International audiencePhase equilibria of oxygen-bearing aromatic compounds, hydrocarbons and water mixtures are of essential interest in many processes using feeds originating from biomass. The strong non-ideal thermodynamic behavior of these systems sometimes results in immiscibility with both water and alkanes.To address this problem, the GC-PPC-SAFT equation of state [Tamouza et al., 2004; Nguyen-Huynh et al., 2008a] is extended to some selected components: phenol, alkyl-phenols, alkyl-benzoates, benzaldehyde and anisole. However, as in these multifunctional compounds, the proximity of polar functional groups may result in a lack of transferability of the parameters from the monofunctional homologous species, some parameters have been a...
Liquid-liquid equilibria of N-formylmorpholine (NFM) with alkanes (n-hexane, n-heptane, isononane), ...
This work is focused on the thermodynamic modeling of systems related to biodiesel processing using ...
A new three constant equation of state for fluids and fluid mixtures has been proposed. The equation...
International audiencePhase equilibria of oxygen-bearing aromatic compounds, hydrocarbons and water ...
Anisol and its derivatives are typically used in the flavoring and fragrance industry, and they are ...
Parameters needed for the Statistical Associating Fluid Theory (SAFT) equation of state are usually ...
International audienceThe present work proposes an analysis of the solubility of a number of importa...
Group-contribution polar versions of SAFT equations of state are very useful for predictive calculat...
International audienceThe SAFT-LJ EOS improved by Sun and Dubessy (2010, 2012) is extended to water-...
Vapor–liquid equilibria (VLE), liquid–liquid equilibria (LLE), and vapor–liquid–liquid equilibria (V...
Process modeling and feasibility studies for biofuel production require accurate phase equilibria da...
AbstractThe application of the SAFT-γ Mie group contribution approach [Papaioannou et al., J. Chem. ...
International audienceIn this work, experimental vapor−liquid equilibria (VLE) of water + ethanol + ...
The fuel industry in many parts of the world is blending alcohols with motor fuel either to extend t...
We show how to extend the Hudson-McCoubrey combining rules, which were de-rived assuming the Lennard...
Liquid-liquid equilibria of N-formylmorpholine (NFM) with alkanes (n-hexane, n-heptane, isononane), ...
This work is focused on the thermodynamic modeling of systems related to biodiesel processing using ...
A new three constant equation of state for fluids and fluid mixtures has been proposed. The equation...
International audiencePhase equilibria of oxygen-bearing aromatic compounds, hydrocarbons and water ...
Anisol and its derivatives are typically used in the flavoring and fragrance industry, and they are ...
Parameters needed for the Statistical Associating Fluid Theory (SAFT) equation of state are usually ...
International audienceThe present work proposes an analysis of the solubility of a number of importa...
Group-contribution polar versions of SAFT equations of state are very useful for predictive calculat...
International audienceThe SAFT-LJ EOS improved by Sun and Dubessy (2010, 2012) is extended to water-...
Vapor–liquid equilibria (VLE), liquid–liquid equilibria (LLE), and vapor–liquid–liquid equilibria (V...
Process modeling and feasibility studies for biofuel production require accurate phase equilibria da...
AbstractThe application of the SAFT-γ Mie group contribution approach [Papaioannou et al., J. Chem. ...
International audienceIn this work, experimental vapor−liquid equilibria (VLE) of water + ethanol + ...
The fuel industry in many parts of the world is blending alcohols with motor fuel either to extend t...
We show how to extend the Hudson-McCoubrey combining rules, which were de-rived assuming the Lennard...
Liquid-liquid equilibria of N-formylmorpholine (NFM) with alkanes (n-hexane, n-heptane, isononane), ...
This work is focused on the thermodynamic modeling of systems related to biodiesel processing using ...
A new three constant equation of state for fluids and fluid mixtures has been proposed. The equation...