ARCHIVED REPORTS XR0002730 - Laserfiche WebLink

Home Browse Search

Mir M Table A 1 Dual Phase Extraction System-Sou Vapor Extraction Performance Data ARCO 4932 16 East Harding Way Stockton California TPH as Gasoline Benzene MtBE Well Field Well Field Fib Influent Influent Influent Hour Meter Oflutart Blower Manlfdd Manifold Well Field Well Field Concen-Removal Net Removed Concen-Removal Net Remov Concen- Removal Net Rem oved Sample Date Reading Valve Vacuum Vacuum Temperature Flow Rate Flow Rat Influent Efflue traUon Rate Removed t0 Date tratron Rate Removed to Date tration Rate Removed to Date ID Sampled (hours) (%Open) ('Hg) ('H2O) (F) (acfm) (scfm) (ppmv) (ppmv) (ppmv) (lbs/day) (pounds) (pounds) (ppmv) (lbs/day)(pounds) (pounds) (ppmv) (lbs/day) (pounds) (pounds) 05/14/03 a 10 1D0% _ _ 50000+ 0 0 0 0 0 0 0 0 0 0 0 0 INF 05129103 b c 252 0% 13 402 -- 150 2 135 48 000 11 16 000 811 409 409 190 76 38 38 2 100 95 48 48 F INF 07!08!03 d 28 0 2% 20 0 — » 137 2 120 20 000 1 1 17 000 766 26 435 200 7 1 0 25 41 4 200 169 44 52 INF 08/07/03 3987 0% 10 60 821 2062 169 43 SW 0 21 6 100 385 8 936 9 371 24 1 2 65 69 210 12 1 403 1 455 D9105103 e INF 09109!03 1 10208 0% 15 136 80 1 162 7 104 7 840 0 0 D 2 900 113 6 459 15 831 -32 01 17 86 28 10 166 1 621 10109103 1 724 3 0% 15 5 — — — -- 550 0 1993 17 823 — » 2 88 — » 32 1 653 INF 10123103 20568 0% 13 -- — 138 98 1 500 0 620 23 939 18762 <4 6 00 1 89 37 12 15 1 668 10129/03 22036 0% 14 — — 165 117 1 1 DO 2 5 — — 260 19 022 — -- 0 89 —-- 45 1 673 11/05/03 2 251 5 0% 14 110 78 1 000 45 — -- —19 107 — — 0 89 15 167401 !NF 11/13/03 g 2 325 6 0% 15 80 771 1767 137 1 180 0 00 1200 62 130 19 237 <1 6 <56 1 9 0 i 3 3 1680 0 1 0 89 <5 B 0 3 2 3 1 676 INF 12103103 2 804 9 0% 15 140 — 1900 121 3 800 0 00 630 28 901 20 138 <0 16 00 1 90 INF 01/12104 3,7435 0% 15 150 — 1627 116 226 00 29 2 591 20 729 <0 032 00 0 90 48 03 66 16% INF 02104/04 4 274 4 D% 15 — — 982 111 2600 00 64 530 19 235 20 9 <0 32 00 D 90 <1 1 00 33 1 689 INF 03103/04 4 788 2 0% 15 — — 210 0 237 603 0 0 0 340 27 495 21459 1 7 4 1 1 92 063 00 086 1 690 INF 04/06/04 5 512 9 0% 13 — » 2380 269 2780 00 490 44 1 D63 22 522 24 02 42 96 <28 02 40 1 694 INF 05125!04 6 104 7 0% 10 — — 1470 166 1027 00 67 4 584 23 106 <0 080 00 21 98 <0 28 00 29 1 697 !NF 06/14/04 6 480 8 0% 15 — — 1030 116 3200 00 200 8 89 23195 <0 89 00 0 98 180 62 49 1 746 INF 07/13/44 6 938 7 0% 15 — » 899 102 1216 00 IDD 3 106 23 301 12 00 0 98 65 0 2 61 1 807 INF 08/01104 h 7 208 5 0% 152 -- — 772 87 889 00 150 4 43 23 344 19 00 0 99 48 12 41 1 815 INF 09109104 7 826 7 0% 15 — 1105 125 200 00 210 9 113 23 457 14 00 078 99 32 12 21 1 836 INF 110/0004 I 80371 0% 15 — — 77 1 87 130 00 110 3 101 23 559 059 Do 051 100 23 06 15 1 851 — 79 9 90 10 0 0 0 120 4 79 23 638 055 00 031 100 11 03 10 1 861 INF 11/01104 8 597 3 0% 15 iNF i2113104 9 603 3 0% 15 — — 905 102 800 00 140 5 175 23 812 17 00 123 102 <0 69 0 D 7 1 868 INF Ot105105 10 076 6 0% 15 -- — 840 95 407 00 140 4 90 23,903 17 00 087 102 <0 56 00 0 1 868 INF 02709105 10 916 9 0% 15 — 699 79 331 00 99 3 122 24 025 0 81 00 104 103 33 01 2 1 870 INF 03115/05 11 225 5 0% 18 697 79 64 1 00 97 3 33 24 058 082 00 022 104 36 01 1 1 871 INF 04/14/05 11 780 0 0% 15 — — 701 79 271 00 — — — -- — — i REPORTING PERIOD FIRST QUARTER 2005 TOTAL POUNDS REMOVED 3,944 104 1,8 14 3033 TOTAL GALLONS REMOVED 246 PERIOD POUNDS REMOVED 246 2 1 3 40 029 4 PERIOD GALLONS REMOVED TOTAL AVG FLOW RATE 121 scfm TOTAL PERCENT OPERATIONAL 73% PERIOD PERCENT OPERATIONAL 69% Definitions Chemical Properties acfm=Actual cubic feel per minute "H2O=Inches of water Standard conditions 60 F 1 atm scfm =Standard cubic feet per minute FID=Flame ionization Defector Vapor density of gasoline=0 26 pounds per cubic feet(assumes molecular weight of gasdme Is i00 pounds per pound male} lbs=Pounds MtBE =Methyl tert-butyl ether Vapor density of benzene=0 206 pounds per cubic feet =Data not available Vapor density of MTBE=0 232 pounds per cubic feet ppmv=Parts per million by volumeLiquid density of benzene=7 34 pounds per gallon TPH=Total petroleum hydrocarbons Liquid density of gasoline=6 1 pounds per gallon 'Hg=Inches of mercury Liquid density of MtBE=6 1a pounds per gallon Notes a System start-up and shake-down b Source test for San.Joaquin Valley Unified Air Pollution Control District performed c Analyte values given were analyzed beyond the EPA recommended holding time The analysis was performed because the original analysis detected an anatyte in the associated blank as well as in the sample d Permananent system start up e SVE system shut down due to a car running Into the compound L50Y. system restarted utodialer Installed stem down on arrival due to clogged finer stem down on arrival due to power failure ta not available at time of reporting I IBP ARCON93240 S WOdM Tahles%RCO 4932 03M Tables 1005 xis Pape 1 or i