Laserfiche WebLink
CI <br /> = Resultant average concentration of nitrate-nitrogen in recharge water-(ppm NO,-N) <br /> = Volume rate of wastewater entering the soil averaged over the gross developed area in inches per yr <br /> = Total nitrogen concentration of wastewater in mg N/L <br /> d = Fraction (%) of nitrate-nitrogen loss due to denai�7ification in'the soil <br /> R = Average recharge rate of rainfall -inches perS§3.2 j <br /> Nb= Background nitrate-nitrogen concentration of rnf�lLlrecharge, exclusive of wastewater influences <br /> (ppm NO,-N) ---_ <br /> Values and Assumptions <br /> I= 144 gpd x 250 work d/yr=36,000 gals=total WW/yr=4,813 cu ft = 0.14 in. <br /> 9.45 Ac x 43,560 sq ft/Ac x(1 ft/12 in.) <br /> Nw = 113 mg N/L: 10%reduction from the septic tank =(1-0.1)113 = 102 mg N/L <br /> d = Assume 0% due to the sandy nature of the native soil and therefore low denitrification potential <br /> R = 11 in/yr. <br /> Nb= Assumed to be 0.1 ppm NO,-N <br /> 0.14 in/yr(102 mg N/L) (1 -0)+(11 in/)r x 0.1 ma/L) <br /> Nr = (0.14 in/yr+ 11 in/yr) <br /> Nr = 1.4 ppm as nitrate-nitrogen(NO,-N) or 6.2 p m as nitrate(NO,) <br /> The calculated nitrate loading concentration in the recharge effluent from the Office Building is <br /> calculated to be under the Maximum Contaminant Level limit for nitrate in drinking water. The <br /> variables used in the calculations above are conservative. For example, the use of 113 mg N/L, which <br /> was determined from actual septic tank effluent from three commercial facilities is a much higher <br /> nitrogen concentration than those concentrations published in the sources referenced in Table 4. <br /> Secondly, various researchers place the nitrogen reduction occurring in septic tanks at 10%to 20%. <br /> From the May 8, 2003 Symposium "Onsite Wastewater Treatment- Nitrogen Removal,"Dr. Stuart <br /> Oakley of Chico State University states that"approximately 20% of the total nitrogen generated is <br /> removed in the septic tank." As noted above, a conservative estimate of 10%was used for the <br /> proposed septic tank. <br /> C. SEPTIC SYSTEM OPERATIONAL PARAMETERS AND COMPONENTS - <br /> AREA TO SERVE THE MANTECA RV STORAGE PARK <br /> SSS§ 3.7. The design of the pressurized filter bed disposal system for the Manteca RV Storage Park <br /> will be under the direction of Mr. Carl Fiorica, R.C.E. of RBF Consulting - Roseville California. <br /> Discussion of efficient operation, disposal field longevity, and environmental protection are based <br /> upon the environmental parameters discussed below. An overview of the system operation is as <br /> follows for the new Office Building: Influent waste from the building will gravity through a four-inch <br /> ABS tightline(0.25 inch/1 ft)-into the first compartment of a two-compartment 1,200 gal septic tank. <br /> The effluent will then gravity into the second compartment which will be the pump "chamber. This <br /> chamber will have an Orenco Biotube filter vault, and a duplex pump system to pressurize effluent for <br /> disposal to two filter-beds, as depicted on the Site Plans. As referenced below, each filter bed is to be <br /> 10 ft wide and 40 ft long. <br /> 12 <br /> Chesney Consulting <br />