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1 <br />' • Treatment and disposal of significant volumes of extracted groundwater is problematic and <br /> was one of the reasons pump and treat was not implemented in 1990 This is still an issue <br />' today, and even more so given an expected extraction rate of 30 gpm <br />' • Fenton's Reagent. Fenton's Reagent is infected into the subsurface under pressure via a <br /> series of infection points or wells Highly reactive hydroxyl radicals are generated which <br /> oxidize hydrocarbons primarily into carbon dioxide and water Because conventional <br />' Fenton's Reagent operates at a low pH range of 3 — 4, and large amounts of heat and vapor <br /> are generated due to the use of high reagent concentrations under pressure, modified Fenton's <br /> Reagent patented by ISOTEC was evaluated for the site to replace the conventional Fenton's <br />' Reagent It uses stabilized hydrogen peroxide and chelated-iron catalysts to avoid the <br /> conventional requirements of strong acids and high reagent concentrations, and consequently <br /> reduces the generation of heat and mobilized organic vapor and contaminants as well as the <br />' risk of explosion Modified Fenton's Reagent reacts at a pH range of 5 - 7 <br /> The addition of heat and/or liquids below the water level in areas that contain LPH and <br />' residual phase hydrocarbons may cause downgradient mobilization due to changes in pore <br /> pressure Case studies have shown transport of residual hydrocarbons away from infection <br /> points (Appendix I) <br />' Because the saturated zone is heterogeneous and largely silty, infected material is not <br /> expected to be uniformly distributed and instead flows in preferential channels in the <br />' saturated zone, making hydrocarbon removal from fine-grained materials difficult Based on <br /> current site conditions, use of this alternative is expected to have limited effectiveness and <br /> raises potential risks <br /> I <br /> I <br />' CrSProq«ts173942VMA5TERNWP1WP03035WPlx dm 20 <br />