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)
0.0157 329.45
0.1448 332.55
0.1585 332.85
0.1721 333.25
0.1867 333.75
0.2010 334.15
0.2124 334.65
0.2240 334.95
0.2359 335.35
0.2481 335.85
0.2596 336.3
0.0263 329.69
0.2702 336.65
0.2769 337.05
0.2866 337.45
0.2945 337.95
0.3095 338.45
0.3236 339.15
0.3435 340.25
0.3532 340.6
0.3636 341.21
0.3686 341.45
0.0395 330.01
0.3791 342.05
0.3908 342.77
0.4022 343.45
0.4105 343.55
0.4125 344.05
0.4282 344.95
0.4349 345.45
0.4399 345.95
0.4513 346.45
0.4609 347.25
0.0544 330.34
0.4722 347.95
0.4876 348.95
0.0700 330.69
0.0832 331.01
0.1004 331.38
0.1150 331.73
0.1282 332.05
19551; acetone + 1-ethyl-3-methylimidazolium trifluoromethanesulfonate; 00024:00632