Datasets
-
Mole fraction (10)
-
Liquid-liquid equilibrium temperature, K (2)
-
Pvap - Vapor or sublimation pressure, kPa (4)
-
Azeotropic pressure, kPa (2)
Mole fraction of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 298.2 (Liquid mixture 1)
Mole fraction of Water (2) - Liquid mixture 1 |
0.9957 |
0.9959 |
Mole fraction of Water (2)
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid mixture 2)
- Pressure, kPa = 101.3 (Liquid mixture 2)
Mole fraction of Water (2) - Liquid mixture 2 |
0.2385 |
0.2372 |
Azeotropic composition: mole fraction of Benzenemethanol, «alpha»-methyl- (1)
[ref]
Temperature, K - Liquid |
Azeotropic composition: mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid |
293.15 |
0.0022 |
303.15 |
0.0028 |
313.15 |
0.0032 |
323.15 |
0.0040 |
333.15 |
0.0050 |
343.15 |
0.0060 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
298.20 |
0.9734 |
318.20 |
0.9756 |
328.20 |
0.9761 |
308.20 |
0.9742 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
298.20 |
0.0536 |
318.20 |
0.0681 |
328.20 |
0.0676 |
308.20 |
0.0613 |
Mole fraction of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 298.2 (Liquid mixture 1)
Mole fraction of Water (2) - Liquid mixture 1 |
0.9957 |
0.9959 |
Mole fraction of Water (2)
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid mixture 2)
- Pressure, kPa = 101.3 (Liquid mixture 2)
Mole fraction of Water (2) - Liquid mixture 2 |
0.2385 |
0.2372 |
Azeotropic composition: mole fraction of Benzenemethanol, «alpha»-methyl- (1)
[ref]
Temperature, K - Liquid |
Azeotropic composition: mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid |
293.15 |
0.0022 |
303.15 |
0.0028 |
313.15 |
0.0032 |
323.15 |
0.0040 |
333.15 |
0.0050 |
343.15 |
0.0060 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
298.20 |
0.9734 |
318.20 |
0.9756 |
328.20 |
0.9761 |
308.20 |
0.9742 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
298.20 |
0.0536 |
318.20 |
0.0681 |
328.20 |
0.0676 |
308.20 |
0.0613 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.0097 |
365.87 |
0.4588 |
401.08 |
0.5457 |
379.11 |
0.5646 |
368.05 |
0.7624 |
293.00 |
0.7896 |
287.73 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.0097 |
365.87 |
0.4588 |
401.08 |
0.5457 |
379.11 |
0.5646 |
368.05 |
0.7624 |
293.00 |
0.7896 |
287.73 |
Vapor or sublimation pressure, kPa
[ref]
Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
293.15 |
2.39 |
293.15 |
2.29 |
293.15 |
2.33 |
293.15 |
2.34 |
293.15 |
2.36 |
293.15 |
2.37 |
293.15 |
2.39 |
293.15 |
2.38 |
293.15 |
2.36 |
293.15 |
2.27 |
293.15 |
2.41 |
293.15 |
2.19 |
303.15 |
