Mixture of Octanoic acid, methyl ester + Decanoic acid, methyl ester
Datasets
-
Mole fraction (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Octanoic acid, methyl ester (1)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Octanoic acid, methyl ester (1) - Liquid |
Mole fraction of Octanoic acid, methyl ester (1) - Gas |
2.00 |
0.0000 |
0.0000 |
2.00 |
0.0599 |
0.2468 |
2.00 |
0.0876 |
0.3286 |
2.00 |
0.1403 |
0.4554 |
2.00 |
0.1772 |
0.5127 |
2.00 |
0.2702 |
0.6436 |
2.00 |
0.3594 |
0.7283 |
2.00 |
0.5113 |
0.8351 |
2.00 |
0.6194 |
0.8883 |
2.00 |
0.7321 |
0.9251 |
2.00 |
0.8258 |
0.9546 |
2.00 |
0.8732 |
0.9679 |
2.00 |
1.0000 |
1.0000 |
6.00 |
0.0000 |
0.0000 |
6.00 |
0.0595 |
0.2304 |
6.00 |
0.0899 |
0.3179 |
6.00 |
0.1437 |
0.4425 |
6.00 |
0.1793 |
0.5024 |
6.00 |
0.2727 |
0.6353 |
6.00 |
0.3640 |
0.7241 |
6.00 |
0.5175 |
0.8312 |
6.00 |
0.6476 |
0.8825 |
6.00 |
0.7441 |
0.9226 |
6.00 |
0.8340 |
0.9563 |
6.00 |
0.8774 |
0.9670 |
6.00 |
1.0000 |
1.0000 |
10.00 |
0.0000 |
0.0000 |
10.00 |
0.0609 |
0.2296 |
10.00 |
0.0921 |
0.3112 |
10.00 |
0.1442 |
0.4286 |
10.00 |
0.1821 |
0.4928 |
10.00 |
0.2753 |
0.6246 |
10.00 |
0.3662 |
0.7087 |
10.00 |
0.5213 |
0.8163 |
10.00 |
0.6485 |
0.8814 |
10.00 |
0.7507 |
0.9228 |
10.00 |
0.8352 |
0.9526 |
10.00 |
0.8785 |
0.9657 |
10.00 |
1.0000 |
1.0000 |
Mole fraction of Octanoic acid, methyl ester (1)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Octanoic acid, methyl ester (1) - Liquid |
Mole fraction of Octanoic acid, methyl ester (1) - Gas |
2.00 |
0.0000 |
0.0000 |
2.00 |
0.0599 |
0.2468 |
2.00 |
0.0876 |
0.3286 |
2.00 |
0.1403 |
0.4554 |
2.00 |
0.1772 |
0.5127 |
2.00 |
0.2702 |
0.6436 |
2.00 |
0.3594 |
0.7283 |
2.00 |
0.5113 |
0.8351 |
2.00 |
0.6194 |
0.8883 |
2.00 |
0.7321 |
0.9251 |
2.00 |
0.8258 |
0.9546 |
2.00 |
0.8732 |
0.9679 |
2.00 |
1.0000 |
1.0000 |
6.00 |
0.0000 |
0.0000 |
6.00 |
0.0595 |
0.2304 |
6.00 |
0.0899 |
0.3179 |
6.00 |
0.1437 |
0.4425 |
6.00 |
0.1793 |
0.5024 |
6.00 |
0.2727 |
0.6353 |
6.00 |
0.3640 |
0.7241 |
6.00 |
0.5175 |
0.8312 |
6.00 |
0.6476 |
0.8825 |
6.00 |
0.7441 |
0.9226 |
6.00 |
0.8340 |
0.9563 |
6.00 |
0.8774 |
0.9670 |
6.00 |
1.0000 |
1.0000 |
10.00 |
0.0000 |
0.0000 |
10.00 |
0.0609 |
0.2296 |
10.00 |
0.0921 |
0.3112 |
10.00 |
0.1442 |
0.4286 |
10.00 |
0.1821 |
0.4928 |
10.00 |
0.2753 |
0.6246 |
10.00 |
0.3662 |
0.7087 |
10.00 |
0.5213 |
0.8163 |
