中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Multiscale analysis and modeling of multiphase chemical reactors

文献类型:会议论文

作者Bi, Hsiaotao T.1,2; Li, Jinghai1
出版日期1905-06-26
关键词Fluidized beds - Heat transfer - Iterative methods - Mass transfer - Molecular structure - Multiphase flow - Reaction kinetics
卷号15
期号6
DOI10.1163/1568552042456223
页码607-627
英文摘要Multiphase gas-solids fluidized bed reactors are of multiscale structure, i.e. single particles, particle clusters/bubbles and reactor vessel, and of multiple physics, i.e. hydrodynamics, heat and mass transfer, and reaction kinetics. The formation of complex structures/patterns in each regime is a result of a compromise between dominant mechanisms at multiple scales. Coupling of hydrodynamics, heat and mass transfer, and reaction kinetics takes place at molecular and particle levels where conductive and convective transfer and diffusion within the internal pores of the catalyst are accompanied by the adsorption, surface reaction and desorption of reactant and product on the surface. This work first presents an overview of the general multiscale approaches, including the sequential approach, iterative/concurrent approach and the variational multiscale approach, applicable to multiphase flow and reaction systems, followed by a review on multiscale modeling of gas-solids fluidized bed reactors including bubbling/turbulent and fast fluidized bed reactors. Finally, a multiscale circulating fluidized bed reactor model is outlined in which hydrodynamics are modeled by the combined energy-minimization multiscale/two-fluid computational fluid dynamics coupled with multiscale heat and mass transfer sub-models and reaction kinetics. The interaction and compromise among dominant mechanisms are represented by the variational criterion.
项目编号H. B. is grateful to the K. C. Wong Foundation for providing a research fellowship to support this work during his visit to the Institute of Process Engineering.
资助机构VSP BV
学科主题Chemical Reactors
源URL[http://ir.ipe.ac.cn/handle/122111/59608]  
作者单位1.Multi-phase Reaction Laboratory, Institute of Process Engineering, Chinese Academy of Sciences, PO Box 353, Beijing 100080, China
2.Fluidization Research Centre, Department of Chemical Engineering, University of British Columbia, Vancouver, BC V6T 1Z4, Canada
推荐引用方式
GB/T 7714
Bi, Hsiaotao T.,Li, Jinghai. Multiscale analysis and modeling of multiphase chemical reactors[C]. 见:.

入库方式: OAI收割

来源:过程工程研究所

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