INAUGURAL–DISSERTATION zur Erlangung der Doktorwürde der ...
INAUGURAL–DISSERTATION zur Erlangung der Doktorwürde der ...
INAUGURAL–DISSERTATION zur Erlangung der Doktorwürde der ...
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4.1. One-dimensional Evaporating Water Spray in Nitrogen 61<br />
Tab. 4.2: Droplet size distribution of water spray<br />
d(t = 0 s) [µm] f [(µm) −1 ] d(t = 1 s) [µm] d(t = 50 s) [µm] ]<br />
10.643 0.409 0.000 0.000<br />
12.913 4.091 0.000 0.000<br />
15.588 11.434 0.000 0.000<br />
18.745 11.762 0.000 0.000<br />
22.468 8.472 0.000 0.000<br />
26.858 7.112 0.000 0.000<br />
32.037 7.093 5.138 0.000<br />
38.145 7.481 21.332 0.000<br />
45.350 7.304 32.506 0.000<br />
53.848 6.609 43.584 0.000<br />
63.870 5.439 55.492 0.000<br />
75.692 4.491 68.770 0.000<br />
89.635 4.073 83.872 0.000<br />
106.080 4.319 101.257 0.000<br />
125.478 4.574 121.427 0.000<br />
148.355 3.579 144.946 0.000<br />
175.337 1.490 172.462 0.000<br />
207.163 0.255 204.735 0.000<br />
244.697 0.015 242.646 99.381<br />
The k value is usually estimated from the material properties such as density, diffusivity,<br />
etc., and in general, it has a value in the range of 10 −7 to 10 −11 . Just for the sake of<br />
explanation, k is assumed to be 1.0E-09 m 2 /s. The change in the droplet diameter is<br />
computed at t = 1 s using d 2 law is given in Tab. 4.2, see the third column. Comparing<br />
the values of droplet diameter at t = 0 s and t = 1 s, it shows that the droplet diameter<br />
decreases and lower size droplets vanish. Using these data, the computed d 32 at t =<br />
1 s is 117.126 µm, which shows an increase from initial value. This increase continues<br />
till certain evaporation time (see last column in Tab. 4.2), whereupon the Sauter mean<br />
diameter starts to decrease because most of the smaller size droplets vanish and only<br />
few droplets have finite size. The Sauter mean diameter of this distribution decreases<br />
to 99.381 µm after 50 s of d 2 law evaporation rate (see the last column in Tab. 4.2).<br />
Figure 4.8 shows the plots of droplet velocities subjected to only drag force (left),<br />
and drag force with gravity (right) for three different sized droplets, respectively. In<br />
case of only drag caused by the surrounding gas with initial velocity of 0.078 m/s (experimental<br />
value), the velocity decreases at first due to drag force and later the droplets