ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received December 28, 2006
Accepted June 28, 2007
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

Improved algorithm for calculation of binary liquid-liquid equilibrium compositions with NRTL model based on equal area rule

School of Chemical Engineering & Institute of Chemical Processes, Seoul National University, Shinlim-dong, Gwanak-gu, Seoul 151-744, Korea
Korean Journal of Chemical Engineering, March 2008, 25(2), 345-353(9), 10.1007/s11814-008-0057-7
downloadDownload PDF

Abstract

Typical methods for calculation of binary liquid-liquid equilibrium compositions such as surfactant systems need proper initial guesses and/or checking the sign of the second derivative of molar Gibbs energy change of mixing, ΔG. Eubank and Hall [1] have shown the equal area rule (EAR) applies to the composition derivative of the Gibbs energy of a binary system at fixed pressure and temperature. Methods based on EAR do not need to check the sign of the second derivative of ΔG because EAR is a necessary and sufficient condition for phase equilibrium. However, the algorithm proposed by Eubank and Hall needs a reasonable initial guess. Furthermore, it is not easy to apply the algorithm to activity coefficient models such as Non-Random Two Liquid (NRTL) because the first and second derivatives of ΔG as a function of composition have various shapes for some sets of NRTL parameters. In this work, we have developed an improved algorithm for calculation of binary liquid-liquid equilibrium compositions based on EAR considering the various shapes of NRTL model. This algorithm needs neither any initial guess nor checking the sign of the second derivative of ΔG.

References

Eubank PT, Hall KR, AIChE J., 41(4), 924 (1995)
Prausnitz JM, Lichtenthaler RN, de Azevedo EG, Molecular thermodynamics of fluid-phase equilibria, 3rd ed., Prentice-Hall, Englewood Cliffs, NJ (1999)
Shyu GS, Hanif NS, Alvarado JF, Hall KR, Eubank PT, Ind. Eng. Chem. Res., 34(12), 4562 (1995)
Renon H, Prausnitz JM, AIChE J., 14, 135 (1968)
Sφrensen JM, Arlt W, Liquid-liquid equilibrium data collection, Vol. 1: Binary Systems, DECHEMA, Germany (1979)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
TEL. No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로