NR 465.38(8)(e)4.
4. Use the data collected during the performance test to calculate and record the average pressure drop. This average pressure drop shall be the minimum operating limit for the dilute stream across the concentrator.
NR 465.38(8)(f)
(f) Emission capture systems. For each capture device that is not part of a PTE that meets the criteria of
sub. (6) (a), establish an operating limit for either the gas volumetric flow rate or duct static pressure, as specified in
subds. 1. and
2. The operating limit for a PTE is specified in Table 1 of this subchapter.
NR 465.38(8)(f)1.
1. During the capture efficiency determination required by
sub. (1) and described in
subs. (5) and
(6), you shall monitor and record either the gas volumetric flow rate or the duct static pressure for each separate capture device in your emission capture system at least once every 15 minutes during each of the 3 test runs at a point in the duct between the capture device and the add-on control device inlet.
NR 465.38(8)(f)2.
2. Calculate and record the average gas volumetric flow rate or duct static pressure for the 3 test runs for each capture device. This average gas volumetric flow rate or duct static pressure shall be the minimum operating limit for that specific capture device.
NR 465.38(9)
(9) What are the requirements for continuous parameter monitoring system installation, operation and maintenance? NR 465.38(9)(a)(a)
General. You shall install, operate and maintain each CPMS specified in
pars. (c),
(e),
(f) and
(g) according to
subds. 1. to
6. You shall install, operate and maintain each CPMS specified in
pars. (b) and
(d) according to
subds. 3. to
5.
NR 465.38(9)(a)1.
1. The CPMS shall complete a minimum of one cycle of operation for each successive 15-minute period. You shall have a minimum of 4 equally spaced successive cycles of CPMS operation in one hour.
NR 465.38(9)(a)2.
2. You shall determine the average of all recorded readings for each successive 3-hour period of the emission capture system and add-on control device operation.
NR 465.38(9)(a)3.
3. You shall record the results of each inspection, calibration and validation check of the CPMS.
NR 465.38(9)(a)4.
4. You shall maintain the CPMS at all times and have available necessary parts for routine repairs of the monitoring equipment.
NR 465.38(9)(a)5.
5. You shall operate the CPMS and collect emission capture system and add-on control device parameter data at all times that a controlled coating operation is operating, except during monitoring malfunctions, associated repairs and required quality assurance or control activities, including, if applicable, calibration checks and required zero and span adjustments.
NR 465.38(9)(a)6.
6. You may not use emission capture system or add-on control device parameter data recorded during monitoring malfunctions, associated repairs, out-of-control periods or required quality assurance or control activities when calculating data averages. You shall use all the data collected during all other periods in calculating the data averages for determining compliance with the emission capture system and add-on control device operating limits.
NR 465.38(9)(a)7.
7. A monitoring malfunction is any sudden, infrequent, not reasonably preventable failure of the CPMS to provide valid data. Monitoring failures that are caused in part by poor maintenance or careless operation are not malfunctions. Any period for which the monitoring system is out-of-control and data are not available for required calculations is a deviation from the monitoring requirements.
NR 465.38(9)(b)
(b) Capture system bypass line. You shall meet the requirements of
subds. 1. and
2. for each emission capture system that contains bypass lines that could divert emissions away from the add-on control device to the atmosphere.
NR 465.38(9)(b)1.
1. You shall monitor or secure the valve or closure mechanism controlling the bypass line in a non-diverting position in such a way that the valve or closure mechanism cannot be opened without creating a record that the valve was opened. The method used to monitor or secure the valve or closure mechanism shall meet one of the requirements specified in
subd. 1. a. to
e.
NR 465.38(9)(b)1.a.
a. Install, calibrate, maintain and operate according to the manufacturer's specifications a flow control position indicator that takes a reading at least once every 15 minutes and provides a record indicating whether the emissions are directed to the add-on control device or diverted from the add-on control device. The time of occurrence and flow control position shall be recorded, as well as every time the flow direction is changed. The flow control position indicator shall be installed at the entrance to any bypass line that could divert the emissions away from the add-on control device to the atmosphere.
NR 465.38(9)(b)1.b.
b. Secure any bypass line valve in the closed position with a car-seal or a lock-and-key type configuration. You shall visually inspect the seal or closure mechanism at least once every month to ensure that the valve is maintained in the closed position, and the emissions are not diverted away from the add-on control device to the atmosphere.
NR 465.38(9)(b)1.c.
c. Ensure that any bypass line valve is in the closed (non-diverting) position through monitoring of valve position at least once every 15 minutes. You shall inspect the monitoring system at least once every month to verify that the monitor will indicate valve position.
