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

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

Circular-Volute Casings<br />

Several pump manufacturers have conduct<strong>ed</strong> tests to evaluate the hydraulic<br />

performance of pumps with circular volutes. A study of the results<br />

of these tests reveals that circular volutes improve the hydraulic performance<br />

of small high head or low specific spe<strong>ed</strong> units <strong>and</strong> impair the<br />

performance of high specific spe<strong>ed</strong> pumps. Specifically, pump efficiency<br />

is improv<strong>ed</strong> below specific spe<strong>ed</strong>s of 600. For specific spe<strong>ed</strong>s above 600<br />

the efficiency of circular-volute designs will be 95% of that possible with<br />

conventional volute designs. This can be explain<strong>ed</strong> by remembering that<br />

in a conventional volute a uniform pressure <strong>and</strong> velocity distribution exists<br />

around the impeller periphery only at the BEP. At off-peak capacities,<br />

velocities <strong>and</strong> pressures are not uniform. For circular volutes the<br />

opposite is true. Uniform velocity <strong>and</strong> pressure exist only at zero flow.<br />

This uniformity is progressively destroy<strong>ed</strong> as the capacity is increas<strong>ed</strong>,<br />

Therefore, at BEP the casing losses are generally greater than those of<br />

the conventional volute. For low specific spe<strong>ed</strong> pumps, however, there is<br />

some gain in efficiency due to a circular volute since the benefits of the<br />

Improv<strong>ed</strong> surface finish in the machin<strong>ed</strong> volute outweigh the problems<br />

creat<strong>ed</strong> by the nonuniform pressure distribution. A comparison of the efficiency<br />

of circular <strong>and</strong> conventional volutes is shown in Figure 5-4. The<br />

use of a circular volute design should be consider<strong>ed</strong> in the following instances:<br />

• For small, high head, low specific spe<strong>ed</strong> (N s 500-600) pumps.<br />

» For a pump casing that must accommodate several impeller sizes.<br />

• For a pump in which foundry limitations have dictat<strong>ed</strong> an overly wide<br />

impeller b 2 .<br />

» For a pump that must use a fabricat<strong>ed</strong> casing.<br />

« For a pump that requires that the volute passage be machin<strong>ed</strong> in the<br />

case casting.<br />

General <strong>Design</strong> Considerations<br />

It was point<strong>ed</strong> out previously that the casing itself represents only<br />

losses <strong>and</strong> does not add anything to the total energy develop<strong>ed</strong> by the<br />

pump. In designing pump casings it is therefore important to utilize all<br />

available means of minimizing casing losses. However, commercial considerations<br />

dictate some deviations from this approach, <strong>and</strong> experience

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