Datasets
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Mole fraction (4)
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Tboil - Boiling temperature at pressure P, K (4)
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Gas |
0.0000 |
0.0000 |
0.1661 |
0.3501 |
0.2555 |
0.4999 |
0.3011 |
0.5607 |
0.3569 |
0.6299 |
0.3922 |
0.6616 |
0.4028 |
0.6791 |
0.4605 |
0.7348 |
0.4863 |
0.7629 |
0.5041 |
0.7758 |
0.6068 |
0.8419 |
0.6998 |
0.8985 |
0.7561 |
0.9276 |
0.8104 |
0.9551 |
0.8526 |
0.9752 |
1.0000 |
1.0000 |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2)
[ref]
Fixed |
Measured |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Gas |
0.0000 |
53.30 |
0.0000 |
0.0410 |
53.30 |
0.1220 |
0.0990 |
53.30 |
0.2210 |
0.1790 |
53.30 |
0.3670 |
0.2480 |
53.30 |
0.4770 |
0.2960 |
53.30 |
0.5430 |
0.3520 |
53.30 |
0.6080 |
0.4250 |
53.30 |
0.6850 |
0.5210 |
53.30 |
0.7530 |
0.5750 |
53.30 |
0.8060 |
0.6750 |
53.30 |
0.8670 |
0.7550 |
53.30 |
0.9080 |
0.8240 |
53.30 |
0.9400 |
0.9110 |
53.30 |
0.9720 |
0.9770 |
53.30 |
0.9930 |
1.0000 |
53.30 |
1.0000 |
0.0000 |
66.70 |
0.0000 |
0.0400 |
66.70 |
0.0950 |
0.0590 |
66.70 |
0.1390 |
0.0890 |
66.70 |
0.2340 |
0.1400 |
66.70 |
0.2990 |
0.1710 |
66.70 |
0.3590 |
0.2350 |
66.70 |
0.4750 |
0.2870 |
66.70 |
0.5250 |
0.3510 |
66.70 |
0.5990 |
0.4250 |
66.70 |
0.6740 |
0.5100 |
66.70 |
0.7490 |
0.5800 |
66.70 |
0.8030 |
0.6250 |
66.70 |
0.8320 |
0.6850 |
66.70 |
0.8660 |
0.7250 |
66.70 |
0.8910 |
0.7990 |
66.70 |
0.9270 |
0.8700 |
66.70 |
0.9560 |
0.9380 |
66.70 |
0.9760 |
0.9800 |
66.70 |
0.9940 |
1.0000 |
66.70 |
1.0000 |
0.0000 |
80.00 |
0.0000 |
0.0360 |
80.00 |
0.0670 |
0.1800 |
80.00 |
0.3650 |
0.2500 |
80.00 |
0.4710 |
0.3250 |
80.00 |
0.5660 |
0.4080 |
80.00 |
0.6510 |
0.4500 |
80.00 |
0.6930 |
0.4990 |
80.00 |
0.7360 |
0.5750 |
80.00 |
0.7960 |
0.5750 |
80.00 |
0.7960 |
0.6500 |
80.00 |
0.8460 |
0.7240 |
80.00 |
0.8900 |
0.8100 |
80.00 |
0.9310 |
0.8750 |
80.00 |
0.9590 |
0.9190 |
80.00 |
0.9750 |
0.9760 |
80.00 |
0.9930 |
1.0000 |
80.00 |
1.0000 |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Gas |
0.0000 |
0.0000 |
0.1661 |
0.3501 |
0.2555 |
0.4999 |
0.3011 |
0.5607 |
0.3569 |
0.6299 |
0.3922 |
0.6616 |
0.4028 |
0.6791 |
0.4605 |
0.7348 |
0.4863 |
0.7629 |
0.5041 |
0.7758 |
0.6068 |
0.8419 |
0.6998 |
0.8985 |
0.7561 |
0.9276 |
0.8104 |
0.9551 |
0.8526 |
0.9752 |
1.0000 |
1.0000 |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2)
[ref]
Fixed |
Measured |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Gas |
0.0000 |
53.30 |
0.0000 |
0.0410 |
53.30 |
