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lM�r[�sRYoflLxr[aam - <br /> Pump Selection Design �� � <br /> Minnesota Pollution Worksheet :� . : : ������� ` <br /> Control A enc -� <br /> Equivalent Len�th Factors(fL.)for PVC Pipe <br /> 10. Equivalent length of pipe fittings. Fittin�s <br /> Section 9 is for Coliection Systems ONLY ond does NOT need to be Pipe Diameter(i�.) <br /> comp/eted for individual subsurface sewage treatment systems. Fitxing Type �� Z 3 <br /> Quanity X Equivalent Length Factor=Equivalent Length Gate Valve �.07 1.38 2.04 <br /> 90 Deg Elbow 4.03 5.17 7.67 <br /> 45 Deg Elbow 2.15 2J6 4.09 <br /> Fitting Type Quantity Equivalent Equivalent Tee-Flow Thru 2.68 3.45 5.11 <br /> Length Fador Length (ft) �-Branc ow . 5 15.30 <br /> X Swing Check Vatve 13,40 17.20 25.50 <br /> Gate Valve - Angte valve 20.10 25.80 38.40 <br /> 90 Deg Elbow X = Globe Valve 45-60 58.60 86.90 <br /> Butterfly Valve 7.75 11.50 <br /> 45 Deg Elbow X = <br /> Tee-Ftow Thru X - <br /> Tee-Branch Flow X ' NOTE: Equivalent length values for PVC pipe <br /> Swin Check Valve fittings are based on calculations using the Hazen- <br /> � X Witliams Equation. See Advanced Designs for 5Sf5 <br /> Mgle Vatve X = for equation. Other pipe material may require <br /> different equivatent length fadors. Verify other <br /> Globe Valve X - equivalent length factors with pipe material <br /> X _ manufacturer. <br /> Butterfly Valve - <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 /> B. Totol Pipe Length =Supply Pipe Length(5.B)+Equivalent Pipe Length (9.A.) Hazen-Williams Equation for h <br /> � ft ` �� fc = ��ft L _ 10.5 * L *�Q=C)i.gsa Qin gpm <br /> �l.r 4.8b55 L in feet <br /> C. Hazen-Williams friction loss due to pipe fittings and suppty pipe(h): D D in inches <br /> 10.5 X Total Pipe Length (9.6) X (Ftow Rate �Constant)''� = Pipe Diameter'�B6ss <br /> 10.5 X �ft X (��gpm + 130),esz t ��fta.aess _ ��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 Fridion Loss from the Supply Pipe and Pipe Fittings for collection systems(Line 10.C) <br /> NOTE:Supply Friction toss(Line 8)need ONLY be used if NOT n collection system. <br /> NOTE:Friction Loss from the Suppty Pipe and Pipe Fittings(Line 9.C)need ONLY be used if system is a coliection system. <br /> 15.0 ft + 5.0 ft + �ft + 2.6 ft = 22.6 fc <br /> 3. PUMP SELECTION <br /> A pump must be selected to deliver at least 36 GPM(Line 1 or Line 2)with at least 23 feet of total head. <br /> I hereby certify that I have completed this work in accordance with all applicable ordinances,rules and laws. <br /> Joseph J Olson 810 11/04l09 <br /> (Designer) (Signature) (License#) (Date) <br />