Isobaric vapor-liquid equilibrium data for the binary system methyl acetate + isopropyl acetate and the quaternary system methyl acetate + methanol + isopropanol + isopropyl acetate at 101.3 kPa Xiao, L.; Wang, Q.l.; Wang, H.x.; Qiu, T.; Fluid Phase Equilibria 2013, 344, 79-83
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Boiling point at pressure
- Methodology: Ebulliometric method (Recirculating still)
- Phase(s): Gas' Liquid
- Substances:
Data
| x (mol mol-1) | Tbp (K) |
| 0 | 361.65 |
| 0.390 | 344.75 |
| 0.442 | 343.35 |
| 0.482 | 341.95 |
| 0.551 | 339.95 |
| 0.596 | 338.95 |
| 0.686 | 336.55 |
| 0.748 | 335.15 |
| 0.777 | 334.35 |
| 0.806 | 333.75 |
| 1 | 330.95 |
| 0.040 | 358.75 |
| 0.065 | 357.15 |
| 0.094 | 355.75 |
| 0.111 | 354.95 |
| 0.174 | 352.35 |
| 0.234 | 349.95 |
| 0.275 | 348.15 |
| 0.327 | 346.85 |
32615; methyl ethanoate + 1-methylethyl ethanoate; 00022:00200