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Centrifugal Pumps Design and Application 2nd ed - Val S. Lobanoff, Robert R. Ross (Butterworth-Heinemann, 1992)

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236 <strong>Centrifugal</strong> <strong>Pumps</strong>: <strong>Design</strong> <strong>and</strong> <strong>Application</strong><br />

volute back to the suction will also be more uniform resulting in a r<strong>ed</strong>uction<br />

in localiz<strong>ed</strong> wear in the vicinity of the casing near the impeller eye.<br />

The degree of casing concentricity must be reconcil<strong>ed</strong> with the pump<br />

specific spe<strong>ed</strong> <strong>and</strong> efficiency. For example, a 12-in. slurry pump (N s =<br />

1,350) with a conventional volute could have a 82% peak efficiency,<br />

whereas the same pump with a semi-concentric casing will have an efficiency<br />

of 80.5%. Concentric casing designs produce flat efficiency<br />

curves that are sustain<strong>ed</strong> at a high level over a wide range of flows making<br />

it more amenable to off-design point operation.<br />

Up to 1,200 N s fully concentric casings could be adopt<strong>ed</strong> without too<br />

much sacrifice in efficiency (Figure 13~4a).<br />

From 1,200 to 1,800 N s the casings should be semi-concentric, progressing<br />

towards a spiral-volute configuration at the high end of specificspe<strong>ed</strong>.<br />

A compromise is therefore reach<strong>ed</strong> between efficiency <strong>and</strong> rate of<br />

wear (Figure 13-4b).<br />

Above 1,800 N s the pump should only be appli<strong>ed</strong> to mildly abrasive<br />

services <strong>and</strong> a spiral-volute casing will be utiliz<strong>ed</strong> in the interests of<br />

higher peak efficiency (Figure 13-4c).<br />

Impeller<br />

Open impellers are us<strong>ed</strong> where the abrasion is not too severe as they<br />

have good air h<strong>and</strong>ling capabilities <strong>and</strong> are cheaper to produce. However,<br />

performance deteriorates when the front clearance opens up due to wear.<br />

Clos<strong>ed</strong> impellers are preferr<strong>ed</strong> over open impellers for severe abrasive<br />

slurries since those impellers are more robust <strong>and</strong> will last longer. Also<br />

clos<strong>ed</strong> impellers are not nearly so sensitive to fall off in performance<br />

when the front clearance increases.<br />

The requirement for extra thick impeller vanes can cause restrictions at<br />

the impeller eye <strong>and</strong> inlets. Three to five vanes are normal, depending on<br />

the pump specific spe<strong>ed</strong> <strong>and</strong> solids h<strong>and</strong>ling capability.<br />

Pump out vanes are normally provid<strong>ed</strong> on the rear shroud. These vanes<br />

have the effect of minimizing the pressure at the pump stuffing box <strong>and</strong><br />

r<strong>ed</strong>ucing the axial hydraulic unbalance. The power absorb<strong>ed</strong> by these<br />

vanes is not all wast<strong>ed</strong> since it helps to generate head. A small drop in<br />

efficiency can be expect<strong>ed</strong>.<br />

Wear Plates<br />

Suction-side wear plates should always be provid<strong>ed</strong> on metal slurry<br />

pumps, <strong>and</strong> if the service is severe, the plate should extend into the suction<br />

nozzle. The suction-side wear plate is usually the part which ne<strong>ed</strong>s<br />

replacement most often.

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