Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Mole fraction of Ethane, 1,2-dichloro- (2) - Gas |
---|---|
0.0510 | 0.1510 |
0.1100 | 0.3420 |
0.1870 | 0.5010 |
0.2330 | 0.5390 |
0.2670 | 0.5650 |
0.2770 | 0.5870 |
0.3100 | 0.6130 |
0.4530 | 0.7280 |
0.5500 | 0.7880 |
0.5760 | 0.8100 |
0.6860 | 0.8300 |
0.7040 | 0.8530 |
0.7750 | 0.8830 |
0.8300 | 0.9090 |
0.8810 | 0.9310 |
0.9370 | 0.9570 |
0.9920 | 0.9820 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Mole fraction of Ethane, 1,2-dichloro- (2) - Gas |
---|---|
0.0510 | 0.1510 |
0.1100 | 0.3420 |
0.1870 | 0.5010 |
0.2330 | 0.5390 |
0.2670 | 0.5650 |
0.2770 | 0.5870 |
0.3100 | 0.6130 |
0.4530 | 0.7280 |
0.5500 | 0.7880 |
0.5760 | 0.8100 |
0.6860 | 0.8300 |
0.7040 | 0.8530 |
0.7750 | 0.8830 |
0.8300 | 0.9090 |
0.8810 | 0.9310 |
0.9370 | 0.9570 |
0.9920 | 0.9820 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0510 | 389.65 |
0.1100 | 379.35 |
0.1870 | 371.55 |
0.2330 | 370.15 |
0.2670 | 368.65 |
0.2770 | 366.85 |
0.3100 | 366.15 |
0.4530 | 363.35 |
0.5500 | 361.15 |
0.5760 | 360.55 |
0.6860 | 359.55 |
0.7040 | 358.75 |
0.7750 | 358.15 |
0.8300 | 357.75 |
0.8810 | 357.35 |
0.9370 | 356.95 |
0.9920 | 356.65 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0510 | 389.65 |
0.1100 | 379.35 |
0.1870 | 371.55 |
0.2330 | 370.15 |
0.2670 | 368.65 |
0.2770 | 366.85 |
0.3100 | 366.15 |
0.4530 | 363.35 |
0.5500 | 361.15 |
0.5760 | 360.55 |
0.6860 | 359.55 |
0.7040 | 358.75 |
0.7750 | 358.15 |
0.8300 | 357.75 |
0.8810 | 357.35 |
0.9370 | 356.95 |
0.9920 | 356.65 |