CFD-DEM study of effect of bed thickness for bubbling fluidized beds
被引:80
作者:
Li, Tingwen
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机构:
Natl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USA
URS Corp, Morgantown, WV 26505 USANatl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USA
Li, Tingwen
[1
,2
]
Gopalakrishnan, Pradeep
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h-index: 0
机构:
Natl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USA
Virginia Tech, Dept Mech Engn, Blacksburg, VA 24061 USANatl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USA
Gopalakrishnan, Pradeep
[1
,3
]
Garg, Rahul
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机构:
Natl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USA
URS Corp, Morgantown, WV 26505 USANatl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USA
Garg, Rahul
[1
,2
]
Shahnam, Mehrdad
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h-index: 0
机构:
Natl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USANatl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USA
Shahnam, Mehrdad
[1
]
机构:
[1] Natl Energy Technol Lab, Dept Energy, Morgantown, WV 26505 USA
[2] URS Corp, Morgantown, WV 26505 USA
[3] Virginia Tech, Dept Mech Engn, Blacksburg, VA 24061 USA
Bubbling fluidized bed;
CFD;
Wall effect;
Discrete element method;
Pseudo-2D;
Flow hydrodynamics;
DIGITAL IMAGE-ANALYSIS;
EXPERIMENTAL VALIDATION;
NUMERICAL-SIMULATION;
PART I;
HYDRODYNAMICS;
VELOCITY;
BEHAVIOR;
FLOWS;
MODEL;
SOFTWARE;
D O I:
10.1016/j.partic.2012.02.006
中图分类号:
TQ [化学工业];
学科分类号:
081705 [工业催化];
摘要:
The effect of bed thickness in rectangular fluidized beds is investigated through the CFD-DEM simulations of small-scale systems. Numerical results are compared for bubbling fluidized beds of various bed thicknesses with respect to particle packing, bed expansion, bubble behavior, solids velocities, and particle kinetic energy. Good two-dimensional (2D) flow behavior is observed in the bed having a thickness of up to 20 particle diameters. However, a strong three-dimensional (3D) flow behavior is observed in beds with a thickness of 40 particle diameters, indicating the transition from 2D flow to 3D flow within the range of 20-40 particle diameters. Comparison of velocity profiles near the walls and at the center of the bed shows significant impact of the front and back walls on the flow hydrodynamics of pseudo-2D fluidized beds. Hence, for quantitative comparison with experiments in pseudo-2D columns, the effect of walls has to be accounted for in numerical simulations. (c) 2012 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.