| 1 |
GCA-EOS extension to mixtures of phenol ethers and derivatives with hydrocarbons and water
Sanchez FA, Ille Y, Dahmen N, Pereda S
Fluid Phase Equilibria, 490, 13, 2019 |
| 2 |
Phase equilibrium engineering of glycerol acetates fractionation with pressurized CO2
Montoya MF, Sanchez FA, Hegel PE, Pereda S
Journal of Supercritical Fluids, 132, 51, 2018 |
| 3 |
Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
Prieto MG, Williams-Wynn MD, Bahadur I, Sanchez FA, Mohammadi AH, Pereda S, Ramjugernath D
Journal of Chemical Thermodynamics, 105, 226, 2017 |
| 4 |
Thermodynamic model for biomass processing in pressure intensified technologies
Prieto MG, Sanchez FA, Pereda S
Journal of Supercritical Fluids, 96, 53, 2015 |
| 5 |
Modeling the phase behavior of cyclic compounds in mixtures of water, alcohols and hydrocarbons
Soria TM, Sanchez FA, Pereda S, Bottini SB
Fluid Phase Equilibria, 361, 143, 2014 |
| 6 |
Thermodynamic model for process design, simulation and optimization in the production of biodiesel
Cotabarren N, Hegel P, Pereda S
Fluid Phase Equilibria, 362, 108, 2014 |
| 7 |
Supercritical production and fractionation of fatty acid esters and acylglycerols
Soto G, Hegel P, Pereda S
Journal of Supercritical Fluids, 93, 74, 2014 |
| 8 |
GCA-EoS: A SAFT group contribution model-Extension to mixtures containing aromatic hydrocarbons and associating compounds
Sanchez FA, Pereda S, Brignole EA
Fluid Phase Equilibria, 306(1), 112, 2011 |
| 9 |
Phase equilibria modeling of biodiesel related mixtures using the GCA-EoS model
Andreatta AE, Lugo R, de Hemptinne JC, Brignole EA, Bottini SB
Fluid Phase Equilibria, 296(2), 75, 2010 |
| 10 |
Modeling alcohol plus water plus hydrocarbon mixtures with the group contribution with association equation of state GCA-EoS
Soria TM, Sanchez FA, Pereda S, Bottini SB
Fluid Phase Equilibria, 296(2), 116, 2010 |
