[FNa1] The regulatory requirements pertain only to the list of substances; the right hand columns (Methods and PQL) are given for informational purposes only. See also footnotes 5 and 6. [FNa2] Common names are those widely used in government regulations, scientific publications, and commerce; synonyms exist for many chemicals. [FNa3] Chemical Abstracts Service registry number. Where "Total" is entered, all species in the ground water that contain this element are included. [FNa4] CAS index names are those used in the 9th Cumulative Index [FNa] 5 Suggested Methods refer to analytical procedure numbers used in EPA Report SW-846 "Test Methods for Evaluating Solid Waste", third edition and updates, as incorporated by reference in section 66260.11. Analytical details can be found in SW-846 and in documentation on file at the agency. The packed column gas chromatography methods 8010, 8020, 8030, 8040, 8060, 8080, 8090, 8110, 8120, 8140, 8150, 8240, and 8250 were promulgated methods through Update IIB of SW-846 and, as of Update III, the Agency has replaced these methods with "capillary column GC methods", as the suggested methods. [FNa] 6 Practical Quantitation Limits (PQLs) are the lowest concentrations of analytes in ground waters that can be reliably determined within specified limits of precision and accuracy by the indicated methods under routine laboratory operating conditions. The PQLs listed are generally stated to one significant figure. CAUTION: The PQL values in many cases are based only on a general estimate for the method and not on a determination for individual compounds; PQLs are not a part of the regulation. [FNa] 7 Polychlorinated biphenyls (CAS RN 1336-36-3); this category contains congener chemicals, including constituents of Aroclor-1016 (CAS RN 12674-11-2); Aroclor-1221 (CAS RN 11104-28-2), Aroclor-1232 (CAS RN 11141-16-5), Aroclor-1242 (CAS RN 53469-21-9), Aroclor-1248 (CAS RN 12672-29-6), Aroclor-1254 (CAS RN 11097-69-1), and Aroclor-1260 (CAS RN 11096-82-5). The PQL shown is an average value for PCB congeners. [FNa] 8 This category contains congener chemicals, including ng tetrachlorodibenzo-p-dioxins (see also 2,3,7,8-TCDD), pentachlorodibenzo-p-dioxins, and hexachlorodibenzo-p-dioxins. The PQL shown is an average value for PCDD congeners. [FNa] 9 This category contains congener chemicals, including tetrachlorodibenzofurans, pentachlorodibenzofurans, and hexachlorodi-benzonfurans. The PQL shown is an average value for PCDF congeners.
Note: Authority cited: Sections 25150, 25159 and 58012, Health and Safety Code. Reference: Sections 25150, 25159 and 25159.5, Health and Safety Code; and 40 CFR Part 264, Appendix IX.
s 66264.1030. Applicability. (a) The regulations in this article apply to owners and operators of facilities that treat, store, or dispose of RCRA hazardous wastes (except as provided in Section 66264.1). (b) Except for section 66264.1034, subsections (d) and (e), this article applies to process vents associated with distillation, fractionation, thin-film evaporation, solvent extraction, or air or steam stripping operations that manage RCRA hazardous wastes with organic concentrations of at least 10 ppmw, if these operations are conducted in one of the following: (1) a unit that is subject to the permitting requirements of chapter 20, or (2) a unit (including a hazardous waste recycling unit) that is not exempt from permitting under the provisions of section 66262.34(a) (i.e., a hazardous waste recycling unit that is not a 90-day tank or container) and that is located at a hazardous waste management facility otherwise subject to the permitting requirements of chapter 20, or (3) A unit that is exempt from permitting under the provisions of section 66262.34(a) (i.e., a "90-day" tank or container) and is not a recycling unit under the provisions of section 66261.6. (c) If the owner and operator of a facility subject to this article received a final permit under RCRA section 3005 prior to December 6, 1996, the requirements of this article shall be incorporated into the permit when the permit is reissued in accordance with the requirements of 40 CFR 124.15 or reviewed in accordance with the requirements of section 66270.50(d). Until such date when the owner and operator receives a final permit incorporating the requirements of this article, the owner and operator is subject to the requirements of article 27. (d) The requirements of this article do not apply to the process vents at a facility where the facility owner or operator certifies that all of the process vents that would otherwise be subject to this article are equipped with and operating air emission controls in accordance with the process vent requirements of an applicable Clean Air Act regulation codified under 40 CFR part 60, part 61, or part 63. The documentation of compliance under regulations at 40 CFR part 60, part 61, or part 63 shall be kept with, or made readily available with, the facility operating record.
