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研究生: 呂世婷
Lu, Shih-Ting
論文名稱: 多孔性除濕輪體氣流特性分析
Analysis of Air Flow Characteristics of Porous Desiccant Wheel
指導教授: 李旺龍
Li, Wang-Long
學位類別: 碩士
Master
系所名稱: 工學院 - 材料科學及工程學系
Department of Materials Science and Engineering
論文出版年: 2021
畢業學年度: 109
語文別: 中文
論文頁數: 98
中文關鍵詞: 除濕輪 、氧化鋁 、多孔介質
外文關鍵詞: desiccant wheel, alumina, porous media
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  • 轉輪式乾燥機使用吸附能力佳之材料作為除濕輪,並以此作為吸附劑吸收潮濕空氣中的水分。當潮濕的室內空氣進入除濕輪後,除濕輪會吸附其中的水分,因此通過除濕輪後,空氣中的水分含量較低,然而吸附劑具有吸附容量的限制,吸附一定重量的水後將失去吸附功能,此時除濕輪另一側會通過高溫且相對濕度較低的氣流,並將除濕輪中的水分帶走,使其重新回到乾燥狀態繼續吸附潮濕空氣中的水分。
    然而氣流間會產生交互作用,導致溫度與水氣在不同氣流間傳遞,使原本向出口移動的乾燥氣流受到水分含量較多的氣流影響,致使乾燥效果不如預期,相對濕度較低的高溫氣流則會將熱量傳遞給乾燥後的氣流,使其溫度升高,若需要除濕的對象為熱敏感物質,則會對其造成損毀,而原本相對濕度較低的高溫氣流降溫後,飽和含水量也隨之下降,使相對濕度增加,因此對除濕輪的乾燥能力也會下降,使除濕輪中殘留較多水氣,降低除濕效率。
    為了避免上述情況,本文建立乾燥機模型,對流速分佈與溫度分佈進行分析,並探討不同操作條件(如:除濕輪孔隙、孔徑、出口流速等)對流速與溫度造成的影響,研究成果將有利於未來設計乾燥機。

    There will be an interaction between the airflows in air-drying machine, resulting in the transfer of temperature and moisture between different airflows. First, if water from wet air diffuses to air which is dried by desiccant wheel, drying efficiency will be less than expected. Second, heat will transfer to dry air flow from air flow with high temperature, making its temperature increases. If there is a heat-sensitive material in the room, it may be damaged by this reason. In order to have deep understanding of the above problems, this research uses the finite element method to simulate the airflow characteristics in the air-drying machine. The major of the analysis results can be summarized into the following conclusions: (1) When the porosity decreases, the velocity of the air flow will decrease, and easily flow to the outlet duct on the same side. (2) When the temperature difference between the two airflows is small, the airflow velocity will decrease, and the velocity distribution in the desiccant wheel will be relatively smooth and will not change drastically.

    摘要 I Extended Abstract II 誌謝 X 目錄 XI 表目錄 XIV 圖目錄 XV 符號總表 XVIII 第一章 緒論 1 1.1 前言 1 1.2文獻回顧 3 1.2.1 孔隙流體之流動特性 3 1.2.2 多孔介質流體流動模型 4 1.2.3 多孔介質熱傳研究 7 1.3 研究動機與目的 12 1.4 論文架構 12 第二章 研究理論 15 2.1 質量守恆方程式 16 2.2 動量守恆方程式 17 2.3 Navier-Stokes方程式 18 2.4 多孔介質相關理論 20 2.4.1 孔隙率(Porosity) 20 2.4.2 達西定律與滲透率(Permeability) 20 2.4.3 Modified Navier-Stokes方程式 25 2.5 溫度場基本理論 25 2.5.1 熱傳導(Thermal Conduction)定律 25 2.5.2 熱對流(Heat Convection)定律 26 2.6 能量守恆方程式 27 2.6.1 固體能量守恆方程式 27 2.6.2 流體能量守恆方程式 28 第三章 數值分析 31 3.1 有限元素法 31 3.2 幾何模型建立與材料參數 32 3.3 邊界條件設定 34 3.3.1 流場的邊界條件 34 3.3.2 溫度場的邊界條件 34 3.3.3 Newton-Raphson法 35 3.4 模擬分析流程 37 3.5 網格測試 38 第四章 結果與討論 40 4.1 氣流特性驗證 40 4.2多孔介質內氣流特性之分析 47 4.2.1 孔隙率對氣流特性之影響 48 4.2.2 除濕輪與風管間距及孔隙率對氣流特性之影響 62 4.2.3 氣流出口流速之影響 69 4.2.4 孔隙率及氣流出口流速對溫度及流速分佈之影響 75 4.2.5 除濕輪孔徑對氣流特性之影響 79 4.2.6 除濕輪厚度之影響 83 4.2.7 除濕輪進氣溫度對氣流特性之影響 87 第五章 結論與未來展望 91 5.1 結論 91 5.2 未來展望 92 參考文獻 93

    [1] Gibson, L. J., Ashby, M. F., & Harley, B. A, Cellular materials in nature and medicine. Cambridge University Press., 2010.
