Two- and three-dimensional hydrodynamic modeling of a pseudo-2D turbulent fluidized bed with Geldart B particle

被引:20
作者
Chang, Jian [1 ]
Wu, Zejun [1 ]
Wang, Xin [1 ]
Liu, Wenyi [1 ]
机构
[1] North China Elect Power Univ, Sch Energy Power & Mech Engn, Beijing 102206, Peoples R China
基金
中国国家自然科学基金;
关键词
Hydrodynamics; Pseudo; 2D; Turbulent fluidized bed; Geldart B particle; 2D/3D models; GAS-SOLID FLOW; NUMERICAL-SIMULATION; CFD SIMULATION; BEHAVIOR; REACTOR; MTO;
D O I
10.1016/j.powtec.2019.04.028
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study presents a comprehensive comparision between 2D and 3D hydrodynamic modeling of a pseudo-2D turbulent fluidized bed with Geldart B particle. Based on the Euler-Euler approach and the EMMS-based drag model, 2D/3D CFD models are established, their sensitivities to the restitution coefficient and the specularity coefficient are analyzed, and the 2D/3D hydrodynamic simulations are performed and compared. The simulation results show that 3D simulations are more sensitive to the restitution coefficient and the specularity coefficient than 2D simulations. At the beginning of fluidization process, 2D simulation predicts greater bubble size and higher bed expansion than 3D simulation; as a complete fluidization is achieved, 2D model exhibits higher solid concentrations in the middle transition and the upper dilute-phase regions; the fluidization process in the 2D simulation develops more quickly than that in the 3D computation. Both the 2D and 3D models could capture the global flow behavior in the bottom dense-phase region of the turbulent fluidized bed reasonably. In the middle and upper regions, however, the 2D model overestimates the solid concentration and particle velocity while the 3D simulation gives better hydrodynamic prediction. For the present pseudo-2D turbulent fluidized bed with Geldart B particle, the bottom dense-phase region resembles 2D flow and 2D simulations may be adequate; however, the middle and upper regions exhibit 3D flow and full 3D simulations are needed. (C) 2019 Elsevier B.V. All rights reserved.
引用
收藏
页码:159 / 168
页数:10
相关论文
共 30 条
  • [1] 3D Eulerian modeling of thin rectangular gas-solid fluidized beds: Estimation of the specularity coefficient and its effects on bubbling dynamics and circulation times
    Altantzis, C.
    Bates, R. B.
    Ghoniem, A. F.
    [J]. POWDER TECHNOLOGY, 2015, 270 : 256 - 270
  • [2] CFD modeling of the coke combustion in an industrial FCC regenerator
    Amblard, Benjamin
    Singh, Raj
    Gbordzoe, Eusebius
    Raynal, Ludovic
    [J]. CHEMICAL ENGINEERING SCIENCE, 2017, 170 : 731 - 742
  • [3] Influence of two- and three-dimensional simulations on bubble behavior in gas-solid fluidized beds with and without immersed horizontal tubes
    Asegehegn, Teklay Weldeabzgi
    Schreiber, Matthias
    Krautz, Hans Joachim
    [J]. POWDER TECHNOLOGY, 2012, 219 : 9 - 19
  • [4] Numerical simulation of turbulent fluidized bed with Geldart B particles
    Benzarti, Salma
    Mhiri, Hatem
    Bournot, Herve
    Occelli, Rene
    [J]. ADVANCED POWDER TECHNOLOGY, 2014, 25 (06) : 1737 - 1747
  • [5] Numerical simulation of a commercial FCC regenerator using Multiphase Particle-in-Cell methodology (MP-PIC)
    Berrouk, Abdallah S.
    Huang, Allen
    Bale, Shivkumar
    Thampi, Priyanka
    Nandakumar, Krishnaswamy
    [J]. ADVANCED POWDER TECHNOLOGY, 2017, 28 (11) : 2947 - 2960
  • [6] A state-of-the-art review of gas-solid turbulent fluidization
    Bi, HT
    Ellis, N
    Abba, IA
    Grace, JR
    [J]. CHEMICAL ENGINEERING SCIENCE, 2000, 55 (21) : 4789 - 4825
  • [7] Analysis of the bubbling behaviour of 2D gas solid fluidized beds Part I. Digital image analysis technique
    Busciglio, Antonio
    Vella, Giuseppa
    Micale, Giorgio
    Rizzuti, Lucio
    [J]. CHEMICAL ENGINEERING JOURNAL, 2008, 140 (1-3) : 398 - 413
  • [8] Cammarata L., 2003, International Journal of Chemical Reactor Engineering, V1
  • [9] Two- and three-dimensional CFD modeling of Geldart A particles in a thin bubbling fluidized bed: Comparison of turbulence and dispersion coefficients
    Chalermsinsuwan, Benjapon
    Gidaspow, Dimitri
    Piumsomboon, Pornpote
    [J]. CHEMICAL ENGINEERING JOURNAL, 2011, 171 (01) : 301 - 313
  • [10] Computational Investigation of a Turbulent Fluidized-bed FCC Regenerator
    Chang, Jian
    Wang, Gang
    Lan, Xingying
    Gao, Jinsen
    Zhang, Kai
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (11) : 4000 - 4010