| 1 |
The NRTL-PRA group contribution EoS for the simultaneous prediction of LLE, VLE and h(E) of hydrocarbon mixtures with associating compounds
Neau E, Raspo I, Escandell J
Fluid Phase Equilibria, 427, 126, 2016 |
| 2 |
Enzymatic synthesis of butyl acetate in a packed bed reactor under liquid and supercritical conditions
Escandell J, Wurm DJ, Belleville MP, Sanchez J, Harasek M, Paolucci-Jeanjean D
Catalysis Today, 255, 3, 2015 |
| 3 |
Prediction of solid polycyclic aromatic hydrocarbons solubility in water, with the NRTL-PR model
Escandell J, Raspo I, Neau E
Fluid Phase Equilibria, 362, 87, 2014 |
| 4 |
A generalized reference state at constant volume for the prediction of phase equilibria from low pressure model parameters: Application to size-asymmetric systems and to the Wong-Sandler mixing rule
Neau E, Escandell J, Raspo I
Chemical Engineering Science, 66(18), 4148, 2011 |
| 5 |
A new formulation of the predictive NRTL-PR model in terms of k(ij) mixing rules. Extension of the group contributions for the modeling of hydrocarbons in the presence of associating compounds
Escandell J, Neau E, Nicolas C
Fluid Phase Equilibria, 301(1), 80, 2011 |
| 6 |
Modeling of Highly Nonideal Systems: 1. A Generalized Version of the NRTL Equation for the Description of Low-Pressure Equilibria
Neau E, Escandell J, Nicolas C
Industrial & Engineering Chemistry Research, 49(16), 7580, 2010 |
| 7 |
Modeling of Highly Nonideal Systems: 2. Prediction of High Pressure Phase Equilibria with the Group Contribution NRTL-PR EoS
Neau E, Escandell J, Nicolas C
Industrial & Engineering Chemistry Research, 49(16), 7589, 2010 |
| 8 |
Diffusion Coefficients of Organic Compounds at Infinite Dilution in Ternary Mixtures: Experimental Determinations and Modeling
Safi A, Nicolas C, Neau E, Escandell J
Journal of Chemical and Engineering Data, 55(12), 5449, 2010 |
| 9 |
The Soave, Twu and Boston-Mathias alpha functions in cubic equations of state Part I. Theoretical analysis of their variations according to temperature
Neau E, Hernandez-Garduza O, Escandell J, Nicolas C, Raspo I
Fluid Phase Equilibria, 276(2), 87, 2009 |
| 10 |
The Soave, Twu and Boston-Mathias alpha functions in cubic equations of state. Part II. Modeling of thermodynamic properties of pure compounds
Neau E, Raspo I, Escandell J, Nicolas C, Hernandez-Garduza O
Fluid Phase Equilibria, 276(2), 156, 2009 |
