Operational condition: Temperature, K = 293.94 (Liquid)
| Mole fraction of Propane (2) - Liquid | Mole fraction of Propane (2) - Gas |
|---|---|
| 0.0142 | 0.3026 |
| 0.0417 | 0.5533 |
| 0.0508 | 0.5996 |
| 0.1290 | 0.7815 |
| 0.1372 | 0.7909 |
| 0.2092 | 0.8467 |
| 0.2464 | 0.8646 |
| 0.2476 | 0.8651 |
| 0.3336 | 0.8935 |
| 0.3849 | 0.9055 |
| 0.4368 | 0.9156 |
| 0.4895 | 0.9245 |
| 0.4917 | 0.9248 |
| 0.5408 | 0.9321 |
| 0.5895 | 0.9388 |
| 0.6374 | 0.9452 |
| 0.6879 | 0.9517 |
| 0.7364 | 0.9580 |
| 0.7866 | 0.9647 |
| 0.8397 | 0.9722 |
| 0.8920 | 0.9802 |
| 0.9441 | 0.9891 |
| 0.9658 | 0.9931 |
| 0.9868 | 0.9973 |
Operational condition: Temperature, K = 312.85 (Liquid)
| Mole fraction of Propane (2) - Liquid | Mole fraction of Propane (2) - Gas |
|---|---|
| 0.0076 | 0.1421 |
| 0.0267 | 0.3647 |
| 0.0431 | 0.4774 |
| 0.0856 | 0.6374 |
| 0.1309 | 0.7230 |
| 0.1755 | 0.7735 |
| 0.2231 | 0.8093 |
| 0.2725 | 0.8358 |
| 0.3267 | 0.8576 |
| 0.3785 | 0.8740 |
| 0.4302 | 0.8875 |
| 0.4825 | 0.8993 |
| 0.4873 | 0.9003 |
| 0.5353 | 0.9099 |
| 0.5834 | 0.9189 |
| 0.6321 | 0.9275 |
| 0.6828 | 0.9362 |
| 0.7322 | 0.9446 |
| 0.7844 | 0.9538 |
| 0.8362 | 0.9634 |
| 0.8888 | 0.9738 |
| 0.9438 | 0.9859 |
| 0.9664 | 0.9913 |
| 0.9927 | 0.9981 |
Operational condition: Temperature, K = 293.94 (Liquid)
| Mole fraction of Propane (2) - Liquid | Mole fraction of Propane (2) - Gas |
|---|---|
| 0.0142 | 0.3026 |
| 0.0417 | 0.5533 |
| 0.0508 | 0.5996 |
| 0.1290 | 0.7815 |
| 0.1372 | 0.7909 |
| 0.2092 | 0.8467 |
| 0.2464 | 0.8646 |
| 0.2476 | 0.8651 |
| 0.3336 | 0.8935 |
| 0.3849 | 0.9055 |
| 0.4368 | 0.9156 |
| 0.4895 | 0.9245 |
| 0.4917 | 0.9248 |
| 0.5408 | 0.9321 |
| 0.5895 | 0.9388 |
| 0.6374 | 0.9452 |
| 0.6879 | 0.9517 |
| 0.7364 | 0.9580 |
| 0.7866 | 0.9647 |
| 0.8397 | 0.9722 |
| 0.8920 | 0.9802 |
| 0.9441 | 0.9891 |
| 0.9658 | 0.9931 |
| 0.9868 | 0.9973 |
Operational condition: Temperature, K = 312.85 (Liquid)
| Mole fraction of Propane (2) - Liquid | Mole fraction of Propane (2) - Gas |
|---|---|
| 0.0076 | 0.1421 |
| 0.0267 | 0.3647 |
| 0.0431 | 0.4774 |
| 0.0856 | 0.6374 |
| 0.1309 | 0.7230 |
| 0.1755 | 0.7735 |
| 0.2231 | 0.8093 |
| 0.2725 | 0.8358 |
| 0.3267 | 0.8576 |
| 0.3785 | 0.8740 |
| 0.4302 | 0.8875 |
| 0.4825 | 0.8993 |
| 0.4873 | 0.9003 |
| 0.5353 | 0.9099 |
| 0.5834 | 0.9189 |
| 0.6321 | 0.9275 |
| 0.6828 | 0.9362 |
| 0.7322 | 0.9446 |
| 0.7844 | 0.9538 |
| 0.8362 | 0.9634 |
| 0.8888 | 0.9738 |
| 0.9438 | 0.9859 |
| 0.9664 | 0.9913 |
| 0.9927 | 0.9981 |
Operational condition: Temperature, K = 312.85 (Liquid)
