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

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

3. All volute areas should be design<strong>ed</strong> to provide a smooth change of<br />

areas.<br />

4. Circular volutes should be consider<strong>ed</strong> for pumps below a specific<br />

spe<strong>ed</strong> of 600. Circular volutes should not be consider<strong>ed</strong> for multistage<br />

pumps.<br />

5. The total divergence angle of the diffusion chamber should be be<br />

tween 7 <strong>and</strong> 13 degrees. The final kinetic energy conversion is obtain<strong>ed</strong><br />

in the discharge nozzle in a single-stage pump <strong>and</strong> in both the<br />

discharge nozzle <strong>and</strong> crossover in a multi-stage pump.<br />

6. In designing a volute, be liberal with the space surrounding the impeller.<br />

In multi-stage pumps in particular, enough space should be<br />

provid<strong>ed</strong> between the volute walls <strong>and</strong> the impeller shroud to allow<br />

one-half inch each way for end float <strong>and</strong> casting variations, A volute<br />

that is tight in this area will create axial thrust <strong>and</strong> manufacturing<br />

problems.<br />

The Use of Universal Volute Sections for St<strong>and</strong>ard Volute <strong>Design</strong>s<br />

It has been not<strong>ed</strong> that when the volute sections of different pumps are<br />

factor<strong>ed</strong> to the same throat area; their contours are almost identical. Any<br />

differences that do exist can be trac<strong>ed</strong> to mechanical considerations or the<br />

designer's whim, rather than any important principle of hydraulic design.<br />

Similarly, factoring the impeller width <strong>and</strong> the radial gap between the impeller<br />

<strong>and</strong> the cutwater reveals that the values of these parameters also lie<br />

in a very narrow r<strong>and</strong>om range.<br />

In other words, the entire discharge portion of the pump casing when<br />

view<strong>ed</strong> in cross section <strong>and</strong> factor<strong>ed</strong> to a common throat area has only<br />

minor variations throughout the entire specific spe<strong>ed</strong> spectrum. This fact<br />

enables us to eliminate the usual trial-<strong>and</strong>-error method of designing volute<br />

sections while still consistently producing casings to a high st<strong>and</strong>ard<br />

of hydraulic design. To facilitate this process we have prepar<strong>ed</strong> a set of<br />

"universal" volute drawings on which the typical volute sections describ<strong>ed</strong><br />

above have been laid out for a 10 sq in. throat area. Once the<br />

designer has chosen his throat area, he can quickly produce the requir<strong>ed</strong><br />

volute sections by factoring the sections shown for the "universal" volute.<br />

Sections for a single-volute pump are shown in Figures 5-5 <strong>and</strong><br />

5-6, <strong>and</strong> sections for a double volute pump are shown in Figure 5-7.<br />

The <strong>Design</strong> of Rectangular Double Volutes<br />

For low capacity (500-600 GPM) or low to m<strong>ed</strong>ium specific spe<strong>ed</strong><br />

(N s < 1,100) pumps, a rectangular volute design should be consider<strong>ed</strong>.

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