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0 9 a <br /> TABLE 3 <br /> VAPOR REMEDIATION SYSTEM STATUS <br /> THRIFTY OIL STATION 11171, STOCKTON, CA <br /> Hour meter Cumulative Hrssince Vapor Inlet TPHg TPHg removed Cumulative TPHg Mass Volume <br /> Date reading Operation Last visit Flow Rate Concentration within period TPHg removed Removal Rate Removed <br /> (hrs)` (hrs) (hrs) (cfm) (ppmv) (ug1L) (Ibs) (Ibs) (tbs/hr) (gallons) Remarks <br /> 01131105 16 996 31 836 172 144 2 240 20533 142 582 1 19 22 632 1 <br /> 02/07/05 17 167 32 007 171 144 No 12 5 N0 5525 105 69 142 688 062 22 646 9 Shur down system for ows <br /> 02/14105 17 167 32 007 0 143 5525 142 688 22 648 9 Restarted <br /> 02/21/05 17 330 32 170 163 141 5525 478 142 693 003 22 649 6 <br /> 02/28/05 17 426 32 266 96 141 5525 280 142 696 003 22 650 1 <br /> 03107/05 17 524 32 364 98 143 531 2 170 5791 142 753 059 22 659 3 <br /> 03/14105 17 616 32 456 92 142 2 170 10640 142 860 1 16 22 676 2 <br /> 03121/05 17 632 32 472 16 141 2 170 1837 142 878 1 15 22 679 1 Found system off restarted <br /> NOTE Inlet Concentration obtained from laboratory analytical results and assumed the same until subsequent sampling event <br /> Volume of hydrocarbons removed calculation assumes gasoline density of 6 3 <br /> In February 2002 this table was corrected due to some formula errors in the hydrocarbon removal columns Older versions of this table may have different numbers <br /> f <br /> E <br /> 1 <br /> 171ves Page 6 of 4/52005 <br />