Isobaric Vapor-Liquid Equilibria for Three Ternary Systems: Water + 2-Propanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate, Water + 1-Propanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate, and Water + 1-Propanol + 1-Butyl-3-methylimidazolium Tetrafluoroborate Zhang, L.; Han, J.; Wang, R.; Qiu, X.; Ji, J.; Journal of Chemical & Engineering Data 2007, 52, 1401-1407
Data
P = 100 kPa
x (mol mol-1) x (mol mol-1) Tbp (K)
0.0016 0.8302 355.46
0.0462 0.4231 358.52
0.0499 0.8390 355.05
0.0612 0.6394 355.44
0.0750 0.4054 358.72
0.0837 0.7579 354.92
0.1010 0.7920 354.75
0.1064 0.6040 355.33
0.1121 0.3825 358.94
0.1272 0.7195 354.72
0.1536 0.3570 359.61
0.0066 0.6820 355.6
0.1584 0.7392 354.44
0.1700 0.6817 354.53
0.1705 0.5540 355.21
0.2060 0.3248 359.97
0.2171 0.6402 354.4
0.2182 0.6843 354.18
0.2415 0.4985 355.16
0.2682 0.5951 354.3
0.2786 0.2800 360.62
0.2929 0.6156 354.04
0.0088 0.4462 358.12
0.3119 0.5566 354.25
0.3271 0.4317 355.23
0.3502 0.2359 361.48
0.3527 0.5206 354.24
0.3714 0.5435 354.01
0.3893 0.4882 354.26
0.4180 0.3607 355.54
0.4325 0.1852 363.03
0.4654 0.4570 354.11
0.4756 0.4121 354.43
0.0108 0.8750 355.37
0.5033 0.2941 356.08
0.5259 0.1275 365.73
0.5654 0.3329 354.79
0.5656 0.3649 354.43
0.5764 0.0964 367.87
0.6209 0.2022 357.54
0.6632 0.2466 355.48
0.6671 0.2715 354.82
0.7077 0.1344 359.75
0.7453 0.1050 361.29
0.0167 0.8169 355.35
0.7663 0.1557 356.94
0.7729 0.1742 355.89
0.8252 0.1037 358.8
0.8420 0.1108 357.37
0.0224 0.6697 355.54
0.0238 0.4369 358.36
0.0378 0.8501 355.08
0.0414 0.7952 355.17
24486; propan-2-ol + water + 1-ethyl-3-methylimidazolium tetrafluoroborate; 00004:00082:00322