| 1 |
(Solid plus liquid) equilibrium phase diagrams in binary mixtures containing terpenes: New experimental data and analysis of several modelling strategies with modified UNIFAC (Dortmund) and PC-SAFT equation of state
Okuniewski M, Paduszynski K, Domanska U
Fluid Phase Equilibria, 422, 66, 2016 |
| 2 |
Application of the UNIFAC models for prediction and description of excess molar enthalpies for binary mixtures of n-propanol, acetic acid, n-propyl acetate, and water
Letyanina I, Tsvetov N, Toikka A
Fluid Phase Equilibria, 427, 202, 2016 |
| 3 |
Measurement, correlation and prediction of isothermal vapor-liquid equilibria of different systems containing vegetable oils
Belting PC, Gmehling J, Bolts R, Rarey J, Ceriani R, Chiavone O, Meirelles AJA
Fluid Phase Equilibria, 395, 15, 2015 |
| 4 |
(Vapour plus liquid) equilibria, (VLE) excess molar enthalpies and infinite dilution activity coefficients of selected binary systems involving n-hexyl pyridinium bis(trifluoromethylsulphonyl)imide ionic liquid: Experimental and predictions using modified UNIFAC (Dortmund)
Bahadur I, Pal A, Gmehling J, Hector T, Tumba K, Singh S, Ebenso EE
Journal of Chemical Thermodynamics, 90, 92, 2015 |
| 5 |
Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
Belting PC, Rarey J, Gmehling J, Ceriani R, Chiavone-Filho O, Meirelles AJA
Fluid Phase Equilibria, 361, 215, 2014 |
| 6 |
Present status of the modified UNIFAC model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids
Hector T, Gmehling J
Fluid Phase Equilibria, 371, 82, 2014 |
| 7 |
Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC
Hector T, Uhlig L, Gmehling J
Fluid Phase Equilibria, 338, 135, 2013 |
| 8 |
Extension of modified UNIFAC (Dortmund) matrix to piperidinium ionic liquids
Paduszynski K, Domanska U
Fluid Phase Equilibria, 353, 115, 2013 |
| 9 |
Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine
Klauck M, Silbermann R, Metasch R, Unger S, Schmelzer J
Fluid Phase Equilibria, 314, 169, 2012 |
| 10 |
Prediction of phase equilibria and excess properties for systems with ionic liquids using modified UNIFAC: Typical results and present status of the modified UNIFAC matrix for ionic liquids
Nebig S, Gmehling J
Fluid Phase Equilibria, 302(1-2), 220, 2011 |
