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Cited article:

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Computer calculation of the optimal parameters of a model for the simultaneous representation of experimental binary and ternary vapor-liquid and liquid-liquid equilibrium data

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Excess thermodynamics functions of 1-propanol + methyl propanoate and 1-propanol + methyl butanoate systems

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A new ebulliometric technique. Vapour-liquid equilibria in the binary systems ethanol-n-heptane and ethanol-n-nonane

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

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Vapour—liquid equilibrium of the systems 1-propanol—2,2,4-trimethylpentane and 2-propanol-n-hexane

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

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

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New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixtures

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Zur Korrelation von Grenzaktivitätskoeffizienten und Aktivitätskoeffizienten in endlichen Konzentrationsbereichen unter Anwendung moderner Inkrementen‐ und mathematischer Verfahren

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

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The Canadian Journal of Chemical Engineering 55 (5) 609 (1977)
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