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)
0.01373 0.8016
0.54850 33.38
0.62706 37.51
0.69560 40.75
0.75336 43.19
0.80065 44.97
0.82443 45.95
0.84009 46.3
0.86024 47.06
0.89034 47.91
0.91598 48.56
0.04012 2.331
0.93721 49.06
0.95431 49.45
0.96781 49.75
0.97792 49.99
0.98496 50.15
0.98991 50.29
0.99323 50.39
0.99546 50.48
0.99713 50.54
0.99831 50.6
0.06659 3.907
0.99927 50.65
1 50.69
0.10901 6.462
0.15714 9.437
0.21695 13.25
0.28965 17.86
0.37209 23.01
0.46203 28.44
22442; propan-1-ol + 1-methyl-1-octylpyrrolidinium bis(trifluoromethylsulfonyl)amide; 00101:02464