中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Comparison of two-fluid and discrete particle modeling of gas-particle flows in micro fluidized beds

文献类型:期刊论文

作者Liu, Xu1,2; Su, Jinglin2; Qian, Yanan1,2; Cui, Lijie1; Liu, Xiaoxing1,2
刊名POWDER TECHNOLOGY
出版日期2018-10-01
卷号338页码:79-86
ISSN号0032-5910
关键词Micro Fluidized Beds Cfd-dem Two-fluid Model Regime Transition Boundary Condition
DOI10.1016/j.powtec.2018.06.039
英文摘要

The formation of a more porous zone in the near wall region has been commonly suggested to be one of the main mechanisms of the delayed onset of fluidization in micro fluidized beds (MFBs). If such geometrical effect still plays a major role once the bed is fluidized, it will challenge the applications of Two-Fluid Model (TFM) to simulate micro fluidized beds. In this work this issue is assessed by taking the simulation results of the Computational Fluid Dynamics coupled with the Discrete Element Method (CFD-DEM) as the benchmark data. Both the delayed onset of fluidization and the advanced onset of turbulent fluidization predicted by CFD-DEM simulations are successfully captured by the TFM simulations. The radial profiles of solids volume fraction and solids axial velocity predicted by TFM and CFD-DEM simulations are also in well agreement. Such results demonstrate that TFM can be appropriately used to model micro fluidized beds systems. Parameter analyses show that TFM simulation results are closely related to the input parameter setting. The minimum bubbling velocity predicted by TFM simulations closely depends on the chosen value of frictional packing limit. And the specularity coefficient has a significant impact on the predicted solids flow behavior. (C) 2018 Published by Elsevier B.V.

WOS关键词Reaction Analyzer ; Numerical Simulations ; Membrane Reactors ; Solid Reactions ; Fixed-beds ; Cfd ; Velocity ; Hydrodynamics ; Diameter ; Gasification
资助项目National Natural Science Foundation of China[21576265]
WOS研究方向Engineering
语种英语
出版者ELSEVIER SCIENCE BV
WOS记录号WOS:000447569200009
资助机构National Natural Science Foundation of China
源URL[http://ir.ipe.ac.cn/handle/122111/26159]  
专题中国科学院过程工程研究所
通讯作者Cui, Lijie; Liu, Xiaoxing
作者单位1.Univ Chinese Acad Sci, Beijing 100049, Peoples R China
2.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
推荐引用方式
GB/T 7714
Liu, Xu,Su, Jinglin,Qian, Yanan,et al. Comparison of two-fluid and discrete particle modeling of gas-particle flows in micro fluidized beds[J]. POWDER TECHNOLOGY,2018,338:79-86.
APA Liu, Xu,Su, Jinglin,Qian, Yanan,Cui, Lijie,&Liu, Xiaoxing.(2018).Comparison of two-fluid and discrete particle modeling of gas-particle flows in micro fluidized beds.POWDER TECHNOLOGY,338,79-86.
MLA Liu, Xu,et al."Comparison of two-fluid and discrete particle modeling of gas-particle flows in micro fluidized beds".POWDER TECHNOLOGY 338(2018):79-86.

入库方式: OAI收割

来源:过程工程研究所

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