本實驗以FC-72 為工作流體,進行小間隙兩端封閉水平狹窄矩形 空間的飽和池沸騰實驗,分析在不同的間隙與不同的可溶解氣體含量 對起始過熱度、沸騰曲線以及臨界熱通量的影響。
以下是本實驗所歸納的結果:
1. 在未加入可溶解氣體(Cg=0)時,在低熱通量,間隙 S=3mm、S=2mm 與S=1mm 熱傳係數相差不多。在高熱通量 S=3mm 有最高的熱傳 係數,且臨界熱通量隨著間隙增大而增高。
2. 在加入可溶解氣體(Cg=0.0029)時,在低熱通量,間隙 S=3mm 有 最大的熱傳係數。在高熱通量,也是間隙S=3mm 有最高的熱傳係 數,而在臨界熱通量也隨著間隙增大而增高。
3. 相同間隙下,可以發現在低熱通量時有加入可溶解氣體時熱傳係 數都較佳。加入可溶解氣體時的臨界熱通量都比未加入可溶解氣 體時高,大約增高10%~45%。但是加入微量可溶解氣體對於抑制 溫度偏移情形沒有幫助,在兩種可溶解氣體含量下,在間隙S=3mm 與S=2mm 皆可觀察到溫度偏移。
本實驗在有加入可溶解氣體的情況下熱傳係數皆高於未加入可 溶解氣體時。若繼續增加可溶解氣體含量或更改加熱面構造,熱傳係 數以及臨界熱通量使否能向上提升,或者使得溫度偏移現象消失,這
些都值得後續相關研究。
附錄
B. 熱損失q"loss,由2.4 節得
參考文獻
1. McAdams, W. H., Kennel, W. E., Minden, C. S., Carl R., Picornell, P.
M., and Dew, J. E., 1949, “Heat Transfer at High Rates to Water With Surface Boiling”, Industrial and Engineering Chemistry, Vol. 41, No.
9.
2. Pike, F. p., Miller, P. D., Jr., and Beatty K. O., Jr., 1955, “Effect of Gas Evolution on Surface Boiling at Wire Coils”, Chem. Engrg. Prog.
Symp. Series, Vol. 51, No. 17, pp. 13-19.
3. Behar, M., Courtaud, M., Ricque, R., and Semeria, R., 1966,
“Fundamental Aspects of Subcooled Boiling With and Without Dissolve Gasses” , Proc. 3rd Int. Heat Trans. Conf., Vol. IV, pp. 1-11.
4. Nukiyama, S., 1934, “The maximum and Minimum Value of Heat Transfer from Metal to Boiling Water under Atmosphere Pressure”, Int.
J. Heat Mass Transfer, Vol.9, pp. 1419-1433.
5. Volmer, 1945, “M. Kinetik der Phasenbildung”, Edwards Bros., Ann Arbor.
6. You, S.M., Simon, T.W., Bar-Cohen, A., Hong, Y.S., 1995, “Effect of dissolved gas content on pool boiling of a highly wetting fluid”, J.
Heat Transfer 117, pp. 687-692.
7. O’Connor, J.P., You, S.M., Chang, J.Y., 1996, “Gas-saturated pool boiling heat transfer from smooth and micro porous surfaces in FC-72”, J. Heat Transfer 118, pp. 662-667.
8. Hong, Y.S., Ammerman, C. N., and You, S.M., “Boiling Characteristics of Cylindrical Heaters in Saturated, Gas Saturated, and Pure- Subcooled FC-72”, J. Heat Transfer 119, pp. 313-318.
9. You, S.M., Simon, T.W., Bar-Cohen, A., 1995, “Experriments on Nucleate Boiling Heat Transfer with a Highly-Wetting Dielectric Fluid:Effect of Pressure, Subcooling and Dissolved Gas Content”, J.
Heat Transfer 118, pp. 564-571.
10.Fujiia, M., Nashiyama, E., Yamanaka, G., 1979, “Nucleate Pool Boiling Heat Transfer from Micro-porous Heating Surface:, Advances in Enhanced Heat Transfer”, ASME, pp. 45-51.
11.Nishikawa, K., Fujita, Y., Uchida, S., and Ohta, H., 1994, “Effect of Surface Configuration on Nucleate Boiling Heat Transfer”, Int. J. Heat and Mass Transfer, v.27, pp. 1559-1571.
12.Aderson, T. M., Mudawar, I., 1989, ”Microelectronic Cooling by Enhanced Pool Boiling of A Dielectric Fluorocarbon Liquid”, J. heat transfer, vol. 111, pp. 752-759.
13.You, S. M., Bar-Cohen, A. and Simon, T. W., 1990, "Boiling Incipience and Nucleate Boiling Heat Transfer of Highly-Wetted Dielectric Fluids From Electronic Materials", InterSociety Conference on Thermal Phenomena
14.Rohsenow, W. M., 1952, “A Method of Correlating Heat Transfer Data for Surface Boiling of Liquids”, Trans. ASME, Vol. 174, pp.969-975.
15.Mikic, B. B., Bohsenow, W. M., 1969, “A New Correction of Pool Boiling Data Including the Effect Surface Characterfistics”, J. of Heat Transfer, pp. 245-250.
16.Bonjour, Jocelyn, Clausse, Marc and Lallemand, Monique, 2000,
“Experimental Study of The Coalescence Phenomenon During Nucleate Pool Boiling”, Experimental Thermal and Fluid Science, v.
20, pp.180-187.
17.Gu, J. M., Lu, M., 1999, “The New Assumption for Calculating Heat Transfer in Pool Boiling”, Heat and Mass Transfer, v.35, pp.295-297.
18.Arik,M., Bar-Cohen, A., 1998, “Immersion Cooling of High Heat Flux Microelectronics with Dielectric Liquids.” International Symposium on Advanced Packaging Materials, pp. 229-247.
19.Bar-Cohen, A., 1992, “State-of-the Art and Trends in the Thermal Packaging of the Electronic Equipment”, J. Electronic Packaging, V.114, pp. 257-270.
20.Oktay, S., 1994, “Beyond Thermal Limits in the Computers Systems”, Kluwer Academic Public, Dor drecht.
21.Isaacson, E., and Isaacson, N., 1975, “Dimensional Method in Engineering and Physics”, Edward Arnold, London.
22.Katto, Y., 1978, “Generalized Correlations for Critical Heat Flux of Natural Convection Boiling in Confined”, Trans. FSME, vol.44, pp.
3908-3911
23.Yao, S. C., and Chang, Y., 1983, “Pool Boiling Heat Transfer in a Confined Space”, Int. J. Heat Mass Trans., v.26, pp. 841-847.
24.Misale, M., Guglielmini, G., Frogheri, M., and Bergles, A.E., 1999,
“FC-72 Pool Boiling from Finned Surfaces Placed in a Narrow Channel:Preliminary Result”, Heat and Mass Transfer, v.34, pp.
449-452.
25.陳文忠, 2002, “Study of Pool Boiling of Dielectric Fluid FC-72 Between Two Plates”, 國立交通大學碩士論文
26.張妤綺, 2003, “Study of Boiling of Dielectric Fluid FC-72 in a Narrow Rectangular Space”, 國立交通大學碩士論文
27.3M Company, Physical Properties Data, 2002, Private Communication, Katoka Japan.
28.Kline, S. J., 1985, “The Purpose of Uncertainty Analysis”, J. Fluids Engineering, v.107, pp. 153-160.