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1 <br />' 18 February 1997 <br /> AGE-NC Project No 95-0104 <br />' Page 7 of 22 <br />' (unsaturated)zone and draw the vapor into extraction wells screened within the contaminant plume <br /> The hydrocarbon vapor is drawn from the wells and "treated" in one of several possible treatment <br /> units (carbon canisters, internal combustion engines, thermal oxidizers and catalytic oxidizers) Air <br />' injection wells may be installed outside the contaminant plume to increase air flow to the extraction <br /> unit <br />' An internal-combustion (IC) system draws the vapor stream into the carburetor system of the engine <br /> and mixes the vapor with air prior to combustion Exhaust gasses (oxides of carbon and hydrogen) <br /> are further broken down in a catalytic converter before being emitted to the atmosphere These <br /> systems require supplemental fuel, such as propane or natural gas, which can greatly increase <br /> expenses as vapor concentiations decrease below levels normally required for combustion Typically, <br /> internal combustion engines work effectively where in-situ hydrocarbon concentrations approach the <br /> 40,000 parts per million - volume (ppmv) required for peak performance of the engine As <br /> concentrations decrease below 20,000 ppmv, supplemental fuel requirements, and therefore expenses, <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 /> A carbon-canister system operates by i outing hydrocarbon vapor through activated carbon filters <br /> lie where adsorption of h}drocarbons onto carbon takes place, removing the hydrocarbons from the <br /> vapor stream This type of system v.orks best for low concentrations of hydrocarbons, but becomes <br /> expensive when high concentrations of hydrocarbon vapor necessitate frequent canister replacement <br /> and disposal of spent carbon <br /> I 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 temperature <br /> of approximately 14007 Relative to internal combustion systems, these systems may be slightly <br /> more expensive to purchase and install, however, they can operate at higher air flow rates, and <br /> therefore remediate sites at a faster rate For this system to be effective, hydrocarbon concentrations <br /> should range from 5,000 ppmv to 30,000 ppmv They also operate at much lower noise levels than <br /> internal combustion systems <br /> Catalytic oxidation units provide anottier 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 /> supplemental fuel thari either thermal oxidizers or internal combustion engines Other requirements <br /> and limitations are similar to those for internal-combustion and thermal oxidizer systems <br /> b 1 2 REQUIRED SOIL CONDITIONS <br /> • Operation of the blower in a vapor extractions stem creates a partial vacuum in the subsurface, <br /> I <br />