NR 465.38(9)(b)1.d.
d. Use an automatic shutdown system in which the coating operation is stopped when flow is diverted by the bypass line away from the add-on control device to the atmosphere when the coating operation is running. You shall inspect the automatic shutdown system at least once every month to verify that it will detect diversions of flow and shut down the coating operation.
NR 465.38(9)(b)1.e.
e. Install, calibrate, maintain and operate according to the manufacturer's specifications a flow direction indicator that takes a reading at least once every 15 minutes and provides a record indicating whether the emissions are directed to the add-on control device or diverted from the add-on control device. Each time the flow direction changes, the next reading of the time of occurrence and flow direction shall be recorded. The flow direction indicator shall be installed in each bypass line or air makeup supply line that could divert the emissions away from the add-on control device to the atmosphere.
NR 465.38(9)(b)2.
2. If any bypass line is opened, you shall include a description of why the bypass line was opened and the length of time it remained open in the semiannual compliance reports required in
s. NR 465.35 (2).
NR 465.38(9)(c)
(c) Thermal oxidizers and catalytic oxidizers. If you are using a thermal oxidizer or catalytic oxidizer as an add-on control device, including those used with concentrators or with carbon adsorbers to treat desorbed concentrate streams, you shall comply with the requirements in
subds. 1. to
3.
NR 465.38(9)(c)1.
1. For a thermal oxidizer, install a gas temperature monitor in the firebox of the thermal oxidizer or in the duct immediately downstream of the firebox before any substantial heat exchange occurs.
NR 465.38(9)(c)2.
2. For a catalytic oxidizer, install gas temperature monitors upstream or downstream or both of the catalyst bed as required in
sub. (8) (b).
NR 465.38(9)(c)3.
3. For all thermal oxidizers and catalytic oxidizers, you shall meet the requirements in
par. (a) and the requirements in
subd. 3. a. to
e. for each gas temperature monitoring device.
NR 465.38(9)(c)3.a.
a. Locate the temperature sensor in a position that provides a representative temperature.
NR 465.38(9)(c)3.b.
b. Use a temperature sensor with a measurement sensitivity of 5
°F or 1.0% of the temperature value, whichever is larger.
NR 465.38(9)(c)3.c.
c. Before using the sensor for the first time or when relocating or replacing the sensor, perform a validation check by comparing the sensor output to a calibrated temperature measurement device or by comparing the sensor output to a simulated temperature.
NR 465.38(9)(c)3.d.
d. Conduct an accuracy audit every quarter and after every deviation. Accuracy audit methods include comparisons of sensor output to redundant temperature sensors, to calibrated temperature measurement devices, or to temperature simulation devices.
NR 465.38(9)(c)3.e.
e. Conduct a visual inspection of each sensor every quarter if redundant temperature sensors are not used.
NR 465.38(9)(d)
(d) Regenerative carbon adsorbers. If you are using a regenerative carbon adsorber as an add-on control device, you shall monitor the total regeneration desorbing gas mass flow for each regeneration cycle, the carbon bed temperature after each regeneration and cooling cycle, and comply with
par. (a) 3. to
5. and
subds. 1. to
3.
NR 465.38(9)(d)1.
1. The regeneration desorbing gas mass flow monitor shall be an integrating device having a measurement sensitivity of plus or minus 10% capable of recording the total regeneration desorbing gas mass flow for each regeneration cycle.
NR 465.38(9)(d)2.
2. The carbon bed temperature monitor shall be capable of recording the temperature within 15 minutes of completing any carbon bed cooling cycle.
NR 465.38(9)(d)3.
3. For all regenerative carbon adsorbers, you shall meet the requirements in
par. (c) 3. a. to
e. for each temperature monitoring device.
NR 465.38(9)(e)
(e) Condensers. If you are using a condenser, you shall monitor the product side condenser outlet gas temperature and comply with
par. (a) and
subds. 1. and
2.
NR 465.38(9)(e)1.
1. The temperature monitor shall provide a gas temperature record at least once every 15 minutes.
NR 465.38(9)(e)2.
2. For all condensers, you shall meet the requirements in
par. (c) 3. for each temperature monitoring device.
NR 465.38(9)(f)
(f) Concentrators. If you are using a concentrator, such as a zeolite wheel or rotary carbon bed concentrator, you shall comply with the requirements in
subds. 1. and
2.
NR 465.38(9)(f)1.
1. You shall install a temperature monitor in the desorption gas stream. The temperature monitor shall meet the requirements in
pars. (a) and
(c) 3.
