Investigation of Water/Ethanol Mixture Separation by 2-Butanone and Diethyl Ether at 291.15 K: Experimental Results and Theoretical Correlation

This study describes the separation of ethanol from an aqueous solution using liquid-liquid extraction.Two ternary systems, water-ethanol-2-butanone and water-ethanol-diethyl ether, were investigated at 291.15 K and atmospheric pressure using the cloud point method.Both ternary systems had a type 1 liquid-liquid equilibrium diagram.The experimental tie-line data were correlated using the non-random two-liquid (NRTL) thermo dynamic model and the Hand correlation.The separation factors and distribution coefficients were calculated to evaluate the separation performance.The selectivity diagram was also used to determine the most suitable solvent for ethanol separation.Among the two solvents studied, diethyl ether exhibited the best capability for extracting ethanol from aqueous solution in this study.

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Publication Details

Journal
Chemical and Biochemical Engineering Quarterly
Published
2026-11-05
DOI
https://doi.org/10.15255/cabeq.2026.2528
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
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article

Investigation of Water/Ethanol Mixture Separation by 2-Butanone and Diethyl Ether at 291.15 K: Experimental Results and Theoretical Correlation

Nadjet Boulkroune, Soumaya Larous, Nadjah Roubhi, Mohamed El Amdjed Seghir
Chemical and Biochemical Engineering Quarterly
Phase Equilibria and Thermodynamics
article

Investigation of Water/Ethanol Mixture Separation by 2-Butanone and Diethyl Ether at 291.15 K: Experimental Results and Theoretical Correlation

Nadjet Boulkroune, Soumaya Larous, Nadjah Roubhi, Mohamed El Amdjed Seghir
article en

Abstract

This study describes the separation of ethanol from an aqueous solution using liquid-liquid extraction.Two ternary systems, water-ethanol-2-butanone and water-ethanol-diethyl ether, were investigated at 291.15 K and atmospheric pressure using the cloud point method.Both ternary systems had a type 1 liquid-liquid equilibrium diagram.The experimental tie-line data were correlated using the non-random two-liquid (NRTL) thermo dynamic model and the Hand correlation.The separation factors and distribution coefficients were calculated to evaluate the separation performance.The selectivity diagram was also used to determine the most suitable solvent for ethanol separation.Among the two solvents studied, diethyl ether exhibited the best capability for extracting ethanol from aqueous solution in this study.

Chemical and Biochemical Engineering Quarterly(3)
University of Constantine 3 (DZ)
Openalex Percentile: Top 27%
Phase Equilibria and Thermodynamics
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