CFD simulation and experiment of residence time distribution in short-contact cyclone reactors

被引:21
|
作者
Zhang, Yuchun [1 ]
Wang, Zhenbo [2 ]
Jin, Youhai [2 ]
Li, Zhihe [1 ]
Yi, Weiming [1 ]
机构
[1] Shandong Univ Technol, Sch Agr Engn & Food Sci, Zibo 255049, Shandong, Peoples R China
[2] China Univ Petr, State Key Lab Heavy Oil, Dongying 266580, Shandong, Peoples R China
关键词
Short-contact cyclone reactor; Gas-solid two phase; CFD; Residence time distribution; Tracer method; GAS-SOLID FLOW; FLUIDIZED-BED; DRAG MODELS; FAST PYROLYSIS; VALIDATION; REGION;
D O I
10.1016/j.apt.2015.05.009
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An Eulerian-Eulerian two-fluid model that incorporated the kinetic theory of granular flow was used to describe the gas-solid two-phase flow in short-contact cyclone reactors. By comparing with the experimental data, we found that the simulated data calculated with Gidaspow drag force model performs best. Besides, when the restitution coefficient is 0.95, the simulated results fit the best with experimental results. Then we mainly focused on the component concentration distribution and residence time distribution characteristics in this paper. The species transport method was validated for the prediction and a video camera and the colored particle tracer method were employed in the experiments. The results indicate that the vacuum gas oil (VGO) and catalysts flow down spirally along the wall and the gasoline and coke + dry gas are mostly in the central part, so the VGO has more contact time with catalysts than other components. The simulated results show a good agreement with the experimental data. (C) 2015 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.
引用
收藏
页码:1134 / 1142
页数:9
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