Operational condition: Pressure, kPa = 94.13 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of 1-Butanol (1) - Liquid | y1[mol/mol] of 1-Butanol (1) - Vapour |
| 388.95 | 0.0000 | 0.0000 |
| 388.85 | 0.0180 | 0.0090 |
| 389.45 | 0.0600 | 0.0390 |
| 390.05 | 0.1050 | 0.0780 |
| 390.15 | 0.1170 | 0.0950 |
| 390.85 | 0.1610 | 0.1240 |
| 391.75 | 0.2340 | 0.1880 |
| 392.05 | 0.2540 | 0.2090 |
| 392.65 | 0.3040 | 0.2590 |
| 392.95 | 0.3550 | 0.3110 |
| 393.45 | 0.4590 | 0.4390 |
| 393.45 | 0.4850 | 0.4750 |
| 393.45 | 0.5450 | 0.5550 |
| 393.25 | 0.5900 | 0.6140 |
| 392.95 | 0.6570 | 0.7020 |
| 392.55 | 0.7310 | 0.7900 |
| 391.35 | 0.8240 | 0.8890 |
| 390.35 | 0.9200 | 0.9600 |
| 389.75 | 0.9540 | 0.9800 |
| 388.95 | 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.33 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of 1-Butanol (1) - Liquid | y1[mol/mol] of 1-Butanol (1) - Vapour |
| 391.25 | 0.0280 | 0.0140 |
| 391.85 | 0.0910 | 0.0600 |
| 392.55 | 0.1540 | 0.1160 |
| 392.35 | 0.1700 | 0.1260 |
| 393.05 | 0.2270 | 0.1780 |
| 393.95 | 0.3150 | 0.2580 |
| 394.25 | 0.3370 | 0.2830 |
| 394.85 | 0.3920 | 0.3400 |
| 395.25 | 0.4450 | 0.3960 |
| 395.75 | 0.5440 | 0.5240 |
| 395.75 | 0.5670 | 0.5570 |
| 395.75 | 0.5960 | 0.5960 |
| 395.75 | 0.6190 | 0.6290 |
| 395.45 | 0.6570 | 0.6790 |
| 395.25 | 0.7110 | 0.7520 |
| 394.75 | 0.7700 | 0.8230 |
| 393.65 | 0.8440 | 0.9020 |
| 392.55 | 0.9240 | 0.9620 |
| 391.95 | 0.9550 | 0.9810 |
Operational condition: Temperature, K = 298.15 (VLE)
| P [kPa] - VLE | x1[mol/mol] of 1-Butanol (1) - Liquid |
|---|---|
| 2.067 | 0.0000 |
| 1.633 | 0.1030 |
| 1.393 | 0.2020 |
| 1.223 | 0.3000 |
| 1.093 | 0.4050 |
| 1.009 | 0.5000 |
| 0.9690 | 0.6000 |
| 0.9530 | 0.7000 |
| 1.004 | 0.7920 |
| 1.095 | 0.8920 |
| 1.137 | 0.9240 |
| 1.267 | 1.0000 |