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� OSTP Pump Selection Design . <br /> LINIVERSITY ;��, .' <br /> Minnesota Pollution Worksheet OF MINNESOTA �"'� ` - <br /> Control A enc � 1 1"Y <br /> 10, Equivalent length of pipe fittings. Equivalent Length Factors (ft.)for PVC Pipe <br /> Fittings <br /> Section 10 is for Col(ection Systems ONLY ond does NOT need to be ' <br /> I Pipe Diameter(in.) <br /> completed for individual subsurface sewage treatment systems. ; Fitting Type �,� 2 3 <br /> Quantity X Equivalent Length Factor=Equivalent Length ' Gate valve i.o7 1.38 2.oa <br /> 90 Deg Elbow 4.03 5.17 7.67 <br /> Fitting Type Quantity Equivalent Equivalent 45 Deg Elbow 2.t5 2.76 4.09 <br /> Length Factor Length(ft) Tee-Flow Thru 2.68 3.45 5.11 <br /> Tee-Branch ftow 8.05 10.30 15.30 <br /> Gate Valve X - Swing Check Valve 13.40 17.20 25.50 <br /> 90 Deg Etbow X = Angle vatve 20.10 25.80 38.40 <br /> ; Globe Vatve 45.60 58.60 86.90 <br /> 45 Deg Elbow X - Butterfly valve - 7.75 11.50 <br /> Tee-Flow Thru X = <br /> Tee-Branch Flow X = NOTE: Equivalent length values for PVC pipe <br /> fittings are based on calculations using the Hazen- <br /> Swing Check Valve X - Williams Equation. See Advanced Designs for SSfS <br /> Angte Valve X = for equation. Other pipe material may require <br /> Globe Valve X = different equivalent length factors. Verify other <br /> equivalent length factors with pipe material <br /> Butterfly Valve X = manufadurer. <br /> Valve 10 X = NOTE: System insta(ter 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 Equivalent Length due to pipe fittings: �ft <br /> Hazen-Williams Equation for h <br /> B. Tota(Pipe Length =Supply Pipe Length (5.6)+Equivatent Pipe Length (9.A.) 1� j <br /> /1 = x ��_�11.55 :� � <br /> � ft + � ft = �ft I �a.S7 � <br /> C, Hazen-Williams friction loss due to pipe fittings and supply pipe(h�): Q in gpm L in feet D in inches C= 130 <br /> (10.5 .- Pipe Diameter'�e�) X ( Ftow Rate : Constant)'�85 X Total Pipe Length (10.6) <br /> (10.5 : �ina.8� � X (�9Pm=130)�.es X �ft =�ft <br /> 11. Toto(Head requirement is the sum of the E(evation Difference (Line 3),the Distribution Head Loss(Line 4),Additionat Head Loss(Line 5), <br /> and either Supply Friction Loss(Line 9),or Friction Loss from the Supply Pipe and Pipe Fittings for collection systems(Line 10.C) <br /> NOTE:Supp(y Friction Loss(Line 8)need ONLY be used if NOT a collection system. <br /> NOTE:Friction Loss from the Supply Pipe and Pipe Fittings(Line 9.C)need ONLY be used if system is a col(ection system. <br /> 7.0 ft * 5.0 ft + �ft + 1.1 ft = 13.1 tt <br /> 3. PUMP SELECTION <br /> A pump must be selected to deliver at least 38 GPM(Line 1 or Line 2)with at least 14 feet of total head. <br /> Comments: Pump type <br />