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)
0.02745 4.687
0.66123 123.3
0.72745 135.3
0.78243 144.9
0.82685 152.4
0.86204 157.9
0.89059 162.5
0.91829 166.5
0.93678 169.2
0.95213 171.5
0.96456 173.3
0.07554 13.17
0.97439 174.9
0.98771 177.1
0.99162 177.8
0.99434 178.3
0.99626 178.6
0.99756 178.9
0.99856 179.1
0.99918 179.2
0.99969 179.4
1 179.4
0.12136 21.53
0.18245 32.89
0.24879 45.23
0.32601 59.76
0.41039 76.0
0.49778 92.68
0.58379 108.9
22440; methanol + 1-methyl-1-octylpyrrolidinium bis(trifluoromethylsulfonyl)amide; 00016:02464