2018
DOI: 10.1016/j.fluid.2018.02.024
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On the calculation of nearest neighbors in activity coefficient models

Abstract: DOI to the publisher's website. • The final author version and the galley proof are versions of the publication after peer review. • The final published version features the final layout of the paper including the volume, issue and page numbers. Link to publication General rights Copyright and moral rights for the publications made accessible in the public portal are retained by the authors and/or other copyright owners and it is a condition of accessing publications that users recognise and abide by the legal… Show more

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Cited by 7 publications
(2 citation statements)
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“…where f k and q k are the volume and surface fraction of compound 1 in the mixture, respectively. This expression in combination with the residual part of the UNIQUAC model or COSMOSPACE model gives better results for binary equilibria of alkane-alkane and alkane alcohol systems [46] than the combination with original Staverman-Guggenheim combinatorial activity coefficient model. Substitution of Eqs.…”
Section: The Total Activity Coefficientmentioning
confidence: 99%
“…where f k and q k are the volume and surface fraction of compound 1 in the mixture, respectively. This expression in combination with the residual part of the UNIQUAC model or COSMOSPACE model gives better results for binary equilibria of alkane-alkane and alkane alcohol systems [46] than the combination with original Staverman-Guggenheim combinatorial activity coefficient model. Substitution of Eqs.…”
Section: The Total Activity Coefficientmentioning
confidence: 99%
“…the Dortmund Data Bank [70]. Based on this wealth of experimental information, wellhoned semi-empirical models, such as UNIFAC [130][131][132][133][134][135][136], DISQUAC [137][138][139][140], and the recent MOQUAC model [141] have been developed for correlating, extrapolating and predicting, in particular, molar excess Gibbs energies G E and molar excess enthalpies H E , over reasonably large temperature ranges. However, estimated infinite-dilution properties, aqueous solubilities of hydrocarbons, and excess heat capacities C E P of liquid mixtures are frequently not satisfactory [142].…”
Section: Property Changes On Mixing and Excess Propertiesmentioning
confidence: 99%