Phase equilibria properties of binary and ternary systems containing di-isopropyl ether + isobutanol + benzene at 313.15 K Villamañán, R.; Chamorro, C.; Martín, M.; Segovia, J.; Fluid Phase Equilibria 2006, 239, 178-182
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Vapor pressure
- Methodology: CCELL:UFactor:2
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | P (kPa) |
| 0 | 3.996 |
| 0.3996 | 20.077 |
| 0.4488 | 20.808 |
| 0.4495 | 20.827 |
| 0.4994 | 21.458 |
| 0.4995 | 21.452 |
| 0.5492 | 21.99 |
| 0.5495 | 22.001 |
| 0.5990 | 22.465 |
| 0.6013 | 22.476 |
| 0.6488 | 22.879 |
| 0.0584 | 8.181 |
| 0.6995 | 23.248 |
| 0.7491 | 23.57 |
| 0.8001 | 23.875 |
| 0.8553 | 24.145 |
| 0.8990 | 24.341 |
| 0.9518 | 24.518 |
| 1 | 24.38 |
| 0.0982 | 10.54 |
| 0.1500 | 13.099 |
| 0.2072 | 15.356 |
| 0.2539 | 16.881 |
| 0.2995 | 18.06 |
| 0.3496 | 19.157 |
| 0.3991 | 20.053 |
30131; benzene + 2-methyl-1-propanol; 00029:00147