NR 440.644(4)(b)3.
3. The owner or operator of an affected facility who seeks to comply with the equipment design and performance specifications, as described under
par. (j), shall repeat the performance test when directed by the department or when the owner or operator elects to operate the capture system or control device at conditions different from the most recent determination of control device efficiency or measurement of capture system retention time or face velocity. The performance test shall be conducted in accordance with the procedures described under
par. (f) 2. b.
NR 440.644(4)(b)4.
4. The owner or operator of each tread end cementing operation and each green tire spraying operation using only water-based sprays (inside and outside or both) containing less than 1.0% by weight of VOC is not required to conduct a monthly performance test as described in
par. (d). In lieu of conducting a monthly performance test, the owner or operator of each tread end cementing operation and each green tire spraying operation shall submit formulation data or the results of Method 24 analysis annually to verify the VOC content of each tread end cement and each green tire spray material, provided the spraying formulation has not changed during the previous 12 months. If the spray material formulation changes, formulation data or Method 24 analysis of the new spray shall be conducted to determine the VOC content of the spray and reported within 30 days as required under
sub. (7) (j).
NR 440.644(4)(c)
(c) For each undertread cementing operation, each sidewall cementing operation, each green tire spraying operation where organic solvent-based sprays are used, each Michelin-A operation, each Michelin-B operation, and each Michelin-C automatic operation where the owner or operator seeks to comply with the uncontrolled monthly VOC use limits, the owner or operator shall use the following procedure to determine compliance with the applicable (depending upon duration of compliance period) uncontrolled monthly VOC use limit specified under
sub. (3) (a) 1. b.,
2. b.,
6. b.,
7. b.,
8. b.,
9. b. and
10. b. If both undertread cementing and sidewall cementing are performed at the same affected facility during a month, then the kg/mo limit specified under
sub. (3) (a) 1. b. shall apply for that month.
NR 440.644(4)(c)1.
1. Determine the density and weight fraction VOC (including dilution VOC) of each cement or green tire spray from its formulation or by analysis of the cement of green tire spray using Method 24 of Appendix A of
40 CFR part 60, incorporated by reference in
s. NR 440.17. If a dispute arises, the department may require an owner or operator who used formulation data to analyze the cement or green tire spray using Method 24 of Appendix A,
40 CFR part 60, incorporated by reference in
s. NR 440.17.
NR 440.644(4)(c)2.
2. Calculate the total mass of VOC used at the affected facility for the month (M
o) by the following procedure:
NR 440.644(4)(c)2.a.
a. For each affected facility for which cement or green tire spray is delivered in batch or via a distribution system that serves only the affected facility: -
See PDF for diagram 
where “a" equals the number of different cements or green tire sprays used during the month that are delivered in batch or via a distribution system that serves only a single affected facility.
NR 440.644(4)(c)2.b.
b. For each affected facility for which cement or green tire spray is delivered via a common distribution system that also serves other affected or existing facilities:
1) Calculate the total mass of VOC used for all of the facilities served by the common distribution system for the month (M): -
See PDF for diagram
where “b" equals the number of different cements or green tire sprays used during the month that are delivered via a common distribution system that also serves other affected or existing facilities.
2) Determine the fraction (Fo) of M used at the affected facility by comparing the production records and process specifications for the material cemented or sprayed at the affected facility for the month to the production records and process specifications for the material cemented or sprayed at all other facilities served by the common distribution system for the month or by another procedure acceptable to the administrator.
3) Calculate the total monthly mass of VOC used at the affected facility for the month (Mo):
Mo = MFo
NR 440.644(4)(d)
(d) For each tread end cementing operation and each green tire spraying operation where water-based cements or sprays containing 1.0%, by weight, of VOC or more are used (inside, outside, or both) that do not use a VOC emission reduction system, the owner or operator shall use the following procedure to determine compliance with the VOC emission per tire limit specified under
sub. (3) (a) 3.,
5. a. and
b. and
7. a. and
b.
NR 440.644(4)(d)2.
2. Calculate the total mass of VOC used at the affected facility for the month (M
o ) as specified under
par. (c) 2.
NR 440.644(4)(d)3.
3. Determine the total number of tires cemented or sprayed at the affected facility for the month (T
o ) by the following procedure:
NR 440.644(4)(d)3.a.
a. For a tread end cementing operation, T
o equals the number of tread or combined tread/sidewall components that receive an application of tread end cement for the month.
NR 440.644(4)(d)3.b.
b. For a green tire spraying operation that uses water-based inside green tire sprays, T
o equals the number of green tires that receive an application of water-based inside green tire spray for the month.
NR 440.644(4)(d)3.c.
c. For a green tire spraying operation that uses water-based outside green tire sprays, T
o equals the number of green tires that receive an application of water-based outside green tire spray for the month.
NR 440.644(4)(d)5.
5. Calculate the mass of VOC emitted per tire cemented or sprayed at the affected facility for the month (N):
N = G
NR 440.644(4)(e)
(e) For each bead cementing operation that does not use a VOC emission reduction system, the owner or operator shall use the following procedure to determine compliance with the VOC emission per bead limit specified under
sub. (3) (a) 4.
