Discrete element investigation of flow patterns and segregation in a spheronizer

被引:15
作者
Bouffard, J. [1 ]
Bertrand, F. [1 ]
Chaouki, J. [1 ]
Dumont, H. [2 ]
机构
[1] Ecole Polytech, Dept Chem Engn, Stn Ctr Ville, PQ H3C 3A7, Canada
[2] Merck Frosst Canada Ltd, Pharmaceut Res & Dev, Kirkland, PQ H9H 3L1, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Spheronizer; Mixing; Segregation; Discrete element method; Flow pattern; Shear rate; SIMULATION; FRICTION; PARTICLE;
D O I
10.1016/j.compchemeng.2012.09.023
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
Powder flow in a spheronizer is characterized by a toroidal motion and the flow patterns depend on the disc velocity and the fill level, but also on the particle properties. This work investigates numerically, with a discrete element method (DEM), the impact of these parameters on segregation patterns and the flow dynamics for bidisperse particle size distributions. Characterization of the segregation, by means of a mixing index and the relation with the shear stress in the toroidal domain, is presented. Characteristics, such as mixing curves, concentration profiles and azimuthal velocity correlations, are discussed. A logarithmic expression has been developed to account for the shear stress on the evolution of the azimuthal velocity inside the particulate bed. The combination of the mixing indexes and the concentration profiles is used to quantify the changes observed on the segregation when the fill level and the rotational rate of the spheronizer disk are varied. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:170 / 182
页数:13
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