Note: Authority cited: Sections 25150, 25159, 25159.5, 25245 and 58012, Health and Safety Code. Reference: Sections 25150, 25159 and 25159.5, Health and Safety Code; and 40 CFR section 264.1030.
s 66264.1032. Standards: Process Vents. (a) The owner or operator of a facility with process vents associated with distillation, fractionation, thin-film evaporation, solvent extraction, or air or steam stripping operations managing hazardous wastes organic concentrations of at least 10 ppmw shall either: (1) reduce total organic emissions from all affected process vents at the facility below 1.4 kg/h (3 lb/h) and 2.8 Mg/yr (3.1 tons/yr); or (2) reduce, by use of a control device, total organic emissions from all affected process vents at the facility by 95 weight percent. (b) If the owner or operator installs a closed-vent system and control device to comply with the provisions of subsection (a) of this section the closed-vent system and control device shall meet the requirements of Section 66264.1033. (c) Determinations of vent emissions and emission reduction or total organic compound concentrations achieved by add-on control devices shall be based on engineering calculations or performance tests. If performance tests are used to determine vent emissions, emission reductions, or total organic compound concentrations achieved by add-on control devices, the performance tests shall conform with the requirements of Section 66264.1034(c). (d) When an owner or operator and the Department do not agree on determinations of vent emissions and/or emission reductions or total organic compound concentrations achieved by add-on control devices based on engineering calculations, the procedures in Section 66264.1034(c) shall be used to resolve the disagreement.
Note: Authority cited: Sections 25150 and 25159, Health and Safety Code. Reference: Sections 25159 and 25159.5, Health and Safety Code; 40 CFR section 264.1032.
s 66264.1033. Standards: Closed-vent Systems and Control Devices. (a)(1) Owners or operators of closed-vent systems and control devices used to comply with provisions of this chapter shall comply with the provisions of this section. (2) The owner or operator of an existing facility who cannot install a closed-vent system and control device to comply with the provisions of this article on the effective date that the facility becomes subject to the provisions of this article shall prepare an implementation schedule that includes dates by which the closed-vent system and control device will be installed and in operation. The controls shall be installed as soon as possible, but the implementation schedule may allow up to 18 months of installation and start-up time after the effective date that the facility becomes subject to this article. All units that begin operation after the dates indicated below shall comply with the rules immediately (i.e., shall have control devices installed and operating on start-up of the affected unit): (A) December 21, 1990 for units that transfer, treat, store, or dispose of RCRA hazardous wastes, unless the owner/operator of the unit is exempt from regulation under 40 CFR, Section 264.1; (B) Six months after the effective date of these regulations for units that transfer, treat, store, or dispose of RCRA hazardous wastes, if the owner/operator of the unit is exempt from regulation under 40 CFR, Section 264.1 but not exempt from regulation under Section 66264.1. (b) A control device involving vapor recovery (e.g., a condenser or absorber) shall be designed and operated to recover the organic vapors vented to it with an efficiency of 95 weight percent or greater unless the total organic emission limits of Section 66264.1032(a)(1) for all affected process vents can be attained at an efficiency less than 95 weight percent. (c) An enclosed combustion device (e.g., a vapor incinerator, boiler, or process heater) shall be designed and operated to reducethe organic emissions vented by it by 95 weight percent or greater;to achieve a total organic compound concentration of 20 ppmv, expressed as the sum of the actual compounds, not carbon equivalents, on a dry basis corrected to 3 percent oxygen; or to provide a minimum residence time of 0.50 seconds at a minimum temperature of 760 degrees C. If a boiler or process heater is used as the control device, then the vent stream shall be introduced into the flame zone of the boiler or process heater. (d)(1) A flare shall be designed for and operated with no visible emissions as determined by the methods specified in subsection (e)(1) of this section, except for periods not to exceed a total of five minutes during any two consecutive hours. (2) A flare shall be operated with a flame present at all times, as determined by the methods specified in subsection (f)(2)(C) of this section. (3) A flare shall be used only if the net heating value of the gas being combusted is 11.2 MJ/scm (300 Btu/scf) or greater if the flare is steam-assisted or air-assisted; or if the net heating value of the gas being combusted is 7.45 MJ/scm (200 Btu/scf) or greater if the flare is non-assisted. The net heating value of the gas being combusted shall be determined by the methods specified in subsection (e)(2) of this section. (4)(A) A steam-assisted or non-assisted flare shall be designed for and operated