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
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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 | |
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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