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Chlorinated VOC treatment by ozone and hydrogen peroxide is well documented and as a <br /> result, chemical oxidation is considered a technically feasible technology for mitigation of <br /> the groundwater impacts identified at the CHSL, but the chemical oxidation reactors typically <br /> used to treat VOC-impacted water are extremely expensive and more complex when <br /> compared to other equally-effective ex-situ treatment technologies. As a result, although <br /> technically feasible, this alternative is considered not viable and will not be considered for <br /> further analysis. <br /> Above-ground Metal Enhanced Reductive Dehalogenation (MERD) Reactor: Not Viable—This <br /> technology is similar to the in-situ MERD technology in that the extracted groundwater is <br /> passed through above-ground reactive vessels that contain iron shavings. Degradation of <br /> chlorinated VOCs is then accomplished in a fashion similar to the in-situ MERD technology <br /> (Section 3.5.1). Data from field tests indicate that this technology may be as effective as air <br /> stripping and GAC technologies in removing select halogenated VOCs from groundwater; <br /> however, the available data do not support the use of MERD to reduce VOC concentrations <br /> lower than those measured in groundwater samples collected at the CHSL. For this reason, <br /> MERD reactor technology is considered not viable for mitigation of the low concentrations <br /> of VOCs identified at the CHSL. <br /> • <br /> Reverse Osmosis: Not Viable — This technology is appropriate to treat groundwater <br /> contaminated by inorganic constituents such as TDS, chloride, and nitrates. Water is forced <br /> through a semi-permeable membrane, producing a clean effluent and a "reject" stream <br /> (brine) that contains high concentrations of the inorganic contaminant. The reject stream is <br /> then trucked off site or placed in an evaporator pond for disposal. <br /> While this technology is considered an effective means of treating inorganic compounds in <br /> groundwater, the technology is considered not viable for treatment of organic contaminants <br /> at the CHSL. <br /> Ion Exchange: Not Viable - This technology also addresses elevated concentrations of <br /> inorganic constituents such as TDS, chloride and nitrates. Water passes over a series of resin <br /> columns where contaminants are bound by adsorption processes. Thus, the process <br /> produces a clean effluent. As the adsorption sites on the resin media become saturated, the <br /> resin must undergo a regeneration process using a strong acid and base solution. This <br /> produces a "reject" stream that contains high concentrations of brine. The reject stream is <br /> then trucked off site or placed in an evaporator pond for disposal. <br /> • <br /> Engineering Feasibility Study Geo-Lo Page ■ 20 <br /> Corral Hollow Sanitary Landfill A S S O C I A T E Sg <br /> January 25,2013 <br />