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. OSTP Pump Selection Desi�n --�. . <br /> UNIVERSITY � �`,�, �} <br /> Mi�so�ta� Pollution W��'�($heE,at OF IVIINNESOTA '�`��� <br /> 10. Equiralent length of pipe fittings. Equivalent Len�th Factors(ft.)for PVC Pips <br /> Sectian f0 is Jor Cdlection Systems ONLY and does NOT need to be Fittin�s <br /> completed far individtio!subsurfoce sewage treaGrt/snt systems. F��� ' �P����r(ie.)3 <br /> Quantity X Equivalent Length Factor=Equivalent Length Gate valve 1.07 1.38 2.04 <br /> 90 Deg Eibow 4.03 5.17 7.67 <br /> Fitting Type Quantity �E�h�r Equival°nt 45 Deq Elbow 2.15 2.76 4.09 <br /> Len$th(ft) Tee-Flaw Thru 2.68 3.45 5.11 <br /> ee- ranc ow <br /> Gate Valve X � Swtng Check Vatve 13.40 17.20 25.50 <br /> 90 Deg Etbow X = Angte valv�e 20.10 25.80 3g.qp <br /> 45 Deg Elbow X � Globe Valve 45.60 58.60 86.90 <br /> ButOerfly Valv�e - 7.75 11.50 <br /> Tee-Flow Thru X a <br /> Tee-Branch Flow X = NOTE:Equivalent length val�s for PVC pipe <br /> Swing Check Vatve X = fittings are based on calculations�aing the Hazen- <br /> Wiltiams Equation. See Advanced Designs for SSTS <br /> Angle Valve X = for equation. Other pipe materiat may require <br /> Gtobe Valve X a different equivalent length factors. Verify other <br /> equivalent length fadors with pipe material <br /> Butterfly Valve X = manufacturer. <br /> Valve 10 X = NOTE:System instalter sFwuld contact system <br /> Valve 11 X � desiSner if the numbe�of fittings varies from the <br /> desiqn to the actual irutallation. <br /> A. S�n of Equivalent Length due to pfpe fittiogs: C�ft <br /> Hazen-Williams Equation for h <br /> B. Total Plpe LenSth =SupptY�Pe�3�(5.B)+Equivatent Pipe Length(9.A) 1�.5 <br /> �^� y� - ��Q_���_ss �:L <br /> �� ft `�� ft a L�Jft I D4.87 <br /> C. Hazen-Williams fricti�loss d�to pipe fittings and wpply pipe(hr)� Q in gpm L in feet D in inches C=130 <br /> (10.5 + Pipe piameter'-�) X ( Flow Rate $ Constant)�'85 X Total Pipe Length(10.6) <br /> (10.5 + ��ina.s�� X ��9Pr►►+130),.as X 1._�ft =�ft <br /> �1• Tota(Head requirement is the sum of the Elewotion Difference (Line 3),the Distribution Head Loss(line 4),Additional Head Loss(line 5), <br /> and efther Supply Friction Loss(Line 9),or Fridion Loss from the Supp(y Pipe and Pipe Fitti�gs for coltection systems(Line 10.C) <br /> NOTE:S�p/y Friction Lo�ss(Line 8)need ONLY be�ed if NOT a col(ection systern. <br /> NOTE:Friction L�s from the S�ply p;pe Qr�d p�pe Fittings(Line 9.C)need ONLY be used if system is a col(ection system. <br /> 16.0 ft + 5.0 ft + ��ft + 3.4 ft m 24.4 ft <br /> 3. PUMP SELECTION <br /> A P�P must be setected to dHiver at least 29 GPM(Line t or Line 2)with at least 25 feet of total head. <br /> Comme�ts: PumP tYPe <br /> �hereby certify thffi I have c�mpleted this work in accoManoe with aN applicable or�inanc�,rules and laws. <br /> '����SOp 810 05/11 H 0 <br /> (�5�) (Sigrwture) (License!1) (Date <br /> ) <br />