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等通量壁多孔饱和圆管中粘性耗散对热发展强迫对流的影响

K·霍曼 A·鲍尔夏海 A·伊吉拉里

K·霍曼, A·鲍尔夏海, A·伊吉拉里. 等通量壁多孔饱和圆管中粘性耗散对热发展强迫对流的影响[J]. 应用数学和力学, 2006, 27(5): 547-554.
引用本文: K·霍曼, A·鲍尔夏海, A·伊吉拉里. 等通量壁多孔饱和圆管中粘性耗散对热发展强迫对流的影响[J]. 应用数学和力学, 2006, 27(5): 547-554.
K. Hooman, A. Pourshaghaghy, A. Ejlali. Effects of Viscous Dissipation on Thermally Developing Forced Convection in a Porous Saturated Circular Tube With an Isoflux Wall[J]. Applied Mathematics and Mechanics, 2006, 27(5): 547-554.
Citation: K. Hooman, A. Pourshaghaghy, A. Ejlali. Effects of Viscous Dissipation on Thermally Developing Forced Convection in a Porous Saturated Circular Tube With an Isoflux Wall[J]. Applied Mathematics and Mechanics, 2006, 27(5): 547-554.

等通量壁多孔饱和圆管中粘性耗散对热发展强迫对流的影响

详细信息
    作者简介:

    K·霍曼,讲师(联系人.Tel/Fax:+98-77-4540376;E-mail:Hooman@pgu.ac.ir).

  • 中图分类号: O357.3

Effects of Viscous Dissipation on Thermally Developing Forced Convection in a Porous Saturated Circular Tube With an Isoflux Wall

  • 摘要: 基于Brinkman流动模型,研究了等通量壁多孔饱和圆管中粘性耗散对强迫对流的影响.在热发展区域,进行了数值研究;在充分发展区域,进行了摄动分析并求得温度分布的表达式和Nusselt数.在发展区域,利用数值解得到的充分发展Nusselt数与渐近分析结果进行了比较,吻合很好.
  • [1] Nield D A,Bejan A.Convection in Porous Media[M].2nd Ed. New York :Springer,1999.
    [2] Nield D A, Kuznetsov A V, Xiong M. Thermally developing forced convection in a porous medium: parallel plate channel with walls at constant temperature, with longitudinal conduction and viscous dissipation effects[J].Internat J Heat Mass Transfer,2003,46:643─651. doi: 10.1016/S0017-9310(02)00327-7
    [3] Nield D A, Kuznetsov A V, Xiong M. Thermally developing forced convection in a porous medium: parallel plate channel or circular tube with walls at constant heat flux[J].J Porous Media,2003,6:203—212. doi: 10.1615/JPorMedia.v6.i3.50
    [4] Nield D A, Kuznetsov A V, Xiong M. Thermally developing forced convection in a porous medium: parallel plate channel or circular tube with walls at constant temperature[J].J Porous Media,2004,7:19—27. doi: 10.1615/JPorMedia.v7.i1.30
    [5] Kuznetsov A V, Xiong M, Nield D A. Thermally developing forced convection in a porous medium: circular tube with walls at constant temperature, with longitudinal conduction and viscous dissipation effects[J].Trans Porous Media,2003,53:331—345. doi: 10.1023/A:1025060524816
    [6] Mahmud S, Fraser R A. Flow and heat transfer inside porous stack: steady state problem[J].Internat Comm Heat Mass Transfer,2004,31(7):951—962. doi: 10.1016/j.icheatmasstransfer.2004.05.005
    [7] Ranjbar-Kani A A, Hooman K. Viscous dissipation effects on thermally developing forced convection in a porous medium: circular duct with isothermal wall[J].Internat Comm Heat Mass Transfer,2004,31(6):897—907. doi: 10.1016/S0735-1933(04)00076-4
    [8] Hooman K, Gorji-Bandpy M. Laminar heat transfer to a highly viscous fluid flow in entrance region of a porous saturated circular tube with uniform wall temperature[J].IUST-Internat J Eng Sci,2004,15(3):61—66.
    [9] Hooman K, Gorji-Bandpy M. Effects of viscous dissipation on forced convection in a porous saturated duct with a uniform wall temperature[J].Heat Transfer Research,2004,35(7/8):588—597. doi: 10.1615/HeatTransRes.v35.i78.120
    [10] Nield D A, Kuznetsov A V, Xiong M. Effects of viscous dissipation and flow work on forced convection in a channel filled by a saturated porous medium[J].Trans Porous Media,2004,56:351—367. doi: 10.1023/B:TIPM.0000026087.77213.c8
    [11] Hooman K,Ranjbar-Kani A A. Forced convection in a fluid-saturated porous-medium tube with isoflux wall[J].Internat Comm Heat Mass Transfer,2003,30:1015—1026. doi: 10.1016/S0735-1933(03)00160-X
    [12] Mahmud S, Fraser R A. Flow, thermal, and entropy generation characteristics inside a porous channel with viscous dissipation[J].Internat J Thermal Science,2005,44:21—32. doi: 10.1016/j.ijthermalsci.2004.05.001
    [13] Bejan A.Convection Heat Transfer[M].New York :Wiley,1984.
    [14] Al-Hadrami A K, Elliott L, Ingham D B. A new model for viscous dissipation in porous media across a range of permeability values[J].Trans Porous Media,2003,53:117—122. doi: 10.1023/A:1023557332542
    [15] Nield D A. Resolution of a paradox involving viscous dissipation and nonlinear drag in a porous medium[J].Trans Porous Media,2000,41:349—357. doi: 10.1023/A:1006636605498
    [16] Kaviany M. Laminar flow through a porous channel bounded by isothermal parallel plates[J].Internat J Heat Mass Transfer,1985,28:851—858. doi: 10.1016/0017-9310(85)90234-0
    [17] Nield D A. Modelling fluid flow in saturated porous media and at interfaces[A].In:Ingham D B, Pop I Eds.Transport Phenomena in Porous Media Ⅱ[C].Oxford :Elsevier Science, 2002.
    [18] Shah R K, London A L.Laminar Flow Forced Convection in Ducts (Advances in Heat Transfer)[M].New York :Academic Press,1978.
    [19] Kaka S, Shah R K, Aung W.Handbook of Single-Phase Convective Heat Transfer[M].New York:Wiley,1987.
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出版历程
  • 收稿日期:  2005-02-22
  • 修回日期:  2005-08-18
  • 刊出日期:  2006-05-15

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