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 2014, 371, 82-92
Data
T = 353.15 K
x (mol mol-1) P (kPa)
0.03062 3.586
0.61932 74.49
0.69064 82.02
0.75080 87.9
0.80018 92.4
0.83976 95.77
0.85677 97.23
0.87229 98.36
0.88687 99.52
0.91181 101.3
0.93282 102.7
0.05736 6.66
0.95003 103.9
0.96378 104.8
0.97458 105.6
0.98262 106.1
0.98819 106.6
0.99210 106.9
0.99472 107.1
0.99648 107.3
0.99780 107.4
0.99870 107.5
0.08646 10.11
0.99944 107.6
1 107.6
0.15021 17.85
0.21579 25.9
0.29044 35.11
0.36637 44.66
0.44946 54.82
0.53704 65.25
22441; ethanol + 1-methyl-1-octylpyrrolidinium bis(trifluoromethylsulfonyl)amide; 00071:02464