大孔隙率多孔介质内热弥散现象数值模拟

doi:10.3969/j.issn.0438-1157.2014.03.015

化工学报 ›› 2014, Vol. 65 ›› Issue (3): 870-878.DOI: 10.3969/j.issn.0438-1157.2014.03.015

大孔隙率多孔介质内热弥散现象数值模拟

陈仲山, 解茂昭, 刘宏升

大连理工大学能源与动力工程学院, 辽宁大连 116024

收稿日期:2013-06-26 修回日期:2013-11-29 出版日期:2014-03-05 发布日期:2014-03-05
通讯作者: 解茂昭
作者简介:陈仲山（1984—），男，博士研究生。
基金资助:
国家自然科学基金项目（51176021）。

Numerical simulation of thermal dispersion in porous media with large porosity

CHEN Zhongshan, XIE Maozhao, LIU Hongsheng

School of Energy and Power Engineering, Dalian University of Technology, Dalian 116024, Liaoning, China

Received:2013-06-26 Revised:2013-11-29 Online:2014-03-05 Published:2014-03-05
Supported by:
supported by the National Natural Science Foundation of China(51176021).

摘要/Abstract

摘要： 采用Surface Evolver泡沫演化动力学软件构建理想的大孔隙率多孔介质的几何模型：Weaire-Phelan模型。通过对有效热导率的计算，确定了该模型的适用范围。在此基础上优选两组几何参数作为计算依据，流体相分别采用空气和水，固体相为铝T-6201，通过数值模拟，研究了孔径、Darcy速度和流-固热扩散系数比的影响。数值计算结果表明：孔径越小，热弥散效应越强，流体本身的热物性对弥散的影响越明显；横向分量远小于纵向分量。当工质为气体时，横向分量可以忽略不计，最后得到了计算纵向与横向热弥散系数的经验关联式。

关键词: 多孔介质, 数值模拟, 模型, 热弥散, 孔隙率

Abstract: The structure of porous media with large porosity is described by a spatial periodic Weaire-Phelan model, which is built by the Surface Evolver software, and the application range of this model is determined by comparison of experimental data and simulation result for thermal effective conductivity. Based on the model, numerical computations on two specimens, with air and water as working fluids and aluminum T-6201 as solid matrix, are conducted. The effects of working parameters, such as pore size, Darcy velocity and ratio of thermal diffusion coefficient of fluid to solid, on the thermal dispersion are discussed. The simulation result shows that smaller diameter and stronger dispersion result in a more sensible dependency on thermal physical properties. In addition, the transversal component is far smaller than the longitudinal one. Empirical correlations for the longitudinal and transversal thermal dispersion are obtained in term of Peclet number.

Key words: porous medium, numerical simulation, model, thermal dispersion, porosity

中图分类号:

TK124

陈仲山, 解茂昭, 刘宏升. 大孔隙率多孔介质内热弥散现象数值模拟[J]. 化工学报, 2014, 65(3): 870-878.

CHEN Zhongshan, XIE Maozhao, LIU Hongsheng. Numerical simulation of thermal dispersion in porous media with large porosity[J]. CIESC Journal, 2014, 65(3): 870-878.

