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:128
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | Tbp (K) |
| 0 | 459.73 |
| 0.4399 | 366.7212 |
| 0.5100 | 363.816 |
| 0.6499 | 361.6598 |
| 0.7200 | 360.63 |
| 0.7899 | 359.5657 |
| 0.8599 | 357.09 |
| 0.9300 | 355.57 |
| 0.0050 | 445.5325 |
| 0.0100 | 436.1964 |
| 0.0150 | 428.8066 |
| 0.0199 | 422.794 |
| 0.0899 | 388.23 |
| 0.1599 | 380.5 |
| 0.2299 | 372.1293 |
| 0.3000 | 368.901 |
29972; 2-methylpropan-2-ol + 2-ethyl-1-hexanol; 00347:00435