NR 440.644(4)(e)2.
2. Calculate the total mass of VOC used at the affected facility for the month (M
o) as specified under
par. (c) 2.
NR 440.644(4)(e)3.
3. Determine the number of beads cemented at the affected facility during the month (B
o) using production records; B
o equals the number of beads that receive an application of cement for the month.
NR 440.644(4)(e)5.
5. Calculate the mass of VOC emitted per bead cemented at the affected facility for the month (N
b):
Nb = Gb
NR 440.644(4)(f)
(f) For each tread end cementing operation and each bead cementing operation that use a VOC emission reduction system with a control device that destroys VOC (e.g., incinerator), the owner or operator shall use the following procedure to determine compliance with the emission limit specified under
sub. (3) (a) 3. and
4.
NR 440.644(4)(f)1.
1. Calculate the mass of VOC used per tire cemented at the affected facility for the month (G), as specified under
par. (d) 1. to
4., or mass of VOC used per bead cemented at the affected facility for the month (G
b), as specified under
par. (e) 1. to
4.
NR 440.644(4)(f)2.
2. Calculate the mass of VOC emitted per tire cemented at the affected facility for the month (N) or mass of VOC emitted per bead cemented for the affected facility for the month (N
b):
N = G(1 - R)
Nb = Gb(1 - R)
For the initial performance test, the overall reduction efficiency (R) shall be determined as prescribed under par. (f) 2. a. to d. After the initial performance test, the owner or operator may use the most recently determined overall reduction efficiency (R) for the performance test. No monthly performance tests are required. The performance test shall be repeated during conditions described under par. (b) 2.
NR 440.644(4)(f)2.a.
a. The owner or operator of an affected facility shall construct a temporary enclosure around the application and drying areas during he performance test for the purpose of capturing fugitive VOC emissions. The enclosure shall be maintained at a negative pressure to ensure that all evaporated VOC are measurable. Determine the fraction (F
c) of total VOC used at the affected facility that enter the control device: -
See PDF for diagram
where:
“m" is the number of vents from the affected facility to the control device
“n" is the number of vents from the affected facility to the atmosphere and form the temporary enclosure
NR 440.644(4)(f)2.b.
b. Determine the destruction efficiency of the control device (E) by using values of the volumetric flow rate of each of the gas streams and the VOC content (as carbon) of each of the gas streams in and out of control device: -
See PDF for diagram
where:
“m" is the number of vents from the affected facility to the control device
“p" is the number of vents after the control device
R = EFc
NR 440.644(4)(f)2.d.
d. The owner or operator of an affected facility may substitute the following procedure as an acceptable alternative to the requirements prescribed under
par. (f) 2. a. This alternative procedure is acceptable only in cases where a single VOC is used and is present in the capture system. The average capture efficiency value derived from a minimum of 3 runs shall constitute a test.
1) For each run, ``i", measure the mass of the material containing a single VOC used. This measurement shall be made using a scale that has both a calibration and a readability to within 1% of the mass used during the fun. This measurement may be made by filling the direct supply reservoir, for example, rollers, pumps, hoses, to a marked level at the start of the run and then refilling to the same mark from a more easily weighed container, for example, a separate supply drum, at the end of the fun. The change in mass of the supply drum would equal the mass of the material used in the run. If only the direct supply reservoir is weighed, the amount of material in or on the related application equipment shall be the same at the start and end of the run. All additions of VOC containing material shall be properly accounted for in determining the mass of material used during that run.
2) For each run, “i", measure the mass of the material containing a single VOC which is present in the direct supply reservoir and related application equipment at the start of the run, unless the ending weight fraction VOC in the material is greater than or equal to 98.5% of the starting weight fraction VOC in the material, in which case, this measurement is not required. This measurement may be made directly by emptying the direct supply reservoir and related application equipment and then filling them to a marked level from an easily weighed container, for example, a separate supply drum. The change in mass of the supply drum would equal the mass of material in the filled direct supply reservoir and related application equipment. Alternatively, this measurement may be made by weighing the direct supply reservoir and related application equipment at the start of the run and subtracting the mass of the empty direct supply reservoir and related application equipment (tare weight).
3) For each run, “i", the starting weight fraction VOC in the material shall be determined by Method 24 analysis of a sample taken from the direct supply reservoir at the beginning of the run.
4) For each run, “i", the ending weight fraction VOC in the material shall be determined by Method 24 analysis of a sample taken from the direct supply reservoir at the end of the run.
5) For each run, “i", in which the ending weight fraction VOC in the material is greater than or equal to 98.5% of the starting weight fraction VOC in the material, calculate the mass of the single VOC used (Mi) by multiplying the mass of the material used in the run by the starting weight fraction VOC of the material used in the run.
