中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Multi-scale modeling of gas-liquid-solid three-phase fluidized beds using the EMMS method

文献类型:期刊论文

作者Jin, GD
刊名CHEMICAL ENGINEERING JOURNAL
出版日期2006-03-15
卷号117期号:1页码:1-11
关键词gas-liquid-solid three-phase fluidization multi-scale method EMMS model bubble diameter bubble wake
ISSN号1385-8947
其他题名Chem. Eng. J.
中文摘要A multi-scale model for the gas-liquid-solid three-phase fluidized beds is developed on the basis of the principles of the EMMS model. For this purpose, the flowing structure in the gas-liquid-solid system is divided into five phases and considered under different spatial scales: a solid-liquid phase describing the micro-scale interaction between solid particles and liquid, a gas phase, a bubble wake phase and two inter-phases that, respectively, describe the meso-scale interaction of the dispersed bubbles and bubble wakes with the surrounding liquid-solid pseudo-homogeneous suspension. In order to obtain the steady state of such a system with eight unknowns, in addition to seven mass and momentum conservation conditions and an inequality constraint for the mean bubble diameter, the stability condition N-st -> min is used. The model is solved and checked with the experimental data available in several references which cover a broad range of operating conditions from the conventional expanded fluidized bed to the circulating fluidized bed, indicating that the model is capable of describing the global hydrodynamics of the complex flow in the three-phase system with acceptable accuracy. (c) 2005 Elsevier B.V. All rights reserved.
英文摘要A multi-scale model for the gas-liquid-solid three-phase fluidized beds is developed on the basis of the principles of the EMMS model. For this purpose, the flowing structure in the gas-liquid-solid system is divided into five phases and considered under different spatial scales: a solid-liquid phase describing the micro-scale interaction between solid particles and liquid, a gas phase, a bubble wake phase and two inter-phases that, respectively, describe the meso-scale interaction of the dispersed bubbles and bubble wakes with the surrounding liquid-solid pseudo-homogeneous suspension. In order to obtain the steady state of such a system with eight unknowns, in addition to seven mass and momentum conservation conditions and an inequality constraint for the mean bubble diameter, the stability condition N-st -> min is used.
WOS标题词Science & Technology ; Technology
类目[WOS]Engineering, Environmental ; Engineering, Chemical
研究领域[WOS]Engineering
关键词[WOS]MASS-TRANSFER ; BUBBLE ; SIMULATION ; SYSTEMS ; HYDRODYNAMICS ; SIMILITUDE ; TURBULENCE ; PARTICLE ; COLUMN ; FLOW
收录类别SCI
原文出处://WOS:000235859400001
语种英语
WOS记录号WOS:000235859400001
公开日期2013-10-24
版本出版稿
源URL[http://ir.ipe.ac.cn/handle/122111/4023]  
专题过程工程研究所_研究所(批量导入)
作者单位1.Chinese Acad Sci, Inst Proc Engn, Beijing 100080, Peoples R China
2.Chinese Acad Sci, Inst Proc Engn, Beijing 100080, Peoples R China
推荐引用方式
GB/T 7714
Jin, GD. Multi-scale modeling of gas-liquid-solid three-phase fluidized beds using the EMMS method[J]. CHEMICAL ENGINEERING JOURNAL,2006,117(1):1-11.
APA Jin, GD.(2006).Multi-scale modeling of gas-liquid-solid three-phase fluidized beds using the EMMS method.CHEMICAL ENGINEERING JOURNAL,117(1),1-11.
MLA Jin, GD."Multi-scale modeling of gas-liquid-solid three-phase fluidized beds using the EMMS method".CHEMICAL ENGINEERING JOURNAL 117.1(2006):1-11.

入库方式: OAI收割

来源:过程工程研究所

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