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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 93<br />

Figure 8-8. Performance curve showing NPSHR cavitation free <strong>and</strong> NPSHR 3%<br />

head loss.<br />

"Cavitation-free NPSHR" cannot be demonstrat<strong>ed</strong> by a suppression<br />

test, as no head loss will be evident. Therefore, to satisfy the normal requirement<br />

for testing on the pump manufacturer's test st<strong>and</strong>, it is suggest<strong>ed</strong><br />

that two NPSHR curves be offer<strong>ed</strong> with the pump quotation.<br />

These would be "cavitation-free NPSHR" <strong>and</strong> the conventional 3% head<br />

loss NPSHR (Figure 8-8).<br />

Cavitation-Free NPSHR<br />

As describ<strong>ed</strong> earlier, cavitation is the formation of vapor-fill<strong>ed</strong> cavities<br />

in the pump<strong>ed</strong> liquid resulting from a sufficient r<strong>ed</strong>uction of the liquid<br />

pressure to vaporize a proportion of the liquid. To prevent this vaporization<br />

<strong>and</strong> the damage associat<strong>ed</strong> with it, the pump designer must first consider<br />

the head losses in the most critical area, which is between the inlet<br />

nozzle of the pump <strong>and</strong> the leading <strong>ed</strong>ges of the first-stage impeller<br />

blades, This head loss is a result of the following factors:<br />

1. Head loss due to friction.<br />

2. Head drop due to fluid acceleration, which is the energy requir<strong>ed</strong> to<br />

accelerate the flow from the suction nozzle to the impeller eye.<br />

3. Head shock loss due to blade entry, which is the localiz<strong>ed</strong> drop at<br />

the blade leading <strong>ed</strong>ge <strong>and</strong> is a function of the angle of attack <strong>and</strong><br />

blade entry shape.

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