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球床通道内CFD网格适用性分析 被引量:1

Analysis of Grid Applicability in the CFD of Packed Bed
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摘要 为了研究球床通道内网格效应对CFD计算精度的影响,本文采用两类网格划分形式,对体心堆积结构球床通道内层流和湍流下的阻力和传热特性进行了数值计算。通过对比发现:在层流时,流道内的整体网格密度是决定阻力和传热特性计算结果精度的主要因素,在相同条件下,阻力对网格密度的依赖程度大于传热。而湍流时,决定阻力和传热特性计算结果精度的主要因素是近壁面网格数量,通过构建贴体附面层网格,能够在保证计算精度的条件下,有效地控制整体网格数量。 To develop meshes for computational fluid dynamics simulations of flow and heat transfer in packed bed.Adapting two types of meshing strategies,the flow resistance and heat transfer characteristics in structure packed bed of body-centered packing under laminar and turbulent flows were calculated.The results show that,in the laminar flow,the global mesh density is the main factor,which to determine the accuracy of calculated results of flow resistance and heat transfer,and the dependence of flow resistance on the mesh density is greater than heat transfer.Under Turbulence flow condition,the near-wall mesh count is the main factor.By constructing the boundary layer of body-fitted grid is not only to improve the accuracy of results but also to control the overall number of grid effectively.
出处 《工程热物理学报》 EI CAS CSCD 北大核心 2013年第7期1303-1306,共4页 Journal of Engineering Thermophysics
基金 国家自然科学基金资助项目(No.11075042)
关键词 球床通道 数值模拟 网格效应 流动传热 packed bed numerical simulation grid effect flow and heat transfer
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参考文献7

  • 1张楠,孙中宁,阎昌琪.三维随机填充球床通道内流场数值分析[J].原子能科学技术,2012,46(B12):792-795. 被引量:5
  • 2杨剑,王劲,步珊珊,曾敏,王秋旺.颗粒有序堆积多孔介质对流换热实验研究[J].工程热物理学报,2012,33(5):851-855. 被引量:17
  • 3Nijemeisland M,Dixon A G.CFD Study of Fluid Flow and Wall Heat Transfer in a Fixed Bed of Spheres[].American Institute of Chemical Engineers Journal.2004
  • 4Romkes S J P,Dautzenberg F M,van den Bleek C M,et al.CFD Modeling and Experimental Validation of Particle-to-Fluid Mass and Heat Transfer in a Packed Bed at Very Low Channel to Particle Diameter Ratio[].Chemical Engineering Journal.2003
  • 5BAKER M J,TABOR G R.Computational anal-ysis of transitional air flow through packed col-umns of spheres using the finite volume technique[].Computers and Chemistry.2010
  • 6Eppinger, T,K Seidler, et al."DEM-CFD simulations of fixed bed reactors with small tube to particle diameter ratios."[].Chemical Engineering.2011
  • 7Anthony G. Dixon,M. Ertan Taskin,Michiel Nijemeisland,E. Hugh Stitt.Systematic mesh development for 3D CFD simulation of fixed beds:Single sphere study[].Computers and Chemistry.2011

二级参考文献14

  • 1NIJEMEISLAND M, DIXON A G. CFD studyof fluid flow and wall heat transfer in a fixed bed of spheres[J]. AIChE, 2004, 50(5):906-921.
  • 2ROMKES S J P, DAUTZENBERG F M, van den BLEEK C M, et al. CFD modelling and ex- perimental validation of particle-to-fluid mass and heat transfer in a packed bed at very low channel to particle diameter ratio[J]. Chemical Engineer- ing Journal, 2003, 96(1-3): 3-13.
  • 3BAKER M J, TABOR G R. Computational anal- ysis of transitional air flow through packed col- umns of spheres using the finite volume technique [J]. Computers and Chemical Engineering, 2010, 34(6): 878-885.
  • 4EPPINGER T, SEIDLER K, KRAUME M. DEM-CFD simulations of fixed bed reactors with small tube to particle diameter ratios[J].Chemical Engineering Journal, 2011, 166(1) : 324-331.
  • 5张楠,孙中宁.随机填充球床通道内流动阻力特性数值研究[c]//第十二届全国反应堆热工流体会议论文集.成都:中核核反应堆热工水力技术重点实验室,2011.
  • 6de KLERK A. Voidage variation in packed beds at small column to particle diameter ratios[J]. AIChE, 2003, 49(8): 2 022-2 029.
  • 7EISFELD B, SCHNITZLEIN K. The influence of confining walls on the pressure drop in packed beds[J]. Chemical Engineering Science, 2001, 56(14): 4 321-4 329.
  • 8YANG J,WANG Q W,ZENG M,et al.Computational Study of Forced Convective Heat Transfer in Structured Packed Beds With Spherical or Ellipsoidal Particles[].Chemical Engineering Science.2010
  • 9P. R. Gunjal,V. V. Ranade,R. V. Chaudhari.Computational Study of a Single-phase Flow in Packed Beds of Spheres[].American Institute of Chemical Engineers Journal.2005
  • 10Romkes SJP,Dautzenberg FM,van den Bleek CM,Calis HPA.CFD modelling and experimental validation of particle-to-fluid mass and heat transfer in a packed bed at very low channel to particle diameter ratio[].Chemical Engineering Journal.2003

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