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Addendum to Corrective Action Plan Page 8 <br /> • Former Manna Pro Site <br /> Project No 207 3 <br /> • August 12,2002 <br /> displace the water in the blank casing This will require about 15 to 18 psig at the <br /> surface To accomplish this, an additional compressor we needed <br />' 6 2.1 Carbon Unit Installation <br />' The report of the first phase remedial operations documented the relative leanness of the <br /> extracted vapors This lean vapor would appear to make use of a thermal oxidizer cost- <br /> ineffective as a means to destroy the evolved gasoline-laden vapors We suggest that the <br /> most cost-effective method of treating the evolved gasoline vapors is to use a large <br /> activated carbon-unit system A single 12,000-pound carbon filter will be installed to as <br /> the main vapor treatment device A smaller, 2,000-pound activated carbon filtration unit <br /> will be installed down-stream of the large unit and will be intended as a "polish" unit to <br /> remove and residual gasoline that may escape the main unit prior to discharge to the <br /> atmosphere As the project proceeds, it is expected that the rate at which gasoline is <br />' removed will be reduced At some point it may become appropriate to replace the <br /> 12,000-pound carbon filter with a smaller unit <br />' 4.1.4 Conveyance Piping & Manifold Installation <br />� . Conveyance piping will be installed in trenches to protect it from traffic with the idea that <br /> it will be connected to the treatment equipment and eventually incorporated into a larger <br /> remedial manifold system Trenches will be back filled with road base and compacted <br /> Upon completion of compaction work, each trench will be capped with asphalt Vapor <br /> extraction and air sparge conveyance piping will be installed to connect each sparge well <br /> and extraction well to manifolds in the central treatment system compound Vapor <br /> extraction and air sparge well manifolds will be constructed to allow modification of <br /> airflow and extraction from the different remedial wells The vapor extraction manifold <br /> will include a mechanism that will allow sample collection and use of the well for passive <br /> I air recharge Rotameters and magnahelic gauges will be installed "in line" on both the air <br /> sparge and vapor extraction well manifolds to measure airflow and pressure/vacuum <br /> Diagrams of the remedial system and manifolds are attached as Figures 3 and 4 At the <br /> I conclusion of the project, the entire area will be re-paved with the type and quality of <br /> asphalt originally used by the owner of the Property <br /> 4.2 Remedial System Operation <br /> Once started, the system we be operated continuously until the rate of gasoline recovery <br /> becomes fall below 1 pound per day The sparge well will be operated continuously <br /> except for system repairs and servicing The vapor extraction wells will be cycled as <br /> described above <br />■ 2937 Veneman Ave,#B240 Geo-Phase Environmental Inc Phone(209) 569-0293 <br /> Modesto, CA 95356 Fax(209) 569-0295 <br />