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

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NPSH 99<br />

Figure 8-17. Influence of plate inserts on NPSHR.<br />

It can be assum<strong>ed</strong> that this improvement is influenc<strong>ed</strong> by r<strong>ed</strong>uc<strong>ed</strong> separation,<br />

improv<strong>ed</strong> flow stability <strong>and</strong> streamlining, a progressive increase<br />

in velocity, <strong>and</strong> the resulting r<strong>ed</strong>uc<strong>ed</strong> turbulence. It must also be accept<strong>ed</strong><br />

that any disturbance in the approach to the impeller can cause unequal<br />

distribution of flow rates into the two impeller eyes at different locations,<br />

These diversions from the correct angle of attack at the leading <strong>ed</strong>ge of<br />

the blades produce a corresponding head loss.<br />

The test confirms that the cavitation characteristics of a good impeller<br />

design can be impair<strong>ed</strong> by poor suction nozzle design. This is particularly<br />

true with double-entry impeller pumps where the complex nozzle<br />

geometry can adversely affect KI. A well design<strong>ed</strong> suction nozzle has a<br />

gradual decrease in area from nozzle to impeller, allowing a progressive<br />

increase in velocity. Area distribution guidelines are shown in Figure<br />

7-4. The range suggest<strong>ed</strong> permits impellers of different suction specific<br />

spe<strong>ed</strong>s to be us<strong>ed</strong> with a common suction.<br />

Using the actual suction nozzle area ratio at Section A-B gives a reasonable<br />

means of estimating K } (Figure 8-18). For the same incidence<br />

angle a, K 2 has a higher value at capacities above design. For estimating<br />

K 2 use Figure 8-19.<br />

influence of Liquid<br />

The boiling of the liquid in the process of cavitation is a thermal process<br />

<strong>and</strong> is dependent on the liquid properties, pressure, temperature, latent<br />

heat of vaporization, <strong>and</strong> specific heat. To make this boiling possible,<br />

the latent heat of vaporization must be deriv<strong>ed</strong> from the liquid flow.

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