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The VOC concentrations in groundwater leaving the upper screen of the well are significantly <br />' lower than the influent hydrocarbon concentrations Most of the treated groundwater leaving the <br /> upper screened section of the well is retained in the UVB circulation cell and re-enters the lower <br /> screen section a number of times Since the treated groundwater leaving the UVB well is almost <br /> saturated with oxygen, the effluent groundwater enriches the saturated zone with dissolved <br /> oxygen, enhancing aerobic biodegradation throughout the circulation cell <br />' The UVB percent stripping efficiency is defined as (1- Co,,, / C,,,) x 100, where Coin is the <br /> concentration of volatile and semivolatile hydrocarbon constituents in groundwater leaving the <br /> upper screen of the UVB well, and C,,, is the concentration of volatile and semivolatile <br />' hydrocarbon constituents in groundwater entering the lower screen of the UVB well <br /> Representative samples of groundwater entering and leaving the lower and upper screens of a <br /> UVB well, respectively, are collected from monitoring wells installed as close to the UVB well <br /> as possible while avoiding any damage to the UVB well packing <br /> 3.2 DESCRIPTION OF UVB SYSTEM AT FORMER EXXON RS 7-3942 <br />' The UVB treatment system at former Exxon RS 7-3942 consists of an in situ, 400-millimeter- <br /> diameter reduced pressure air stripper and a 5-HP blower and includes a weatherproof cover and <br />' moisture knockout drum The moisture knockout drum has a built-in stripping unit to treat any <br /> accumulated water prior to removal Vapors stripped from groundwater in the UVB air stripper <br /> are extracted by the UVB vacuum blower A Grundfos pump (1/3 HP, 110 volt, 6 3 amp, single <br /> phase) is used as the support pump to maintain the desired flow rate of water through the UVB <br /> system The pressure outlet of the UVB blower is connected to a Thermtech VAC 25 <br />' thermal/catalytic oxidizer, to destroy VOC vapors in a heated chamber prior to release into the <br /> ambient air The Thermtech VAC 25 was already onsite to treat soil vapor extracted by the SVE <br /> system The existing piping manifold at the site was modified to connect the UVB vacuum <br />' blower to the oxidizer (Figure 3) <br /> The UVB well consists of an upper and a lower screen and 16-inch nominal diameter well <br />' casing The well casing is made of mild galvanized steel with a 0 25-inch thickness The lower <br /> (Irrigator®) well screen has 4 feet of 0 025-inch slots and a 2 5-foot-long tight-wind sump with <br /> plate bottom The upper well screen is double-cased and has approximately 6 feet of 0 040-inch <br /> slots The UVB well completion diagram, along with the diagrams for adjacent monitoring wells <br /> UVB-MW 1 and UVB-MW2, is provided as Figure 4, and on its own in Appendix A <br />' The wellhead is sealed with a steel flange and HDPE cover The internal UVB well components <br /> are a fixed inflatable packer, a single-speed support pump, and an air stripper The support pump <br /> allows a regulated amount of water to enter the air stripper, independent of the airlift pump effect <br />' created by the rising air bubbles in the stripper The UVB well components are depicted in <br /> Figure 5 <br /> The design of the UVB system installed at former Exxon RS 7-3942 was based on the <br /> assumptions and technical data outlined in the Technical Plan (EA 1996) Based on those <br /> assumptions and technical data, the upstream and downstream stagnation point distance S and <br /> capture zone widths B, and Bh were calculated (EA 1996) and are shown in Figure 6 <br />' WP61 73942 R01397 3 6 <br />