Pressure drop for two phase counter-current flow in a packed column with a novel internal

被引:19
|
作者
Han, MH [1 ]
Lin, HF [1 ]
Yuan, YH [1 ]
Wang, DZ [1 ]
Jin, Y [1 ]
机构
[1] Tsing Hua Univ, Dept Chem Engn, Beijing 100084, Peoples R China
关键词
catalytic distillation; internal; pressure drop; cross flow; counter-current flow; model;
D O I
10.1016/S1385-8947(03)00059-7
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A novel internal made of several structured porous passages can eliminate excessive pressure drop and "flooding" in a packed column with conventional gas liquid counter-current flow. A pressure drop model is developed on the assumption that the internal part divides the gas flow into two branches, one of which contacts the liquid in a conventional counter-current flow and the other in a new cross current flow. The model shows that the gas velocity for counter-current flow in a column with these internal parts of 15-30% volume fraction is about 5-30% of that without the internal parts and more gas flows in the cross current pattern. Decreases in the gas velocity and liquid hold-up make the pressure drop low. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
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页码:179 / 187
页数:9
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