Hydrodynamic modelling of binary mixture in a gas bubbling fluidized bed using the kinetic theory of granular flow
被引:110
作者:
Lu, HL
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机构:
Harbin Inst Technol, Coll Energy Sci & Engn, Dept Power Engn, Harbin 150001, Peoples R ChinaHarbin Inst Technol, Coll Energy Sci & Engn, Dept Power Engn, Harbin 150001, Peoples R China
Lu, HL
[1
]
He, YR
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h-index: 0
机构:Harbin Inst Technol, Coll Energy Sci & Engn, Dept Power Engn, Harbin 150001, Peoples R China
He, YR
Gidaspow, D
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机构:Harbin Inst Technol, Coll Energy Sci & Engn, Dept Power Engn, Harbin 150001, Peoples R China
Gidaspow, D
机构:
[1] Harbin Inst Technol, Coll Energy Sci & Engn, Dept Power Engn, Harbin 150001, Peoples R China
[2] IIT, Dept Chem & Environm Engn, Chicago, IL 60613 USA
gas bubbling fluidized bed;
multi-fluid model;
kinetic theory of granular flow;
D O I:
10.1016/S0009-2509(02)00635-8
中图分类号:
TQ [化学工业];
学科分类号:
0817 [化学工程与技术];
摘要:
A multi-fluid Eularian CFD model with closure relationships according to the kinetic theory of granular flow has been applied to study the motions of particles in the gas bubbling fluidized bed with the binary mixtures. The mutual interactions between the gas and particles and the collisions among particles were taken into account. Simulated results shown that the hydrodynamics of gas bubbling fluidized bed related with the distribution of particle sizes and the amount of energy dissipated in particle-particle interaction. In order to obtain realistic bed dynamics from fundamental hydrodynamic models, it is important to correctly take the effect of particle size distribution and energy dissipation due to non-ideal particle-particle interactions into account. (C) 2003 Elsevier Science Ltd. All rights reserved.