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

多孔饱和矩形管中粘性随温度变化对熵产、热和流体流动的影响

K·霍曼 H·戈金西

K·霍曼, H·戈金西. 多孔饱和矩形管中粘性随温度变化对熵产、热和流体流动的影响[J]. 应用数学和力学, 2007, 28(1): 61-69.
引用本文: K·霍曼, H·戈金西. 多孔饱和矩形管中粘性随温度变化对熵产、热和流体流动的影响[J]. 应用数学和力学, 2007, 28(1): 61-69.
K. Hooman, H. Gurgenci. Effects of Temperature-Dependent Viscosity Variation on Entropy Generation,Heat,and Fluid Flow Through a Porous-Saturated Duct of Rectangular Cross-Section[J]. Applied Mathematics and Mechanics, 2007, 28(1): 61-69.
Citation: K. Hooman, H. Gurgenci. Effects of Temperature-Dependent Viscosity Variation on Entropy Generation,Heat,and Fluid Flow Through a Porous-Saturated Duct of Rectangular Cross-Section[J]. Applied Mathematics and Mechanics, 2007, 28(1): 61-69.

多孔饱和矩形管中粘性随温度变化对熵产、热和流体流动的影响

详细信息
    作者简介:

    K·霍曼(联系人.Tel/Fax:+61-402-206033;E-mail:k.hooman@uq.edu.au);H·戈金西,教授(Tel/Fax:+61-7-33653607;E-mail:h.gurgenci@uq.edu.au).

  • 中图分类号: O357.3

Effects of Temperature-Dependent Viscosity Variation on Entropy Generation,Heat,and Fluid Flow Through a Porous-Saturated Duct of Rectangular Cross-Section

