In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system monochloracetic acid (MCA) + dichloroacetic acid (DCA) + diethylene glycol dipentyl ether (DGDP). The extractant DGDP enhances the relative volatility of the MCA/DCA system from 1.2 without extractant up to 4. The non-ideal behavior in the liquid and vapor phase was reasonably well correlated with the NRTL and Hayden–O’Connell (HOC) model, respectively. The binary and ternary VLE data were correlated separately to obtain a better description of both dataset
Isobaric vapour - liquid equilibria have been determined at 101.325 kPa for three binary mixtures: b...
Isobaric vapor–liquid equilibrium data for pure components cyclopentyl methyl ether (CPME) and cyclo...
Methyldiethanolamine (MDEA) is a widely used chemical in the natural gas processing industry as a so...
In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system...
In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system...
Isobaric vapor–liquid equilibrium (VLE) data for the binary system monochloroacetic acid + dichloroa...
The isobaric vapor–liquid equilibrium (VLE) data for the systems (thioglycolic acid + water), (thiog...
Isobaric vapor liquid equilibrium (VLE) data for the binary mixture of glycerol ethyl acetal (GEA) a...
Vapor liquid equilibria (VLE) of the binary systems n-butanal + butyric acid and n-butanol + acetic ...
Vapor-liquid equilibrium (VLE) data for the binary systems tetrahydrofuran (THF) + acetic acid (AA) ...
In this work, the isothermal liquid-liquid equilibrium (LLE) and isobaric vapor-liquid equilibrium (...
The number of newly synthesized and produced organic chemicals has increased extremely quickly. Howe...
The isobaric vapour-liquid equilibrium (VLE) for mixtures of cyclohexanol-phenylmethanol were invest...
International audienceFurther to the Part I of the present paper, the second Part is concentrated ar...
© 2018 American Chemical Society. Methyldiethanolamine (MDEA) is a widely used chemical in the natur...
Isobaric vapour - liquid equilibria have been determined at 101.325 kPa for three binary mixtures: b...
Isobaric vapor–liquid equilibrium data for pure components cyclopentyl methyl ether (CPME) and cyclo...
Methyldiethanolamine (MDEA) is a widely used chemical in the natural gas processing industry as a so...
In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system...
In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system...
Isobaric vapor–liquid equilibrium (VLE) data for the binary system monochloroacetic acid + dichloroa...
The isobaric vapor–liquid equilibrium (VLE) data for the systems (thioglycolic acid + water), (thiog...
Isobaric vapor liquid equilibrium (VLE) data for the binary mixture of glycerol ethyl acetal (GEA) a...
Vapor liquid equilibria (VLE) of the binary systems n-butanal + butyric acid and n-butanol + acetic ...
Vapor-liquid equilibrium (VLE) data for the binary systems tetrahydrofuran (THF) + acetic acid (AA) ...
In this work, the isothermal liquid-liquid equilibrium (LLE) and isobaric vapor-liquid equilibrium (...
The number of newly synthesized and produced organic chemicals has increased extremely quickly. Howe...
The isobaric vapour-liquid equilibrium (VLE) for mixtures of cyclohexanol-phenylmethanol were invest...
International audienceFurther to the Part I of the present paper, the second Part is concentrated ar...
© 2018 American Chemical Society. Methyldiethanolamine (MDEA) is a widely used chemical in the natur...
Isobaric vapour - liquid equilibria have been determined at 101.325 kPa for three binary mixtures: b...
Isobaric vapor–liquid equilibrium data for pure components cyclopentyl methyl ether (CPME) and cyclo...
Methyldiethanolamine (MDEA) is a widely used chemical in the natural gas processing industry as a so...