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i <br /> 4 0 CONCLUSIONS AND RECOMMENDATIONS <br /> The soil boring data and analytical results indicate the following <br /> o The silt layers beneath the site have adsorbed greater quantities of TPHg <br /> ' containinants than the sandy layers These results are consistent with the fact that <br /> fine particles, such as silt, have more surface area for adsorption of contaminants <br /> ' o The soil clean-up rate would be relatively slow and be controlled by the diffusion of <br /> the TPHg vapor from the silt to the sand layers These site conditions make <br /> prediction of cleanup time very uncertain <br /> ' o TPHg contaminants were present in the groundwater Based on the analytical results <br /> of soil boning samples taken at 66 feet, it appears that the decline of the groundwater <br /> table, from a depth of approximately 60 feet in past years, to below 66 feet, has <br /> resulted in contamination of the lower vadose zone No soil data was obtained below <br /> 66 feet <br /> ' o The vertical and lateral extent of contamination has not been completely defined <br /> from the three soil borings Based on the concentrations shown on Figure 3 and on <br /> the assumption that the contaminants have dispersed in the north-south directions <br /> similarly to the dispersion indicated in the east-west direction (Cross-section A-A'), <br /> the estimated total quantity of TPHg in the vadose soil beneath the tank <br /> emplacement is approximately 13,000 pounds Calculations are included in <br /> Appendix C <br /> ' The pilot test field data and analytical results indicate the following <br /> o The radius of influence of VEW-1 is adequate to extract soil vapor from a 25-30 foot <br /> ' radius around the well The location of the extraction well is in the apparent source <br /> area and therefore would facilitate removal of the contaminants <br /> o The size of the pilot blower, piping and carbon beds is adequate for full scale <br /> operation of a one extraction well system <br /> ' o The calculated quantity of TPHg adsorbed by the carbon beds during the pilot test <br /> is inconsistent with the average adsorption rate, (approximately 15 pounds <br /> hydrocarbon/100 pounds carbon) specified by the manufacturer Calculations base <br /> on vapor sample laboratory analyses estimate that 440 pounds of TPHg were <br /> removed during the pilot test However, monitoring of the outlet of the first stage <br /> ' carbon beds with the, PID did not, however, indicate breakthrough of VOC's At a <br /> maximum of 10-20% rate of TPHg adsorption on activated carbon for two 220 pound <br /> carbon beds, 88 pounds of TPHg contaminants would have been removed from the <br /> ' soil Calculations are included in Appendix C The reason for this discrepancy is <br /> being evaluating <br /> 4 REMEDIATION <br /> tSERVICES, INC <br />