MULTICOMPONENT 3-PHASE AZEOTROPIC DISTILLATION .2. PHASE-STABILITY AND PHASE-SPLITTING ALGORITHMS

被引:48
作者
CAIRNS, BP [1 ]
FURZER, IA [1 ]
机构
[1] UNIV SYDNEY,DEPT CHEM ENGN,SYDNEY,NSW 2006,AUSTRALIA
关键词
D O I
10.1021/ie00103a041
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A literature review of three-phase distillation calculation procedures highlights the large number of efforts that have been made to account for the appearance of a second liquid phase on a distillation tray. The numerical problems due to the introduction of a second liquid phase during an iteration scheme are summarized in a table containing the known 15 solution sets. Many of these solutions contain a liquid-phase-splitting algorithm. A new algorithm based on Michelsen's phase-stability test and phase-splitting algorithm has been developed. New procedures in the iteration method and to identify liquid-phase instability have been produced and verified. These new procedures use analytical partial derivatives which can be determined from modern thermodynamic models to describe nonideal liquid-phase behavior. The predicted separation performance of a three-phase azeotropic distillation column using this new algorithm is in good agreement with the experimental data collected in part 1 of this series. © 1990, American Chemical Society. All rights reserved.
引用
收藏
页码:1364 / 1382
页数:19
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