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11 August_1997 <br /> off AGE-NC Project No. 95-0118 <br /> Page 3 of 9 <br /> derived from both marine and non-marine sediment, and are generally formed in alluvium derived <br /> from mixed rock sources. <br /> 2.4. GROUND WATER DEPTH AND FLOW DIRECTION <br /> Ground water is currently encountered at a depth of approximately 35 feet bsg and has a dominant <br /> northwesterly flow direction. Ground water occurs in a generally sandy layer extending from <br /> approximately 30 feet to 45 feet bsg. <br /> The uppermost ground water flows in an unconfined aquifer. With increasing depth, the aquifer <br /> becomes semi-confined due to.the presence of mixed heterogeneous layers of sediments. The <br /> sedimentary units.are relatively horizontal and continuous over the site. Relative ground water <br /> elevation maps for the site have been included in previous Quarterly Reports prepared by AGE. <br /> .3.0. SCOPE OF WORK <br /> =� An SVE system in conjunction with an IAS system is the recommended method of remediation for <br /> the petroleum hydrocarbons at the site. In order to maximize the efficiency of the clear,,-up efforts, <br /> a 24-hour operation of the system is planned. A typical destruction rate of greater than 97% of <br /> hydrocarbon vapor can be expected throughout the entire cleanup duration. <br /> 3.1. PROPOSED SOIL VAPOR EXTRACTION SYSTEM DESIGN <br /> A thermal destruction process is proposed for hydrocarbon vapor recovery by utilizing a direct fired <br /> thermal oxidizer vapor extraction system (VES). A typical diagram of the system is illustrated in <br /> Figure 3 -Diagram of Proposed Vapor Extraction System. <br /> The VES will be connected through a pipe manifold to the vapor recovery wells and should be able <br /> to operate between 150 and 200 cubic feet per minute (cfm). The thermal oxidizer can be outfitted <br /> with a catalytic module and/or a heat exchanger to provide an effective destruction ratio at reduced <br /> concentrations of hydrocarbon vapor. Soil vapor will be extracted from a configuration of extraction <br /> wells using a vacuum blower and routed to the thermal oxidizer. Supplemental fuel (i.e. natural gas) <br /> will be added to maintain'the optimal temperature for a maximum destruction rate of hydrocarbon <br /> vapor. Additional information on the proposed soil vapor extraction unit is included in Appendix A. <br /> Advanced GeoEnvironmental,Inc. <br />