Page 130 - Water and wastewater engineering
P. 130

INTAKE STRUCTURES 3-27

              Pumps are selected from those commonly available from pump manufacturers. This then
          becomes a problem of matching a  pump characteristic  or  head-discharge  curve from a pump
          manufacturer’s catalog or database to the system head curve.
               A typical, constant speed, vertical turbine curve is shown in  Figure 3-17 . Important features
          of the curve to be noted are:

                •  The head delivered (ordinate) is  per stage.  Thus, for higher heads than noted, multiple
               stages are identified in the selection of the pump.

               •  The maximum number of stages that may be used is specified.
               •  The  best efficiency point  (BEP) is a function of the flow rate and the head.
               •  The required net positive suction head (NPSH  R  ) may be specified  per stage  or as a total for
               the maximum number of stages. Typically, it is only critical for the first stage.
               •  Multiple impeller sizes allow some adjustment over the range of capacity and head.

                   Radial loads on the impeller and problems with cavitation are minimized when the pump is
          operated at its BEP. Although it is not possible to operate at the BEP all the time, there is a range
          of operating conditions that is preferred to optimize the life of the pump. The American National



           Curve no. 3-18
           Size 1                Rpm 1750
           Single-stage lab head and horse-power with
           enameled cast iron bowls and bronze impeller
           Effieciency shown for 2 or more stages                       A   32 cm
            No.  Eff.              Eff.                                 B   31 cm
           stages  change  Material  change  4.0
            1    1   Imp.-C.I.      0       3.0
            2    0   Imp.-C.I. Enn  0     Head per stage, m  2.0  A
            3    0   Bowl-C.I.      1
            4    0   Bowl-Brz.      1       1.0             B
           Eye area   32 cm
           Thurst constang - A   2.3                                           2
           Thurst constang - B   2.3
           Thurst constang - C   2.3           NPSH required
                                                                               1  NPSH required  at pump inlet, m
           Max. no. std. stages   35        80                                 0
           Max. operating pressure    3,900 kPa
           Std. lateral   0.375
           Std. shaft dia.  2.0 cm          60
           Impeller number   P-2397-10                       A
           Impeller wt.   25.0 kg
           Bowl conn. - flanged           Efficiency, %  40
           Add 37 cm per additional stage
           Enclosed line shaft              20
                      72 cm
                                             0   100  200  300  400
                                    35 cm          Discharge, m /h
                                                           3



          FIGURE 3-17
           Typical vertical head-discharge curve.
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