References

[1]

Published Parameters UNIFAC - DDBST GmbH — ddbst.com. http://www.ddbst.com/published-parameters-unifac.html. [Accessed 23-04-2024].

[2]

Juergen Gmehling, Peter Rasmussen, and Aage Fredenslund. Vapor-liquid equilibriums by UNIFAC group contribution. Revision and extension. 2. Industrial & Engineering Chemistry Process Design and Development, 21(1):118–127, January 1982. doi:10.1021/i200016a021.

[3]

Henrik K. Hansen, Peter Rasmussen, Aage Fredenslund, Martin Schiller, and Juergen Gmehling. Vapor-liquid equilibria by UNIFAC group contribution. 5. Revision and extension. Industrial & Engineering Chemistry Research, 30(10):2352–2355, October 1991. doi:10.1021/ie00058a017.

[4]

Eugenia Almeida Macedo, Ulrich Weidlich, Juergen Gmehling, and Peter Rasmussen. Vapor-liquid equilibriums by UNIFAC group contribution. Revision and extension. 3. Industrial & Engineering Chemistry Process Design and Development, 22(4):676–678, October 1983. doi:10.1021/i200023a023.

[5]

Steen Skjold-Jorgensen, Barbel Kolbe, Jurgen Gmehling, and Peter Rasmussen. Vapor-Liquid Equilibria by UNIFAC Group Contribution. Revision and Extension. Industrial & Engineering Chemistry Process Design and Development, 18(4):714–722, October 1979. doi:10.1021/i260072a024.

[6]

Detlef Tiegs, Peter Rasmussen, Juergen Gmehling, and Aage Fredenslund. Vapor-liquid equilibria by UNIFAC group contribution. 4. Revision and extension. Industrial & Engineering Chemistry Research, 26(1):159–161, January 1987. doi:10.1021/ie00061a030.

[7]

Roland Wittig, Jürgen Lohmann, and Jürgen Gmehling. Vapor-Liquid Equilibria by UNIFAC Group Contribution. 6. Revision and Extension. Industrial & Engineering Chemistry Research, 42(1):183–188, January 2003. doi:10.1021/ie020506l.

[8]

T. Holderbaum and J. Gmehling. PSRK: A Group Contribution Equation of State Based on UNIFAC. Fluid Phase Equilibria, 70(2-3):251–265, December 1991. doi:10.1016/0378-3812(91)85038-V.

[9]

Sven Horstmann, Anna Jabłoniec, Jörg Krafczyk, Kai Fischer, and Jürgen Gmehling. PSRK group contribution equation of state: comprehensive revision and extension IV, including critical constants and α-function parameters for 1000 components. Fluid Phase Equilibria, 227(2):157–164, January 2005. doi:10.1016/j.fluid.2004.11.002.

[10]

Kevin G Joback. Designing Molecules Possessing Desired Physical Property Values. Thesis (Ph. D.), Massachusetts Institute of Technology, Cambridge, Massachusetts, 1989.

[11]

K.G. Joback and R.C. Reid. ESTIMATION OF PURE-COMPONENT PROPERTIES FROM GROUP-CONTRIBUTIONS. Chemical Engineering Communications, 57(1-6):233–243, July 1987. doi:10.1080/00986448708960487.