参考文献 34

[1]	Banhart J. Manufacture, characterization and application of cellular metals and metal foams[J]. Progress in Materials Science, 2001, 46: 559-632
[2]	Zhao C Y. Review on thermal transport in high porosity cellular metal foams with open cells[J]. International Journal of Heat and Mass Transfer, 2012, 55(13/14): 3618-3632
[3]	Dukhan N. Correlations for the pressure drop for flow through metal foam[J]. Experiments in Fluids, 2006, 41(4): 665-672
[4]	Inayat A, Schwerdtfeger J, Freund H, Korner C. Periodic open-cell foams: pressure drop measurements and modeling of an ideal tetrakaidecahedra packing[J]. Chemical Engineering Science, 2011, 66(12): 2758-2763
[5]	Habisreuther P, Djordjevic N, Zarzalis N. Statistical distribution of residence time and tortuosity of flow through open-cell foams[J]. Chemical Engineering Science, 2009, 64(23): 4943-4954
[6]	Singh R, Kasana H S. Computational aspects of effective thermal conductivity of highly porous metal foams[J]. Applied Thermal Engineering, 2004, 24(13): 1841-1849
[7]	Calmidi V V, Mahajan R L. Forced convection in high porosity metal foams[J]. Journal of Heat Transfer, 2000, 122: 557-565
[8]	Calmidi V V, Mahajan R L. The effective thermal conductivity of high porosity fibrous metal foams[J]. Journal of Heat Transfer, 1999, 121: 466-471
[9]	Boomsma K,Poulikakos D, Ventikos Y. Simulations of flow through open cell metal foams using an idealized periodic cell structure[J]. International Journal of Heat and Fluid Flow, 2003, 24(6): 825-834
[10]	Krishnan S, Garimella S V, Murthy J Y. Simulation of thermal transport in open-cell metal foams: effect of periodic unit-cell structure[J]. Journal of Heat Transfer, 2008, 130(2): 024503-1-024503-5
[11]	Lu T J, Stone H A, Ashby M F. Heat transfer in open-cell metal foams[J]. Acta Mater., 1998, 46(10): 3619-3635
[12]	Dukhan N, Chen K C. Heat transfer measurements in metal foam subjected to constant heat flux[J]. Experimental Thermal and Fluid Science, 2007, 32(2): 624-631
[13]	Lu W, Zhao C Y, Tassou S A. Thermal analysis on metal-foam filled heat exchangers(Ⅰ): Metal-foam filled pipes[J]. International Journal of Heat and Mass Transfer, 2006, 49(15/16): 2751-2761
[14]	Zhao C Y, Lu T J, Hodson H P, et al. Natural convection in metal foams with open cells[J]. International Journal of Heat and Mass Transfer, 2005, 48(12): 2452-2463
[15]	Zhao C Y, Lu W, Tassou S A. Thermal analysis on metal-foam filled heat exchangers(Ⅱ): Tube heat exchangers[J]. International Journal of Heat and Mass Transfer, 2006, 49(15/16): 2762-2770
[16]	Slichter C S. Field measurements of the rate of movement of underground waters[R]. United States Geological Survey Water-Supply and Irrigation Paper, 1905
[17]	Aris R. On the dispersion of a solute by diffusion, convection and exchange between phases[J]. Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences, 1959, 252(1271): 538-550
[18]	Aris R. On the dispersion of a solute in a fluid flowing through a tube[J]. Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences, 1956, 235(1200): 67-77
[19]	Hsu C T, Cheng P. Thermal dispersion in a porous medium[J]. Int. J. Heat Mass Transfer, 1990, 33(8): 1587-1597
[20]	Hsiao K T, Advani S G. Modified effective thermal conductivity due to heat dispersion in fibrous porous media[J]. Int. J. Heat Mass Transfer, 1999, 42: 1237-1254
[21]	Moyne C, Didierjean S, Amaral Souto H P, da Silveira O T. Thermal dispersion in porous media: one equation model[J]. Int. J. Heat Mass Transfer, 2000, 43: 3853-3867
[22]	Kuwahara F, Nakayama A. Numerical determination of thermal dispersion coefficients using a periodic porous structure[J]. Journal of Heat Transfer, 1999, 121 (2):160-163
[23]	Pedras M H J, de Lemos M J S. Thermal dispersion in porous media as a function of the solid-fluid conductivity ratio[J]. International Journal of Heat and Mass Transfer, 2008, 51(21/22): 5359-5367
[24]	Shi Junrui(史俊瑞), Li Benwen(李本文), Xu Youning(徐有宁),Xue Zhijia(薛治家),Wang Shuqun(王树群). Flame characteristics for diffusion filtration combustion[J].CIESC Journal(化工学报), 2012, 63(11): 3500-3505
[25]	Delgado J M P Q. A critical review of dispersion in packed beds[J]. Heat and Mass Transfer, 2005, 42(4): 279-310
[26]	Goldsztein G H. Solute transport in porous media: dispersion tensor of periodic networks[J]. Applied Physics Letters, 2007, 91(5): 054101-054103
[27]	Carbonell R G, Whitaker S. Dispersion in pulsed systems(Ⅱ): Theoretical developments for passive dispersion in porous media[J]. Chemical Engineering Science, 1983, 38(11): 1795-1802
[28]	Pinson F, Gregoire O, Quintard M, Simonin O. Modeling of turbulent heat transfer and thermal dispersion for flows in flat plate heat exchangers[J]. International Journal of Heat and Mass Transfer, 2007, 50(7/8): 1500-1515
[29]	Sahraoui M, Kaviany M. Slip and no-slip temperature boundary conditions at interface of porous plain media: convection[J]. International Journal Heat Mass Transfer, 1994, 37(6): 1029-1044
[30]	Didierjean S, Amaral Souto H P, Delannay R, Moyne C. Dispersion in periodic porous media. Experience versus theory for two-dimensional systems[J]. Chemical Engineering Science, 1997, 52(12): 1861-1874
[31]	Krishnan S, Murthy J Y, Garimella S V. Direct simulation of transport in open-cell metal foam[J]. Journal of Heat Transfer, 2006, 128(8): 793-799
[32]	Kaviany M. Principles of Heat Transfer in Porous Media[M]. 2nd ed. New York: Springer, 1995: 121-216
[33]	Bhattacharya A, Calmidi V V, Mahajan R L. Thermophysical properties of high porosity metal foam[J]. International Journal of Heat and Mass Transfer, 2002,45:1017-1031
[34]	Boomsma K, Poulikakos D. On the effective thermal conductivity of a three dimensionally structured fluid-saturated metal foam[J]. International Journal of Heat and Mass Transfer, 2001, 44:827-836

