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SITE CONCEPTUAL MODEL AND REMEDIAL ACTION PLAN 6 <br /> 7-Eleven Store No 14117, 2725 Country Club Blvd Stockton,CA June 20 2002 <br /> ICarbon adsorption using granular activated carbon (GAC) can be used to treat extracted soil vapors at a <br /> reduction efficiency of up to 99 percent Cost-effectiveness is generally greatest at low vapor <br /> concentrations of less than 5% of the lower explosive limit (LEL), due to the cost of exchanging fresh <br /> carbon for organic-saturated carbon once saturation has been achieved <br /> ' Catalytic oxidizers are also used to destroy organic vapors during SVE, and operate most cost-efficiently <br /> at moderate vapor concentrations of 5—25% LEL (700 - 3,500 parts per million by volume [ppm(v)]) <br /> Catalytic oxidizers are capable of destroying at least 95% of extracted hydrocarbon vapors within their <br /> ' optimum concentration operating range At concentrations higher than the maximum capacity of the <br /> equipment, dilution is required At concentrations of less than 5% LEL, auxiliary electricity is required <br /> ' Thermal oxidizers are used to destroy organic vapors during soil vapor extraction, and operate most cost- <br /> efficiently at concentrations ranging from 25—60% LEL (3,500 - 8,400 ppm[v]) Thermal oxidizers have a <br /> I destruction efficiency of at least 95% At influent concentrations of more than 60% LEL, dilution is <br /> required At concentrations of less than 60% LEL, auxiliary fuel (natural gas) is required in varying <br /> amounts (more is required as concentrations decrease) Both catalytic and thermal oxidizers require <br /> ' electricity to operate, and can also require natural gas for combustion <br /> 43 Dual-Phase Extraction/Intrinsic Biodegradation <br /> Dual-phase extraction (DPE) consists of simultaneous groundwater extraction and SVE Equipment used <br /> ' for DPE includes either a combination of submersible pumps to extract the groundwater operated <br /> simultaneously with SVE using the same well, or insertion of a drop tube into the well for water extraction <br /> combined with SVE In the second scenario, a high-vacuum positive displacement(PD) blower is used to <br /> ' extract the groundwater combined with any vapors entrained in the extracted media, combined with SVE <br /> applied to the vadose-zone portion of the well The PD blower is connected to a"knockout'tank, where, <br /> after separation, the groundwater is routed through GAC prior to discharge to either the storm drain or <br /> ' sanitary sewer Vapors are routed through the SVE part of the system for destruction Successful plume <br /> capture depends on the size of the capture zone relative to the lateral plume distribution, if the <br /> downgradient edge of the plume is contained within the capture zone radius, full plume capture is inferred <br /> The size of the capture zone depends on inherent aquifer properties, number and placement of wells, and <br /> rate of groundwater withdrawal <br /> Intrinsic biodegradation can be successful for remediation of MTBE and TBA, in the proper site setting <br /> For aerobic degradation (observed at dissolved oxygen [DO] levels of more than 3 milligrams per liter <br /> ' [mg/Q, MTBE biodegrades to TBA and/or tert-butyl formate (TBF) TBA then degrades to 2-propanol, <br /> which converts to acetone, then pyruvic acid, with the end product being biomass plus carbon dioxide and <br /> water From TBF, the degradation products are formaldehyde, and then biomass plus carbon dioxide and <br /> ' water(Steffan et al 1997) Anaerobic degradation is also thought to be prevalent under certain <br /> conditions, but the degradation pathways are less well documented <br /> 14117Scm2 doc <br />