Mixture of 1-Pentanol + Propanoic acid, 2-hydroxy-, ethyl ester
Datasets
-
Mole fraction (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 1-Pentanol (1)
[ref]
Fixed |
Measured |
Mole fraction of 1-Pentanol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1-Pentanol (1) - Gas |
0.0000 |
13.00 |
0.0000 |
0.0000 |
101.30 |
0.0000 |
0.0130 |
13.00 |
0.0280 |
0.0320 |
101.30 |
0.0660 |
0.0380 |
101.30 |
0.0770 |
0.0410 |
13.00 |
0.0840 |
0.0430 |
101.30 |
0.0870 |
0.0540 |
101.30 |
0.1060 |
0.0550 |
13.00 |
0.1070 |
0.0670 |
101.30 |
0.1300 |
0.0850 |
101.30 |
0.1590 |
0.0960 |
13.00 |
0.1700 |
0.0990 |
101.30 |
0.1810 |
0.1050 |
101.30 |
0.1910 |
0.1110 |
13.00 |
0.1900 |
0.1180 |
101.30 |
0.2110 |
0.1280 |
13.00 |
0.2150 |
0.1380 |
101.30 |
0.2410 |
0.1390 |
13.00 |
0.2230 |
0.1510 |
101.30 |
0.2580 |
0.1620 |
13.00 |
0.2530 |
0.1680 |
101.30 |
0.2810 |
0.1970 |
101.30 |
0.3200 |
0.2100 |
101.30 |
0.3340 |
0.2140 |
13.00 |
0.3120 |
0.2400 |
101.30 |
0.3690 |
0.2820 |
13.00 |
0.3820 |
0.2830 |
101.30 |
0.4160 |
0.3220 |
101.30 |
0.4570 |
0.3710 |
13.00 |
0.4640 |
0.3750 |
101.30 |
0.5080 |
0.4120 |
101.30 |
0.5440 |
0.4440 |
13.00 |
0.5260 |
0.4730 |
101.30 |
0.5960 |
0.5520 |
13.00 |
0.6140 |
0.5930 |
101.30 |
0.6940 |
0.6530 |
13.00 |
0.6960 |
0.6630 |
101.30 |
0.7510 |
0.7400 |
101.30 |
0.8100 |
0.7890 |
13.00 |
0.8130 |
0.8160 |
101.30 |
0.8650 |
0.8930 |
101.30 |
0.9220 |
0.8950 |
101.30 |
0.9240 |
0.9120 |
13.00 |
0.9190 |
0.9340 |
101.30 |
0.9520 |
0.9570 |
13.00 |
0.9600 |
0.9720 |
101.30 |
0.9790 |
0.9930 |
101.30 |
0.9950 |
1.0000 |
13.00 |
1.0000 |
1.0000 |
101.30 |
1.0000 |
Mole fraction of 1-Pentanol (1)
[ref]
Fixed |
Measured |
Mole fraction of 1-Pentanol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1-Pentanol (1) - Gas |
0.0000 |
13.00 |
0.0000 |
0.0000 |
101.30 |
0.0000 |
0.0130 |
13.00 |
0.0280 |
0.0320 |
101.30 |
0.0660 |
0.0380 |
101.30 |
0.0770 |
0.0410 |
13.00 |
0.0840 |
0.0430 |
101.30 |
0.0870 |
0.0540 |
101.30 |
0.1060 |
0.0550 |
13.00 |
0.1070 |
0.0670 |
101.30 |
0.1300 |
0.0850 |
101.30 |
0.1590 |
0.0960 |
13.00 |
0.1700 |
0.0990 |
101.30 |
0.1810 |
0.1050 |
101.30 |
0.1910 |
0.1110 |
13.00 |
0.1900 |
0.1180 |
101.30 |
0.2110 |
0.1280 |
13.00 |
0.2150 |
0.1380 |
101.30 |
0.2410 |
0.1390 |
13.00 |
0.2230 |
0.1510 |
101.30 |
0.2580 |
0.1620 |
13.00 |
0.2530 |
0.1680 |
101.30 |
0.2810 |
0.1970 |
101.30 |
0.3200 |
0.2100 |
101.30 |
0.3340 |
0.2140 |
13.00 |
0.3120 |
0.2400 |
101.30 |
0.3690 |
0.2820 |
13.00 |
0.3820 |
0.2830 |
101.30 |
0.4160 |
0.3220 |
101.30 |
0.4570 |
0.3710 |
13.00 |
0.4640 |
0.3750 |
101.30 |
0.5080 |
0.4120 |
101.30 |
0.5440 |
0.4440 |
13.00 |
0.5260 |
0.4730 |
101.30 |
0.5960 |
0.5520 |
13.00 |
0.6140 |
0.5930 |
101.30 |
0.6940 |
0.6530 |
13.00 |
0.6960 |
0.6630 |
101.30 |
0.7510 |
0.7400 |
101.30 |
0.8100 |
0.7890 |
13.00 |
0.8130 |
0.8160 |
101.30 |
0.8650 |
0.8930 |
101.30 |
0.9220 |
0.8950 |
101.30 |
0.9240 |
0.9120 |
13.00 |
0.9190 |
0.9340 |
101.30 |
0.9520 |
0.9570 |
