| 研究生: |
黃建霖 Huang, Jian-Lin |
|---|---|
| 論文名稱: |
橢圓管外之紊流薄膜凝結分析 Analyses of Turbulent Film Condensation on Elliptic Tube |
| 指導教授: |
陳朝光
Chen, Chao-Kuang |
| 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: | 2022 |
| 畢業學年度: | 110 |
| 語文別: | 中文 |
| 論文頁數: | 55 |
| 中文關鍵詞: | 紊流 、薄膜 、凝結 、橢圓 |
| 外文關鍵詞: | turbulent, film, condensation, ellipse |
| 相關次數: | 點閱:78 下載:12 |
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本文應用數值方法對具有外部流之橢圓管外的紊流薄膜凝結進行分析。為了簡化數學模型以利於計算,在橢圓的幾何形體上並非使用圓形的極座標(r,θ)來進行運算,而是採用以橢圓偏心率表示之橢圓座標,在方程式的運算上應用了庫爾本類比(Colburn Analogy)來預估汽液界面之摩擦阻力再藉此估算出剪應力,並且使用Kato之紊流模式結合Myong之紊流普朗特數來建立紊流渦流擴散率,外部流場則是採用potential flow theory,而在數值運算的方法上則是採用具高收斂性的二分法(Bisection Method)。
此外,本文將統御方程式進行無因次化後可以透過橢圓偏心率、福祿數、界面剪力參數、普朗特數以及過冷效應等無因次參數,分析紊流薄膜凝結的薄膜厚度、速度分布、溫度梯度及溫度分布、局部熱傳率還有平均熱傳率,了解參數與結果間的關係,並在偏心率為零之圓管特例與相關文獻對比,藉此對方法的可行性以及結果的準確性進行驗證。
而從研究結果中可以了解,液膜膜厚會隨著過冷效應參數、普朗特數以及福祿數的增加而上升,但會因為偏心率的提高而減少。局部熱傳率則是隨著福祿數、普朗特數以及界面剪力參數的提高而上升,但會隨著過冷效應數參數的增加而減少。而平均熱傳率則是隨著界面剪力參數、福祿數以及普朗特數的提高而上升,但會隨著橢圓偏心率以及過冷效應參數的提高而減少。
This research analyzes the problem of turbulent film condensation on the elliptical tube with external flow. To simplify the mathematical model, the coordinates are represented by the ellipse eccentricity, and the Colburn analogy is used to estimate the frictional resistance. And use Kato's turbulent model and Myong's turbulent Prandtl number model to establish the eddy diffusivity, and the external flow uses the potential flow, and the numerical method is Bisection Method which have high convergence and haven’t initial value problem. And investigate the condensation film thickness, velocity distribution, temperature gradient, temperature distribution, local and mean heat transfer coefficient by ellipse eccentricity, Froude number, interfacial shear parameter, Prandtl number, and sub-cooling parameter. Show the relationship between the parameter and result, and verify the accuracy of the model by comparing it with related research.
The results show that the film thickness gets higher by the higher sub-cooling parameter, Prandtl number, Froude number, and interfacial shear parameter, lower ellipse eccentricity. The local heat transfer coefficient gets higher by the Froude number, Prandtl number, and interfacial shear parameter, the lower sub-cooling parameter. The mean heat transfer coefficient gets higher by the interfacial shear parameter, Froude number, and Prandtl number, the lower ellipse eccentricity and the sub-cooling parameter. And the present study has a high similarity with past studies.
[1] Faghri, A., Zhang, Y. "Condensation. In: Fundamentals of Multiphase Heat Transfer and Flow. ", Cham,Springer International Publishing:355-414,2020.
[2] Wang, J., et al., "Direct contact condensation of steam jet in subcooled water: A review. ", Nuclear Engineering and Design 377:111-142,2021.
[3] Wang, X., Xu, B., Chen, Z., et al., "Review of droplet dynamics and dropwise condensation enhancement: Theory, experiments and applications.", Advances in Colloid and Interface Science 305:102684,2022.
[4] Tan, B. et al., "Experimental and theoretical study of vapor/air mixture condensation inside an inclined blind-end pipe in natural convection with considering fog formation.", Int. J. of Heat and Mass Transfer 184:122375,2022.
[5] Nusselt, W.,"The surface condensation of water vapour.", Zeitschrift Des Vereines Deutscher Ingenieure 60: 541-546,1916.
[6] Gregorig, R., et al., "Improved correlation of film condensation data based on a more rigorous application of similarity parameters.", Wärme - und Stoffübertragung 7: 1-13,1974.
[7] Rohsenow, W.M., "Heat Transfer and Temperature Distribution in Laminar-Film Condensation.", Transactions of the American Society of Mechanical Engineers 78(8): 1645-1647,1956.
[8] Sparrow, E.M. and Gregg, J.L., "A Boundary-Layer Treatment of Laminar-Film Condensation.", J. of Heat Transfer 81(1): 13-18,1959.
