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i i i i i >• i >� i i i �� � i ��
<br /> Table 1 -
<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-ReajlnS
<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 Descnpdon Comments (hours) N ("H2O) (scfm) (scfm) (ppmv) (ppmv) (mg1m3) (pounds) (pounds) (mg1m3) (pounds) (pounds)
<br /> 01/31/00 Sample/O&M Startup 2,373 NA NA NA 37 4,800 1,200 4 910 0 0 155 0 000
<br /> 02/03100 Sample/O&M Startup 2,375 3 NA 12 15 2,000 800 4,690 1 1 <2 50 0 000
<br /> 03/08/00 Sample/O&M 2 851 58 76 NA 43 600 18 8,100 493 493 295 021 021
<br /> 03113/00 O&M System down-pending repair of heating coil and high temperature valve sha --- - - 0 493 - 000 021
<br /> 04/21/00 O&M Repair/Restart 2,975 12 52 43 43 - - -- 158 651 --- 130 151
<br /> 04/24/00 Sample/O&M 3,039 88 50 57 47 1,500 85 7 900 90 742 <2 50 003 153
<br /> 05/01100 Sample/O&M 3,206 100 54 NA 53 700 8 4,650 207 949 <2 50 008 162
<br /> 06105100 SampletO&M 3,717 61 28 36 31 3,000 800 4,810 284 1,233 <0 500 009 171
<br /> 07110/00 Sample/O&M 4,150 52 75 52 43 300 50 504 184 1,417 <0160 009 180
<br /> 07/17/00 O&M KO tank full 4,178 17 - --- --- - - --- 0 1,417 - 000 180
<br /> 07124/00 O&M Unknown 4,199 12 92 76 72 5,000 3000 --- 10 1,427 --- 001 180
<br /> 08107/00 Sample/O&M KO tank full 4,229 9 68 61 55 2,500 1,800 3,180 10 1,437 1 71 001 1 81
<br /> 08/14/00 O&M KO tank full 4,397 100 80 69 42 350 55 - 104 1 541 --- 004 1 85
<br /> 08/28/00 O&M 4,734 100 80 74 43 150 35 --- 215 1,757 - 008 193
<br /> 09/07100 Sample/O&M KO tank full 4,759 10 60 55 49 3,000 1,500 4,800 22 1,779 <1 25 001 194
<br /> 09/11/00 0&M 4,856 101 60 57 45 3200 1,200 - 78 1,857 --- 002 196
<br /> 09118/00 0&M 5,023 100 64 52 40 --- - - 121 1,978 --- 003 1 99
<br /> 10104100 Sample/O&M- 5 407 100 78 70 43 - - 295 2 273 -- 008 207
<br /> {t PORTING PERtOD-JULY�1� HR GH SEPTEMBER330;2000 n x w � '" E r �.'� ;"
<br /> 2 O7
<br /> POUNDS`IMOVED FROM JANUARY 31,2000 THROIfGH OCTOBER 4;2000 = �� v °-� �# N a �' 2,273 /� p
<br /> -.N.0 tw " vSa. Ilk a S b U '" Y�O
<br /> GALLON REMOVED FROM JANUARY31;200D THROi1GH OCTOBER 4,`2aD0=�` `_ `rs -,� "� 373 i
<br /> A 9rY^Sx�X �.r m m - m f-F -- -:I 4
<br /> POUNDS REMOVED FIR 10 THROUGH OCT6BER 4,2000 `; y; = '- m "� -s r 856 0 27 � - r
<br /> C - _ _ �x- y r�rw
<br /> GALLONS REMOVED FROM JULY 1D THI�OUGHFOCTOHEFt 4 2000 x -,_ 140 0 04 _ Asa
<br /> aP
<br /> t'4"`X..""amE <y' - I -. V-., ��
<br /> AVERAGE FLOW�RAsFiOMJULY 10 THROUGH OCTOBER 4,240R•= 48 -x _ �; � - ;
<br /> r x4�
<br /> PERCENT�OPERATIONAL FRO M�JULYz1D,THROUGH,OCT013€R4;"2000,s 60°/
<br /> }
<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 /> 8800391AISvedata(new)ITABLE 1 10/10/00
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