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
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