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)
0.01503 0.4838
0.46749 13.89
0.54829 15.79
0.62244 17.3
0.68770 18.46
0.74317 19.29
0.81275 20.22
0.85053 20.68
0.88349 20.96
0.91133 21.16
0.93424 21.33
0.03606 1.162
0.95266 21.44
0.96674 21.54
0.97679 21.6
0.98407 21.66
0.98919 21.71
0.99279 21.74
0.99568 21.77
0.99745 21.79
0.99906 21.81
1 21.82
0.05372 1.734
0.08515 2.743
0.12293 3.934
0.17025 5.393
0.22970 7.229
0.30093 9.347
0.38301 11.69
33213; butan-1-ol + 1-hexyl-3-methylpyridinium 1,1,1-trifluoro-N-[(trifluoromethyl)sulfonyl]methanesulfonamide; 00081:03433