NR 465.38(9)(f)2.
2. You shall install a device to monitor pressure drop across the zeolite wheel or rotary carbon bed. The pressure monitoring device shall meet the requirements in
pars. (a) and
(g) 2.
NR 465.38(9)(g)
(g) Emission capture systems. The capture system monitoring system shall comply with the applicable requirements in
subds. 1. and
2.
NR 465.38(9)(g)1.a.
a. Locate a flow sensor in a position that provides a representative flow measurement in the duct from each capture device in the emission capture system to the add-on control device.
NR 465.38(9)(g)1.c.
c. Perform an initial sensor calibration in accordance with the manufacturer's requirements.
NR 465.38(9)(g)1.d.
d. Perform a validation check before initial use or upon relocation or replacement of a sensor. Validation checks include comparison of sensor values with electronic signal simulations or via relative accuracy testing.
NR 465.38(9)(g)1.e.
e. Conduct an accuracy audit every quarter and after every deviation. Accuracy audit methods include comparisons of sensor values with electronic signal simulations or via relative accuracy testing.
NR 465.38(9)(g)1.g.
g. Perform visual inspections of the sensor system quarterly if there is no redundant sensor.
NR 465.38(9)(g)2.
2. For each pressure drop measurement device, you shall comply with the requirements in
par. (a) and
subd. 2. a. to
g.
NR 465.38(9)(g)2.a.
a. Locate the pressure sensor in or close to a position that provides a representative measurement of the pressure drop across each opening you are monitoring.
NR 465.38(9)(g)2.b.
b. Use a pressure sensor with an accuracy of at least 0.5 inches of water column or 5% of the measured value, whichever is larger.
NR 465.38(9)(g)2.c.
c. Perform an initial calibration of the sensor according to the manufacturer's requirements.
NR 465.38(9)(g)2.d.
d. Conduct a validation check before initial operation or upon relocation or replacement of a sensor. Validation checks include comparison of sensor values to calibrated pressure measurement devices or to pressure simulation using calibrated pressure sources.
NR 465.38(9)(g)2.e.
e. Conduct accuracy audits every quarter and after every deviation. Accuracy audits include comparison of sensor values to calibrated pressure measurement devices or to pressure simulation using calibrated pressure sources.
NR 465.38(9)(g)2.f.
f. Perform monthly leak checks on pressure connections. A pressure of at least 1.0 inches of water column to the connection shall yield a stable sensor result for at least 15 seconds.
NR 465.38(9)(g)2.g.
g. Perform a visual inspection of the sensor at least monthly if there is no redundant sensor.
Table 1
Operating Limits if Using the Emission Rate With Add-On Controls Option in s. NR 465.33 (2) (c)
Table 2
Default Organic HAP Mass Fraction for Solvents and Solvent Blends
You may use the mass fraction values in the following table for solvent blends for which you do not have test data or manufacturer's formulation data and which match either the solvent blend name or the chemical abstract series (CAS) number. If a solvent blend matches both the name and CAS number for an entry, that entry's organic HAP mass fraction shall be used for that solvent blend. Otherwise, use the organic HAP mass fraction for the entry matching either the solvent blend name or CAS number, or use the organic HAP mass fraction from Table 3 of this subchapter if neither the name or CAS number match.
-
See PDF for table 
Table 3
Default Organic HAP Mass Fraction for Petroleum Solvent Groups a
You may use the mass fraction values in the following table for solvent blends for which you do not have test data or manufacturer's formulation data.
-
See PDF for table
a Use this table only if the solvent blend does not match any of the solvent blends in Table 2 by either solvent blend name or CAS number and you only know whether the blend is aliphatic or aromatic.
b Mineral Spirits 135, Mineral Spirits 150 EC, Naphtha, Mixed Hydrocarbon, Aliphatic Hydrocarbon, Aliphatic Naphtha, Naphthol Spirits, Petroleum Spirits, Petroleum Oil, Petroleum Naphtha, Solvent Naphtha, Solvent Blend.
c Medium-flash Naphtha, High-flash Naphtha, Aromatic Naphtha, Light Aromatic Naphtha, Light Aromatic Hydrocarbons, Aromatic Hydrocarbons, Light Aromatic Solvent.
NR 465.38 History
History: CR 05-040: cr. Register February 2006 No. 602, eff. 3-1-06. NR 465.41
NR 465.41
What this subchapter covers. NR 465.41(1)
(1)
What is the purpose of this subchapter? This subchapter establishes national emission standards for hazardous air pollutants (NESHAP) for miscellaneous metal parts and products surface coating facilities. This subchapter also establishes requirements to demonstrate initial and continuous compliance with the emission limits specified in
s. NR 465.43 (1).
