shelby County, the Technical Secretary, upon demonstration that stable-flame conditions are maintained, may waive the net heating value and exit velocity requirements of the C.F.R. section; or

(c) Maintain a TRE index value greater than 1.0 without the use of VOC emission control devices.

(4) Monitoring requirements as follow apply:

(a) The owner or operator of an air oxidation facility that uses an incinerator to seek to comply with the VOC emission limit specified under Subparagraph (3)(a) of this rule, shall install, calibrate, maintain, and operate according to manufacture's specifications the following equipment:

1. A temperature monitoring device equipped with a continuous recorder and having an accuracy of ± 1 percent of the temperature being monitored expressed in degrees Celsius or ± 0.5°C, whichever is greater.

(i) Where an incinerator other than a catalytic incinerator is used, a temperature monitoring device shall be installed in the firebox.

(ii) Where a catalytic incinerator is used, temperature monitoring devices shall be installed in the gas stream immediately before and after the catalyst bed.

2. A flow indicator that provides a record of vent stream flow to the incinerator at least once every hour for each air oxidation facility. The flow indicator shall be installed in the vent stream from each air oxidation facility at a point closest to the inlet of each incinerator and before being joined with any other vent stream.

(b) The owner or operator of an air oxidation facility that uses a flare to seek to comply with Subparagraph (3)(b) of this rule shall install, calibrate, maintain, and operate according to manufacture's specifications the following equipment:

1. A heat sensing device, such as an ultra-violet sensor or thermocouple, at the pilot light to indicate the continuous presence of a flame.

2. A flow indicator that provides a record of vent stream flow to the flare at least once every hour for each air oxidation facility. The flow indicator shall be installed in the vent stream from each air oxidation facility at a point closest to the flare and before being joined with any other vent stream.

(c) The owner or operator of an air oxidation facility that uses a boiler or process heater to seek to comply with Subparagraph (3)(a) of this rule shall install, calibrate, maintain, and operate according to the manufacturer's specifications the following equipment:

1. A flow indicator that provides a record of vent stream flow to the boiler or process heater at least once every hour for each air oxidation facility. The flow indicator shall be installed in the vent stream from each air oxidation reactor within a facility at a point closest to the inlet of each boiler or process heater and before being joined with any other vent stream.

2. A temperature monitoring device in the firebox equipped with a continuous recorder and having an accuracy of ±1 percent of the temperature being measured expressed in degrees Celsius or ±0.5°C, whichever is greater, for boilers or process heaters of less than 44 MW (150 million Btu/hr) heat input design capacity.

3. Monitor and record the periods of operation of the boiler or process heater if the design input capacity of the boiler or process heater is 44 MW (150 million Btu/hr) or greater. The records shall be readily available for inspection.

(d) The owner or operator of an air oxidation facility that seeks to demonstrate compliance with the TRE index value limit specified under Subparagraph (3)(c) of this rule shall install, calibrate, maintain, and operate according to manufacturer's specifications the following equipment:

1. Where an absorber is the final recovery device in a recovery system:

(i) A scrubbing liquid temperature monitoring device having an accuracy of ±1 percent of the temperature being monitored, expressed in degrees Celsius or ±0.5°C, whichever is greater, and a specific gravity monitoring device having an accuracy of ±0.02 specific gravity unit, each equipped with a continuous recorder; and

(ii) An organic monitoring device used to indicate the concentration level of organic compounds exiting the recovery device based on a detection principle such as infrared, photoionization, or thermal conductivity, each equipped with a continuous recorder.

2. Where a condenser is the final recovery device in a recovery system:

(i) A condenser exit (product site) temperature monitoring device equipped with a continuous recorder and having an accuracy of ±1 percent of the temperature being monitored expressed in degrees Celsius or ±0.5°C, whichever is greater; and

3. Where a carbon adsorber is the final recovery device in a recovery system:

(i) An integrating steam flow monitoring device having an accuracy of ±10 percent, and a carbon bed temperature monitoring device having an accuracy of ±1 percent of the temperature being monitored expressed in degrees Celsius or ±0.5°C, whichever is greater, both equipped with a continuous recorder; and

(5) The following methods shall be used to demonstrate compliance with Paragraph (3) of this rule:

(a) The following equation shall be used to calculate the TRE index for a given vent stream:

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where:

TRE = The total resource effectiveness index value. E = The measured hourly emissions in units of kilograms/hour (kg/h).

