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作者(中文):陳威甫
作者(外文):Chen, wei fu
論文名稱(中文):利用計算流體力學模擬評估不規則填充物
論文名稱(外文):Evaluation of Random Packings by Using CFD Simulation
指導教授(中文):鄭西顯
指導教授(外文):Jang, Shi Shang
口試委員(中文):汪上曉
陳榮輝
吳煒
口試委員(外文):Wong,Shan Hill
Chen, Jung hu
Wu, wei
學位類別:碩士
校院名稱:國立清華大學
系所名稱:化學工程學系
學號:103032501
出版年(民國):105
畢業學年度:104
語文別:中文
論文頁數:51
中文關鍵詞:填充物模擬接觸面積雙向流流體體積法計算流體力學
外文關鍵詞:PackingSimulationInterfacial areaCountercurrent flowVolume of fluid methodComputational fluid dynamics(CFD)
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在燃燒後捕捉製程中,常使用二氧化碳吸收塔進行碳捕獲。因此,如何減少碳捕獲的成本為一重要課題。在傳統二氧化碳吸收技術上,捕獲設備體積龐大是造成碳捕獲成本高的主要原因之一,由於氣液體質傳效率低造成需使用龐大設備體積來彌補質傳效率的問題。近年來,許多的二氧化碳捕獲製程的研究,均朝向如何改善吸收塔質傳效率改善的議題。吸收塔中的氣液接觸面面積是最重要的質傳參數,也因此氣液接觸面面積最受關注。
本研究提出以數個非實質上隨意排列的不規則填料推疊模型,取代隨意堆疊不規則填料之流場,利用計算流體力學(computational fluid dynamics, CFD)模擬方法評估填充物結構,模擬氣液雙向流在填料間的三維數值模擬,使用流體體積方法(volume of fluid, VOF)探討氣液體接觸面積與持液率(liquid holdup)在流場內部的情形與變化。並以流體體積方法來捕捉氣液交界面之移動。模擬結果顯示氣液接觸面積和持液率皆會隨著液體進口速度增加而增加。為了驗證模擬結果的準確性,將模擬結果與文獻關係式比較,結果顯示兩者之結果相當相近,證實了本模型的可行性。因此,本研究提出了一個可行之研究方法能有效地用來模擬隨意堆疊不規則填料之流場。
Post-combustion capture processes by using CO2 absorber are considered one of the options for Carbon Capture. Consequently, how to reduce CO2 capture cost is an important issue. Huge volume of the absorption equipment is the main cause of high CO2 capture cost. Traditional CO2 absorption equipment has drawback of huge volume, mainly because of the low gas-liquid mass transfer efficiency. That led to use volume of equipment to make up the problem of mass transfer efficiency. In recent years, there has been many studies of CO2 capture process toward improvement of absorber mass transfer efficiency. It is shown that the most important mass-transfer parameter is the interfacial area, hence, it has been deeply concerned.
In the present study, we propose an approach by arranging several artificial models randomly to substitute the real random packing fields. To begin with, we use CFD simulation to evaluate packing structure, with a focus on parameters such as the interfacial areas and liquid holdups. Three dimensional numerical simulations of gas-liquid countercurrent flow in random packings are performed. Interfacial areas and liquid holdups are investigated using the volume of fluid method. Moreover, the VOF method is used to capture the gas–liquid interface motion. Results show that interfacial areas and liquid holdups increase with increasing liquid flow rates. In order to validate the accuracy of our model, the simulations results are compared to several correlations from literatures, and find that our simulation result is analogous to the ones in the literature, which indicates our model is reliable. As a result, this work shows how our method can be used as an effective tool to simulate and provide related information on random packing fields.
