This study involves the modification of the Universal Quasi-Chemical model (UNIQUAC) model in order to improve the prediction of the equilibrium data compared to the other conventional activity coefficient models used. The modification takes place by taking the coordination number (z) a fitting parameter and as a second order polynomial function of temperature and employing objective functions on either temperature, vapor composition, activity coefficient, or both temperature and vapor composition difference between the experimental and the predicted VLE data. This modification produces three additional fitting parameters to the original model which is located at the combinatorial term of the model. The values for the coordination number we...
The UNIQUAC model for the excess Gibbs energy is modified using chemical theory to account for chain...
Vapor-Liquid equilibrium (VLE) data involving alcohols and hydrocarbons are relevant to the gas and ...
<p>Arguably, the most important of the basic thermodynamic properties of fluids, vapor pressure has ...
This study involves the modification of the Universal Quasi-Chemical model (UNIQUAC) model in order ...
Vapor–liquid equilibria (VLE), liquid–liquid equilibria (LLE), and vapor–liquid–liquid equilibria (V...
Generalized activity coefficient models are often essential for predicting the extent of liquid noni...
The correlation of experimental liquid–liquid equilibrium (LLE) data for ternary and quaternary syst...
Many important processes in the oil and gas industry (e.g., distillation, absorption, extraction) in...
Running vapor-liquid equilibrium (VLE) data correlation with interaction parameters independent of t...
The activity coefficient models that have been proposed for correlation of Vapor-Liquid Equilibrium ...
The UNIQUAC activity coefficient model and fugacity coefficient model of modified Redlich-Kwong pred...
Phase behavior properties of chemical species and their mixtures are essential to design chemical pr...
This is an extended research of the paper (Islam et al., 2011) conducted to obtain a universal set o...
The analysis has been carried out of the possible theoretical types of ternary systems regarding the...
Vapor-liquid equilibrium (VLE) data for allyl alcohol + water and allyl alcohol + benzene systems ha...
The UNIQUAC model for the excess Gibbs energy is modified using chemical theory to account for chain...
Vapor-Liquid equilibrium (VLE) data involving alcohols and hydrocarbons are relevant to the gas and ...
<p>Arguably, the most important of the basic thermodynamic properties of fluids, vapor pressure has ...
This study involves the modification of the Universal Quasi-Chemical model (UNIQUAC) model in order ...
Vapor–liquid equilibria (VLE), liquid–liquid equilibria (LLE), and vapor–liquid–liquid equilibria (V...
Generalized activity coefficient models are often essential for predicting the extent of liquid noni...
The correlation of experimental liquid–liquid equilibrium (LLE) data for ternary and quaternary syst...
Many important processes in the oil and gas industry (e.g., distillation, absorption, extraction) in...
Running vapor-liquid equilibrium (VLE) data correlation with interaction parameters independent of t...
The activity coefficient models that have been proposed for correlation of Vapor-Liquid Equilibrium ...
The UNIQUAC activity coefficient model and fugacity coefficient model of modified Redlich-Kwong pred...
Phase behavior properties of chemical species and their mixtures are essential to design chemical pr...
This is an extended research of the paper (Islam et al., 2011) conducted to obtain a universal set o...
The analysis has been carried out of the possible theoretical types of ternary systems regarding the...
Vapor-liquid equilibrium (VLE) data for allyl alcohol + water and allyl alcohol + benzene systems ha...
The UNIQUAC model for the excess Gibbs energy is modified using chemical theory to account for chain...
Vapor-Liquid equilibrium (VLE) data involving alcohols and hydrocarbons are relevant to the gas and ...
<p>Arguably, the most important of the basic thermodynamic properties of fluids, vapor pressure has ...