大孔隙率多孔介质内热弥散现象数值模拟

Numerical simulation of thermal dispersion in porous media with large porosity

PDF (PC)

可视化

被引次数

摘要/Abstract

引用本文

使用本文

参考文献 34

相关文章 15

编辑推荐

Metrics

本文评价

[1]	宋嘉豪, 王文. 斯特林发动机与高温热管耦合运行特性研究[J]. 化工学报, 2023, 74(S1): 287-294.
[2]	张思雨, 殷勇高, 贾鹏琦, 叶威. 双U型地埋管群跨季节蓄热特性研究[J]. 化工学报, 2023, 74(S1): 295-301.
[3]	连梦雅, 谈莹莹, 王林, 陈枫, 曹艺飞. 地下水预热新风一体化热泵空调系统制热性能研究[J]. 化工学报, 2023, 74(S1): 311-319.
[4]	金正浩, 封立杰, 李舒宏. 氨水溶液交叉型再吸收式热泵的能量及分析[J]. 化工学报, 2023, 74(S1): 53-63.
[5]	叶展羽, 山訸, 徐震原. 用于太阳能蒸发的折纸式蒸发器性能仿真[J]. 化工学报, 2023, 74(S1): 132-140.
[6]	张义飞, 刘舫辰, 张双星, 杜文静. 超临界二氧化碳用印刷电路板式换热器性能分析[J]. 化工学报, 2023, 74(S1): 183-190.
[7]	王志国, 薛孟, 董芋双, 张田震, 秦晓凯, 韩强. 基于裂隙粗糙性表征方法的地热岩体热流耦合数值模拟与分析[J]. 化工学报, 2023, 74(S1): 223-234.
[8]	王浩, 王振雷. 基于自适应谱方法的裂解炉烧焦模型化简策略[J]. 化工学报, 2023, 74(9): 3855-3864.
[9]	李科, 文键, 忻碧平. 耦合蒸气冷却屏的真空多层绝热结构对液氢储罐自增压过程的影响机制研究[J]. 化工学报, 2023, 74(9): 3786-3796.
[10]	何松, 刘乔迈, 谢广烁, 王斯民, 肖娟. 高浓度水煤浆管道气膜减阻两相流模拟及代理辅助优化[J]. 化工学报, 2023, 74(9): 3766-3774.
[11]	韩晨, 司徒友珉, 朱斌, 许建良, 郭晓镭, 刘海峰. 协同处理废液的多喷嘴粉煤气化炉内反应流动研究[J]. 化工学报, 2023, 74(8): 3266-3278.
[12]	邢雷, 苗春雨, 蒋明虎, 赵立新, 李新亚. 井下微型气液旋流分离器优化设计与性能分析[J]. 化工学报, 2023, 74(8): 3394-3406.
[13]	于旭东, 李琪, 陈念粗, 杜理, 任思颖, 曾英. 三元体系KCl + CaCl₂ + H₂O 298.2、323.2及348.2 K相平衡研究及计算[J]. 化工学报, 2023, 74(8): 3256-3265.
[14]	诸程瑛, 王振雷. 基于改进深度强化学习的乙烯裂解炉操作优化[J]. 化工学报, 2023, 74(8): 3429-3437.
[15]	闫琳琦, 王振雷. 基于STA-BiLSTM-LightGBM组合模型的多步预测软测量建模[J]. 化工学报, 2023, 74(8): 3407-3418.