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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 Readin
<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) (mg1m3) (pounds) (pounds)
<br /> 01/15/01 O&M 6,936 100 50 52 45 250 110 39 2,223 --- 004 24
<br /> 01/22/01 O&M 7,104 99 52 51 46 300 100 39 2,262 - 004 25
<br /> 01/29/01 O&M 7,192 52 43 49 43 310 90 --- 19 2,282 --- 002 25
<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 0&M 7,796 67 42 47 45 550 30 --- 7 2,317 001 25
<br /> 03/05/01 Sample/0&M 7,964 100 57 48 45 150 60 228 5 2,321 <0 25 001 2 5
<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 2 6
<br /> 04/23/01 O&M 9,021 100 90 NA 17 350 65 5 2 369 --- 000 2 6
<br /> 04/30/01 0&M 9,025 2 System down due to high water knockout&no power for system restart-System restarted on 5/21101
<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 6 2,375 <0 01 000 26
<br /> 06/11/01 O&M 9,529 100 96 44 40 40 40 -- 3 2,378 -- 000 26
<br /> 06/20/01 0&M 9,676 68 90 47 39 --- - 3 2,380 --- 000 26
<br /> 06/25/01 0&M 9,787 93 76 48 42 - --- --- 2 2,383 000 26
<br /> REPQRTING;PERfODSECONDQUARTER2o01,APRIL2;�20D1THROUGH(JUNE 25;2DD1�� l ss `, � t
<br /> POUNDS',REMOVEDYSINCEVSTARTUP' ? � 2,383 2 6
<br /> ws,..f i u
<br /> � � � E391 t^ ate 03
<br /> GAUL`ON&REMOVED SINCE STARTUP o> r 9i�
<br /> POUNDS`REMOVED FRAM APRlL 2�,20 D1�171-11ROUGK�JUNE=25;2001
<br /> � , ss
<br /> GAL'LONS$REMOVED�FROM APRIL 2,2001 THADUGH�JUNE�25;,2D01 � � '�',�.. `µ„_�� Vit, ��,{ -� ,$ 7 �-,„z�: � 00
<br /> AVERAGEFL'OWRATEIFROM;APRIL�2 2DO11THROUGH JUNE 25,2001 3 38 - x#
<br /> PER ECiJTsOPREATIONALFORM�APfiIL�2;,2o01THROIJGH,JUNE 25,t20oi 63 � � '05
<br /> nj
<br /> TPH=Total petroleum hydrocarbons Total system flow rate accounts for the flow after dilution
<br /> "H20=Inches of water Density of benzene=7 34 pounds per gallon
<br /> scfm=Standard cubic feet per minute Density of gasoline=6 1 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 /> 88*A1Svedala_2g01\TABLE 1 &2 of 2 10/4/2001
<br /> � .� r ..s. ttitttttt�f /lit.. ta■I■ r ■� I♦ � � r � � � �
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