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Tic <br /> n VV <br /> ASS OCIATES I N C . <br /> I <br /> Selected soil samples will be immediately placed in a cooler with ice and delivered under <br /> chain-of-custody documentation to a State-certified analytical laboratory . Soil samples will be <br /> analyzed for TPHg by EPA method 8015 ; BTEX by EPA method 8020; and MTBE, TBA, <br /> -I TAME , DIPE, and ETBE by EPA method 8260 . <br /> Similar to the VES, the actual radius of influence for each sparge well will vary and the effective <br /> radius of influence will be evaluated following long-term operation of the AS system. <br /> In-situ air sparging is the process of injecting air into the saturated zone via sparge wells. Sparge <br /> wells are designed with a screen interval at a depth approximately 15 to 20 feet below the water <br /> table. Pressurized air is forced out through the screen and into the saturated zone. The air foams <br /> 4 1 bubbles that rise to the unsaturated zone, carrying trapped and dissolved contaminants . Vapor <br /> extraction wells in the unsaturated zone capture sparged air, which is then treated through the <br /> vapor extraction system. The AS system will include a compressor, associated piping, control <br /> ! valves, pressure gauges, flow meters, instrumentation and controls; and a remediation shed shared <br /> with the VES . Based on ATC' s experience at similar sites and the results of the pilot tests, a Gast <br /> ( 2567-P 132-T908X rotary vane compressor would be sufficient to operate the air sparge component <br /> I. J of the system. The compressor would create a maximum of 20 pounds per square inch pressure and <br /> a maximum airflow rate of 18 standard cubic feet per minute. A process and instrumentation <br /> ( diagram for the AS is shown on Figure 14. <br /> L_J <br /> 5.2.3 Remediation System Layout <br /> (l Components of the vapor extraction and air sparge system would be located in an enclosed shed on <br /> the south side of the on-site building. This will preclude public access and reduce noise. A <br /> network of subsurface piping will be used to convey off gas from the extraction wells to the <br /> remediation shed. The trenching system layout is shown on Figure 15 . The same trenches will be <br /> used for the air sparge system. Piping will be used to convey air to the sparge wells for injection to <br /> the subsurface. Piping will be installed at a maximum depth of two feet as shown on Figure 16 . A <br /> two-foot by two-foot well vault will be installed over each vapor extraction and au sparge well. A <br /> gate valve will be installed at each well head to control the airflow in or out of the well. In <br /> addition, a sampling port will be installed at each vapor extraction well for monitoring purposes. <br /> ( % Equipment operation will require the installation of an electrical power source and meter base. Site <br /> system requirements include a 220V, single phase 150 amp power source and meter base. A <br /> NEMA 4, UL Listed Control Panel will be located at the shed. <br /> II <br /> 6.0 REMEDIATION SYSTEM CONSTRUCTION <br /> Upon review and approval of the remediation system design plans and specifications by PHSIEHD, <br /> I`J ATC will complete the following tasks. <br /> l � <br /> w:\wordpro\62596\reports\irp.doc 8 <br /> L:i <br />