13.00 |
0.9600 |
0.9720 |
101.30 |
0.9790 |
0.9930 |
101.30 |
0.9950 |
1.0000 |
13.00 |
1.0000 |
1.0000 |
101.30 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1-Pentanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
13.00 |
366.65 |
0.0000 |
101.30 |
427.62 |
0.0130 |
13.00 |
366.25 |
0.0320 |
101.30 |
426.35 |
0.0380 |
101.30 |
426.15 |
0.0410 |
13.00 |
365.45 |
0.0430 |
101.30 |
426.05 |
0.0540 |
101.30 |
425.55 |
0.0550 |
13.00 |
365.25 |
0.0670 |
101.30 |
425.15 |
0.0850 |
101.30 |
424.45 |
0.0960 |
13.00 |
364.35 |
0.0990 |
101.30 |
424.15 |
0.1050 |
101.30 |
423.95 |
0.1110 |
13.00 |
364.05 |
0.1180 |
101.30 |
423.75 |
0.1280 |
13.00 |
363.65 |
0.1380 |
101.30 |
422.95 |
0.1390 |
13.00 |
363.35 |
0.1510 |
101.30 |
422.65 |
0.1620 |
13.00 |
363.15 |
0.1680 |
101.30 |
422.15 |
0.1970 |
101.30 |
421.65 |
0.2100 |
101.30 |
421.25 |
0.2140 |
13.00 |
362.45 |
0.2400 |
101.30 |
420.55 |
0.2820 |
13.00 |
361.75 |
0.2830 |
101.30 |
419.85 |
0.3220 |
101.30 |
419.15 |
0.3710 |
13.00 |
360.85 |
0.3750 |
101.30 |
418.05 |
0.4120 |
101.30 |
417.45 |
0.4440 |
13.00 |
360.45 |
0.4730 |
101.30 |
416.75 |
0.5520 |
13.00 |
359.85 |
0.5930 |
101.30 |
415.05 |
0.6530 |
13.00 |
359.35 |
0.6630 |
101.30 |
414.25 |
0.7400 |
101.30 |
413.35 |
0.7890 |
13.00 |
358.95 |
0.8160 |
101.30 |
412.55 |
0.8930 |
101.30 |
412.05 |
0.8950 |
101.30 |
411.95 |
0.9120 |
13.00 |
358.65 |
0.9340 |
101.30 |
411.55 |
0.9570 |
13.00 |
358.45 |
0.9720 |
101.30 |
411.35 |
0.9930 |
101.30 |
411.15 |
1.0000 |
13.00 |
358.35 |
1.0000 |
101.30 |
411.05 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1-Pentanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
13.00 |
366.65 |
0.0000 |
101.30 |
427.62 |
0.0130 |
13.00 |
366.25 |
0.0320 |
101.30 |
426.35 |
0.0380 |
101.30 |
426.15 |
0.0410 |
13.00 |
365.45 |
0.0430 |
101.30 |
426.05 |
0.0540 |
101.30 |
425.55 |
0.0550 |
13.00 |
365.25 |
0.0670 |
101.30 |
425.15 |
0.0850 |
101.30 |
424.45 |
0.0960 |
13.00 |
364.35 |
0.0990 |
101.30 |
424.15 |
0.1050 |
101.30 |
423.95 |
0.1110 |
13.00 |
364.05 |
0.1180 |
101.30 |
423.75 |
0.1280 |
13.00 |
363.65 |
0.1380 |
101.30 |
422.95 |
0.1390 |
13.00 |
363.35 |
0.1510 |
101.30 |
422.65 |
0.1620 |
13.00 |
363.15 |
0.1680 |
101.30 |
422.15 |
0.1970 |
101.30 |
421.65 |
0.2100 |
101.30 |
421.25 |
0.2140 |
13.00 |
362.45 |
0.2400 |
101.30 |
420.55 |
0.2820 |
13.00 |
361.75 |
0.2830 |
101.30 |
419.85 |
0.3220 |
101.30 |
419.15 |
0.3710 |
13.00 |
360.85 |
0.3750 |
101.30 |
418.05 |
0.4120 |
101.30 |
417.45 |
0.4440 |
13.00 |
360.45 |
0.4730 |
101.30 |
416.75 |
0.5520 |
13.00 |
359.85 |
0.5930 |
101.30 |
415.05 |
0.6530 |
13.00 |
359.35 |
0.6630 |
101.30 |
414.25 |
0.7400 |
101.30 |
413.35 |
0.7890 |
13.00 |
358.95 |
0.8160 |
101.30 |
412.55 |
0.8930 |
101.30 |
412.05 |
0.8950 |
101.30 |
411.95 |
0.9120 |
13.00 |
358.65 |
0.9340 |
101.30 |
411.55 |
0.9570 |
13.00 |
358.45 |
0.9720 |
101.30 |
411.35 |
0.9930 |
101.30 |
411.15 |
1.0000 |
13.00 |
358.35 |
1.0000 |
101.30 |
411.05 |
Sources