Influence of solid-phase wall boundary condition on CFD simulation of spouted beds

被引:94
作者
Lan, Xingying [2 ]
Xu, Chunming [2 ]
Gao, Jinsen [2 ]
Al-Dahhan, Muthanna [1 ]
机构
[1] Missouri Univ Sci & Technol, Rolla, MO 65401 USA
[2] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
关键词
Spouted beds; Numerical simulation; Boundary condition; Hydrodynamics; Specularity coefficient; Particle-wall restitution coefficient; COMPUTATIONAL FLUID-DYNAMICS; NUMERICAL-SIMULATION; KINETIC-THEORY; GAS; FLOWS; HYDRODYNAMICS; COEFFICIENT; PARTICLES; PROFILES; BEHAVIOR;
D O I
10.1016/j.ces.2011.10.064
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The influence of solid-phase wall boundary condition in terms of specularity coefficient and particle-wall restitution coefficient on the flow behavior of spouted beds was investigated using two-fluid model approach in the computational fluid dynamics software FLUENT 6.3. Parametric studies of specularity coefficient and particle-wall restitution coefficient were performed to evaluate their effects on the flow hydrodynamics in terms of fountain height, spout diameter, pressure drop, local voidage and particles velocity. The numerical predictions were compared with available experimental data in the literatures to obtain the suitable values of specularity coefficient and particle-wall restitution coefficient for spouted beds. The simulated results show that the solid-phase wall boundary condition plays an important role in CFD modeling of spouted beds. The specularity coefficient has a pronounced effect on the spouting behavior and a small specularity coefficient (0.05) can give good predictions, while the particle-wall restitution coefficient is not critical for the holistic flow characteristics. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:419 / 430
页数:12
相关论文
共 36 条
[1]   Computational fluid dynamics of high density circulating fluidized bed riser: Study of modeling parameters [J].
Almuttahar, Adnan ;
Taghipour, Fariborz .
POWDER TECHNOLOGY, 2008, 185 (01) :11-23
[2]  
[Anonymous], 1975, TURBULENCE
[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]   Fluid Dynamic Study of a Semicylindrical Spouted Bed: Evaluation of the Shear Stress Effects in the Flat Wall Region Using Computational Fluid Dynamics [J].
Bettega, Rodrigo ;
da Rosa, Cezar A. ;
Correa, Ronaldo G. ;
Freire, Jose T. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (24) :11181-11188
[6]   CFD MODELLING OF A SEMI-CYLINDRICAL SPOUTED BED: NUMERICAL SIMULATION AND EXPERIMENTAL VERIFICATION [J].
Bettega, Rodrigo ;
Felkl de Almeida, Andre Ricardo ;
Correa, Ronaldo Guimaraes ;
Freire, Jose Teixeira .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2009, 87 (02) :177-184
[7]   SCALE-UP STUDY OF SPOUTED BEDS USING COMPUTATIONAL FLUID DYNAMICS [J].
Bettega, Rodrigo ;
Guimaraes-Correa, Ronaldo ;
Freire, Jose Teixeira .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2009, 87 (02) :193-203
[8]  
Cammarata L, 2003, INT J CHEM REACT ENG, V1
[9]   A BUBBLING FLUIDIZATION MODEL USING KINETIC-THEORY OF GRANULAR FLOW [J].
DING, J ;
GIDASPOW, D .
AICHE JOURNAL, 1990, 36 (04) :523-538
[10]   Computational fluid dynamics (CFD) modeling of spouted bed: Assessment of drag coefficient correlations [J].
Du, W ;
Bao, XJ ;
Xu, J ;
Wei, WS .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (05) :1401-1420