Based on a quasilattice model of a multicomponent soln., 3 equations are derived relating component activity coeffs. to the compn. of a liq. mixt. The equations also apply to systems showing limited miscibility. Temp. dependence of activity coeffs. is built in. The equations were tested for 16 binary systems, 5 of which show limited miscibility, and for 4 ternary systems. The enthalpic Wilson equation, one of the 3, gives the best prediction of binary vapor-liq. equil. Both the enthalpic Wilson equation and the Orye equations give good results of comparable accuracy for the ternary systems. [on SciFinder (R)
The paper describes methods for calculating chemical equilibria based on a constrained Gibbs free en...
The applicability of a formalism involving an exponential function of composition x1 in interpreting...
This paper presents the results of a liquid–liquid equilibrium data correlation for 11 ternary syste...
Based on a quasilattice model of a multicomponent soln., 3 equations are derived relating component ...
Mansoori, G.A., 1980. Classical thermodynamic basis of activity coefficients: Predictive and consist...
A general equation for the estimation of thermodynamic excess properties of multicomponent systems f...
Isothermal vapor-liquid equilibrium relationships were determined at 950°C in a Colburn still for th...
[[abstract]]©1994 Elsevier - A new mixing model for cubic equations of states that is theoretically ...
The concept of a regular liquid or solid solution was first introduced by Hildebrand (1) and subsequ...
Based on the well-known concepts of statistics of nearest neighbors in a lattice and on the BethePei...
Experimental vapor-liquid equilibria data were taken on the system, water-monoethanolamine-diethylen...
A rather general expression for the excess Gibbs free energy of a nonionic liquid mixture has been d...
A cubic formalism is proposed for representation of thermodynamic properties of ternary and higher o...
An equation previously developed for estimation of the excess thermodynamic properties of multicompo...
The vapor–liquid equilibria of binary associating fluids containing alcohols are described using a c...
The paper describes methods for calculating chemical equilibria based on a constrained Gibbs free en...
The applicability of a formalism involving an exponential function of composition x1 in interpreting...
This paper presents the results of a liquid–liquid equilibrium data correlation for 11 ternary syste...
Based on a quasilattice model of a multicomponent soln., 3 equations are derived relating component ...
Mansoori, G.A., 1980. Classical thermodynamic basis of activity coefficients: Predictive and consist...
A general equation for the estimation of thermodynamic excess properties of multicomponent systems f...
Isothermal vapor-liquid equilibrium relationships were determined at 950°C in a Colburn still for th...
[[abstract]]©1994 Elsevier - A new mixing model for cubic equations of states that is theoretically ...
The concept of a regular liquid or solid solution was first introduced by Hildebrand (1) and subsequ...
Based on the well-known concepts of statistics of nearest neighbors in a lattice and on the BethePei...
Experimental vapor-liquid equilibria data were taken on the system, water-monoethanolamine-diethylen...
A rather general expression for the excess Gibbs free energy of a nonionic liquid mixture has been d...
A cubic formalism is proposed for representation of thermodynamic properties of ternary and higher o...
An equation previously developed for estimation of the excess thermodynamic properties of multicompo...
The vapor–liquid equilibria of binary associating fluids containing alcohols are described using a c...
The paper describes methods for calculating chemical equilibria based on a constrained Gibbs free en...
The applicability of a formalism involving an exponential function of composition x1 in interpreting...
This paper presents the results of a liquid–liquid equilibrium data correlation for 11 ternary syste...