(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.

(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:

(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.

(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.

(D) A statement signed and dated by the owner or operator certifying that the operating parameters used in the design analysis reasonably represent the conditions that exist when the hazardous waste management unit is or would be operating at the highest load or capacity level reasonably expected to occur.

(E) A statement signed and dated by the owner or operator certifying that the control device is designed to operate at an efficiency of 95 percent or greater unless the total organic concentration limit of Section 66264.1032(a) is achieved at an efficiency less than 95 weight percent or the total organic emission limits of Section 66264.1032(a) for affected process vents at the facility can be attained by a control device involving vapor recovery at an efficiency less than 95 weight percent. A statement signed and dated by the control device manufacturer or vendor certifying that the control equipment meets the design specifications may be used to comply with this requirement.

(F) If performance tests are used to demonstrate compliance, all test results.

(A) for a thermal vapor incinerator designed to operate with a minimum residence time of 0.50 second at a minimum temperature of 760 degrees C, period when the combustion temperature is below 760 degrees C;

(B) for a thermal vapor incinerator designed to operate with an organic emission reduction efficiency of 95 weight percent or greater, period when the combustion zone temperature is more than 28 degrees C below the design average combustion zone temperature established as a requirement of subsection (b)(4)(C)1 of this section;

(C) for a catalytic vapor incinerator, period when:

(D) for a boiler or process heater, period when:

(E) for a flare, period when the pilot flame is not ignited;

(F) for a condenser that complies with Section 66264.1033(f)(2)(F)1, period when the organic compound concentration level or readings of organic compounds in the exhaust vent stream from the condenser are more than 20 percent greater than the design outlet organic compound concentration level established as a requirement of paragraph (b)(4)(C)5 of this section;

(G) for a condenser that complies with Section 66264.1033(f)(2)(F)2, period when:

(H) for a carbon adsorption system such as a fixed-bed carbon adsorber that regenerates the carbon bed directly on-site in the control device and complies with Section 66264.1033(f)(2)(G)1, period when the organic compound concentration level or readings of organic compounds in the exhaust vent system from the carbon bed are more than 20 percent greater than the design exhaust vent stream organic compound concentration level established as a requirement of subsection (b)(4)(C)6 of this section;

(I) for a carbon adsorption system such as a fixed-bed carbon adsorber that regenerates the carbon bed directly on-site in the control device and complies with Section 66264.1033(f)(2)(G)(2), period when the vent stream continues to flow through the control device beyond the pre-determined carbon bed regeneration time established as a requirement of subsection (b)(4)(C)6 of this section;

(A) date and time when control device is monitored for carbon breakthrough and the monitoring device reading;

(B) date when existing carbon in the control device is replaced with fresh carbon; and

(A) the instrument identification number, the closed-vent system component identification number, and the operator name, initials, or identification number.

(B) the date the leak was detected and the date of first attempt to repair the leak.

(C) the date of successful repair of the leak.

(D) maximum instrument reading measured by Method 21 of 40 CFR part 60, appendix A after it is successfully repaired or determined to be nonrepairable.

(E) “Repair delayed” and the reason for the delay if a leak is not repaired within 15 calendar days after discovery of the leak.