    [2] Friedheim, J., Guo, Q., Young, S., & Gomez, S. Testing and evaluation techniques for drilling fluids-shale interaction and shale stability. In 45th US Rock Mechanics/Geomechanics Symposium. OnePetro, 2011.
    [3] Ongaro, F., De Falco, P., Barbieri, E., & Pugno, N. M. Mechanics of filled cellular materials. Mechanics of Materials, 97, 26-47, 2016.
    [4] Weiss, F., Cai, S., Hu, Y., Kyoo Kang, M., Huang, R., & Suo, Z. Creases and wrinkles on the surface of a swollen gel. Journal of Applied Physics, 114(7), 073507, 2013.
    [5] Garcia-Moreno, F., Mukherjee, M., Solórzano, E., & Banhart, J. Metal foams–towards microcellular materials. International journal of materials research, 101(9), 1134-1139, 2010.
    [6] Park, G. G., Yang, T. H., Yoon, Y. G., Lee, W. Y., & Kim, C. S. Pore size effect of the DMFC catalyst supported on porous materials. International Journal of Hydrogen Energy, 28(6), 645-650, 2013.
    [7] Hammel, E. C., Ighodaro, O. R., & Okoli, O. I. Processing and properties of advanced porous ceramics: An application based review. Ceramics International, 40(10), 15351-15370, 2014.
    [8] Zotov, R., Meshcheryakov, E., Livanova, A., Minakova, T., Magaev, O., Isupova, L., & Kurzina, I. Influence of the composition, structure, and physical and chemical properties of aluminium-oxide-based sorbents on water adsorption ability. Materials, 11(1), 132, 2018.
    [9] Meshcheryakov, E. P., Reshetnikov, S. I., Sandu, M. P., Knyazev, A. S., & Kurzina, I. A. Efficient Adsorbent-Desiccant Based on Aluminium Oxide. Applied Sciences, 11(6), 2457, 2021.
    [10] Chant, E. E.; Jeter, S. M. On the Use of the Parabolic Concentration Profile Assumption for a Rotary Desiccant Dehumidifier. Journal of Solar Energy Engineering, 117(1), 45–50, 1995.
    [11] Sutera, S. P., & Skalak, R. The history of Poiseuille's law. Annual review of fluid mechanics, 25(1), 1-20, 1993.
    [12] Darcy, H. Les fontaines publiques de la ville de Dijon: exposition et application... Victor Dalmont, 1856.
    [13] Hazen, A. Some physical properties of sand and gravel with special reference to their use in filtration. 24th Ann, Rep., Mass. State Board of Health, Boston, 1983.
    [14] Forchheimer, P. Wasserbewegung durch boden. Z. Ver. Deutsch, Ing., 45, 1782-1788, 1901.
    [15] E. Krüger. Die Grundwasserbewegung. Internationale Mitteilungen für Bodenkunde, p. 105, 1918.
    [16] Brinkman, H. C. A calculation of the viscous force exerted by a flowing fluid on a dense swarm of particles. Flow, Turbulence and Combustion, 1(1), 27-34, 1949.
    [17] Nield, D. A. The limitations of the Brinkman-Forchheimer equation in modeling flow in a saturated porous medium and at an interface.International Journal of Heat and Fluid Flow, 12(3), 269-272, 1991.
    [18] Kim, S. Y., Kang, B. H., & Hyun, J. M. Heat transfer from pulsating flow in a channel filled with porous media. International journal of heat and mass transfer,37(14), 2025-2033, 1994.
    [19] Vafai, K., & Kim, S. On the limitations of the Brinkman-Forchheimer-extended Darcy equation. International Journal of Heat and Fluid Flow,16(1), 11-15, 1995.
    [20] Ergun, S. Fluid flow through packed columns. Chem. Eng. Prog.,48, 89-94, 1952.
    [21] Dukhan N. Analysis of Brinkman-extended Darcy flow in porous media and experimental verification using metal foam[J]. Journal of Fluids Engineering, 134: 1201-1206, 2012.
    [22] Irmay, S. Theoretical models of flow through porous media, RILEM Symp. Transfer of Water in porous media, Paris. Bull. RILEM,29, 37-43, 1964.
