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t , , , <br /> �. , �t � . <br /> • I <br />. Debamiae pom�caPadtT . . <br /> Mi�imum,sugge�trd ts 600 gallo�+s per hour(10 gpa��o seay ahead of . <br /> wa�oer usa:ace. <br /> �m�mn w�eoed for�div�ery to a d:op booc oE a hoeee syseem is Z.?00 <br /> g�Ilo�s Per ho�a t�gpat)eo prav�t bus7d-ap oE pnmaae ia�+op booc. ; <br /> U�e valae fro�dnign oF peman�d��ribudon sy�mti , <br /> SELELTED PtJll�CAl'ACl'YY�SPm ►"��'x . �P�+N� <br /> P�a�ut ot D� <br />.�hpd jtqs�mbt � . 1 I 4.s' <br /> Eirysda�di�a�oe betMre��aod ponu of di�rge. �.v.�os Di�s <br /> �eet <br />, If pumping m�p�n�e d3sdsbuaan sqs�n.add$ve feet fot pee�uz �'� <br /> � ' .. �-tsb <br /> ��^� 13 indt t0 iaeh 3.0 iael� <br />� ��b� � hisi�l��100RdpM <br /> a. Eaber ftiction b's tabk urith Epm and pipe diaa�e�et. <br /> Ite�d hiCtlOtf�in feet pet 100 feet irOm p�ge R18. 10 0.69 0.2D- <br /> F.L=3,,a_fL/100 ft of pipe �''o►a . •i4 %� o�.3s <br /> : b. Debernrine tOtal(7ipe 1Qngtlt fronl pan�p tD disCttaTg! 16 1.63 0.48 <br /> po;n� pdd 25 peroa,t to pipe ia+gth for stting �a zo3 0.60 <br /> loss.Ot tme s 8tttag 1C�s Chsrt F.Qnivalatt P1P� ?S 3.13 1.11 Q.16 <br /> lengdt-1.?5 t�es PiPe length� 30 J.23 1.SS 0.23 <br /> 'i�x 1.ZSs �_�fee! 35 'f.90 206 0.30 <br /> c. Calcnla�e total fr�ticn lass by multiplying � 1�3 3.�Za as <br /> fric�ion lass in h/1001t bY���PiP��8'� So - -- 3.99 o.S8 <br /> TOlil friCffOn lO�s i ?�=_x 1_f�=100•_�fe!! 33 • 4.76 0.70 <br /> 4. Total hesd required 3s the sum of elevation diff�aence, . � 60 5.60 0.82 �. <br /> speciai hdd tequirea�astr.and total frictfon loss. <br /> P �"=-'f= <br /> . . (� � �� <br /> TOTAI.I�F1lD �_feet . . <br />• seiecKon <br />~A pump muat b�xlecsed taddivet at kast�gpm tSEe�t�with at least �� <br /> �feet of totai 11ad(Sbep 8�. ' m+M••m s� r,.ow: �a�u.�ous �a oa► <br /> �a�ae rti.c ar �csiocMcs <br /> , t a � rs <br />). Toql Pna+poat Volume - : �oe m �.o .o,r, <br /> l. To nu�omi�e pump IiEe xkct sump si�e for 4 to 5 P�P aP��PQ�Y• � : .00 ;�; =n: � <br /> �� <br /> `.�8Pd♦4� � �`� 8sllo�u Pet d�e 's e's si� � '��' <br />! GkulaEe dsainbaClc s �aso �oo sro � <br /> l. De�tu tOtal P�Pe�6��� • tsoo sr� +a� c.�..n <br /> 2. De�ermine liquid wlua+e of pip�_,�,g�llons per 100 ieet. (ue page RIS) F I$a <br /> 3. Multiply I���wh�e�badc�titY�+� m.n�aer c.no�-4 �ao rea <br />'S�ud draiab�elc q�►is 10 pa+o�rt oE pnatp�d qusatih►. A lae��e dr�dc 1.25 . 7.77_ <br />�eesnts�wiU d�pump�ation d�d�ncy�iiBhttY�P�P�S� ao�es ars <br />,��y��y�u���.e«� n�o�a�►�. ' 1.5 10.58 <br /> 2 17.43 <br /> 3. Tota!pump out wlume eqnals dox volwme sdrainbacic' To��� � ' 24.$7 <br /> ,���gaito�'per d°'e+-�3-gall°'�s 3 38.4 <br /> 4 66.1 • <br />