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S ECOR _. <br /> Ms. Vicky McCartney <br /> September 15, 2003 <br /> Page 5 <br /> Though interim remediation via groundwater batch extraction appears to have effectively reduced <br /> concentrations of MtBE in the source area, MtBE and a significant amount TBA mass still remains <br /> within the source area;During interim groundwater batch extraction activities, concentrations of TBA <br /> have remained at elevated yet stable levels (Table 4).'Since MtBE levels appear to have reached <br /> asymptotic levels as a result of groundwater batch extraction activities (Figures 3 through 5) and <br /> elevated concentrations of TBA are present in source area wells MW-1R, MW-2R, and VW-1, <br /> SECOR proposes an alternate interim remedial action plan, which is presented below. <br /> REVISED TRAP <br /> To further expedite remediation of the dissolved plume beneath the site, SECOR recommends <br /> discontinuing interim remediation via groundwater batch extraction. To further enhance source <br /> removal and prevent the further off-site migration of MtBE and TBA, SECOR proposes the installation <br /> of an OS system for the removal of petroleum hydrocarbons and fuel oxygenates beneath and in the <br /> vicinity of the site. With subsurface soils consisting predominantly of mixtures of silt and sand within <br /> the upper portion of the saturated zone (approximately 12 to 14 feet bgs), the introduction of ozone <br /> through several OS points would directly destroy dissolved petroleum hydrocarbons, MtBE,-and-TRA, <br /> and stimulate in-sift a rr oobic biodegradation of dissolved petro eum hydrocarbons and petroleum <br /> hydrocarbons in the saturated zone by increasing su surface oxygen concentrations. Though <br /> concentrations may initially increase due to the desorption of petroleum hydrocarbons from soil <br /> .( f caused by the aggressive mechanical scrubbing action of the ozone- OS is capable of <br /> �✓ facilitating subsequent rapid degradation of the dissolvedplu em beneath th site. The installation of <br /> OS points along the eastern/northeastern property boundaryary would act as a barrier, inhibiting <br /> migration of dissolved petroleum hydrocarbons, MtBE, and TBA further downgradient of the site. <br /> Conceptual Design of the OS System <br /> ,�41, <br /> A total of 10 OS points (OS-1 through OS-10) are proposeZthe' area surrounding the USTs. The <br /> locations of the wells were selected based on an asssum�d$0-foot ozone radius of influence, in order <br /> to maximize the remedial coverage in the vicinity of the USTs and along the eastern/northeastern <br /> perimeter of the site. A work plan for.the installation of the OS points is included in the following <br /> section. <br /> Process Flow <br /> Ozone injection tubing (approximately 3/8-inch diameter), doubly-contained within PVC tubing, will <br /> connect each OS well to a 10-point panel, located in a small remediation compound behind the <br /> station building. The panel will be plumbed to a 10-point injection solenoid within the OS unit, <br /> allowing rotation of the injection lines between the 10 OS points at a rate of 6 standard cubic feet per <br /> minute (scfm). The OS unit will be equipped with a compressor rated to deliver 6 scfm at 10 pounds <br /> per square inch (psi). The proposed layout of the OS system is presented as Figure 7. <br /> Remediation System Permitting and Installation <br /> Following approval cif the TRAP, OS well construction permits will be obtained from San Joaquin <br /> County Environmental Health Division (SJCEHD). Construction of the remediation system will begin, <br /> following the approval of permits, and receipt of necessary equipment. <br /> 11ConocoPhillips%Tosco Marketing11I1931Reports\Revised TRAP&WP.doc <br />