Page 102 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
P. 102

Be st Practice 2 .19          Pump Best Practices


         Best Practice 2.19Practice 2.19Practice 2.19
         Best
         Best
         Monitor parallel centrifugal pump operation by the use of  Lessons Learned
         manual or automatic differential pipe temperature to pre-  Centrifugal pumps operating in parallel are prone to
         vent parallel pump failure.                        damage from liquid vaporization when one or more pumps
           Pumps that operate in parallel are subject to significant component  have deficient head/flow curves resulting from internal
         damage if they are not individually protected against minimum flow e  component wear.
         and usually they are not.
                                                              It has been my experience that most parallel pump systems are not
           When pumps operate in parallel, the pump with the lowest head
                                                            monitored for individual reduced pump flow, and are not provided with
         produced (worn pump and/or pump operating at the lowest speed) will
                                                            individual pump minimum flow protection. As a result, significant pump
         be forced to reduced flow.
                                                            components can and will occur when one or more pumps have internal
           Typically, for cost saving reasons, the minimum flow protection for
                                                            wear or operate at a reduced speed compared to the other pumps.
         the pumps is installed in the pump discharge header and therefore
         does not provide individual pump protection.       Benchmarks
           As the flow to any centrifugal pump decreases (see supporting
         material below), the pump efficiency reduces and approaches 0% at  This monitoring approach has been used since the mid-1990s to
                                                            ensure parallel pump optimum safety and reliability (MTBFs greater
         zero flow. As a result, the pump differential temperature, which is close  than 80 months).
         to zero degrees Celsius in the safe operating region of flow, will in-
         crease significantly as pump flow decreases.
           Monitoring pump differential temperature is therefore a practical
         way of determining parallel pump internal condition and speed (if the
         pump driver is a variable speed type).
       B. P. 2.19. Supporting Material                        A reduction in pump efficiency will result in an increase in
                                                            pump fluid differential temperature, which can be measured by
       Figure 2.19.1 shows a typical centrifugal pump performance  contact thermometers on the inlet and discharge pipe. This in-
       curve and the efficiency islands, which shows how the efficiency  crease in temperature will therefore indicate reduced pump
       of any centrifugal pump varies with flow. As a worn or reduced  flow and the condition and or reduced speed of the affected
       speed pump is forced to lower flows by the more efficient pump  pump. Please refer to Figure 2.19.2 below.
       in the parallel pump system, pump efficiency will reduce.  Pump efficiency is low at low flows.








































       Fig 2.19.1   A typical centrifugal pump performance curve (Courtesy of Union Pump Co.)

           76
   97   98   99   100   101   102   103   104   105   106   107