| 研究生: |
陳軍豪 Chen, Jun-hao |
|---|---|
| 論文名稱: |
根據實驗溫度量測值估算散熱鰭片於濕空氣下之熱傳特性 Estimation of Heat Transfer Characteristics on a Wet Fin using Experimental Temperature Data |
| 指導教授: |
陳寒濤
Chen, Han-taw |
| 學位類別: |
碩士 Master |
| 系所名稱: |
工學院 - 機械工程學系 Department of Mechanical Engineering |
| 論文出版年: | 2007 |
| 畢業學年度: | 95 |
| 語文別: | 中文 |
| 論文頁數: | 100 |
| 中文關鍵詞: | 鰭片高度 、鰭片效率 、強制對流 、鰭片間距 |
| 外文關鍵詞: | fin spacing, fin height, fin efficiency, forced convection |
| 相關次數: | 點閱:221 下載:1 |
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本文乃以有限差分法(Finite difference method)並配合最小平方法(Least-squares scheme)及溫度量測值來估算不同風速於溼空氣下之散熱鰭片的平均熱傳係數(Average heat transfer coefficient)、總熱傳量(Total heat transfer rate)和鰭片效率(Fin efficiency)。鰭片上的熱傳係數是非均勻的,為了預測鰭片上之熱傳係數,因此將鰭片分割成數個小區域,並假設每個區域上之熱傳係數為常數。
於強制對流條件下,平均熱傳係數會隨著風速和鰭片高度增加而增加,而鰭片效率會隨著風速增加而減少。於相同風速下,平均熱傳係數會隨著鰭片間距的增大而減少並趨近於單一鰭片之值。結果顯示於強制對流(Forced convection)之環境下,鰭片間距與鰭片高度對本文預測值的影響不容忽視。而為了驗証本文反算法之準確性及合理性,本文之強制對流之平均熱傳係數的預測值將與相關文獻作比較。
The present study applies the finite difference method in conjunction with the least-squares scheme and measured temperatures to estimate the average convection heat transfer coefficient, total heat transfer rate and fin efficiency on a wet fin for various air speeds. The heat transfer coefficient on this rectangular fin is non-uniform. Thus the whole plate fin is divided into sub-fin regions in order to predict the average heat transfer coefficient on a wet fin. The average convection heat transfer coefficient on those sub-fin regions is assumed to be constant.
The average heat transfer coefficient increases with increasing the air speed and the fin height, and the fin efficiency decreases with increasing the air speed for various fin spacing in forced convection. The average heat transfer coefficient decreases with increasing the fin spacing for a fixed air speed. It can also approach its corresponding asymptotical value obtained from a single fin for the fin spacing above a certain value. The effects of the fin spacing and fin height on the present estimates can not be negligible in forced convection. A comparison of the forced convection heat transfer coefficient between the present estimates and previous results is made in order to evidence the accuracy and reliability of the present inverse scheme.
[1] D.R. Haper and W.B. Brown, “Mathematical equations for heat conduction in the fins of air cooled engines,” N. A. C. A. Rept, pp. 158, 1922.
[2] T.E. Schmidt, “Heat transfer calculations for extended surfaces,” Refrigerating Engineering, pp. 351-357, 1949.
[3] W. Elenbaas, “The heat dissipation of parallel plates by free convection,” Physica, 1 pp. 1-28, 1942.
[4] W. Elenbaas, “The dissipation of heat by free convection-the inner surfaces of vertical tubes of different shapes of cross section,” Physica, 8 pp. 865-874, 1942.
[5] S. Ostrach, “Laminar natural-convection flow and heat transfer of fluids with and without heat sources in channels with constant wall temperatures,” NACA Tech. Note2863, 1952.
[6] J.R. Bodoia and J.F. Osterle, “The development of free convection between heated vertical plates,” ASME J. Heat transfer, Vol. 84 pp. 40-44, 1962.
[7] H. Zarbronsky, “Efficiency of a heat exchanger using square fins on round tube,” Carbide and carbon Chemical Company, K-25 Plant Oak Ridge,Tennessee. August 15, 1952.
[8] L.T. Chen, “Two-dimensional fin efficiency with combined heat and mass transfer between water-wetted fin surface and moving moist airstream,” Int. J. Heat Fluid Flow, Vol. 12, pp. 71-76, 1991.
[9] S.Y. Liang, T.N. Wong, and G.K. Nathan, “Comparision of one-dimensional and two-dimensional models for wet-srface fin efficiency of a plate-fin-tube heat exchanger,” Appl. Therm. Eng., Vol. 20, pp. 941-962, 2000.
[10] A. Besednjak, and A. Poredos, “Efficiency of cooled cooled extended surfaces,” Int. J. Refrig., Vol. 21, pp. 372-380, 1998.
[11] A.V. Chizhov, and K. Takayama, “The impact of compressible liquid droplet on hot rigid surface,” Int. J. Heat and Mass Transfer, Vol. 47, pp. 1391-1401, 2004.
[12] R.P. Selvam, L. Lin, and R. Ponnappan, “Direct simulation of spray cooling:Effect of vapor bubble growth and liquid droplet impact on heat transfer,” Int. J. Heat and Mass Transfer, Vol. 49, pp. 4265-4278, 2006.