with an exit velocity, as determined by the methods specified in subsection (e)(3) of this section, less than 18.3 m/s (60 ft/s), except as provided in subsections (B) and (C) of this section. (B) A steam-assisted or non-assisted flare designed for and operated with an exit velocity, as determined by the method specified in subsection (e)(3) of this section, equal to or greater than 18.3 m/s (60 ft/s) but less than 122 m/s (400 ft/s) is allowed if the net heating value of the gas being combusted is greater than 37.3 MJ/scm (1,000 Btu/scf). (C) A steam-assisted or non-assisted flare designed for and operated with an exit velocity, as determined by the methods specified in subsection (e)(3) of this section, less than the velocity, V max as determined by the method specified in subsection (e)(4) of this section and less than 122 m/s (400 ft/s) is allowed. (5) An air-assisted flare shall be designed and operated with an exit velocity less than the velocity, V max, as determined by the method specifiec in subsection (e)(5) of this section. (6) A flare used to comply with this section shall be steam-assisted, air-assisted, or non-assisted. (e)(1) Reference Method 22 in 40 CFR, Part 60, incorporated by reference in Section 66260.11 of this chapter, shall be used to determine the compliance of a flare with the visible emission provisions of this article. The observation period is two hours and shall be used according to Method 22. (2) The net heating value of the gas being combusted in a flare shall be calculated using the following equation: n Ht =K[ S Ci Hi ] i=1 where: Ht = Net heating value of the sample, MJ/scm; where the net enthalpy per mole of off gas is based on combustion at 25 degress C and 760 mm Hg, but the standard temperature for determining the volume corresponding to 1 mol is 20 degress C; K = Constant, 1.74 x 10 -7 (1/ppm) (g mol/scm) (MJ/kcal) where standard temperature for (g mol/scm) is 20 degrees C; Ci = Concentration of sample component i in ppm on a wet basis, as measured for organics by Reference Method 18 in 40 CFR, Part 60 and measured for hydrogen and carbon monoxide by ASTM D 1946-82 (incorporated by reference as specified in Section 66260.11); and Hi = Net heat combustion of sample component i, kcal/g mol at 25 degrees C and 760 mm Hg. The heats of combustion may be determined using ASTM D 2382-83 (incorporated by reference as specified in Section 66260.11) if published values are not available or cannot be calculated. (3) The actual exit velocity of a flare shall be determined by dividing the volumetric flow rate (in units of standard temperature and pressure), as determined by Reference Methods 2, 2A, 2C, or 2D in 40 CFR, Part 60 as appropriate, by the unobstructed (free) cross-sectional area of the flare tip. (4) The maximum allowed velocity in m/s, V max, for a flare complying with subsection (d)(4)(C) of this section shall be determined by the following equation: Log10 (Vmax ) = (HT +28.8)/31.7 where: 28.8 = Constant, 31.7 = Constant, HT = The net heating value as determined in subsection (e)(2) of this section. (5) The maximum allowed velocity in m/s, V MAX, for an air-assisted flare shall be determined by the following equation: Vmax = 8.706 + 0.7084 (HT) where: 8.076 = Constant, 0.7084 = Constant, HT = The net heating value as determined in subsection (e)(2) of this section. (f) The owner or operator shall monitor and inspect each control device required to comply with this section to ensure proper operation and maintenance of the control device by implementing the following requirements: (1) install, calibrate, maintain, and operate according to the manufacturer's specifications a flow indicator that provides a record of vent stream flow from each affected process vent to the control device at least once every hour. The flow indicator sensor shall be installed in the vent stream at the nearest feasible point to the control device inlet but before the point at which the vent streams are combined; and (2) install, calibrate, maintain, and operate according to the manufacturer's specifications a device to continuously monitor control device operation as specified below: (A) for a thermal vapor incinerator, a temperature monitoring device equipped with a continuous recorder. The device shall have an accuracy of +/- 1 percent of the temperature being monitored in degrees C or +/- 0.5 degrees C, whichever is greater. The temperature sensor shall be installed at a location in the combustion chamber downstream of the combustion zone; (B) for a catalytic vapor incinerator, a temperature monitoring device equipped with a continuous recorder. The device shall be capable of monitoring temperature at two locations and have an accuracy of +/- 1 percent of the temperature being monitored in degrees C or +/- 0.5 degrees C, whichever is greater. One temperature sensor shall be installed in the vent stream at the nearest feasible point to the catalyst bed inlet and a second temperature sensor shall be installed in the vent stream at the nearest feasible point to the catalyst bed outlet; (C) for a flare, a heat sensing monitoring device equipped with a continuous recorder that indicates the continuous ignition of the pilot flame; (D) for a boiler or process heater having a design heat input capacity less than 44 MW, a