Datasets
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Azeotropic composition: mole fraction (4)
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Tboil - Boiling temperature at pressure P, K (2)
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Azeotropic temperature, K (2)
Azeotropic composition: mole fraction of Nonane (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Nonane (1) - Liquid |
40.00 |
0.5300 |
Mole fraction of Nonane (1)
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Nonane (1) - Liquid |
Mole fraction of Nonane (1) - Gas |
1.0000 |
1.0000 |
0.9670 |
0.9340 |
0.9560 |
0.8780 |
0.9260 |
0.8590 |
0.9070 |
0.8380 |
0.8590 |
0.7640 |
0.8350 |
0.7320 |
0.8280 |
0.7560 |
0.7550 |
0.6690 |
0.7510 |
0.6760 |
0.6850 |
0.6190 |
0.5950 |
0.5780 |
0.4390 |
0.4730 |
0.4050 |
0.4540 |
0.3760 |
0.4340 |
0.3210 |
0.4030 |
0.2830 |
0.3720 |
0.2750 |
0.3700 |
0.2560 |
0.3610 |
0.2390 |
0.3660 |
0.1860 |
0.2940 |
0.1760 |
0.2730 |
0.1400 |
0.2290 |
0.1210 |
0.2110 |
0.1060 |
0.1880 |
0.0900 |
0.1690 |
0.0790 |
0.1470 |
0.0590 |
0.1170 |
0.0550 |
0.1100 |
0.0000 |
0.0000 |
Azeotropic composition: mole fraction of Nonane (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Nonane (1) - Liquid |
40.00 |
0.5300 |
Mole fraction of Nonane (1)
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Nonane (1) - Liquid |
Mole fraction of Nonane (1) - Gas |
1.0000 |
1.0000 |
0.9670 |
0.9340 |
0.9560 |
0.8780 |
0.9260 |
0.8590 |
0.9070 |
0.8380 |
0.8590 |
0.7640 |
0.8350 |
0.7320 |
0.8280 |
0.7560 |
0.7550 |
0.6690 |
0.7510 |
0.6760 |
0.6850 |
0.6190 |
0.5950 |
0.5780 |
0.4390 |
0.4730 |
0.4050 |
0.4540 |
0.3760 |
0.4340 |
0.3210 |
0.4030 |
0.2830 |
0.3720 |
0.2750 |
0.3700 |
0.2560 |
0.3610 |
0.2390 |
0.3660 |
0.1860 |
0.2940 |
0.1760 |
0.2730 |
0.1400 |
0.2290 |
0.1210 |
0.2110 |
0.1060 |
0.1880 |
0.0900 |
0.1690 |
0.0790 |
0.1470 |
0.0590 |
0.1170 |
0.0550 |
0.1100 |
0.0000 |
0.0000 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Nonane (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
1.0000 |
391.78 |
0.9670 |
390.96 |
0.9560 |
390.46 |
0.9260 |
389.79 |
0.9070 |
389.65 |
0.8590 |
388.73 |
0.8350 |
388.33 |
0.8280 |
388.45 |
0.7550 |
387.70 |
0.7510 |
387.61 |
0.6850 |
387.20 |
0.5950 |
386.82 |
0.4390 |
386.77 |
0.4050 |
386.80 |
0.3760 |
386.89 |
0.3210 |
387.10 |
0.2830 |
387.29 |
0.2750 |
387.40 |
0.2560 |
387.79 |
0.2390 |
387.72 |
0.1860 |
388.15 |
0.1760 |
388.33 |
0.1400 |
388.78 |
0.1210 |
389.10 |
0.1060 |
389.40 |
0.0900 |
389.72 |
0.0790 |
389.76 |
0.0590 |
390.56 |
0.0550 |
390.62 |
0.0000 |
392.54 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Nonane (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
1.0000 |
391.78 |
0.9670 |
390.96 |
0.9560 |
390.46 |
0.9260 |
389.79 |
0.9070 |
389.65 |
0.8590 |
388.73 |
0.8350 |
388.33 |
0.8280 |
388.45 |
0.7550 |
387.70 |
0.7510 |
387.61 |
0.6850 |
387.20 |
0.5950 |
386.82 |
0.4390 |
386.77 |
0.4050 |
386.80 |
0.3760 |
386.89 |
0.3210 |
387.10 |
0.2830 |
387.29 |
0.2750 |
387.40 |
0.2560 |
387.79 |
0.2390 |
387.72 |
0.1860 |
388.15 |
0.1760 |
388.33 |
0.1400 |
388.78 |
0.1210 |
389.10 |
0.1060 |
389.40 |
0.0900 |
389.72 |
0.0790 |
389.76 |
0.0590 |
390.56 |
0.0550 |
390.62 |
0.0000 |
392.54 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
40.00 |
386.70 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
40.00 |
386.70 |
Sources