  • 摘要: 研究了充填流体-饱和多孔介质的矩形管中,随温度变化的粘性对充分发展强迫对流的影响.采用Darcy流动模型并假设粘性-温度为倒线性关系.管壁视为均匀热通量,即Kays和Crawford称为的H边界条件.当流体粘性随温度升高而降低时,管壁的Nusselt数增大.求解速度和温度分布时,利用热力学第二定律求解了局部平均熵产率.根据Brinkman数、Péclet数、粘性变化数、无量纲管壁热通量和管道截面宽高比,给出了熵产率、Bejan数、传热不可逆性和流体流动不可逆性的表达式.这些表达式是该类问题参数研究的基础.可以看出,当管道截面宽高比的增大使熵产率减小时,方形管中流动产生的熵大于矩形管,这类似于Ratts和Raut研究的明流(clear flow)情况.
  • [1] Nield D A,Bejan A.Convection in Porous Media[M].New York:Springer-Verlag,1999.
    [2] Lauriat G,Ghafir R.Forced convective heat transfer in porous media[A].In:Vafai K,Ed.Handbook of Porous Media[C].New York:Dekker,2000,201.
    [3] Haji-Sheikh A,Vafai K.Analysis of flow and heat transfer in porous media imbedded inside various-shaped ducts[J].Internat J Heat Mass Transfer,2004,47(8/9):1889-1905. doi: 10.1016/j.ijheatmasstransfer.2003.09.030
    [4] Haji-Sheikh A.Heat transfer to fluid flow in rectangular passages filled with porous materials[J].ASME J Heat Transfer,2006,128(6):550-556. doi: 10.1115/1.2188507
    [5] Haji-Sheikh A,Nield D A,Hooman K.Heat transfer in the thermal entrance region for flow through rectangular porous passages[J].Internat J Heat Mass Transfer,2006,49(17/18):3004-3015. doi: 10.1016/j.ijheatmasstransfer.2006.01.040
    [6] Hooman K,Merrikh A A.Forced convection in a duct of rectangular cross-section saturated by a porous medium[J].ASME J Heat Transfer,2006,128(6):596-600. doi: 10.1115/1.2188510
    [7] Hooman K.Analysis of entropy generation in porous media imbedded inside elliptical passages[J].Internat J Heat Technology,2005,23(2):145-149.
    [8] Hooman K.Fully developed temperature distribution in a porous saturated duct of elliptical cross-section, with viscous dissipation effects and entropy generation analysis[J].Heat Transfer Research,2005,36(3):237-245. doi: 10.1615/HeatTransRes.v36.i3.70
    [9] Hooman K.Entropy-energy analysis of forced convection in a porous-saturated circular tube considering temperature-dependent viscosity effects[J].Internat J Exergy,2006,3(4):436-451. doi: 10.1504/IJEX.2006.010235
    [10] Harms T M,Jog M A,Manglik R M.Effects of temperature-dependent viscosity variations and boundary conditions on fully developed laminar steady forced convection in a semicircular duct[J].ASME J Heat Transfer,1998,120(3):600-605. doi: 10.1115/1.2824317
    [11] Ling J X,Dybbs A.The effect of variable viscosity on forced convection over a flat plate submerged in a porous medium[J].ASME J Heat Transfer,1992,114(4):1063-1065. doi: 10.1115/1.2911882
    [12] Kays W M,Crawford M E.Convective Heat and Mass Transfer[M].New York:McGraw-Hill,1993.
    [13] Bejan A.Entropy Generation Through Heat and Fluid Flow[M].New York:Wiley,1982.
    [14] Ratts E B,Raut A G.Entropy generation minimization of fully developed internal flow with constant heat flux[J].ASME J Heat Transfer,2004,126(4):656-659. doi: 10.1115/1.1777585
    [15] Sahin A Z.Second law analysis of laminar viscous flow through a duct subjected to a constant wall temperature[J].ASME J Heat Transfer,1998,120(1):76-83. doi: 10.1115/1.2830068
    [16] Al-Zahranah I T,Yilbas B S.Thermal analysis in pipes: influence of variable viscosity on entropy generation[J].Entropy,2004,6(3):344-363. doi: 10.3390/e6030344
    [17] Nield D A,Porneala D C,Lage J L.A theoretical study, with experimental verification of the viscosity effect on the forced convection through a porous medium channel[J].ASME J Heat Transfer,1999,121(2):500-503. doi: 10.1115/1.2826011
    [18] Hooman K.Effects of temperature-dependent viscosity on thermally developing forced convection through a porous medium[J].Heat Trans Res,2005,36(1/2):132-140. doi: 10.1615/HeatTransRes.v36.i12.150
    [19] Narasimhan A,Lage J L.Modified Hazen-Dupuit-Darcy model for forced convection of a fluid with temperature-dependent viscosity[J].Internat J Heat Mass Transfer,2001,123(1):31-38.
    [20] Narasimhan A,Lage J L,Nield D A.New theory for forced convection through porous media by fluids with temperature-dependent viscosity[J].ASME J Heat Transfer,2001,123(6):1045-1051. doi: 10.1115/1.1409268
    [21] Narasimhan A,Lage J L.Variable viscosity forced convection in porous medium channels[A].In:Vafai K,Ed.Handbook of Porous Media[C].2nd Ed.Taylor and Francis:Boca Raton,2005,195.
    [22] Nield D A,Kuznetsov A V.Effects of temperature dependent viscosity in forced convection in a porous medium: layered medium analysis[J].J Porous Media,2003,6(3):213-222. doi: 10.1615/JPorMedia.v6.i3.60
    [23] Mahmud S,Fraser R A.Flow, heat transfer, and entropy generation characteristics inside a porous channel with viscous dissipation[J].Internat J Therm Sci,2005,44(1):21-32. doi: 10.1016/j.ijthermalsci.2004.05.001
    [24] Bejan A.Convection Heat Transfer[M].Hoboken:Wiley,1984.
  • 加载中
计量
  • 文章访问数:  2383
  • HTML全文浏览量:  81
  • PDF下载量:  488
  • 被引次数: 0
出版历程
  • 收稿日期:  2006-03-15
  • 修回日期:  2006-09-07
  • 刊出日期:  2007-01-15

目录

    /

    返回文章
    返回