留言板

尊敬的读者、作者、审稿人, 关于本刊的投稿、审稿、编辑和出版的任何问题, 您可以本页添加留言。我们将尽快给您答复。谢谢您的支持!

姓名
邮箱
手机号码
标题
留言内容
验证码

非Darcy多孔介质中的非线性对流

M·R·帕沙

M·R·帕沙. 非Darcy多孔介质中的非线性对流[J]. 应用数学和力学, 2010, 31(5): 533-543. doi: 10.3879/j.issn.1000-0887.2010.05.004
引用本文: M·R·帕沙. 非Darcy多孔介质中的非线性对流[J]. 应用数学和力学, 2010, 31(5): 533-543. doi: 10.3879/j.issn.1000-0887.2010.05.004
M. K. Partha. Non-Linear Convection in a Non-Darcy Porous Medium[J]. Applied Mathematics and Mechanics, 2010, 31(5): 533-543. doi: 10.3879/j.issn.1000-0887.2010.05.004
Citation: M. K. Partha. Non-Linear Convection in a Non-Darcy Porous Medium[J]. Applied Mathematics and Mechanics, 2010, 31(5): 533-543. doi: 10.3879/j.issn.1000-0887.2010.05.004

非Darcy多孔介质中的非线性对流

doi: 10.3879/j.issn.1000-0887.2010.05.004
详细信息
  • 中图分类号: O357.3

Non-Linear Convection in a Non-Darcy Porous Medium

  • 摘要: 利用温度-浓度-密度关系,研究非Darcy多孔介质中的自由对流问题.对于不同的惯性参数、传递参数、Rayleigh数、Lewis数、Soret数和Dufour数,分析了非线性温度参数和浓度参数对非线性对流的影响.浮力对对流起着辅助的附加作用,当惯性作用不计时,切向速度随着非线性温度和浓度的增加而急剧地增加.然而,当惯性效应不为0时,非线性温度和浓度对切向速度的影响是有限的.对两个传递参数、惯性影响参数以及控制非线性温度和浓度的其他参数,取不同的数值时,浓度分布有点儿变化,并在不同的范围内传播.随着非线性温度和浓度的增加,传热/传质在很大的范围内变化,这取决于是Dacry多孔介质,还是非Darcy多孔介质.当所有的影响(惯性的影响、两个传递系数的影响、Soret和Dufour的影响)同时为0/不为0,在非线性温度/浓度参数以及浮力的共同作用下,分析了传热/传质的变化.发现在Darcy多孔介质中,温度和浓度以及它们的交叉扩散,对传热/传质的影响,要比非Darcy多孔介质要大.发现了浮力的负面作用,随着非线性温度系数的增加,传热/传质率是提高的,而随着非线性浓度系数的增加,传热/传质率是下降的.
  • [1] Lai F C, Kulacki F A. Coupled heat and mass transfer by natural convection from vertical surfaces in porous media[J]. Int J Heat and Mass Transfer, 1991, 34(4/5): 1189-1194. doi: 10.1016/0017-9310(91)90027-C
    [2] Angirasa D, Peterson G P, Pop I. Combined heat and mass transfer by natural convection with opposing buoyancy effects in a fluid saturated porous medium[J]. Int J Heat Mass Transfer, 1977, 40(12): 2755-2773.
    [3] Murthy P V S N. Effect of double dispersion on mixed convection heat and mass transfer in non-Darcy porous medium[J]. Trans ASME J Heat Transfer, 2000, 122(3): 476-484. doi: 10.1115/1.1286995
    [4] Nield D A, Bejan A. Convection in Porous Media[M]. 3rd ed. New York: Springer, 2006.
    [5] Postelnicu A. Effects of thermophoresis particle deposition in free convection boundary layer from a horizontal flat plate embedded in a porous medium[J]. Int J Heat Mass Transfer, 2007, 50(15/16): 2981-2985. doi: 10.1016/j.ijheatmasstransfer.2006.12.012
    [6] Anghel M, Takhar H S, Pop I. Dufour and Soret effects on free convection boundary layer flow over a vertical surface embedded in a porous medium[J]. Studia Universitatics Babes-Bolyai Mathematica, 2000, 45: 11-21.
    [7] Cheng P, Minkowcyz W J. Free convection about a vertical flat plate embedded in a porous medium with application to heat transfer from a dike[J]. J Geophys Res, 1977, 82: 2040-2044. doi: 10.1029/JB082i014p02040
    [8] Cheng P. The influence of lateral mass flux on free convection boundary layers in saturated porous medium[J]. Int J Heat Mass Transfer, 1977, 20(3): 201-206. doi: 10.1016/0017-9310(77)90206-X
    [9] Bejan A, Khair K R. Heat and mass transfer by natural convection in a porous medium[J]. Int J Heat Mass Transfer, 1985, 28(5): 909-918. doi: 10.1016/0017-9310(85)90272-8
    [10] Cheng P. Buoyancy induced boundary layer flows in Geothermal reservoirs[C]Proc of the 2nd Work Shop on Geothermal Reservoir Engineering. Standford, California: Standford University, 1976: 236-246.
    [11] Cengel Y A. Heat Transfer—a Practical Approach[M]. 2nd ed. New Delhi-India:Tata McGraw Hill, 2003.
    [12] Verms G. Thermophoresis-enhanced deposition rates in combustion turbine blade passages[J]. J Engrg Power, 1979, 101: 542-548. doi: 10.1115/1.3446614
    [13] Goren S L. On free convection in water at 40℃[J]. Chem Eng Sci, 1966, 21(6/7): 515-518. doi: 10.1016/0009-2509(66)85065-0
    [14] Sinha P C. Fully developed laminar free convection flow between vertical parallel plates[J]. Chem Eng Sci, 1969, 24(1): 33-38. doi: 10.1016/0009-2509(69)80005-9
    [15] Gilpin R R. Cooling of a horizontal cylinder of water through its maximum density point at 4℃[J]. Int J Heat Mass Transfer, 1975, 18(11): 1307-1315. doi: 10.1016/0017-9310(75)90241-0
    [16] Vanier C R, Tien C. Effect of maximum density and melting on natural convection heat transfer from a vertical plate[J]. Chem Engng Frog Symp Ser, 1968, 64(82):240-254.
    [17] Yen Y-C, Effects of density inversion on free convective heat transfer in porous layer heated from below[J]. Int J Heat Mass Transfer, 1974, 17(11): 1349-1356.
    [18] Partha M K, Murthy P V S N, Raja Shekhar G P. Soret and Dufour effects in a non-Darcy porous medium[J]. ASME J Heat Transfer, 2006, 128(6): 605-610. doi: 10.1115/1.2188512
  • 加载中
计量
  • 文章访问数:  1428
  • HTML全文浏览量:  83
  • PDF下载量:  751
  • 被引次数: 0
出版历程
  • 收稿日期:  1900-01-01
  • 修回日期:  2010-02-19
  • 刊出日期:  2010-05-15

目录

    /

    返回文章
    返回