Ionic Liquids as Entrainers in Extractive Distillation: Isobaric Vapor-Liquid Equilibria for Acetone + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Orchillés, A.V.; Miguel, P.J.; Vercher, E.; Martínez-Andreu, A.; Journal of Chemical & Engineering Data 2007, 52, 141-147
Data
P = 100 kPa
x (mol mol-1) Tbp (K)
0.0030 337.58
0.0774 339.81
0.0903 340.21
0.1048 340.68
0.1126 340.9
0.1247 341.37
0.1352 341.69
0.1447 342.05
0.1523 342.3
0.1612 342.7
0.1669 342.88
0.0061 337.68
0.1798 343.3
0.1866 343.69
0.1980 344.13
0.2110 344.67
0.2228 345.19
0.2334 345.67
0.2455 346.21
0.2564 346.7
0.2687 347.32
0.2782 347.78
0.0117 337.87
0.2921 348.45
0.3065 349.35
0.3246 350.35
0.3442 351.55
0.3656 352.75
0.3912 354.55
0.4235 356.55
0.4504 358.35
0.4743 360.15
0.0192 338.1
0.0281 338.36
0.0373 338.63
0.0480 338.94
0.0563 339.19
0.0649 339.42
5080; methanol + 1-ethyl-3-methylimidazolium trifluoromethanesulfonate; 00016:00632