CPFD simulation of cluster effect on mass transfer and reaction in downer with FCC particles

被引:5
作者
Liu, Yancong [1 ,2 ]
Shi, Xiaogang [1 ]
Wu, Yingya [1 ]
Wang, Chengxiu [1 ]
Gao, Jinsen [1 ]
Lan, Xingying [1 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[2] Monash Univ, Dept Chem Engn, ARC Res Hub Computat Particle Technol, Melbourne, Vic 3800, Australia
基金
中国国家自然科学基金;
关键词
Downer; Cluster; Ozone decomposition; CPFD; CIRCULATING FLUIDIZED-BED; SOLIDS FLOW STRUCTURE; PERFORMANCE EVALUATION; HYDRODYNAMICS; RISER; MODEL; BEHAVIOR;
D O I
10.1016/j.powtec.2022.117572
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, a cluster-based mass transfer and reaction model was proposed according to large number of simulation results by conducting ozone decomposition inside spherical cluster, which is more realistic compared with the conventional homogeneous description of mass transfer and chemical reaction process. Then, this model was coupled with three-dimensional Computational Particle Fluid Dynamics (CPFD) approach to simulate the ozone decomposition in pilot-scale gas-solids downer. According to the comparison between simulation results and experiment measurements, it was found that the model sufficiently considering the clustering effects on the hydrodynamics and chemical reaction predicted better ozone concentration distribution than the model based on homogeneous assumption. Meanwhile, the comprehensive model with consideration of cluster could accurately predict the gas-solids flow behaviors and reaction characteristics with different particle properties under different operating conditions. Finally, the effects of operating conditions such as superficial gas velocity and solids circulating flux on the hydrodynamics and reaction characteristics inside downer were fully analyzed on the basis of the accurate model predictions.
引用
收藏
页数:17
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