0.1220 |
0.0990 |
53.30 |
0.2210 |
0.1790 |
53.30 |
0.3670 |
0.2480 |
53.30 |
0.4770 |
0.2960 |
53.30 |
0.5430 |
0.3520 |
53.30 |
0.6080 |
0.4250 |
53.30 |
0.6850 |
0.5210 |
53.30 |
0.7530 |
0.5750 |
53.30 |
0.8060 |
0.6750 |
53.30 |
0.8670 |
0.7550 |
53.30 |
0.9080 |
0.8240 |
53.30 |
0.9400 |
0.9110 |
53.30 |
0.9720 |
0.9770 |
53.30 |
0.9930 |
1.0000 |
53.30 |
1.0000 |
0.0000 |
66.70 |
0.0000 |
0.0400 |
66.70 |
0.0950 |
0.0590 |
66.70 |
0.1390 |
0.0890 |
66.70 |
0.2340 |
0.1400 |
66.70 |
0.2990 |
0.1710 |
66.70 |
0.3590 |
0.2350 |
66.70 |
0.4750 |
0.2870 |
66.70 |
0.5250 |
0.3510 |
66.70 |
0.5990 |
0.4250 |
66.70 |
0.6740 |
0.5100 |
66.70 |
0.7490 |
0.5800 |
66.70 |
0.8030 |
0.6250 |
66.70 |
0.8320 |
0.6850 |
66.70 |
0.8660 |
0.7250 |
66.70 |
0.8910 |
0.7990 |
66.70 |
0.9270 |
0.8700 |
66.70 |
0.9560 |
0.9380 |
66.70 |
0.9760 |
0.9800 |
66.70 |
0.9940 |
1.0000 |
66.70 |
1.0000 |
0.0000 |
80.00 |
0.0000 |
0.0360 |
80.00 |
0.0670 |
0.1800 |
80.00 |
0.3650 |
0.2500 |
80.00 |
0.4710 |
0.3250 |
80.00 |
0.5660 |
0.4080 |
80.00 |
0.6510 |
0.4500 |
80.00 |
0.6930 |
0.4990 |
80.00 |
0.7360 |
0.5750 |
80.00 |
0.7960 |
0.5750 |
80.00 |
0.7960 |
0.6500 |
80.00 |
0.8460 |
0.7240 |
80.00 |
0.8900 |
0.8100 |
80.00 |
0.9310 |
0.8750 |
80.00 |
0.9590 |
0.9190 |
80.00 |
0.9750 |
0.9760 |
80.00 |
0.9930 |
1.0000 |
80.00 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
413.57 |
0.1661 |
407.14 |
0.2555 |
403.52 |
0.3011 |
401.69 |
0.3569 |
399.40 |
0.3922 |
398.25 |
0.4028 |
397.54 |
0.4605 |
395.23 |
0.4863 |
394.15 |
0.5041 |
393.49 |
0.6068 |
390.45 |
0.6998 |
387.75 |
0.7561 |
385.45 |
0.8104 |
384.15 |
0.8526 |
383.15 |
1.0000 |
382.28 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
53.30 |
394.71 |
0.0410 |
53.30 |
392.00 |
0.0990 |
53.30 |
389.82 |
0.1790 |
53.30 |
386.62 |
0.2480 |
53.30 |
383.74 |
0.2960 |
53.30 |
381.98 |
0.3520 |
53.30 |
380.32 |
0.4250 |
53.30 |
378.01 |
0.5210 |
53.30 |
375.50 |
0.5750 |
53.30 |
373.93 |
0.6750 |
53.30 |
371.53 |
0.7550 |
53.30 |
369.86 |
0.8240 |
53.30 |
368.31 |
0.9110 |
53.30 |
366.84 |
0.9770 |
53.30 |
365.46 |
1.0000 |
53.30 |
365.01 |
0.0000 |
66.70 |
400.93 |
0.0400 |
66.70 |
399.46 |
0.0590 |
66.70 |
398.15 |
0.0890 |
66.70 |
397.00 |
0.1400 |
66.70 |
395.15 |
0.1710 |
66.70 |
393.04 |
0.2350 |
66.70 |
390.30 |
0.2870 |
66.70 |
388.98 |
0.3510 |
66.70 |
386.41 |
0.4250 |
66.70 |
384.06 |
0.5100 |
66.70 |
381.90 |
0.5800 |
66.70 |
379.90 |
0.6250 |
66.70 |
378.65 |
0.6850 |
66.70 |
377.45 |
0.7250 |
66.70 |
376.31 |
0.7990 |
66.70 |
374.68 |
0.8700 |
66.70 |
373.15 |
0.9380 |
