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vaii0i4vv0 tv:it r&& waccjoucis aumraleew WJUe <br /> pump <br /> SfEEEffON PRO EEIU�E <br /> A. Pun Ip capacity <br /> Bete nim hOW-PRESSURE BIMI13I4TIAM-PAGE, lira#7 <br /> umpcapasity = 36- GPM-- <br /> Pump-eapasityshow4be-between 2G4W441D-GPM Rw chargiMa-MaWold <br /> or for pumping to a gravity situation,.is, a drop box or distribution box. <br /> W DO mine raluirements <br /> i <br /> 1'_ E levatim c6Hirence,between pump and the point of discharge = 12 <br /> 2. pwmping-te-a-pressur , add-&feetof head roquWed-aLthe <br /> .rmnfttd: If-pumping to srgrovity'sysWm mse-zereo(0)feet of head:- ' 5� <br /> 3 loss <br /> Enter-fnchon-loss teble•wit#gpf*- wand pipe diameter. 2.0 <br /> 0?25 <br /> LOSS IN PLASTIC PIPE <br /> TE NOMINAL PIPE DIAMETER PLOW RATE NAL PIPE DIAMETER <br /> 1:S 2- 3 'II�ERNM 1.S 2 3 <br /> 247 0.73 O.tt' 35 61 _ 2.06 0.30 <br /> wm 1.14- 646- .. 40— d 94- 2.84 Oc3� <br /> 30.- 5.23 155- OSS �4s 11.07 3.26 0.41L <br /> rictionk= 2.@&. Jaetpe -100ftof-pi w <br /> Qetarotne total pipe.laagthfM a-pump to di=bs Points _ 2JM:0 <br /> Add 25%to pipe lengt rabow to account W NiAg-loss = 350.4 feet pipe <br /> Calculate total friction loss by multiplying friction loss in ft/100 We by <br /> valent Pipe length ab" <br /> 2.06 X 35G 00- lg 721.00 1100 ^ 7.2 ft head <br /> E: -is the sura-ofthe-elevatiB1•plus additioick-&prossyre <br /> for he manifold i32 plus the total friction loss 38c. <br /> 12.0 plus 5.0- pkss-• 7.2 ! equals. 24.2 ft total head <br /> 0. The Pump fe"Im 3& __ ►a" 24 feet of head <br /> PAGU. s- OF-. 1s.- 40 W11Ow St,Orono <br />