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' : � __ OSTP Pump Selec�ion Design _ <br /> Minnesota Poilution UNIVERSITY <br /> Control A enc Worksheet OF�IINNESOTA � ti��: <br /> i0. Equivalent length of pipe fittings. Equivalent Length Factors(ft.)for PVG Pipe <br /> Section 10 is for Collection Systems ONLY and does N07 need to be Fittings <br /> completed for individuai subsurface sewage treatment systems. Fiuing Type �Pe Diameter(in.) <br /> 1 Yz 2 3 <br /> Quantity X Equivalent Length Factor=Equivatent Length Gate valve �.07 �.38 2.04 <br /> 90 Deg Elbow 4.03 5.17 7_67 <br /> Fitting Type Quantity Equivatent Equivalent 45 Deg Elbow 2.15 2.76 4.09 <br /> Length Fdctor Length(ft) Tee-Row Thru 2.68 3.45 5_11 <br /> Tee-Branch F ow 8.05 10.30 15.30 <br /> Gate Valve X - Swing Check Vatve 13.40 17.20 25.50 <br /> 90 Deg EtbOw X = Angle Valve 20_10 25_80 38.40 <br /> 45 Deg Elbow X _ Gtobe Valve 45.60 58.60 86.90 <br /> Butterfly Valve - 7J5 11.50 <br /> Tee-Fiow l"hru X = <br /> Tee-Branch Flow X = NOTE:Equivalent tength vatues for PVC pipe <br /> Swing Check Valve X _ Fittings are based on caltutations using the Hazen- <br /> Williams Equation. See Advanced Designs for SSTS <br /> Angte Valve X = for equa[ion. Other pipe material may require <br /> Globe Vatve X = different equivalent length factors. Yerify other <br /> equivalent length factors with pipe material <br /> Buttertly Vatve X = manufacturer. <br /> Vatve 10 X = NOTE:System instatler should contact system <br /> Valve 11 X _ designer if the number of fittings varies from the <br /> desiQn to the actual installation. <br /> A. Sum of Equivatent Length due to pipe fittings: C�ft <br /> Hazen-Wiltiams Equation for h <br /> B. Tota1 Pipe Length =Supply Pipe Length(5.6)+Equivalent Pipe Length (9.A.j 1 0.5 <br /> C� ft + � ft =�ft h.f = Da_s� ��Q-C)i.ss x�L <br /> C. Hazen-Williams friction loss due to pipe fittings and suppty pipe(hf): Q in gpm L in feet D in inches C=130 <br /> (10.5 = Pipe Diameter"�87) X ( Ftow Rate : Constant)'�� X Total Pipe Length (1d.6) <br /> (10.5 : ��ina'$�) X (L____�gpm�130},.ss X ��ft =�ft <br /> 11• Total Head requirement is the sum of the E(evation Difference (Line 3),the Distribution Head Loss(Line 4),Additional Head Loss(Line 5), <br /> and either Supply Friction Loss(Line 9),or Fnction Loss from the Suppty Pipe and Pipe Fittings for coltection systems(Line 10.Cj <br /> NOFE:Suppty Friction Loss(Line 8)need ONlY be used if NOT a cotlection system. <br /> NOTE:Friction Loss from the Suppiy Pipe and Pipe Fittings(Line 4.C)need ONLY be used if sysrem is a collection system. <br /> 9.0 ft + 5.0 ft + ��ft + 0.1 ft = 94.1 ft <br /> 3. PUMP SELECTION <br /> A pump must be selected to deliver at least 9 GPM(Line 1 or Line 2)with at teast �5 feet of total head. <br /> Comments: Pump type <br /> i hereby certify that I have completed this work in accordance with all applicable ordinances,rules and laws. <br /> � <br /> Joseph J Olson �----�_l- 810 12/08/10 <br /> (Designer) ��-'� (Signature) (License#) (Date) <br />