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NLS§ 4.2, SSS§ 6.7, SSS§ 5.4, 6.8. The soils directly underlying the proposed filter bed area <br />reveal a permeability that correlates with the texture analysis of the sandy loam/loamy sand <br />receiving soils. However, shallow (-24") perc test results revealed apparent soil compaction, <br />which may have been caused by farm machinery/implements. <br />A backhoe test pit excavated adjacent to the existing vineyard east of the stormwater infiltration <br />basin indicates probable denitrification evidence, with the nitrate -nitrogen concentrations <br />decreasing from the 6 ft depth to the 9 ft depth by 31% (172 ppm to 118 ppm). This denitrification <br />value of 31 % was used in the nitrate loading calculations. <br />New drinking water regulations focusing on supplying safe drinking water for all Central Valley <br />residents while simultaneously protecting the economic viability of California agriculture, are <br />prompting the introduction of several new programs to address regulations, one of which is the <br />Nitrate Control Program (NCP). In addition, the California Sustainable Winegrowing Alliance <br />(CSWA) advances the wine industry's commitment to environmental stewardship and social <br />responsibility. The following lists the specific OWTS design parameters to mitigate nitrate impact, <br />and promote environmental stewardship and sustainability: <br />• The 4,000 gallon septic tank will retain particulate/organic matter received from existing <br />septic tank carryover effluent that will be pumped to this tank. The large hydraulic <br />residence time (HRT) this tank provides will reduce the organic nitrogen fractions through <br />anaerobic digestion and removal of all nitrogen fractions by eventual tank pumping, thus <br />ultimately reducing nitrate formation. <br />• The Polylok PL -625 high flow effluent filter, rated for 8,000 gpd will trap particulate <br />matter before effluent flows from the 4,000 gallon tank into the 1,500 gallon pump <br />chamber tank. By trapping particulate matter, Biochemical Oxygen Demand (BOD) and <br />Total Suspended Solids (TSS) can be reduced by 28% and 63%, respectively (Ref. 7, Pg. <br />183), thus creating a more favorable soil environment for effluent treatment. <br />• The 1,500 gallon pump chamber tank has two compartments, with the first compartment <br />adding additional HRT for trapping and digesting organic matter. <br />• The two high head effluent pumps have built-in filter screens for additional particulate <br />screening. <br />• Effluent pumped to the filter bed will alternate between the two pumps and between the <br />two zones of the filter bed. Equal distribution of effluent between the two filter bed zones <br />will give each zone time to assimilate and treat the effluent within the soil environment by <br />preventing saturated soil conditions to materialize. <br />The pump cycles will operate "on -demand" and not "time -dose" since wastewater flows every 24 <br />hours are anticipated to be relatively constant at least six months of the year; at pre -crush, crush <br />and post -crush. Consideration may be given to time dosing the other six months of the year. <br />Nothing is to be stored on, and no vehicles other than farm machinery/implements are to be driven <br />over the filter bed area. This farm equipment must be the lightest weight available, preferably with <br />tractor treads to minimize psi pressure. <br />Page -11- <br />Chesney Consulting <br />