Page 351 - Boiler_Operators_Handbook,_Second_Edition
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336                                                                               Boiler Operator’s Handbook


               help to realize that a centrifugal pump simply boosts the
               pressure a certain amount and that boost is related to the
               flow of water through the pump. You can stop stirring
               the water in your bowl and it will still overflow once it
               has filled. You can also vary the difference (head) you’re
               creating by changing the speed at which you stir it.
                    Back from playing in the kitchen sink? Good. I
               trust you now understand that there is no such thing as
               a limit on the flow through a centrifugal pump; the high-
               est possible flow is much more than the design value
               and the minimum is zero. Without check valves in the
               discharge piping a higher external differential pressure
               than the pump can handle will result in flow backwards
               through the pump. The actual flow rate is dependent on
               the performance of the pump itself and the difference in
               pressure between suction and discharge.
                    Oh there’s a design point, a flow and differential
               that the engineer calculated for selecting the pump and           Figure 10-72. Wear rings
               that’s usually indicated in the manual and on the pump
               curve. What you, as an operator, have to deal with is the  ring and casing where erosion can cause problems. Too
               actual flowing conditions. The odds that the actual con-  thin a gasket will normally bind the pump up.
               ditions are precisely the same as the design conditions     You’ll find a lot of variety in centrifugal pumps
               are between slim and none.                           depending on their application. The pressure differential
                    A feature of centrifugal pumps that’s frequently  they can produce depends on the density of the liquid be-
               forgotten is the use of wear rings (Figure 10-72) The  ing pumped and the speed of the tips of the vanes in the
               space between the casing and the eye of the impeller  impeller. To make a pump operate at a higher differential
               is all that separates the suction and discharge pressure  pressure with the same liquid the diameter of the impel-
               zones of the pump so some water has to bleed back  ler is increased. Once the impeller’s maximum diameter
               through that space because they can’t rub. As the pump  is reached a faster motor is used. As the impeller diameter
               is used small particles in the liquid and the liquid itself  and speed increases the stress on the metal gets higher so
               can erode the material on either side of that gap and pro-  there are practical limits on the pressure boost.
               vision of wear rings makes it possible to restore a pump     If a larger differential pressure is required the
               to a like-new condition by simply replacing the wear  pump is supplied with additional impellers. We call
               rings. The casing wear rings, right one hanging loose in  them ‘multi-stage’ pumps. The pressure is increased a
               the photo, are keyed to set in the casing and not rotate.  little in each impeller which, along with its volute and
               The impeller wear ring is heated then inserted onto the  share of the casing constitutes a stage. That way high
               end of the impeller where it shrinks on for a tight fit.  pressures can be developed without making pumps of
                    No, a strainer in the suction piping (standard re-  very large diameter.
               quirement for most pumps) does not remove the small      Since the eye (inlet of an impeller) is exposed to
               particles that erode the wear rings; the strainer does  suction pressure at that stage and the rest is exposed to
               remove pieces that would jam between them. Usually  the discharge pressure of that stage there’s a difference
               a pump with wear rings will also have a shaft sleeve. I  in axial forces on the stage (Figure 10-73). In single stage
               should mention that you should be cautious when re-  pumps holes are drilled through the back plate of the
               placing wear rings and anytime you reassemble a split  impeller and a second set of wear rings added to bal-
               case pump because the outer wear ring can be distorted  ance the pressure. (Figure 10-74) In multi-stage pumps
               when the two halves of the pump casing bear down  the stages are reversed on the shaft (Figure 10-75) so the
               on it. Always make sure the pump rotates by hand as  imbalance of one stage is opposed by the imbalance of
               you’re drawing up on the bolts that hold the two casing  another. Some pumps with vertical shafts are designed
               halves together. Also, don’t install a thicker gasket on a  so the axial thrust helps offset the weight of the shaft
               pump simply because you don’t have the right thickness  and impeller. Despite the best design, there’s no guaran-
               on hand, that will create gaps between the outer wear  tee the pump will not see some axial forces so one end
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