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' 20 January 2005 <br /> AGE-NC Project No 97-0343 <br />' Page 10 of 21 <br />' (oxides of carbon and hydrogen) are further broken down in a catalytic converter before being <br /> emitted to the atmosphere These systems require supplemental fuel, such as propane or natural gas, <br /> which can become expensive as vapor concentrations decrease below levels normally required for <br />' combustion Typically, Internal combustion engines work effectively where in-situ hydrocarbon <br /> concentrations approach the 40,000 parts per million-volume(ppmv)required for peak performance <br /> of the engine As concentrations decrease below 20,000 ppmv, supplemental fuel requirements <br />' become burdensome Another disadvantage of these systems is the noise generated by the engine, <br /> however, this can be mitigated by placing the unit Inside an enclosure, such as a building <br />' In a carbon-canister system, hydrocarbon vapor Is routed through activated carbon filters where <br /> adsorption of hydrocarbons onto carbon takes place, removing the hydrocarbons from the vapor <br /> stream This type of system works best for low concentrations of hydrocarbons, but becomes <br />' expensive when high concentrations ofhydrocarbon vapors necessitate frequent canister replacement <br /> and disposal of spent carbon <br />' Thermal oxidation systems destroy hydrocarbons by open-flame combustion Natural gas is <br /> commonly used as supplemental fuel, heating the extracted vapor stream to a combustion <br /> temperature of approximately 1400°F Relative to internal combustion systems,these systems may <br /> be slightly more expensive to purchase and install However, they can operate at higher air flow <br /> rates, and therefore remediate sites at a faster rate For this system to be effective, hydrocarbon <br />' concentrations should range from 5,000 ppmv to 30,000 ppmv Thermal oxidation systems operate <br /> at much lower noise levels than internal combustion systems <br /> Catalytic oxidation units provide another option for treating vadose-zone contamination,particularly <br /> after other extraction systems have reached their effective limits due to lowered hydrocarbon <br /> concentrations These systems operate at temperatures of approximately 700°F, requiring less <br /> I supplemental fuel than either thermal oxidizers or internal combustion engines Other requirements <br /> and Iimitations are similar to those for internal-combustion and thermal oxidizer systems <br /> 9 12 Required Soil Conditions <br /> Operation of the blower in a vapor extraction system creates a partial vacuum in the subsurface, <br /> inducing air"currents"through the soil pore spaces Vapors move by convection toward the area of <br /> lowered air pressure (the extraction point) The efficiency of this process is proportional to soil <br /> porosity and permeability Qualitative information has been gained through the examination of soil <br /> samples collected at the site Soil above 50 feet and in the vadoze zone consists of sand and silts with <br /> some clay, rendering vapor extraction as an effective remediation method Soil between 20 and 35 <br /> feet(three extraction wells exist a this depth)has a relatively high sand content,potentially making <br /> vapor extraction more effective for this zone Figures 4 and 5 show subsurface soil types at the site <br /> IAdvanced GeoEnviron mental,Inc <br /> I <br />