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HYDRAULICS AND WATERWORKS FORMULAS        341

             where    H   total dynamic head, m (ft)
                        t
                   H (H )   discharge (suction) head measured at discharge (suction) nozzle
                    d  S
                          of pump referenced to the centerline of the pump impeller, m (ft)
                   V (V )   velocity in discharge (suction) nozzle, m/s (ft/s)
                    d  s
                                                            2
                                                     2
                       g   acceleration due to gravity, 9.81 m/s (32.2 ft/s )
                    h (h )   static discharge (suction) head, m (ft)
                    d  s
                   h (h )   frictional head loss in discharge (suction) piping, m (ft)
                    fd  fg
                  h  (h )   minor fitting and valve losses in discharge (suction) piping
                   md  ms
                          system, m (ft). Entrance loss is included in computing the
                          minor losses in the suction piping.
               The reference datum for writing Eq. (12.146) is taken as the elevation of the
             centerline of the pump impeller. In accordance with the standards of the
             Hydraulic Institute, distances (heads) above datum are considered positive; dis-
             tances below datum are considered negative.
               In terms of the static head, Eq. (12.146) can be written as
                                                         2
                                                        V d
                         H t   H stat   h fs  
h ms   h fd  
h md    (12.149)
                                                        2g
             where  H   total dynamic head, m (ft)
                    t
                  H stat    total static head, m (ft)
                       h – h s
                        d
                                                  2
             In Eq. (12.149), the energy in the velocity head V d  2g  is usually considered to
             be lost at the outlet of the piping system. In practice, this loss of energy is taken
             as being equivalent to the exit loss and is included as a minor loss.
               The energy (Bernoulli’s) equation can also be applied to determine the total
             dynamic head on the pump. The energy equation written between the suction
             and discharge nozzle of the pump is
                                      2             2
                           H t    P d     V d    z d    P s     V s    z s  (12.150)
                                    2g             2g
             where   H   total dynamic head, m (ft)
                      t
                                                      2
                                                           2
                  P (P )   discharge (suction) gage pressure, kN/m (lb /ft )
                                                         f
                      s
                   d
                                                    3
                                               3
                         specific weight of water, N/m (lb /ft )
                                                  f
                  V (V )   velocity in discharge (suction) nozzle, m/s (ft/s)
                   d
                      s
                                                           2
                                                   2
                      g   acceleration due to gravity, 9.81 m/s (32.2 ft/s )
                   z (z )   elevation of zero of discharge (suction) gage above datum, m (ft)
                      s
                   d
             Head losses within the pump are incorporated in the total dynamic head term in
             Eq. (12.150).
             Pump Efficiency and Power Input
             Pump performance is measured in terms of the capacity that a pump can dis-
             charge against a given head and at a given efficiency. The pump capacity is a
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