temperature monitoring device equipped with a continuous recorder. The device shall have an accuracy of +/- 1 percent of the temperature being monitored in degrees C or +/- 0.5 degrees C, whichever is greater. The temperature sensor shall be installed at a location in the furnace downstream of the combustion zone; (E) for a boiler or process heater having a design heat input capacity greater than or equal to 44 MW, a monitoring device equipped with a continuous recorder to measure a parameter(s) that indicates good combustion operating practices are being used; and (F) for a condenser, either: 1. a monitoring device equipped with a continuous recorder to measure the concentration level of the organic compounds in the exhaust vent system from the condenser; or 2. a temperature monitoring device equipped with a continuous recorder. The device shall be capable of monitoring temperature at two locations and have an accuracy of +/- 1 percent of the temperature being monitored in degrees C or +/- 0.5 degrees C, whichever is greater. One temperature sensor shall be installed at a location in the exhaust vent stream from the condenser, and a second temperature sensor shall be installed at a location in the coolant fluid exiting the condenser; and (G) for a carbon adsorption system that regenerates the carbon bed directly in the control device such as a fixed-bed carbon adsorber, either: 1. a monitoring device equipped with a continuous recorder to measure the concentration level of the organic compounds in the exhaust vent system from the carbon bed; or 2. a monitoring device equipped with a continuous recorder to measure a parameter that indicates the carbon bed is regenerated on a regular, predetermined time cycle; and (3) inspect the readings from each monitoring device required by subsection (f)(1) and (2) of this section at least once each operating day to check control device operation and, if necessary, immediately implement the corrective measures necessary to ensure the control device operates in compliance with the requirements of this section. (g) An owner or operator using a carbon adsorption system such as a fixed-bed carbon adsorber that regenerates the carbon bed directly on-site in the control device shall replace the existing carbon in the control device with fresh carbon at a regular, pre-determined time interval that is no longer than the carbon service life established as a requirement of Section 66264.1035(b)(4)(C)6. (h) An owner or operator using a carbon adsorption system such as a carbon canister that does not regenerate the carbon bed directly on-site in the control device shall replace the existing carbon in the control device with fresh carbon on a regular basis by using one of the following procedures: (1) monitor the concentration level of the organic compounds in the exhaust vent stream from the carbon adsorption system on a regular schedule, and replace the existing carbon with fresh carbon immediately when carbon breakthrough is indicated. The monitoring frequency shall be daily or at an interval no greater than 20 percent of the time required to consume the total carbon working capacity established as a requirement of Section 66264.1035(b)(4)(C)7, whichever is longer; or (2) replace the existing carbon with fresh carbon at a regular, predetermined time interval that is less than the design carbon replacement interval established as a requirement of Section 66264.1035(b)(4)(C)7. (i) An alternative operational or process parameter may be monitored if it can be demonstrated that another parameter will ensure that the control device is operated in conformance with these standards and the control device's design specifications. (j) An owner or operator of an affected facility seeking to comply with the provisions of this chapter by using a control device other than a thermal vapor incinerator, catalytic vapor incinerator, flare, boiler, process heater, condenser, or carbon adsorption system is required to develop documentation including sufficient information to describe the control device operation and identify the process parameter or parameters that indicate proper operation and maintenance of the control device. (k)(1) Closed-vent systems shall be designed for and operated with no detectable emissions, as indicated by an instrument reading of less than 500 ppm above background and by visual inspections, as determined by the methods specified as Section 66264.1034(b). (2) Closed-vent systems shall be monitored to determine compliance with this section during the initial leak detection monitoring, which shall be conducted by the date that the facility becomes subject to the provisions of this section, annually, and at other times as requested by the Department. (3) Detectable emissions, as indicated by an instrument reading greater than 500 ppm and visual inspections, shall be controlled as soon as practicable, but not later than 15 calendar days after the emission is detected. (4) A first attempt at repair shall be made as soon as possible, to minimize escape of hazardous constituent to environment, but no later than 24 hours after the emission is detected. (l) Closed-vent systems and control devices used to comply with provisions of this article shall be operated at all times when emissions may be vented to them.