10.00 |
0.6485 |
0.8814 |
10.00 |
0.7507 |
0.9228 |
10.00 |
0.8352 |
0.9526 |
10.00 |
0.8785 |
0.9657 |
10.00 |
1.0000 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Octanoic acid, methyl ester (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
2.00 |
0.0000 |
389.10 |
2.00 |
0.0599 |
384.54 |
2.00 |
0.0876 |
382.68 |
2.00 |
0.1403 |
379.60 |
2.00 |
0.1772 |
378.05 |
2.00 |
0.2702 |
374.23 |
2.00 |
0.3594 |
370.96 |
2.00 |
0.5113 |
366.72 |
2.00 |
0.6194 |
364.20 |
2.00 |
0.7321 |
362.67 |
2.00 |
0.8258 |
361.11 |
2.00 |
0.8732 |
360.38 |
2.00 |
1.0000 |
356.53 |
6.00 |
0.0000 |
412.93 |
6.00 |
0.0595 |
408.87 |
6.00 |
0.0899 |
406.82 |
6.00 |
0.1437 |
403.53 |
6.00 |
0.1793 |
401.41 |
6.00 |
0.2727 |
397.19 |
6.00 |
0.3640 |
393.96 |
6.00 |
0.5175 |
389.40 |
6.00 |
0.6476 |
386.72 |
6.00 |
0.7441 |
384.71 |
6.00 |
0.8340 |
383.10 |
6.00 |
0.8774 |
382.33 |
6.00 |
1.0000 |
380.50 |
10.00 |
0.0000 |
424.43 |
10.00 |
0.0609 |
421.07 |
10.00 |
0.0921 |
418.71 |
10.00 |
0.1442 |
415.46 |
10.00 |
0.1821 |
413.48 |
10.00 |
0.2753 |
409.12 |
10.00 |
0.3662 |
405.67 |
10.00 |
0.5213 |
401.32 |
10.00 |
0.6485 |
398.43 |
10.00 |
0.7507 |
396.50 |
10.00 |
0.8352 |
394.76 |
10.00 |
0.8785 |
393.92 |
10.00 |
1.0000 |
391.77 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Octanoic acid, methyl ester (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
2.00 |
0.0000 |
389.10 |
2.00 |
0.0599 |
384.54 |
2.00 |
0.0876 |
382.68 |
2.00 |
0.1403 |
379.60 |
2.00 |
0.1772 |
378.05 |
2.00 |
0.2702 |
374.23 |
2.00 |
0.3594 |
370.96 |
2.00 |
0.5113 |
366.72 |
2.00 |
0.6194 |
364.20 |
2.00 |
0.7321 |
362.67 |
2.00 |
0.8258 |
361.11 |
2.00 |
0.8732 |
360.38 |
2.00 |
1.0000 |
356.53 |
6.00 |
0.0000 |
412.93 |
6.00 |
0.0595 |
408.87 |
6.00 |
0.0899 |
406.82 |
6.00 |
0.1437 |
403.53 |
6.00 |
0.1793 |
401.41 |
6.00 |
0.2727 |
397.19 |
6.00 |
0.3640 |
393.96 |
6.00 |
0.5175 |
389.40 |
6.00 |
0.6476 |
386.72 |
6.00 |
0.7441 |
384.71 |
6.00 |
0.8340 |
383.10 |
6.00 |
0.8774 |
382.33 |
6.00 |
1.0000 |
380.50 |
10.00 |
0.0000 |
424.43 |
10.00 |
0.0609 |
421.07 |
10.00 |
0.0921 |
418.71 |
10.00 |
0.1442 |
415.46 |
10.00 |
0.1821 |
413.48 |
10.00 |
0.2753 |
409.12 |
10.00 |
0.3662 |
405.67 |
10.00 |
0.5213 |
401.32 |
10.00 |
0.6485 |
398.43 |
10.00 |
0.7507 |
396.50 |
10.00 |
0.8352 |
394.76 |
10.00 |
0.8785 |
393.92 |
10.00 |
1.0000 |
391.77 |
Sources