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r rr r rw r r ■r ti r ra r r� �r r�• �I Table 1 Treatment System Performance Data The Transmission Shop 515 West Charter Way Stockton,California Field TPH as Gasoline Benzene FID RWing Hour Meter Percent Blower Flow Rate Total System Influent Net Removed Influent Net Removed Site va Reading Operational Vacuum 0 Mandold Flow Rate Influent Effluent Concentra8pn Removed' to Date Concentration Removed' tD Date Date Descripllon Comments (hours) (%) ('H20) (scfm) (scfm) (ppmv) (ppmv) (mg1m3) (pounds) (pounds) ("3) (pounds) (pounds) i 1/31100 Sample/O&M Startup 2373 NA NA NA 37 4,800 1,200 4910 0 0 155 0 00 2!030 Sample/O&M Startup 2 375 3 NA 12 15 2,000 800 4 690 1 1 <2 50 0 00 03108!00 Samp"&M 2 851 58 76 NA 43 600 18 8100 493 493 295 0 21 02 03113100 0&M System down-pending repair of haatmg coil and high temperature valve shaft — — — D 493 — DDD 0 2 AMID0 O&M Rep&/Restan 2975 12 52 43 43 — — 158 651 — 130 15 )41241D0 Samplef0&M 3 039 88 50 57 47 1 500 85 7 900 90 742 <2 50 003 15 01100 Sample/O&M 3206 10D 54 NA 53 7D0 8 4 650 207 949 <250 008 16 06105100 Sampl"M 3,717 61 28 36 31 3,000 800 4,810 284 1,233 <0500 009 17 07/10100 Samplel0&M 4150 52 75 52 43 300 50 504 184 1417 <0160 009 18 07/17100 0&M KO tank full 4,178 17 — — --- — — — 0 1417 — 000 18 07124!00 0&M Unknown 4199 12 92 76 72 5,000 3000 --- 10 1427 — 001 18 08107100 SampWNDW KO tank fug 4 229 9 68 61 55 2 500 1800 3,180 10 1437 171 001 18 08!14100 0&M KO tank fug 4,397 100 8D 69 42 350 55 -- 104 1,541 — 004 19 08128100 0&M 4734 100 80 74 43 150 35 — 215 1,757 — 008 19 09107100 Samplel0&M KO tank fun 4 759 10 60 55 49 3,000 1,500 4 800 18 1,775 <125 001 19 09111100 0&M 4 856 101 60 57 45 3 200 1200 --- 78 1853 — 001 2 0 09/18100 O&M 5,023 100 64 52 40 — — — 121 1974 — 002 20 10/04100 Sample/O&M- 5 407 100 78 70 43 — — 1020 179 2153 <0 500 0 09 21 101D910D O&M 5 527 100 78 63 44 900 400 — 20 2,173 — 003 21 10/16100 0&M 5 695 100 78 61 56 100 25 — 36 2,209 — 005 21 10/25100 0&M 5,911 100 68 63 55 100 60 — 45 2 254 — 007 22 10/30100 O&M 5,938 22 System down due to no power in compound D 2 254 000 22 11/30/00 O&M 5 938 0 System down due to failed acuator valve 0 2 254 000 22 12104100 0&M 5,938 0 64 — 59 — — — 0 2,254 — 000 22 12!13100 Sample=m 6154 10D 70 58 62 — — 566 40 2,294 <Z50 013 23 12118100 0&M 6,265 93 fit 60 57 900 450 — 34 2,328 — 006 24 011D4101 SampWO&M baked catalyst 6,674 100 42 48 46 ?1000 X1000 2 260 158 2,486 26 018 26 REPORTING PERIOD FOURTH QUARTER 2000,OCTOBER4 THROUGH JANUARY 4 2001 POUNDS REMOVED SINCE STARTUP r 2.6 GALLONS REMOVED SINCE STARTUP 408 r OA POUNDS REMOVED FROM OCTOBER 4 THROUGH JANUARY 41215011- GALLONS ;2001•ALLONS REMOVED FROM OCTOBER 4 THROUGH JANUARY 4,2001' S5 01 AVERAGE FLOW RATE FROM OCTOBER 4THROUGH JANUARY 4,2001 i 53 J, PERCENT'OPERATIONAL FROM OCTOBER 4 THROUGH JANUARY4,2001' 57% n 4 I =Total petroleum hydrocarbons Total system Sow rate accounts for the Sow after dilutim H2O=Inches of water Densly of benzene e 7 34 pounds per galon �clnn=Standard cubic feet per minute Density of gasoGrre=61 pounds per gallon pmv=Pats per minion by volume =Since last hour meter reading FA=Not available or not applicable Anaiytcal result not evadable M lime of report prepard n N 11C0161U0MSwDR2001U(W12201 s2iTABLE 1 1122!01 Page 1 of 1