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Second Quarter 2004 Groundwater Monitoring/Remediation Status Report <br /> Moore Petroleum Bulk Plant,5491 F.Street,Banta,California <br /> Page 5 <br /> Analysis Performed: <br /> Analysis Abbreviation Designation USEPA Method No. <br /> Total Petroleum Hydrocar_bonsF TPHg <br /> as Gasoline <br /> Total Petroleum Hydrocarbons TPHd Gas/Diesel- <br /> -as Diesel <br /> Range 8015 Modified <br /> Total Petroleum Hydrocarbons Kerosene Hydrocarbons <br /> as Kerosene <br /> Total Petroleum Hydrocarbons <br /> as Motor Oil TPHmo <br /> Benzene <br /> Toluene Aromatic . <br /> BTEX Volatile 8020 <br /> Eth lbenzene <br /> Xylenes (Total) Organics <br /> Tertiary But i Alcohol TBA <br /> Methyl Tertiary Butyl Ether MTBE Fuel <br /> Di-isopropyl Ether. DIPS <br /> Ethyl TertiaryButyl Ether ETBE Oxygenates 8260B <br /> Tertiary Amyl Methyl Ether TAME <br /> 1,2-Dichloroethane 1,2-DCALead <br /> Ethylene Dibromide EDB Scaven ers <br /> REMEDIATION SYSTEM SUMMARY <br /> Soil Vapor Extraction System <br /> System description: <br /> Petroleum vapors are extracted from the subsurface through three monitoring/vapor wells (VEW- <br /> 3/MW-8, MW-1, and VEW-4/MW-7) and two vapor extraction wells (VEW-1 and VEW-2). The <br /> wells are manifolded together with PVC piping in the remediation compound before connecting <br />{ to the extraction system (Figure 2). The vapor extraction system is a 5-horsepower positive- <br /> displacement blower discharging to a 100-cfm catalytic oxidizer where vapor is incinerated and <br /> discharged to the atmosphere. <br /> System startup date: June 17, 2002 <br /> Current system mode: Catalytic operation since startup <br />{ Active extraction wells: VEW-1 through VEW-4 <br /> Inactive extraction wells/reason: MW-1/system optimization, zero concentrations <br />