Page 254 - Root Cause Failure Analysis
P. 254

242       Root Cause Failure Analysis

                   The NPSHA also can be increased by decreasing the temperature of the liquid being
                   pumped. This decreases the saturation pressure, which increases the NPSH,.
                   If the head losses in the suction piping can be reduced, the NPSHA will be increased.
                   Methods for reducing head losses include increasing the pipe diameter; reducing the
                   number of elbows, valves, and fittings in the pipe; and decreasing the pipe length.
                   It also may be possible to stop cavitation by reducing the pump’s NPSHR, which is
                   not a constant for a given pump under all conditions. Typically, the NPSHR increases
                   significantly as the pump’s flow rate increases. Therefore, reducing the flow rate by
                   throttling a  discharge valve  decreases NPSHR.  In  addition  to  flow  rate,  NPSH,
                   depends on pump speed. The faster the pump’s impeller rotates, the greater is the
                   NPSHR. Therefore, if the speed of a variable-speed centrifugal pump is reduced, the
                   NPSHR of the pump is decreased.

                   Variations in the Total System Head

                   Centrifugal-pump performance follows its  hydraulic curve  (i.e., head  versus flow
                   rate). Therefore, any variation in the total back pressure of the system causes a change
                   in the pump’s flow or output. Because pumps are designed to operate at their best effi-
                   ciency point (BEP), they become more and more unstable as they are forced to oper-
                   ate at any other point because of  changes in total system pressure, or head (TSH).
                   This  instability has  a  direct  impact  on  centrifugal-pump performance,  reliability,
                   operating costs, and required maintenance.

                   Symptoms

                   The symptoms of failure due to variations in TSH include changes in motor speed and
                   flow rate.

                   Motor Speed  The brake horsepower of the motor that drives a pump is load depen-
                   dent. As the pump’s operating point deviates from BEP, the amount of  horsepower
                   required  also changes. This causes a change in  the pump’s rotating speed, which
                   either increases or decreases depending on the amount of  work that the pump must
                   perform.

                   Flow Rate  The volume of liquid delivered by the pump varies with changes in TSH.
                   An increase in the total system back pressure results in a decreased flow, while a back
                   pressure reduction increases the pump’s output.

                   Solutions
                   The best solution to problems caused by TSH variations is to prevent the variations.
                   While it is not possible to completely eliminate them, the operating practices for cen-
                   trifugal pumps should limit operation to an acceptable range of  system demand for
                   flow and pressure. If system demand exceeds the pump’s capabilities, it may be nec-
   249   250   251   252   253   254   255   256   257   258   259