Mixture of 1-Butanol, 3-methyl-, acetate + Ethyl Acetate
Datasets
-
Mole fraction (2)
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Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Ethyl Acetate (2)
[ref]
Fixed |
Measured |
Pressure, kPa - Gas |
Mole fraction of Ethyl Acetate (2) - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
100.00 |
1.0000 |
1.0000 |
100.00 |
0.9360 |
0.9940 |
100.00 |
0.8810 |
0.9880 |
100.00 |
0.8350 |
0.9820 |
100.00 |
0.7980 |
0.9770 |
100.00 |
0.7530 |
0.9700 |
100.00 |
0.7260 |
0.9650 |
100.00 |
0.6930 |
0.9590 |
100.00 |
0.6670 |
0.9550 |
100.00 |
0.6300 |
0.9430 |
100.00 |
0.5970 |
0.9330 |
100.00 |
0.5780 |
0.9280 |
100.00 |
0.5530 |
0.9230 |
100.00 |
0.5190 |
0.9110 |
100.00 |
0.4460 |
0.8760 |
100.00 |
0.3410 |
0.8010 |
100.00 |
0.3060 |
0.7800 |
100.00 |
0.2920 |
0.7700 |
100.00 |
0.2630 |
0.7430 |
100.00 |
0.2450 |
0.7050 |
100.00 |
0.2080 |
0.6580 |
100.00 |
0.1580 |
0.5620 |
100.00 |
0.1460 |
0.5250 |
100.00 |
0.1350 |
0.5040 |
100.00 |
0.1220 |
0.4850 |
100.00 |
0.0830 |
0.3790 |
100.00 |
0.0120 |
0.0690 |
100.00 |
0.0000 |
0.0000 |
50.00 |
1.0000 |
1.0000 |
50.00 |
0.9540 |
0.9970 |
50.00 |
0.9290 |
0.9950 |
50.00 |
0.8940 |
0.9920 |
50.00 |
0.8230 |
0.9860 |
50.00 |
0.7750 |
0.9780 |
50.00 |
0.7370 |
0.9740 |
50.00 |
0.6320 |
0.9590 |
50.00 |
0.5160 |
0.9220 |
50.00 |
0.4700 |
0.8910 |
50.00 |
0.4180 |
0.8730 |
50.00 |
0.3700 |
0.8520 |
50.00 |
0.3220 |
0.8190 |
50.00 |
0.2990 |
0.7970 |
50.00 |
0.2630 |
0.7620 |
50.00 |
0.2390 |
0.7410 |
50.00 |
0.2060 |
0.6990 |
50.00 |
0.1810 |
0.6470 |
50.00 |
0.1390 |
0.5640 |
50.00 |
0.1010 |
0.4300 |
50.00 |
0.0160 |
0.1040 |
50.00 |
0.0000 |
0.0000 |
Mole fraction of Ethyl Acetate (2)
[ref]
Fixed |
Measured |
Pressure, kPa - Gas |
Mole fraction of Ethyl Acetate (2) - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
100.00 |
1.0000 |
1.0000 |
100.00 |
0.9360 |
0.9940 |
100.00 |
0.8810 |
0.9880 |
100.00 |
0.8350 |
0.9820 |
100.00 |
0.7980 |
0.9770 |
100.00 |
0.7530 |
0.9700 |
100.00 |
0.7260 |
0.9650 |
100.00 |
0.6930 |
0.9590 |
100.00 |
0.6670 |
0.9550 |
100.00 |
0.6300 |
0.9430 |
100.00 |
0.5970 |
0.9330 |
100.00 |
0.5780 |
0.9280 |
100.00 |
0.5530 |
0.9230 |
100.00 |
0.5190 |
0.9110 |
100.00 |
0.4460 |
0.8760 |
100.00 |
0.3410 |
0.8010 |
100.00 |
0.3060 |
0.7800 |
100.00 |
0.2920 |
0.7700 |
100.00 |
0.2630 |
0.7430 |
100.00 |
0.2450 |
0.7050 |
100.00 |
0.2080 |
0.6580 |
100.00 |
0.1580 |
0.5620 |
100.00 |
0.1460 |
0.5250 |
100.00 |
0.1350 |
0.5040 |
100.00 |
0.1220 |
0.4850 |
100.00 |
0.0830 |
0.3790 |
100.00 |
0.0120 |
0.0690 |
100.00 |
0.0000 |
0.0000 |
50.00 |
1.0000 |
1.0000 |
50.00 |
0.9540 |
0.9970 |
50.00 |
0.9290 |
0.9950 |
50.00 |
0.8940 |
0.9920 |
50.00 |
0.8230 |
0.9860 |
50.00 |
0.7750 |
0.9780 |
50.00 |
0.7370 |
0.9740 |
50.00 |
0.6320 |
0.9590 |
50.00 |
0.5160 |
0.9220 |
50.00 |
0.4700 |
0.8910 |
50.00 |
0.4180 |
0.8730 |
50.00 |
0.3700 |
0.8520 |
50.00 |
0.3220 |
0.8190 |
50.00 |
0.2990 |
0.7970 |
50.00 |
0.2630 |
0.7620 |
50.00 |
0.2390 |
0.7410 |
50.00 |
0.2060 |
0.6990 |
50.00 |
0.1810 |
