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MagnehelicTM gauges attached to the test well and individual monitoring points are used to measure vacuum A <br /> thermal anemometer, or a Pitot tube, inserted into a manifold attached to the test well, is used to measure vapor <br /> extraction flow rates If the vacuum is below 10 inches of water column, a thermal anemometer is used If the <br /> vacuum is greater than 10 inches of water column, the flow rate will be measured using a pitot tube and <br /> MagnehelicTM gauge An Alpha OneTM, or equivalent, air sampling pump is used to collect influent vapor <br /> samples into one liter TedlarTM bags from the manifold sampling port If necessary, effluent air samples are also <br /> collected into one liter TedlarTM bags A photo-ionization detector is used to measure volatile hydrocarbon <br /> concentrations in collected air samples An LEL/oxygen meter is used to measure percent LEL and percent oxygen <br /> in collected influent air samples One influent sample, and if necessary, one effluent sample,will be analyzed at a <br /> State-certified environmental laboratory for total petroleum hydrocarbons as gasoline according to EPA Method 8015 <br /> and for benzene,toluene, ethylbenzene and xylenes (BTEX) according to EPA Method 8020 Additional analyses <br /> will be performed as required by the permit or specific project requirements All data is recorded in a written log by <br /> the vapor extraction test technician Depending on equipment used, some data is also recorded in computer <br /> generated printouts or into electronic data logs <br /> Data Evaluation <br /> Radius f Influence <br /> The test is performed at several pressure/flow rate combinations (steps)to determine the optimal vacuum and flow <br /> rate needed to obtain a sufficient radius of influence for one well The radius of influence will be determined as the <br /> radius from the extraction well to a distance from the well where the measured vacuum is one percent of the applied <br /> vacuum(Buscheck&Peargin, 199 1) Alternatively,the radius of influence may be defined as the estimated distance <br /> from the extraction well where vacuums are not less than 0 1 inches of water (Johnson, 1994) This radius of <br /> influence is assumed to approximate the maximum distance from the extraction well at which contaminated soil will <br /> be remediated through volatilization Although there are limitations inherent in determining the radius of influence <br /> based on pressure distributions (Johnson & Ettinger, 1994), this method is generally accepted as a screening <br /> technique The radius of influence may not necessarily increase significantly beyond a certain flow rate and vacuum <br /> Therefore,the optimal vacuum and flow rate will be based on blower efficiency relative to the area of influence and <br /> may not necessarily be the maximum vacuum and flow rate This evaluation will be determined graphically by <br /> plotting the vacuums observed at each monitoring point versus the distance of the monitoring point from the <br /> extraction well for each step test Semi-log paper may be used to obtain a straight line fit through the data for each <br /> applied flow rate and vacuum In addition,the applied flow rates and corresponding vacuums for each test will be <br /> plotted on smear paper to evaluate the effect of vacuum on flow rates <br /> Perineabilgy <br /> Data collected from several monitoring points during each test will be evaluated to determine the permeability of the <br /> formation following the method outlined by P C Johnson, et al(1990)based on the flow rate and transient pressure <br /> distribution data Two different permeability calculations presented by Johnson, et al (1990) and summarized by <br /> Dupont(1993) can be performed depending on site parameters The first calculation assumes radial flow with no <br /> vertical leakage and relatively long screens (>10 ft) The second calculation assumes some vertical flow, shallow <br /> soil contamination and relatively short well screens (<10 ft) For a derivation and presentation of the calculations <br /> refer to the original references <br /> Number of Extraction.We Is Requircd <br /> Once an approximate permeability value has been obtained and is consistent with known subsurface lithology, the <br /> feasibility of reducing hydrocarbon contamination through vapor extraction in a reasonable period of time(<5 years) <br /> can be estimated using the model presented by P C Johnson, et al (1990) This model is based on the maximum <br /> contaminant vapor concentrations in extracted Vapors, residual soil contaminant composition, vapor pressure, <br /> assumed soil temperature and the ideal gas law and will be determined with the aid of the computer program called <br /> "HyperVentilate®" (Johnson, 1992) The number of vapor extraction wells needed to remediate the contaminated <br /> is soil within five years will be determined from the results of the pilot test and the feasibility calculations and is <br /> approximately equal to the estimated area of contamination divided by the area of influence of one well All <br /> CLEARWATER GROUP(SVE TEST) 2 revised June 29, 2001 <br />