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dc.contributor.author
Mota, Fátima L.
dc.contributor.author
Queimada, António J.
dc.contributor.author
Andreatta, Alfonsina Ester
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Pinho, Simão P.
dc.contributor.author
Macedo, Eugénia A.
dc.date.available
2018-08-06T22:15:37Z
dc.date.issued
2012-05-25
dc.identifier.citation
Mota, Fátima L.; Queimada, António J.; Andreatta, Alfonsina Ester; Pinho, Simão P.; Macedo, Eugénia A.; Calculation of drug-like molecules solubility using predictive activity coefficient models; Elsevier Science; Fluid Phase Equilibria; 322-323; 25-5-2012; 48-55
dc.identifier.issn
0378-3812
dc.identifier.uri
http://hdl.handle.net/11336/54365
dc.description.abstract
The A-UNIFAC, UNIFAC, and NRTL-SAC models are used to predict solubility in pure solvents of a set of drug-like molecules. To apply A-UNIFAC, a new set of residual interaction parameters between the . ACOH group and six other groups had to be estimated. The solute model parameters of NRTL-SAC were also estimated for this set of molecules. NRTL-SAC showed better performance at 298.15. K, with an average absolute deviation of 37.6%. Solubility dependence with temperature was also studied: all models presented average deviations around 40%. In general, there is an improvement given by the A-UNIFAC over the UNIFAC in aqueous systems, proving the importance of taking association into account.The reference solvent approach was also applied improving the results. Solubility in pure solvents can now be predicted with an average deviation around 35.2%. This approach reduces differences previously found between the three models, being a powerful methodology.
dc.format
application/pdf
dc.language.iso
eng
dc.publisher
Elsevier Science
dc.rights
info:eu-repo/semantics/openAccess
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.subject
A-Unifac
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Complex Chemicals
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Modelling
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Nrtl-Sac
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Solubility
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Unifac
dc.subject.classification
Otras Ingeniería Química
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Ingeniería Química
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INGENIERÍAS Y TECNOLOGÍAS
dc.title
Calculation of drug-like molecules solubility using predictive activity coefficient models
dc.type
info:eu-repo/semantics/article
dc.type
info:ar-repo/semantics/artículo
dc.type
info:eu-repo/semantics/publishedVersion
dc.date.updated
2018-07-11T13:45:18Z
dc.journal.volume
322-323
dc.journal.pagination
48-55
dc.journal.pais
Países Bajos
dc.journal.ciudad
Amsterdam
dc.description.fil
Fil: Mota, Fátima L.. Universidad de Porto. Laboratory of Separation and Engineering; Portugal
dc.description.fil
Fil: Queimada, António J.. Universidad de Porto. Laboratory of Separation and Engineering; Portugal
dc.description.fil
Fil: Andreatta, Alfonsina Ester. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
dc.description.fil
Fil: Pinho, Simão P.. Instituto Politécnico de Bragança; Portugal
dc.description.fil
Fil: Macedo, Eugénia A.. Universidad de Porto. Laboratory of Separation and Engineering; Portugal
dc.journal.title
Fluid Phase Equilibria
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/pii/S0378381212000611
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1016/j.fluid.2012.02.003
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