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� v <br /> G � <br /> � r <br /> ASSOCIATES I NC J <br /> ft/1,000 ft) which is an average value obtained from historical groundwater elevation data The <br /> remaining cells values in the IBOUND matrix were set at an initial value of —10 feet with a <br /> ' corresponding IBOUND value of I (active cell) The recharge package was used with a recharge <br /> flux of 3 17E-08 feet per second (ft/sec) This corresponds to a typical annual rainfall of 12- - -- <br /> inches per year No wells were included in the flow model The model was based on natural <br /> flow conditions that would be present at the site once the pump and treat system is <br /> decommissioned The soil is assumed to be sand and silty sand based on information from soil <br /> ' boring previous subsurface investigations A bulk density of 42 47 kilograms per cubic foot <br /> (kglft3) and an effective porosity of 0 25 were assigned to the soil These parameters were <br /> chosen based on typical values for silty sands Information regarding assumptions and input <br /> ' parameters is given listed in Table 6 <br /> 5.2 Transport model using MT3D—Run Number 1 <br /> ' MT3D was used to generate a solute transport model using the flow model created in <br /> MODFLOW Advection was modeled using the Advection Package, dispersion was modeled <br /> ' using the dispersion package, and biodegradation of dissolved hydrocarbons was modeled <br /> using the chemical reaction package The transport model was created for volatile organic <br /> hydrocarbons for a 10-year period at 1-year intervals In this run of the model, initial TPHg <br /> concentrations were interpolated from an isoconcentration map of dissolved TPHg <br /> concentrations in groundwater generated from laboratory analytical data from the November <br /> 2003 sampling event This model shows the fate and transport of the existing TPHg �5r��tes <br /> ' ,S'UUYGe <br /> contaminant plume with the source removed Information regarding assumptions and input /'c01a11-tl <br /> parameters is given listed in Table 6 s��Id S4 <br /> ' The results of this MT3D model run indicates that the groundwater contaminant plume will <br /> continue to decrease in size and concentrations of hydrocarbon contaminants will decrease <br /> ' significantly over the next several years The model predicts that TPHg concentrations in weld_ 0 Flu <br /> MW3 will decrease from the current maximum concentrations of approximately 1,700 ug/1 to <br /> concentrations of approximately 3 ugll in 5 years to concentrations of less than 0 0002 in 10 <br /> ' years The model predicts similar decreases in TPHg concentrations in wells MWI. and <br /> MW4 Figures 12, 13, and 14 show hydrographs of wells MW1, MW3, and MW4, <br /> respectively The hydrographs show TPHg concentrations over time predicted with the MT3D <br /> ' model These predicted trends in decreasing hydrocarbon contaminant concentrations are in ft«J ti's] <br /> accord with trends in TPHg and benzene concentrations over the past 5 years as shown in �Gz,+ <br /> laboratory analytical data collected during quarterly groundwater sampling events A map '>W1111401f <br /> showing TPHg isocontours protected over time generated with the MT3D model is shown in f ss 4— <br /> Figures 15 and 16 VG <br /> ' 53 Transport model using MT3D—Run Number 2 <br /> MT3D was used to generate a solute transport model using the flow model created in <br /> MODFLOW Advection was modeled using the Advection Package, dispersion was modeled <br /> w 1271421reportslclosure doc 17 <br />