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Jun 6 1996 4 20Ph1 IEG TECHNOLOGIES No 2616 P 22/34 <br /> M � <br />. Basic System Concept <br /> As shown in Figure 1, the UV8 system consists of a specially adapted groundwater well with <br /> two separate screen sections, a groundwater treatment unit located inside the well casing <br /> (typically a "stripping reactor"), an above-ground mounted blower, and an optional off-air <br /> treatment system, The blower creates a reduced pressure within the air-tight well casing. <br /> Atmospheric air is introduced to the system, by virtue of the pressure differential, via a fresh <br /> air pipe which is open at the ground surface and connected to the stripping reactor located <br /> in the well casing Fresh air is drawn through the fresh air pipe into the stripping reactor <br /> where it is directed to a sieve plate. As air bubbles migrate upward from the sieve plate, they <br /> strip the VOCs dissolved in groundwater passing through the stripping reactor. The off-air <br /> stream, which now includes vapor-phase contaminants, is brought to the surface by the <br /> blower and treated as necessary <br /> The rapidly expanding and rising air bubbles produce an air-lift pump effect which, together <br /> with the vacuum in the well casing, elevates the groundwater in the well and causes suction <br /> at the lower well screen The subsequent fall of groundwater along the walls of the well <br /> produces an oscillating hydraulic pressure which forces the water horizontally through the <br /> upper screen into the aquifer A portion of the treated groundwater eventually migrates from <br /> the upper screen to the lower screen by means of an extensive three-dimensional groundwater <br /> flow field. in the presence of a natural groundwater flow, a portion of the flow entering the <br /> well casing will be new upstream waters which have entered through the upstream capture <br /> zone. An equal portion leaving the well 'casing will exit the circulation cell through the <br /> downstream release zone. These flows and the dimensions of the capture zone, circulation <br /> cell, and release zone can be calculated using design aids based on numerical simulations of <br /> the groundwater hydraulics. <br /> Aerobic biodegradation of organic contaminants is enhanced by the recirculation of <br /> oxygenated groundwater into the aquifer The vadose zone and capillary fringe are remediated <br /> by virtue of their exposure to the upper screened section of the UVB well by soil flushing and <br /> soil vapor extraction mechanisms <br /> Case History- Troutman—North Carolina <br /> A UVB 400 mm system (16 inch diameter well casing) was installed in September 1992 at <br /> a former retail gasoline facility in the Piedmont physiographic province in west central North <br /> Carolina A site map depicting well locations and isopleths of total BTEX concentrations prior <br /> to UVB activation appear in Figure 2 The saturated regolith consists of saprolite from a depth <br /> of about 45 feet from land surface to the top of weathered rock at about 65 feet from land <br /> surface. The saprolite is heterogeneous and vanes in grain size from medium to fine sand, to <br /> silt with clay, and is derived from the bedrock, a quartz-biotite gneiss <br /> A diagram showing the construction details of the UVB well is given as Figure 3 Depth to <br /> water at this site is 45 feet below ground surface Groundwater flow is to the south and the <br /> approximate hydraulic conductivity is 1 9 x 10-4cm/sec, A 20 foot interval of the saturated <br /> zone is being addressed by the UVB system <br /> i <br /> z <br /> 1 <br />