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George's Service <br /> Remedial Action Work Plan <br /> Project No.425.2 <br /> June 30,2011 <br /> 6.1.5. Sparge Point <br /> As described above, our proposed sparge point will consist of a 24" long fine screened <br /> interval designed to produce fine bubbles with maximum surface area. We found that this <br /> type of delivery system worked just as well during the pilot test as the more expensive sparge <br /> points and has the added advantage of being able to be cleaned by mechanical scrubbing <br /> methods if the well becomes bio-fouled. <br /> 6.1.6. Air Sparging Equipment <br /> The air sparging equipment will consist of a blower/air compressor, controller, manifold, <br /> piping, fittings, pressure gauges and distribution valves. Three bids must be solicited for the <br /> project in order to stay in compliance with USTCFP requirements. <br /> The required injection pressures and flow rates utilized in the sparging system must be <br /> sufficient to overcome the head pressure of the overlying water column and the capillary <br /> pressure of the subsurface soil. The flow rates must be as high as possible to deliver air to <br /> the maximum possible area of the plume. The injection pressures will be lower than the <br /> pressures which may cause the lateral spreading of contamination plume. <br /> Initially, air will be injected into the subsurface to open up the soil pore space. The <br /> pressurized air will be delivered through diffusers that will introduce fine bubbles into the <br /> soil. The bubbles will form micro-channels or preferential pathways through which the air <br /> will flow. While in the channels the air will allow the gasoline to undergo a phase transfer <br /> from dissolved to vapor phase. The system will operate in pulse mode to allow the micro- <br /> channels to repeatedly fill and empty which will cause a reaction chamber type response. <br /> The increased DO will oxidize the MTBE as well as other constituents and unconsumed <br /> oxygen will serve to augment the bio-remediation capacity of the aquifer. <br /> The EPA has stated that I PSI of injection pressure is necessary for every 2.3 feet of <br /> hydraulic head. (USEPA: How to Evaluate Alternative Cleanup Technologies for <br /> Underground Storage Tank Sites, May, 1995). Water Table is at about 12 feet bgs. This <br /> would require an injection pressure of 4.4 PSI (10 feet divided by 2.3). <br /> 6.2. Low Vacuum Soil Vapor Extraction <br /> A low vacuum soil vapor extraction (SVE) is proposed to remove volatile organic <br /> compounds from the subsurface by drawing air through the porous gravel excavation backfill <br /> area and surrounding subsurface soils. <br /> In July, 2009, GTI conducted a soil vapor pilot test to evaluate the feasibility for site <br /> remediation using soil vapor extraction technology. A vacuum blower was temporarily <br /> attached to VEW-I and run for eight horns. Vacuum pressure draw down was measured in <br /> surrounding groundwater monitoring wells, volumetric air flow was measured, emissions <br /> were monitored using a portable photo-ionization detector, and vapor samples were collected <br /> for laboratory analysis. <br /> Geological Tech dcs Inc. 17 <br /> 4252 RAP.docx <br />