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

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

Figure 8-18. Estimating K,.<br />

The extent of cavitation damage depends on the proportion of vapor releas<strong>ed</strong>,<br />

the rapidity of liberation, <strong>and</strong> the vapor specific volume, lairing<br />

this into consideration the cavitation face calculation can be correct<strong>ed</strong> by<br />

applying a gas-to-liquid ratio factor C b (Figure 8-20). On this basis, cold<br />

water must be consider<strong>ed</strong> the most damaging of the commonly pump<strong>ed</strong><br />

liquids. Similarly, this difference in behavior applies to water at different<br />

temperatures. A review of the properties of water <strong>and</strong> its vapor at several<br />

temperatures shows the specirlc volume of vapor decreases rapidly as<br />

pressure <strong>and</strong> temperature increase. This difference in behavior under<br />

cavitating conditions makes cold water more damaging than hot.<br />

The problems associat<strong>ed</strong> with cold water are substantiat<strong>ed</strong> by operating<br />

experience in the field, where pumps h<strong>and</strong>ling certain hydrocarbon fluids<br />

or water at temperatures significantly higher than room temperature<br />

will operate satisfactorily with a lower NPSHA than would be requir<strong>ed</strong><br />

for cold water.

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