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): Mole fraction
- Methodology: OTHER
- Phase(s): Gas' Liquid
- Substances:
Data
| x (mol mol-1) | x (mol mol-1) |
| 0.0218 | 0.0098 |
| 0.2797 | 0.1231 |
| 0.3246 | 0.1431 |
| 0.3871 | 0.1704 |
| 0.4312 | 0.1939 |
| 0.4661 | 0.2113 |
| 0.5106 | 0.2352 |
| 0.5503 | 0.2602 |
| 0.5856 | 0.2835 |
| 0.6169 | 0.3055 |
| 0.6322 | 0.3165 |
| 0.0454 | 0.0204 |
| 0.6619 | 0.3384 |
| 0.6908 | 0.3632 |
| 0.7301 | 0.3993 |
| 0.7514 | 0.4207 |
| 0.7901 | 0.4666 |
| 0.8195 | 0.5076 |
| 0.8425 | 0.5441 |
| 0.8600 | 0.5739 |
| 0.8784 | 0.6082 |
| 0.8901 | 0.6326 |
| 0.0555 | 0.025 |
| 0.9013 | 0.6579 |
| 0.9105 | 0.68 |
| 0.9204 | 0.7058 |
| 0.9320 | 0.7369 |
| 0.9424 | 0.7685 |
| 0.9510 | 0.7961 |
| 0.9606 | 0.8295 |
| 0.9720 | 0.8731 |
| 0.9780 | 0.8975 |
| 0.9855 | 0.9299 |
| 0.0690 | 0.031 |
| 0.1040 | 0.047 |
| 0.1201 | 0.0541 |
| 0.1628 | 0.0735 |
| 0.1983 | 0.0887 |
| 0.2309 | 0.1032 |
17654; 2-methylpropan-2-ol + ethyl butanoate; 00347:00596