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tn <br /> HELD LOSS DUE TO PIPE FRICTION DATE: <br /> PROJECT <br /> IPE SIZE (inches): .-...--- _ PE SIZE(InChes}: <br /> ---�-� - --- <br /> LENGTH OF PIPE Rf LENGTH OF PIPE <br /> ------------------- or <br /> FLO (gp } <br /> FLOW �m <br /> {gp } <br /> TYPE OF PIPE(DIP,PVC): Ch= 100 TYPE OF PIPE(DIP,PVC); Ch= 13D <br /> FRICTION HEAD LOSS 1.97ft FRICTION HEAD LOSS 7.10ft w <br /> VELOCITY 5.104 <br /> VELOCITY 5.104 A.a <br /> STATIC HEAD {" <br /> MINOR HEAD LOSSES <br /> Formula's <br /> FITTING Material #USED Le Material #USEQ Le <br /> GAT>;i PLUG VALVE{open} DIP 2.00 PVC hl=L=(C91,32*A'0h"R"0.63)^1.852 <br /> BALL VALVE(open) DIP PVC <br /> SWING l CHECK VALVE(open} DIP 22.50 PVC Le-K*D 1 Ft <br /> BUTTERFLY VALVE(open) DIP PVC <br /> GLOBE VALVE(open) DIP - - - PVC A=PI DA2 f 4 <br /> ANGLE VALVE(open) DIP PVC <br /> 90 deg. ELBOW(STANDARD) DIP 14.00 PVC <br /> 90 deg. ELBOW(LONG) DIP PVC <br /> 45 deg.ELBO DIP 5.33 PVC 5.33 f <br /> STANDARD TEE(RUN) DIP 4.47 PVC <br /> �1ANUAKU ILt[bKf'kIYUH) UIl- Laiwagom "ku-00 I rdV <br /> OTHER KNOWN LOSSES DIP I PVC <br /> EQUIVALENT LENGTH 54.83 1 5.33 <br /> HEAD Lass 5.73#t <br /> TOTAL DYNAMIC HEAD 26.81ft <br /> 4 <br /> n <br />