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) |
| 307.43 | 3.99 |
| 355.75 | 32.86 |
| 359.66 | 37.89 |
| 363.22 | 42.93 |
| 366.39 | 47.84 |
| 368.76 | 51.85 |
| 371.61 | 57.06 |
| 374.55 | 62.82 |
| 376.93 | 67.79 |
| 379.15 | 72.78 |
| 381.03 | 77.2 |
| 315.56 | 5.99 |
| 383.63 | 83.72 |
| 385.84 | 89.68 |
| 387.69 | 94.78 |
| 389.16 | 98.95 |
| 389.90 | 100.0 |
| 391.39 | 105.57 |
| 322.93 | 8.48 |
| 328.64 | 10.98 |
| 335.75 | 14.98 |
| 341.55 | 18.96 |
| 342.95 | 20.0 |
| 346.88 | 23.44 |
| 351.45 | 27.95 |
1804; isobutyl acetate; 00317