Prediction of mass transfer columns with dumped and arranged packings - Updated summary of the calculation method of Billet and Schultes

被引:335
作者
Billet, R
Schultes, M
机构
[1] Raschig GmbH, D-67061 Ludwigshafen, Germany
[2] Ruhr Univ Bochum, D-4630 Bochum, Germany
关键词
packings; mass transfer; mass transfer coefficients; pressure drop; loading point; flooding point; liquid holdup;
D O I
10.1205/026387699526520
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A good knowledge of the relationship between the two-phase countercurrent flow of a packed mass transfer column is essential for the design of rectification, absorption and desorption columns. Based on a physical model the authors describe their updated equations for calculating gas and liquid side mass transfer coefficients, pressure drop of dry or irrigated random and structured packings, their loading and flooding points as well as their liquid holdup. Based on one of the largest experimental databases in the world, the calculated results give only small deviations from the database.
引用
收藏
页码:498 / 504
页数:7
相关论文
共 12 条
[2]   Fluid dynamics and mass transfer in the total capacity range of packed columns up to the flood point [J].
Billet, R ;
Schultes, M .
CHEMICAL ENGINEERING & TECHNOLOGY, 1995, 18 (06) :371-379
[3]  
BILLET R, 1987, I CHEM E S SER, V104, pB255
[4]  
BILLET R, 1991, BEITRAGE VERFAHRENS, P88
[5]  
Billet R., 1993, CHEM ENG TECHNOL, V16, P1, DOI [10.1002/ceat.270160102, DOI 10.1002/CEAT.270160102]
[6]  
BILLET R, 1987, I CHEM E S SER, V104, pA171
[7]  
Billet R., 1993, Chem. Eng. Technol., V16, P370
[8]  
Billet R, 1995, Packed towers in processing and environmental technology
[9]  
Billet R., 1991, CHEM ENG TECHNOL, V14, P89, DOI [10.1002/ceat.270140203, DOI 10.1002/CEAT.270140203]
[10]  
BILLET R, 1983, FESTSCHRIFT FAKULTAT, P24