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� � OSTP Pump Selection Design uN��ERs�TY <br /> Minnesota Pollution Worksheet OF MINNESOTA <br /> Control A e�c -�- <br /> 10. Equivalent tength of pipe fittings. Equivalent Length Factors(ft.)for PVC Pipe <br /> Fittings <br /> Section 10 is for Collection Systems ONLY and dces NOT need to be <br /> completed for individual subsurface sewage treatment systems. Fitting Type �Pe Diameter(in.) <br /> 1 Yz 2 3 <br /> Quantity X Equivalent Length Factor=Equivalent Length Gate vatve 1.07 1.38 2.oa <br /> 90 Deg Elbow 4.03 5.17 7.67 <br /> Equivalent Equivalent 45 Deg Elbow 2.15 2.76 4.09 <br /> Fitting Type Quantity Length Fador length (ft) Tee-Flow Thru 2.68 3.45 5.11 <br /> Tee-Branc F ow 8.05 10.30 15.30 <br /> Gate Valve X - Swing CheCk Ydlve 13.40 17.20 25.50 <br /> 90 Deg Etbow X = Angle vatve 20.70 25.80 38.40 <br /> Gtobe Valve 45.60 58.60 86.90 <br /> 45 Deg Elbow X - Butterfty Valve - 7J5 11.50 <br /> Tee-Ftow 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 - Witliams Equation. See Advanced Designs for SSTS <br /> Angle Valve X = for equation. Other pipe material may require <br /> Globe Vatve X = different equivalent length factors. Verify other <br /> equivatent tength factors with pipe material <br /> Butcerfly Valve X = manufacturer. <br /> Valve 10 X = NOTE: System insta(ler should contact system <br /> designer if the number of fittings varies from the <br /> Valve 11 X - desiQn to the actual installation. <br /> A. Sum of Equivatent Length due to pipe fittings: �ft <br /> Hazen-Williams Equation for h <br /> B. Total Prpe Length =Suppty Pipe Length (5.6)+Equivalent Pipe Length (9.A.) 1�.5 n <br /> � ft + � ft - �ft h.f D4.87 *�`� TC)1.85 �kL <br /> C, Hazen-Witliams friction loss due to pipe fittings and suppty pipe(h�): Q in gpm L in feet D in inches C= 130 <br /> (10.5 .- Pipe Diameter°�$') X ( Flow Rate = Constant)'�85 X Totat Pipe Length (10.6) <br /> (10.5 : �in4.s� � X (�9Pm=130),.as X �ft =�ft <br /> 11• Tota(Head requirement is the sum of the Elevation Difference (Line 3),the Distribution Head Loss(Line 4),Additionat Head Loss(Line 5), <br /> and either Supply Friction Loss(Line 9),or Friction Loss from the Supply Pipe and Pipe Fittings for co(lection systems(Line 10.C) <br /> NOTE:Supply Friction Loss(Line 8)need ONlY be used if NOT a collection system. <br /> NOTE:Friction toss from the Supp/y Pipe and Pipe Fittings(Line 9.C)need ONLY 6e used if system is a col(ection system. <br /> 9.0 h + 5.0 ft + �ft + 3.8 ft = 17.8 ft <br /> 3. PUMP SELECTION <br /> A pump must be selected to deliver at teast 29 GPM(Line 1 or Line 2)with at least �$ feet of total head. <br /> Comments: Pump type <br /> I hereby certify that I have compieted this work in accordance with all applicable ordinances,rules and laws. <br /> , <br /> Joseph J Olson � 810 04/16/10 <br /> (Designer) '-� . (Signature) (License#) (Date) <br />