Figure 3 illustrates another heater assembly which was used for
observing the behavior of liquid droplets on the heater surface. A Pyrex
block shaped into an anomalous prism configuration was substituted for
the copper block. An 18 mm * 18 mm area in the top surface was plated with
a thin transparent ITO (indium tin oxide) film which could serve as the
source of Joule-heat generation. Since the electric resistance of the ITO
film linearly increases with an increase in temperature, the heater surface
temperature could be evaluated by measuring the resistance of the ITO film.
Every experiment with this glass-prism heater was performed under a steady
thermal condition in contrast with the experiments with the copper-block
heater. Procedure |
The volume flux data thus obtained are plotted in Fig. 4 against
the radial distance from the center of the heater surface. It is found
that the volume flux under each prescribed condition is nearly uniform
within a radius of some 15 mm of the center but significantly radius-dependent
over a peripheral region. Thus, the volume flux averaged over the area
within 15-mm radius is used as Dm, the nominal spray volume flux, in this
paper. |
Table 1 Experimental Spray Parameters
Coolant |
Nozzle |
Liquid pressure (MPa) |
Flow rate (cm3/s) |
Spray volume flux Dm(m3/m2・s) |
Droplet dia. dm(μm) |
Droplet velocity Vm(m/s) |
We |
Water |
TG-0.3 |
0.394 |
4.08 |
1.35×10-4 |
68 |
5.6 |
30 |
Water |
TG-0.4 |
0.196 |
3.90 |
1.42×10-4 |
92 |
5.1 |
33 |
Water |
TG-0.4 |
0.394 |
5.50 |
1.97×10-4 |
60 |
5.8 |
28 |
Water |
TG-2 |
0.098 |
12.43 |
3.70×10-3 |
386 |
10.8 |
622 |
FC-72 |
TG-0.3 |
0.296 |
2.20 |
2.25×10-4 |
60 |
5.8 |
283 |
FC-72 |
TG-0.4 |
0.196 |
3.90 |
2.17×10-4 |
54 |
2.8 |
59 |