Section 33-24-02-173 - Standards - Closed-vent systems and control devices1. Requirements for remanufacturers or other persons of closed-vent systems and control devices. a. The remanufacturer or other person that stores or treats the hazardous secondary materials in hazardous secondary material management units using closed-vent systems and control devices used to comply with provisions of sections 33-24-02-170 through 33-24-02-179 shall comply with the provisions of this section.b. The remanufacturer or other person that stores or treats the hazardous secondary materials in existing hazardous secondary material management units who cannot install a closed-vent system and control device to comply with the provisions of sections 33-24-02-170 through 33-24-02-179 on the effective date that the hazardous secondary material management units become subject to the provisions of sections 33-24-02-170 through 33-24-02-179 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 must be installed as soon as possible, but the implementation schedule may allow up to thirty months after the effective date that the hazardous secondary material management units become subject to sections 33-24-02-170 through 33-24-02-179 for installation and start-up. The remanufacturer or other person that stores or treats the hazardous secondary materials shall enter the implementation schedule in the operating record located onsite. All hazardous secondary material management units that begin operation after July 13, 2015, and are subject to the provisions of sections 33-24-02-170 through 33-24-02-179 when operation begins, shall comply with sections 33-24-02-170 through 33-24-02-179 immediately (for example, must have control devices installed and operating on start-up of the affected unit); the thirty month implementation schedule does not apply.2. A control device involving vapor recovery (for example, a condenser or adsorber) must be designed and operated to recover the organic vapors vented to it with an efficiency of ninety-five weight percent or greater unless the total organic emission limits of subdivision a of subsection 1 of section 33-24-02-172 for all affected process vents can be attained at an efficiency less than ninety-five weight percent.3. An enclosed combustion device (for example, a vapor incinerator, boiler, or process heater) must be designed and operated to reduce the organic emissions vented to it by ninety-five weight percent or greater; to achieve a total organic compound concentration of twenty parts per million volume, expressed as the sum of the actual compounds, not carbon equivalents, on a dry basis corrected to three percent oxygen; or to provide a minimum residence time of fifty hundredths seconds at a minimum temperature of seven hundred sixty degrees Celsius. If a boiler or process heater is used as the control device, the vent stream must be introduced into the flame zone of the boiler or process heater.4. Flares. a. A flare must be designed for and operated with no visible emissions as determined by the methods specified in subdivision a of subsection 5, except for periods not to exceed a total of five minutes during any two consecutive hours.b. A flare must be operated with a flame present at all times, as determined by the methods specified in paragraph 3 of subdivision b of subsection 6.c. A flare may be used only if the net heating value of the gas being combusted is eleven and two-tenths mega joules per standard cubic meter at standard conditions (three hundred British thermal units per standard cubic foot at standard conditions) or greater if the flare is steam-assisted or air-assisted; or if the net heating value of the gas being combusted is seven and forty-five hundredths mega joules per cubic meter at standard conditions (two hundred British thermal units per standard cubic foot at standard conditions) or greater if the flare is nonassisted. The net heating value of the gas being combusted must be determined by the methods specified in subdivision b of subsection 5.d. Steam-assisted or nonassisted flare. (1) A steam-assisted or nonassisted flare must be designed for and operated with an exit velocity, as determined by the methods specified in subdivision c of subsection 5, less than eighteen and three-tenths meters per second (sixty feet per second), except as provided in paragraphs 2 and 3.(2) A steam-assisted or nonassisted flare designed for and operated with an exit velocity, as determined by the methods specified in subdivision c of subsection 5, equal to or greater than eighteen and three-tenths meters per second (sixty feet per second) but less than one hundred twenty-two meters per second (four hundred feet per second) is allowed if the net heating value of the gas being combusted is greater than thirty seven and three-tenths mega joules per cubic meter at standard conditions (one thousand British thermal units per standard cubic foot at standard conditions).(3) A steam-assisted or nonassisted flare designed for and operated with an exit velocity, as determined by the methods specified in subdivision c of subsection 5, less than the velocity, Vmax, as determined by the method specified in subdivision d of subsection 5 and less than one hundred twenty-two meters per second (four hundred feet per second) is allowed.e. An air-assisted flare must be designed and operated with an exit velocity less than the velocity, Vmax, as determined by the method specified in subdivision e of subsection 5.f. A flare used to comply with this section must be steam-assisted, air-assisted, or nonassisted.5. Methods. a. Referenced Method 22 in 40 CFR part 60 must be used to determine the compliance of a flare with the visible emission provisions of sections 33-24-02-170 through 33-24-02-179. The observation period is two hours and shall be used according to Method 22.b. The net heating value of the gas being combusted in a flare must be calculated using the following equation: Click here to view image.
