Page 75 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Pump Best Practices      Be st Practice 2.7

































              Fig 2.7.15   Centrifugal pump head vs. flow curve

                                                                   seal chamber pressures and temperatures to change and lead to
                                                                   premature seal wear and/or failure. Note that the stated EROE
               1. The EROE flow range is + 10% and  50% of the pump best
                  efficiency point (BEP) flow                        low flow range can be reduced if the pump or fluid have any of
               2. All ‘bad actor pumps’ (more than one component failure per  the characteristics noted in Figure 2.7.18.
                  year) should be checked for EROE.
               3. To determine that the pump is operating in EROE:
                   Calculate the pump head required
                   Measure the flow
                   Plot the intersection of head and flow on the pump shop test  Pumps with suction specific speeds > 8,000 (customary units)
                   curve                                              Double suction pumps
                                                                      Water pumps with low NPSH margin
                                                                      Fluids with S.G. < 0.7
                                                                      Pumps with Inducers
              Fig 2.7.16   EROE Facts
                If a flow meter is not installed, Figure 2.7.17 defines the
              options that are available to determine the pump flow, so the  Fig 2.7.18   Factors that can reduce low flow EROE range
              EROE can be obtained.
                The flow values in Figure 2.7.17 can be determined by hand  Therefore, we always recommend that the first step in
              calculations using the equations available in any pump text  seal condition monitoring be determination of pump opera-
              (power equation and pump temperature rise equation).  tion within its EROE. If the ‘bad actor’ pump is operating
                It can be seen that the EROE will provide a reasonable guide  outside its EROE, we recommend the action shown in
              that usually will eliminate hydraulic disturbances that can cause  Figure 2.7.19.
                                                                     If seal reliability does not improve when operating within the
                                                                   EROE, further investigation is required concerning the process
               1. Measure motor amps and calculate power           conditions in the seal chamber and/or flush system.
               2. Record control valve position, valve differential pressure, fluid
                  S.G. and calculate valve flow (pump flow).
               3. Measure pump pipe differential temperature and calculate
                  pump efficiency                                      Consult operations to determine if process changes can be
               4. Obtain an ultrasonic flowmeter to measure flow        made to operate in EROE
               5. For items 1 and 3, locate the calculated value (power or  Define target EROE parameters for operations (flow, amps,
                  efficiency) on the pump test curve to determine pump flow  control valve postion, delta T)


              Fig 2.7.17   Available pump flow determination options  Fig 2.7.19   If a centrifugal pump is outside its EROE




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