Note: Authority cited: Sections 25150 and 25159, Health and Safety Code. Reference: Sections 25159 and 25159.5, Health and Safety Code; 40 CFR section 264.1033.
s 66264.1034. Test Methods and Procedures. (a) Each owner or operator subject to the provisions of this article shall comply with the test methods, procedures and requirements provided in this section. (b) When a closed-vent system is tested for detectable emissions, as required in Section 66264.1033(k), 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 in 40 CFR, part 60; (3) the instrument shall be calibrated before use on each day of its use by the procedures specified in Reference Method 21 in 40 CFR, part 60; and (4) calibration gases shall be: (A) zero air (less than 10 ppm of hydrocarbon in air); and (B) a mixture of methane or n-hexane and air at a concentration of approximately, but less than, 10,000 ppm methane or n-hexane; and (5) the background level shall be determined as set forth in Reference Method 21 in 40 CFR, part 60; (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 in 40 CFR, part 60; and (7) the arithmetic difference between the maximum concentration indicated by the instrument and the background level is compared with 500 ppm for determining compliance. (c) Performance tests to determine compliance with Section 66264.1032(a) and with the total organic compound concentration limit of Section 66264.1033(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: (A) method 2 in 40 CFR, Part 60 for velocity and volumetric flow rate; (B) method 18 in 40 CFR, Part 60 for organic content; (C) each performance test shall consist of three separate runs; each run conducted for at least one 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; (D) total organic mass flow rates shall be determined by the following equation: n Eh = Qsd (<> Ci MWi ) [0.0416] [10<>-6 ] i=1 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, dry standard m<>3 /h; n = Number of organic compounds in the vent gas; C i = Organic concentration in ppm, dry basis, of compound i in the vent gas, as determined by Method 18; MW i = Molecular weight of organic compound i in the vent gas, kg/kg-mol; 0.0416= Conversion factor for molar volume, kg-mol/m<>3 (at 293 K and 760 mm Hg); 10<>-6 = Conversion from ppm, ppm<>-1 . (E) the annual total organic emission rate shall be determined by the following equation: EA = (Eh) (H) 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. (F) 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 subsection (c)(1)(D) of this section) and by summing the annual total organic mass emission rates (EA, as determined in subsection (c)(1)(E) of this section) 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. Operators during periods of start-up, 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: (A) sampling ports adequate for the test methods specified in subsection (c)(1) of this section; (B) safe sampling plateform(s); (C) safe access to sampling plateform(s); and (D) 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's or operator's control, compliance may, upon the Department's written 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 article, the owner or operator shall 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 10 ppmw using one of the following two methods: (1) direct measurement of the organic concentration of the waste using the following procedures: (A) the owner or operator shall 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; (B) for waste generated on-site, the grab samples shall 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 off-site, the grab samples shall 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 truck and the waste is not diluted or mixed with other waste; (C) each sample shall be analyzed and the total organic concentration of the sample shall be computed using Method 9060 or 8260 of SW-846 third edition and updates, as incorporated by reference under Section 66260.11; (D) 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 shall 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 10 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 10 ppmw, or prior specification 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 10 ppmw shall be made as follows: (1) by the effective date that the facility becomes subject to the provisions of this article or by the date when the waste is first managed in a waste management unit, whichever is later; and (A) for continuously generated waste, annually, or (B) 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 Department do not agree on whether a distillation, fractionation, thin-film evaporation, solvent extraction, or air or steam stripping operation manage a hazardous waste with organic concentrations of at least 10 ppmw based on knowledge of the waste, the procedures in Method 8260 of SW-846 third edition and updates, (as incorporated by reference in Section 66260.11 of this division), shall be used to resolve the dispute.
