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I <br /> I <br /> Hydrogeologic conditions at the site warrant consideration of an alternative to groundwater <br /> extraction, (GWE), soil vapor extraction (SVE), and air sparging (AS) because the frequent <br />' occurrence of clay and silt would limit the remediation potential and cost-effectiveness of those <br /> technologies Costs for purchasing, installing, and operating these types of systems for the first <br /> year could be on the order of $100,000 to $200,000, and on the order of $50,000 (or more) per <br />' year to operate thereafter Disruption to the Barnes Trucking facility, and resultant econornic <br /> impact, caused by system installations would both be substantial <br />' It is Clearwater's opinion that the iSOC technology would be a feasible alternative for <br /> enhancement of the biodegradation potential at the site The 1SOC technology has been <br /> demonstrated to be effective for BTEX, MTBE, and gasoline-contaminated sites with low <br />' permeability soils The iSOC system is simple to install and maintain, requires no electricity or <br /> fuel, generates no wastes, and is easily adaptable to standard 2" PVC wells Installation of <br /> several additional wells may be recommended to allow for sufficient plume coverage Effective <br />' application of iSOC does require operation within water-saturated materials Previous site <br /> investigations have demonstrated that a significant majority of sorbed-phase soil contamination <br />' on the site is located well within the saturated zone — typically 20 to 25 ft below surface grade <br /> (bgs) The fine-grained soil types on the site more than likely have appreciable moisture content <br /> above the observed water levels — that condition could allow for oxygen diffusion above those <br /> observed water levels More specifically, the iSOC will promote biodegrading activity within <br /> the capillary fringe zone due to seasonal water table fluctuations, however, the effect of the iSOC <br /> would not be expected to be significant within the vadose (unsaturated) zone Nevertheless, a <br />' majority of the sorbed-phase contamination is indicated to be located well within the saturated <br /> zone, and, given the low permeability soil conditions on the site, enhanced biodegradation would <br /> be the only remaining method for remediation of the vadose zone without excavation The <br />' anticipated cost for implementation of an iSOC system at the site would be on the order of <br /> $50,000 to $75,000 Annual O&M costs would be expected to be on the order of $2,000 to <br /> $3,000 — not including costs for quarterly groundwater monitoring, or any additional biological <br />' or chemical analysis An overview of oxygen-enhanced bioremediation, and a detailed <br /> description of the iSOC technology, including conceptual design for the site, are provided below <br /> A summary of remedial alternative comparisons is provided below in Table 1 <br />' Overview - Bioremediation of Petroleum Hydrocarbons Using Dissolved Oxygen <br />' The use of dissolved oxygen in contaminated ground water to enhance natural attenuation of <br /> gasoline constituents (MTBE and BTEX) has been growing as a remediation technology since <br /> the mid 1990's Presently there are a variety of techMologies available which will introduce low <br />' to moderate concentrations (10-20 ppm) of stable dissolved oxygen into ground water <br /> Once this elevated dissolved oxygen mixes with ground water, natural biodegradation occurs and <br />' the gasoline constituents are consumed by aerobic microorganisms Dissolved gasoline <br /> constituents in ground water can be treated by mechanical technologies such as groundwater <br /> pump and treat systems (GWE), SVE, or AS Those technologies are appropriate for some <br />' ZB 178C Addendum to CAP 2 December 31,2003 <br />