CFD prediction of segregating fluidized bidisperse mixtures of particles differing in size and density in gas-solid fluidized beds

被引:52
作者
Coroneo, M. [1 ]
Mazzei, L. [2 ]
Lettieri, P. [2 ]
Paglianti, A. [1 ]
Montante, G. [1 ]
机构
[1] Univ Bologna, Dept Chem Min & Environm Engn, I-40131 Bologna, Italy
[2] UCL, Dept Chem Engn, London WC1E 7JE, England
关键词
Fluidization; Solids mixture; Segregation; CFD; Gas-fluidized bed; Multiphase flow; KINETIC-THEORY; DISCRETE PARTICLE; GRANULAR FLOW; NUMERICAL-SIMULATION; BINARY-MIXTURES; VALIDATION; DYNAMICS; MODELS;
D O I
10.1016/j.ces.2011.02.019
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work investigates the capability of a fully predictive computational fluid dynamics method to catch the main features of binary segregating fluidized beds of particles differing in size and density. In particular, the numerical solution of a multiphase fluid-dynamic model based on an Eulerian description of both the continuous and the two dispersed phases and the kinetic theory of granular flows for modelling the inter-particle interactions is considered. The results obtained under a number of different operating conditions are compared with experimental data reported in the literature and the effect of grid size, time step and discretization schemes for the convective terms on axial segregation is also discussed. The capability of the model to correctly predict the minimum fluid velocity at which the mixture becomes steadily fluidized and fully mixed is also tested. Our calculations demonstrate that firm conclusions on the CFD model reliability in the prediction of the segregation dynamics in fluidized beds can be drawn only after careful verification of numerical uncertainties at the operating conditions under investigation. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2317 / 2327
页数:11
相关论文
共 56 条
[1]   A FLUID MECHANICAL DESCRIPTION OF FLUIDIZED BEDS [J].
ANDERSON, TB ;
JACKSON, R .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04) :527-&
[2]  
[Anonymous], 1987, US
[3]   Numerical study of segregation using a new drag force correlation for polydisperse systems derived from lattice-Boltzmann simulations [J].
Beetstra, R. ;
van der Hoef, M. A. ;
Kuipers, J. A. M. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :246-255
[4]   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
[5]   Analysis of the bubbling behaviour of 2D gas solid fluidized beds Part II. Comparison between experiments and numerical simulations via Digital Image Analysis Technique [J].
Busciglio, Antonio ;
Vella, Giuseppa ;
Micale, Giorgio ;
Rizzuti, Lucio .
CHEMICAL ENGINEERING JOURNAL, 2009, 148 (01) :145-163
[6]  
Chapman S., 1970, The mathematical theory of non-uniform gases
[7]   FLUIDIZED BINARY-MIXTURES IN WHICH THE DENSER COMPONENT MAY BE FLOTSAM [J].
CHIBA, S ;
NIENOW, AW ;
CHIBA, T ;
KOBAYASHI, H .
POWDER TECHNOLOGY, 1980, 26 (01) :1-10
[8]   Numerical simulation of particulate flow by the Eulerian-Lagrangian and the Eulerian-Eulerian approach with application to a fluidized bed [J].
Chiesa, M ;
Mathiesen, V ;
Melheim, JA ;
Halvorsen, B .
COMPUTERS & CHEMICAL ENGINEERING, 2005, 29 (02) :291-304
[9]   Uncertainties and CFD code validation [J].
Coleman, HW ;
Stern, F .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 1997, 119 (04) :795-803
[10]   CFD simulations of particle mixing in a binary fluidized bed [J].
Cooper, S ;
Coronella, CJ .
POWDER TECHNOLOGY, 2005, 151 (1-3) :27-36