Generalized activity coefficient models are often essential for predicting the extent of liquid nonideality in a mixture in the absence of experimental data. This work is focused on generalizing the interaction parameters of three widely used activity coefficient models, nonrandom two-liquid (NRTL), universal quasi-chemical (UNIQUAC), and Wilson. Specifically, we applied a theory-framed quantitative structure–property relationship (TF-QSPR) modeling approach for the purpose of generalization. In this modeling approach, theoretical frameworks, such as the NRTL model, are used to describe the phase behavior properties, and QSPR methodology is used to generalize the binary interaction parameters of the models. In this study, a binary VLE datab...
New Quantitative Structure‐Property Relationships (QSPR) are presented to predict the flash point of...
Phase characterization of liquid–liquid mixtures is required in numerous chemical process calculatio...
Phase equilibrium data are essential for the proper design and operation of most chemical processes....
Activity coefficients are used in phase equilibria calculations to account for the nonideal behavior...
Phase behavior properties of chemical species and their mixtures are essential to design chemical pr...
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...
Many important processes in the oil and gas industry (e.g., distillation, absorption, extraction) in...
The correlation of experimental liquid–liquid equilibrium (LLE) data for ternary and quaternary syst...
The present work deals with fitting literature data of liquid – liquid equilibria and to obtain a ne...
Running vapor-liquid equilibrium (VLE) data correlation with interaction parameters independent of t...
This is an extended research of the paper (Islam et al., 2011) conducted to obtain a universal set o...
Quantitative structure property relationships (QSPR) are increasingly used for the prediction of phy...
The activity coefficient models that have been proposed for correlation of Vapor-Liquid Equilibrium ...
This thesis focuses on the development of quantitative structure-activity relationship (QSPR) models...
New Quantitative Structure‐Property Relationships (QSPR) are presented to predict the flash point of...
Phase characterization of liquid–liquid mixtures is required in numerous chemical process calculatio...
Phase equilibrium data are essential for the proper design and operation of most chemical processes....
Activity coefficients are used in phase equilibria calculations to account for the nonideal behavior...
Phase behavior properties of chemical species and their mixtures are essential to design chemical pr...
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...
Many important processes in the oil and gas industry (e.g., distillation, absorption, extraction) in...
The correlation of experimental liquid–liquid equilibrium (LLE) data for ternary and quaternary syst...
The present work deals with fitting literature data of liquid – liquid equilibria and to obtain a ne...
Running vapor-liquid equilibrium (VLE) data correlation with interaction parameters independent of t...
This is an extended research of the paper (Islam et al., 2011) conducted to obtain a universal set o...
Quantitative structure property relationships (QSPR) are increasingly used for the prediction of phy...
The activity coefficient models that have been proposed for correlation of Vapor-Liquid Equilibrium ...
This thesis focuses on the development of quantitative structure-activity relationship (QSPR) models...
New Quantitative Structure‐Property Relationships (QSPR) are presented to predict the flash point of...
Phase characterization of liquid–liquid mixtures is required in numerous chemical process calculatio...
Phase equilibrium data are essential for the proper design and operation of most chemical processes....