Datasets
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Mole fraction (2)
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Binary diffusion coefficient, m2/s (4)
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Vapor Liquid Equilibrium at Constant Pressure (2)
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Vapor Liquid Equilibrium at Constant Temperature
Mole fraction of Acetone (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Acetone (2) - Liquid |
Mole fraction of Acetone (2) - Gas |
| 283.20 |
0.0120 |
0.6450 |
| 283.20 |
0.0370 |
0.8430 |
| 283.20 |
0.0870 |
0.9210 |
| 283.20 |
0.2910 |
0.9690 |
| 283.20 |
0.5520 |
0.9860 |
| 283.20 |
0.8260 |
0.9970 |
| 295.20 |
0.0120 |
0.4990 |
| 295.20 |
0.0370 |
0.7650 |
| 295.20 |
0.0870 |
0.8680 |
| 295.20 |
0.2910 |
0.9480 |
| 295.20 |
0.5520 |
0.9760 |
| 295.20 |
0.8260 |
0.9910 |
| 308.20 |
0.0120 |
0.4020 |
| 308.20 |
0.0370 |
0.6660 |
| 308.20 |
0.0870 |
0.8180 |
| 308.20 |
0.2910 |
0.9240 |
| 308.20 |
0.5520 |
0.9740 |
| 308.20 |
0.8260 |
0.9880 |
| 324.20 |
0.0120 |
0.2600 |
| 324.20 |
0.0370 |
0.5220 |
| 324.20 |
0.0870 |
0.7070 |
| 324.20 |
0.2910 |
0.8920 |
| 324.20 |
0.5520 |
0.9500 |
| 324.20 |
0.8260 |
0.9850 |
Mole fraction of Acetone (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Acetone (2) - Liquid |
Mole fraction of Acetone (2) - Gas |
| 283.20 |
0.0120 |
0.6450 |
| 283.20 |
0.0370 |
0.8430 |
| 283.20 |
0.0870 |
0.9210 |
| 283.20 |
0.2910 |
0.9690 |
| 283.20 |
0.5520 |
0.9860 |
| 283.20 |
0.8260 |
0.9970 |
| 295.20 |
0.0120 |
0.4990 |
| 295.20 |
0.0370 |
0.7650 |
| 295.20 |
0.0870 |
0.8680 |
| 295.20 |
0.2910 |
0.9480 |
| 295.20 |
0.5520 |
0.9760 |
| 295.20 |
0.8260 |
0.9910 |
| 308.20 |
0.0120 |
0.4020 |
| 308.20 |
0.0370 |
0.6660 |
| 308.20 |
0.0870 |
0.8180 |
| 308.20 |
0.2910 |
0.9240 |
| 308.20 |
0.5520 |
0.9740 |
| 308.20 |
0.8260 |
0.9880 |
| 324.20 |
0.0120 |
0.2600 |
| 324.20 |
0.0370 |
0.5220 |
| 324.20 |
0.0870 |
0.7070 |
| 324.20 |
0.2910 |
0.8920 |
| 324.20 |
0.5520 |
0.9500 |
| 324.20 |
0.8260 |
0.9850 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
| 0.0125 |
0.0000 |
| 0.1000 |
0.0000 |
| 0.2000 |
0.0000 |
| 0.3000 |
0.0000 |
| 0.4000 |
0.0000 |
| 0.5000 |
0.0000 |
| 0.6000 |
0.0000 |
| 0.7000 |
0.0000 |
| 0.8000 |
0.0000 |
| 0.9000 |
0.0000 |
| 0.9915 |
0.0000 |
| 0.9925 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
| 0.0125 |
0.0000 |
| 0.1000 |
0.0000 |
| 0.2000 |
0.0000 |
| 0.3000 |
0.0000 |
| 0.4000 |
0.0000 |
| 0.5000 |
0.0000 |
| 0.6000 |
0.0000 |
| 0.7000 |
0.0000 |
| 0.8000 |
0.0000 |
| 0.9000 |
0.0000 |
| 0.9915 |
0.0000 |
| 0.9925 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
| 0.0125 |
0.0000 |
| 0.1000 |
0.0000 |
| 0.2000 |
0.0000 |
| 0.3000 |
0.0000 |
| 0.4000 |
0.0000 |
| 0.5000 |
0.0000 |
| 0.6000 |
0.0000 |
| 0.7000 |
0.0000 |
| 0.8000 |
0.0000 |
| 0.9000 |
0.0000 |
| 0.9915 |
0.0000 |
| 0.9925 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
| 0.0125 |
0.0000 |
| 0.1000 |
0.0000 |
| 0.2000 |
0.0000 |
| 0.3000 |
0.0000 |
| 0.4000 |
0.0000 |
| 0.5000 |
0.0000 |
| 0.6000 |
0.0000 |
| 0.7000 |
0.0000 |
| 0.8000 |
0.0000 |
| 0.9000 |
0.0000 |
| 0.9915 |
0.0000 |
| 0.9925 |
0.0000 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
99.46 (VLE)
| Fixed |
Measured |
| T [K] - VLE |
x1[mol/mol] of Acetone (2) - Liquid |
y1[mol/mol] of Acetone (2) - Vapour |
| 388.15 |
0.0100 |
0.1050 |
| 385.15 |
0.0250 |
0.2250 |
| 380.25 |
0.0500 |
0.4050 |
| 376.95 |
0.0700 |
0.4720 |
| 364.85 |
0.1540 |
0.6980 |
| 360.05 |
0.1980 |
0.7500 |
| 358.55 |
0.2150 |
0.7730 |
| 354.85 |
0.2650 |
0.8090 |
| 351.95 |
0.3120 |
0.8370 |
| 341.75 |
0.5350 |
0.9300 |
| 339.35 |
0.6070 |
0.9430 |
| 337.65 |
0.6590 |
0.9510 |
| 334.75 |
0.7630 |
0.9720 |
| 333.15 |
0.8190 |
0.9780 |
| 331.25 |
0.8970 |
0.9880 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
| T [K] - VLE |
x1[mol/mol] of Acetone (2) - Liquid |
| 374.5 |
0.1240 |
| 361.64 |
0.2420 |
| 353.15 |
0.3540 |
| 347.36 |
0.4600 |
| 343.18 |
0.5610 |
| 339.49 |
0.6570 |
| 336.47 |
0.7490 |
| 334.05 |
0.8360 |
| 331.83 |
0.9200 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
298.15 (VLE)
| Fixed |
Measured |
| P [kPa] - VLE |
x1[mol/mol] of Acetone (2) - Liquid |
y1[mol/mol] of Acetone (2) - Vapour |
| 9.733 |
0.1600 |
0.9140 |
| 15.465 |
0.4350 |
0.9610 |
| 19.865 |
0.6500 |
0.9750 |
| 21.865 |
0.7900 |
0.9840 |
| 24.265 |
0.9050 |
0.9890 |
| 25.331 |
0.9510 |
0.9910 |
Sources