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EXXON,4444 PERSHING -2- 12 November 1996 <br /> STOCKTON,SAN JOAQUIN COUNTY <br /> THE REMEDIATION PROPOSAL <br /> A soil vapor extraction system (SVES) was installed and began operation in 1994 The system consisted <br /> of four vadose zone wells screened from 10 to 30 feet bgs A total of 16,000 lbs of hydrocarbons have <br /> been removed <br /> However, significant soil contamination remains trapped in soil below the water table, between 27 and <br /> 42 feet bgs In March 1996, depth to water was approximately 20 to 21 feet In addition to two air <br /> sparging wells and six vapor extraction wells, Exxon's consultant, EA Engineering, Science, and <br /> Technology, has proposed to use UVB (Unterdruck Verdampfer Brunnen- vacuum vaporizer well) <br /> technology <br /> The UVB system extracts groundwater through a lower well screen section, strips VOCs from the water <br /> in a negative pressure stripping reactor (air stripper), and discharges the treated groundwater through an <br /> upper well screen section, back to the aquifer It also uses an aboveground vacuum extraction blower <br /> Gases from the UVB, along with the gases from the air sparging and vapor extraction system, will be <br /> treated with a catalytic oxidizer The system does not lower the water table <br /> The proposed UVB treatment well is 16 inch galvanized steel, with two screened zones below the water <br /> surface, one at the bottom of the treatment interval, and one at the top The borehole annulus between <br /> the two screened zones is sealed with bentonite A packer is installed in the treatment well between the <br /> two screened zones to ensure one directional flow of the groundwater A pipe is placed through the <br /> packer, extending from the pump, which provides groundwater from the lower zone, to the air stripper in <br /> the upper zone <br /> The upper part of the well, is maintained below atmospheric pressure by a centrifugal blower The air <br /> for the in-situ stripping is drawn in through a fresh air pipe, the upper end is open to the atmosphere, and <br /> the lower end terminates in a pinhole plate (diffuser) in the air stripper The negative pressure within the <br /> upper part of the well causes a water level rise within the treatment well The air stepper is balanced <br /> below the groundwater level, within the treatment well, and is free floating to allow for changing water <br /> levels Between the pinhole plate and the water surface is the stripping zone, in which air bubble flow <br /> strips VOCs from the groundwater The rising air bubbles also produce an air lift pumping effect, which <br /> moves the water up, and causes a suction effect at the bottom of the well <br /> The upward streaming, stripped groundwater leaves the well casing through the upper screen The mass <br /> of flowing groundwater leaving the upper screen is counterbalanced by the flow of groundwater toward <br /> the lower screened section,thereby setting up a three-dimensional groundwater circulation cell around <br /> the UVB well Contaminated groundwater flows toward the well through the lower screen and is moved <br /> up in the treatment well to the stripping zone by the action of the pump and the air lift effect The water <br /> is stripped of VOCs, and is returned to the groundwater through the upper screen The artificial <br /> groundwater circulation cell established by the UVB system is superimposed over the natural <br /> groundwater flow surface, and results in a three-dimensional flow regime around the UVB well <br />