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

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

1.
波斯湾大学布什尔工程学院机械工程系,布什尔 000000,伊朗;2.德里兰大学工程学院机械工程系,德里兰 000000,伊朗;3.皮措帕斯法律与合同公司,德里兰 000000,伊朗

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
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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

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

1.
Mechanical Engineering Department, Bushehr Engineering Faculty, Persian Gulf University, Bushehr, Iran;

摘要

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．
- 强迫对流 /
- 粘性耗散 /
- Brinkman模型 /
- Darcy数 /
- Nusselt数
Abstract: The viscous dissipation effect on forced convection in a porous saturated circular tube with an isoflux wall is investigated on the basis of the Brinkman flow model. For the thermally developing region, a numerical study was reported while a perturbation analysis was presented to find expressions for the temperature profile and the Nusselt number for the fully developed region. The fully developed Nusselt number found by numerical solution for the developing region was compared with that of asymptotic analysis and a good degree of agreement is observed.
- forced convection /
- viscous dissipation /
- Brinkman model /
- Darcy number /
- Nusselt number

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参考文献(19)

[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.