Datasets
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Mole fraction (4)
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Tboil - Boiling temperature at pressure P, K (2)
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Azeotropic temperature, K (2)
Mole fraction of Octane (1)
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Octane (1) - Liquid |
Mole fraction of Octane (1) - Gas |
1.0000 |
1.0000 |
0.9830 |
0.9840 |
0.9820 |
0.9830 |
0.9800 |
0.9820 |
0.9780 |
0.9790 |
0.9750 |
0.9740 |
0.9600 |
0.9670 |
0.9250 |
0.9250 |
0.9230 |
0.9340 |
0.7950 |
0.8870 |
0.7690 |
0.8520 |
0.6800 |
0.8300 |
0.6630 |
0.7910 |
0.5710 |
0.7810 |
0.5200 |
0.7270 |
0.4060 |
0.6810 |
0.3690 |
0.6790 |
0.3650 |
0.6650 |
0.3010 |
0.6300 |
0.2840 |
0.6320 |
0.2580 |
0.6130 |
0.2010 |
0.5140 |
0.1920 |
0.5320 |
0.1660 |
0.4830 |
0.1460 |
0.4470 |
0.1310 |
0.4120 |
0.1280 |
0.4130 |
0.1120 |
0.3780 |
0.0710 |
0.2810 |
0.0630 |
0.2620 |
0.0560 |
0.2470 |
0.0380 |
0.1780 |
0.0370 |
0.1710 |
0.0000 |
0.0000 |
Azeotropic composition: mole fraction of Octane (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Octane (1) - Liquid |
40.00 |
0.9800 |
Mole fraction of Octane (1)
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Octane (1) - Liquid |
Mole fraction of Octane (1) - Gas |
1.0000 |
1.0000 |
0.9830 |
0.9840 |
0.9820 |
0.9830 |
0.9800 |
0.9820 |
0.9780 |
0.9790 |
0.9750 |
0.9740 |
0.9600 |
0.9670 |
0.9250 |
0.9250 |
0.9230 |
0.9340 |
0.7950 |
0.8870 |
0.7690 |
0.8520 |
0.6800 |
0.8300 |
0.6630 |
0.7910 |
0.5710 |
0.7810 |
0.5200 |
0.7270 |
0.4060 |
0.6810 |
0.3690 |
0.6790 |
0.3650 |
0.6650 |
0.3010 |
0.6300 |
0.2840 |
0.6320 |
0.2580 |
0.6130 |
0.2010 |
0.5140 |
0.1920 |
0.5320 |
0.1660 |
0.4830 |
0.1460 |
0.4470 |
0.1310 |
0.4120 |
0.1280 |
0.4130 |
0.1120 |
0.3780 |
0.0710 |
0.2810 |
0.0630 |
0.2620 |
0.0560 |
0.2470 |
0.0380 |
0.1780 |
0.0370 |
0.1710 |
0.0000 |
0.0000 |
Azeotropic composition: mole fraction of Octane (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Octane (1) - Liquid |
40.00 |
0.9800 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Octane (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
1.0000 |
368.32 |
0.9830 |
368.47 |
0.9820 |
368.31 |
0.9800 |
368.27 |
0.9780 |
368.31 |
0.9750 |
368.50 |
0.9600 |
368.29 |
0.9250 |
368.42 |
0.9230 |
368.73 |
0.7950 |
368.97 |
0.7690 |
369.70 |
0.6800 |
369.97 |
0.6630 |
370.52 |
0.5710 |
371.42 |
0.5200 |
372.27 |
0.4060 |
374.02 |
0.3690 |
374.89 |
0.3650 |
374.75 |
0.3010 |
376.17 |
0.2840 |
376.79 |
0.2580 |
377.40 |
0.2010 |
379.79 |
0.1920 |
379.92 |
0.1660 |
381.05 |
0.1460 |
382.05 |
0.1310 |
382.61 |
0.1280 |
382.32 |
0.1120 |
383.43 |
0.0710 |
385.83 |
0.0630 |
386.66 |
0.0560 |
386.79 |
0.0380 |
388.75 |
0.0370 |
388.62 |
0.0000 |
392.54 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Octane (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
1.0000 |
368.32 |
0.9830 |
368.47 |
0.9820 |
368.31 |
0.9800 |
368.27 |
0.9780 |
368.31 |
0.9750 |
368.50 |
0.9600 |
368.29 |
0.9250 |
368.42 |
0.9230 |
368.73 |
0.7950 |
368.97 |
0.7690 |
369.70 |
0.6800 |
369.97 |
0.6630 |
370.52 |
0.5710 |
371.42 |
0.5200 |
372.27 |
0.4060 |
374.02 |
0.3690 |
374.89 |
0.3650 |
374.75 |
0.3010 |
376.17 |
0.2840 |
376.79 |
0.2580 |
377.40 |
0.2010 |
379.79 |
0.1920 |
379.92 |
0.1660 |
381.05 |
0.1460 |
382.05 |
0.1310 |
382.61 |
0.1280 |
382.32 |
0.1120 |
383.43 |
0.0710 |
385.83 |
0.0630 |
386.66 |
0.0560 |
386.79 |
0.0380 |
388.75 |
0.0370 |
388.62 |
0.0000 |
392.54 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
40.00 |
368.30 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
40.00 |
368.30 |
Sources