ON THE EFFICIENCY OF DISCRETE PARTICLE MODELING OF GAS-SOLID FLUIDIZED BED REACTOR

被引:0
作者
Wu, C. L. [1 ]
Berrouk, A. S. [2 ]
Nandakumar, K. [2 ]
机构
[1] Guangdong Ocean Univ, Coll Engn, Zhanjiang 534088, Peoples R China
[2] Petr Inst, Chem Engn Program, Abu Dhabi, U Arab Emirates
来源
CBEE 2009: PROCEEDINGS OF THE 2009 INTERNATIONAL CONFERENCE ON CHEMICAL, BIOLOGICAL AND ENVIRONMENTAL ENGINEERING | 2010年
关键词
SIMULATION; DYNAMICS;
D O I
10.1142/9789814295048_0049
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A robust three-dimensional discrete particle model (3D DPM) for unstructured meshes is presented to model the gas-solid flows in fluidized beds. Inter-particle interactions are taken into account through a hard-sphere approach. A multifaceted numerical strategy is developed to enhance the computational efficiency. Simulation results demonstrate the ability of the model to capture many important characteristics such as spouting, particle clustering and core-annulus flow structures in gas-solid fluidization systems at specified operating conditions.
引用
收藏
页码:235 / +
页数:2
相关论文
共 10 条
[1]  
Gidaspow D., 1994, Multiphase Flow and Fluidization, P1
[2]   Hydrodynamic modelling of dense gas-fluidised beds: comparison and validation of 3D discrete particle and continuum models [J].
Goldschmidt, MJV ;
Beetstra, R ;
Kuipers, JAM .
POWDER TECHNOLOGY, 2004, 142 (01) :23-47
[3]   Discrete particle simulation of bubble and slug formation in a two-dimensional gas-fluidised bed: A hard-sphere approach [J].
Hoomans, BPB ;
Kuipers, JAM ;
Briels, WJ ;
vanSwaaij, WPM .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (01) :99-118
[4]   3-DIMENSIONAL FLOW VISUALIZATION OF DILUTELY DISPERSED SOLIDS IN BUBBLING AND CIRCULATING FLUIDIZED-BEDS [J].
HORIO, M ;
KUROKI, H .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (15) :2413-2421
[5]   EFFICIENT ALGORITHMS FOR MANY-BODY HARD PARTICLE MOLECULAR-DYNAMICS [J].
MARIN, M ;
RISSO, D ;
CORDERO, P .
JOURNAL OF COMPUTATIONAL PHYSICS, 1993, 109 (02) :306-317
[6]   Particle-motion-resolved discrete model for simulating gas-solid fluidization [J].
Ouyang, J ;
Li, JH .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) :2077-2083
[7]   DISCRETE PARTICLE SIMULATION OF 2-DIMENSIONAL FLUIDIZED-BED [J].
TSUJI, Y ;
KAWAGUCHI, T ;
TANAKA, T .
POWDER TECHNOLOGY, 1993, 77 (01) :79-87
[8]   Dense particulate flow model on unstructured mesh [J].
Wu, C. L. ;
Zhan, J. M. ;
Li, Y. S. ;
Lam, K. S. .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (17) :5726-5741
[9]   Accurate void fraction calculation for three-dimensional discrete particle model on unstructured mesh [J].
Wu, C. L. ;
Zhan, J. M. ;
Li, Y. S. ;
Lam, K. S. ;
Berrouk, A. S. .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (06) :1260-1266
[10]   DEM simulation of the particle dynamics in two-dimensional spouted beds [J].
Zhao, X-L. ;
Li, S. -Q. ;
Liu, G. -Q. ;
Yao, Q. ;
Marshall, J. -S. .
POWDER TECHNOLOGY, 2008, 184 (02) :205-213