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

被引:298
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
相关论文
共 78 条
[1]   The role of meso-scale structures in rapid gas-solid flows [J].
Agrawal, K ;
Loezos, PN ;
Syamlal, M ;
Sundaresan, S .
JOURNAL OF FLUID MECHANICS, 2001, 445 :151-185
[2]   Assessment of rolling resistance models in discrete element simulations [J].
Ai, Jun ;
Chen, Jian-Fei ;
Rotter, J. Michael ;
Ooi, Jin Y. .
POWDER TECHNOLOGY, 2011, 206 (03) :269-282
[3]   Improvement, validation and application of CFD/DEM model to dense gas-solid flow in a fluidized bed [J].
Alobaid, Falah ;
Epple, Bernd .
PARTICUOLOGY, 2013, 11 (05) :514-526
[4]   Efficient parallel CFD-DEM simulations using OpenMP [J].
Amritkar, Amit ;
Deb, Surya ;
Tafti, Danesh .
JOURNAL OF COMPUTATIONAL PHYSICS, 2014, 256 :501-519
[5]   A FLUID MECHANICAL DESCRIPTION OF FLUIDIZED BEDS [J].
ANDERSON, TB ;
JACKSON, R .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04) :527-&
[6]   Drag force of intermediate Reynolds number flow past mono- and bidisperse arrays of spheres [J].
Beetstra, R. ;
van der Hoef, M. A. ;
Kuipers, J. A. M. .
AICHE JOURNAL, 2007, 53 (02) :489-501
[7]   Mixing and segregation in a bidisperse gas-solid fluidised bed: a numerical and experimental study [J].
Bokkers, GA ;
Annaland, MVS ;
Kuipers, JAM .
POWDER TECHNOLOGY, 2004, 140 (03) :176-186
[8]   A semi-empirical model for the drag force and fluid-particle interaction in polydisperse suspensions [J].
Cello, Fernando ;
Di Renzo, Alberto ;
Di Maio, Francesco Paolo .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (10) :3128-3139
[9]   Coupled discrete element and finite volume solution of two classical soil mechanics problems [J].
Chen, Feng ;
Drumm, Eric C. ;
Guiochon, Georges .
COMPUTERS AND GEOTECHNICS, 2011, 38 (05) :638-647
[10]   Modeling particle-laden flows: A research outlook [J].
Curtis, JS ;
van Wachem, B .
AICHE JOURNAL, 2004, 50 (11) :2638-2645