References for the UNIFAC method
- Last UpdatedAug 13, 2024
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Fredenslund, A.; Jones, R. L.; Prausnitz, J. M. Group-Contribution Estimation of Activity Coefficients in Nonideal Liquid Mixtures. AIChE J. 1975, 21 (6), 1086-1099. DOI: 10.1002/aic.690210607
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Derr, E. L.; Deal, C.H. Analytical Solutions of Groups: Correlation of Activity Coefficients Through Structural Group Parameters. Inst. Chem. Eng. Symp. Ser. 1969, 32 (3), 40.
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Gonzalez, H. E.; Abildskov, J.; Gani, R.; Rousseaux, P.; Le Bert, B. A Method for Prediction of UNIFAC Group Interaction Parameters. AIChE J. 2007, 53 (6), 1620-1632. DOI: 10.1002/aic.11171
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Skjold-Jørgensen, S.; Kolbe, B.; Gmehling, J.; Rasmussen, P. Vapor-Liquid Equilibria by UNIFAC Group Contribution. Revision and Extension. Ind. Eng. Chem. Process Des. Dev. 1979, 18 (4), 714-722. DOI: 10.1021/i260072a024
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Macedo, E. A.; Weidlich, U.; Gmehling, J.; Rasmussen, P. Vapor-Liquid Equilibria by UNIFAC Group Contribution. Revision and Extension. 3. Ind. Eng. Chem. Process Des. Dev. 1983, 22 (4), 676-678. DOI: 10.1021/i200023a023
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Hansen, H. K.; Rasmussen, P.; Fredenslund, A.; Schiller, M.; Gmehling, J. Vapor-Liquid Equilibria by UNIFAC Group Contribution. 5. Revision and Extension. Ind. Eng. Chem. Res. 1991, 30 (10), 2352-2355. DOI: 10.1021/ie00058a017
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Weidlich, V.; Gmehling, J. A Modified UNIFAC Model. 1. Prediction of VLE, hE, and g∞. Ind. Eng. Chem. Res. 1987, 26 (7), 1372-1381. DOI: 10.1021/ie00067a018
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Gmehling, J.; Li, J.; Schiller, M. A Modified UNIFAC Model. 2. Present Parameter Matrix and Results for Different Thermodynamic Properties. Ind. Eng. Chem Res. 1993, 32 (1), 178-193. DOI: 10.1021/ie00013a024
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Gmehling, J.; Lohmann, J.; Jakob, A.; Li, J.; Joh, R. A Modified UNIFAC Model. 3. Revision and Extension. Ind. Eng. Chem Res. 1998, 37 (12), 4876-4882. DOI: 10.1021/ie980347z
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DDBST GmbH. The UNIFAC Consortium. http://www.ddbst.com/unifac-consortium.html (accessed Feb 12, 2024).