Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Acetaldehyde (1) - Liquid | Mole fraction of Acetaldehyde (1) - Gas |
---|---|
1.0000 | 1.0000 |
0.9642 | 0.9967 |
0.9213 | 0.9922 |
0.8757 | 0.9859 |
0.7915 | 0.9742 |
0.6733 | 0.9514 |
0.6219 | 0.9393 |
0.5147 | 0.9007 |
0.4107 | 0.8392 |
0.3878 | 0.8178 |
0.3072 | 0.7560 |
0.2754 | 0.7122 |
0.2236 | 0.6532 |
0.1737 | 0.5686 |
0.1501 | 0.5071 |
0.1252 | 0.4447 |
0.0926 | 0.3577 |
0.0433 | 0.1884 |
0.0098 | 0.0467 |
0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Acetaldehyde (1) - Liquid | Mole fraction of Acetaldehyde (1) - Gas |
---|---|
1.0000 | 1.0000 |
0.9642 | 0.9967 |
0.9213 | 0.9922 |
0.8757 | 0.9859 |
0.7915 | 0.9742 |
0.6733 | 0.9514 |
0.6219 | 0.9393 |
0.5147 | 0.9007 |
0.4107 | 0.8392 |
0.3878 | 0.8178 |
0.3072 | 0.7560 |
0.2754 | 0.7122 |
0.2236 | 0.6532 |
0.1737 | 0.5686 |
0.1501 | 0.5071 |
0.1252 | 0.4447 |
0.0926 | 0.3577 |
0.0433 | 0.1884 |
0.0098 | 0.0467 |
0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Acetaldehyde (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
1.0000 | 293.84 |
0.9642 | 294.94 |
0.9213 | 295.83 |
0.8757 | 297.12 |
0.7915 | 299.42 |
0.6733 | 303.41 |
0.6219 | 305.91 |
0.5147 | 311.12 |
0.4107 | 316.53 |
0.3878 | 318.43 |
0.3072 | 322.95 |
0.2754 | 324.95 |
0.2236 | 329.37 |
0.1737 | 332.98 |
0.1501 | 335.49 |
0.1252 | 337.50 |
0.0926 | 340.61 |
0.0433 | 345.43 |
0.0098 | 349.15 |
0.0000 | 350.20 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Acetaldehyde (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
1.0000 | 293.84 |
0.9642 | 294.94 |
0.9213 | 295.83 |
0.8757 | 297.12 |
0.7915 | 299.42 |
0.6733 | 303.41 |
0.6219 | 305.91 |
0.5147 | 311.12 |
0.4107 | 316.53 |
0.3878 | 318.43 |
0.3072 | 322.95 |
0.2754 | 324.95 |
0.2236 | 329.37 |
0.1737 | 332.98 |
0.1501 | 335.49 |
0.1252 | 337.50 |
0.0926 | 340.61 |
0.0433 | 345.43 |
0.0098 | 349.15 |
0.0000 | 350.20 |