CFD simulation of hydrodynamics of gas-solid multiphase flow in downer reactors: revisited

被引:18
作者
Kim, Yong Nam [1 ]
Wu, Changning [1 ]
Cheng, Yi [1 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, Beijing Key Lab Green Chem React Engn & Technol, Beijing 100084, Peoples R China
关键词
Hydrodynamics; Multiphase flow; CFD; Simulation; Turbulence; Downer; FLUIDIZED-BED; KINETIC-THEORY; DILUTE; MODELS; PIPE;
D O I
10.1016/j.ces.2011.07.036
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the present work, a k(1)-epsilon(1)-k(2)-k(12) two-fluid model based on the kinetic theory of granular flow (KTGF) was employed to predict the flow behavior of gas and solids in downers, where the particles of small size as 70 mu m in diameter apparently interact with the gas turbulence. The turbulence energy interaction between gas and solids was described by different k(12) transport equations, while the particle dissipation by the large-scale gas turbulent motion was taken into account through a drift velocity. Johnson-Jackson boundary condition was adopted to describe the influence of the wall on the hydrodynamics. The simulation results by current CFD model were compared with the experimental data and simulation results reported by Cheng et al. (1999. Chem. Eng. Sci. 54, 2019) and Zhang and Zhu (1999. Chem. Eng. Sci. 54, 5461). Good agreement was obtained based on the PDE-type k(12) transport equation. The results demonstrated that the proposed model could provide good physical understanding on the hydrodynamics of gas-solid multiphase flow in downers. Using the current model, the mechanism for formation and disappearance of the dense-ring flow structure and the scale-up characteristics of downers were discussed. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:5357 / 5365
页数:9
相关论文
共 25 条
[1]   Gas-solid flow modelling based on the kinetic theory of granular media: validation, applications and limitations [J].
Balzer, G .
POWDER TECHNOLOGY, 2000, 113 (03) :299-309
[2]  
BALZER G, 1996, CIRCULATING FLUIDIZE, V5, P432
[3]   Evaluation of boundary conditions used to model dilute, turbulent gas/solids flows in a pipe [J].
Benyahia, S ;
Syamlal, M ;
O'Brien, TJ .
POWDER TECHNOLOGY, 2005, 156 (2-3) :62-72
[4]   Study of the ability of multiphase continuum models to predict core-annulus flow [J].
Benyahia, Sofiane ;
Syamlal, Madhava ;
O'Brien, Thomas J. .
AICHE JOURNAL, 2007, 53 (10) :2549-2568
[5]   GAS-PARTICLE 2-PHASE TURBULENT-FLOW IN A VERTICAL DUCT [J].
CAO, J ;
AHMADI, G .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1995, 21 (06) :1203-1228
[6]   Modeling the hydrodynamics of downer reactors based on kinetic theory [J].
Cheng, Y ;
Guo, YC ;
Wei, F ;
Jin, Y ;
Lin, WY .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) :2019-2027
[7]   CFD simulation of hydrodynamics in the entrance region of a downer [J].
Cheng, Y ;
Wei, F ;
Guo, YC ;
Jin, Y .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (04) :1687-1696
[8]  
Cheng Y, 2000, J Ind Eng Chem, V51, P344
[9]   Downer reactor: From fundamental study to industrial application [J].
Cheng, Yi ;
Wu, Changning ;
Zhu, Jingxu ;
Wei, Fei ;
Jin, Yong .
POWDER TECHNOLOGY, 2008, 183 (03) :364-384
[10]   Fluid dynamics of a pressurized fluidized bed: comparison between numerical solutions from two-fluid models and experimental results [J].
Enwald, H ;
Almstedt, AE .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (03) :329-342