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FFintothecompartment of the first conventional septic tank, as is common practice. O+G <br /> bove 30 mg/L can be detrimental to the permeability of the receiving soils by <br /> l pores. Also, waste streams with O+G concentrations exceeding 30 mg/L can <br /> rmance of Package Treatment Plants (PTP). <br /> In addition to analysis of O+G from the grease tank, other constituents-of-concern were also <br /> analyzed for comparison with the analysis of the conventional septic tank effluent. As noted, <br /> there is a significant Total Kjeldahl Nitrogen(TKN) concentration in the grease tank and a Total <br /> Suspended Solids (TSS) concentration that is more than double the conventional septic tank. The <br /> Biochemical Oxidation Demand (BODS) measures wastewater strength with the test results <br /> indicating an extremely high strength wastewater at 3663 mg/L. <br /> TABLE 3 <br /> Analysis of Effluent Analysis of Effluent Crites and I-S.E.P.A. <br /> ANALYTE From Last from the Last Grease Tchobanoglous: <br /> Conventional Septic Interceptor Tank Residential Complete Mix <br /> Tank:. (Roth Tanks Nixed) Septic Tank Values <br /> Total Kjeldahl Nitrogen 66.7 mg/L 52.7 mg/I. 70.3 mg/L 35-100 mg/1. <br /> (TKO) (59.7 mg/L I <br /> Ammonia Nitrogen 31.5 mg/L 11.7 mg/L 41.2 mg/L 6-18 mg/L <br /> (NH,-N) (21.6 mg/L) <br /> Organic Nitrogen 35.3 mg/L 41.0 mg/L 29.1 mg/L 30-82 mg/L <br /> (38.2 mg/l,) <br /> Total Suspended Solids 216 mg/L 472 mg/L 503 mg/L 200-290 mg/L <br /> (TSS) (344 mg/L I <br /> Biochemical Oxygen 836 mg/L 3663 mg/L 450 mg/L 200-290 mg/L <br /> Demand(BODS) (2250 mg/L) <br /> PH 6.3 4.8 N/A N/A <br /> Total Alkalinity 390 mg/L 161 mg/L N/A N/A <br /> Oil and Grease N/A 232 mg/L 164 mg/1. N/A <br /> CONCLUSIONS AND RECOMMENDATIONS <br /> The soils within the proposed disposal area reveal favorable permeability characteristics from <br /> four ft below existing grade down to 25 ft. The final grade is proposed to be approximately one ft <br /> lower than current grade in this area. This will place the bottom of the filter bed disposal <br /> structure, and therefore the soil-effluent interface, at the top of permeable strata. <br /> Regarding the referenced sand stratum from 10 ft to 15 ft below grade and the possibility of <br /> adverse permeability conditions created by the phenomenon of percolating effluent congregating <br /> on top of this sand stratum: Since the coarser stratum is comparatively thin(five ft thick)with the <br /> soil becoming a uniform loam from 15 ft to 25 ft in depth, no adverse effects are expected. As <br /> referenced, there may be anaerobic conditions above this sand stratum which promote <br /> denitrification. <br /> Page 5 of 7 <br /> Chesney Consulting <br />