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r� <br /> rr <br /> i + <br /> • with the spacing of the cut rent recovery wells These two new wells f o i m <br /> a barrier fat the movement of contaminated groundwater acioss the <br /> entire northern and western (downgiadient) end of the property <br /> The gi oundwatei-r ecovei y wells were drilled with a di ill t tg equipped with <br /> 8-inch diameter hollow-stem augers by West Hazmat Drilling Corp of <br /> Rancho Cordova, California between November 27 and 29, 2001 The <br /> wells were constructed with 2-inch diainetei flush thteaded, schedule 40 <br /> 0 020-inch factory slotted PVC well screen and blank casing The wells <br /> were screened between 9 and 19-feet bgs to allow for pumping from the <br /> entire thickness of the water bearing zone, from above the top of t h e <br /> highest historical water level to the bottom of the aquifer dust above the <br /> silty clay layer Blank casing was installed above this screened interval <br /> Lonestar #2112 sand was placed between the well casing and the boring <br /> from the bottom of the boring to 2-feet above the screened interval A 1 - <br /> foot thick bentonite layer was placed between the sandpack and t h e <br /> overlying cement sanitary seal A Portland cement sanitary seal was <br /> placed above the bentonite layer to prevent surface water from <br /> infiltrating into the well The wellheads were piped directly into t h e <br /> existing NEEP system manifold using buried I-inch diameter schedule 40 <br /> PVC pipe (Figure 3) See Appendix C for the well completion logs <br /> 3 -4 Well Develop <br /> On December 4 and 5, 2001, ASE associate geologist Erik Paddlef of d <br /> developed each of the AS and groundwater recovery wells using multiple <br /> episodes of surge-block agitation and bailer and pump evacuation Over <br /> ten well casing volumes of water were removed from each well during <br /> development, and evacuation continued until the water was relatively <br /> clear Well development purge water was remediated by the on-site <br /> groundwater treatment system No free-floating hydrocarbons or sheen <br /> were present on the surface of groundwater during well development <br /> 4 . 0 REMEDIATION SYSTEM COMPONENTS <br /> 4. 1 Vapor-Extraction Abatement Device <br /> The in-situ VE system uses a 300 cubic inch displacement, six cylinder <br /> internal combustion (IC) engine unit to oxidize extracted hydrocarbons <br /> The IC engine is equipped with a power take off (PTO)-driven blower-type <br /> vacuum pump (Roots #33) to extract volatile gasoline-laden air (soil gas) <br /> • from the VE wells (Figure 4) Under current operating conditions, the VE <br /> Frank's One Stop ASNE Remediation System Installation Report — February 2002 <br /> -3- <br />