摘要 i
Abstract ii
目錄 iii
圖目錄 vi
表目錄 viii
第一章 緒論 1
1.1研究背景 1
1.2文獻回顧 5
1.2.1填充物介紹 5
1.2.2不規則填料 5
1.2.3環型填料 6
1.2.4規則填料 7
1.2.5 CFD模擬軟體應用於填充物構型設計 8
1.3研究動機與目的 13
第二章 研究方法 14
2.1模擬簡介 14
2.2數值方法介紹 15
2.3統御方程式 18
2.3.1質量守恆方程式 18
2.3.2動量守恆方程式 18
2.3.3能量守恆方程式 19
2.3.4體積分率方程式 19
2.3.5紊流方程式 20
2.3.6狀態方程式 20
2.3.7表面張力 20
2.4流場幾何 21
2.4.1填充物堆疊方法 25
2.5邊界條件 26
2.6網格切割 26
第三章 模擬驗證分析 28
3.1模擬前處理建模 28
3.2流體物理性質設定 29
3.3邊界條件設定 29
3.4數值模擬設定流程 30
3.4.1前處理部分 30
3.4.2 FLUENT部分 31
3.4.3後處理部分 31
3.5實驗結果 31
3.6實驗驗證 33
第四章 模擬結果 36
4.1氣相體積百分率結果 36
4.2液體進口流速對氣液接觸面積之影響 37
4.3氣液接觸面積與文獻驗證比較結果 39
4.4液體進口流速對持液率之影響 42
4.5持液率與文獻驗證比較結果 43
第五章 結論 46
參考文獻 47

[1] J. Albo, P. Luis, and A. Irabien, "Carbon dioxide capture from flue gases using a cross-flow membrane contactor and the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate," Industrial & Engineering Chemistry Research, vol. 49, pp. 11045-11051, 2010.
[2] T. H. Oh, "Carbon capture and storage potential in coal-fired plant in Malaysia—A review," Renewable and Sustainable Energy Reviews, vol. 14, pp. 2697-2709, 2010.
[3] G. T. Rochelle, "Amine scrubbing for CO2 capture," Science, vol. 325, pp. 1652-1654, 2009.
[4] P. Feron, "Progress in post-combustion CO2 capture," in First Regional Carbon Management Symposium,(May) Dhahran,Saudi Arabia, 2006.
[5] T. Yokoyama, "Japanese R&D on large-scale CO2 capture," presented at the Seperations Technology VI:New Perspective on Very Large-Scale Operations, Kingfisher Resort, Fraser Island, Queensland, Australia, 2006.
[6] N. McDowell, N. Florin, A. Buchard, J. Hallett, A. Galindo, G. Jackson, C. S. Adjiman, C. K. Williams, N. Shah, and P. Fennell, "An overview of CO2 capture technologies," Energy & Environmental Science, vol. 3, pp. 1645-1669, 2010.
[7] J. Chen, C. Liu, X. Yuan, and G. Yu, "CFD simulation of flow and mass transfer in structured packing distillation columns," Chinese Journal of Chemical Engineering, vol. 17, pp. 381-388, 2009.
[8] M. Haghshenas Fard, M. Zivdar, R. Rahimi, M. Nasr Esfahani, A. Afacan, K. Nandakumar,and KT. Chuang, "CFD simulation of mass transfer efficiency and pressure drop in a structured packed distillation column," Chemical Engineering & Technology, vol. 30, pp. 854-861, 2007.
[9] A. Hoffmann, I. Ausner, J. U. Repke, and G. Wozny, "Fluid dynamics in multiphase distillation processes in packed towers," Computers & Chemical Engineering, vol. 29, pp. 1433-1437, 2005.
[10] S. A. Owens, M. R. Perkins, R. B. Eldridge, K. W. Schulz, and R. A. Ketcham, "Computational fluid dynamics simulation of structured packing," Industrial & Engineering Chemistry Research, vol. 52, pp. 2032-2045, 2013.
[11] M. R. Khosravi Nikou and M. R. Ehsani, "Turbulence models application on CFD simulation of hydrodynamics, heat and mass transfer in a structured packing," International Communications in Heat and Mass Transfer, vol. 35, pp. 1211-1219, 2008.
[12] L. Raynal and A. Royon-Lebeaud, "A multi-scale approach for CFD calculations of gas–Liquid flow within large size column equipped with structured packing," Chemical Engineering Science, vol. 62, pp. 7196-7204, 2007.
[13] B. Szulczewska, I. Zbicinski, and A. Gorak, "Liquid flow on structured packing: CFD simulation and experimental study," Chemical Engineering & Technology, vol. 26, pp. 580-584, 2003.
[14] A. Gorak and Z. Olujic, Distillation: Equipment and Processes: Academic Press, 2014.
