The phase equilibrium data for methanol + ethanol + isooctane systems were obtained at 303.15 K. Data for methanol + ethylbenzene + isooctane system were taken from literature. The effect of ethanol addition on the system equilibrium was investigated at the same temperature. The distribution curves for ternary and quaternary system was analyzed. The experimental results for ternary systems were correlated with UNIQUAC and NRTL equations. For the ternary systems studied here, the NRTL equation is more accurate than the UNIQUAC. The equilibrium data for the three ternary systems were used to determine interactions parameters for the UNIQUAC equation. For the quaternary system, the experimental data can be fitted more accurately to UNIQUAC equ...
The process of recovery by liquid–liquid extraction of ethanol manufactured in a fermentation proces...
High pressure–temperature isopleths were obtained, experimentally, for the binary system of methanol...
Liquid–liquid equilibrium data for the ternary system 1-pentanol–ethanol–water have been determined ...
The influence of temperature on the miscibility of the {methanol + p-xylene + isooctane} and {methan...
ABSTRACT: INTRODUCTION The precise liquid-liquid equilibria (LLE) data is necessary to rational desi...
International audienceOriginal very low solubility data for binary (methanol + dodecane) and ternary...
Abstract Liquid-liquid equilibrium of methanol + toluene+ hexane ternary system at 278.15,283.15, 28...
The knowledge and the ability to describe the phase equilibrium behavior of systems composed of tran...
(Liquid + liquid) equilibrium (LLE) data for the ternary system (water + butyric acid + isoamyl alco...
Isobaric vapor-liquid equilibria data at 101.3 kPa were reported for the binary mixtures (methyl ace...
Vapor-liquid equilibria (VLE) in alkanes and alcohols was measured and a contribution Patel-Teja (GP...
In this work authors present the experimental liquid–liquid equilibria (LLE) data of water + ethanol...
The liquid–liquid equilibrium of the water + 1-butanol + isoamyl alcohol system at 303.15 and 313.15...
Transesterification reactions are common in the production of some important chemicals, such as biod...
Liquid–liquid (L–L), solid–liquid (S–L), and solid–liquid–liquid (S–L–L) equilibrium data for the wa...
The process of recovery by liquid–liquid extraction of ethanol manufactured in a fermentation proces...
High pressure–temperature isopleths were obtained, experimentally, for the binary system of methanol...
Liquid–liquid equilibrium data for the ternary system 1-pentanol–ethanol–water have been determined ...
The influence of temperature on the miscibility of the {methanol + p-xylene + isooctane} and {methan...
ABSTRACT: INTRODUCTION The precise liquid-liquid equilibria (LLE) data is necessary to rational desi...
International audienceOriginal very low solubility data for binary (methanol + dodecane) and ternary...
Abstract Liquid-liquid equilibrium of methanol + toluene+ hexane ternary system at 278.15,283.15, 28...
The knowledge and the ability to describe the phase equilibrium behavior of systems composed of tran...
(Liquid + liquid) equilibrium (LLE) data for the ternary system (water + butyric acid + isoamyl alco...
Isobaric vapor-liquid equilibria data at 101.3 kPa were reported for the binary mixtures (methyl ace...
Vapor-liquid equilibria (VLE) in alkanes and alcohols was measured and a contribution Patel-Teja (GP...
In this work authors present the experimental liquid–liquid equilibria (LLE) data of water + ethanol...
The liquid–liquid equilibrium of the water + 1-butanol + isoamyl alcohol system at 303.15 and 313.15...
Transesterification reactions are common in the production of some important chemicals, such as biod...
Liquid–liquid (L–L), solid–liquid (S–L), and solid–liquid–liquid (S–L–L) equilibrium data for the wa...
The process of recovery by liquid–liquid extraction of ethanol manufactured in a fermentation proces...
High pressure–temperature isopleths were obtained, experimentally, for the binary system of methanol...
Liquid–liquid equilibrium data for the ternary system 1-pentanol–ethanol–water have been determined ...