where:
HT = 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 1 mol is 20°C;
K= Constant, 1.74 x 10-7 (1/ppm) (g mol/scm) (MJ/kcal) where standard temperature for (g mol/scm) is 20°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, as incorporated by reference as specified in section 33-24-01-05; and
Hi= Net heat of combustion of sample component i, kcal/9 mol at 25°C and 760 mm Hg. The heats of combustion may be determined using ASTM D 2382-83, as incorporated by reference as specified in section 33-24-01-05, if published values are not available or cannot be calculated.
c. The actual exit velocity of a flare must 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.d. The maximum allowed velocity in m/s, Vmax , for a flare complying with paragraph 3 of subdivision d of subsection 4 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 subdivision b.
e. The maximum allowed velocity in m/s, Vmax, for an air-assisted flare must be determined by the following equation: Vmax = 8.706+0.7084 (HT)
where:
8.706 = Constant,
0.7084 = Constant,
HT = The net heating value as determined in subdivision b.
6. The remanufacturer or other person that stores or treats the hazardous secondary material 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: a. 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 must 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. b. Install, calibrate, maintain, and operate according to the manufacturer's specifications a device to continuously monitor control device operation as specified below: (1) For a thermal vapor incinerator, a temperature monitoring device equipped with a continuous recorder. The device must have an accuracy of plus or minus one percent of the temperature being monitored in degrees Celsius or plus or minus five-tenths degrees Celsius, whichever is greater. The temperature sensor must be installed at a location in the combustion chamber downstream of the combustion zone.(2) For a catalytic vapor incinerator, a temperature monitoring device equipped with a continuous recorder. The device must be capable of monitoring temperature at two locations and have an accuracy of plus or minus one percent of the temperature being monitored in degrees Celsius or plus or minus five-tenths degrees Celsius, whichever is greater. One temperature sensor must be installed in the vent stream at the nearest feasible point to the catalyst bed inlet and a second temperature sensor must be installed in the vent stream at the nearest feasible point to the catalyst bed outlet.(3) For a flare, a heat sensing monitoring device equipped with a continuous recorder that indicates the continuous ignition of the pilot flame.(4) For a boiler or process heater having a design heat input capacity less than forty-four megawatts, a temperature monitoring device equipped with a continuous recorder. The device must have an accuracy of plus or minus one percent of the temperature being monitored in degrees Celsius or plus or minus five-tenths degrees Celsius, whichever is greater. The temperature sensor must be installed at a location in the furnace downstream of the combustion zone.(5) For a boiler or process heater having a design heat input capacity greater than or equal to forty-four megawatts, a monitoring device equipped with a continuous recorder to measure a parameter or parameters that indicates good combustion operating practices are being used.(6) For a condenser, either: (a) A monitoring device equipped with a continuous recorder to measure the concentration level of the organic compounds in the exhaust vent stream from the condenser, or(b) A temperature monitoring device equipped with a continuous recorder. The device must be capable of monitoring temperature with an accuracy of plus or minus one percent of the temperature being monitored in degrees Celsius or plus or minus five-tenths degrees Celsius, whichever is greater. The temperature sensor must be installed at a location in the exhaust vent stream from the condenser exit (for example, product side).(7) For a carbon adsorption system that regenerates the carbon bed directly in the control device such as a fixed-bed carbon adsorber, either: (a) A monitoring device equipped with a continuous recorder to measure the concentration level of the organic compounds in the exhaust vent stream from the carbon bed, or(b) 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.c. Inspect the readings from each monitoring device required by subdivisions a and b 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.7. A remanufacturer or other person that stores or treats hazardous secondary material in a hazardous secondary material management unit using a carbon adsorption system such as a fixed-bed carbon adsorber that regenerates the carbon bed directly onsite in the control device shall replace the existing carbon in the control device with fresh carbon at a regular, predetermined time interval that is no longer than the carbon service life established as a requirement of subparagraph f of paragraph 3 of subdivision d of subsection 2 of section 33-24-02-175.8. A remanufacturer or other person that stores or treats hazardous secondary material in a hazardous secondary material management unit using a carbon adsorption system such as a carbon canister that does not regenerate the carbon bed directly onsite 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: a. 