[15] W. L. McCabe, J. C. Smith, and P. Harriott, Unit Operations of Chemical Engineering vol. 5: McGraw-Hill New York, 1956.
[16] R. Billet and M. Schultes, "Prediction of mass transfer columns with dumped and arranged packings: updated summary of the calculation method of Billet and Schultes," Chemical Engineering Research and Design, vol. 77, pp. 498-504, 1999.
[17] Q. Li, W. Ma, and Z. Zhang, "Research and development trend of column packing," Chemical Industry and Engineering Process, vol. 24, pp. 619-624, 2005.
[18] 莊維鈞, 雷良恒, and 劉茂林, 化工原理: 清華大學出版社, 1993.
[19] Y. Don, "現代填料塔技術(一)塔填料的發展和選擇," Chemical Production and Technology, pp. 16-27, 1996.
[20] S. Sunder, H. C. Klotz, and G. A. Meski, "Optimal corrugated structured packing," US 6,357,728, 2003.
[21] J. F. Billingham and M. J. Lockett, "Packing with improved capacity for rectification systems," 5,632,934, 1997.
[22] M. J. Lockett and J. F. Billingham, "Structured packing with asymmetric crimp pattern," US 6,314,756, 2001.
[23] J. Hodson, J. Fletcher, and K. Porter, "Fluid mechanical studies of structured distillation packings," in Institution of Chemical Engineers Symposium Series, 1997, pp. 999-1007.
[24] C. van Gulijk, "Using computational fluid dynamics to calculate transversal dispersion in a structured packed bed," Computers & Chemical Engineering, vol. 22, pp. S767-S770, 1998.
[25] J. M. Van Baten and R. Krishna, "Liquid-phase mass transfer within KATAPAK-S® structures studied using computational fluid dynamics simulations," Catalysis Today, vol. 69, pp. 371-377, 2001.
[26] J. M. Van Baten, J. Ellenberger, and R. Krishna, "Radial and axial dispersion of the liquid phase within a KATAPAK-S® structure: experiments vs. CFD simulations," Chemical Engineering Science, vol. 56, pp. 813-821, 2001.
[27] J. M. van Baten, and R. Krishna, "Gas and liquid phase mass transfer within KATAPAK-S® structures studied using CFD simulations," Chemical Engineering Science, vol. 57, pp. 1531-1536, 2002.
[28] M. Klöker, E. Kenig, and A. Górak, "On the development of new column internals for reactive separations via integration of CFD and process simulation," Catalysis Today, vol. 79, pp. 479-485, 2003.
[29] M. Klöker, E. Y. Kenig, R. Piechota, S. Burghoff, and Y. Egorov, "CFD‐based study on hydrodynamics and mass transfer in fixed catalyst beds," Chemical Engineering & Technology, vol. 28, pp. 31-36, 2005.
[30] Y. Egorov, F. Menter, M. Klöker, and E. Kenig, "On the combination of CFD and rate-based modelling in the simulation of reactive separation processes," Chemical Engineering and Processing: Process Intensification, vol. 44, pp. 631-644, 2005.
[31] C. F. Petre, F. Larachi, I. Iliuta, and B. Grandjean, "Pressure drop through structured packings: Breakdown into the contributing mechanisms by CFD modeling," Chemical Engineering Science, vol. 58, pp. 163-177, 2003.
[32] F. Larachi, C. F. Petre, I. Iliuta, and B. Grandjean, "Tailoring the pressure drop of structured packings through CFD simulations," Chemical Engineering and Processing: Process Intensification, vol. 42, pp. 535-541, 2003.
[33] L. Raynal, C. Boyer, and J. P. Ballaguet, "Liquid holdup and pressure drop determination in structured packing with CFD simulations," The Canadian Journal of Chemical Engineering, vol. 82, pp. 871-879, 2004.
[34] P. Zhang, C. Liu, X. Yuan, G. Yu, and K. Yu, "CFD simulations of liquid phase flow in structured packed column," Journal of Chemical Industry and Engineering(China), vol. 55, pp. 1369-1373, 2004.
[35] I. Iliuta and F. Larachi, "Mechanistic model for structured-packing-containing columns: irrigated pressure drop, liquid holdup, and packing fractional wetted area," Industrial & Engineering Chemistry Research, vol. 40, pp. 5140-5146, 2001.
