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16 April 1997 <br />AGE -NC Project No 95-012I <br />Page 4 of 9 <br />are depicted in Figure 4 - Proposed Soil Vapor Extraction Well Locations During drilling activities, <br />soil borings will be advanced to depths of approximately 20 feet bsg All hollow stem augers will be <br />steam -cleaned prior to advancement in each borehole Cuttings and rinseate generated during drilling <br />activities will be containerized in properly labeled D O T model 17H 55 -gallon drums, and stored <br />on-site in an area inaccessible to the general public <br />Soil borings will be completed as 2 -inch diameter SVE wells using both 0 020 -inch screened and <br />schedule 40 blank poly vinyl chloride (PVC) casing A Lonestar #3 sand will be utilized as a filter <br />Pack in and slightly above the screened interval Bentonite chips will be utilized as an approximate <br />five-foot annular seal located above the filter pack, while a Portland Type II cement will be utilized <br />as a grout to surface grade A proposed as -built construction diagram is illustrated in Figure 5 - <br />Proposed Soil Vapor Extraction Well Drage am <br />3 1 2 PROPOSED SYSTEM LOCATION AND DESIGN <br />The location of the VES unit is proposed near the southeast corner of the Nomellini Construction <br />Company building This location will reduce the amount of trenching and piping needed to install the <br />system A gated enclosure, approximately 15 by 20 feet, will secure the VES unit <br />One -inch diameter PVC piping will be installed underground from the proposed SVE well head <br />locations to a vapor dropout drum The PVC piping will carry hydrocarbon vapors from the SVE <br />well heads to the VES unit A brass flow control valve will be installed in each line so that vapors can <br />be drawn from each weII independently A plan of the proposed piping system and enclosed VES unit <br />location are depicted in Figure 6 - Proposed Piping Syatem <br />3 1 3 PROPOSED SUPPLEMENTAL FUEL <br />Supplemental fuel is proposed for the operation of the selected VES unit An automatic air dilution <br />module adjusts for the optimal combustion parameters by adding oxygen and/or supplemental fuel <br />Natural gas is readily available on-site A dedicated gas line could be installed by representative of <br />P G & E that would connect directly to the VES unit Furthermore, a meter would be installed to <br />monitor supplemental fuel consumption <br />3 1 4 PROPOSED MONITORING ACTIVITIES <br />The VES unit will be monitored weekly using a photo -ionization detector (PID) to ensure optimal <br />destruction of recovered hydrocarbon vapors, and to monitor cleanup progress The PID readings <br />will be recorded from the influent end of the VES unit, and recorded before and after catalytic <br />