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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  
dc.subject
MONOCARBOXYLIC ACID  
dc.subject
SEPARATION FACTOR  
dc.subject.classification
Ingeniería de Procesos Químicos  
dc.subject.classification
Ingeniería Química  
dc.subject.classification
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