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Mr. David Nitz <br />Pag s 2 <br />January 12, 1987 <br />Measured percolation rates are consistent to somewhat rapid for the <br />texture of the soil materials in which the percolation tests were <br />run. <br />The City of Orono requires at least three feet elevation difference <br />between the bottom of the filter rock of a septic system and ground <br />water or indication of periodic soil saturation such as soil <br />mottling. To meet this requirement, a mound septic system is <br />recommended for the primary and secondary septic systems at this <br />site. <br />The mound is designed to serve a four bedroom house with a <br />whirlpool bath. Design sewage flow for the house is 600 gallons <br />per day. A sewage flow of 100 gallons per day is added for the <br />whirlpool bath. Total design sewage flow is 700 gallons per day. <br />with a design infiltration rate of 1.2 gallons effluent per square <br />foot per day for the medium sand fill material of the mound, the <br />required rock bed area of the mound is 700 square feet. <br />700 gal/day 1.2 gal/ft2/day = 583 ft2 <br />A rock bed 10.0 feet wide by 60.0 feet long provides the needed <br />area. A minimum of one foot (1.01) of medium sand should be <br />constructed below the rock bed. <br />The pressure distribution system of the mound consists of Schec _e <br />40 PVC plastic pipe. The supply pipe should slope back towards the <br />pumping chamber so that it drains after the mound is dosed. The <br />la::ezals are 1.5 inch inside diamete- r-pes. The laterals should <br />have 1/4 inch diameter holes drilled at a spacing of 3.0 feet. The <br />laterals should be assembled to the manifold so that the holes <br />point downwards into the rock bed. The distal ends of the laterals <br />should be drilled norizontally in the end cap near the crown of the <br />pipe to facilitate air venting. <br />A submersible effluent pump capable c•f deliver.Lng at least 45 <br />gallons per minute against a total dynamic head of at least 10.2 <br />feet should be selected. Headlosse- are calculated as follows: <br />1. Verti.:al headloss of 4.5 feet between pump disc,arge (approx. <br />elev. 95.0) and manifold (approx. elev. 99.5), <br />i�tion �oss of 0.7 feet in 20 feet of supply pipe (3.3 feet <br />per 100 feet 2.0 inch I.D. plastic pipe at 45 gpm flow), <br />3. Five feet (5.01) to account for losses in distribution network. <br />