Add to ORKGIn the present study a thermodynamic model for prediction of gas-liquid equilibrium at high pressures and different temperatures prepared for the binary systems of carbon dioxide (1) with each of the one of the liquid physical solvents (2) (sulfolane, n-methyl-2-pyrrolidone and propylene carbonate) using Peng-Robenson equation of state (PR-EOS) with different mixing rules to show the effect of the type of mixing rule used.Comparison of the experimental phase equilibrium data in the literature with the results of the model showed very good representation for some mixing rules and good for the others.</p
The ability to predict the behaviour of high-pressure mixtures of carbon dioxide and alcohol is impo...
Carbon dioxide/water (CO2/H2O) mixtures are of much interest in carbon capture and storage, atmosphe...
In this work, thermodynamic models for fitting the phase equilibrium of binary systems were applied,...
The high-pressure phase equilibrium in binary mixtures of carbon dioxide and various liquids such as...
One of the most important design considerations which should not be ignored during the equipment de...
High pressure vapor-liquid phase equilibrium data (P-T-x-y) for the binary mixtures of organic solve...
In this work the phase behavior of the binary system (ethyl lactate + CO2) was studied in the pressu...
VLE in carbon dioxide binary mixts. with phenol and di-Ph carbonate were studied. The bubble points ...
The phase behaviour of the pyrrole–carbon dioxide binary system was investigated in a variable volum...
Vapor-liquid equilibrium data were measured for the carbon dioxide + ethyl n-butyrate (EB) binary sy...
Measurements of high-pressure gas-liquid equilibria of the binary system carbon dioxide-citral were ...
It is currently acknowledged that thermodynamic models routinely used to model the behavior of fluid...
The phase behavior of the carbon dioxide + cycloalkane mixtures usually receives low attention, thou...
In this work, thermodynamic models for fitting the phase equilibrium of binary systems were applied,...
An appropriate thermodynamic model is vital for simulating the multiple industrial processes involvi...
The ability to predict the behaviour of high-pressure mixtures of carbon dioxide and alcohol is impo...
Carbon dioxide/water (CO2/H2O) mixtures are of much interest in carbon capture and storage, atmosphe...
In this work, thermodynamic models for fitting the phase equilibrium of binary systems were applied,...
The high-pressure phase equilibrium in binary mixtures of carbon dioxide and various liquids such as...
One of the most important design considerations which should not be ignored during the equipment de...
High pressure vapor-liquid phase equilibrium data (P-T-x-y) for the binary mixtures of organic solve...
In this work the phase behavior of the binary system (ethyl lactate + CO2) was studied in the pressu...
VLE in carbon dioxide binary mixts. with phenol and di-Ph carbonate were studied. The bubble points ...
The phase behaviour of the pyrrole–carbon dioxide binary system was investigated in a variable volum...
Vapor-liquid equilibrium data were measured for the carbon dioxide + ethyl n-butyrate (EB) binary sy...
Measurements of high-pressure gas-liquid equilibria of the binary system carbon dioxide-citral were ...
It is currently acknowledged that thermodynamic models routinely used to model the behavior of fluid...
The phase behavior of the carbon dioxide + cycloalkane mixtures usually receives low attention, thou...
In this work, thermodynamic models for fitting the phase equilibrium of binary systems were applied,...
An appropriate thermodynamic model is vital for simulating the multiple industrial processes involvi...
The ability to predict the behaviour of high-pressure mixtures of carbon dioxide and alcohol is impo...
Carbon dioxide/water (CO2/H2O) mixtures are of much interest in carbon capture and storage, atmosphe...
In this work, thermodynamic models for fitting the phase equilibrium of binary systems were applied,...