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 must be daily or at an interval no greater than twenty percent of the time required to consume the total carbon working capacity established as a requirement of subparagraph g of paragraph 3 of subdivision d of subsection 2 of section 33-24-02-175, whichever is longer.b. 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 subparagraph g of paragraph 3 of subdivision d of subsection 2 of section 33-24-02-175.9. 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.10. A remanufacturer or other person that stores or treats hazardous secondary material at an affected facility seeking to comply with the provisions of sections 33-24-02-170 through 33-24-02-179 by using a control device other than a thermal vapor incinerator, catalytic vapor incinerator, flare, boiler, process heater, condenser, or carbon adsorption system shall 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.11. A closed-vent system must meet either of the following design requirements: a. A closed-vent system must be designed to operate with no detectable emissions, as indicated by an instrument reading of less than five hundred parts per million volume above background as determined by the procedure in subsection 2 of section 33-24-02-174, and by visual inspections; orb. A closed-vent system must be designed to operate at a pressure below atmospheric pressure. The system must be equipped with at least one pressure gauge or other pressure measurement device that can be read from a readily accessible location to verify that negative pressure is being maintained in the closed-vent system when the control device is operating. 12. The remanufacturer or other person that stores or treats the hazardous secondary material shall monitor and inspect each closed-vent system required to comply with this section to ensure proper operation and maintenance of the closed-vent system by implementing the following requirements: a. Each closed-vent system that is used to comply with subdivision a of subsection 11 must be inspected and monitored in accordance with the following requirements: (1) An initial leak detection monitoring of the closed-vent system must be conducted by the remanufacturer or other person that stores or treats the hazardous secondary material on or before the date that the system becomes subject to this section. The remanufacturer or other person that stores or treats the hazardous secondary material shall monitor the closed-vent system components and connections using the procedures specified in subsection 2 of section 33-24-02-174 to demonstrate that the closed-vent system operates with no detectable emissions, as indicated by an instrument reading of less than five hundred parts per million volume above background.(2) After initial leak detection monitoring required in paragraph 1, the remanufacturer or other person that stores or treats the hazardous secondary material shall inspect and monitor the closed-vent system as follows: (a) Closed-vent system joints, seams, or other connections that are permanently or semi-permanently sealed (for example, a welded joint between two sections of hard piping or a bolted and gasketed ducting flange) must be visually inspected at least once per year to check for defects that could result in air pollutant emissions. The remanufacturer or other person that stores or treats the hazardous secondary material shall monitor a component or connection using the procedures specified in subsection 2 of section 33-24-02-174 to demonstrate that it operates with no detectable emissions following any time the component is repaired or replaced (for example, a section of damaged hard piping is replaced with new hard piping) or the connection is unsealed (for example, a flange is unbolted).(b) Closed-vent system components or connections other than those specified in subparagraph a must be monitored annually and at other times as requested by the department, except as provided for in subsection 15, using the procedures specified in subsection 2 of section 33-24-02-174 to demonstrate that the components or connections operate with no detectable emissions.(3) If a defect or leak is detected, the remanufacturer or other person that stores or treats the hazardous secondary material shall repair the defect or leak in accordance with the requirements of subdivision c.(4) The remanufacturer or other person that stores or treats the hazardous secondary material shall maintain a record of the inspection and monitoring in accordance with the requirements specified in section 33-24-02-175.b. Each closed-vent system that is used to comply with subdivision b of subsection 11 must be inspected and monitored in accordance with the following requirements: (1) The closed-vent system must be visually inspected by the remanufacturer or other person that stores or treats the hazardous secondary material to check for defects that could result in air pollutant emissions. Defects include visible cracks, holes, or gaps in ductwork or piping or loose connections.