Simulation of chemical reaction process in gas-particle CFB downers by anisotropic turbulent mass transfer model

被引:3
作者
Li, Wenbin [1 ]
Yu, Kuotsung [2 ]
Yuan, Xigang [2 ]
Shao, Yuanyuan [1 ]
Zhu, Jesse [1 ,3 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Tianjin 300072, Peoples R China
[2] Tianjin Univ, Sch Chem Engn & Technol, State Key Lab Chem Engn, Tianjin 300072, Peoples R China
[3] Univ Western Ontario, Dept Chem & Biochem Engn, Particle Technol Res Ctr, London, ON, Canada
关键词
Circulating fluidized bed downer; Gas-solid two-phase mass transfer; Anisotropic turbulent mass; diffusion; Computational fluid dynamics; CIRCULATING FLUIDIZED-BED; CRACKING REACTION; TRANSFER COEFFICIENT; DYNAMICS SIMULATION; HYDRODYNAMICS; RISERS; REACTORS; FLOW; DISPERSION; LIMESTONE;
D O I
10.1016/j.cherd.2018.01.039
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A recently developed model, called the Reynolds mass flux (RMF) model is adopted for the simulation of multiphase flow involving chemical reaction in gas-particle CFB downers. The newly deduced Reynolds mass flux equation is utilized for closing the turbulent mass transfer equation, thereby realizing the simulation of anisotropic turbulent mass transfer. The simulations are validated with experimental data in literatures. The results indicate that the turbulent mass diffusion in downers would show significant anisotropic character. (C) 2018 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:452 / 459
页数:8
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