Ca = the VOC concentration in each gas stream leaving the control device and entering the atmosphere (parts per million by volume, as carbon).
Cb = the VOC concentration in each gas stream entering the control device (parts per million by volume, as carbon).
Cf = the VOC concentration in each gas stream emitted directly to the atmosphere (parts per million by volume, as carbon).
Dc = density of each coating, as received (kilograms per liter).
Dd = density of each diluent VOC solvent (kilograms per liter).
Dr = density of VOC solvent recovered by an emission control device (kilograms per liter).
E = VOC destruction efficiency of the control device (fraction).
F = the proportion of total VOC's emitted by an affected facility that enters the control device (fraction).
G = the volume-weighted average mass of VOC's in coatings consumed in a calendar month per unit volume of coating solids applied (kilograms per liter).
Lc = the volume of each coating consumed, as received (liters).
Ld = the volume of each diluent VOC-solvent added to coatings (liters).
Lr = the volume of VOC-solvent recovered by an emission control device (liters).
Ls = the volume of coating solids consumed (liters).
Md = the mass of diluent VOC-solvent consumed (kilograms).
Mo = the mass of VOC's in coatings consumed, as received (kilograms).
Mr = the mass of VOC's recovered by an emission control device (kilograms).
N = the volume weighted average mass of VOC emissions to the atmosphere per unit volume of coating solids applied (kilograms per liter).
Qa = the volumetric flow rate of each gas stream leaving the control device and entering the atmosphere (dry standard cubic meters per hour).
Qb = the volumetric flow rate of each gas stream entering the control device (dry standard cubic meters per hour).
Qf = the volumetric flow rate of each gas stream emitted directly to the atmosphere (dry standard cubic meters per hour).
R = the overall VOC emission reduction achieved for an affected facility (fraction).
T = the transfer efficiency (fraction).
Vs = the proportion of solids in each coating (or input stream), as received (fraction by volume).
Wo = the proportion of VOC's in each coating (or input stream), as received (fraction by weight).
(SUM Ldj Ddj will be 0 if no VOC solvent is added to the coatings, as received.)
Where: n is the number of different coatings used during the calendar month and m is the number of different diluent VOC-solvents used during the calendar month.
Where: n is the number of different coatings used during the calendar month.
Select the appropriate transfer efficiency from Table 1. If the owner or operator can demonstrate to the satisfaction of the Technical Secretary that transfer efficiencies other than those shown are appropriate, the Technical Secretary will approve their use on a case-by- case basis. Transfer efficiency values for application methods not listed below shall be determined by the Technical Secretary on a case-by-case basis. An owner or operator must submit sufficient data for the Technical Secretary to judge the accuracy of the transfer efficiency claims.
TABLE 1. - Transfer Efficiencies
Application methods | Transfer | efficiency (T) |
Air atomized spray | 0.25 | |
Airless spray | .25 | |
Manual electrostatic spray | .60 | |
Nonrotational automatic electrostatic spray | .70 | |
Rotating head electrostatic spray | ||
(manual and automatic) | .80 | |
Dip coat and flow coat | .90 | |
Electrodeposition | .95 |
Where more than one application method is used within a single surface coating operation, the owner or operator shall determine the composition and volume of each coating applied by each method through a means acceptable to the Technical Secretary and compute the weighted average transfer efficiency by the following equation:
Where n is the number of coatings used and p is the number of application methods used.
N = G
Where n is the number of gas streams entering the control device and m is the number of gas streams emitted directly to the atmosphere.
Where: n is the number of gas streams entering the control device, and m is the number of gas streams leaving the control device and entering the atmosphere.
R = EF
N = G (1-R)
Mr = Lr Dr
Tenn. Comp. R. & Regs. 1200-03-16-.37
Authority: T.C.A. §§ 68-25-105 and 4-5-202.