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4-57 Oxidation f 3 Page 2 of 5 <br /> >Internal Combustion Engine Oxidation <br /> ,, <br /> Organic contaminants in air can be used as fuel and burned in an internal combustion <br /> engine. When the concentration of organics is too low, auxiliary fuel is added to enhance <br /> the oxidation. <br /> > Thermal Oxidation <br /> In most cases, the thermal or catalytic oxidation process can be enhanced to reduce <br /> auxiliary fuel costs by using an air-to-air heat exchanger to transfer heat from the exhaust <br /> gases to the incoming contaminated air. Typically, about 50% of the heat of the exhaust <br /> gases is recovered. <br /> > UV Oxidation <br /> Oxidation of organic contaminants in air can also be achieved by UV oxidation. As <br /> described in UV Oxidation of Wastewater(Tech_no_log y_Profile._Section_4.44), UV oxidation <br /> is the process by which chemical bonds of the contaminants are broken under the <br /> influence of UV light. Products of photo-degradation vary according to the matrix in which <br /> the process occurs, but the complete conversion of an organic contaminant to CO2, H2O, <br /> etc. is not probable. <br /> TO P <br /> Synonyms: <br /> DSERTS Code: F21 (UV Oxidation) <br /> TO P <br /> Applicability: <br /> The target contaminant groups for oxidation are nonhalogenated VOCs and SVOCs, and <br /> fuel hydrocarbons. Both precious metal and base metal catalysts have been developed <br /> that are reportedly capable of effectively destroying halogenated (including chlorinated) <br /> hydrocarbons. Specific chlorinated hydrocarbons that have been treated include TCE, <br /> TCA, methylene chloride, and 1,1-DCA. <br /> i <br /> TOPA <br /> Limitations: <br /> The following factors may limit applicability and effectiveness: <br /> • If sulfur or halogenated compounds or high particulate loadings are in the emissions <br /> stream, the catalyst can be poisonedideactivated and require replacement. <br /> • Destruction of halogenated compounds requires special catalysts, special materials <br /> or construction, and the addition of a flue gas scrubber to reduce acid gas <br /> emissions. <br /> • Influent gas concentrations must be < 25% of the lower explosive limit for catalytic <br /> and thermal oxidation. <br /> • The presence of chlorinated hydrocarbons (see comment above) and some heavy <br /> metals (e.g., lead) may poison a particular catalyst. <br /> http://www.frtr_gov/matrix2/section4/4-59.html 10/22/2004 <br />