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Ta <br /> Treatment System erformance Data <br /> The Transmission Shop <br /> 515 West Charter Way <br /> Stockton,California <br /> Field TPN as Gasoline Benzene <br /> FID Readino <br /> Hour Meter Percent Blower Flow Rate Total System Influent Net Removed Influent Net Removed <br /> Site Visit Reading Operational Vacuum at Manifold Flow Rate Influent Effluent Concentration Removed' to Date Concentration Removed' to Date <br /> Date Description Comments (hours) (°/°} ("H2O) (scfm) (scfm) (ppmv) (ppmv) (mglm3) (pounds) (pounds) (mg1m3) (pounds) (pounds) <br /> 03/05101 Samplel0&M 7 964 100 57 48 45 150 60 228 7 2 323 <0 25 001 25 <br /> 03112101 O&M 8 014 30 59 46 43 230 100 --- 2 2 325 — 000 25 <br /> 03!19101 0&M 8182 100 74 43 39 350 95 6 2 330 — 001 25 <br /> 03/29101 O&M 9422 100 78 46 48 140 50 — 10 2 340 — 001 25 <br /> 04!02101 8amplel0&M 8 517 99 80 45 42 180 50 112 2 2 342 <0 25 000 26 <br /> 040101 0&M 8 685 100 82 3B 30 150 38 --- 2 2 344 — 000 25 <br /> REPORTING PERIOD FIRST QUARTER 2001;JANUARY 4,2001 THROUGH MARCH 29,1001 - m <br /> POUNDS REMOVED SINCE STARTUP 2,340 _ 25 <br /> GALLONS REMOVED SINCE STARTUPE_ 384 _ ?_ 03^ A <br /> POUNDS REMOVED FROM JANUARY 4 THROUGH MARCH 29,2061 1780 <br /> GALLONS REMOVES]FROM JANUARY 4 THROUGH MARCH 29,2001 _ _ ^29 2 00 <br /> AVERAGE FLOW RATE FROM JANUARY 4 THROUGH MARCH 29,2001 E <br /> PERCENT OPERATIONAL FROM JANUARY 4 THROUGH MARCH 29,2001 ; 67% <br /> PH=7otal petroleum hydrocarbons Total system flaw rate accounts for the flow after dilution <br /> H2O=Inches of water Density of benzene=7 34 pounds per gallon <br /> sch=Standard cubic feet per minute Density of gasdine=61 pounds pergallon <br /> ppmv=Parts per n on by volume =Since last hour meter reading <br /> NA=Not avalable or not applicable Analybcai result notavadable at bme of reW preparation <br /> IT CORPORATION <br /> N ISxflPIZ001Ws1e80-0139 1A1041901ml ids <br /> Page 2 of 2 <br />