(2) The remanufacturer or other person that stores or treats the hazardous secondary material shall perform an initial inspection of the closed-vent system on or before the date that the system becomes subject to this section. Thereafter, the remanufacturer or other person that stores or treats the hazardous secondary material shall perform the inspections at least once every year.(3) In the event that a defect or leak is detected, the remanufacturer or other person that stores or treats the hazardous secondary material shall repair the defect in accordance with the requirements of subdivision c.(4) The remanufacturer or other person that stores or treats the hazardous secondary material shall maintain a record of the inspection and monitoring in accordance with the requirements specified in section 33-24-02-175.c. The remanufacturer or other person that stores or treats the hazardous secondary material shall repair all detected defects as follows: (1) Detectable emissions, as indicated by visual inspection, or by an instrument reading greater than five hundred parts per million volume above background, must be controlled as soon as practicable, but not later than fifteen calendar days after the emission is detected, except as provided for in paragraph 3.(2) A first attempt at repair must be made no later than five calendar days after the emission is detected.(3) Delay of repair of a closed-vent system for which leaks have been detected is allowed if the repair is technically infeasible without a process unit shutdown, or if the remanufacturer or other person that stores or treats the hazardous secondary material determines that emissions resulting from immediate repair would be greater than the fugitive emissions likely to result from delay of repair. Repair of such equipment must be completed by the end of the next process unit shutdown.(4) The remanufacturer or other person that stores or treats the hazardous secondary material shall maintain a record of the defect repair in accordance with the requirements specified in section 33-24-02-175.13. Closed-vent systems and control devices used to comply with provisions of sections 33-24-02-170 through 33-24-02-179 must be operated at all times when emissions may be vented to them.14. The owner or operator using a carbon adsorption system to control air pollutant emissions shall document all carbon that is a hazardous waste and which is removed from the control device is managed in one of the following manners, regardless of the average volatile organic concentration of the carbon: a. Regenerated or reactivated in a thermal treatment unit that meets one of the following: (1) The owner or operator of the unit has been issued a final hazardous waste permit under 33-24-06 which implements the requirements of sections 33-24-05-300 through 33-24-05-309; or(2) The unit is equipped with and operating air emission controls in accordance with the applicable requirements of sections 33-24-02-170 through 33-24-02-179 and sections 33-24-02-200 through 33-24-02-214 or the applicable requirements of subsection 5 of section 33-24-06-16; or(3) The unit is equipped with and operating air emission controls in accordance with a national emission standard for hazardous air pollutants under 40 CFR part 61 or 40 CFR part 63.b. Incinerated in a hazardous waste incinerator for which the owner or operator either: (1) Has been issued a final hazardous waste permit under 33-24-06 which implements the requirements of sections 33-24-05-144 through 33-24-05-159; or(2) Has designed and operates the incinerator in accordance with the interim status requirements of subsection 5 of section 33-24-06-16.c. Burned in a boiler or industrial furnace for which the owner or operator either: (1) Has been issued a final hazardous waste permit under 33-24-06 which implements the requirements of sections 33-24-05-525 through 33-24-05-549; or(2) Has designed and operates the boiler or industrial furnace in accordance with the interim status requirements of sections 33-24-05-525 through 33-24-05-549.15. Any components of a closed-vent system that are designated, as described in subdivision i of subsection 3 of section 33-24-02-175, as unsafe to monitor are exempt from the requirements of subparagraph b of paragraph 2 of subdivision a of subsection 12 if: a. The remanufacturer or other person that stores or treats the hazardous secondary material in a hazardous secondary material management unit using a closed-vent system determines the components of the closed-vent system are unsafe to monitor because monitoring personnel would be exposed to an immediate danger as a consequence of complying with subparagraph b of paragraph 2 of subdivision a of subsection 12; andb. The remanufacturer or other person that stores or treats the hazardous secondary material in a hazardous secondary material management unit using a closed-vent system adheres to a written plan that requires monitoring the closed-vent system components using the procedure specified in subparagraph b of paragraph 2 of subdivision a of subsection 12 as frequently as practicable during safe-to-monitor times.N.D. Admin Code 33-24-02-173
Adopted by Administrative Rules Supplement 2016-359, January 2016, effective 1/1/2016.General Authority: NDCC 23-20.3-03
Law Implemented: NDCC 23-20.3-03, 23-20.3-04