[36] Y. Yuan, M. Han, D. Wang, and Y. Jin, "Experimental and CFD analysis of two-phase cross/countercurrent flow in the packed column with a novel internal," Chemical Engineering Science, vol. 60, pp. 6210-6216, 2005.
[37] F. Gu, X. G. Yuan, and G. C. Yu, "CFD simulation of liquid film flow on inclined plates," Chemical Engineering & Technology, vol. 27, pp. 1099-1104, 2004.
[38] Y. Xu, S. Paschke, J. U. Repke, J. Yuan, and G. Wozny, "Computational approach to characterize the mass transfer between the counter-current gas-liquid flow," Chemical Engineering & Technology, vol. 32, pp. 1227-1235, 2009.
[39] Y. Xu, J. Yuan, J. U. Repke, and G. Wozny, "CFD study on liquid flow behavior on inclined flat plate focusing on effect on flow rate," Engineering Applications of Computational Fluid Mechanics, vol. 6, pp. 186-194, 2012.
[40] P. Valluri, O. K. Matat, G. F. Hewitt, and M. A. Mendes, "Thin film flow over structured packings at moderate Reynolds numbers," Chemical Engineering Science, vol. 60, pp. 1965-1975, 2005.
[41] Y. Haroun, L. Raynal, and D. Legendre, "Mass transfer and liquid hold-up determination in structured packing by CFD," Chemical Engineering Science, vol. 75, pp. 342-348, 2012.
[42] J. Chen, C. Liu, Y. Li, Y. Huang, X. Yuan, and G. Yu, "Experimental investigation of single-phase flow in structured packing by LDV*," Chinese Journal of Chemical Engineering, vol. 15, pp. 821-827, 2007.
[43] A. Ataki and H. J. Bart, "Experimenatal and CFD simulaition study for the wetting of a structured packing element with liquids," Chemical Engineering & Technology, vol. 29, pp. 336-347, 2006.
[44] Y. Haroun, L. Raynal, and P. Alix, "Prediction of effective area and liquid hold-up in structured packings by CFD," Chemical Engineering Research and Design, vol. 92, pp. 2247-2254, 2014.
[45] D. A. Pham, Y. Lim, H. Jee, E. Ahn, and Y. Jung, "Porous media Eulerian computional fluid dynamics(CFD) model of amine absorber with structured-packing for CO2 removal," Chemical Engineering Science, vol. 132, pp. 259-270, 2015.
[46] ANSYS fluent theory guide: ANSYS, Inc., 2013.
[47] S. V. Patankar and D. B. Spalding, "A calcualation procedure for heat,mass and ,momentum transfer in three-dimensional parabolic flows," International Journal of Heat and Mass Transfer, vol. 15, pp. 1787-1806, 1972.
[48] D. S. Jang, R. Jetli, and S. Acharya, "Comparison of the PISO,SIMPLER and SIMPLEC algorithms for the treatment of the pressure-velocity coupling in steady flow problems," Numerical Heat Transfer, vol. 10, pp. 209-228, 1986.
[49] J. U. Brackbill, D. B. Kothe, and C. Zemach, "A continuum method for modeling surface tension," Journal of Computational Physics, vol. 100, pp. 335-354, 1993.
[50] R. B. Bird, W. E. Stewart, and E. N. Lightfoot, Transport Phenomena: John Wiley & Sons, Inc, 2005.
[51] K. Onda, H. Takeuchi, and Y. Okumoto, "Mass transfer coefficients between gas and liquid phases in packed columns," Journal of Chemical Engineering of Japan, pp. 56-62, 1968.
[52] R. Billet and M. Schultes, "Predicting mass trasnfer in packed columns," Chemical Engineering & Technology, vol. 16, pp. 1-9, 1993.
[53] J. L. Bravo and J. R. Fair, "Generallzed correlation for mass transfer in packed distillation columns," Industrial & Engineering Chemistry Process Design and Development, vol. 21, pp. 162-170, 1982.
[54] L. Stichlmair, J. L. Bravo, and J. R. Fair, "General model for prediction of pressure drop and capacity of countercurrent gas/liauid packed columns," Gas Separation & Purification, vol. 3, pp. 19-28, 1989.

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