FL = The vent stream flow rate in scm/min, at a standard temperature of 20°C.

For a Category E stream (see Table 1), the factor f(FL)^0.5 should be replaced with

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where:

H_T = Vent stream net heating value in units of MJ/scm, where the net enthalpy per mole of offgas is based on combustion at 25°C (68°F) and 760 millimeters of Mercury (mm Hg), but the standard temperature for determining the volume corresponding to one mole is 20°c, as in the definition of FL.

a, b, c, d, e, and f = Specific coefficients for six different general categories of process vent streams. The set of coefficients that apply to a given air oxidation process vent stream are specified in Table 1.

TABLE 1. COEFFICIENTS OF THE TOTAL RESOURCE EFFECTIVENESS (TRE)

INDEX EQUATION

A1. For Chlorinated Process Vent Streams, if 0 <= Net Heating Value (MJ/scm) <= 3.5:

FL <= Vent Stream Flow Rate (scm/min)	a	b	c	d	e	f
FL <= 13.5	48.73	0	0.404	-0.1632	0	0
13.5 < FL <= 700	42.35	0.624	0.404	-0.1632	0	0.0245
700 < FL <= 1,400	84.38	0.678	0.404	-0.1632	0	0.0346
1,400 < FL <= 2,100	126.41	0.712	0.404	-0.1632	0	0.0424
2,100 < FL <= 2,800	168.44	0.747	0.404	-0.1632	0	0.0490
2,800 < FL <= 3,500	210.47	0.758	0.404	-0.1632	0	0.0548

A2. For Chlorindated Process Vent Streams, if 3.5 < Net Heating Value (MJ/scm):

FL - Vent Stream Flow Rate (scm/min)	a	b	c	d	e	f
FL <= 13.5	47.76	0	0.292	0	0	0
13.5 < FL <=700	41.58	0.605	0.292	0	0	0.0245
700 < FL <= 1,400	82.84	0.658	0.292	0	0	0.0346
1,400 < FL <= 2,100	123.10	0.691	0.292	0	0	0.0424
2,100 < FL <= 2,800	165.36	0.715	0.292	0	0	0.0490
2,800 < FL <= 3,500	206.62	0.734	0.292	0	0	0.0548

B. For Nonchlorinated Process Vent Streams, if 0 <= Net Heating Value (MJ/scm) <= 0.48:

FL - Vent Stream Flow Rate (scm/min)	a	b	c	d	e	f
FL <= 13.5	19.05	0	0.113	-0.214	0	0
13.5 < FL <= 1,350	16.61	0.239	0.113	-0.214	0	0.0245
1,350 < FL <= 2,700	32.91	0.260	0.113	-0.214	0	0.0346
2,700 < FL <= 3,500	49.21	0.273	0.113	-0.214	0	0.0424

C. For Nonchlorindated Process Vent Streams, if 0.48 < Net Heating Value (MJ/scm) <= 1.9:

FL - Vent Stream Flow Rate (scm/min)	a	b	c	d	e	f
FL <= 13.5 13.5 < FL <= 1, 350 1,350 < FL <= 2,700	19.74 18.30 36.28	0 0.138 0.150	0.400 0.400 0.400	-0.202 -0.202 -0.202	0 0 0	0 0.0245 0.0346
2,700 < FL<=4,050	54.26	0.158	0.400	-0.202	0	0.0424

D. For Nonchlorinated Process Vent Streams, if 1.9 < Net Heating Value (MJ/scm) <= 3.6:

FL - Vent Stream Flow Rate (scm/min)	a	b	c	d	e	f
FL <= 13.5 13.5 < FL <= 1, 190 1,190 < FL <= 2,380	15.24 13.63 26.95	0 0.157 0.171	0.033 0.033 0.033	0 0 0	0 0 0	0 0.0245 0.0346
2,380 < FL <= 3,570	40.27	0.179	0.033	0	0	0.0424

