We carried out a molecular simulation study of the vapor-liquid equilibria of alkane-CO2 and perfluoro-alkane-CO2 binary mixtures using the Gibbs ensemble Monte Carlo method. We used simple interaction site models and the conventional Lorentz-Berthelot combining rules for the cross interaction between the solute and solvent species with no adjustable parameters to predict the vapor-liquid phase equilibrium of the hexane-CO2 and perfluorohexane-CO2 mixtures. The predicted CO2 mole fraction on the liquid branch is higher than the experimental results by about 10-13%. The gas-phase solubility of hexane and perfluorohexane in CO2 is generally smaller than the experimental results. The model predicts a higher solubility for the perfluoroalkanes ...
Mixtures of carbon dioxide and some hydrocarbons will form liquid-liquid-vapor equilibrium at tempe...
International audienceAccurate knowledge of the thermodynamic properties of CO2+ contaminant mixture...
Mixtures of carbon dioxide and some hydrocarbons will form liquid-liquid-vapor equilibrium at tempe...
Gibbs ensemble Monte Carlo simulations were performed to calculate the vapor- liquid coexistence pro...
The phase behavior of binary mixtures of carbon dioxide (CO2) and hydrofluoroethers (HFEs) has been ...
The perturbed-chain statistical associating fluid theory (PC-SAFT) is used to investigate the vapor-...
We present a single-particle Lennard-Jones (L-J) model for CO2 and N2. Sim-plified L-J models for ot...
International audienceA polar version of the group contribution PC-SAFT equation of state (GC-PPC-SA...
International audienceA polar version of the group contribution PC-SAFT equation of state (GC-PPC-SA...
We present a single-particle Lennard-Jones (L-J) model for CO2 and N2. Simplified L-J models for oth...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
Knowledge of the phase behavior of mixtures of oil with carbon dioxide and water is essential for re...
Mixtures of carbon dioxide and some hydrocarbons will form liquid-liquid-vapor equilibrium at tempe...
International audienceAccurate knowledge of the thermodynamic properties of CO2+ contaminant mixture...
Mixtures of carbon dioxide and some hydrocarbons will form liquid-liquid-vapor equilibrium at tempe...
Gibbs ensemble Monte Carlo simulations were performed to calculate the vapor- liquid coexistence pro...
The phase behavior of binary mixtures of carbon dioxide (CO2) and hydrofluoroethers (HFEs) has been ...
The perturbed-chain statistical associating fluid theory (PC-SAFT) is used to investigate the vapor-...
We present a single-particle Lennard-Jones (L-J) model for CO2 and N2. Sim-plified L-J models for ot...
International audienceA polar version of the group contribution PC-SAFT equation of state (GC-PPC-SA...
International audienceA polar version of the group contribution PC-SAFT equation of state (GC-PPC-SA...
We present a single-particle Lennard-Jones (L-J) model for CO2 and N2. Simplified L-J models for oth...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
International audienceIsothermal Vapor-Liquid Equilibrium (VLE) data for the binary mixture of CO 2 ...
Knowledge of the phase behavior of mixtures of oil with carbon dioxide and water is essential for re...
Mixtures of carbon dioxide and some hydrocarbons will form liquid-liquid-vapor equilibrium at tempe...
International audienceAccurate knowledge of the thermodynamic properties of CO2+ contaminant mixture...
Mixtures of carbon dioxide and some hydrocarbons will form liquid-liquid-vapor equilibrium at tempe...