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

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

Figure 8-3. Cavitation damage—at leading <strong>ed</strong>ge of one vane.<br />

NPSHR is in fact pr<strong>ed</strong>icting the losses in the critical area between suction<br />

nozzle <strong>and</strong> the leading <strong>ed</strong>ge of the first-stage impeller blades (Figure 84).<br />

Moderate Spe<strong>ed</strong> <strong>Pumps</strong><br />

One method us<strong>ed</strong> successfully for many years by pump designers will<br />

pr<strong>ed</strong>ict MPSHR with reasonable accuracy when the pump liquid is water.<br />

The inlet velocity of the liquid entering the impeller eye, CMI» <strong>and</strong> the<br />

peripheral velocity of the impeller blade, U t , are calculat<strong>ed</strong> <strong>and</strong> the ratio<br />

us<strong>ed</strong> to pr<strong>ed</strong>ict NPSHR (Figure 3-6), The chart is valid only for flows<br />

between 50% <strong>and</strong> 100% BEP at maximum impeller diameter. For capacities<br />

above 100% BEP, apply the factors indicat<strong>ed</strong> on the chart. Development<br />

of this chart is a result of acquisition of many years of pump test<br />

data. <strong>Val</strong>ues read from the chart will approximate the NPSHR establish<strong>ed</strong><br />

during pump testing using 3 % head loss as criteria. When velocities exce<strong>ed</strong><br />

those shown, the chart should not be extrapolat<strong>ed</strong>.<br />

The most commonly us<strong>ed</strong> method in determining the cavitation characteristics<br />

of a centrifugal pump is to cause a breakdown in the normal head<br />

capacity curve. This is done by holding the spe<strong>ed</strong> <strong>and</strong> suction pressure

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