E. For Nonchlorinated Process Vent Streams, if 3.6 < Net Heating Value (MJ/scm):

FL - Vent Stream Flow Rate (scm/min)	a	b	c	d	e	f
FL <= 13.5	15.24	0	0	0.0090	0	0
13.5 < FL <= 1,190	13.63	0	0	0.0090	0.0503	0.0245
1,190 < FL <= 2,380	26.95	0	0	0.0090	0.0546	0.0346
2,380 < FL <= 3,570	40.27	0	0	0.0090	0.0573	0.0424

(b) Each owner or operator of an air oxidation facility seeking to comply with Subparagraph (1)(b) or (3)(c) of this rule shall recalculate the TRE index value for that air oxidation facility whenever process changes are made. Some examples of process changes are changes in production capacity, feedstock type, or catalyst type, or whenever there is replacement, removal, or addition of recovery equipment. The TRE index value shall be recalculated based on test data, or on best engineering estimates of the effects of the change to the recovery system.

(c) Reference Method 1 or 1A, as appropriate, for selection of the sampling sites. The control device inlet sampling site for determination of vent stream molar composition or VOC reduction efficiency shall be prior to the inlet of the control device and after the recovery system.

(d) Reference Method 2, 2A, 2C, or 2D, as appropriate, for determination of the volumetric flow rates.

(e) The emission rate correction factor, integrated sampling and analysis procedure of

Method 3 shall be used to determine the oxygen concentration (%0) for the purposes 2d of determining compliance with the 20 ppmv limit. The sampling site shall be the same as that of the VOC samples and the samples shall be taken during the same time that the VOC samples are taken. The VOC concentration corrected to 3 percent O (C) 22 shall be computed using the following equation:

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where:

C_c = Concentration of VOC corrected to 3 percent 0₂ , dry basis, ppm by volume.

C_voc = Concentration of VOC, dry basis, ppm by volume.\

%0_2d = Concentration of 0₂ , dry basis, percent by volume.

(f) Reference Method 18 to determine concentration of VOC in the control device outlet and the concentration of VOC in the inlet when the reduction efficiency of the control device is to be determined, according to the following:

1. The sampling time for each run shall be 1 hour in which either an integrated sample or four grab samples shall be taken. If grab sampling is used, then the samples shall be taken at 15-minute intervals.

2. The emission reduction (R) of VOC shall be determined using the following equation:

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where:

R = Emission reduction, percent by weight.

E_i = Mass rate of VOC entering the control device, kg VOC/hr.

E_o = Mass rate of VOC discharged to the atmosphere, kg VOC/hr.

3. The mass rates of VOC (E_i , E_o) shall be computed using the following equations:

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where:

C_ij , C_oj = Concentration of sample component "j" of the gas stream at the inlet and outlet of the control device, respectively.

M_ij , M_oj = Molecular weight of sample component "j" of the gas stream at the inlet and outlet of the control device, respectively, g/g- mole (lb/lb-mole) .

Q_i , Q_o = Flow rate of gas stream at the inlet and outlet of the control device, respectively, dscm/min (dscf/hr).

K₂ = Constant, 2.494 x 10^-6 (1/ppm) (g-mole/scm) (kg/g) (min/h), where standard temperature for (g-mole/scm) is 20⁰ C.

4. The VOC concentration (C_voc) is the sum of the individual components and shall be computed for each run using the following equation:

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where:

C_voc = Concentration of VOC, dry basis, ppm by volume.

C_j = Concentration of sample components in the sample.

n = Number of components in the sample.

(g) When a flare is used to seek to comply with Subparagraph (3)(b) of this rule, the flare shall comply with the requirements of 40 C.F.R. 60.18, as of July 1, 1991.

