4.5 Article

CFD-DEM simulation of spouting of corn-shaped particles

期刊

PARTICUOLOGY
卷 10, 期 5, 页码 562-572

出版社

ELSEVIER SCIENCE INC
DOI: 10.1016/j.partic.2012.03.011

关键词

Gas-solid flow; Discrete element method; Spouted bed; Corn-shaped particle; Multi-sphere method

资金

  1. National Natural Science Foundation of China [50976025]
  2. Major State Basic Research Development Program of China [2011CB201505]
  3. Foundation of Graduate Creative Program of Jiangsu [CXZZ-0148]
  4. Scientific Research Foundation of Graduate School of Southeast University [YBJJ1107]

向作者/读者索取更多资源

Three dimensionally coupled computational fluid dynamics (CFD) and discrete element method (DEM) were used to investigate the flow of corn-shaped particles in a cylindrical spouted bed with a conical base. The particle motion was modeled by the DEM, and the gas motion by the k-epsilon two-equation turbulent model. A two-way coupling numerical iterative scheme was used to incorporate the effects of gas-particle interactions in terms of momentum exchange. The corn-shaped particles were constructed by a multi-sphere method. Drag force, contact force, Saffman lift force, Magnus lift force, and gravitational force acting on each individual particle were considered in establishing the mathematical modeling. Calculations were carried out in a cylindrical spouted bed with an inside diameter of 200 mm, a height of 700 mm, and a conical base of 60 degrees. Comparison of simulations with experiments showed the availability of the multi-sphere method in simulating spouting action with corn-shaped particles, but it depended strongly on the number and the arrangement of the spherical elements. Gas-solid flow patterns, pressure drop, particle velocity and particle concentration at various spouting gas velocity were discussed. The results showed that particle velocity reaches a maximum at the axis and then decreases gradually along the radial direction in the whole bed. Particle concentration increases along the radial direction in the spout region but decreases in the fountain region, while it is nearly constant in the annulus region. Increasing spouting gas velocity leads to larger pressure drop, remarkably increased speed of particle moving upward or downward, but decreased particle concentration. (c) 2012 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.

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