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 (2)
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Octane (2) - Liquid |
Mole fraction of Octane (2) - Gas |
1.0000 |
1.0000 |
0.9210 |
0.9330 |
0.8400 |
0.8840 |
0.8360 |
0.8730 |
0.7630 |
0.8410 |
0.6990 |
0.7860 |
0.6650 |
0.7920 |
0.6250 |
0.7470 |
0.6110 |
0.7600 |
0.5690 |
0.7210 |
0.5130 |
0.7140 |
0.4690 |
0.6770 |
0.3530 |
0.5940 |
0.3200 |
0.5890 |
0.3170 |
0.5640 |
0.2850 |
0.5460 |
0.2530 |
0.5090 |
0.2510 |
0.5050 |
0.2430 |
0.5040 |
0.1960 |
0.4390 |
0.1790 |
0.3980 |
0.1400 |
0.3570 |
0.1140 |
0.3190 |
0.1020 |
0.2770 |
0.0860 |
0.2570 |
0.0830 |
0.2560 |
0.0710 |
0.2220 |
0.0590 |
0.1910 |
0.0220 |
0.0800 |
0.0000 |
0.0000 |
Azeotropic composition: mole fraction of Octane (2)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Octane (2) - Liquid |
40.00 |
0.9800 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Octane (2) - Liquid |
Mole fraction of Octane (2) - Gas |
1.0000 |
1.0000 |
0.9210 |
0.9330 |
0.8400 |
0.8840 |
0.8360 |
0.8730 |
0.7630 |
0.8410 |
0.6990 |
0.7860 |
0.6650 |
0.7920 |
0.6250 |
0.7470 |
0.6110 |
0.7600 |
0.5690 |
0.7210 |
0.5130 |
0.7140 |
0.4690 |
0.6770 |
0.3530 |
0.5940 |
0.3200 |
0.5890 |
0.3170 |
0.5640 |
0.2850 |
0.5460 |
0.2530 |
0.5090 |
0.2510 |
0.5050 |
0.2430 |
0.5040 |
0.1960 |
0.4390 |
0.1790 |
0.3980 |
0.1400 |
0.3570 |
0.1140 |
0.3190 |
0.1020 |
0.2770 |
0.0860 |
0.2570 |
0.0830 |
0.2560 |
0.0710 |
0.2220 |
0.0590 |
0.1910 |
0.0220 |
0.0800 |
0.0000 |
0.0000 |
Azeotropic composition: mole fraction of Octane (2)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Octane (2) - Liquid |
40.00 |
0.9800 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Octane (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
1.0000 |
367.97 |
0.9210 |
368.37 |
0.8400 |
368.88 |
0.8360 |
368.78 |
0.7630 |
369.47 |
0.6990 |
369.90 |
0.6650 |
370.35 |
0.6250 |
370.77 |
0.6110 |
371.01 |
0.5690 |
371.58 |
0.5130 |
372.28 |
0.4690 |
372.98 |
0.3530 |
375.72 |
0.3200 |
375.65 |
0.3170 |
375.95 |
0.2850 |
376.81 |
0.2530 |
377.75 |
0.2510 |
377.66 |
0.2430 |
377.93 |
0.1960 |
379.45 |
0.1790 |
380.03 |
0.1400 |
381.52 |
0.1140 |
382.30 |
0.1020 |
383.00 |
0.0860 |
383.79 |
0.0830 |
383.37 |
0.0710 |
384.44 |
0.0590 |
385.05 |
0.0220 |
386.89 |
0.0000 |
388.11 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of Octane (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
1.0000 |
367.97 |
0.9210 |
368.37 |
0.8400 |
368.88 |
0.8360 |
368.78 |
0.7630 |
369.47 |
0.6990 |
369.90 |
0.6650 |
370.35 |
0.6250 |
370.77 |
0.6110 |
371.01 |
0.5690 |
371.58 |
0.5130 |
372.28 |
0.4690 |
372.98 |
0.3530 |
375.72 |
0.3200 |
375.65 |
0.3170 |
375.95 |
0.2850 |
376.81 |
0.2530 |
377.75 |
0.2510 |
377.66 |
0.2430 |
377.93 |
0.1960 |
379.45 |
0.1790 |
380.03 |
0.1400 |
381.52 |
0.1140 |
382.30 |
0.1020 |
383.00 |
0.0860 |
383.79 |
0.0830 |
383.37 |
0.0710 |
384.44 |
0.0590 |
385.05 |
0.0220 |
386.89 |
0.0000 |
388.11 |
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