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): Boiling point at pressure
- Methodology: Ebulliometric method (Recirculating still)
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | Tbp (K) |
| 1 | 371.05 |
| 0.4048 | 391.86 |
| 0.3685 | 393.12 |
| 0.3255 | 394.8 |
| 0.2899 | 396.03 |
| 0.2385 | 397.96 |
| 0.1981 | 399.75 |
| 0.1677 | 400.62 |
| 0.1135 | 402.06 |
| 0.0597 | 403.67 |
| 0.0313 | 404.31 |
| 0.9514 | 371.29 |
| 0 | 404.8 |
| 0.9123 | 372.13 |
| 0.8244 | 374.51 |
| 0.7381 | 377.43 |
| 0.6495 | 380.32 |
| 0.5562 | 384.7 |
| 0.5093 | 387.45 |
| 0.4499 | 389.61 |
14204; 1,1-dimethylethyl ethanoate + chlorobenzene; 01345:01685