Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Diisopropyl Ether, 2-Propyl Alcohol, and n-Butyl Propionate at 101.3 kPa Lladosa, E.; MontoĢn, J.B.; Burguet, M.C.; Baviera, R.; Journal of Chemical & Engineering Data 2009, 54, 2991-2995
- 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) |
| 340.70 | 0.750 | 0.248 | 0.269 | 0.688 |
| 346.41 | 0.741 | 0.242 | 0.198 | 0.586 |
| 347.13 | 0.577 | 0.408 | 0.441 | 0.374 |
| 348.35 | 0.493 | 0.491 | 0.559 | 0.274 |
| 348.96 | 0.383 | 0.608 | 0.754 | 0.162 |
| 349.48 | 0.676 | 0.298 | 0.234 | 0.474 |
| 350.30 | 0.590 | 0.383 | 0.326 | 0.376 |
| 351.50 | 0.481 | 0.492 | 0.44 | 0.272 |
| 351.78 | 0.370 | 0.607 | 0.623 | 0.173 |
| 352.32 | 0.222 | 0.765 | 0.844 | 0.076 |
| 354.00 | 0.111 | 0.88 | 0.919 | 0.033 |
| 341.71 | 0.914 | 0.083 | 0.056 | 0.895 |
| 354.28 | 0.628 | 0.328 | 0.216 | 0.374 |
| 354.58 | 0.369 | 0.596 | 0.501 | 0.18 |
| 354.73 | 0.506 | 0.453 | 0.326 | 0.277 |
| 354.77 | 0.762 | 0.192 | 0.109 | 0.478 |
| 354.87 | 0.193 | 0.782 | 0.751 | 0.073 |
| 355.06 | 0.879 | 0.077 | 0.041 | 0.566 |
| 341.73 | 0.639 | 0.359 | 0.51 | 0.465 |
| 342.56 | 0.706 | 0.287 | 0.318 | 0.59 |
| 342.78 | 0.850 | 0.143 | 0.106 | 0.793 |
| 344.56 | 0.578 | 0.415 | 0.549 | 0.367 |
| 344.83 | 0.512 | 0.485 | 0.703 | 0.266 |
| 345.51 | 0.651 | 0.336 | 0.35 | 0.481 |
| 346.24 | 0.839 | 0.144 | 0.1 | 0.702 |
25861; propan-2-ol + diisopropyl ether + butyl propanoate; 00082:00250:00750