(h) The following test methods shall be used for determining the net heating value of the gas combusted to determine compliance under Subparagraph (3)(b) of this rule, and for determining the process vent stream TRE index value to determine compliance under Subparagraph (3)(c) of this rule:

1. For selection of sampling site:

(i) Reference Method 1 or 1A, as appropriate, for selection of the sampling site. The sampling site for the vent stream flow rate and molar composition determination prescribed in Parts 2 and 3 of this subparagraph shall be, except for the situations outlined in Subpart (ii) of this part, prior to the inlet of any control device, prior to any post-reactor dilution of the stream with air, and prior to any post-reactor introduction of halogenated compounds into the vent stream. No transverse site selection method is needed for vents smaller than 4 inches in diameter.

(ii) If any gas stream other than the air oxidation vent stream is normally conducted through the final recovery device:

(I) The sampling site for vent stream flow rate and molar composition shall be prior to the final recovery device and prior to the point at which the nonair oxidation stream is introduced.

(II) The efficiency of the final recovery device is determined by measuring the VOC concentration using Method 18 at the inlet to the final recovery device after the introduction of any nonair oxidation vent stream and at the outlet of the final recovery device.

(III) This efficiency is applied to the VOC concentration measured prior to the final recovery device and prior to the introduction of the nonair oxidation stream to determine the concentration of VOC in the air oxidation stream from the final recovery device. This concentration of VOC is then used to perform the calculations outlined in Parts 4 and 5 of this subparagraph.

2. For determining molar composition of the process vent stream:

(i) Reference Method 18 to measure the concentration of VOC including those containing halogens.

(ii) ASTM D1946-77 to measure the concentration of carbon monoxide and hydrogen.

(iii) Reference Method 4 to measure the content of water vapor.

3. For volumetric flow rate Reference Method 2, 2A, 2C, or 2D, as appropriate.

4. For net heating value of the vent stream, the following equation:

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where:

H_T = Net heating value of the sample, MJ/scm, where the net enthalpy per mole of offgas is based on combustion at 25°C and 760 mm Hg, but the standard temperature for determining the volume corresponding to one mole is 20°C, as in the definition of Q_s (offgas flow rate).

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where standard temperature for (g-mole) / scm is 20°C.

C_j = Concentration of compound j in ppm, as measured for organics by Reference Method 18 and measured for hydrogen and carbon monoxide by ASTM D1946-77 as indicated in Part 2 of this subparagraph.

H_j = Net heat of combustion of compound j, kcal/g-mole, based on combustion at 25°C and 760 mm Hg. The heats of combustion of vent stream components would be required to be determined using ASTM D2382-76 if published values are not available or cannot be calculated.

5. For emission rate of VOC in the process vent stream, the following equation:

Click to view Image

where:

E_voc = Emission rate of VOC in the sample, kg/hr.

K₂ = Constant, 2.494 x 10^-6 (1/ppm) (g-mole/scm) (kg/g) (min/hr), where standard temperature for (g-mole/scm) is 20°C.

C_j = Concentration on a dry basis of compound j in ppm as measured by Reference Method 18 as indicated in Part 2 of this subparagraph.

M_j = Molecular weight of sample j, g/g-mole.

Q_s = Vent stream flow rate (scm/min) at a standard temperature of 20°C.

(6) The owner or operator of a facility subject to this rule shall keep the records specified in this paragraph for at least 3 years. These records, as follow, shall be made available to the Technical Secretary immediately upon request:

(a) Where an owner or operator subject to this rule seeks to demonstrate compliance with Subparagraph (3)(a) of this rule through the use of either a thermal or catalytic incinerator:

1. The average firebox temperature of the incinerator (or the average temperature upstream and downstream of the catalyst bed for a catalytic incinerator), measured at least every 15 minutes and averaged over the same time period as the compliance test, and

2. The percent reduction of VOC determined as specified in Subparagraph (3)(a) of this rule that is achieved by the incinerator, or the concentration of VOC determined as specified in Subparagraph (3)(a) of this rule at the outlet of the control device on a dry basis corrected to 3 percent oxygen.

