Two- and three-dimensional computational studies of liquid-solid fluidization

被引:9
|
作者
Zhang, Kai [1 ]
Guan, Yanjun [1 ]
Yao, Xiuying [2 ]
Li, Yunning [3 ]
Fan, Xianfeng [3 ]
Brandani, Stefano [3 ]
机构
[1] North China Elect Power Univ, Ctr Chem Eng Clean Energy, Beijing 102206, Peoples R China
[2] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[3] Univ Edinburgh, Sch Engn, Edinburgh EH9 3JL, Midlothian, Scotland
基金
中国国家自然科学基金; 英国工程与自然科学研究理事会;
关键词
Liquid-solid fluidization; Hydrodynamics; CFD modelling; 2-D and 3-D simulation; CFD SIMULATION; INTERPARTICLE FORCES; NUMERICAL-SOLUTION; HYPERBOLIC SYSTEM; BEDS; FLOW; GAS; HYDRODYNAMICS; STABILITY; EXPANSION;
D O I
10.1016/j.powtec.2012.09.046
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The present work Compares the hydrodynamics in the 2-dimension (2-D) and 3-dimension (3-D) liquid-solid fluidized beds using a simple two-fluid model suggested by Brandani and Zhang (2006). This model considers the effect of the particles dispersed on the momentum equations into the inviscid model A of Gidaspow (1994). Numerical simulations are conducted in the platform of CFX 4.4, a commercial CFD code, together with user-defined FORTRAN subroutines. Based on the independence of mesh size and time step in the 2-D bed, detailed hydrodynamics are compared numerically in the 2-D and 3-D beds after a sudden change in the liquid inlet velocity and the physical property of the liquid-solid system. The computational results show that the bed height, surface height and vertical solid holdup profile within the 2-D and 3-D beds are in the good agreement after a decrease in the liquid inlet velocity or an increase in the liquid-solid density difference and liquid viscosity. However, the differences of surface height and vertical solid holdup profile are found between the 2-D and 3-D simulation when the liquid inlet velocity is increased or the particle diameter is decreased. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:180 / 191
页数:12
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