More operable fully thermally coupled distribution column configurations for multicomponent distillation

被引:50
作者
Agrawal, R [1 ]
机构
[1] Air Prod & Chem Inc, Allentown, PA 18195 USA
关键词
distillation; thermally coupled system; control; operability;
D O I
10.1205/026387699526449
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
More operable fully thermally coupled distillation column configurations do not have the classical problem of controlling vapour transfers from one column to another. A simple and easy to use procedure is presented to:draw all possible such distillation column configurations for the separation of an n-component feed mixture into n product streams, each enriched in one of the components. All the more operable fully thermally coupled configurations that can be derived from the known sequential and satellite column configurations are illustrated for four and five component feed mixtures. A brief discussion for the distillation of an n-component feed mixture in a single; column shell is also presented.
引用
收藏
页码:543 / 553
页数:11
相关论文
共 21 条
[1]   Are thermally coupled distillation columns always thermodynamically more efficient for ternary distillations? [J].
Agrawal, R ;
Fidkowski, ZT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (08) :3444-3454
[2]   More operable arrangements of fully thermally coupled distillation columns [J].
Agrawal, R ;
Fidkowski, ZT .
AICHE JOURNAL, 1998, 44 (11) :2565-2568
[3]   Synthesis of distillation column configurations for a multicomponent separation [J].
Agrawal, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (04) :1059-1071
[4]  
AUER H, 1997, AICHE M LOS ANG CA
[5]   Complex distillation arrangements: Extending the Petlyuk ideas [J].
Christiansen, AC ;
Skogestad, S ;
Lien, K .
COMPUTERS & CHEMICAL ENGINEERING, 1997, 21 :S237-S242
[6]  
Christiansen AC, 1997, ICHEME S SERIES, V142, P745
[7]   Optimal design of thermally coupled distillation columns [J].
Dünnebier, G ;
Pantelides, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (01) :162-176
[8]  
FIDKOWSKI ZT, 1987, AICHE J, V33, P654
[9]  
FRESHWATER DC, 1975, CHEM ENG, V301, P533
[10]  
HENLEY EJ, 1981, EQUILIBRIUM STAGE SE, P529