Page 230 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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202                       Applied Process Design for Chemical and Petrochemical Plants

                                                          (3-20)

                                                          (3-21)





            For a fixed speed [25] :

                                                          (3-23)

                                                          (3-24)


                                                          (3-25)

               For  geometrically similar impellers  operating  at  the
            same specific speed, the affinity laws are [25,11]:







                                                                                Capacity , Gpm.

                                                                    Figure 3-55. Relation of speed change to pump characteristics.
                                                         (3- 28)
                                                                    2.  For changes  (cut-down) in impeller  diameter  (not
                                                                  design) at fixed efficiency: [ 111
            where: condition of subscript (2) represents the new non-
            cavitating or  desired  condition,  and  condition  of  sub-
            script (1) represents the condition for which a set of con-                                        (3 - 29)
            ditions are known.
               These relations do not hold exactly if the ratio of speed
            change is greater than 1.5 to 2.0, nor do they hold if suc-
            tion conditions become limiting, such as NPSH.                                                     (3- 30)
               Figure 3-55 illustrates the application  of these perfor-
                                                                                 :]
            mance laws to the 1750 rpm curves (capacity, brake horse-   BHP,  = BHP, [  [ 21  3
                                                                                      3
            power, and efficiency) of  a particular pump to arrive at                                          (3- 31)
            the  1450 rpm  and 1150 rpm  curves. Note  that  the  key
            value  is  the  constant  efficiency  of  points  (1) and  (2).
            When the speed drops to 1450 rpm, capacity drops:     where dl is the original impeller diameter in inches, and
                                                                  subscript (2) designates the new or desired conditions cor-
               Q2  = 204(1450/1750)   169 GPM                     responding to the new impeller diameter, d2. All perfor-
                                                                  mance changes occur simultaneously when converting from
               The head also drops:                               condition  (1) to condition  (2), no single condition can be
                                                                  true unless related to its corresponding other conditions.
                                                                    An impeller can be cut from one size down to another
               H,  = 64(1450/1750)2 = 44 ft
                                                                  on a  lathe, and provided the  change  in  diameter  is  not
                                                                  greater than 20 percent, the conditions of new operation
            and:                                                  can be described by the type of calculations above. A cut to
                                                                  reach 75-80  percent of the original diameter may adverse-
               (BHP), = 6.75(1450/1750)3 = 3.84 BHP               ly affect performance by greatly lowering the efficiency [4].
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