Page 169 - Chemical Process Equipment - Selection and Design
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7.4. CRITERIA  FOR  SELECTION  OF PUMPS  141

                                                               identifies impeller and case size and other details which are stated in
                                                               a  catalog.  Each  combination  of  head  and  capacity will  have  an
                                                          i    efficiency  near  the  maximum  of  that  style.  Although  centrifugal
                                         GPM                   pumps  function over  a  wide  range  of  pressure  and  $~QW rates,  as
                                                               represented  by  characteristic curves like  those  of  Figures 7.2  and
                                                               7.7, they are often characterized by  their performance ab  the peak
                                                               efficiency,  as  stated  in  the  previous  section.  Approximate
                                                               efficiencies of  centrifugal pumps as functions of  head  and capacity
                                                               are on Figure 7.11 and elsewhere here.
                                                                  Centrifugal pumps have a number of good qualities:

                                                               1. They are simple in construction, are inexpensive. are available in
                                                                 a large variety of  materials, and have low maintenance cost.
                                                               2.  They operate at high speed so that they can be driven directly by
                                                                 electrical motors.
                                                               3.  They give steady delivery, can handle slurHies and take up little
               20          100            200            300     floor space.
                             HEAD,  FEET  OF  LIOUID
                                                               Some of  their drawbacks are
           Figure 7.11. Approximate efficiencies of  centrifugal pumps in terms
           of  GPM and head in feet of  liquid.
                                                               4.  Single stage pumps cannot develop high pressures except at very
                                                                 high speeds (10,000 rpm for instance). Multistage pumps for high



                                                  Valve open on       3
                                                                      0
            reverse stroke                        forward stroke      ti
                                                  Valve open on
                                                  reverse stroke
                                                                                 Time
                                     (a)                                                 (b)







                                    (C)


                                               Discharge





                                                                         SUCTION
                                                                                    DISCHARGE
                                                                                        A








                                                                                   SCREW  SCREW
                   (e)                            (b
           Figure 7.U. Some types of  positive displacement pumps. (a) Valve action of  a double acting reciprocating piston pump. (b) Discharge curve
           of  a  single acting piston  pump  operated  by  a crank;  half-sine wave.  (c) Discharge curve of  a simplex double acting pump  as in  (a).  (d)
           Discharge curve of  a duplex, double acting pump. (e) An external gear pump; characteristics are in Figure 7.8(c). (f) Internal gear pump; the
           outer gear is driven, the inner one follows. (8) A double screw pump. (h) Peristaltic pump in which fluid is squeezed through a flexible tube
           by the follower. (i) Double diaphragm pump shown in discharge position (BIF unit of  General Signal). (j) A turbine pump with  essentially
           positive displacement characteristics (data on Fig. 7.4(a)].
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