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 = 343.15 K
x (mol mol-1) P (kPa)
0.00619 0.8374
0.35931 44.04
0.43797 52.81
0.51513 60.88
0.58742 67.73
0.65235 72.69
0.71098 73.18
0.79357 73.23
0.83768 73.24
0.87598 73.24
0.90808 73.26
0.01788 2.401
0.93425 73.28
0.95438 73.31
0.96866 73.34
0.97881 73.37
0.98570 73.39
0.99038 73.41
0.99393 73.43
0.99639 73.44
0.99841 73.46
1 73.47
0.03048 4.041
0.05246 6.848
0.07816 10.08
0.11265 14.41
0.15735 20.06
0.21363 26.89
0.28263 35.14
17521; benzene + 1-butyl-3-methylimidazolium hexafluorophosphate; 00029:00481