[9] Chen, M. M., "An Analytical Study of Laminar Film Condensation: Part 1—Flat Plates.", J. of Heat Transfer 83(1): 48-54,1961.
[10] Koh, J. C. Y., "An Integral Treatment of Two-Phase Boundary Layer in Film Condensation.", J. of Heat Transfer 83(3): 359-362,1961.
[11] Sugawara, S., et al., "The condensation of vapour flowing normal to a horizontal pipe.", Proc. 6th Jap. Nat. Cong. App. Mech, Paper 3-4, pp.385,1956.
[12] Le Fevre, E. J. and Mandelsweig, S. I., "The effect of vertically downward velocity on the heat transfer from stream-nitrogen mixtures condensing on a horizontal cylinder.”, MSc Thesis, Univ. London,1960.
[13] Mayhew, Y. and Aggarwal, J., "Laminar film condensation with vapour drag on a flat surface.", Int. J. of Heat and Mass Transfer 16(10): 1944-1949, 1973.
[14] Nicol, A. and Wallace, D. "Condensation with appreciable vapor velocity and variable wall temperature. ", Symp. on Steam Turbine Condensers,1976.
[15] Nobbs, D. W., "The effect of downward vapor velocity and inundation on the condensation rates on horizontal tubes and tube banks", University of Bristol, 1975.
[16] Asano, K., et al., "Forced convection film condensation of vapors in the presence of noncondensable gas on a small vertical flat plate.", J. of Chemical Engineering of Japan 12(3): 196-202,1979.
[17] South, V., III and Denny, V. E., "The Vapor Shear Boundary Condition for Laminar Film Condensation.", J. of Heat Transfer 94(2): 248-249,1972.
[18] Cess, R. D., "Laminar-film condensation on a flat plate in the absence of a body force.", Zeitschrift für angewandte Mathematik und Physik ZAMP 11(5): 426-433,1960.
[19] Koh, J., "Film condensation in a forced-convection boundary-layer flow.", Int. Journal of Heat and Mass Transfer 5(10): 941-954,1962.
[20] Shekriladze, I. G. and V. Gomelauri., "Theoretical study of laminar film condensation of flowing vapor.", Int. J. of Heat and Mass Transfer 9(6): 581-591,1966.
[21] Denny, V. E. and Mills, A. F., "Laminar Film Condensation of a Flowing Vapor on a Horizontal Cylinder at Normal Gravity.", J. of Heat Transfer 91(4): 495-501,1969.
[22] Jacobs, H. R., "An integral treatment of combined body force and forced convection in laminar film condensation.", Int. J. of Heat and Mass Transfer 9(7): 637-648,1966.
[23] Fujii, T. and. Uehara, H., "Laminar film condensation on a vertical surface.", Int. J. Heat Mass Transfer 15: pp.217-233,1972.
[24] Gaddis, E., "Solution of the two phase boundary-layer equations for laminar film condensation of vapour flowing perpendicular to a horizontal cylinder.", Int. J. of Heat and Mass Transfer 22(3): 371-382,1979.
[25] Fujii, T., et al., "Condensation of steam on a horizontal tube-the influence of oncoming velocity and thermal condition at the tube wall.", Condensation Heat Transfer: 35-43,1979.
[26] Lee, W. C. and Rose, J. W., "Film condensation on a horizontal tube-effect of vapour velocity, ", Int. Heat Transfer Conference Digital Library, Begel House Inc,1982.
[27] Truckenbrodt, E., "Ein einfaches Näherungsverfahren zum Berechnen der laminaren Reibungsschicht mit Absaugung.", Forschung auf dem Gebiete des Ingenieurwesens 22(5): 147-157,1956.
[28] Dhir, V. and Lienhard, J., "Laminar Film Condensation on Plane and Axisymmetric Bodies in Nonuniform Gravity.", J. of Heat Transfer 93(1): 97-100,1971.
[29] Karimi, A. "Laminar film condensation on helical reflux condensers and related configurations.", Int. J. of Heat and Mass Transfer 20(11): 1137-1144,1977.
[30] Ali, A. and McDonald, T.W., "Laminar film condensation on horizontal elliptical cylinders: A first approximation for condensation on inclined tube.", ASHRAE Trans. 83,No.2: 242-249,1977.
[31] Cheng, S. and Tao, J., "Study of condensation heat transfer for elliptical pipes in a stationary saturated vapor.", ASME J. Heat Transfer 96: 405-408,1988.
[32] Wang, J. C. Y., Ma, Y. and Liu, J., "Vapor condensation on a horizontal elliptical tube.", Proceedings of the XVIIIth International Congress of Refrigeration Paper No. 160,1991.
[33] Fieg, G. P. and Roetzel, W., "Calculation of laminar film condensation in/on inclined elliptical tubes.", Int. J. of Heat and Mass Transfer 37(4): 619-624,1994.
[34] Yang, S.A. and Chen, C.K., "Filmwise condensation on nonisothermal horizontal elliptical tubes with surface tension.", J. of Thermophysics and Heat Transfer 7(4): 729-732,1993.