[13] M.E. Goldstein, W. Yang, and J.A. Clark, “Momentum and Heat Transfer in Laminar Flow of Gas with Liquid-Droplet Suspension Over a Circular Cylinder,” J. Heat Transfer, 89C, pp. 185-194, 1967.
[14] I.L. Maclaine-Cross, and P.J. Banks, “Coupled Heat and Mass Transfer in Regenerators-prediction Using an Analogy with Heat Transfer,” J. of Heat Transfer, Vol. 15, pp. 1225-1242, 1972.
[15] I.L. Maclaine-Cross, and P.J. Banks, “A General Theory of Wet Surface Heat Exchangers and its Application to Regenerative Evaporative Cooling,” J. of Heat Transfer, Vol. 103, pp. 579-585, 1981.
[16] W.M. Yan, “Effects of Film Vaporization on Turbulent Mixed Convection Heat and Mass Transfer in a Vertical Channel,” Int. J. Heat and Mass Transfer, Vol. 38, No. 4, pp. 713-722, 1995.
[17] L.C. Chow, D.E. Tilton, and M.R. Pais, “High Power Density Spray Cooling,” WRDC-TR-89-2082, Wright Laboratory, OH, 1989.
[18] S.S. Hsieh, T.C. Fan, and H.H. Tsai, “Spray cooling characteristics of water and R-134a. Part II: transient cooling,” Int. J. Heat and Mass Transfer, Vol. 47, pp. 5713-5724, 2004.
[19] E.A. Silk, J. Kim, and K. Kiger, “Spray cooling of enhanced surfaces: Impact of structured surface geometry and spray axis inclination,” Int. J. Heat and Mass Transfer, Vol. 49, pp. 4910-4920, 2006.
[20] S.C. Yao, and C.C. Hsieh, “Evaporative heat transfer characteristics of a water spray on micro-structured silicon surfaces,” Int. J. Heat and Mass Transfer, Vol. 49, pp. 962-974, 2006.
[21] J.R. Rybicki, and I. Mudawar, “Single-phase and two-phase cooling characteristics of upward-facing and downward-facing sprays,” Int. J. Heat and Mass Transfer, Vol. 49, pp. 5-16, 2006.
[22] M. Ghodbane, and J.P. Holman, “Experimental Study of Spray Cooling with Freon-113,” Int. J. Heat and Mass Transfer, Vol. 34, pp. 1163-1174, 1991.
[23] S.S. Hsieh, and C.H. Tien, “R-134a spray dynamics and impingement cooling in the non-boiling regime,” Int. J. Heat and Mass Transfer, Vol. 50, pp. 502-512, 2007.
[24] H.T. Chen, J.P. Song, and Y.T. Wang, “Prediction of heat transfer coefficient on the fin inside one-tube plate finned-tube heat exchangers,” Int. J. Heat and Mass Transfer, Vol. 48, pp. 2697-2707, 2005.
[25] H.T. Chen, and J.C. Chou, “Investigation of natural-convection heat transfer coefficient on a vertical square fin of finned-tube heat exchangers,” Int. J. Heat and Mass Transfer, Vol. 49, pp. 3034-3044, 2006.
[26] 王宏志,“利用逆運算法並配合溫度量測值預測結露時之平板鳍管式熱交換器的熱傳性質,” 國立成功大學機械工程研究所, 碩士論文,2006.
[27] A. Bejan, “Heat Transfer,”John Wiley & Sons, Inc., New York, pp. 53-62, 1993.
[28] T.V. Jones, C.M.B. Russell, “Efficiency of rectangular fins,” ASME/AIChE National Heat Transfer Conference, Orlando, Florida, pp. 27-30, 1980.
[29] F.E.M. Saboya, E.M. Sparrow, “Local and average heat transfer coefficients for one-row plate fin and tube heat exchanger configurations,” ASME Journal of Heat Transfer, Vol. 96, pp.265-272, 1974.
[30] Y.T. Lin, K.C. Hsu, Y.J. Chang, and C.C. Wang, “Performance of rectangular fin in wet conditions: visualization and wet fin eifficiency,” ASME, J. Heat Transfer, Vol. 123, pp. 827-836, 2001.
[31] C.N. Lin, and J.Y. Jang, “A two-dimensional fin efficiency analysis of combined heat and mass transfer in elliptic fins,” Int. J. Heat and Mass Transfer, Vol. 45, pp. 3839-3847, 2002.
[32] V.S. Arpaci, “Introduction to Heat Transfer, ” pp. 580, 1999.
[33] 王啟川, “熱交換器設計(I) ,”五南圖書出版有限公司, 2003.
[34] J.E.R. Coney, C.G.W. Sheppard, and E.A.M. Shafei, “Fin performance with dehumidification form humid air: a numerical investigation,”Int. J. Heat and Fluid Flow., Vol. 10, pp. 224-231, 1989.
[35] S.N. Kondepudi, and D.L. O’Neal, “Performance of finned tube heat exchangers under frosting condition: Ⅱ. Comparison of experimental data with model,” Rev. Int. Froid., Vol. 16, pp. 181-184, 1993.
[36] 劉立熙,“以反算法配合溫度量測值預測矩形鳍片上之熱物理量,” 國立成功大學機械工程研究所, 碩士論文, 2007.