(b) Where an owner or operator subject to the provisions of this rule seeks to demonstrate compliance with Subparagraph (3)(a) of this rule through the use of a boiler or process heater:

1. A description of the location at which the vent stream is introduced into the boiler or process heater, and

2. The average combustion temperature of the boiler or process heater with a design heat input capacity of less than 44 MW (150 million Btu/hr) measured at least every 15 minutes and averaged over the same time period of the compliance testing.

(c) Where an owner or operator subject to the provisions of this rule seeks to comply with Subparagraph (3)(b) of this rule through the use of a smokeless flare, flare design (i.e., steam-assisted, air-assisted, or non-assisted), all visible emission readings, heat content determinations, flow rate measurements, and exit velocity determinations made during the compliance test, continuous records of the flare pilot flame monitoring, and records of all periods of operation during which the pilot flame is absent.

(d) Where an owner or operator seeks to demonstrate compliance with Subparagraph (3)(c) of this rule:

1. Where an absorber is the final recovery device in a recovery system, the exit specific gravity and average exit temperature of the absorbing liquid, measured at least every 15 minutes and averaged over the same time period of the compliance testing (both measured while the vent stream is normally routed and constituted), or

2. Where a condenser is the final recovery device in a recovery system, the average exit (product side) temperature, measured at least every 15 minutes and averaged over the same time period of the compliance testing while the vent stream is normally routed and constituted, or

3. Where a carbon adsorber is the final recovery device in a recovery system, the total steam mass flow measured at least every 15 minutes and averaged over the same time period of the compliance test (full carbon bed cycle), temperature of the carbon bed after regeneration (and within 15 minutes of completion of any cooling cycle(s)), and duration of the carbon bed steaming cycle (all measured while the vent stream is normally routed and constituted), or

4. As an alternative to Part 1, 2, or 3 of this subparagraph, the concentration level or reading indicated by the organic monitoring device at the outlet of the absorber, condenser, or carbon adsorber measured at least every 15 minutes and averaged over the same time period of the compliance testing while the vent stream is normally routed and constituted.

5. All measurements and calculations performed to determine the TRE index value of the vent stream.

(e) Each owner or operator subject to the provisions of this rule shall keep up-to-date continuous records of the equipment operating parameters specified to be monitored under Subparagraphs (4)(a) and (4)(c) of this rule as well as up-to-date records of periods of operation during which the parameter boundaries established during the most recent compliance test are exceeded. The Technical Secretary may at any time require a report of these data. Where a combustion device is used by an owner or operator seeking to demonstrate compliance with Subparagraph (3)(a) or (3)(c) of this rule, periods of operation during which the parameter boundaries established during the most recent performance tests are exceeded and therefore an instance of noncompliance has occurred are defined as follows:

1. For thermal incinerators, all 3-hour periods of operation during which the average combustion temperature was more than 28°C (50°F) below the average combustion temperature during the most recent test at which compliance with Subparagraph (3)(a) of this rule was determined.

2. For catalytic incinerators, all 3-hour periods of operation during which the average temperature of the vent stream immediately before the catalyst bed is more than 28°C (50°F) below the average temperature of the vent stream during the most recent test at which compliance with Subparagraph (3)(a) of this rule was determined. The owner or operator also shall record all 3-hour periods of operation during which the average temperature difference across the catalyst bed is less than 80 percent of the average temperature difference of the device during the most recent test at which compliance with Subparagraph (3)(a) of this rule was determined.

3. All 3-hour periods of operation during which the average combustion temperature was more than 28°C (50°F) below the average combustion temperature during the most recent test at which compliance with Subparagraph (3)(a) of this rule was determined for boilers or process heaters with a design heat input capacity of less than 44 MW (150 million Btu/hr).

4. For boilers or process heaters, whenever there is a change in the location at which the vent stream is introduced into the flame zone as required under Subparagraph (3)(a) of this rule.

(f) Each owner or operator subject to the provisions of this rule shall keep up-to-date continuous records of the flow indication specified under Parts (4)(a)2, (4)(b)2, and (4)(c)1 of this rule, as well as up-to-date records of all periods when the vent stream is diverted from the control device or has no flow rate.

