Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing Ortega, J.; Espiau, F.; Postigo, M.; Journal of Chemical & Engineering Data 2003, 48, 916-924
- Journal: Journal of Chemical & Engineering Data
- Sample Quantity(ies): Boiling point at pressure
- Methodology: EBULLIO:UFactor:4
- Phase(s): Liquid
- Substances:
Data
| x (mol mol-1) | Tbp (K) |
| 0.0218 | 355.9 |
| 0.2797 | 360.2 |
| 0.3246 | 361.13 |
| 0.3871 | 362.37 |
| 0.4312 | 363.43 |
| 0.4661 | 364.21 |
| 0.5106 | 365.28 |
| 0.5503 | 366.42 |
| 0.5856 | 367.45 |
| 0.6169 | 368.42 |
| 0.6322 | 368.91 |
| 0.0454 | 356.38 |
| 0.6619 | 369.93 |
| 0.6908 | 371.03 |
| 0.7301 | 372.63 |
| 0.7514 | 373.55 |
| 0.7901 | 375.45 |
| 0.8195 | 377.06 |
| 0.8425 | 378.52 |
| 0.8600 | 379.66 |
| 0.8784 | 380.98 |
| 0.8901 | 381.96 |
| 0.0555 | 356.54 |
| 0.9013 | 382.86 |
| 0.9105 | 383.63 |
| 0.9204 | 384.54 |
| 0.9320 | 385.74 |
| 0.9424 | 386.87 |
| 0.9510 | 387.84 |
| 0.9606 | 388.93 |
| 0.9720 | 390.22 |
| 0.9780 | 391.06 |
| 0.9855 | 392.07 |
| 0.0690 | 356.71 |
| 0.1040 | 357.31 |
| 0.1201 | 357.49 |
| 0.1628 | 358.32 |
| 0.1983 | 358.85 |
| 0.2309 | 359.44 |
17654; 2-methylpropan-2-ol + ethyl butanoate; 00347:00596