Isothermal vapor-liquid equilibrium relationships were determined at 950°C in a Colburn still for the ternary mixture water-n-propanol monoethanolamine and its three binary mixtures. The van Laar equation was found to describe the alcohol-water binary slightly better than the three-suffix Margules equation. The reverse was found to be true for the amine - water system. Because of a "concentration" effect, none of the equations employed in this investigation were very successful in predicting the amine-alcohol system. The Margules equation was found to have greater possibilities than either the van Lear or the symmetrical equations in predicting the ternary activity coefficients for this system. It was shown from this and a parallel investig...
[[abstract]]©1994 Elsevier - A new mixing model for cubic equations of states that is theoretically ...
The vapor–liquid equilibria of binary associating fluids containing alcohols are described using a c...
The temperature and the composition of the vapor–liquid–liquid equilibrium (VLLE) and the vapor–liqu...
Experimental vapor-liquid equilibria data were taken on the system, water-monoethanolamine-diethylen...
The vapor-liquid equilibrium of binary systems of triethylamine with methylalcohol, ethylalcohol, n-...
In this work, the isothermal liquid-liquid equilibrium (LLE) and isobaric vapor-liquid equilibrium (...
There binary pairs of aceton-butanol, aseton-ethanol, n-butanol-ethanol and ternary pairs ofaceton-b...
(Liquid + liquid) equilibrium (LLE) data of the solubility (binodal) curves and tie-line end composi...
With the increasing need for large quantities of pure hydrocarbons in recent years, methods of predi...
Mansoori, G.A., 1980. Classical thermodynamic basis of activity coefficients: Predictive and consist...
Isobaric vapor-liquid equilibrium measurements are reported for the binary mixtures of n-Butylamine ...
Two expressions for the excess Gibbs free energy are presented which correlate and predict vapor-liq...
Based on a quasilattice model of a multicomponent soln., 3 equations are derived relating component ...
This work presents vapor pressure data for water, 1-propanol, and 2-propanol as well as their binary...
Isothermal vapour-liquid equilibrium measurements have been measured by a forced-recirculation type ...
[[abstract]]©1994 Elsevier - A new mixing model for cubic equations of states that is theoretically ...
The vapor–liquid equilibria of binary associating fluids containing alcohols are described using a c...
The temperature and the composition of the vapor–liquid–liquid equilibrium (VLLE) and the vapor–liqu...
Experimental vapor-liquid equilibria data were taken on the system, water-monoethanolamine-diethylen...
The vapor-liquid equilibrium of binary systems of triethylamine with methylalcohol, ethylalcohol, n-...
In this work, the isothermal liquid-liquid equilibrium (LLE) and isobaric vapor-liquid equilibrium (...
There binary pairs of aceton-butanol, aseton-ethanol, n-butanol-ethanol and ternary pairs ofaceton-b...
(Liquid + liquid) equilibrium (LLE) data of the solubility (binodal) curves and tie-line end composi...
With the increasing need for large quantities of pure hydrocarbons in recent years, methods of predi...
Mansoori, G.A., 1980. Classical thermodynamic basis of activity coefficients: Predictive and consist...
Isobaric vapor-liquid equilibrium measurements are reported for the binary mixtures of n-Butylamine ...
Two expressions for the excess Gibbs free energy are presented which correlate and predict vapor-liq...
Based on a quasilattice model of a multicomponent soln., 3 equations are derived relating component ...
This work presents vapor pressure data for water, 1-propanol, and 2-propanol as well as their binary...
Isothermal vapour-liquid equilibrium measurements have been measured by a forced-recirculation type ...
[[abstract]]©1994 Elsevier - A new mixing model for cubic equations of states that is theoretically ...
The vapor–liquid equilibria of binary associating fluids containing alcohols are described using a c...
The temperature and the composition of the vapor–liquid–liquid equilibrium (VLLE) and the vapor–liqu...