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1
2 A A A
3 1. 3
4 4 1.1 CPU
5 5 1.2
6 2. 6
7 7 2.1 Fig. 2.1 CHF MHF CHF Fig. 2.1 Boiling curve.
8 8 2.2 [1] hr λ f l = = ( f f X ) 3 ( ) ( ) p ( p/p ) s p 3 c a 1+3( pa 3 c ) p p /p X ( )( ) 1 c ρ 2 2 pl 1 2 λ1σρv v 1 2 = qr M P h q = 34.8 T 3 q T
9 3. 9
10 Fig. 3.1 Fig. 3.1 Experimental apparatus.
11 Fig. 3.2 Fig. 3.2 Boiling cell.
12 Fig. 3.3 Fig. 3.4 Fig W 20W CPU Fig W 1.5 Fig. 3.3 Optical setup. Fig. 3.4 Optical system. Fig. 3.5 Power meter. Fig. 3.6 Diode laser.
13 NEC TH3102MR Fig µm 3.00 msec / line 0.75 sec / page mm FASTCAM-Net Max frame / sec 1000 frame / sec Pixel S-VHS HVC-SL Fig frame / sec 10 sec Fig. 3.7 Radiation thermometer. Fig. 3.8 High speed video camera.
14 µm Si 15 mm nm 10 µm Table 3.1 Fig. 3.9 Table 1 Fig Table 3.1 Cavity pattern. S S1 1 mm S2 2 mm HC 4 mm Honeycomb 7 S20 20 µm Fig. 3.9 Mask pattern. Fig Adapter for heated surface.
15 15 DRIE 2 inch 3 µm / min µm Fig S=20 µm µm a b c d 0.5 µm 80 µm b DRIE 0.1 µm a b c d Fig Magnification of cavities.
16
17 4. 17
18 Fig. 4.1 Fig Fig mm
19 19 Fig. 4.1 Gaussian distribution. [W] Current [A] Fig. 4.2 Average laser power. Before Cutting After Cutting
20 Fig. 4.3 Fig Fig sec
21 21 Fig. 4.3 Temperature data-1. Fig. 4.4 Temperature data-2. Fig. 4.5 Temperature data-3.
22 frame / sec 1000 frame / sec 10 msec 100 msec Fig. 4.6 S1 S2 S1 Fig. 4.7 Fig. 4.6 Top view of boiling surface. Fig. 4.7 Method of observing bubbles.
23 5. 23
24 S1 S1 Fig. 5.1 a 23 b 34 c cm 2 aheat Flux kw / m 2 bheat Flux kw / m 2 cheat Flux kw / m Fig. 5.1 Bubbling from cavities.s1
25 S2 S2 Fig. 5.2 S1 S cm 2 aheat Flux kw / m 2 bheat Flux kw / m 2 cheat Flux kw / m Fig. 5.2 Bubbling from cavities.s2
26 HC HC Fig. 5.3 S1 S cm 2 aheat Flux kw / m 2 bheat Flux kw / m 2 cheat Flux kw / m Fig. 5.3 Bubbling from cavities.hc
27 S20 S20 Fig cm 2 aheat Flux kw / m 2 bheat Flux kw / m 2 cheat Flux kw / m Fig. 5.4 Bubbling from cavities. S20
28 S1S S1 Fig. 5.5 S1 1 mm a 5 mm S1
29 aheat Flux kw / m bheat Flux kw / m 2 2 cheat Flux kw / m dheat Flux kw / m Fig. 5.5 Bubble departing number.s1
30 S S=1 mm d Fig. 5.6 S1 5 mm 6 mm S S1 Mean number of departing bubbles Distance [mm] Fig. 5.6 Distribution of bubbling frequency.
