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dc.contributor.author
Yalin, I.
dc.contributor.author
Çehreli, Süheyla
dc.contributor.author
Andreatta, Alfonsina Ester
dc.contributor.author
Senol, A.
dc.date.available
2021-05-06T03:29:13Z
dc.date.issued
2020-08
dc.identifier.citation
Yalin, I.; Çehreli, Süheyla; Andreatta, Alfonsina Ester; Senol, A.; Phase Equilibria of Ternary Liquid–Liquid Systems (Water + C1–C4 Monocarboxylic Acids + Dibutyl Ether) at Three Different Temperatures: Modeling with A-UNIFAC; Springer/Plenum Publishers; Journal Of Solution Chemistry; 49; 7-8; 8-2020; 1009-1028
dc.identifier.issn
0095-9782
dc.identifier.uri
http://hdl.handle.net/11336/131460
dc.description.abstract
Liquid–liquid equilibrium (LLE) data for the ternary systems composed of water, C1–C4 monocarboxylic acids, and dibutyl ether were determined at three different temperatures (293.15, 303.15, and 313.15 K) and atmospheric pressure. The experimental solubility curves and mutual solubilities of (water + dibutyl ether) were determined by the cloud-point method, whereas the tie-lines of conjugate phases were obtained via GC analysis. The examined C1–C4 monocarboxylic acids are valuable components for estimating the effect of acid structure on LLE. The separation factor calculated from experimental LLE data is indicative of the ability of the solvent to effectively recover the acid. Equilibrium distribution of C1–C4 acids is better for more structured propionic and butyric acids as compared to less structured formic and acetic acids, and the general ranking with respect to the separation factor (S) follows the order: C4 > C3 > C2 > C1, and T293.15 < T303.15 ≤ T313.15. The LLE data were predicted with the group-contribution method A-UNIFAC with the newly estimated parameters, which shows an appropriate consistency with the experimental data.
dc.format
application/pdf
dc.language.iso
eng
dc.publisher
Springer/Plenum Publishers
dc.rights
info:eu-repo/semantics/restrictedAccess
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.subject
A-UNIFAC
dc.subject
LIQUID–LIQUID EQUILIBRIA
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MONOCARBOXYLIC ACID
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SEPARATION FACTOR
dc.subject.classification
Ingeniería de Procesos Químicos
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Ingeniería Química
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INGENIERÍAS Y TECNOLOGÍAS
dc.title
Phase Equilibria of Ternary Liquid–Liquid Systems (Water + C1–C4 Monocarboxylic Acids + Dibutyl Ether) at Three Different Temperatures: Modeling with A-UNIFAC
dc.type
info:eu-repo/semantics/article
dc.type
info:ar-repo/semantics/artículo
dc.type
info:eu-repo/semantics/publishedVersion
dc.date.updated
2021-04-28T22:00:24Z
dc.journal.volume
49
dc.journal.number
7-8
dc.journal.pagination
1009-1028
dc.journal.pais
Estados Unidos
dc.description.fil
Fil: Yalin, I.. Istanbul University cerrahpasa; Turquía
dc.description.fil
Fil: Çehreli, Süheyla. Istanbul University cerrahpasa; Turquía
dc.description.fil
Fil: Andreatta, Alfonsina Ester. Universidad Tecnológica Nacional. Facultad Regional San Francisco; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Córdoba; Argentina
dc.description.fil
Fil: Senol, A.. Istanbul University cerrahpasa; Turquía
dc.journal.title
Journal Of Solution Chemistry
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/https://link.springer.com/article/10.1007%2Fs10953-020-01006-x
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1007/s10953-020-01006-x
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