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A modified UNIFAC model for the calculation of thermodynamic properties of aqueous and non-aqueous solutions containing sugars

dc.contributor.authorPeres, António M.
dc.contributor.authorMacedo, Eugénia A.
dc.date.accessioned2011-02-01T11:04:38Z
dc.date.available2011-02-01T11:04:38Z
dc.date.issued1997
dc.description.abstractA UNIFAC based model is proposed to describe experimental thermodynamic properties of aqueous and non-aqueous solutions containing common sugars, e.g., D-glucose, D-fructose and sucrose. A new group 'OHring' is introduced due to proximity effects. New temperature-independent UNIFAC interaction parameters are estimated based on the binary data available for both D-glucose and D-fructose and only on the solubility data for sucrose. The UNIFAC model used in this work is able to accurately predict the water activity, boiling temperature and freezing point of aqueous sucrose solutions. However, the predictions of the osmotic coefficients for the sucrose/water system present relative deviations up to 9%. Satisfactory predictions of vapor-liquid and solid-liquid equilibrium data for ternary and quaternary mixtures of D-glucose, D-fructose, sucrose and water components are also obtained. This approach uses the symmetric convention for all the components, i.e. the pure fused sugar at solution pressure and temperature is its reference state. Therefore, it allows to carry out in a straightforward way, calculations of solid-liquid equilibria of sugars in mixed solvents. It is shown that the new UNIFAC model is able to qualitatively predict the ternary solubility data of D-glucose D-xylose, D-mannose and sucrose in mixed solvent mixtures of ethanol/water, methanol/water and ethanol/methanol. A comparison with a modified UNIQUAC- essentially correlative model--and a UNIFAC -correlative and predictive model- approaches available in the literature is also given: the performance of the model proposed in this work is in general inferior to that of the UNIQUAC model, however it gives always a better agreement with the experimental data when compared with another UNIFAC based model available in the literature.por
dc.description.sponsorshipJunta Nacional de Investigação Científica e Tecnológica -PRAXIS XXI (Lisboa, Portugal)por
dc.identifier.citationPeres, António M.; Macedo, Eugénia A. (1997). A modified UNIFAC model for the calculation of thermodynamic properties of aqueous and non-aqueous solutions containing sugars. Fluid Phase Equilibria. ISSN 0378-3812. 139:1-2, p. 47-74por
dc.identifier.doi10.1016/S0378-3812(97)00196-9
dc.identifier.issn0378-3812
dc.identifier.urihttp://hdl.handle.net/10198/3223
dc.language.isoengpor
dc.peerreviewedyespor
dc.publisherElsevierpor
dc.subjectUNIFACpor
dc.subjectSolid-liquid equilibriapor
dc.subjectVapor-liquid equilibriapor
dc.subjectWater-Ethanol-Methanolpor
dc.subjectCarbohydratespor
dc.titleA modified UNIFAC model for the calculation of thermodynamic properties of aqueous and non-aqueous solutions containing sugarspor
dc.typejournal article
dspace.entity.typePublication
oaire.citation.endPage74por
oaire.citation.issue139por
oaire.citation.startPage47por
oaire.citation.titleFluid Phase Equilibriapor
person.familyNamePeres
person.givenNameAntónio M.
person.identifier107333
person.identifier.ciencia-idCF16-5443-F420
person.identifier.orcid0000-0001-6595-9165
person.identifier.ridI-8470-2012
person.identifier.scopus-author-id7102331969
rcaap.rightsrestrictedAccesspor
rcaap.typearticlepor
relation.isAuthorOfPublication7d93be47-8dc4-4413-9304-5b978773d3bb
relation.isAuthorOfPublication.latestForDiscovery7d93be47-8dc4-4413-9304-5b978773d3bb

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