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h <br /> Cincludipng <br /> ATEAL LENGTH AND DIAMETER <br /> ping to consist of PVC Schedule 40. As determined above,lateral length shall be 31.5 ft each lateral, <br /> the f inch clean-out sweep assembly.The diameter shall be 1 inch I.D. <br /> PERFORATION SIZE,SPACING AND NUMBER PER LATERAL <br /> Perforations shall be 5132 in. dia. For effluent distribution applications to be -4 ftZ/orifice, the spacing of <br /> perforations= 3 feet(area per orifice x no. of laterals on each side of center feed - (absorption area width) <br /> =4 ft' x 3 _5 ft= 3 ft. The number of perforations per lateral shall be: <br /> N=(p_x)+0.5 = (31.5 ft-3 ft) + 0.5 = 21 perforations per lateral x 6 laterals= 126 total perforations <br /> LATERAL DISCHARGE RATE(LDR) <br /> Recommended distal pressure is 5 ft, translates to 0.68 gpm per orifice. LDR=0.68 gpm/perforation x 11 <br /> perforations/lateral =7.5 gpm/lateral <br /> MANIFOLD AND FORCE MAIN DIAMETER <br /> The force main and manifold shall be 2.0 in. I.D., composed of PVC Schedule 40. <br /> NETWORK DISCHARGE RATE (NDR) <br /> NDR=6 laterals x 7.5 gpm/lateral =45 gpm. <br /> APPROXIMATE TOTAL DYNAMIC HEAD(TDH) <br /> The TDH cannot be accurately determined at this time since some design factors are unknown. <br /> Consequently, an estimate of the TDH is provided assuming a total distance of 35 feet from the chamber to <br /> the end distribution network for the primary mound system. The TDH the pump must work against: <br /> System network head= 1.3 (conv. factor) x distal pressure 5 ft=6.5 ft <br /> Elevation distance between the pump and the highest elevation of the distribution network =9.0 ft <br /> Friction loss in force main =7 ft(185 ft of force main+ manifold) +add-on friction loss of 8 ft= <br /> TDH: 6.5 + 9 + 7 + 8 = 31 ft <br /> k <br /> PUMP REQUIREMENTS <br /> A=duplex pump-system;each-pump puiriping 45=gprn again kt>31"feet of head. The selection based on the <br /> System Performance Curve found on the Plans. <br /> APPROXIMATE DOSE VOLUME <br /> A=dose volume of: 20°Io of.design flow'(gal/d'ADF)-shall be used=.75 gallons. This conforms with the <br /> California State Water Resources Control Board- Guidelines for the Deskon, Installation and <br /> _Operations of Mound Sewage Disposal Systems document of"recommended dosing volumes"found in <br /> Section 34.0, Page 17, Table C. Use 5 times the lateral void volume: <br /> Lateral dia. = 1.0 in. <br /> Lateral length = 31.5 ft <br /> Number of laterals= 6 <br /> Lateral void volume=0.041 gal/ft <br /> 'CNet Dose-Voluine-=5'x 31:5 x 6 x 0:041'=;77 gals/dose. <br /> Floats shall be set to dose an approximate volume of 75 gals/dose <br /> By ha"ving orifices in.thi f2 "o'clock position with shields,the pumps will not have to charge the piping <br /> .network at the time of every dose. <br /> 17 <br /> Chesney Consulting <br />