Influence of immersed surface shape on the heat transfer process and flow pattern in a fluidized bed using numerical simulation.

被引:6
|
作者
Corcoles, J. I. [1 ,2 ]
Acosta-Iborra, A. [3 ]
Almendros-Ibanez, J. A. [1 ,2 ]
机构
[1] Univ Castilla La Mancha, T S Ingenieros Ind, Dpto Mecan Aplicada Ingn Proyectos, Campus Univ S N, Albacete 02071, Spain
[2] Univ Castilla La Mancha, Renewable Energy Res Inst, Sect Solar & Energy Efficiency, C Investigacion S N, Albacete 02071, Spain
[3] Univ Carlos III Madrid, Thermal & Fluids Engn Dept, ISE Res Grp, Avda Univ 30, Madrid, Spain
关键词
Fluidized bed; Immersed surface; Computational particle fluid dynamic; Hydrodynamics; Local heat transfer coefficient; TRANSFER COEFFICIENTS; HORIZONTAL TUBES; SOLIDS; MODEL; CPFD; PARTICLES; DIAMETER;
D O I
10.1016/j.ijheatmasstransfer.2021.121621
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper presents a 2-D numerical simulation of a freely bubbling fluidized bed with immersed surfaces, using the Computational Particle Fluid Dynamics (CPF D ) model implemented in the Barracuda commercial software. The heat transfer coefficients obtained are compared with an experimental study available in the open literature and numerical simulations based on the two-fluid model approach performed by other authors. Two different immersed surfaces, representing spherical and cylindrical geometries were studied. The simulations results show different heat transfer mechanisms, depending on the angular position in the two immersed surface geometries studied. The time average heat transfer coefficient around the whole heat transfer surface were 25 % and 38 % lower than the experimental study, for the cylindrical and spherical surfaces, respectively. These differences are lower than the results obtained with the two fluid model approach reported in the open literature. The numerical results indicate that CPFD-Barracuda is able to properly simulate the heat transfer and the dynamics of the bed in defluidized regions, such as on the top of an immersed surface, where the two-fluid model fails and overpredicts the heat transfer rate. (c) 2021 Elsevier Ltd. All rights reserved.
引用
收藏
页数:16
相关论文
共 50 条
  • [1] Numerical simulation of mass and heat transfer process in centrifugal fluidized bed
    Wang, Hai
    Shi, Mingheng
    Huagong Xuebao/Journal of Chemical Industry and Engineering (China), 2002, 53 (10): : 1040 - 1045
  • [2] Numerical investigation of the effect of the location of an immersed tube in a fluidized bed on heat transfer of surface-to-bed
    Wei, Bangji
    Lv, Guojun
    Meng, Xiangfei
    Khalid, Zeinab
    Huang, Qunxing
    Jiang, Xuguang
    POWDER TECHNOLOGY, 2023, 430
  • [3] IMMERSED SURFACE HEAT TRANSFER IN A VIBRATED FLUIDIZED BED.
    Malhotra, Karun
    Mujumdar, Arun S.
    1983, (26):
  • [4] Particle-Scale Simulation of the Flow and Heat Transfer Behaviors in Fluidized Bed with Immersed Tube
    Zhao, Yongzhi
    Jiang, Maoqiang
    Liu, Yanlei
    Zheng, Jinyang
    AICHE JOURNAL, 2009, 55 (12) : 3109 - 3124
  • [5] IMMERSED SURFACE HEAT-TRANSFER IN A VIBRATED FLUIDIZED-BED
    MALHOTRA, K
    MAJUMDAR, AS
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (10) : 1983 - 1992
  • [6] Discrete Particle Simulation of Heat Transfer in Pressurized Fluidized Bed with Immersed Cylinders
    Wahyudi, Hadi
    Chu, Kaiwei
    Yu, Aibing
    POWDERS AND GRAINS 2013, 2013, 1542 : 1118 - 1121
  • [7] Numerical prediction of heat transfer between a bubbling fluidized bed and an immersed tube bundle
    A. Schmidt
    U. Renz
    Heat and Mass Transfer, 2005, 41 : 257 - 270
  • [8] Numerical prediction of heat transfer between a bubbling fluidized bed and an immersed tube bundle
    Schmidt, A
    Renz, U
    HEAT AND MASS TRANSFER, 2005, 41 (03) : 257 - 270
  • [9] Micro-scale simulation of heat transfer behavior in fluidized bed with immersed tube
    Zhao Y.-Z.
    Jiang M.-Q.
    Xu P.
    Zheng J.-Y.
    Zhejiang Daxue Xuebao (Gongxue Ban)/Journal of Zhejiang University (Engineering Science), 2010, 44 (06): : 1178 - 1184
  • [10] Surface-particle-emulsion model of heat transfer between a fluidized bed and an immersed surface
    Wang, L
    Wu, P
    Ni, XZ
    POWDER TECHNOLOGY, 2005, 149 (2-3) : 127 - 138