Influence of flow guiding conduit on pressure drop and convective heat transfer in packed beds

被引:13
作者
Guo, Zehua [1 ,2 ]
Sun, Zhongning [1 ,2 ]
Zhang, Nan [1 ,2 ]
Ding, Ming [1 ,2 ]
Zhou, Yanmin [1 ,2 ]
机构
[1] Harbin Engn Univ, Fundamental Sci Nucl Safety & Simulat Technol Lab, Harbin 150001, Heilongjiang, Peoples R China
[2] Harbin Engn Univ, Coll Nucl Sci & Technol, Harbin 150001, Heilongjiang, Peoples R China
基金
中央高校基本科研业务费专项资金资助; 中国国家自然科学基金;
关键词
Packed bed; CFD; Flow guiding conduit; Fluid flow management; Convective heat transfer; Pressure drop; FLUID-FLOW; CFD SIMULATIONS; REYNOLDS-NUMBER; FIXED-BEDS; SMALL TUBE; TRANSPORT; PARTICLES; REACTORS; SPHERES; MODEL;
D O I
10.1016/j.ijheatmasstransfer.2019.01.066
中图分类号
O414.1 [热力学];
学科分类号
摘要
Packed beds with large tube-to-particle diameter ratios (D/d) suffer from poor lateral heat transport. Consequently, for applications with internal heat generation, fluid with high temperature concentrates in the center of packed beds, which is unfavorable to the design of high efficiency reactors. To address this problem, a novel method is developed: a free channel-flow guiding conduit (FGC)-is constructed in the center of a packed bed using highly fluid-penetrable material. Therefore, in the presented work, CFD simulations are carried out to study the influences of FGC to a conventional packed bed on packing structure, fluid flow distribution as well as heat transfer. It shows that cold fluid with high velocities is guided directly into the original hot zones where fluid temperature is generally higher in a conventional packing. Fluid flow in the lateral direction can be promoted with the Venturi effect. Moreover, with the FGC in proper sizes, pressure drop can be reduced about 16-26%; heat transfer coefficients merely drop 4-6%. However, although favorable effects could be achieved using the FGC, it is also observed that if an oversized flow guiding conduit was imposed into a packed bed, loss of effective cooling for particles would be also resulted since excess fluid could bypass through the conduit. Consequently, unexpected fluid temperature distribution could get some recovery. These findings are helpful for understanding of transport phenomena in packed beds as well as the design of high efficiency reactors. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:489 / 502
页数:14
相关论文
共 35 条
  • [1] Characteristics of convective heat transport in a packed pebble-bed reactor
    Abdulmohsin, Rahman S.
    Al-Dahhan, Muthanna H.
    [J]. NUCLEAR ENGINEERING AND DESIGN, 2015, 284 : 143 - 152
  • [2] Bird B.R., 2007, Transport Phenomena, VSecond
  • [3] On contact point modifications for forced convective heat transfer analysis in a structured packed bed of spheres
    Bu, S. S.
    Yang, J.
    Zhou, M.
    Li, S. Y.
    Wang, Q. W.
    Guo, Z. X.
    [J]. NUCLEAR ENGINEERING AND DESIGN, 2014, 270 : 21 - 33
  • [4] Carman PC., 1937, T I CHEM ENG-LOND, V15, P150, DOI 10.1016/s0263-8762(97)80003-2
  • [5] A DNS study of flow and heat transfer through slender fixed-bed reactors randomly packed with spherical particles
    Das, Saurish
    Deen, Niels G.
    Kuipers, J. A. M.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2017, 160 : 1 - 19
  • [6] Voidage variation in packed beds at small column to particle diameter ratio
    de Klerk, A
    [J]. AICHE JOURNAL, 2003, 49 (08) : 2022 - 2029
  • [7] Local transport and reaction rates in a fixed bed reactor tube: Endothermic steam methane reforming
    Dixon, Anthony G.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2017, 168 : 156 - 177
  • [8] Systematic mesh development for 3D CFD simulation of fixed beds: Contact points study
    Dixon, Anthony G.
    Nijemeisland, Michiel
    Stitt, E. Hugh
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2013, 48 : 135 - 153
  • [9] Experimental validation of high Reynolds number CFD simulations of heat transfer in a pilot-scale fixed bed tube
    Dixon, Anthony G.
    Walls, Gregory
    Stanness, Helen
    Nijemeisland, Michiel
    Stitt, E. Hugh
    [J]. CHEMICAL ENGINEERING JOURNAL, 2012, 200 : 344 - 356
  • [10] Systematic mesh development for 3D CFD simulation of fixed beds: Single sphere study
    Dixon, Anthony G.
    Taskin, M. Ertan
    Nijemeisland, Michiel
    Stitt, E. Hugh
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2011, 35 (07) : 1171 - 1185