4.33 |
303.15 |
4.19 |
303.15 |
4.25 |
303.15 |
4.25 |
303.15 |
4.27 |
303.15 |
4.28 |
303.15 |
4.31 |
303.15 |
4.31 |
303.15 |
4.27 |
303.15 |
4.24 |
303.15 |
4.19 |
303.15 |
4.35 |
313.15 |
7.50 |
313.15 |
7.32 |
313.15 |
7.41 |
313.15 |
7.39 |
313.15 |
7.41 |
313.15 |
7.42 |
313.15 |
7.47 |
313.15 |
7.46 |
313.15 |
7.40 |
313.15 |
7.34 |
313.15 |
7.47 |
323.15 |
12.49 |
323.15 |
12.30 |
323.15 |
12.41 |
323.15 |
12.37 |
323.15 |
12.38 |
323.15 |
12.38 |
323.15 |
12.45 |
323.15 |
12.45 |
323.15 |
12.35 |
323.15 |
12.32 |
323.15 |
12.34 |
333.15 |
20.10 |
333.15 |
19.92 |
333.15 |
20.05 |
333.15 |
20.00 |
333.15 |
19.98 |
333.15 |
19.97 |
333.15 |
20.06 |
333.15 |
20.07 |
333.15 |
19.91 |
333.15 |
19.89 |
333.15 |
19.95 |
343.15 |
31.35 |
343.15 |
31.23 |
343.15 |
31.36 |
343.15 |
31.33 |
343.15 |
31.26 |
343.15 |
31.25 |
343.15 |
31.37 |
343.15 |
31.40 |
343.15 |
31.14 |
343.15 |
31.15 |
353.15 |
47.52 |
353.15 |
47.56 |
353.15 |
47.66 |
353.15 |
47.73 |
353.15 |
47.55 |
353.15 |
47.55 |
353.15 |
47.72 |
353.15 |
47.60 |
353.15 |
47.36 |
353.15 |
47.34 |
353.15 |
47.18 |
363.15 |
70.22 |
363.15 |
70.52 |
363.15 |
70.53 |
363.15 |
70.86 |
363.15 |
70.52 |
363.15 |
70.54 |
363.15 |
70.79 |
363.15 |
70.60 |
363.15 |
70.23 |
363.15 |
70.20 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.0000 |
2.33 |
293.15 |
0.8722 |
1.45 |
293.15 |
1.0000 |
0.01 |
303.15 |
0.0000 |
4.24 |
303.15 |
0.7629 |
3.83 |
303.15 |
0.8720 |
2.53 |
303.15 |
1.0000 |
0.02 |
313.15 |
0.0000 |
7.38 |
313.15 |
0.7635 |
6.43 |
313.15 |
0.8723 |
4.22 |
313.15 |
1.0000 |
0.04 |
323.15 |
0.0000 |
12.34 |
323.15 |
0.6609 |
12.29 |
323.15 |
0.7645 |
10.38 |
323.15 |
0.8731 |
6.75 |
323.15 |
1.0000 |
0.10 |
333.15 |
0.0000 |
19.92 |
333.15 |
0.6623 |
19.44 |
333.15 |
0.7659 |
16.17 |
333.15 |
0.8743 |
10.42 |
333.15 |
1.0000 |
0.20 |
343.15 |
0.0000 |
31.17 |
343.15 |
0.6643 |
29.70 |
343.15 |
0.7678 |
24.44 |
343.15 |
0.8760 |
15.58 |
343.15 |
1.0000 |
0.40 |
353.15 |
0.0000 |
47.38 |
353.15 |
0.6668 |
44.00 |
353.15 |
0.7702 |
35.91 |
353.15 |
0.8782 |
22.64 |
353.15 |
1.0000 |
0.76 |
363.15 |
0.0000 |
70.18 |
363.15 |
0.5855 |
69.50 |
363.15 |
0.6698 |
63.42 |
363.15 |
0.7730 |
51.47 |
363.15 |
0.8809 |
32.06 |
363.15 |
1.0000 |
1.35 |
Vapor or sublimation pressure, kPa
[ref]
Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
293.15 |
2.39 |
293.15 |
2.29 |
293.15 |
2.33 |
293.15 |
2.34 |
293.15 |
2.36 |
293.15 |
2.37 |
293.15 |
2.39 |
293.15 |
2.38 |
293.15 |
2.36 |
293.15 |
2.27 |
293.15 |
2.41 |
293.15 |
2.19 |
303.15 |
4.33 |
303.15 |
4.19 |
303.15 |
4.25 |
303.15 |
