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Table D1
<br /> Treatment System Performance Data
<br /> The Transmission Shop
<br /> 515 West Charter Way
<br /> Stockton,California
<br /> Field TPH as Gasoline Benzene
<br /> FID Reading
<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) N ('H2O) (scfm) (scfm) (ppmv) (ppmv) (mg/m3) (pounds) (pounds) (mg/m3) (pounds) (pounds)
<br /> 02/05/01 Sample/O&M 7,347 93 40 47 44 1000 250 473 9 2,291 <0 5 001 25
<br /> 02/12/01 O&M 7,515 100 40 49 45 400 90 --- 10 2,300 --- 001 25
<br /> 02/19/01 O&M 7,684 100 43 40 43 130 35 --- 9 2,310 001 25
<br /> 02/26/01 O&M 7,796 67 42 47 45 550 30 --- 7 2,317 --- 001 25
<br /> 03/05/01 Sample/O&M 7,964 100 57 48 45 150 60 228 5 2,321 <0 25 001 25
<br /> 03/12/01 O&M 8,014 30 59 46 43 230 100 --- 1 2,323 --- 000 25
<br /> 03/19/01 O&M 8,182 100 74 43 39 350 95 --- 4 2,327 001 25
<br /> 03/29/01 O&M 8,422 100 78 46 48 140 50 --- 7 2,334 --- 001 25
<br /> 04/02/01 Sample/O&M 8,517 99 80 45 42 180 50 112 7 2,342 <0 25 000 25
<br /> 04/09/01 O&M 8,685 100 82 38 30 150 38 --- 9 2,351 --- 000 25
<br /> 04/16/01 O&M 8,853 100 82 40 40 280 60 --- 12 2,363 --- 001 26
<br /> 04/23/01 O&M 9,021 100 90 NA 17 350 65 5 2,369 --- 000 26
<br /> 04/30/01 O&M 9,025 2 System down due to high water knockout&no power for system restart-System restarted on 5121/01
<br /> 05/21/01 Sample/O&M 9,025 NA 82 61 49 >10K >10K 874 0 2,369 <0 25 000 26
<br /> 06/04/01 Sample/O&M 9,362 100 92 47 41 100 35 120 8 2,377 <0 01 000 26
<br /> 06/11/01 O&M 9,529 100 96 44 40 40 40 --- 4 2,381 --- 000 26
<br /> 06/20/01 O&M 9,676 68 90 47 39 --- --- - 3 2,384 000 26
<br /> 06/25/01 O&M 9,787 93 76 48 42 --- --- - 3 2,387 000 26
<br /> 07/09/01 O&M 10,123 100 68 44 40 --- --- --- 8 2,395 -- 000 26
<br /> 07/16/01 Sample/O&M 10,292 100 68 43 39 125 45 40 1 2,396 <0 01 000 26
<br /> 07/24/01 O&M 10,483 99 70 43 41 , 150 40 System shut down pending contract negotiations
<br /> REP,ORTING)PERIOD,THIRD QUARTERi2001PJULY 91THROUGH,JULYA24,12001 K;iy A
<br /> POUNDS'REMOVED SINCE1,STARTUP.' ° 2,396
<br /> t 26
<br /> GAL OL N EMOVED SI C ARTUP393 t
<br /> f f 03
<br /> POIJNDS:REMOVED)FROM JJULY�9PTHRQUGH JULV24;12001 9 0
<br /> . , P
<br /> L'Exw!kP�°a;`� '7 6 5xi xFC�rSFY.
<br /> GALLONS�REMOVED FROM ULULY69 THROUGH JULY 2LV jV6WM0 4,2001. 1 nn s
<br /> AVERAGE FLOW RATE FROM JULY 9 T'H OUGH JULM4 2001. 40 F
<br /> 41 � � c .-
<br /> PERCENT&OPERATIONAFROMJULY/97HROUGH�JULY24;2001: 100%
<br /> TPH=Total petroleum hydrocarbons Total system flow rate accounts for the flow after dilution
<br /> "H2O=Inches of water Density of benzene=7 34 pounds per gallon
<br /> scfm=Standard cubic feet per minute Density of gasoline=61 pounds per gallon
<br /> ppmv Parts per million by volume `=Since last hour meter reading
<br /> NA=Not available or not applicable "=Analytical result not available at time of report preparation
<br /> 8*1 A1Svedata_3g01\TABLE 1 Sle 2 of 2 10/24/2001
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