Page 87 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Pump Best Practices     Best Practice 2 .12














                                                                   Fig 2.12.9   Recirculation flow pattern in impeller at low flows





















                                                                   Fig 2.12.10   Discharge recirculation flow pattern






              Fig 2.12.8   Flange to vane entrance losses

              liquid tangential velocity (VT) increase head (energy). The total
              pressure reduction from the suction flange to the impeller vanes
              is the result of:
                Friction losses in the flow passage                 Fig 2.12.11   Low flow temperature rise can cause vapor formation
                Liquid acceleration
                Entry shock losses at the impeller vane tips
                                                                           Pump head            1
                                                                    DT ¼                                  1
                Therefore, each pump has a distinct pressure drop for any  337; 100   C P  Pump efficiency
              given flow, which is the result of pump case, inlet volute and        Pump head          1
              impeller design. If the pressure drop from the suction flange to    DT ¼                            1
                                                                                    778   C P   Pump efficiency
              the impeller vane reduces the pressure below the liquid’s vapor
              pressure, vapor will be formed at the impeller vanes.
                There are also two (2) other causes of vapor formation within  Where:    Pump  head  is  calculated  from  data  in

              an impeller. Low flow velocities at any location within the im-  m-kgf  ft-lb f
              peller can cause separation of flow stream lines, and lead to low  kgM  lb M
              pressure areas (cells) inside the impeller. If the pressure within                  KJ       BTU
              these cells is less than the fluid’s vapor pressure, vapor will form  Cp is specific heat of the fluid in
                                                                                                  C   kg    F -LBmass
              (refer to Figures 2.12.9 and 2.12.10).                                        m-kgf
                The curvature of the impeller vanes will always result in  367,100 is conversion factor
              lower velocities on the pressure side of the vane (the side                     kJ
              that cannot be readily observed). Therefore, vaporization
                                                                                         FT   LB F
              caused by flow separation occurs on the pressure or ‘backside’  778 is conversion factor
              of the vane. This phenomenon is commonly known as                           BTU
              recirculation.                                         Pump efficiency is expressed as a decimal.
                Pump efficiency is low at low flows:                   If the temperature rise increases the fluid’s vapor pressure
                Liquid temperature rise increases by               above the surrounding pressure, the fluid will vaporize.

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