Isobaric vapor-liquid phase equilibria for the binary systems of tert-butanol + 2-ethyl-1-hexanol and n-butanol + 2-ethyl-1-hexanol Ghanadzadeh, H.; Ghanadzadeh, A.; Sariri, R.; Boshra, A.; Fluid Phase Equilibria 2005, 233, 123-128
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Boiling point at pressure
- Methodology: EBULLIO:UFactor:64
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | Tbp (K) |
| 0 | 458.15 |
| 0.6500 | 396.1976 |
| 0.8600 | 393.335 |
| 0.9270 | 392.0 |
| 0.0112 | 444.5697 |
| 0.0200 | 441.3355 |
| 0.0900 | 418.6233 |
| 0.1685 | 409.6233 |
| 0.3000 | 402.89 |
| 0.3400 | 400.95 |
| 0.4400 | 399.5 |
| 0.5100 | 398.2821 |
29971; butan-1-ol + 2-ethyl-1-hexanol; 00081:00435