Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa Fan, K.; Zhou, F.; Chen, C.; Li, Y.; Li, W.; Xiao, B.; Xu, C.; Journal of Chemical & Engineering Data 2018, 63, 2637-2643
- Journal: Journal of Chemical & Engineering Data
- Sample Quantity(ies): Mole fraction
- Methodology: Chromatography
- Phase(s): Gas' Liquid
- Substances:
Data
| x (mol mol-1) | x (mol mol-1) |
| 1 | 1.0 |
| 0.4048 | 0.6151 |
| 0.3685 | 0.5706 |
| 0.3255 | 0.5054 |
| 0.2899 | 0.4527 |
| 0.2385 | 0.375 |
| 0.1981 | 0.308 |
| 0.1677 | 0.2614 |
| 0.1135 | 0.174 |
| 0.0597 | 0.0895 |
| 0.0313 | 0.046 |
| 0.9514 | 0.9891 |
| 0 | 0.0 |
| 0.9123 | 0.9789 |
| 0.8244 | 0.9497 |
| 0.7381 | 0.9111 |
| 0.6495 | 0.8575 |
| 0.5562 | 0.7831 |
| 0.5093 | 0.7371 |
| 0.4499 | 0.6709 |
14204; 1,1-dimethylethyl ethanoate + chlorobenzene; 01345:01685