0.6470 |
50.00 |
0.1390 |
0.5640 |
50.00 |
0.1010 |
0.4300 |
50.00 |
0.0160 |
0.1040 |
50.00 |
0.0000 |
0.0000 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Gas |
Mole fraction of Ethyl Acetate (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
100.00 |
1.0000 |
349.53 |
100.00 |
0.9360 |
350.12 |
100.00 |
0.8810 |
351.42 |
100.00 |
0.8350 |
352.84 |
100.00 |
0.7980 |
354.05 |
100.00 |
0.7530 |
355.01 |
100.00 |
0.7260 |
356.20 |
100.00 |
0.6930 |
357.43 |
100.00 |
0.6670 |
358.33 |
100.00 |
0.6300 |
359.89 |
100.00 |
0.5970 |
361.24 |
100.00 |
0.5780 |
362.30 |
100.00 |
0.5530 |
363.21 |
100.00 |
0.5190 |
364.65 |
100.00 |
0.4460 |
368.66 |
100.00 |
0.3410 |
375.95 |
100.00 |
0.3060 |
378.12 |
100.00 |
0.2920 |
379.19 |
100.00 |
0.2630 |
381.52 |
100.00 |
0.2450 |
383.76 |
100.00 |
0.2080 |
386.24 |
100.00 |
0.1580 |
392.08 |
100.00 |
0.1460 |
393.44 |
100.00 |
0.1350 |
395.29 |
100.00 |
0.1220 |
396.46 |
100.00 |
0.0830 |
401.17 |
100.00 |
0.0120 |
412.30 |
100.00 |
0.0000 |
413.46 |
50.00 |
1.0000 |
330.01 |
50.00 |
0.9540 |
330.69 |
50.00 |
0.9290 |
330.99 |
50.00 |
0.8940 |
331.85 |
50.00 |
0.8230 |
333.55 |
50.00 |
0.7750 |
334.85 |
50.00 |
0.7370 |
336.13 |
50.00 |
0.6320 |
339.59 |
50.00 |
0.5160 |
344.37 |
50.00 |
0.4700 |
346.68 |
50.00 |
0.4180 |
349.41 |
50.00 |
0.3700 |
351.38 |
50.00 |
0.3220 |
354.46 |
50.00 |
0.2990 |
356.77 |
50.00 |
0.2630 |
359.43 |
50.00 |
0.2390 |
361.57 |
50.00 |
0.2060 |
364.26 |
50.00 |
0.1810 |
366.87 |
50.00 |
0.1390 |
370.84 |
50.00 |
0.1010 |
375.99 |
50.00 |
0.0160 |
388.47 |
50.00 |
0.0000 |
391.07 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Gas |
Mole fraction of Ethyl Acetate (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
100.00 |
1.0000 |
349.53 |
100.00 |
0.9360 |
350.12 |
100.00 |
0.8810 |
351.42 |
100.00 |
0.8350 |
352.84 |
100.00 |
0.7980 |
354.05 |
100.00 |
0.7530 |
355.01 |
100.00 |
0.7260 |
356.20 |
100.00 |
0.6930 |
357.43 |
100.00 |
0.6670 |
358.33 |
100.00 |
0.6300 |
359.89 |
100.00 |
0.5970 |
361.24 |
100.00 |
0.5780 |
362.30 |
100.00 |
0.5530 |
363.21 |
100.00 |
0.5190 |
364.65 |
100.00 |
0.4460 |
368.66 |
100.00 |
0.3410 |
375.95 |
100.00 |
0.3060 |
378.12 |
100.00 |
0.2920 |
379.19 |
100.00 |
0.2630 |
381.52 |
100.00 |
0.2450 |
383.76 |
100.00 |
0.2080 |
386.24 |
100.00 |
0.1580 |
392.08 |
100.00 |
0.1460 |
393.44 |
100.00 |
0.1350 |
395.29 |
100.00 |
0.1220 |
396.46 |
100.00 |
0.0830 |
401.17 |
100.00 |
0.0120 |
412.30 |
100.00 |
0.0000 |
413.46 |
50.00 |
1.0000 |
330.01 |
50.00 |
0.9540 |
330.69 |
50.00 |
0.9290 |
330.99 |
50.00 |
0.8940 |
331.85 |
50.00 |
0.8230 |
333.55 |
50.00 |
0.7750 |
334.85 |
50.00 |
0.7370 |
336.13 |
50.00 |
0.6320 |
339.59 |
50.00 |
0.5160 |
344.37 |
50.00 |
0.4700 |
346.68 |
50.00 |
0.4180 |
349.41 |
50.00 |
0.3700 |
351.38 |
50.00 |
0.3220 |
354.46 |
50.00 |
0.2990 |
356.77 |
50.00 |
0.2630 |
359.43 |
50.00 |
0.2390 |
361.57 |
50.00 |
0.2060 |
364.26 |
50.00 |
0.1810 |
366.87 |
50.00 |
0.1390 |
370.84 |
50.00 |
0.1010 |
375.99 |
50.00 |
0.0160 |
388.47 |
50.00 |
0.0000 |
391.07 |
Sources