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 | 355.59 |
| 0.4263 | 363.5 |
| 0.3671 | 365.15 |
| 0.2707 | 368.55 |
| 0.1781 | 373.85 |
| 0.1128 | 379.95 |
| 0.0715 | 385.45 |
| 0.0460 | 390.45 |
| 0.0309 | 395.15 |
| 0.0207 | 397.85 |
| 0.0073 | 402.05 |
| 0.8859 | 356.5 |
| 0 | 404.8 |
| 0.8536 | 356.95 |
| 0.8156 | 357.15 |
| 0.7455 | 358.05 |
| 0.7101 | 358.45 |
| 0.6223 | 359.75 |
| 0.5364 | 361.25 |
| 0.4620 | 362.65 |
14203; 2-methylpropan-2-ol + chlorobenzene; 00347:01685