4.25 |
303.15 |
4.27 |
303.15 |
4.28 |
303.15 |
4.31 |
303.15 |
4.31 |
303.15 |
4.27 |
303.15 |
4.24 |
303.15 |
4.19 |
303.15 |
4.35 |
313.15 |
7.50 |
313.15 |
7.32 |
313.15 |
7.41 |
313.15 |
7.39 |
313.15 |
7.41 |
313.15 |
7.42 |
313.15 |
7.47 |
313.15 |
7.46 |
313.15 |
7.40 |
313.15 |
7.34 |
313.15 |
7.47 |
323.15 |
12.49 |
323.15 |
12.30 |
323.15 |
12.41 |
323.15 |
12.37 |
323.15 |
12.38 |
323.15 |
12.38 |
323.15 |
12.45 |
323.15 |
12.45 |
323.15 |
12.35 |
323.15 |
12.32 |
323.15 |
12.34 |
333.15 |
20.10 |
333.15 |
19.92 |
333.15 |
20.05 |
333.15 |
20.00 |
333.15 |
19.98 |
333.15 |
19.97 |
333.15 |
20.06 |
333.15 |
20.07 |
333.15 |
19.91 |
333.15 |
19.89 |
333.15 |
19.95 |
343.15 |
31.35 |
343.15 |
31.23 |
343.15 |
31.36 |
343.15 |
31.33 |
343.15 |
31.26 |
343.15 |
31.25 |
343.15 |
31.37 |
343.15 |
31.40 |
343.15 |
31.14 |
343.15 |
31.15 |
353.15 |
47.52 |
353.15 |
47.56 |
353.15 |
47.66 |
353.15 |
47.73 |
353.15 |
47.55 |
353.15 |
47.55 |
353.15 |
47.72 |
353.15 |
47.60 |
353.15 |
47.36 |
353.15 |
47.34 |
353.15 |
47.18 |
363.15 |
70.22 |
363.15 |
70.52 |
363.15 |
70.53 |
363.15 |
70.86 |
363.15 |
70.52 |
363.15 |
70.54 |
363.15 |
70.79 |
363.15 |
70.60 |
363.15 |
70.23 |
363.15 |
70.20 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.0000 |
2.33 |
293.15 |
0.8722 |
1.45 |
293.15 |
1.0000 |
0.01 |
303.15 |
0.0000 |
4.24 |
303.15 |
0.7629 |
3.83 |
303.15 |
0.8720 |
2.53 |
303.15 |
1.0000 |
0.02 |
313.15 |
0.0000 |
7.38 |
313.15 |
0.7635 |
6.43 |
313.15 |
0.8723 |
4.22 |
313.15 |
1.0000 |
0.04 |
323.15 |
0.0000 |
12.34 |
323.15 |
0.6609 |
12.29 |
323.15 |
0.7645 |
10.38 |
323.15 |
0.8731 |
6.75 |
323.15 |
1.0000 |
0.10 |
333.15 |
0.0000 |
19.92 |
333.15 |
0.6623 |
19.44 |
333.15 |
0.7659 |
16.17 |
333.15 |
0.8743 |
10.42 |
333.15 |
1.0000 |
0.20 |
343.15 |
0.0000 |
31.17 |
343.15 |
0.6643 |
29.70 |
343.15 |
0.7678 |
24.44 |
343.15 |
0.8760 |
15.58 |
343.15 |
1.0000 |
0.40 |
353.15 |
0.0000 |
47.38 |
353.15 |
0.6668 |
44.00 |
353.15 |
0.7702 |
35.91 |
353.15 |
0.8782 |
22.64 |
353.15 |
1.0000 |
0.76 |
363.15 |
0.0000 |
70.18 |
363.15 |
0.5855 |
69.50 |
363.15 |
0.6698 |
63.42 |
363.15 |
0.7730 |
51.47 |
363.15 |
0.8809 |
32.06 |
363.15 |
1.0000 |
1.35 |
Azeotropic pressure, kPa
[ref]
Temperature, K - Liquid |
Azeotropic pressure, kPa - Liquid |
293.15 |
2.35 |
303.15 |
4.27 |
313.15 |
7.41 |
323.15 |
12.39 |
333.15 |
20.00 |
343.15 |
31.29 |
Azeotropic pressure, kPa
[ref]
Temperature, K - Liquid |
Azeotropic pressure, kPa - Liquid |
293.15 |
2.35 |
303.15 |
4.27 |
313.15 |
7.41 |
323.15 |
12.39 |
333.15 |
20.00 |
343.15 |
31.29 |
Sources