Experimental vapor-liquid equilibria data were taken on the system, water-monoethanolamine-diethylene glycol. Proposed correlations involving relationships between isothermal activity coefficients and liquid composition were applied to the data on this and one other ternary system. The results indicate that a substantial amount of further investigation on other systems is necessary to establish any major conclusions
Liquid–liquid equilibrium data were determined for the two ternary systems of water + thioglycolic a...
Ethylene glycol is an organic solvent used in extractive distillation to separate water–ethanol mixt...
Isobaric vapor-liquid equilibrium (VLE) data have been measured for the binary systems ethyl ethanoa...
Isothermal vapor-liquid equilibrium relationships were determined at 950°C in a Colburn still for th...
In this work the influence of temperature and composition on the activity coefficient in solution ha...
Running vapor-liquid equilibrium (VLE) data correlation with interaction parameters independent of t...
The freezing points of the system methanol-glycol-water were investigated by Conrad, Hill and Ballma...
This study involves the modification of the Universal Quasi-Chemical model (UNIQUAC) model in order ...
Isothermal vapour-liquid equilibrium measurements have been measured by a forced-recirculation type ...
In this work, the isothermal liquid-liquid equilibrium (LLE) and isobaric vapor-liquid equilibrium (...
Two expressions for the excess Gibbs free energy are presented which correlate and predict vapor-liq...
We present new experimental data on the isobaric vapor–liquid equilibria (VLE) of four binary mixtur...
Vapour-liquid equilibrium data for the system ethanol-water were determined at one atmosphere pressu...
A modified recirculation Dvorak and Boublik still was used in the equilibrium determination. The vap...
With the increasing need for large quantities of pure hydrocarbons in recent years, methods of predi...
Liquid–liquid equilibrium data were determined for the two ternary systems of water + thioglycolic a...
Ethylene glycol is an organic solvent used in extractive distillation to separate water–ethanol mixt...
Isobaric vapor-liquid equilibrium (VLE) data have been measured for the binary systems ethyl ethanoa...
Isothermal vapor-liquid equilibrium relationships were determined at 950°C in a Colburn still for th...
In this work the influence of temperature and composition on the activity coefficient in solution ha...
Running vapor-liquid equilibrium (VLE) data correlation with interaction parameters independent of t...
The freezing points of the system methanol-glycol-water were investigated by Conrad, Hill and Ballma...
This study involves the modification of the Universal Quasi-Chemical model (UNIQUAC) model in order ...
Isothermal vapour-liquid equilibrium measurements have been measured by a forced-recirculation type ...
In this work, the isothermal liquid-liquid equilibrium (LLE) and isobaric vapor-liquid equilibrium (...
Two expressions for the excess Gibbs free energy are presented which correlate and predict vapor-liq...
We present new experimental data on the isobaric vapor–liquid equilibria (VLE) of four binary mixtur...
Vapour-liquid equilibrium data for the system ethanol-water were determined at one atmosphere pressu...
A modified recirculation Dvorak and Boublik still was used in the equilibrium determination. The vap...
With the increasing need for large quantities of pure hydrocarbons in recent years, methods of predi...
Liquid–liquid equilibrium data were determined for the two ternary systems of water + thioglycolic a...
Ethylene glycol is an organic solvent used in extractive distillation to separate water–ethanol mixt...
Isobaric vapor-liquid equilibrium (VLE) data have been measured for the binary systems ethyl ethanoa...