Influence of void fraction calculation on fidelity of CFD-DEM simulation of gas-solid bubbling fluidized beds

被引:281
|
作者
Peng, Zhengbiao [1 ]
Doroodchi, Elham [1 ]
Luo, Caimao [2 ]
Moghtaderi, Behdad [2 ]
机构
[1] Univ Newcastle, Prior Res Ctr Adv Particle Proc & Transport, Discipline Chem Engn, Sch Engn, Callaghan, NSW 2308, Australia
[2] Univ Newcastle, Sch Engn, Discipline Chem Engn, Callaghan, NSW 2308, Australia
基金
澳大利亚研究理事会;
关键词
solids processing; CFD; particulate flows; fluidization; numerical solutions; DISCRETE PARTICLE SIMULATION; LATTICE-BOLTZMANN SIMULATIONS; ROLLING FRICTION; NUMERICAL-SIMULATION; DYNAMIC SIMULATION; BIDISPERSE ARRAYS; DRAG FORCE; FLOW; MODEL; ELEMENT;
D O I
10.1002/aic.14421
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The correct calculation of cell void fraction is pivotal in accurate simulation of two-phase flows using a computational fluid dynamics-discrete element method (CFD-DEM) approach. Two classical approaches for void fraction calculations (i.e., particle centroid method or PCM and analytical approach) were examined, and the accuracy of these methodologies in predicting the particle-fluid flow characteristics of bubbling fluidized beds was investigated. It was found that there is a critical cell size (3.82 particle diameters) beyond which the PCM can achieve the same numerical stability and prediction accuracy as those of the analytical approach. There is also a critical cell size (1/19.3 domain size) below which meso-scale flow structures are resolved. Moreover, a lower limit of cell size (1.63 particle diameters) was identified to satisfy the assumptions of CFD-DEM governing equations. A reference map for selecting the ideal computational cell size and the suitable approach for void fraction calculation was subsequently developed. (c) 2014 American Institute of Chemical Engineers AIChE J, 60: 2000-2018, 2014
引用
收藏
页码:2000 / 2018
页数:19
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