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KURENAI : Kyoto University Research Information Repository

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dv<br />

pfD a€-f = Ti - opgD ,(43)<br />

where of is the velocity of an element of _a liquid ligament at z. And the<br />

interfacial shear stress Ti is given in terms of interfacial friction factor<br />

fias<br />

Ti = fi<br />

1 pgvg•(44)<br />

When the gravity term is negligible compared'with the interfacial term, Eq.<br />

(43) can be rewritten as<br />

dvf---------------<br />

= dt =dz(45)<br />

1g 1 f v2f<br />

p 2 pfD i g<br />

At z = £, this velocity is equal to the initial velocity of the droplet, that<br />

is<br />

vf(z=t) = vi(46)<br />

Integrating Eq. (45) from z = 0 to z = z,, one can obtain<br />

2pfviD=2fi p9v29£I(47)<br />

Equation (47) implies that the kinetic energy of the droplet entrained is<br />

equal to the work exerted on the element of a liquid ligament by gas flow.<br />

The ligament of liquid at the pool interface, as shown in Fig . 2, can be<br />

regarded as a sequence of several droplets which are about to be entrained .<br />

Therefore, the interfacial shear stress may be related to the drag coefficient<br />

for a droplet in the wake regime, i.e., Eq. (33), thus<br />

-0.5<br />

fi CD--ReD(48)<br />

The length of the liquid ligament is assumed to be proportional to the width<br />

of the ligament which is on the order of the droplet diameter in analogy with<br />

the Rayleigh instability of a liquid jet. Then,<br />

268

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