Note: Authority cited: Sections 25150, 25159 and 58012, Health and Safety Code. Reference: Sections 25159 and 25159.5, Health and Safety Code; 40 CFR Section 264.1034.
s 66264.1035. Recordkeeping Requirements. (a)(1) Each owner or operator subject to the provisions of this article shall comply with the recordkeeping requirements of this section. (2) An owner or operator of more than one hazardous waste management unit subject to the provisions of this article may comply with the recordkeeping requirements for these hazardous waste management units in one recordkeeping system if the system identifies each record by each hazardous waste management unit. (b) Owners and operators shall record or include the following information in the facility operating record: (1) for facilities that comply with the provisions of Section 66264.1033(a)(2), an implementation schedule that includes dates by which the closed-vent system and control device will be installed and in operation. The schedule shall also include a rationale of why the installation cannot be completed at an earlier date. The implementation schedule shall be in the facility operating record by the effective date that the facility becomes subject to the provisions of this article; (2) up-to-date documentation of compliance with the process vent standards in Section 66264.1032, including: (A) information and data identifying all affected process vents, annual throughout and operating hours of each affected unit, estimated emission rates for each affected vent and for the overall facility (i.e., the total emissions for all affected vents at the facility), and the approximate location within the facility of each affected unit (e.g., identify the hazardous waste management units on a facility plot plan); and (B) information and data supporting determinations of vent emissions and emission reductions achieved by add-on control devices based on engineering calculations or source tests. For the purpose of determining compliance, determinations of vent emissions and emission reductions shall be made using operating parameter values (e.g., temperatures, flow rates, or vent stream organic compounds and concentrations) that represent the conditions that result in maximum organic emissions, such as when the waste management unit is operating at the highest load or capacity level reasonably expected to occur. If the owner or operator takes any action (e.g., managing a waste of different composition or increasing operating hours of affected waste management units) that would result in an increase in total organic emissions from affected process vents at the facility, then a new determination is required. (3) Where an owner or operator chooses to use test data to determine the organic removal efficiency or total organic compound concentration achieved by the control device, a performance test plan. The test plan shall include: (A) a description of how it is determined that the planned test is going to be conducted when the hazardous waste management unit is operating at the highest load or capacity level reasonably expected to occur. This shall include the estimated or design flow rate and organic content of each vent stream and define the acceptable operating range of key process and control device parameters during the test program; (B) a detailed engineering description of the closed-vent system and control device including: 1. manufacturer's name and model number of control device; 2. type of control device; 3. dimensions of the control device; 4. capacity; and 5. construction materials; and (C) a detailed description of sampling and monitoring procedures including sampling and monitoring locations in the system, the equipment to be used, sampling and monitoring frequency, and planned analytical procedures for sample analysis. (4) Documentation of compliance with Section 66264.1033, documentation shall include the following information: (A) a list of all information references and sources used in preparing the documentation; and (B) records, including the dates, of each compliance test required by Section 66264.1033(k); (C) If engineering calculations are used, a design analysis, specifications, drawings, schematics, and piping and instrumentation diagrams based on the appropriate sections of "APTI Course 415: Control of Gaseous Emissions" (incorporated by reference as specified in Section 66260.11) or other engineering texts acceptable to the Department that present basic control device design information. Documentation provided by the control device manufacturer or vendor that describes the control device design in accordance with subsection (b)(4)(C)1 through (b)(4)(C)7 of this section shall be required to be submitted to the Department to comply with this requirement. The design analysis shall address the vent system characteristics and control device operation parameters as specified below. 1.For a thermal vapor incinerator, the design analysis shall consider the vent stream composition, constituent concentrations, and flow rate. The design analysis shall also establish the design minimum and average temperature in the combustion zone and the combustion zone residence time. (continued)