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• • <br /> TABLE 2 CARBON VAPOR RECOVERY SUMMARY, FORMER REGAL STATION 603 <br /> AUTHORITY TO CONSTRUCT PERMIT 4N-1090-3-1 <br /> HOURS OPERATED 0 00 72 48 239 48 430 48 912 48 1102 98 1298 98 1438 98 <br /> TIME 11 00 18 00 17 00 16 00 18 00 16 50 20 50 16 50 <br /> ' DATE 03/06/96 03/12/96 03/19/96 03/27/96 04/16/96 04/24/96 05/02/96 05/08/96 <br /> TFH MG/L 0 12 0 43 0 18 0 10 0 09 0 10 0 03 0 11 <br /> BENZENE MG/L 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 <br /> TOLUENE MG/L 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 <br /> ETHYLBENZENE MG/L 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 <br /> XYLENES MG/L 71 00 0 00 0 00 0 00 0 00 a 00 0 00 0 00 <br /> FLOW RATE ecfm at 60F 0 00 83 70 83 48 80 00 59 04 64 80 87 81 56 65 <br /> TFH POUND PER DAY 0 000 3 369 1 407 0 749 0 497 0 607 ❑ 247 0 583 <br /> TOTAL LBS TFH RECOVERED 0 00 6 08 22 69 31 27 43 78 48 17 51 65 54 07 <br /> PID PPMV AS C6 NM 9 00 9 10 7 20 8 20 8 60 6 00 1 00 <br /> METHANE t 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 <br /> CO2 t NM 0 25 NM 0 40 0 50 0 75 0 50 0 50 <br /> OXYGEN k NM 20 50 21 00 21 00 20 50 20 50 20 50 21 00 <br /> EFFLUENT CARBON Al <br /> PID 0 00 0 00 7 40 5 00 6 70 7 00 3 50 1 00 <br /> EFFLUENT CARBON A2 <br /> PID 0 00 0 00 4 20 7 00 3 60 8 00 4 80 1 00 <br /> EFFLUENT CARBON A3 <br /> PID 0 00 4 90 2 00 8 50 3 50 1 00 <br /> EFFLUENT CARBON A4 <br /> ' PID 0 00 1 10 1 50 5 60 3 50 1 00 <br /> i <br /> 1 <br /> 1 <br /> I <br /> i <br /> F <br />