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Corrective Action Plan Page 23 <br /> will serve to secure the treatment equipment and screen it from view so that there will be <br /> mmimal visual impact resulting from the installation <br /> Electrical power (480V, 3 phase) for the treatment equipment, will be brought to the site <br /> by overhead lines strung between one of the existing Pacific Gas and Electric Company (P <br />' G& E ) power poles located in the lane behind Tracy Feed and Supply at 1031 "F" Street <br /> (see Figure 6 for location) and a new pole (System 15 on Figure 10) erected within the <br /> proposed enclosure Gates in the enclosure fencing will provide access for system <br />' maintenance and replacement of consumable materials <br /> Principal Process Units <br /> The principal process units and equipment in the groundwater treatment system are as <br /> follows <br /> Air Stripper. The primary system for removing components of gasoline from groundwater <br />' pumped from the recovery wells will be a modular, low-profile air stripper (System 1 on <br /> Figure 10)that removes volatile organic compounds (VOCs) from the water This unit has <br /> a hydraulic capacity of 45 gpm and is equipped with four aeration trays and a blower <br /> capable of generating 300 cfm (cubic feet per minute) of forced air <br /> The influent stream of contaminated water is sprayed into the top of the air stripper <br /> through a course-mist spray nozzle The water then flows downward over the stack of <br /> four baffled aeration trays The stream of forced-air generated by the blower enters the <br /> bottoms of the trays through 3116 in diameter holes This forms a froth of bubbles in the <br /> water and generates a large mass-transfer surface area where the contaminants are <br /> volatized The size and number of trays in the stack is selected to achieve the required <br /> volatization The treated water falls into a reservoir in the bottom of the unit and is <br />' discharged from 4there by means of a pump After exiting from the top of the stack of <br /> aeration trays, the air stream carrying the valorized VOCs is exhausted from the top of the <br />' umt via a chimney <br /> After passing through the air-stripper, the water stream is <br /> pumped through a pair of granular, activated-carbon (GAC), adsorption vessels (System 8 <br /> on Figure 10) which are connected in series Each vessel has a hydraulic capacity of 50 <br /> gpm and contains a 1000 lb charge of activated carbon derived from bituminous-coal The <br /> purpose of these units is to remove any traces of long carbon-chain components of <br /> gasoline that might remain in the water stream after it has passed through the air stripper <br /> They also provide a conservative defense against discharge of any water containing <br />' impermissible concentrations of fuel hydrocarbons that might pass through the air stripper <br /> in the event of an equipment upset <br />' The series arrangement of the pair of GAC units provides for the upstream unit to serve as <br /> the primary means of removing any components of gasoline not removed from the water <br /> stream by the air stripper The quality of water exiting the first unit is monitored by <br />