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Cited article:

Optimizing Thermodynamic Models: The Relevance of Molar Fraction Uncertainties

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Journal of Chemical & Engineering Data 62 (2) 825 (2017)
https://doi.org/10.1021/acs.jced.6b00853

Modeling the Thermodynamics of Fluids Treated by CO2 Capture Processes with Peng–Robinson + Residual Helmholtz Energy-Based Mixing Rules

Silvia Lasala, Paolo Chiesa, Romain Privat and Jean-Noël Jaubert
Industrial & Engineering Chemistry Research 56 (8) 2259 (2017)
https://doi.org/10.1021/acs.iecr.6b04190

Use of heat capacities for the estimation of cubic equation-of-state parameters—application to the prediction of very low vapor pressures of heavy hydrocarbons

Lucie Coniglio, Evelyne Rauzy, André Péneloux and Evelyne Neau
Fluid Phase Equilibria 200 (2) 375 (2002)
https://doi.org/10.1016/S0378-3812(02)00046-8

Reduction of thermodynamic data by means of the multiresponse maximum likelihood principle

S. Kemeny, J. Manczinger, S. Skjold‐Jørgensen and K. Toth
AIChE Journal 28 (1) 20 (1982)
https://doi.org/10.1002/aic.690280105

A new method of parameter adjustment and diagnostic checks on gamma models used in vapor—liquid equilibrium calculations

J. Choliński, M. Palczewska-Tulińska, A. Szafrańska and D. Wyrzykowskastankiewicz
Chemical Engineering Science 36 (1) 173 (1981)
https://doi.org/10.1016/0009-2509(81)80061-9

Multicomponent redox systems: Analytical representation A(Uh), method of analysis and theoretical resolution limits

Michel Denis, Evelyne Neau and Jean Pierre Blein
Journal of Electroanalytical Chemistry and Interfacial Electrochemistry 116 757 (1980)
https://doi.org/10.1016/S0022-0728(80)80304-4

The analysis and design of binary vapour‐liquid equilibrium experiments. Part II: The design of experiments

Thomas L. Sutton and John F. Macgregor
The Canadian Journal of Chemical Engineering 55 (5) 609 (1977)
https://doi.org/10.1002/cjce.5450550520