| Mole fraction of Propane (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 108.80 |
| 0.0076 | 126.60 |
| 0.0267 | 169.60 |
| 0.0431 | 205.50 |
| 0.0856 | 290.10 |
| 0.1309 | 372.00 |
| 0.1755 | 444.90 |
| 0.2231 | 516.10 |
| 0.2725 | 583.20 |
| 0.3267 | 650.80 |
| 0.3785 | 710.00 |
| 0.4302 | 765.50 |
| 0.4825 | 818.50 |
| 0.4873 | 825.70 |
| 0.5353 | 872.20 |
| 0.5834 | 917.60 |
| 0.6321 | 963.20 |
| 0.6828 | 1010.40 |
| 0.7322 | 1057.70 |
| 0.7844 | 1109.20 |
| 0.8362 | 1162.60 |
| 0.8888 | 1220.50 |
| 0.9438 | 1285.90 |
| 0.9664 | 1314.10 |
| 0.9927 | 1349.20 |
| 1.0000 | 1358.50 |
Operational condition: Temperature, K = 312.85 (Liquid)
| Mole fraction of Propane (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 108.80 |
| 0.0076 | 126.60 |
| 0.0267 | 169.60 |
| 0.0431 | 205.50 |
| 0.0856 | 290.10 |
| 0.1309 | 372.00 |
| 0.1755 | 444.90 |
| 0.2231 | 516.10 |
| 0.2725 | 583.20 |
| 0.3267 | 650.80 |
| 0.3785 | 710.00 |
| 0.4302 | 765.50 |
| 0.4825 | 818.50 |
| 0.4873 | 825.70 |
| 0.5353 | 872.20 |
| 0.5834 | 917.60 |
| 0.6321 | 963.20 |
| 0.6828 | 1010.40 |
| 0.7322 | 1057.70 |
| 0.7844 | 1109.20 |
| 0.8362 | 1162.60 |
| 0.8888 | 1220.50 |
| 0.9438 | 1285.90 |
| 0.9664 | 1314.10 |
| 0.9927 | 1349.20 |
| 1.0000 | 1358.50 |
Operational condition: Temperature, K = 293.94 (Liquid)
| Mole fraction of Propane (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
|---|---|
| 0.0000 | 55.40 |
| 0.0142 | 79.30 |
| 0.0417 | 121.50 |
| 0.0508 | 135.10 |
| 0.1290 | 237.20 |
| 0.1372 | 246.70 |
| 0.2092 | 322.90 |
| 0.2464 | 357.50 |
| 0.2476 | 358.50 |
| 0.3336 | 428.80 |
| 0.3849 | 465.80 |
| 0.4368 | 500.30 |
| 0.4895 | 533.20 |
| 0.4917 | 534.90 |
| 0.5408 | 564.30 |
| 0.5895 | 592.60 |
| 0.6374 | 619.90 |
| 0.6879 | 648.60 |
| 0.7364 | 676.60 |
| 0.7866 | 706.50 |
| 0.8397 | 739.70 |
| 0.8920 | 774.80 |
| 0.9441 | 812.40 |
| 0.9658 | 829.00 |
| 0.9868 | 845.70 |
| 1.0000 | 856.50 |
Operational condition: Temperature, K = 293.94 (Liquid)
| Mole fraction of Propane (2) - Liquid | Vapor or sublimation pressure, kPa - Gas |
|---|---|
| 0.0000 | 55.40 |
| 0.0142 | 79.30 |
| 0.0417 | 121.50 |
| 0.0508 | 135.10 |
| 0.1290 | 237.20 |
| 0.1372 | 246.70 |
| 0.2092 | 322.90 |
| 0.2464 | 357.50 |
| 0.2476 | 358.50 |
| 0.3336 | 428.80 |
| 0.3849 | 465.80 |
| 0.4368 | 500.30 |
| 0.4895 | 533.20 |
| 0.4917 | 534.90 |
| 0.5408 | 564.30 |
| 0.5895 | 592.60 |
| 0.6374 | 619.90 |
| 0.6879 | 648.60 |
| 0.7364 | 676.60 |
| 0.7866 | 706.50 |
| 0.8397 | 739.70 |
| 0.8920 | 774.80 |
| 0.9441 | 812.40 |
| 0.9658 | 829.00 |
| 0.9868 | 845.70 |
| 1.0000 | 856.50 |