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TABLE 2 CARBON VAPOR RECOVERY <br /> AUTHORITY TO CONSTRUCT PERMIT <br /> HOURS OPERATED 5828 48 5992 48 6171 48 6355 48 6447 48 6694 48 6791 98 7032 48 <br /> TIME 14 00 10 00 21 00 13 00 9 00 16 00 17 50 18 00 <br /> DATE 11/07/96 11/14/96 11/21/96 11/29/96 12/03/96 12/13/96 12/17/96 12/27/96 <br /> TFH MG/L 0 02 0 02 0 02 0 00 0 07 0 02 0 03 0 00 <br /> BENZENE MG/L 0 00 0 00 0 00 0 00 0 00 0 00 0 01 0 00 <br /> i 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 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 <br /> FLOW RATE scfm at 60F 74 98 68 18 65 54 61 10 53 74 37 52 58 08 55 37 <br />' TFH POUND PER DAY 0 119 0 108 0 141 0 017 0 357 0 081 0 169 0 005 <br /> r TOTAL LBS TFH RECOVERED 138 94 139 71 140 64 141 25 141 97 144 22 144 73 145 60 <br /># PID PPMV AS C6 0 00 0 00 0 00 0 00 0 00 0 00 5 00 0 00 <br /> METHANE 0 00 0 00 0 00 0 00 0 00 0 00 0 00 0 00 <br /> CO2 $ 0 50 NS 0 70 0 45 0 50 0 75 0 50 0 80 <br /> OXYGEN k 20 20 NM 20 00 20 00 21 00 21 00 21 00 20 50 <br /> EFFLUENT CARBON AL <br />} PID 0 00 0 00 0 00 0 00 0 00 0 00 0 50 0 00 <br /> EFFLUENT CARBON A? <br /> PID 0 00 0 00 0 00 0 00 0 00 0 00 0 50 0 00 <br /> EFFLUENT CARBON Ai <br /> PID 0 00 0 00 0 00 0 00 O 00 0 00 0 50 0 00 <br /> EFFLUENT CARBON A4 <br /> PID 0 00 0 00 0 00 0 00 0 00 0 00 1 50 0 00 <br /> i <br /> I <br /> I <br /> i <br /> i <br />