6) For each run, “i", in which the ending weight fraction VOC in the material is less than 98.5% of the starting weight fraction VOC in the material, calculate the mass of the single VOC used (Mi) as follows:
a) Calculate the mass of VOC present in the direct supply reservoir and related application equipment at the start of the run by multiplying the mass of material in the direct supply reservoir and related application equipment at the start of the run by the starting weight fraction VOC in the material for that run.
b) Calculate the mass of VOC present in the direct supply reservoir and related application equipment at the end of the run by multiplying the mass of material in the direct supply reservoir and related application equipment at the end of the run by the ending weight fraction VOC in the material for that run. The mass of material in the direct supply reservoir and related application equipment at the end of the run shall be calculated by subtracting the mass of material used in the run from the mass of material in the direct supply reservoir and related application equipment at the start of the run.
c) The mass of the single VOC used (Mi) equals the mass of VOC present in the direct supply reservoir and related application equipment at the start of the run minus the mass of VOC present in the direct supply reservoir and related application equipment at the end of the run.
7) If Method 25A is used to determine the concentration of the single VOC in the capture system, then calculate the capture efficiency (FC
i) for each run, “i", as follows: -
See PDF for diagram
where:
Ci is the average concentration of the single VOC in the capture system during run “i" (parts per million by volume) corrected for background VOC
NR 440.644 Note
Note:
See sub. (8) (a) 5.
W is the molecular weight of the single VOC, mg/mg-mole (lb/lb-mole)
V is the volume occupied by one mole of ideal gas at standard conditions (20°C, 760 mm Hg) on a wet basis, 2.405 x 10-5 m3/mg-mole (385.3 ft3/lb-mole)
Qi is the volumetric flow in in the capture system during run “i", on a wet basis, adjusted to standard conditions , m3 (ft3)
NR 440.644 Note
Note:
See sub. (8) (a) 5.
106 is the ppm per unity
Mi is the mass of the single VOC used during run “i", mg (lb)
8) If Method 25 is used to determine the concentration of the single VOC in the capture system, then calculate the capture efficiency (FC
i) for each run, “i", as follows: -
See PDF for diagram
where:
Ci is the average concentration of the single VOC in the capture system during run “i" (parts per million, as carbon, by volume) corrected for background VOC
NR 440.644 Note
Note:
See sub. (8) (a) 5.
W is the molecular weight of the single VOC, mg/mg-mole (lb/lb-mole)
V is the volume occupied by one mole of ideal gas at standard conditions (20°C, 760 mm Hg) on a wet basis, 2.405 x 10-5 m3/mg-mole (385.3 ft3/lb-mole)
Qi is the volumetric flow in the capture system during run“i", on a wet basis, adjusted to standard conditions, m
3 (ft3)
NR 440.644 Note
Note:
See sub. (8) (a) 5.
106 is the ppm per unity
Mi is the mass in mg of the single VOC used during run “i"
NC is the number of carbon atoms in one molecule of the single VOC
where:
“n" equals the number of runs made in the test (n u3). In cases where an alternative procedure in this paragraph is used, the requirements in par. (f) 2. b. and c. remain unchanged
NR 440.644(4)(g)
(g) For each undertread cementing operation, each sidewall cementing operation, each green tire spraying operation where organic solvent-based sprays are used, each Michelin-A operation, each Michelin-B operation, and each Michelin-C-automatic operation that use a VOC emission reduction system with a control device that destroys VOC (e.g., incinerator), the owner or operator shall use the following procedure to determine compliance with the percent emission reduction requirement specified under
sub. (3) (a) 1. a.,
2. a.,
6. a.,
7. b.,
8. a.,
9. a. and
10. a. For the initial performance test, the overall reduction efficiency (R) shall be determined as prescribed under
par. (f) 2. a. to
c. The performance test shall be repeated during conditions described under
par. (b) 2. No monthly performance tests are required.
NR 440.644(4)(h)
(h) For each tread end cementing operation and each bead cementing operation that uses a VOC emission reduction system with a control device that recovers VOC (e.g., carbon adsorber), the owner or operator shall use the following procedure to determine compliance with the emission limit specified under
sub. (3) (a) 3. and
4.
NR 440.644(4)(h)1.
1. Calculate the mass of VOC used per tire cemented at the affected facility for the month (G), as specified under
par. (d) 1. to
4., or the mass of VOC used per bead cemented at the affected facility for the month (G
b) as specified under
par. (e) 1. to
4.
NR 440.644(4)(h)2.
2. Calculate the total mass of VOC recovered from the affected facility for the month (M
r):
Mr = Lr Dr
NR 440.644(4)(i)
(i) For each undertread cementing operation, each sidewall cementing operation, each green tire spraying operation where organic solvent-based sprays are used, each Michelin-A operation, each Michelin-B operation, and each Michelin-C-automatic operation that use a VOC emission reduction system with a control device that recovers VOC (e.g., carbon adsorber), the owner or operator shall use the following procedure to determine compliance with the percent reduction requirement specified under
sub. (3) (a) 1. a.,
2. a.,
6. a.,
7. b.,
8. a.,
9. a. and
10. a.
