Modeling the Mean Residence Time of Liquid Phase in the Gas-Liquid Cyclone

被引:4
|
作者
Yang, Junwei [1 ]
Zhang, Xupeng [2 ]
Shen, Guoping [1 ]
Xiao, Jiazhi [1 ]
Jin, Youhai [1 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
[2] Shandong Shtar Sci & Technol Petrochem Co Ltd, Rizhao 276806, Peoples R China
基金
中国博士后科学基金;
关键词
REACTOR; FLOW; PYROLYSIS; DRYER;
D O I
10.1021/acs.iecr.5b02617
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Residence time is a key parameter for the cyclones with mass transfer or reaction process. A model for the cylinder-on-cone cyclone was presented to calculate the mean residence time of the liquid phase, based on a force balance on the wall film. This model was validated using an experiment, which measured the residence time of the liquid phase by the hold-up method. The results demonstrated that the predicted residence times are in good overall agreement with the measured values. Furthermore, the liquid residence time decreases obviously with increasing droplets loading, and decreases less with increasing inlet velocity. The liquid residence time increases with the cylinder diameter. The wall film velocity, however, decreases with increasing cylinder diameter, because the perimeter of liquid wall film is directly proportional to the cylinder diameter.
引用
收藏
页码:10885 / 10892
页数:8
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