Page 111 - Know and Understand Centrifugal Pumps
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Know and Understand Centrifugal Pumps

          4.  Hf - friction head  is  the friction  losses in the system expressed in
             feet  of  head.  The  Hf is  the  measure  of  the  friction  between  the
             pumped  liquid  and  the  internal  walls  of  the  pipe,  valves,
             connections  and  accessories  in  the  suction  and  discharge  piping.
             Because  the  Hv  and  the  Hf are  energies  lost  in  the  system,  this
             energy  would  never  reach  the  final  point  where  it  is  needed.
             Therefore these heads must be calculated and added to the pump at
             the moment of design and specification. Also it’s necessary to know
             these values,  especially when  they’re significant, at the moment of
             analyzing  a  problem  in  the  pump.  The  Hf  and  the  Hv  can  be
             measured with pressure gauges in an existing system (see the Bachus
             & Custodio  formula  in  this  chapter). If the system is  in  planning
             and design stage and does not physically exist, the Hf and Hv can
             be estimated with  pipe  friction  tables  (ahead in this chapter). The
             Hf formula for pipe is:

                    Kfx L
             Hf  =   ~
                      100

             where:  Kf = friction constant for every 100 fi of pipe derived from
             tables  L = actual length of pipe in the system measured in feet.

          The Hf formula for valves and fittings is:
          Hf  =KxHv

                                                                  V2
          where: K = friction constant derived from tables, and Hv = -
                                                                  44
          The sum of these four heads is called the total dynamic head, TDH.



          TDH = HS + Hp + Hf + Hv
          The reason that we use the term ‘dynamic’ is because when the system
          and  the  pump  is  running,  the  elevations,  pressures,  velocities,  and
          friction losses begin to change. In other words, they’re dynamic.





              When the system is designed, the engineer tries to find a pump that‘s  BEP is equal to   I
              or  close  to the system’s TDH  (the system’s TDH E BEP of the  pump).  But once  the
        I     static BEP.
              pump is started,  the system  becomes very dynamic,  leaving  the  poor pump with  a






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