Page 204 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 204

Pumping of Liquids                                       177
                                         - Barrier Fluid In     head is twice that of the rated pressure of one pump at the
           roduct  Y------7                                     designated flow  rate  (Figure 3-35). The pump  casing of

                                                                each stage (particularly the last) must be of sufficient pres-
                                                                sure rating to withstand the developed pressure.


                                                                Pumps in Pardel
          Figure 3-31C. Double mechanical seal, two rotary elements against
          c0mm0n stationary. (By permission, Fischer, E. E., Chern Process-   Pumps  are  operated  in  parallel  to  divide  the  load
          ing, Oct. 1983 [24]1.)                                between two (or more) smaller pumps rather than a single
                                                                large one, or to provide additional capacity in a system on
                                                                short notice, or for many other related reasons. Figure 3-
                                                  r Fluid In
                                                                35 illustrates the operational curve of two identical pumps
          Product                                               in parallel, each pump handling one half the capacity at
                                                      sphere    the system head conditions. In the parallel arrangement of
                                                                two or more pumps of the same or different characteristic
                                                                curves, the capacities of each pump are added, at the head
                                                                of the system, to obtain the delivery BOW of the pump sys-
                                                                tem. Each pump does not have to carry the same flow; but
                    . Tandem double seal. (By permission, Fischer, E. E.,   it will  operate  on  its own  characteristic curve, and must
          Chem. Processing, Oct. 1983 [24].)                    deliver the required head. At a common tie point on the
                                                                discharge of all the pumps, the head will be the same for
          the sum of  the individual discharge pressures of the indi-   each pump, regardless of its flow.
          vidual pumps. For identical pumps, the capacity is that of   The characteristic curves of  each pump must be con-
          one pump, and the discharge pressure of the last pump is   tinuously rising  (right to  left)  as  shown for  the  single
          the sum of  the individual heads of each pump acting as a   pump of Figure 3-35, otherwise with drooping or looped
          single unit. Thus, for two identical pumps  the discharge   curves they may be two flow conditions for any one head,



































                                                          Gallons per minute
                  2. Comparison of impeller types for centrifugal pump performance. (Adapted by permission from Pic-a-Pump, Allis-Chalmers Mfg.
          GO.)
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