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
- Journal: Journal of Chemical & Engineering Data
- Sample Quantity(ies): Mole fraction
- Methodology: CHROM:UFactor:4
- Phase(s): Gas' Liquid
- Substances:
Data
| x (mol mol-1) | x (mol mol-1) | x (mol mol-1) |
| 0.0027 | 0.6149 | 0.995 |
| 0.1538 | 0.6587 | 0.7186 |
| 0.2075 | 0.7050 | 0.6366 |
| 0.2084 | 0.4643 | 0.6658 |
| 0.2421 | 0.5833 | 0.6134 |
| 0.2740 | 0.4163 | 0.6021 |
| 0.3039 | 0.6155 | 0.5428 |
| 0.3234 | 0.5140 | 0.5569 |
| 0.3445 | 0.3647 | 0.5371 |
| 0.4025 | 0.5239 | 0.4787 |
| 0.4191 | 0.4324 | 0.5141 |
| 0.0176 | 0.8813 | 0.9564 |
| 0.4214 | 0.3084 | 0.5014 |
| 0.5025 | 0.2491 | 0.4511 |
| 0.5068 | 0.4271 | 0.4491 |
| 0.5088 | 0.3558 | 0.4584 |
| 0.5834 | 0.1899 | 0.4307 |
| 0.5972 | 0.2804 | 0.4408 |
| 0.6032 | 0.3377 | 0.4345 |
| 0.6692 | 0.1271 | 0.3978 |
| 0.6945 | 0.1975 | 0.4195 |
| 0.6967 | 0.2508 | 0.4247 |
| 0.0178 | 0.7747 | 0.9613 |
| 0.7269 | 0.0849 | 0.3352 |
| 0.7641 | 0.0577 | 0.2889 |
| 0.7783 | 0.1260 | 0.4028 |
| 0.7873 | 0.1668 | 0.4264 |
| 0.8285 | 0.0832 | 0.3977 |
| 0.8494 | 0.1091 | 0.4178 |
| 0.0359 | 0.8643 | 0.9121 |
| 0.0634 | 0.8388 | 0.8543 |
| 0.0771 | 0.7241 | 0.8424 |
| 0.0870 | 0.5532 | 0.8473 |
| 0.1270 | 0.7797 | 0.741 |
| 0.1449 | 0.5108 | 0.7531 |
9235; 1-propanol + water + 1-butyl-3-methylimidazolium tetrafluoroborate; 00004:00009:00101