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Table 10 <br /> Dual Phase Extraction System-Operating Data <br /> Parcel 2A-L&M OU <br /> 666 West Weber Avenue,Stockton,CA <br /> Period 9r Influent Effluent <br /> Hourmeter Totalizer System Volume Average Flow Well Field Operating System Flow VOC VOC VOC' <br /> Reading Reading Flow Discharged Flow Rate Rate Temperature Temperature Vacuum Rate [FID] [FID] Removed <br /> Date (hours) (gal) al (gal) (gal/day) pm (°F) °F) (inHg) (scfm ppmv ppmv) (Ib/day) pH 12 Notes <br /> Constituent Period Vapor Period Liquid Period Total Historical Vapor Historical Liguid Historical Total <br /> lbs. gals lbs. gals lbs. gals lbs. gals lbs. lbs. <br /> gals <br /> SPH - - 6 - 6 - <br /> TPHd 6.0 0.84 6.7 0.9 12.7 0.9 6.0 0.84 9,533 9,539 1,328 <br /> TPHo - 3.9 0.5 3.9 0.5 - 5,135 5,135 674 <br /> TPHg 11.8 1.9 0.1 0.0 11.9 2.0 17,864 2,929 152 18,016 2,954 <br /> Benzene 0.08 0.01 0.001 0.00 0.1 0.01 11.85 1.61 0.07 11.92 1.61 <br /> MtBE 0.14 0.02 0.001 0.00 0.14 0.02 3.41 0.55 0.02 3.43 0.55 <br /> TBA 0.010 0.002 0.0 0.00 - 0.52 0.52 0.08 <br /> Equation: <br /> [Avg of consecutive(Inf Con-Eff Con)(ppmv)] <br /> VOC Removed/day= --------------------------------------------------- X[86.17(g/mole)]X[1 lbs/453.59 g]X[1.2641 moles/1 cf]X[Avg of consecutive flow rates(scfm)]X[60 min/hr]X[24 hr/day] <br /> [1,000,000 parts] <br /> Definitions: <br /> gal=gallons scfm =standard cubic feet per minute PAH=Polycyclic Aromatic Hydrocarbons <br /> gpm=gallons per minute VOC=Volatile Organic Compound acfm=actual cubic feet per minute <br /> °F=degrees Fahrenheit ppmv=parts per million by volume GAC=Granular Activated Hydrocarbon <br /> inHg=inches of Mercury gal=gallons <br /> gpm=gallons per minute ATC=Authority to Construct <br /> Notes: <br /> a =System switched to operate in catalytic mode <br /> b=System switched to operate in thermal mode. <br /> Column under heading VOC(Hexane)Removed(Ib/day) added 2Q10 to track removal rate of total VOCs. <br /> 1 =VOC represented as Hexane(molecular weight 86.17)for VOC vapor mass removal rate calculation. Hexane was used because it was most representative of the lower carbon range <br /> organics. <br /> 2=System permitted under ATC number N-4878-1-1. Source test for air board. Extracted groundwater being held in onsite holding tank. System shut down following source test. <br /> 3=System started for 24-hour collection of vapor PAH samples. <br /> 4=System shut down following completion of vapor PAH sample collection. PAH results outside of ATC limits(no detectable PAHs in influent vapor stream);alternate ATC needed to operate. <br /> 5=Approximately 5,840 gallons of groundwater stored in holding tank discharged to sanitary sewer. <br /> 6=ATC Number N-4878-1-2 issued 7/20/2004.System restarted. <br /> 7=Source test for air board. System shut down following source test due to on-site excavation activities. <br /> 8=Samples collected from wastewater treatment system.Carbon change-out needed. <br /> 9=System shut down following completion of vapor PAH sample collection. <br /> 10=System non-operational since 5/2005.No sampling and no discharge activities occurred. <br /> 11 =System effluent sampled on 7/6/2005 following startup. <br /> 12=Start-up on fresh GAC <br /> 13=pH measurement recorded in the field beginning December 9,2009. <br /> 14=Hourmeter and totalizer readings recorded on Feb 4,2010,all else occurred on Feb 5,2010. <br /> 15=System shut down on August 28,2010 due to the failure of the oil-water seperator transfer pump. Repairs were made and the system was restarted on October 4,2010. <br /> 16=System hour meter was replaced. DPE wells were closed during pilot test conducted from 11/16/10 to 11/19/10. No well field temperature or flow rate were collected;therefore,values from the most recent visit with the same system <br /> vacuum was used instead(07/12/10). <br /> I:\Tidewater\TW Stockton(P2A)\Engineering\O&M\Tables\O&M Tables 201 1\3Q1 1\Parcel 2A OM Tables 3Q11.xlsx Page 3 of 3 <br />