NIST TRC ThermoML Dataset

Experimental and predicted phase equilibria and excess properties for systems with ionic liquids Liebert, V.; Nebig, S.; Gmehling, J.; Fluid Phase Equilibria 2008, 268, 14-20

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Activity coefficient
Methodology: dilutor technique
Phase(s): Liquid
Substances:
1. ethanol C2H6O (LFQSCWFLJHTTHZ-UHFFFAOYSA-N) - Commercial source
2. 1-ethyl-3-methylimidazolium ethylsulfate C8H16N2O4S (VRFOKYHDLYBVAL-UHFFFAOYSA-M) - Commercial source

Data

P = 101 kPa, x = 0 mol mol^-1
T (K)	γ (mol dm³ mol-1 dm^-3)
323.15	0.57
333.15	0.6
343.15	0.65
353.15	0.7

19360; ethanol + 1-ethyl-3-methylimidazolium ethyl sulfate; 00071:01308