Microdynamic modelling and analysis of the mixing and segregation of binary mixtures of particles in gas fluidization

被引:102
作者
Feng, Y. Q. [1 ]
Yu, A. B. [1 ]
机构
[1] Univ New S Wales, Ctr Simulat & Modeling Particulate Syst, Sch Mat Sci & Engn, Sydney, NSW 2052, Australia
关键词
fluidization; segregation; mixing; discrete particle simulation; particle-fluid interaction; particle-particle interaction;
D O I
10.1016/j.ces.2006.08.015
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents a study of the mixing and segregation of particle mixtures in a gas-fluidized bed by means of a discrete particle simulation. Particle mixtures are composed of spherical particles with diameter 2 mm, for jetsam and I mm for flotsam. The particles are initially packed randomly in a rectangular bed and then fluidized by gas uniformly injected at the bottom of the bed. The gas injection velocity varies to cover fixed, partially and fully fluidized bed conditions, in order to establish a full picture about the effect of gas velocity. Segregation/mixing behaviour is analysed in terms of flow patterns, solid concentration profile and mixing kinetics. It is shown that segregation, as a transient process, is strongly affected by gas velocity. There is a gas velocity producing the maximum segregation for a given mixture. Below this velocity, segregation increases and above this velocity, segregation decreases with the increase of gas velocity. The time to reach a macroscopically stable state can be up to tens of seconds, decreasing with the increase of gas velocity. The mechanisms governing the segregation and mixing of particles are elucidated in terms of the interaction forces between particles and between particles and fluid. Particle-fluid interaction initiates fluidization and segregation. Particle-particle interaction, however, also plays an important role in governing the segregation of particles. The degree of segregation results from the complex dynamic balance of the two interactions either locally or globally. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:256 / 268
页数:13
相关论文
共 31 条
  • [1] Discrete particle simulation and visualized research of the gas-solid flow in an internally circulating fluidized bed
    Bin, Y
    Zhang, MC
    Dou, BL
    Song, YB
    Wu, J
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (01) : 214 - 221
  • [2] DISCRETE NUMERICAL-MODEL FOR GRANULAR ASSEMBLIES
    CUNDALL, PA
    STRACK, ODL
    [J]. GEOTECHNIQUE, 1979, 29 (01): : 47 - 65
  • [3] THE VOIDAGE FUNCTION FOR FLUID PARTICLE INTERACTION SYSTEMS
    DIFELICE, R
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1994, 20 (01) : 153 - 159
  • [4] Assessment of model formulations in the discrete particle simulation of gas-solid flow
    Feng, YQ
    Yu, AB
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (26) : 8378 - 8390
  • [5] Discrete particle simulation of gas fluidization of particle mixtures
    Feng, YQ
    Xu, BH
    Zhang, SJ
    Yu, AB
    Zulli, P
    [J]. AICHE JOURNAL, 2004, 50 (08) : 1713 - 1728
  • [6] Numerical study of gas-solid flow in the raceway of a blast furnace
    Feng, YQ
    Pinson, D
    Yu, AB
    Chew, SJ
    Zulli, P
    [J]. STEEL RESEARCH INTERNATIONAL, 2003, 74 (09) : 523 - 530
  • [7] Gidaspow D., 1994, MULTIPHASE FLOW FLUI
  • [8] DEM simulation for attrition of salt during dilute-phase pneumatic conveying
    Han, T
    Levy, A
    Kalman, H
    [J]. POWDER TECHNOLOGY, 2003, 129 (1-3) : 92 - 100
  • [9] Numerical study of cluster formation in a gas-particle circulating fluidized bed
    Helland, E
    Occelli, R
    Tadrist, L
    [J]. POWDER TECHNOLOGY, 2000, 110 (03) : 210 - 221
  • [10] Granular dynamics simulation of segregation phenomena in bubbling gas-fluidised beds
    Hoomans, BPB
    Kuipers, JAM
    van Swaaij, WPM
    [J]. POWDER TECHNOLOGY, 2000, 109 (1-3) : 41 - 48