NR 465.41 Note
Note: This subchapter is based on the federal regulations contained in
40 CFR part 63 Subpart MMMM, as last revised April 26, 2004.
NR 465.41(2)(a)(a) Miscellaneous metal parts and products include metal components of the following types of products as well as the products themselves: motor vehicle parts and accessories, bicycles and sporting goods, recreational vehicles, extruded aluminum structural components, railroad cars, heavy duty trucks, medical equipment, lawn and garden equipment, electronic equipment, magnet wire, steel drums, industrial machinery, metal pipes, and numerous other industrial, household and consumer products. Except as provided in
par. (c), the source category to which this subchapter applies is the surface coating of any miscellaneous metal parts or products, as described in
subd. 1., and it includes the sub-categories listed in
subds. 2. to
6.
NR 465.41(2)(a)1.
1. Surface coating is the application of coating to a substrate. When application of coating to a substrate occurs, then surface coating also includes associated activities, such as surface preparation, cleaning, mixing and storage. However, these activities do not comprise surface coating if they are not directly related to the application of the coating. Coating application with hand-held, non-refillable aerosol containers, touch-up markers, marking pens or the application of paper film or plastic film which may be pre-coated with an adhesive by the manufacturer are not coating operations for the purposes of this subchapter.
NR 465.41(2)(a)2.
2. The general use coating sub-category includes all surface coating operations that are not high performance, magnet wire, rubber-to-metal or extreme performance fluoropolymer coating operations.
NR 465.41(2)(a)3.
3. The high performance coating sub-category includes surface coating operations that are performed using coatings that meet the definition of high performance architectural coating or high temperature coating in
s. NR 465.42 (22).
NR 465.41(2)(a)4.
4. The magnet wire coating sub-category includes surface coating operations that are performed using coatings that meet the definition of magnet wire coatings in
s. NR 465.42 (26).
NR 465.41(2)(a)5.
5. The rubber-to-metal coatings sub-category includes surface coating operations that are performed using coatings that meet the definition of rubber-to-metal coatings in
s. NR 465.42 (39).
NR 465.41(2)(a)6.
6. The extreme performance fluoropolymer coatings sub-category includes surface coating operations that are performed using coatings that meet the definition of extreme performance fluoropolymer coatings in
s. NR 465.42 (18).
NR 465.41(2)(b)
(b) You are subject to this subchapter if you own or operate a new, reconstructed or existing affected source, as defined in
sub. (3), that uses 946 liters (250 gallons) per year, or more, of coatings that contain hazardous air pollutants (HAP) in the surface coating of miscellaneous metal parts and products defined in
par. (a); and that is a major source, is located at a major source or is part of a major source of emissions of HAP. A major source of HAP emissions is any stationary source or group of stationary sources located within a contiguous area and under common control that emits or has the potential to emit any single HAP at a rate of 9.07 megagrams (Mg) (10 tons) or more per year or any combination of HAP at a rate of 22.68 Mg (25 tons) or more per year. You do not need to include coatings that meet the definition of non-HAP coating contained in
s. NR 465.42 (31) in determining whether you use 946 liters (250 gallons) per year, or more, of coatings in the surface coating of miscellaneous metal parts and products.
NR 465.41(2)(c)
(c) This subchapter does not apply to surface coating or a coating operation that meets any of the criteria of
subds. 1. to
17.
NR 465.41(2)(c)1.
1. A coating operation conducted at a facility where the facility uses only coatings, thinners and other additives, and cleaning materials that contain no organic HAP, as determined according to
s. NR 465.46 (2) (a).
NR 465.41(2)(c)2.
2. Surface coating operations that occur at research or laboratory facilities, or are part of janitorial, building and facility maintenance operations, or that occur at hobby shops that are operated for noncommercial purposes.
NR 465.41(2)(c)3.
3. Coatings used in volumes of less than 189 liters (50 gallons) per year, provided that the total volume of coatings exempt under this paragraph does not exceed 946 liters (250 gallons) per year at the facility.
NR 465.41(2)(c)4.
4. The surface coating of metal parts and products performed on-site at installations owned or operated by the armed forces of the United States, including the Coast Guard and the National Guard of any state, or the National Aeronautics and Space Administration, or the surface coating of military munitions manufactured by or for the armed forces of the United States, including the Coast Guard and the National Guard of any state.
NR 465.41(2)(c)5.
5. Surface coating where plastic is extruded onto metal wire or cable or metal parts or products to form a coating.