    [23]Macdonald, I. F., El-Sayed, M. S., Mow, K., & Dullien, F. A. L. Flow through porous media-the Ergun equation revisited. Industrial & Engineering Chemistry Fundamentals, 18(3), 199-208, 1979.
    [24] Fand, R. M., Kim, B. Y. K., Lam, A. C. C., & Phan, R. T. Resistance to the flow of fluids through simple and complex porous media whose matrices are composed of randomly packed spheres, 1987.
    [25] Comiti, J., & Renaud, M. A new model for determining mean structure parameters of fixed beds from pressure drop measurements: application to beds packed with parallelepipedal particles. Chemical Engineering Science, 44(7), 1539-1545, 1989.
    [26] Kececioglu, I., & Jiang, Y. Flow through porous media of packed spheres saturated with water, 1994.
    [27] Vafai, K., & Tien, C. L. Boundary and inertia effects on flow and heat transfer in porous media. International Journal of Heat and Mass Transfer, 24(2), 195-203, 1981.
    [28] Maxwell, J. C. A Treatise on Electricity and Magnetism, Vol. I, 3rd Edition, 1954.
    [29] Qian, J., Li, Q., Yu, K., & Xuan, Y. A novel method to determine effective thermal conductivity of porous materials. Science in China Series E: Technological Sciences, 47(6), 716-724, 2004.
    [30] Froment, G. F., Bischoff, K. B., & De Wilde, J. Chemical reactor analysis and design(Vol. 2). New York: Wiley, 1990.
    [31] Dixon, A. G., DiCostanzo, M. A., & Soucy, B. A. Fluid-phase radial transport in packed beds of low tube-to-particle diameter ratio. International Journal of Heat and Mass Transfer, 27(10), 1701-1713, 1984.
    [32] Vafai, K., Alkire, R. L., & Tien, C. L. An experimental investigation of heat transfer in variable porosity media, 1985.
    [33] Vafai, K., & Kim, S. J. Forced convection in a channel filled with a porous medium: an exact solution. ASME J. Heat Transfer, 111(4), 1103-1106, 1989.
    [34] Chikh, S., Boumedien, A., Bouhadef, K., & Lauriat, G. Analytical solution of non-Darcian forced convection in an annular duct partially filled with a porous medium. International Journal of Heat and Mass Transfer, 38(9), 1543-1551, 1995.
    [35] Lee, D. Y., & Vafai, K. Analytical characterization and conceptual assessment of solid and fluid temperature differentials in porous media. International Journal of Heat and Mass Transfer, 42(3), 423-435, 1999.
    [36] Mohamad AA. Heat transfer enhancements in heat exchangers fitted with porous media, Part I:constant wall temperature[J]. International Journal of Thermal Sciences, 42: 385–395, 2003.
    [37] Haddad, O. M., Al-Nimr, M. A., & Al-Omary, J. S. Forced convection of gaseous slip-flow in porous micro-channels under Local Thermal Non-Equilibrium conditions. Transport in porous media, 67(3), 453-471, 2007.
    [38] Haddad O M, Al-Nimr M A, Sari M S. Forced convection gaseous slip flow in circular porous micro-channels[J]. Transport in Porous Media, 70(2):167-179, 2007.
    [39] Aydın, O., & Avcı, M. On the constant wall temperature boundary condition in internal convection heat transfer studies including viscous dissipation. International communications in heat and mass transfer, 37(5), 535-539, 2010.
    [40] A. Holm, A. Johannes, and K. Wolfgang, Mechanics of Composite Structural Elements, Singapore Pte Ltd: Springer Nature, 2018.
    [41] Laskar, I. I., Hashisho, Z., Phillips, J. H., Anderson, J. E., & Nichols, M. Modeling the effect of relative humidity on adsorption dynamics of volatile organic compound onto activated carbon. Environmental science & technology, 53(5), 2647-2659, 2019.
    [42] R. Anderson, S. Shiri, H. Bindra, J.F. Morris. Experimental results and modeling of energy storage and recovery in a packed bed of alumina particles. Appl. Energy, 119, pp. 521-529, 2014.
    [43] Cheng, D., Peters, E. F., & Kuipers, J. H. Numerical modelling of flow and coupled mass and heat transfer in an adsorption process. Chemical Engineering Science, 152, 413-425, 2016.
    [44] Newton, I. The Method of Fluxions and Infinite Series: With Its Application to the Geometry of Curve Lines. Nourse, 1736.
    [45] J. Raphon. Analysis Aeuationum, 1692.
    [46] Shallcross, D. Handbook of Psychrometric Charts: Humidity diagrams for engineers. Springer Science & Business Media, 2012.

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