[35] Yang, S.A. and Chen, C.K.,"Laminar film condensation on a horizontal elliptical tube with uniform surface heat flux and suction at the porous wall.", J. Chinese Society of Mechanical Engineers 14: 93-93,1993.
[36] Panday, P., "Laminar film condensation of downward flowing vapour on a horizontal elliptic cylinder—A numerical solution.", Int. communications in heat and mass transfer 14(1): 33-43,1987.
[37] Yang, S.A. and Hsu, C.H., "Mixed-convection film condensation on a horizontal elliptical tube with uniform surface heat flux.", Numerical Heat Transfer, Part A Applications 32(1): 85-95,1997.
[38] Yang, S.A. and Hsu, C.H., "Mixed-convection film condensation on a horizontal elliptical tube with variable wall temperature.", J. Chinese Society of Mechanical Engineers 20: 373-384,1997.
[39] Memory, S., et al., "Free and forced convection laminar film condensation on horizontal elliptical tubes.", Int. J. of Heat and Mass Transfer 40(14): 3395-3406,1997.
[40] Si, X.. et al., " Laminar film condensation of pseudo-plastic non-Newtonian fluid with variable thermal conductivity on an isothermal vertical plate. ", Int. J. of Heat and Mass Transfer 92: 979-986,2016.
[41] Uehara, H., Kinoshita, E. and Matsuda, S., "Theoretical Study on Turbulent Film Condensation on a Vertical Plate.", ASME/JSME Thermal Engineering Conference 2: 391-397,1995.
[42] Uehara, H., Kinoshita, E. and Matsuda, S., "Wave and turbulent film condensation on a vertical surface (Correlation for average heat-transfer coefficient).", J. of the Japan Society of Mechanical Engineers(B): 616,1997.
[43] Kato H., et al., "On the Turbulent Heat Transfer by Free Convection from a Vertical Plate.", Int. J. Heat Mass Transfer 11: 1117-1125,1967.
[44] Sarma, P. K., et al., "Turbulent film condensation on a horizontal tube with external flow of pure vapors.", Int. J. of Heat and Mass Transfer 41(3): 537-545,1998.
[45] Colburn, A. P., "A method of correlating forced convection heat-transfer data and a comparison with fluid friction.", Int. J. of Heat and Mass Transfer 7(12): 1359-1384,1964.
[46] Michael, A., et al., "Forced convection condensation on a horizontal tube—experiments with vertical downflow of steam.", ASME Journal of Heat Transfer 111: 792-797,1989.
[47] Chen, C.K. and Hu, H.P., "Turbulent film condensation on a half oval body. ", Int. J. of Heat and Mass Transfer 46(22): 4271-4277,2003.
[48] Chen, C.K. and Hu, H.P., "Turbulent film condensation on a horizontal elliptical tube.", ASME Journal of Heat Transfer 125: 1194-1197,2003.
[49] Hiroshi, H., et al., "Effect of vapour velocity on film condensation of R-113 on horizontal tubes in a crossflow.", Int. J. of Heat and Mass Transfer 29(3): 429-438,1986.
[50] Yang, S.A. and Lin, Y.T., "Turbulent film condensation on a non-isothermal horizontal tube—effect of eddy diffusivity.", Applied Mathematical Modelling 29(12): 1149-1163,2005.
[51] Hu, H.P. and Chen, C.K., "Forced Convection in Film Condensation on a Horizontal Elliptical Tube.", Heat Transfer Engineering 27(9): 60-67,2007.
[52] Homescu, D. and Panday, P.K., "Forced Convection Condensation on a Horizontal Tube:Influence of Turbulence in the Vapor and Liquid Phases.", Transactions of the ASME, Transfer 121 (4): 874-885,1999.
[53] Pletcher, R. H., "Prediction of Transpired Turbulent Boundary Layers. ", ASME J. Heat Mass Transfer: 89-94,1974.
[54] Myong, H.K. et al., "Numerical prediction of turbulent pipe flow heat transfer for various Prandtl number fluids with the improved k-ε turbulence model.", Jsme Int.J.ser.ii 32 (4): 613–622,1989.
[55] Lee, Y.W. et al., "A theoretical study of condensation heat transfer in tubes with novel cross-sections. " Thermal Science and Engineering Progress:28:101075,2022.
[56] Bejan, A., "Convection Heat Transfer. ", John Wiley & Sons,New York,2013.
[57] Solanki, C., et al., "Role of bisection method." Int. J. of Computer Applications Technology and Research 3(8):535-535, 2014.
[58] Hilpert, R., "Wärmeabgabe Von Geheizten Drähten.", Forsch Geb Ingenieurwes 4: 220,1933.
[59] Chiou, J. S. and Chang, T.B. , "Laminar film condensation on a horizontal disk. ", Wärme - und Stoffübertragung 29(3):141-4,1994.
[60] Yang, Z. et al., "Convective heat transfer characteristics of high-pressure gas in heat exchanger with membrane helical coils and membrane serpentine tubes.", Experimental Thermal and Fluid Science:35(7):1427-34, 2011