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i <br /> 25 March 2009 <br /> AGE-NC Project No. 95-0121 <br /> Page 3 of 9 <br /> 3 . 1 , PERMITTING AND PRE-FIELD WORK ACTIVITIES <br /> Applicable site permits will be obtained from the City of Stockton (sanitary sewer waste discharge, <br /> building, electrical, etc.) and from the San Joaquin Valley Air Pollution Control District <br /> (SJVAPCD) . In addition, an update to the health and safety plan presently on file with SJCEHD will <br /> be prepared in accordance with Occupational Safety and Health Guidance Manual for Hazardous <br /> Waste Site Activities (National Institute for Occupational Safety and Health Administration, U.S. <br /> Coast Guard and U. S . Environmental Protection Agency, 1985). Prior to mobilization, all <br /> underground trenching areas will be clearly marked and a utility clearance will be obtained through <br /> Underground Service Alert, <br /> 3 .2. INSTALLATION OF INTERIM REMEDIATION SYSTEM PIPING NETWORK <br /> DPE remediation system piping will be installed underground in a 1 .5-foot wide by a 1 .5-foot deep <br /> trench; the proposed trenching lay-out is depicted in Figure 4; a cross sectional view of the trench <br /> is depicted in Figure 5 . <br /> 3 .3 , REMEDIATION SYSTEM ENCLOSURE <br /> Installation of a 30-foot wide by 35-foot long concrete pad and chain-link, gated enclosure will be <br /> located in southern section of the site currently operated as a road safety equipment sales and rental <br /> firm and will surround the DPE remediation system (Figure 4). As required by City of Stockton <br /> permitting, a secondary surface water containment barrier will be installed surrounding the DPE <br /> system. <br /> 3 .4. PROPOSED INTERIM DUAL PHASE REMEDIATION SYSTEM <br /> The proposed interim remediation DPE system will consist of a 25-horsepower, oil-ring vacuum <br /> blower, with an electric heated catalytic oxidizer to simultaneously extract free-phase petroleum <br /> products, ground water and soil-vapor from on-site wells EW- I (screen interval of 20 to 40 feet <br /> below surface grade - bsg) and VW- 1 (screen interval of 15 to 30 feet bsg) and AW- 1 (screen <br /> interval of 25 to 30 feet bsg). These wells will target remediation on informal hydrogeologic unit 2 <br /> andHU3 . Based upon influent hydrocarbon concentrations reported during the December 2007 pilot <br /> test and projected BTU values delivered through the vapor stream, catalytic oxidation will be <br /> applicable to remediate the vapor stream. The oil-ring blower under standard temperature and <br /> pressure is capable of producing a maximum vacuum of 29-inches mercury (Hg) with a nominal <br /> capacity of 200 cubic feet per minute (cfin). <br /> Advanced GeoEnvironmenml, Inc. <br />