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 |