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): Mole fraction
- Methodology: CHROM:UFactor:16
- Phase(s): Gas' Liquid
- Substances:
Data
| x (mol mol-1) | x (mol mol-1) |
| 0 | 0.0008 |
| 0.4399 | 0.9797 |
| 0.5100 | 0.9819 |
| 0.6499 | 0.9858 |
| 0.7200 | 0.9877 |
| 0.7899 | 0.9899 |
| 0.8599 | 0.9925 |
| 0.9300 | 0.9957 |
| 0.0050 | 0.2984 |
| 0.0100 | 0.4755 |
| 0.0150 | 0.5892 |
| 0.0199 | 0.6667 |
| 0.0899 | 0.92 |
| 0.1599 | 0.9542 |
| 0.2299 | 0.9666 |
| 0.3000 | 0.973 |
29972; 2-methylpropan-2-ol + 2-ethyl-1-hexanol; 00347:00435