Document reEdpmXLrNE4RmdY22vQaBjdE

STANDARD OPERATING PROCEDURE Calculation of the 24-hour average concentration of Vinyl Chloride leaving the Stripping System in ppm on a Dry Resin Basis The calculation is as follows: <JCC 101797 Where: A = 24-hour average concentration of Vinyl Chloride leaving the stripping system in ppm on a dry resin basis. T = Type T resin means resin produced by the solvent process. K = Total number of grades of resin produced during the 24-hour period. L = Total number of times that samples were taken during the production of the grade resin in the 24-hour period. G = Garde of resin e.g., G,. G2. P = Flow rate of stripped varnish to the field storage tanks lb/hour. M = Concentration of Vinyl Chloride in the stripped varnish sample in ppm. F = Flow rate of the rectifying column tails to solvent recover in Ib/hour. C = Concentation of Vinyl Chloride in the rectifying column tails going to solvent recovery in ppm. Qt = Total production of type T resin over the 24-hour period. P = is calculated using this formula: P = T + A + E- (V + S + B + D) Where: T = Total autoclave feeds in lb/hour. A = Acetone flow to the acetone vaporizer in 16/hour. V = Vinyl Chloride make in lb/hour. S = Acetone to solvents in lb/hour. B = Acetone to B-3 in lb/hour. D = Acetone from rectifying column tails to dilution tank in lb/hour. E = Acetone from 2708 tank to dilution tank in lb/hour. UCC 101798 Q is calculated using this formula: T Where: R = Percent total solids in the stripped va ish as a weight percent. UCC 101799 be: Mr. T. D. Epps* Mr. J. F. Erdmann Mr. C. E. Fry Mr. R. E. George Mr. M. E. Griffith Mr. R. T. Kramer* Mr. R. J. Murawski Mr. G * G. Weissert Mr. R. N. Wheeler, Note to be recipients: Resin A is VYLF Resin B is VMCA Resin C is VROH Resin D is VYHG Resin E is VYHG ^Circulated Copies UCC 101800