Page 403 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
P. 403

Be st Practice 7 .7           Lube, Seal and Control Oil System Best Practices
          As a first move, for selecting a properly sized pump, one can
       use the corrected valves of Q and head above to determine the             Positive displacement  Dynamic
       approximate size pump impeller required.
                                                             Rated flow
                                   Qrated                    60 SSU (Normal)     77 GPM                93.3
                      Q selection  ¼                         1000 SSU (Max.)     83.3 GPM              75 GPM
                                Q corr: factor
                                                             Discharge pressure
                            75 GPM                           6 0  S S U  N (  r o  m  ) l a  1 6 0     2 0 0
                 Q selection  ¼     ¼ 93:75 GPM              1 0 0 0  S S U  (Max.)  2 5 0             2 0 0
                              0:8
                                                             Pump horsepower
                                   HD rated                  60 SSU (Normal)     14.8 BHP              23 BHP
                    HD selection  ¼                          1000 SSU (Max.)     19.66 BHP             46 BHP
                                HD: corr factor
                              540:5
                  HD selection  ¼   ¼ 540:5 feet            Fig 7.7.14   Pump performance positive displacement vs. dynamic
                               1:0
                                                            lube oil application
          A selection for a single stage centrifugal pump operating at
       3,550 RPM with a 2" inlet, 1" discharge and 11" diameter im-  A comparison of positive displacement vs. dynamic pump
       peller is made. The curve is noted in Figure 7.7.8 and shows the  performance for this application is noted in Figure 7.7.14 for
       following pump operating points.                     normal and rated points at normal and maximum viscosities.
                                                              The following facts should be noted:
       - Rated flow @ maximum viscosity (1,000 SSU)
                                                            A. The positive displacement pump meets the required
       - Normal flow @ maximum viscosity (1,000 SSU)
       - Rated flow @ normal viscosity (60 SSU)                 discharge pressure at greater flows than specified.
       - Normal flow @ normal viscosity (60 SSU)             B. The dynamic pump meets the required flow at greater
                                                               discharge pressures than specified.
          The following facts can be observed from Figure 7.7.10:  C. The efficiency for a centrifugal pump at high viscosities and
                                                               this relatively low flow rate is significantly lower than the
       A. All operating points other than the rated point at 1,000 SSU  positive displacement pump. Note that for high flow rate
          viscosity exceed the head required of 540.0 feet.    applications the efficiency of a dynamic pump can actually
       B. A specific differential head value exists for each pump flow  exceed a P.D. pump.
          and liquid viscosity.                             D. The required horsepower of a centrifugal pump for this
       C. Pump efficiency is low for this relatively small centrifugal  application is far greater than the positive displacement pump.
          pump and is reduced approximately 50% for the high
          viscosity case.                                     The preceding example demonstrates why positive dis-
                                                            placement pumps are usually favored over dynamic pumps in
          The pump horsepower is calculated by (if a viscosity cor-  relatively low flow systems using viscous liquids. However, if the
       rection is not required):
                                                            liquid viscosity does not vary significantly, and the system flow
                                                            requirements are large, centrifugal pumps provide efficient, low
                   HeadðftÞ  flowðGPMÞ  specific gravity
            BHP ¼                                           maintenance service and are usually used.
                         3960   Pump effciencyð%Þ
                                                              It must be remembered that dynamic pumps, like positive
          If a viscosity correction is required:            displacement pumps, must be provided with the correct suction
                                                            conditions to ensure reliable operation. Cavitation, entrained

              ðheadÞ ðhead viscosity corr:Þ ðflowÞ ðflow viscosity corr:Þ  specific gravity
       BHP ¼
                      ð3960Þ  ðPump efficiencyÞ  ðPump efficiency vicosity corr:Þ



          For the maximum viscosity condition:              gases and low flow rates can cause impeller damage and wear that
                                                            will reduce pressure output and result in lower system flow rates.
                      ð540:5Þ  ð93:75Þ  ð0:8Þ ð:85Þ           The types of pumps used for our example are only two of the
               BHP ¼
                            ð3960Þð:38Þ ð:5Þ                types used for auxiliary system service. Other types of pumps
                    ¼ 46:0 BHP                              that can be used for auxiliary systems are:
                                                            - Gear type (external or internal gear)
          For the normal viscosity condition:
                                                            - Twin screw
                                                            - Lobe type
                            ð540:5Þ  ð75Þð:85Þ
                     BHP ¼                                  - Sliding vane
                              ð3960Þð0:38Þ
                                                              Before concluding this section on auxiliary system pumps,
                         ¼ 23:0 BHP
                                                            the subject of component redundancy must be discussed. In
          The pump NPSH required is obtained from the pump  order to satisfy the design objective of ‘continuously supplying.’
       curve.                                               the pumps, as well as all the major components of the system
           374
   398   399   400   401   402   403   404   405   406   407   408