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1 ' <br /> TABLE 3 <br /> VAPOR REMEDIATION SYSTEM STATUS <br /> THRIFTY OIL STATION#171, STOCKTON, CA <br /> Hourtineter� Cumulattver Hrssince ;"_ Vapor InletTPHg` - " TPHgremove CumulaGver ,f-'THgMa"ss <br /> ' u s a w "���i_ -. ,. x, _ --r. r � ,- ' ^r = ,' a`•. r-.: a� t a�` <br /> Date ' reading Operation Last vlsd` ;`Flow Rater Concentration'='Y , within period, TPHg removed Removal Rate =gemo`ved '' T - s �_ r , <br /> ]r - k-- C F,�oT+ _ a h r �'r :d' y „E ac'` - '.�'— `s_�✓r x, "aiY <br /> (his)* (hrs),€ (his) LL (cfm)4� {ppmv} y k" {te IL° ;I a _ Ihs - (It)slhr) (gallons) �" Remarks <br /> r t r �: f "'.' g } (bs) , k' ( )* f r. s_�' �F'�'h'".'r�,. , i .s'a. <br /> 09/21/05 4 17 690 32 530 1 7 1141 1 -652 242. 142 913 0 35 226647 System ran for a few hours then turned om Reset starter switch <br /> 09128/05 17 697 32 537 7 141 - E 652 2 41 1 142 916 034 22 685 1 System ran for a few hours then tuned off!Reset starter swdch-restart very hard <br /> 10/05/05 17 711 32 551 14 '143 878E 3 590 1577 142 932 1 13 22 687 6 System ran for a taw hours then turned off/Reset overload switch 8 restart again <br /> 10113105', 17 809 32649 98 144 - 3 590 188821 143 120 1 93 227175 yew ran for a few hours than wined ON Reset overload swatch close vatva TB 3rf e-t t W 6 <br /> ten MWS I DO%open <br /> 11/21/05 18 056 1 32 896 247 144 3 590 477561 143 598 1 93 22 793 3 system shut down for o W s --- - - <br /> 11/28/05 - 18 059 r 32 899 -� 3 144 - t 3 590 5801 143 604 1 93 22 794 3 Restart after o W S - - - - <br /> 12105105 18,143 -f - 32 983 11 84 141 I 1 3 590 16072! 143 765 191 22,8198 - <br /> �12112105 18 20; 33045 62�- —_143_— -- - -3 590 _ - 118 21 __ 143 883 f f 1 91 -22 838 5 <br /> 12 21105 --18 294-T3-3-134-- <br /> 89� 144 -- 3 590 17148' 144 054 193 22 865 8 <br /> 12/27/05 - 18 397 -- 33 237 1 D3 - 11427 ,- 1 3 590 --- -197 76� - t 144 252 —- 1 92 22 897 1 <br /> NOTE Inlet Concentration obtained from laboratory analytical results and assumed the same until subsequent sampling event <br /> Volume of hydrocarbons removed calculation assumes gasoline density of 6 3 I J1 <br /> i I In February 2002 this table was corrected due to some formula errors In the hydrocarbon removal columns Older versions at this table may have dtifererit numbers _ <br /> Epi <br /> I <br /> � IE <br /> I <br /> r <br /> I I _ <br /> v li <br /> r <br /> 1 , <br /> 1 h <br /> I <br /> I <br /> E 171ves* I P f9 x/12120066 <br /> I - � <br />