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In-Situ Chemical Oxidation (ISCO) also known as "chemical oxidation ", is an in situ remedial technology that reduces concentrations of volatile constituents adsorbed to soils in the saturated zone. In-situ chemical oxidation involves the introduction of a chemical oxidant into the subsurface for the purpose of transforming ground-water or soil contaminants into less harmful chemical species. There are several different forms of oxidants that have been used for ISCO; the four most commonly used oxidants: permanganate (MnO4-), hydrogen peroxide (H2O2) and iron (Fe) (Fenton-driven, or H2O2-derived oxidation), persulfate (S2O82-), and ozone (O3). The type and physical form of the oxidant indicates the general materials handling and injection requirements. The persistence of the oxidant in the subsurface is important since this affects the contact time for advective and diffusive transport and ultimately the delivery of oxidant to targeted zones in the subsurface.
Application Site-specific conditions and parameters, in conjunction with oxidant-specific characteristics, must be carefully considered to determine whether ISCO is a viable technology for deployment relative to other candidate technologies, and to determine which oxidant is most appropriate. These issues and the advantages and disadvantages should be considered. The breadth of ground-water contaminants amenable to transformation via various oxidants is large. That is, many environmental contaminants react at moderately high rates with these oxidants. Therefore, a wide range of contaminant classes are amenable to chemical oxidative treatment. Mixtures of contaminants may require treatment trains involving the sequential application of technologies to accomplish the treatment objective. Chemical oxidation can be deployed under a variety of applications, i.e., in either the unsaturated or saturated zones, or possibly above-ground, and under a variety of hydrogeologic environments. There are potential advantages and disadvantages of ISCO that should be assessed when considering the deployment of this technology.. Operation Principles (Back to Top) For example, oxidation of trichloroethylene (TCE) and perchloroethylene (PCE) may produce reaction byproducts that include dichloroacetaldehyde and dichloroacetic acid, compounds with lower toxicity. Similarly, oxidation of phenolic compounds may produce an assortment of carboxylic acids (Huling et al. , 1998) that are nontoxic. Oxidation of these byproducts to CO 2 and H 2 O could be accomplished through additional oxidative treatment and expense, but may not be practical for economic purposes. These reaction byproducts may also serve as microbial substrate for natural attenuation processes. In oxidative treatment systems, numerous reactions could potentially occur, including acid/base reactions, adsorption/desorption, dissolution, hydrolysis, ion exchange, oxidation/reduction, precipitation, etc. In environmental systems there is a wide array of reactants and conditions that influence reaction rates and pathways that vary from site to site. Often, numerous reactions are required to achieve innocuous end products, and many of the reaction intermediates are never identified.Some of the factors that determine the effectiveness of ISCO are: System Design (Back to Top) Advantages and Disadvantages (Back to Top)
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