Page 27 - Centrifugal Pumps 2E
P. 27

Specific Speed and Modeling Laws    15

                                     Table 2-4
                       Tabulated Performance at 4,000 RPM
        GPM                 H(ft)               Eff. %                bhp
          0                  445                   0                  37
         113                 443                  28                  45
         226                 438                  48                  52
         337                 427                  52                  60
         452                 412                  70                  66
         565                 381                  74                  73
         678                 330                  73                  77
         732                 298                  72                  76



        the pump specific speed. To obtain suction specific speed continue from
        the rotating speed to NPSHR and vertically to the suction specific speed.
        Pump specific speed is the same for either single-suction or double-suc-
        tion designs.
          For estimating the expected pump efficiencies at the best efficiency
        points, many textbooks have plotted charts showing efficiency as a func-
        tion of specific speed (N s) and capacity (GPM). We have prepared similar
        charts, but ours are based on test results of many different types of pumps
        and many years of experience.
          Figure 2-3 shows efficiencies vs. specific speed as applied to end-suc-
        tion process pumps (API-types). Figure 2-4 shows them as applied to sin-
        gle-stage double-suction pumps, and Figure 2-5 shows them as applied to
        double-volute-type horizontally split multi-stage pumps.
          Figure 2-5 is based on competitive data. It is interesting to note that
        although the specific speed of multi-stage pumps stays within a rather
        narrow range, the pump efficiencies are very high, equal almost to those
        of the double-suction pumps. The data shown are based on pumps having
        six stages or less and operating at 3,560 RPM. For additional stages or
        higher speed, horsepower requirements may dictate an increase in shaft
        size. This has a negative effect on pump performance and the efficiency
        shown will be reduced.
          As can be seen, efficiency increases very rapidly up to N s 2,000, stays
        reasonably constant up to N s 3,500, and after that begins to fall off
        slowly. The drop at high specific speeds is explained by the fact that hy-
        draulic friction and shock losses for high specific speed (low head)
        pumps contribute a greater percentage of total head than for low specific
        speed (high head) pumps. The drop at low specific speeds is explained by
        the fact that pump mechanical losses do not vary much over the range of
        specific speeds and are therefore a greater percentage of total power con-
        sumption at the lower specific speeds.
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