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rFaxntta <br /> ated nitrate loading concentration in the recharge effluent is calculated to be under the <br /> Contaminant Level (MCL) limit for nitrate in drinking water. The variables used in the <br /> ns above are conservative. For example, the use of 87 mg N/L, which was determined <br /> als ank effluent from the referenced Churches, is a much higher nitrogen <br /> a '0n than th se concentrations published in the sources referenced on Page 15, Table 10 oary Report. econdly, various researchers place the nitrogen reduction occurring in septic <br /> 10%to 200 . From the May 8, 2003 Symposium"Onsite Wastewater Treatment-Nitrogen <br /> ,"Dr. S Oakley of Chico State University states that"approximately 20%of the total <br /> enerated is removed in the septic tank."As noted above, no reduction in nitrogen <br /> concentration within the septic tanks was assigned in the calculations. <br /> C. SEPTIC SYSTEM OPERATIONAL PARAMETERS AND COMPONENTS OVERVIEW <br /> SSS 3.7. The design of the proposed pressurized filter bed septic system for the Multipurpose <br /> Buil ' g s based upon the factors of environmental protection, efficient operation, and disposal field <br /> longevity. Although the disposal area may be considered temporary since it is anticipated to be / <br /> operational for less than five years, it must be considered to be operational for an indefinite lifespan, <br /> since the EHD regards any installed decentralized wastewater disposal system to have an indefinite <br /> lifespan. An overview of the wastewater disposal system operation is as follows, and is depicted on <br /> the Site Plans: <br /> Beginning with the restroom west of the kitchen, influent from this restroom will gravity flow west <br /> into a single compartment, 1,200 gallon tank with an effluent filter. Influent from the kitchen will <br /> also gravity flow west into a 2,000 gallon, three-compartment interceptor tank, or grease trap tank. <br /> Effluent from these two tanks will join into a single, six-inch dia. ABS line to gravity flow around the <br /> west end of the Multipurpose Building, and connect to the first of three 2,000 gallon, single <br /> compartment tanks. Influent from the Mens's and Women's Restrooms will also enter this first, <br /> 2,000 gallon tank. Effluent from this first tank will then enter a second single compartment, 2,000 <br /> gallon tank. These two tanks must have a six-inch dia. connection near the floors of the tanks,per <br /> EHD require , effluent will vi ow into a 'rd, single compartment, 2,000 gallon <br /> tank. T ' will be the ump Chambe to pressurize the fi er beds. The Pump Chamb wi <br /> consist of enco Biotube® filtration,with Duplex Pump Sy em. The two pumps w' ] lterrtate <br /> between p ssurizing the tw separate filter b s, operating u er"on-demand"dose cyc se <br /> three tanks wi rovide s' ificant quiescent tr el distanc f approximately the lengths of three- <br /> 2,000 gallon tanks cceptable hydraulic residence time(HRT) to occur. By"on-demand"dosing <br /> of the effluent, this creates surge capacity within the tanks and extends hydraulic residence time. <br /> Effluent will be distributed equally during events and activities at the Multipurpose Building when <br /> demand occurs, and makes the system less complicated to operate for the Church. <br /> The filter bed arrangement will consist of Infiltrator® Chambers with the pressure lateral piping <br /> hanging from the tops of the chambers. Effluent will spray to the tops of the Chambers and trickle <br /> down the sidewalls to the soil-effluent interface. Six-inch louvers are located on each side of the <br /> Chambers to allow oxygen diffusion and potential effluent uptake by plant root structures that may <br /> extend to this depth. <br /> Page -12- <br /> Chesney Consulting <br />