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OSTP Pump Selection Design - , <br /> UNIVERSITY ,.,` <br /> MtPollution <br /> Worksheet OF MINNESOTA 0./77. -.=,-,L.:;1Contof Agency , ,: <br /> 10. Equivalent length of pipe fittings. Equivalent Length Factors(ft.)for PVC Pipe <br /> Fittings <br /> Section 10 is for Collection Systems ONLY and does NOT need to be <br /> completed for individual subsurface sewage treatment systems. Fitting Type Pipe Diameter(in.) <br /> 1Yz 2 3 <br /> Quantity X Equivalent Length Factor=Equivalent Length Gate Valve 1.07 1.38 2.04 <br /> 90 Deg Elbow 4.03 5.17 7.67 <br /> Fitting Type Quantity Equivalent Equivalent 45 Deg Elbow 2.15 2.76 4.09 <br /> Length Factor Length (ft) Tee-Flow Thru 2.68 3.45 5.11 <br /> Tee-Branch Flow 8.05 10.30 15.30 <br /> Gate Valve X = Swing Check Valve 13.40 17.20 25.50 <br /> 90 Deg Elbow X = Angle Valve 20.10 25.80 38.40 <br /> Globe Valve 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 SSTS <br /> Angle 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 = manufacturer. <br /> Valve 10 X = NOTE:System installer should contact system <br /> designer if the number of fittings varies from the <br /> Valve 11 X = design to the actual installation. <br /> A. Sum of Equivalent Length due to pipe fittings: ft <br /> Hazen-Williams Equation for h <br /> B. Total Pipe Length =Supply Pipe Length (5.B) +Equivalent Pipe Length (9.A.) 10.5 ( <br /> ft + ft = ft hf D4.87 x�\Q_01.85 ,gL <br /> C. Hazen-Williams friction loss due to pipe fittings and supply pipe(hf): Qin gpm L in feet Din inches C= 130 <br /> (10.5 Pipe Diameter4•87) X ( Flow Rate : Constant)1•85 X Total Pipe Length (10.B) <br /> (10.5 : in4.87 ) X ( gpm=130)'.85 X ft = ft <br /> 11. Total Head requirement is the sum of the Elevation Difference (Line 3),the Distribution Head Loss(Line 4),Additional 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:Supply 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 collection system. <br /> 9.0 ft + 5.0 ft + ft + 6.4 ft = 20.4 ft <br /> 3. PUMP SELECTION <br /> A pump must be selected to deliver at least 38 GPM(Line 1 or Line 2)with at least 21 feet of total head. <br /> Comments: Pump type <br /> I hereby certify that I have completed this work in accordan with all applicable ordinances,rules and laws. <br /> Joseph J Olson 810 11/09/10 <br /> (Designer) (Signature) (License#) (Date) <br />