Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa Montón, J.; Muñoz, R.; Burguet, M.; Torre, J.d.l.; Fluid Phase Equilibria 2005, 227, 19-25
- Journal: Fluid Phase Equilibria
- Sample Quantity(ies): Vapor pressure
- Methodology: EBULLIO:UFactor:8
- Phase(s): Liquid
- Substances:
Data
| T (K) | P (kPa) |
| 300.93 | 6.93 |
| 331.45 | 35.33 |
| 334.15 | 40.21 |
| 336.65 | 45.17 |
| 338.85 | 49.98 |
| 341.05 | 55.12 |
| 342.95 | 59.92 |
| 344.85 | 65.12 |
| 346.45 | 69.66 |
| 348.15 | 74.84 |
| 349.75 | 79.98 |
| 304.86 | 8.76 |
| 351.25 | 85.09 |
| 352.65 | 90.08 |
| 353.95 | 94.97 |
| 355.15 | 99.63 |
| 355.59 | 100.0 |
| 355.65 | 101.33 |
| 356.55 | 105.13 |
| 357.65 | 109.82 |
| 358.85 | 115.07 |
| 359.83 | 119.91 |
| 309.12 | 11.16 |
| 313.25 | 14.03 |
| 315.48 | 15.81 |
| 320.17 | 20.0 |
| 320.75 | 20.63 |
| 325.05 | 25.76 |
| 328.35 | 30.37 |
1086; tert-butanol; 00347