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KURENAI : Kyoto University Research Information Repository

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a<br />

j* 99 =jagOp1/4(3) 2<br />

pg<br />

where a, g and Op are the surface tension, acceleration due to the<br />

gravity, and difference between the gas and liquid densities,<br />

respectively. In Eq. (2), CK must be determined from experimental data.<br />

However, it has been found that the value of CK depends on the distance<br />

from the interface. Although Eq. (2) shows the effects of velocity and<br />

pressure on Efg, it does not give any information on the effect of height,<br />

which is important in the momentum controlled region.<br />

Sterman [40] correlated the experimental data of entrainment for<br />

steam water systems at pressures from 0.1 MPa to 18 MPa, and proposed a<br />

dimensionless correlation. His correlation depends on the average void<br />

fraction in the pool, therefore, he has also proposed several void<br />

fraction correlations applicable to the problem. For a reasonably large<br />

vessel satisfying the condition given by<br />

*MO*2(4)<br />

D> 260 ,<br />

where the dimensionless diameter of vessel DH is given by<br />

DH = DH RI-76 4)-g(5)<br />

the Sterman correlation can be simplified to<br />

fg = 6.09 x 10jh(6) 9*2.76*-2.3 (PyO.26 '2.21.1E<br />

Here the dimensionless height h* is given by<br />

h= h/'l-----a90p(7)<br />

Y and the liquid viscosity number Nuf based on liquid viscosity of is given<br />

by<br />

258

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