Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems Kamihama, N.; Matsuda, H.; Kurihara, K.; Tochigi, K.; Oba, S.; Journal of Chemical & Engineering Data 2012, 57, 339-344
- Journal: Journal of Chemical & Engineering Data
- Sample Quantity(ies): Mole fraction
- Methodology: Chromatography
- Phase(s): Gas' Liquid
- Substances:
Data
| T (K) | x (mol mol-1) | x (mol mol-1) | x (mol mol-1) | x (mol mol-1) |
| 365.94 | 0.078 | 0.753 | 0.598 | 0.401 |
| 361.77 | 0.230 | 0.528 | 0.401 | 0.598 |
| 366.50 | 0.231 | 0.374 | 0.334 | 0.661 |
| 363.60 | 0.235 | 0.458 | 0.37 | 0.627 |
| 361.83 | 0.255 | 0.478 | 0.369 | 0.629 |
| 364.40 | 0.255 | 0.395 | 0.334 | 0.663 |
| 367.79 | 0.268 | 0.278 | 0.262 | 0.734 |
| 362.54 | 0.279 | 0.416 | 0.336 | 0.662 |
| 365.48 | 0.296 | 0.296 | 0.264 | 0.731 |
| 368.45 | 0.340 | 0.144 | 0.142 | 0.852 |
| 362.39 | 0.393 | 0.24 | 0.21 | 0.787 |
| 366.41 | 0.103 | 0.664 | 0.548 | 0.451 |
| 368.91 | 0.403 | 0.039 | 0.041 | 0.95 |
| 363.98 | 0.416 | 0.165 | 0.152 | 0.844 |
| 360.58 | 0.429 | 0.255 | 0.214 | 0.784 |
| 367.81 | 0.441 | 0.019 | 0.02 | 0.974 |
| 358.86 | 0.467 | 0.27 | 0.223 | 0.776 |
| 360.55 | 0.491 | 0.19 | 0.162 | 0.836 |
| 362.39 | 0.508 | 0.099 | 0.089 | 0.907 |
| 359.93 | 0.571 | 0.11 | 0.098 | 0.899 |
| 357.14 | 0.581 | 0.215 | 0.18 | 0.819 |
| 359.74 | 0.607 | 0.075 | 0.071 | 0.927 |
| 362.64 | 0.159 | 0.633 | 0.474 | 0.525 |
| 359.79 | 0.613 | 0.069 | 0.066 | 0.931 |
| 358.43 | 0.664 | 0.053 | 0.05 | 0.948 |
| 356.24 | 0.678 | 0.123 | 0.11 | 0.889 |
| 353.77 | 0.910 | 0.002 | 0.003 | 0.996 |
| 368.94 | 0.172 | 0.426 | 0.4 | 0.594 |
| 371.77 | 0.181 | 0.333 | 0.344 | 0.648 |
| 364.51 | 0.187 | 0.516 | 0.422 | 0.576 |
| 367.63 | 0.192 | 0.421 | 0.377 | 0.618 |
| 365.43 | 0.193 | 0.483 | 0.406 | 0.591 |
| 368.76 | 0.210 | 0.355 | 0.338 | 0.657 |
12667; ethanol + 1,2-ethanediol + water; 00004:00068:00071