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PUMPS    127
            TABLE 5.3  Symptoms and Possible Causes for Centrifugal Pump Problems

            Symptom                                                     Possible Causes
            Pump does not deliver rated capacity.  Excessive discharge head, not enough NPSH A , suction line not filled, air or vapor pocket in suction
                                             line, plugged impeller or piping, worn or damaged impeller or wearing rings, inadequate foot
                                             valve size, foot valve clogged with debris, internal leakage due to defective gaskets, wrong
                                             direction of rotation, viscosity of liquid more than that for which pump is designed, inlet to
                                             suction line not sufficiently submerged, and pump not up to rated speed.
            Failure to deliver liquid.     Wrong direction of rotation, pump not primed, available NPSH not sufficient, suction line not filled
                                             with liquid, air or vapor pocket in suction line, inlet to suction pipe not sufficiently submerged,
                                             pump not up to rated speed, and total head required greater than head which pump is capable of
                                             delivering.
            No discharge pressure.         Pump improperly primed, not enough NPSH A , plugged impeller or piping, inlet to suction line not
                                             sufficiently submerged, inadequate speed, suction line not filled, air ingress into suction line,
                                             total head required is greater than head pump is capable of delivering, incorrect direction of
                                             rotation, and closed discharge valve.
            Pressure surge.                Not enough NPSH A , air ingress into suction line, entrained air, plugged impeller.
            Inadequate discharge pressure.  Not enough velocity, air/gases in pumped liquid, too small impeller diameter, pump not up to rated
                                             speed, worn or damaged impeller or wearing rings, incorrect rotation, discharge pressure more
                                             than pressure for which pump is designed, viscosity of liquid more than that for which pump is
                                             designed, and internal leakage due to defective gaskets.
            Pump loses liquid after starting.  Suction line not filled with liquid, air leaks in suction line or stuffing boxes, two-phase flow, slug
                                             flow, inlet to suction line not sufficiently submerged, not enough NPSH A , liquid seal piping to
                                             lantern ring plugged, and lantern ring not properly located in stuffing box.
            Excessive power consumption.   Head too small, excessive recirculation, high sp. gr. or high m liquid, misalignment, bent shaft,
                                             bound shaft, packing too tight, rotating element dragging, and incorrect rotation.
            Vibration and noise.           Cavitation, excessive suction lift, starved suction, not enough NPSH A , air ingress, inlet to suction
                                             line not sufficiently submerged, worn or loose bearings, bent shaft, misalignment, bound rotor,
                                             improper location of control valve in discharge line, and foundation not rigid.
            Stuffing boxes overheat.        Packing too tight and/or not lubricated, wrong grade of packing, box insufficiently packed, and
                                             insufficient cooling water to jackets.
            Bearings overheat.             Oil level too low, improper or poor grade oil, dirty bearings and oil, moisture in oil, oil cooler
                                             clogged or scaled, oiling system failure, insufficient cooling water circulation, insufficient
                                             cooling air, bearings too tight, oil seals too close fit on shaft, and misalignment.
            Bearing wear rapidly.          Misalignment, bent shaft, vibration, bearings improperly installed, dirt in bearings, moisture in oil,
                                             excessive cooling of bearings, excessive thrust resulting from mechanical failure inside the
                                             pump, and lack of lubrication.
            Courtesy: GPSA Engineering Data Book, 12th ed.





              . Can the suction size of a centrifugal pump be larger than  . “Positive displacement pumps are usually self-primed
                the pipeline?                                       pumps.” True/False?
                & The piping leading to a centrifugal pump must be at  & True.
                  least one size larger than the inlet flange on the pump.  . What is meant by Simplex, duplex, triplex, and mul-
                  Similarly, the discharge piping leading from the  tiplex in pump terminology?
                  pump should be at least one size larger than the   & Simplex refers to single-piston type of reciprocal
                  flange size on the discharge of the pump.
                                                                       piston pump. A Duplex pump has two pistons; one
                                                                       is on suction mode while the other is on delivery
            5.1.4  Positive Displacement Pumps                         mode. Similarly, triplex and multiplex mean three
                                                                       and multiple number of pistons, respectively, in
              . “Positive displacement pumps generally operate at low  different modes of operation.
                inlet velocities.” True/False?                     . Illustrate valve action for a double-acting reciprocating
                & True. In these cases, generally velocity head portion  piston pump and discharge curves for different flow
                  is ignored.                                       configurations.
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