NR 661.1035(2)(c)3.3. 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. NR 661.1035(2)(d)1.1. A list of all information references and sources used in preparing the documentation. NR 661.1035(2)(d)3.3. 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 in s. NR 660.11, 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 this subdivision may be used to comply with this requirement. The design analysis shall address the vent stream characteristics and control device operation parameters as follows: NR 661.1035(2)(d)3.a.a. 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. NR 661.1035(2)(d)3.b.b. For a catalytic 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 temperatures across the catalyst bed inlet and outlet. NR 661.1035(2)(d)3.c.c. For a boiler or process heater, 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 flame zone temperatures, combustion zone residence time, and description of method and location where the vent stream is introduced into the combustion zone. NR 661.1035(2)(d)3.d.d. For a flare, the design analysis shall consider the vent stream composition, constituent concentrations, and flow rate. The design analysis shall also consider the requirements specified in s. NR 661.1033 (4). NR 661.1035(2)(d)3.e.e. For a condenser, the design analysis shall consider the vent stream composition, constituent concentrations, flow rate, relative humidity, and temperature. The design analysis shall also establish the design outlet organic compound concentration level, design average temperature of the condenser exhaust vent stream, and design average temperatures of the coolant fluid at the condenser inlet and outlet. NR 661.1035(2)(d)3.f.f. For a carbon adsorption system such as a fixed-bed adsorber that regenerates the carbon bed directly on-site in the control device, the design analysis shall consider the vent stream composition, constituent concentrations, flow rate, relative humidity, and temperature. The design analysis shall also establish the design exhaust vent stream organic compound concentration level, number and capacity of carbon beds, type and working capacity of activated carbon used for carbon beds, design total steam flow over the period of each complete carbon bed regeneration cycle, duration of the carbon bed steaming and cooling or drying cycles, design carbon bed temperature after regeneration, design carbon bed regeneration time, and design service life of carbon. NR 661.1035(2)(d)3.g.g. For a carbon adsorption system such as a carbon canister that does not regenerate the carbon bed directly on-site in the control device, the design analysis shall consider the vent stream composition, constituent concentrations, flow rate, relative humidity, and temperature. The design analysis shall also establish the design outlet organic concentration level, capacity of carbon bed, type and working capacity of activated carbon used for carbon bed, and design carbon replacement interval based on the total carbon working capacity of the control device and source operating schedule. NR 661.1035(2)(d)4.4. A statement signed and dated by the remanufacturer or other person that stores or treats the hazardous secondary material certifying that the operating parameters used in the design analysis reasonably represent the conditions that exist when the hazardous secondary material management unit is or would be operating at the highest load or capacity level reasonably expected to occur. NR 661.1035(2)(d)5.5. A statement signed and dated by the remanufacturer or other person that stores or treats the hazardous secondary material certifying that the control device is designed to operate at an efficiency of 95 percent or greater unless the total organic concentration limit specified in s. NR 661.1032 (1) is achieved at an efficiency less than 95 weight percent or the total organic emission limits specified in s. NR 661.1032 (1) 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 provided by the control device manufacturer or vendor certifying that the control equipment meets the design specifications may be used to comply with this requirement. NR 661.1035(2)(d)6.6. If performance tests are used to demonstrate compliance, all test results. NR 661.1035(3)(3) Design documentation and monitoring, operating, and inspection information for each closed-vent system and control device required to comply with the provisions of this section shall be recorded and kept up-to-date at the facility. The information shall include all of the following: NR 661.1035(3)(a)(a) Description and date of each modification that is made to the closed-vent system or control device design. NR 661.1035(3)(b)(b) Identification of operating parameter, description of monitoring device, and diagram of monitoring sensor location or locations used to comply with s. NR 661.1033 (6) (a) and (b). NR 661.1035(3)(d)(d) Date, time, and duration of each period that occurs while the control device is operating when any monitored parameter exceeds the value established in the control device design analysis as follows: NR 661.1035(3)(d)1.1. For a thermal vapor incinerator designed to operate with a minimum residence time of 0.50 second at a minimum temperature of 760°C, the period when the combustion temperature is below 760°C. NR 661.1035(3)(d)2.2. For a thermal vapor incinerator designed to operate with an organic emission reduction efficiency of 95 weight percent or greater, the period when the combustion zone temperature is more than 28 °C below the design average combustion zone temperature established as a requirement under sub. (2) (d) 3. a. NR 661.1035(3)(d)3.3. For a catalytic vapor incinerator, the period when any of the following occur: NR 661.1035(3)(d)3.a.a. Temperature of the vent stream at the catalyst bed inlet is more than 28°C below the average temperature of the inlet vent stream established as a requirement under sub. (2) (d) 3. b. NR 661.1035(3)(d)3.b.b. Temperature difference across the catalyst bed is less than 80 percent of the design average temperature difference established as a requirement under sub. (2) (d) 3. b.