Page 285 - Intro Predictive Maintenance
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276       An Introduction to Predictive Maintenance



                                                             15 HP

                                     65%  70%  75%
                                                                20 HP
            200                                      BEP
                                                80%
                                                                  20 HP
                                                           75%       15 HP
                                                      80%
           Total Dynamc Head (Feet)  100                       65%
            150
                                                            70%





             50




                     100   200    300    400   500    600   700    800   1000

         Figure 13–5 Brake horsepower needs to change with process parameters.



         under specific operating conditions. For example, a pump with a discharge pressure
         of 100psig and a positive pressure of 10psig at the suction will have a  TDH of
         90psig.

         Most pump hydraulic curves define pressure to be TDH rather than actual discharge
         pressure.  This consideration is important when evaluating pump problems. For
         example, a variation in suction pressure has a measurable impact on both discharge
         pressure and volume. Figure 13–3 is a simplified hydraulic curve for a single-stage
         centrifugal pump.  The vertical axis is  TDH, and the horizontal axis is discharge
         volume or flow.

         The best operating point for any centrifugal pump is called the best efficiency point
         (BEP). This is the point on the curve where the pump delivers the best combination
         of pressure and flow. In addition, the BEP defines the point that provides the most
         stable pump operation with the lowest power consumption and longest maintenance-
         free service life.

         In any installation, the pump will always operate at the point where its TDH equals
         the TSH. When selecting a pump, it is hoped that the BEP is near the required flow
         where the TDH equals TSH on the curve. If it is not, some operating-cost penalty will
         result from the pump’s inefficiency. This is often unavoidable because pump selection
         is determined by choosing from what is available commercially as opposed to select-
         ing one that would provide the best theoretical performance.
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