Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid | Mole fraction of Ethane, 1,2-dimethoxy- (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0660 | 0.1540 |
0.1460 | 0.2930 |
0.2230 | 0.4080 |
0.2840 | 0.4870 |
0.3470 | 0.5600 |
0.3940 | 0.6060 |
0.4390 | 0.6500 |
0.4900 | 0.6920 |
0.5090 | 0.7070 |
0.5380 | 0.7270 |
0.5710 | 0.7550 |
0.6460 | 0.8080 |
0.7150 | 0.8520 |
0.7830 | 0.8910 |
0.8500 | 0.9250 |
0.9110 | 0.9550 |
0.9720 | 0.9860 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid | Mole fraction of Ethane, 1,2-dimethoxy- (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0660 | 0.1540 |
0.1460 | 0.2930 |
0.2230 | 0.4080 |
0.2840 | 0.4870 |
0.3470 | 0.5600 |
0.3940 | 0.6060 |
0.4390 | 0.6500 |
0.4900 | 0.6920 |
0.5090 | 0.7070 |
0.5380 | 0.7270 |
0.5710 | 0.7550 |
0.6460 | 0.8080 |
0.7150 | 0.8520 |
0.7830 | 0.8910 |
0.8500 | 0.9250 |
0.9110 | 0.9550 |
0.9720 | 0.9860 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 385.12 |
0.0660 | 381.76 |
0.1460 | 379.45 |
0.2230 | 377.02 |
0.2840 | 375.28 |
0.3470 | 373.55 |
0.3940 | 372.42 |
0.4390 | 371.13 |
0.4900 | 369.84 |
0.5090 | 368.97 |
0.5380 | 368.73 |
0.5710 | 367.46 |
0.6460 | 365.74 |
0.7150 | 364.15 |
0.7830 | 362.74 |
0.8500 | 361.41 |
0.9110 | 360.48 |
0.9720 | 359.50 |
1.0000 | 357.71 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethane, 1,2-dimethoxy- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 385.12 |
0.0660 | 381.76 |
0.1460 | 379.45 |
0.2230 | 377.02 |
0.2840 | 375.28 |
0.3470 | 373.55 |
0.3940 | 372.42 |
0.4390 | 371.13 |
0.4900 | 369.84 |
0.5090 | 368.97 |
0.5380 | 368.73 |
0.5710 | 367.46 |
0.6460 | 365.74 |
0.7150 | 364.15 |
0.7830 | 362.74 |
0.8500 | 361.41 |
0.9110 | 360.48 |
0.9720 | 359.50 |
1.0000 | 357.71 |