66.70 |
371.80 |
0.9800 |
66.70 |
371.25 |
1.0000 |
66.70 |
370.79 |
0.0000 |
80.00 |
406.16 |
0.0360 |
80.00 |
404.51 |
0.1800 |
80.00 |
398.02 |
0.2500 |
80.00 |
395.08 |
0.3250 |
80.00 |
392.39 |
0.4080 |
80.00 |
389.94 |
0.4500 |
80.00 |
388.41 |
0.4990 |
80.00 |
386.96 |
0.5750 |
80.00 |
384.92 |
0.5750 |
80.00 |
384.92 |
0.6500 |
80.00 |
383.03 |
0.7240 |
80.00 |
381.27 |
0.8100 |
80.00 |
379.61 |
0.8750 |
80.00 |
378.06 |
0.9190 |
80.00 |
377.07 |
0.9760 |
80.00 |
376.12 |
1.0000 |
80.00 |
375.66 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
413.57 |
0.1661 |
407.14 |
0.2555 |
403.52 |
0.3011 |
401.69 |
0.3569 |
399.40 |
0.3922 |
398.25 |
0.4028 |
397.54 |
0.4605 |
395.23 |
0.4863 |
394.15 |
0.5041 |
393.49 |
0.6068 |
390.45 |
0.6998 |
387.75 |
0.7561 |
385.45 |
0.8104 |
384.15 |
0.8526 |
383.15 |
1.0000 |
382.28 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
53.30 |
394.71 |
0.0410 |
53.30 |
392.00 |
0.0990 |
53.30 |
389.82 |
0.1790 |
53.30 |
386.62 |
0.2480 |
53.30 |
383.74 |
0.2960 |
53.30 |
381.98 |
0.3520 |
53.30 |
380.32 |
0.4250 |
53.30 |
378.01 |
0.5210 |
53.30 |
375.50 |
0.5750 |
53.30 |
373.93 |
0.6750 |
53.30 |
371.53 |
0.7550 |
53.30 |
369.86 |
0.8240 |
53.30 |
368.31 |
0.9110 |
53.30 |
366.84 |
0.9770 |
53.30 |
365.46 |
1.0000 |
53.30 |
365.01 |
0.0000 |
66.70 |
400.93 |
0.0400 |
66.70 |
399.46 |
0.0590 |
66.70 |
398.15 |
0.0890 |
66.70 |
397.00 |
0.1400 |
66.70 |
395.15 |
0.1710 |
66.70 |
393.04 |
0.2350 |
66.70 |
390.30 |
0.2870 |
66.70 |
388.98 |
0.3510 |
66.70 |
386.41 |
0.4250 |
66.70 |
384.06 |
0.5100 |
66.70 |
381.90 |
0.5800 |
66.70 |
379.90 |
0.6250 |
66.70 |
378.65 |
0.6850 |
66.70 |
377.45 |
0.7250 |
66.70 |
376.31 |
0.7990 |
66.70 |
374.68 |
0.8700 |
66.70 |
373.15 |
0.9380 |
66.70 |
371.80 |
0.9800 |
66.70 |
371.25 |
1.0000 |
66.70 |
370.79 |
0.0000 |
80.00 |
406.16 |
0.0360 |
80.00 |
404.51 |
0.1800 |
80.00 |
398.02 |
0.2500 |
80.00 |
395.08 |
0.3250 |
80.00 |
392.39 |
0.4080 |
80.00 |
389.94 |
0.4500 |
80.00 |
388.41 |
0.4990 |
80.00 |
386.96 |
0.5750 |
80.00 |
384.92 |
0.5750 |
80.00 |
384.92 |
0.6500 |
80.00 |
383.03 |
0.7240 |
80.00 |
381.27 |
0.8100 |
80.00 |
379.61 |
0.8750 |
80.00 |
378.06 |
0.9190 |
80.00 |
377.07 |
0.9760 |
80.00 |
376.12 |
1.0000 |
80.00 |
375.66 |
Sources
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Measurements and correlations of density, viscosity, and vapour-liquid equilibrium for fluoro alcohols
-
Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,3,3-Tetrafluoro-1-propanol + 2,2,3,3,4,4,5,5-Octafluoro-1-pentanol at 53.3, 66.7, 80.0 kPa