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Untitled - Aerobib - Universidad Politécnica de Madrid

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13.15. DROPLET EVAPORATION 329<br />

1<br />

0.9<br />

0.8<br />

0.7<br />

0.6<br />

m/m 0<br />

0.5<br />

0.4<br />

0.3<br />

0.2<br />

0.1<br />

c T /q =2<br />

p1 ∞ l 4 6 8 10<br />

0<br />

0 1 2 3 4 5 6 7 8 9 10<br />

x<br />

Figure 13.7: The ratio m/m 0 as a function of x = c p1(T ∞ − T s)/q l for some values of<br />

c p1T ∞/q l .<br />

Figure 13.7 gives m/m 0 as a function of x, for some values of c p1 T ∞ /q 1 .<br />

When the evaporation velocity is high the fast <strong>de</strong>crease of the evaporation constant<br />

can be seen due to the transport of enthalpy done by the vapour motion.<br />

The previous formulae do not take into account the influence of convection.<br />

Such effect has been studied by Frössling [32], who obtained the following relation<br />

between the evaporation velocity m c with convection and the evaporation velocity at<br />

rest<br />

m c<br />

m = (<br />

1 + 0.276 Sc 1/3 Re 1/2) . (13.106)<br />

Here Sc = µ/ρD 12 and Re = ρvd s /µ are, respectively, the Schmidt number<br />

and the Reynolds number of the motion, µ is the gas viscosity coefficient, d s the<br />

droplet diameter and v the motion velocity. Ranz and Marshall [33] have experimentally<br />

verified this formula. Fig. 13.8 gives m c /m as a function of Sc 2/3 Re.<br />

Formula (13.105) was obtained from experiments at ambient temperature. Ingebo<br />

[34] gives the following empirical formula which represents with good approximation<br />

the experimental results obtained by him from 30 ◦ C to 500 ◦ C<br />

m c<br />

m = ( 1 + 0.151(Sc Re) 0.6) . (13.107)

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