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� OSTP Pump Selection Design <br /> �� UNIVERSITY � <br /> YViinnesota Pollution Worksheet OF MINNESOTA <br /> Control A enc � <br /> 10. Equivalent length of pipe fittings. Equivalent Len�kh 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 sewoge treatment systems. Fitting Type �Fe Diameter(in.) <br /> 1 Y4 2 3 <br /> Quantity X Equivatent Length Factor=Equivalent Length Gate Valve 1.07 7.38 2.oa <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 /> ee- ranc ow . <br /> Gate Valve X - Swing Check Valve 13.40 77.20 25.50 <br /> 90 Deg Elbow X = Angle Valve 20.10 25.80 38.40 <br /> 45 Deg Elbow X _ Glabe Yatve 45.60 58.60 86.90 <br /> 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 calcutations 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 /> Butterfty 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 Equivatent Length due to pipe fittings: �ft <br /> Hazen-Wiliiams Equation for h <br /> B. Tota(Pipe Length =Supply Pipe Length(5.B)+Equivalent Pipe Length (9.A.) l�.s <br /> 1 85 <br /> 0 ft + C� ft - Ofc h.f - D4.s� *�Q-C) � *L <br /> C, Hazen-Williams friction loss due to pipe fittings and supply pipe(h f): Q in gpm L in feet D in inches C= 130 <br /> (10.5 .- Pipe Diameter°�a�) X ( Flow Rate : Constant)'�85 X Total Pipe Length(10.6) <br /> (10.5 : �ina.s� � X (�9pm>130),.es X �ft '�ft .. <br /> 11. Tota(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 Suppty 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 /> 10.0 ft + 5.0 ft + 0.0 ft + 1.7 ft = 16.7 ft <br /> 3. PUMP SELECTION <br /> A pump must be selected to deliver at least 36 GPM(Line 1 or Line 2)with at least �] 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 /> (Designer) (Signature) (License ti) (Date) <br />