A bubble-based EMMS model for gas-solid bubbling fluidization

被引:173
作者
Shi, Zhansheng [1 ,2 ]
Wang, Wei [1 ,2 ]
Li, Jinghai [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
[2] Chinese Acad Sci, Grad Univ, Beijing 100049, Peoples R China
关键词
Meso-scale; Fluidization; Bubble; Simulation; Hydrodynamics; Drag coefficient; CFD SIMULATION; MULTISCALE CFD; FLOW STRUCTURE; BED EXPANSION; FINE POWDERS; 2-PHASE FLOW; DENSE PHASE; HYDRODYNAMICS; PARTICLES; GELDART;
D O I
10.1016/j.ces.2011.07.020
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An EMMS/bubbling model for gas-solid bubbling fluidized bed was proposed based on the energy-minimization multi-scale (EMMS) method (Li and Kwauk, 1994). In this new model, the meso-scale structure was characterized with bubbles in place of clusters of the original EMMS method. Accordingly, the bubbling fluidized bed was resolved into the suspending and the energy-dissipation sub-systems over three sub-phases, i.e., the emulsion phase, the bubble phase and their inter-phase in-between. A stability condition of minimization of the energy consumption for suspending particles (N(5)-> min) was proposed, to close the hydrodynamic equations on these sub-phases. This bubble-based EMMS model has been validated and found in agreement with experimental data available in literature. Further, the unsteady-state version of the model was used to calculate the drag coefficient for two-fluid model (TFM). It was found that TFM simulation with EMMS/bubbling drag coefficient allows using coarser grid than that with homogeneous drag coefficient, resulting in both good predictability and scalability. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:5541 / 5555
页数:15
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