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QST� Pump Setec tion �7esign '�JNIVERSITY �� <br /> Mi�nesotaPollusion WQI��CSI�Ie�t OF MINNESOTA .. ._�'�`.�� <br /> Control A en _, <br /> v t1.05.31 <br /> ' 1. PUTAP GPAGRY <br /> p, pumpir�to Cravitp or Pte53uTe Dlstributi�on: O c�'a�tY �� Salectton requirod <br /> 1. If pumping to gravity enter the gallon Pe►minute of the pump: ��� <br /> 2, IS the pump for the veatment syscem or the collectton sYsiem: <br /> �TrmaosrcSrstem O f�nealmSV�n� Selection requi td fvr wwksFx�r.t to wv►k P►a'Pe'r�Y <br /> 3_ if pumpNtg to a pressurmed treatment 5�ystem,whs�Pert a�YP'e�f system: <br /> �)So1l Treatmer►t Umt Q Media Filter [a Other 4�.� �M <br /> 4. 1f pumping to a 4��d�no�rnon system: <br /> /UM iT of Pr�urr AkD'i6iR�ar LLr!0 of l�lon-LewV ar M[af 9J Catlecflan Systm) <br /> 2. HFJ1D REQUIREMENTS - -- <br /> oi s�mm <br /> �� •�� &polni oi dlsWigc <br /> 3. Elevation DifferEnce • <br /> d <br /> beCw�n P�mP arxf point oF discharge: �t��,� <br /> MOTE:!F'syst�m isun irrdividuvl St+h�wrface sewege creatmertC -- -- � <br /> yyg��,mmplete steps 4-9. tf system fs d Colfettfan 5f+st�, �k�v� 0 o�„m�;. <br /> 611xrnrn <br /> y�p�p�4,�,7 and 8 and go to Step t0. � <br /> _. _.. . . <br /> C ----._ ' . ... <br /> 4. Distribution Head Los� ��ft � ............................. .............• <br /> 5. ��l��. ��ft(due m specialequu�mern,etc.) ��Frietlon Lass in PlasNt Pipr per 100 ft <br /> pistribuHan Head l�ass (C=13Q) <br /> Gravlty Utstributio� = Oft Nomir►2►� �iPe�fameter <br /> Flow RatP � 1 Y, 112 2 3 <br /> P�essure D�stribution based o��Minimum average Nead <br /> Value on Pressure�7lstribution Woricsheet= 10 9.17 3.08 '1.2T 0.31 <br /> Minimum Avere e Nead Oi?rtributian Head Las s 12 12.T1 4.31 1.78 O.d4 - <br /> 1 ft 5 ft 14 16.99 5.74 �.36 0.58 -- <br /> 2ft 6ft <br /> Sft 10ft �6 -- 7,3b 3_03 0.76 O.tO <br /> ys -- s_ia a.�s o_as o.+� <br /> 6. A.St�pplY PiPe Diameter: 2.0 �in 20 •.- 1 t.11 4.68 1.t3 0.16 <br /> 25 -- 16.79 6.92 1.71 0.74 <br /> B•rx1PP{r p��►�6�; 6Q �ft 30 9.65 2.38 0.33 <br /> 7 g��F���S t�t PI�t1c P[pt per 100ft fram Table I: �5 -- - i2.90 3_18 0-4d <br /> 40 -- - 16.52 4.07 0.67 <br /> Fr�a�on�oss= 4.62 n�er�oofi af p�oe 45 --- - -- s.o� o.�o <br /> �. Oeteimine Equlvalent Plpe Length from Fxrr�disctiarge t0 soli dlsp!rsai 50 ... .-- ..- 6.16 0.$6 <br /> area dsCharQe point. Estknate 4Y adding 25%ta AcPP�Y�p��h for 55 -- -- --- 7.35 i.4�' <br /> fi[t�nB� �P�Y��►'3�(6.8) X 1.?S=Equivolent Pipe Leny th 6Q --- --- -- 8_63 1.20 <br /> 6 5 --- --- --- 10.01 1.39 <br /> 60 R X 1.25 - 75.0 ft �0 --- -- -- 11.48 9.80 <br /> 4. C81�ulate SupplY�r9cNan loss by multiplying FMctlan lats Fer f00f (Line 6}by the Equ�vafent Pipe lmgth (Li��and dtvide by 100. <br /> S�+�P�Y Fnctbn loss= <br /> 4.b2 r��er�aort X 75.0 tc * too = 3,5 fc <br /> � � �1 <br />