Particle scale modelling of the multiphase flow in a dense medium cyclone: Effect of vortex finder outlet pressure

被引:34
作者
Chu, K. W. [1 ]
Wang, B. [1 ,3 ]
Yu, A. B. [1 ]
Vince, A. [2 ]
机构
[1] Univ New S Wales, Lab Simulat & Modelling Particulate Syst, Sch Mat Sci & Engn, Sydney, NSW 2052, Australia
[2] Elsa Consulting Grp Pty Ltd, Mt Pleasant, Qld 4740, Australia
[3] Lanzhou Univ, Key Lab Western Chinas Environm Syst, Coll Earth & Environm Sci, Lanzhou 730000, Peoples R China
关键词
Dense medium cyclone; Multiphase flow; Computational fluid dynamics; Discrete element method; Vortex finder pressure; GAS-SOLID FLOW; NUMERICAL-SIMULATION; FLUIDIZED-BEDS; PERFORMANCE; SYSTEMS; HYDROCYCLONE; SEPARATION; BEHAVIOR; COALS; SIZE;
D O I
10.1016/j.mineng.2011.11.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Dense medium cyclone (DMC) is widely used to upgrade run-of-mine coal in the coal industry. In practice, different designs of the outlet geometry of the vortex finder are used to achieve different purposes. However, the underlying mechanisms are not well understood. In this work, this phenomenon is studied numerically with reference to the effect of the pressure at the vortex finder. The simulation is carried out by use of a combined approach of computational fluid dynamics (CFD) and discrete element method (DEM) (CFD-DEM). In the model, DEM is used to describe the motion of discrete coal particles, and CFD to describe the motion of medium slurry which is a mixture of gas, water and fine magnetite particles. It is shown that a relatively small change of the vortex finder pressure can cause significant variations of both the medium-coal flow and DMC performance. An important finding is that the flow direction of the axial velocity of the air phase in the "air-core" could reverse (changing from upward to downward) as the vortex finder pressure increases, which results in the downward viscous drag force on coal particles and consequently causes some low density coal to be misplaced to the reject/underflow. This work suggests that the control of the pressure at the outlet of the vortex finder is important for DMC performance. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:46 / 58
页数:13
相关论文
共 46 条
  • [1] [Anonymous], FLUENT VER 6 2
  • [2] Chu K., 2010, J. Comput. Multiphase Flows, V2, P249
  • [3] Numerical simulation of the gas-solid flow in three-dimensional pneumatic conveying bends
    Chu, K. W.
    Yu, A. B.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (18) : 7058 - 7071
  • [4] Numerical simulation of complex particle-fluid flows
    Chu, K. W.
    Yu, A. B.
    [J]. POWDER TECHNOLOGY, 2008, 179 (03) : 104 - 114
  • [5] CFD-DEM simulation of the gas-solid flow in a cyclone separator
    Chu, K. W.
    Wang, B.
    Xu, D. L.
    Chen, Y. X.
    Yu, A. B.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2011, 66 (05) : 834 - 847
  • [6] CFD-DEM study of the effect of particle density distribution on the multiphase flow and performance of dense medium cyclone
    Chu, K. W.
    Wang, B.
    Yu, A. B.
    Vince, A.
    Barnett, G. D.
    Barnett, P. J.
    [J]. MINERALS ENGINEERING, 2009, 22 (11) : 893 - 909
  • [7] CFD-DEM modelling of multiphase flow in dense medium cyclones
    Chu, K. W.
    Wang, B.
    Yu, A. B.
    Vince, A.
    [J]. POWDER TECHNOLOGY, 2009, 193 (03) : 235 - 247
  • [8] DISCRETE NUMERICAL-MODEL FOR GRANULAR ASSEMBLIES
    CUNDALL, PA
    STRACK, ODL
    [J]. GEOTECHNIQUE, 1979, 29 (01): : 47 - 65
  • [9] Homogeneous and bubbling fluidization regimes in DEM-CFD simulations: Hydrodynamic stability of gas and liquid fluidized beds
    Di Renzo, Alberto
    Di Maio, Francesco Paolo
    [J]. CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) : 116 - 130
  • [10] 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