| 研究生: |
王彰鍵 Wang, Chang-Chien |
|---|---|
| 論文名稱: |
封閉腔體內之高溫差自然對流研究 Numerical Simulation of Natural Convection in Enclosure with Large Temperature Difference |
| 指導教授: |
王振源
Wang, Chen-Yuan |
| 學位類別: |
碩士 Master |
| 系所名稱: |
工學院 - 航空太空工程學系 Department of Aeronautics & Astronautics |
| 論文出版年: | 2004 |
| 畢業學年度: | 92 |
| 語文別: | 中文 |
| 論文頁數: | 111 |
| 中文關鍵詞: | 自然對流 、理想氣體 |
| 外文關鍵詞: | Rayleigh Benard, PISO, Ideal gas, Boussinesq fluid |
| 相關次數: | 點閱:89 下載:6 |
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本研究是封閉腔體內之高溫差自然對流。在左右腔壁溫差的方形腔體,以Boussinesq流體與理想氣體流體作模擬,當使用Boussinesq流體模擬時,等溫線與流線呈左右反對稱,在冷熱壁面的溫度梯度相等。當使用理想氣體流時,於低溫差腔體,冷熱壁面的溫度梯度相等,於高溫差腔體,冷壁面的溫度梯度大於熱壁面的溫度梯度,且高溫差的封閉腔體,壓力隨著腔體內氣體能量增加而升高。在研究中比較相同Ra時,高溫差在冷壁面的溫度梯度大於低溫差在冷壁面的溫線梯度,在熱壁面則相反。高溫差的流線較低溫差的流線偏右下方。
在Rayleigh-Benard問題,長寬比為25,壓力隨著腔體內的能量增加,直到近似穩態,壓力呈些微的振盪。Ra大於14590時,流場隨著時間改變的暫態現象,其暫態現象是無週期性,旋轉數隨著Ra增加而減少。在Ra=14590時,旋轉數約為12~16個。在Ra=136700時,旋轉數約為8~10個。
The objective of this thesis is to study natural convection in enclosure with large temperature difference. Comparisons between results with ideal gas and Boussinesq fluid have been made. In the large temperature difference, the isotherms near the cold wall is denser than that in the realm of hot wall. This study focus on comparing the streamline of diverse temperature difference in the same Rayleigh number. The streamline moves toward the direction of cold wall, and the rolls change the form when increasing the temperature difference of left-right wall.
The other topic is Rayleigh-Benard problem. The pressure increases with the energy of the air of cavity, until quasi-steady the amplitude of the pressure with time is small. In this research aspect ratio is 25, the stream of cavity which has no period, changes with time. The numbers of rolls decrease with increasing Rayleigh number. When the temperature difference is 1000K, the difference of Nusselt number in the realm of cold wall is twice of that in the realm of hot wall, that stand for the different temperature gradient in the realm of wall.
[1] J.P. Abraham and E.M. Sparrow, “Three-dimensional lamminar and turbulent natural convection in a continuously/discretely wall heated enclosure containing a thermal load,”Numerical Heat Transfer, part A, Vol. 44, pp. 105-125, 2003.
[2] I.E. Barton, “Comparison of SIMPLE- and PISO-type algorithms for transient flows,” International Jounal for Numerical Methods in Fluids, Vol. 26, pp. 459-483, 1998.
[3] B.A. Befrui and A.D. Gosman, “EPISO-An implicit non-iterative solution procedure for the calculation of flows in reciprocating engine chambers,” Computer Methods in Applied Mechanics and Engineering, Vol. 79, pp. 279-279, 1990.
[4] R.L. Burden and J.D. Faires, Numerical Analysis, seventh edition, Brooks Cole, 2001.
[5] C.H. Cheng and K.S. Hung, “Numerical predictions of flow and thermal fields in a reciprocating piston-cylinder assembly,” Numerical Heat Transfer, Part A. Vol. 38, pp. 397-421, 2000.
[6] G. De Vahl Davis, “Natural convection of air in a square cavity: A bench mark numerical solution,” International Journal for Numerical Methods in Fluids, Vol. 3, pp. 249-264, 1983.
[7] B. Gebhart, Y. Jaluria, R.L. Mahajan, and B. Sammakia, Buoyancy-induced Flows and Transport, Hemisphere, 1988.
[8] D.D. Gray and A. Giorgini, “The validity of the Boussinesq approxination for liquids and gas,” International Journal of Heat and Mass Transfer, Vol. 19, pp. 545-551, 1976.
[9] M. Hortmann and M. Peric and G. Scheuerer, “Finite volume multigrid prediction of laminar natural convection,” International Journal for Numerical Method in Fluid, Vol. 11, 189-207, 1990.
[10] K.S. Hung and C.H. Cheng, “Pressure effects on natural convection for non-Boussinesq fluid in a rectangular enclosure,” Numerical Heat Transfer, Part A, Vol. 41, pp. 515-528, 2002.
[11] C.Y. Han and S.W. Back, “The effects of radiation on natural convection in rectangular enclosure divided bt two partitions,” Numerical Heat Transfer, part A, Vol. 37, pp. 249-270, 2000.
[12] K.G.T. Hollands and G.D. Raithby, Handbook of Heat Transfer Fundamentals, McGraw-Hill, New York, 1985.
[13] R.I. Issa, “Solution of the implicitly discretised fluid flow equations by operator-splitting,” Journal of Computational Physics, Vol. 62, pp. 40-65, 1984.
[14] S. Kakac and Y. Yener, Convective Heat Transfer, Second edition, CRC Press, Boca Raton, 1995.
[15] S.L. Lee and R.Y. Tzong, “Artificial pressure for preesure-link equation,” International Journal of Heat and Mass Transfer, Vol. 35, No.10, pp.2705-2716, 1992.
[16] D. Mukutmoni and K.T. Yang, “Thermal convection in small enclosures : an atypical bifurcation sequence,” International Journal of Heat and Mass Transfer, Vol. 38, pp. 113-126, 1995.
[17] D. Mukutmoni and K.T. Yang, “Pattern selection for Rayleigh-Benard convection in intermediate aspect ratio boxes,” Numerical Heat Transfer, Part A, Vol. 27, pp. 621-637, 1995.
[18] D. Mishra, K. Muralidhar, P. Munshi, “Experimental study of Rayleigh-Benard convection at intermediate Rayleigh numbers using interferometric tomopraphy,” Fluid Dynamics Research, Vol. 25, pp. 231-255, 1999.
[19] P.J. Oliveira and R.I. Issa, “An improved PISO algorithms for the computation of bouyancy-driven flows,” Numerical Heat Transfer, Part B, Vol. 40, pp. 473-493, 2001.
[20] S. Ostrach, “Natural convection in enclosure,” Advances in Heat Transfer, Vol. 8, pp. 161-226, 1972.
[21] S.V. Patankar, Numerical Heat Transfer and Fluid Flow, Hemisphere Publishing Corporation, 1980.
[22] E.M. Sparrow and J.P. Abraham, “A new buoyancy model replacing the standard pseudo-density difference for internal natural convection in gas,” International Journal of Heat and Mass Transfer, Vol. 46, pp. 3583-3591, 2003.