31 S2 Fig. 5.7 S1 S2 S2
32 aheat Flux kw / m bheat Flux kw / m 2 cheat Flux kw / m 2 dheat Flux kw / m 2 eheat Flux kw / m Fig. 5.7 Bubble departing number.s2
33 S1 S2 2 Fig. 5.8 S1 S2 S1 S2 4 S S=2mm S=1mm Heat Flux [kw/m 2 ] Fig. 5.8 Total bubbling number.
34 S1S2 Judd [2] S2 D 1 S d S e S1S2 Fig. 5.9 Fig S1 D= 5 mm 2 mm D=6 mm 4060 msec S2 S2 D S1 S1 S2 5.2
35 35 Frequency of Occurrences 10 Frequency of Occurrences Elapsed Time [msec] Elapsed Time [msec] Distance 2 mm Distance 2 mm Frequency of Occurrences 10 Frequency of Occurrences Elapsed Time [msec] Elapsed Time [msec] Distance 5 mm Distance 10 mm Frequency of Occurrences 10 Frequency of Occurrences Elapsed Time [msec] Elapsed Time [msec] Distance 29 mm Distance 6 mm Fig. 5.9 Distribution of elapsed time.s1
36 36 Frequency of Occurrences 10 Frequency of Occurrences Elapsed Time [msec] Distance 2 mm Elapsed Time [msec] Distance 2 2 mm Frequency of Occurrences 10 Frequency of Occurrences Elapsed Time [msec] Distance 4 mm Elapsed Time [msec] Distance 2 5 mm Fig Distribution of elapsed time.s2
37 S20 xy log-log 2.2 Fig S1S2HC S2 HC S1 2 S1S2 HC 2 S1 S2 50 kw / m S2 S1
38 38 Heat flux [kw/m 2 ] Nishikawa Fujita HC S2 S1 Natural Convection Superheat [] Fig Boiling curve
39 S1 S2 HC S20 HCS= 4 mm 7 S20S=20 µm 5.4
40 6 40
41 41 S=4mm S=1mmS=2mm S=1mm S=2mm S=2mm S=1mm
42 A 42
43 43 R [ mm ] P [W ] M [m -1 ] f s f p C pl [J/kgK] l [kg/m 3 ] σ λ l [W/mK] v [kg/m 3 ] g h v [J/m 3 ] p c
44 A S1 S
45 45 Bubble Departing Timesec Heated Surface S1 Water Condition Saturated Heat Flux 23.81kW/m
46 46 Bubble Departing Timesec Heated Surface S1 Water Condition Saturated Heat Flux 27.11kW/m
47 47 Bubble Departing Timesec Heated Surface S1 Water Condition Saturated Heat Flux 30.37kW/m
48 48 Bubble Departing Timesec Heated Surface S1 Water Condition Saturated Heat Flux 33.6kW/m
49 49 Bubble Departing Timesec Heated Surface S2 Water Condition Saturated Heat Flux 17.6kW/m
50 50 Bubble Departing Timesec Heated Surface S2 Water Condition Saturated Heat Flux 21.18kW/m
51 51 Bubble Departing Timesec Heated Surface S2 Water Condition Saturated Heat Flux 24.76kW/m
52 52 Bubble Departing Timesec Heated Surface S2 Water Condition Saturated Heat Flux 27.94kW/m
53 53 Bubble Departing Timesec Heated Surface S2 Water Condition Saturated Heat Flux 31.12kW/m
54 54
55 55
56 56 [1] K.Nishikawa and Y.Fujita, "Correlation of Nucleate Boiling Heat Transfer Based on Bubble Population Density," International Journal of Heat and Mass Transfer vol.20, p.233 (1977) [2] Robert Mallozzi, Ross Leonard Judd, Narayanaswamy Balakrishnan, "Interaction of randomness, overlap and the interaction of bubbles forming at adjacent nucleation sites in pool boiling," International Journal of Heat and Mass Transfer 43 (2000) [3] Sushil H. Bhavnani, "Immersion-Cooled Heat Sinks for Electronics: Insight from High-Speed Photography," IEEE Transactions on Components and Packaging Technologies,vol.24,No.2,June [4] Yuto Takagi, Masahiro Shoji, "Bubbling features from a single artificial cavity, " International Journal of Heat and Mass Transfer 44 (2001) [5],", 1999.
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