Numerical simulation on gas-solid two-phase turbulent flow in FCC riser reactors (I) turbulent gas-solid flow-reaction model

被引:0
|
作者
Gao, JS [1 ]
Xu, CM
Yang, GH
Guo, YC
Lin, WY
机构
[1] Petr Univ, State Key Lab Heavy Oil Proc, Beijing 102200, Peoples R China
[2] Tsing Hua Univ, Dept Engn Mech, Beijing 100084, Peoples R China
关键词
riser reactor; turbulent flow; gas-solid flow; flow-reaction model; numerical algorithm;
D O I
暂无
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Gas-solid two-phase turbulent flows, mass transfer, heat transfer and catalytic cracking reactions are known to exert interrelated influences in commercial fluid catalytic cracking (FCC)riser reactors. In the present paper, a three-dimensional turbulent gas-solid two-phase flow-reaction model for FCC riser reactors was developed. The model took into account the gas-solid two-phase turbulent flows, inter-phase heat transfer, mass transfer, catalytic cracking reactions and their interrelated influence. The k-V-k(p) two-phase turbulence model was employed and modified for the two-phase turbulent flow patterns with relatively high particle concentration. Boundary conditions for the flow-reaction model were given. Related numerical algorithm was formed and a numerical code was drawn up. Numerical modeling for commercial FCC riser reactors could be carried out with the presented model.
引用
收藏
页码:12 / 20
页数:9
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