Datasets
-
Activity coefficient (4)
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Activity coefficient of Toluene (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Toluene (1) - Liquid |
| 353.15 |
1.14 |
| 373.15 |
1.13 |
| 393.15 |
1.06 |
Activity coefficient of Cyclohexylamine (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Cyclohexylamine (2) - Liquid |
| 353.15 |
1.19 |
| 373.15 |
1.12 |
Activity coefficient of Toluene (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Toluene (1) - Liquid |
| 353.15 |
1.14 |
| 373.15 |
1.13 |
| 393.15 |
1.06 |
Activity coefficient of Cyclohexylamine (2)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Cyclohexylamine (2) - Liquid |
| 353.15 |
1.19 |
| 373.15 |
1.12 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Mole fraction of Toluene (1) - Liquid |
Temperature, K - Gas |
Mole fraction of Toluene (1) - Gas |
| 0.0000 |
333.15 |
0.0000 |
| 0.0000 |
363.15 |
0.0000 |
| 0.0810 |
363.15 |
0.1540 |
| 0.0950 |
333.15 |
0.2430 |
| 0.1850 |
363.15 |
0.3620 |
| 0.2420 |
363.15 |
0.4370 |
| 0.2510 |
333.15 |
0.4860 |
| 0.3010 |
363.15 |
0.5070 |
| 0.3050 |
333.15 |
0.5670 |
| 0.3700 |
363.15 |
0.5820 |
| 0.3740 |
333.15 |
0.6390 |
| 0.4490 |
363.15 |
0.6450 |
| 0.4570 |
333.15 |
0.7080 |
| 0.5220 |
363.15 |
0.7030 |
| 0.5350 |
333.15 |
0.7390 |
| 0.6030 |
363.15 |
0.7660 |
| 0.6230 |
333.15 |
0.8150 |
| 0.7180 |
363.15 |
0.8330 |
| 0.7980 |
363.15 |
0.8850 |
| 0.7990 |
333.15 |
0.8950 |
| 0.9030 |
363.15 |
0.9430 |
| 1.0000 |
333.15 |
1.0000 |
| 1.0000 |
363.15 |
1.0000 |
Mole fraction of Toluene (1)
[ref]
| Fixed |
Measured |
| Mole fraction of Toluene (1) - Liquid |
Temperature, K - Gas |
Mole fraction of Toluene (1) - Gas |
| 0.0000 |
333.15 |
0.0000 |
| 0.0000 |
363.15 |
0.0000 |
| 0.0810 |
363.15 |
0.1540 |
| 0.0950 |
333.15 |
0.2430 |
| 0.1850 |
363.15 |
0.3620 |
| 0.2420 |
363.15 |
0.4370 |
| 0.2510 |
333.15 |
0.4860 |
| 0.3010 |
363.15 |
0.5070 |
| 0.3050 |
333.15 |
0.5670 |
| 0.3700 |
363.15 |
0.5820 |
| 0.3740 |
333.15 |
0.6390 |
| 0.4490 |
363.15 |
0.6450 |
| 0.4570 |
333.15 |
0.7080 |
| 0.5220 |
363.15 |
0.7030 |
| 0.5350 |
333.15 |
0.7390 |
| 0.6030 |
363.15 |
0.7660 |
| 0.6230 |
333.15 |
0.8150 |
| 0.7180 |
363.15 |
0.8330 |
| 0.7980 |
363.15 |
0.8850 |
| 0.7990 |
333.15 |
0.8950 |
| 0.9030 |
363.15 |
0.9430 |
| 1.0000 |
333.15 |
1.0000 |
| 1.0000 |
363.15 |
1.0000 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Toluene (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
333.15 |
7.51 |
| 0.0000 |
363.15 |
25.59 |
| 0.0810 |
363.15 |
28.53 |
| 0.0950 |
333.15 |
8.78 |
| 0.1850 |
363.15 |
31.66 |
| 0.2420 |
363.15 |
33.58 |
| 0.2510 |
333.15 |
10.71 |
| 0.3010 |
363.15 |
35.48 |
| 0.3050 |
333.15 |
11.43 |
| 0.3700 |
363.15 |
37.47 |
| 0.3740 |
333.15 |
12.27 |
| 0.4490 |
363.15 |
39.89 |
| 0.4570 |
333.15 |
13.16 |
| 0.5220 |
363.15 |
41.97 |
| 0.5350 |
333.15 |
13.99 |
| 0.6030 |
363.15 |
44.29 |
| 0.6230 |
333.15 |
14.94 |
| 0.7180 |
363.15 |
47.42 |
| 0.7980 |
363.15 |
49.63 |
| 0.7990 |
333.15 |
16.76 |
| 0.9030 |
363.15 |
52.41 |
| 1.0000 |
333.15 |
18.56 |
| 1.0000 |
363.15 |
54.49 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Toluene (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
333.15 |
7.51 |
| 0.0000 |
363.15 |
25.59 |
| 0.0810 |
363.15 |
28.53 |
| 0.0950 |
333.15 |
8.78 |
| 0.1850 |
363.15 |
31.66 |
| 0.2420 |
363.15 |
33.58 |
| 0.2510 |
333.15 |
10.71 |
| 0.3010 |
363.15 |
35.48 |
| 0.3050 |
333.15 |
11.43 |
| 0.3700 |
363.15 |
37.47 |
| 0.3740 |
333.15 |
12.27 |
| 0.4490 |
363.15 |
39.89 |
| 0.4570 |
333.15 |
13.16 |
| 0.5220 |
363.15 |
41.97 |
| 0.5350 |
333.15 |
13.99 |
| 0.6030 |
363.15 |
44.29 |
| 0.6230 |
333.15 |
14.94 |
| 0.7180 |
363.15 |
47.42 |
| 0.7980 |
363.15 |
49.63 |
| 0.7990 |
333.15 |
16.76 |
| 0.9030 |
363.15 |
52.41 |
| 1.0000 |
333.15 |
18.56 |
| 1.0000 |
363.15 |
54.49 |
Sources