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Handbook of Turbomachinery Second Edition Revised - Ventech!

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Figure 14 Draft tube setting.<br />

same as the inlet <strong>of</strong> the draft tube. Thus<br />

V 2 e =2g ¼ðpa peÞ=g ðHs hfÞ ð20Þ<br />

Cavitation occurs when the value <strong>of</strong> pe becomes equal to the vapor pressure<br />

<strong>of</strong> the fluid at the local temperature. The cavitation parameter s can be<br />

defined as the ratio <strong>of</strong> exit velocity head and head on the machine. Thus,<br />

s ¼ðV 2 e =2gÞ=H ¼½ðpa pvÞ=g ðHs hfÞŠ=H ð21Þ<br />

where pe has been replaced by the vapor pressure pv. Usually, the head loss<br />

hf is small and is dropped from the equation. Thus a number called the<br />

Thoma cavitation coefficient, named after the German engineer Dietrich<br />

Thoma (1881–1943), can be defined as<br />

s ¼½ðpa pvÞ=g HsŠ=H ð22Þ<br />

In order to avoid cavitation, it is necessary that s > sc, where sc is called the<br />

critical cavitation coefficient. The values <strong>of</strong> sc are determined experimentally<br />

by plotting s versus efficiency. For large values <strong>of</strong> s, efficiency is nearly<br />

constant. When sfalls below sc, however, the efficiency rapidly drops <strong>of</strong>f.<br />

This is also accompanied by increased noise and vibration. Typical values <strong>of</strong><br />

sc are given in Table 4.<br />

Copyright © 2003 Marcel Dekker, Inc.

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