Document kJQJDeQbxp6LR5LJed9Y57ED

FORM N0.45A.202- 1 1 HCL VOLUME 1964 Av.G. % HCl 96.64 i____________________________________ 3.07 CO, 0.01 ____________________________________ 0.07 CO 0.03 N2 0.21 Total Organics - Chlorine 0 JAN FEB 96.36 96.18 3.06 3.24 0.03 0.02 0.13 0.11 0.02 0.02 0.40 0.44 --- 00 PITTSBURGH PLATE GLASS COMPANY CHEMICAL DIVISION LAKE CHARLES, LOUISIANA LABORATORY OPERATIONS REPORT CONFIDENTIAL: _ Subject to Protective Order of 14th Judicial District Court No, 91-1145 MAR APR MAY JUNE JULY AUG SEP OCT NOV DEC 1965 Avg. * 96.46 96.62 3.04 2.87 0.02 0.00 0.10 ` 0.10 0.01 0.00 0.37 0.40 -- 0O 96.16 3.46 n.m 0.07 0.00 0.30 n 96.54 3.07 0.00 0.08 0.00 0.30 0 96.46 96.38 3.23 3.13 0.01 0.02 0.06 0.10 0.00 0.01 0.23 0.35 -- 00 96.66 3.14 0.01 0.03 0.01 0.15 -- 0 96.59 3.24 0.01 0.04 0.01 0.12 - 0 96.74 2.98 0.00 0.06 0.00 0.22 0 96.40 3.35 0.00 0.05 0.01 0.19 0 96.46 3.15 0.01 0.08 0.01 0.29 -- 0 Product H.,0 56ppm 46 68 51 66 6s 36 30 32 70 59 54 56 53 , CO I o - No vj CO Ul - I FORM Nn -i' , I I - 1 SL 012797 PITTSBURGH PLATE GLASS COMPANY CHEMICAL DIVISION LAKE CHARLES, LOUISIANA HYDROGEN CHLORIDE DEPARTMENT OPERATIONS CONFIDENTIAL Subject to Protective nrder of 14th Judicial District Court No. 91-1145 REPORT GENERAL DEPARTMENT HCl Shipped Cl2to HCl H? to HCl T/D t/D MCF/D 1964 AVG . JAN 16.6 23.4 18.0 24.5 -202.9 293.3 FEB MAR "2573" 27.8 27.0 27.6 314.2 336.4 APR 28.7 23.1 346.5 MAY 28.6 28.0 349.5 JUNE 23.2 27.6 348.3 JULY 27.1 27.7 344.3 AUG 28.0 26.9 349.4 SEP OCT NOV DEC 35.8 44.3 45.0 46.4 36.5 44.9 44.5 46.0 439.7 513. r 532.7 537 .2 1965 Avg. 32.5 32.4 392.0 Lbs. Cl2/ton HCl MCF H2/Ton HCl 2200 2088 12 12 2090 1984 1955 1959 1961 2045 1918 1967 1956 1940 1964 1986 12 12 12 12 12 13 12 12 11 12 12 12 KIH/T Well Water _195.5 158.4 145.1 133.1 129.1 124.7 121.9 132.5 134.8 93.5 79.8 80.0 75.3 117.4 M Gals./T 22. 4 16.5 14.9 14.2 13.6 14.2 13.8 13.2 12.5 11.9 10.2 9.6 9.2 12.8 MAN HOURS PER t'ON HCl Producti on Ma i ntenance SALAR1 ED Total Contract M*int. included in above 0.332 0.598 0.451 0.206 0.356 0.148 1.639 0.952 00 0.491 "07565 0.466 07581" 0.478 0.168 0.073 0.099 0.062 0.258 0.148 0.143 0.131 0.121 0.140 0.807 ~0MI 0.696 0.664 0.876 0 ~0 0 0 0 0.517 0.085 0.134 0.736 0 0.481 0.190 0.136 0.807 0 0.414 0.774 0.105 1.293 0 0.332 0.153 0.082 0.567 0 0.333 0.310 0.174 0.096 0.079 0.078 0.586 0.484 00 0.447 0.195 0.120 0.762 0 Line PRESSURE Comp. Disch. Comp. Suct p si G psig " H20 temperature" Gas from #1 Cooler Gas from #2 Cooler Compressor Discharge OT 47 52 16 44 48 286 44 52 18 - 51 235 45 45 44 56 "55 53 22 25 26 --_ 48 47 47 301 300 302 44 58 27 i.8 303 44 44 44 57 57 56 26 27 27 _ 49 49 48 305 306 312 44 48 57 53 23 25 48 45 48 44 299 289 49 46 54 51 28 28 46 47 46 46 290 274 45 55 2.5 ti.fi 48 297 FLOW CU. FT./HOUR H? to 0) Burner H? to W2 Burner 159 128 -- --. - _ - a. i' Cl2 to wi Burner 5 ZCl to Burner 151 111 - --- --- --_ a. _ -- -- -- a. mm Well Water to HCl Operating Time gpm 271 *256 % 76 96 260 "256 100 100 2c 3 100 273 263 100 100 239 231 321 100 100 91 320 300 293 100 97 100 274 _ 99______