Mixture of 1-Butanol, 3-methyl-, propanoate + 1-Butanol, 3-methyl-
Datasets
-
Mole fraction (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 1-Butanol, 3-methyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of 1-Butanol, 3-methyl- (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1-Butanol, 3-methyl- (2) - Gas |
0.0510 |
50.00 |
0.1430 |
0.1270 |
50.00 |
0.3080 |
0.3060 |
50.00 |
0.5530 |
0.4930 |
50.00 |
0.7090 |
0.6170 |
50.00 |
0.7900 |
0.7820 |
50.00 |
0.8700 |
0.8370 |
50.00 |
0.9020 |
0.8860 |
50.00 |
0.9280 |
0.1160 |
101.33 |
0.2770 |
0.2830 |
101.33 |
0.5320 |
0.3440 |
101.33 |
0.5950 |
0.4950 |
101.33 |
0.7130 |
0.5840 |
101.33 |
0.7710 |
0.6450 |
101.33 |
0.8080 |
0.7610 |
101.33 |
0.8720 |
0.8850 |
101.33 |
0.9350 |
0.1070 |
150.00 |
0.2580 |
0.1880 |
150.00 |
0.3980 |
0.2700 |
150.00 |
0.5110 |
0.3570 |
150.00 |
0.6110 |
0.5580 |
150.00 |
0.7630 |
0.6520 |
150.00 |
0.8170 |
0.7270 |
150.00 |
0.8570 |
0.8530 |
150.00 |
0.9220 |
Mole fraction of 1-Butanol, 3-methyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of 1-Butanol, 3-methyl- (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1-Butanol, 3-methyl- (2) - Gas |
0.0510 |
50.00 |
0.1430 |
0.1270 |
50.00 |
0.3080 |
0.3060 |
50.00 |
0.5530 |
0.4930 |
50.00 |
0.7090 |
0.6170 |
50.00 |
0.7900 |
0.7820 |
50.00 |
0.8700 |
0.8370 |
50.00 |
0.9020 |
0.8860 |
50.00 |
0.9280 |
0.1160 |
101.33 |
0.2770 |
0.2830 |
101.33 |
0.5320 |
0.3440 |
101.33 |
0.5950 |
0.4950 |
101.33 |
0.7130 |
0.5840 |
101.33 |
0.7710 |
0.6450 |
101.33 |
0.8080 |
0.7610 |
101.33 |
0.8720 |
0.8850 |
101.33 |
0.9350 |
0.1070 |
150.00 |
0.2580 |
0.1880 |
150.00 |
0.3980 |
0.2700 |
150.00 |
0.5110 |
0.3570 |
150.00 |
0.6110 |
0.5580 |
150.00 |
0.7630 |
0.6520 |
150.00 |
0.8170 |
0.7270 |
150.00 |
0.8570 |
0.8530 |
150.00 |
0.9220 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1-Butanol, 3-methyl- (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0510 |
50.00 |
405.28 |
0.1270 |
50.00 |
401.13 |
0.3060 |
50.00 |
394.39 |
0.4930 |
50.00 |
389.74 |
0.6170 |
50.00 |
387.93 |
0.7820 |
50.00 |
386.26 |
0.8370 |
50.00 |
385.94 |
0.8860 |
50.00 |
385.55 |
0.1160 |
101.33 |
424.67 |
0.2830 |
101.33 |
417.52 |
0.3440 |
101.33 |
415.02 |
0.4950 |
101.33 |
410.53 |
0.5840 |
101.33 |
409.13 |
0.6450 |
101.33 |
407.88 |
0.7610 |
101.33 |
406.71 |
0.8850 |
101.33 |
405.31 |
0.1070 |
150.00 |
441.14 |
0.1880 |
150.00 |
436.18 |
0.2700 |
150.00 |
431.82 |
0.3570 |
150.00 |
428.08 |
0.5580 |
150.00 |
421.78 |
0.6520 |
150.00 |
420.40 |
0.7270 |
150.00 |
419.88 |
0.8530 |
150.00 |
417.70 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1-Butanol, 3-methyl- (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0510 |
50.00 |
405.28 |
0.1270 |
50.00 |
401.13 |
0.3060 |
50.00 |
394.39 |
0.4930 |
50.00 |
389.74 |
0.6170 |
50.00 |
387.93 |
0.7820 |
50.00 |
386.26 |
0.8370 |
50.00 |
385.94 |
0.8860 |
50.00 |
385.55 |
0.1160 |
101.33 |
424.67 |
0.2830 |
101.33 |
417.52 |
0.3440 |
101.33 |
415.02 |
0.4950 |
101.33 |
410.53 |
0.5840 |
101.33 |
409.13 |
0.6450 |
101.33 |
407.88 |
0.7610 |
101.33 |
406.71 |
0.8850 |
101.33 |
405.31 |
0.1070 |
150.00 |
441.14 |
0.1880 |
150.00 |
436.18 |
0.2700 |
150.00 |
431.82 |
0.3570 |
150.00 |
428.08 |
0.5580 |
150.00 |
421.78 |
0.6520 |
150.00 |
420.40 |
0.7270 |
150.00 |
419.88 |
0.8530 |
150.00 |
417.70 |
Sources