(g) Each owner or operator subject to the provisions of this rule who uses a boiler or process heater with a design heat input capacity of 44 MW or greater to comply with Subparagraph (3)(a) of this rule shall keep an up-to-date record of all periods of operation of the boiler or process heater. (Examples of such records could include records of steam use, fuel use, or monitoring data collected pursuant to other regulatory requirements.)

(h) Each owner or operator subject to the provisions of this rule shall keep up-to-date continuous records of the flare pilot flame monitoring specified in Subparagraph (4)(b) of this rule as well as up-to-date records of all periods of operations in which the pilot flame is absent.

(i) Each owner or operator subject to the provisions of this rule shall keep up-to-date continuous records of the equipment operating parameters specified to be monitored under Subparagraph (4)(c) of this rule as well as up-to-date records of periods of operation during which the parameter boundaries established during the most recent compliance test are exceeded. The Technical Secretary may at any time require a report of these data. Where the owner or operator seeks to demonstrate compliance with Subparagraph (3)(c) of this rule, periods of operation during which the parameter boundaries established during the most recent compliance tests are exceeded and therefore an instance of noncompliance has occurred are defined as follows:

1. Where an absorber is the final recovery device in a recovery system, and where an organic monitoring device is not used:

(i) All 3-hour periods of operation during which the average absorbing liquid temperature was more than 11°C (20°F) above the average absorbing liquid temperature during the most recent compliance test that demonstrated that the facility was in compliance, or

(ii) All 3-hour periods of operation during which the average absorbing liquid specific gravity was more than 0.1 unit above, or more than 0.1 unit below, the average absorbing liquid specific gravity during the most recent compliance test that demonstrated that the facility was in compliance.

2. Where a condenser is the final recovery device in a recovery system, and where an organic monitoring device is not used, all 3-hour periods of operation during which the average exit (product site) condenser operating temperature was more than 6°C (11°C) above the average exit (product site) operating temperature during the most recent compliance test that demonstrated that the facility was in compliance.

3. Where a carbon adsorber is the final recovery device in a recovery system and where an organic monitoring device is not used:

(i) All carbon bed regeneration cycles during which the total mass steam flow was more than 10 percent below the total mass steam flow during the most recent compliance test that demonstrated that the facility was in compliance, or

(ii) All carbon bed regeneration cycles during which the temperature of the carbon bed after regeneration [and after completion of any cooling cycle(s)] was more than 10 percent greater than the carbon bed temperature (in degrees Celsius) during the most recent compliance test that demonstrated that the facility was in compliance.

4. Where an absorber, condenser, or carbon adsorber is the final recovery device in the recovery system and an organic monitoring device approved by the Technical Secretary is used, all 3-hour periods of operation during which the average concentration level or reading of organic compounds in the exhaust gases is more than 20 percent greater than the exhaust gas organic compound concentration level or reading measured by the monitoring device during the most recent compliance test that demonstrated that the facility was in compliance.

(j) Each owner or operator subject to the provisions of this rule and seeking to demonstrate compliance with Subparagraph (3)(c) of this rule shall keep up-to-date records of:

1. Any changes in production capacity, feedstock type, or catalyst type, or of any replacement, removal, or addition of recovery equipment or air oxidation reactors;

2. Any calculation of the TRE index value performed pursuant to Subparagraph (5)(b) of this rule.

3. The results of any test performed pursuant to the methods and procedures required by Subparagraph (4)(d) of this rule.

(7) The owner or operator of any facility containing sources subject to this rule shall:

(a) Comply with the initial compliance certification requirements of Paragraph .04(1) of this chapter; and

(b) Comply with the requirements of Paragraph .04(2) of this chapter for excess emissions related to the control devices required to comply with this rule.

Tenn. Comp. R. & Regs. 1200-03-18-.40

Original rule filed May 15, 1979; effective July 10, 1979. Amendment filed October 2, 1979; effective November 16, 1979. Amendment filed April 23, 1992; effective June 7, 1992. Repeal and new rule filed March 8, 1983; effective April 22, 1993. Amendment filed May 16, 1997; effective July 30, 1997.

Authority: T.C.A. §§ 4-5-201 et seq. and 68-201-105.