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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 87<br />

Pr<strong>ed</strong>icting NPSHR<br />

The other side of the coin necessary for reliable operation is of course<br />

accurate pr<strong>ed</strong>iction of NPSHR by the pump designer.<br />

In considering NPSHR, it is necessary to underst<strong>and</strong> that a centrifugal<br />

pump is design<strong>ed</strong> as a hydraulic machine to move liquids. Any amount of<br />

entrain<strong>ed</strong> air or gas present will cause a deterioration in pump performance.<br />

Various tests substantiate the claim that a volume of only one percent<br />

air or gas will cause a loss of head <strong>and</strong> efficiency. As liquid travels<br />

from suction nozzle to impeller eye, it will experience pressure losses<br />

caus<strong>ed</strong> by friction, acceleration, <strong>and</strong> shock at blade entry. If the summation<br />

of these losses permits vaporization of the liquid, vapor bubbles will<br />

form in the impeller eye, travel through the impeller, <strong>and</strong> upon reaching a<br />

high pressure region, collapse. This collapse or implosion of the vapor<br />

bubbles is classic cavitation, which can lead to impairment of performance<br />

<strong>and</strong> impeller damage (Figures 8-2 <strong>and</strong> 8-3). Thus, pr<strong>ed</strong>icting<br />

Figure 8-2. Cavitation damage—looking into impeller eye.

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