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. j <br /> .�.,_ OSTP Pump Selection Design �:� <br /> UNIVERSITY g�'`�` ` <br /> Minnesota Potlution Worksheet OF MINNESOTA <br /> Control A enc "=�� <br /> 10. Equivatent length of pipe fit[ings. Eqwivalent LenEth Factors(ft.)for PVC Pipe <br /> Fittings <br /> Section 10 is for Co(lection Systems ONLY and does NOT rteed to be pipe niameter(in.) <br /> comp(eted for individua(subsurface sewage treatment systems. I Fitting Type �� 2 3 <br /> Quantity X Equivalent Length Factor=Equivalent Length i Gate vatve �.0� 1.38 2.oa <br /> 90 Deq Elbow 4.03 5.17 7.67 <br /> Fitting Type Quantity Equivalent Equivalent i 45 Deg Elbav 2.15 2J6 4.09 <br /> Length Fador Length(ft) Tee-FtowThru 2.68 3.a5 5.11 <br /> i Tee-Branc i ow 1030 15.30 <br /> Gate Valve X ` i Swinq Check Valve 13.40 17.20 25.50 <br /> 90 Deg Elbow X = ' Angte Valve 20.10 25.80 38.a0 <br /> � GlobeValve 45.60 58.60 86.90 <br /> i 45 Deg Elbow x a eutterfty valve - 7J5 1i.50 <br /> I Tee-Flow Thru X = <br /> � Tee-Branch Flow X = NOTE:Equivatent length values for PVC pipe <br /> Swing Check Valve X fittings are based on calculations using the Hazen- <br /> - Wil6fams Equation. See Advanced Designs for SSTS <br /> Mgle Vatve X = for equation. Other pipe materiat may require <br /> Globe Valve x _ different equivalent length factors. Verify other <br /> eyuivalent length factors with pipe material <br /> Butterfty Valve X = manufacturer. <br /> Valve 10 X = N�TE:System installer should contact system <br /> Valve 11 X � designer if the numbe�of fittings varies from the <br /> desiQn to the adual installation. <br /> A. Sum of Equivalent Length due to pipe fittings: �ft <br /> Hazen-Williams Equation for h <br /> B. Totaf Pipe Length a Supply Pipe Length(5.8)+Equivalent Pipe Length(9.A.) 1�.5 <br /> Qfc `0 rt - �n hf = ��.57 '` (�=G)t.s� �L <br /> C, Hazen-Williams friction loss due to pipe fittinvs and supply pipe(h�): Q in gpm L in feet D in inches C-130 <br /> (10.5 .- Pipe Diamecer`�67) X ( Flow Rate a Constant)''°5 X Total Pipe Length(10.6) <br /> (10.5 � �in4.a�� X (C�9Pm�130j,.a� X �ft =�ft <br /> 11• Totaf Head requirement is the sum of the Elevation DifJerence (L1ne 3),the Distribution Head Loss(Line 4),Additional Head Loss(Line 5), <br /> and either Supply Friction Loss(Line 9),ar Friction Loss from the Suppty Pipe and Pipe Fittings for collection systems(Line 10.C) <br /> NOTE:Supply Friction Loss(Lirte 8)need ONLY be used if NOT a co(lettion system. <br /> NOTE:Friction Loss from the Supply Pipe and PiPe Fittings(Line 9.C)creed ONLY be used if rystem is a collection system. <br /> 7.Q ft + 5.0 ft + �ft + 1.2 ft - 13Z ft <br /> 3. PUMP SELECTION <br /> A pump must be selected to deliver at least 3(j GPM(Line 1 or Line 2)with at least �4 feet of totat head. <br /> Comments: Pump type <br /> I hereby certify that I have completed this work in accorciance with ali applipble ordinances,rules and laws. <br /> ���.,,.�.....,�.�.... <br /> Joseph J Olson 810 02l11/11 <br /> (Designer) (Signature) (License#) (Date) <br />