| 1 |
Influence of sulfate-based anion ionic liquids on the separation factor of the binary azeotropic system acetone plus methanol
Matsuda H, Liebert V, Tochigi K, Gmehling J
Fluid Phase Equilibria, 340, 27, 2013 |
| 2 |
Vapor-liquid equilibria of ternary systems with 1-ethyl-3-methylimidazolium ethyl sulfate using headspace gas chromatography
Matsuda H, Tochigi K, Liebert V, Gmehling J
Fluid Phase Equilibria, 307(2), 197, 2011 |
| 3 |
Chemical Equilibrium Conversion of the tert-Amyl-methyl-ether Synthesis in the Presence of n-Pentane, Tetrahydrofuran, or Benzene
Liebert V, Hector T, Gmehling J
Industrial & Engineering Chemistry Research, 49(9), 4412, 2010 |
| 4 |
Measurement and prediction of activity coefficients at infinite dilution (gamma(infinity)), vapor-liquid equilibria (VLE) and excess enthalpies (H-E) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
Nebig S, Liebert V, Gmehling J
Fluid Phase Equilibria, 277(1), 61, 2009 |
| 5 |
Influence of ionic liquids on the separation factor of three standard separation problems
Westerholt A, Liebert V, Gmehling J
Fluid Phase Equilibria, 280(1-2), 56, 2009 |
| 6 |
Measurement and prediction of activity coefficients at infinite dilution (gamma(infinity)), vapor-liquid equilibria (VLE) and excess enthalpies (H-E) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund) (vol 277, pg 61, 2009)
Nebig S, Liebert V, Gmehling J
Fluid Phase Equilibria, 283(1-2), 102, 2009 |
| 7 |
Experimental and predicted phase equilibria and excess properties for systems with ionic liquids
Liebert V, Nebig S, Gmehling J
Fluid Phase Equilibria, 268(1-2), 14, 2008 |
