Mixture of Cyclohexane + 1,2-Ethanediamine, N,N-diethyl-
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.1053 |
0.4880 |
0.2026 |
0.7700 |
0.2548 |
0.8670 |
0.3243 |
0.9520 |
0.3621 |
0.9740 |
0.4196 |
0.9880 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.1053 |
0.4880 |
0.2026 |
0.7700 |
0.2548 |
0.8670 |
0.3243 |
0.9520 |
0.3621 |
0.9740 |
0.4196 |
0.9880 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
273.15 |
0.1222 |
3.38 |
273.15 |
0.2567 |
3.07 |
273.15 |
0.3985 |
2.73 |
273.15 |
0.5410 |
2.32 |
273.15 |
0.6788 |
1.80 |
273.15 |
0.8001 |
1.28 |
273.15 |
0.8994 |
0.78 |
283.15 |
0.1222 |
5.76 |
283.15 |
0.2567 |
5.22 |
283.15 |
0.3985 |
4.62 |
283.15 |
0.5410 |
3.90 |
283.15 |
0.6788 |
3.01 |
283.15 |
0.8001 |
2.15 |
283.15 |
0.8994 |
1.33 |
293.15 |
0.1222 |
9.39 |
293.15 |
0.2567 |
8.51 |
293.15 |
0.3985 |
7.48 |
293.15 |
0.5410 |
6.30 |
293.15 |
0.6788 |
4.85 |
293.15 |
0.8001 |
3.48 |
293.15 |
0.8994 |
2.18 |
298.15 |
0.1222 |
11.82 |
298.15 |
0.2567 |
10.70 |
298.15 |
0.3985 |
9.39 |
298.15 |
0.5410 |
7.90 |
298.15 |
0.6788 |
6.08 |
298.15 |
0.8001 |
4.37 |
298.15 |
0.8994 |
2.76 |
303.15 |
0.1222 |
14.74 |
303.15 |
0.2567 |
13.33 |
303.15 |
0.3985 |
11.68 |
303.15 |
0.5410 |
9.81 |
303.15 |
0.6788 |
7.55 |
303.15 |
0.8001 |
5.44 |
303.15 |
0.8994 |
3.47 |
313.15 |
0.1222 |
22.35 |
313.15 |
0.2567 |
20.19 |
313.15 |
0.3985 |
17.63 |
313.15 |
0.5410 |
14.79 |
313.15 |
0.6788 |
11.39 |
313.15 |
0.8001 |
8.26 |
313.15 |
0.8994 |
5.37 |
323.15 |
0.1222 |
32.89 |
323.15 |
0.2567 |
29.68 |
323.15 |
0.3985 |
25.85 |
323.15 |
0.5410 |
21.65 |
323.15 |
0.6788 |
16.70 |
323.15 |
0.8001 |
12.19 |
323.15 |
0.8994 |
8.08 |
333.15 |
0.1222 |
47.09 |
333.15 |
0.2567 |
42.47 |
333.15 |
0.3985 |
36.90 |
333.15 |
0.5410 |
30.89 |
333.15 |
0.6788 |
23.87 |
333.15 |
0.8001 |
17.56 |
333.15 |
0.8994 |
11.87 |
343.15 |
0.1222 |
65.80 |
343.15 |
0.2567 |
59.30 |
343.15 |
0.3985 |
51.44 |
343.15 |
0.5410 |
43.04 |
343.15 |
0.6788 |
33.35 |
343.15 |
0.8001 |
24.74 |
343.15 |
0.8994 |
17.06 |
353.15 |
0.1222 |
89.93 |
353.15 |
0.2567 |
81.02 |
353.15 |
0.3985 |
70.17 |
353.15 |
0.5410 |
58.70 |
353.15 |
0.6788 |
45.63 |
353.15 |
0.8001 |
34.14 |
353.15 |
0.8994 |
24.02 |
363.15 |
0.1222 |
120.50 |
363.15 |
0.2567 |
108.52 |
363.15 |
0.3985 |
93.87 |
363.15 |
0.5410 |
78.55 |
363.15 |
0.6788 |
61.26 |
363.15 |
0.8001 |
46.23 |
363.15 |
0.8994 |
33.20 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,2-Ethanediamine, N,N-diethyl- (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
273.15 |
0.1222 |
3.38 |
273.15 |
0.2567 |
3.07 |
273.15 |
0.3985 |
2.73 |
273.15 |
0.5410 |
2.32 |
273.15 |
0.6788 |
1.80 |
273.15 |
0.8001 |
1.28 |
273.15 |
0.8994 |
0.78 |
283.15 |
0.1222 |
5.76 |
283.15 |
0.2567 |
5.22 |
283.15 |
0.3985 |
4.62 |
283.15 |
0.5410 |
3.90 |
283.15 |
0.6788 |
3.01 |
283.15 |
0.8001 |
2.15 |
283.15 |
0.8994 |
1.33 |
293.15 |
0.1222 |
9.39 |
293.15 |
0.2567 |
8.51 |
293.15 |
0.3985 |
7.48 |
293.15 |
0.5410 |
6.30 |
293.15 |
0.6788 |
4.85 |
293.15 |
0.8001 |
3.48 |
293.15 |
0.8994 |
2.18 |
298.15 |
0.1222 |
11.82 |
298.15 |
0.2567 |
10.70 |
298.15 |
0.3985 |
9.39 |
298.15 |
0.5410 |
7.90 |
298.15 |
0.6788 |
6.08 |
298.15 |
0.8001 |
4.37 |
298.15 |
0.8994 |
2.76 |
303.15 |
0.1222 |
14.74 |
303.15 |
0.2567 |
13.33 |
303.15 |
0.3985 |
11.68 |
303.15 |
0.5410 |
9.81 |
303.15 |
0.6788 |
7.55 |
303.15 |
0.8001 |
5.44 |
303.15 |
0.8994 |
3.47 |
313.15 |
0.1222 |
22.35 |
313.15 |
0.2567 |
20.19 |
313.15 |
0.3985 |
17.63 |
313.15 |
0.5410 |
14.79 |
313.15 |
0.6788 |
11.39 |
313.15 |
0.8001 |
8.26 |
313.15 |
0.8994 |
5.37 |
323.15 |
0.1222 |
32.89 |
323.15 |
0.2567 |
29.68 |
323.15 |
0.3985 |
25.85 |
323.15 |
0.5410 |
21.65 |
323.15 |
0.6788 |
16.70 |
323.15 |
0.8001 |
12.19 |
323.15 |
0.8994 |
8.08 |
333.15 |
0.1222 |
47.09 |
333.15 |
0.2567 |
42.47 |
333.15 |
0.3985 |
36.90 |
333.15 |
0.5410 |
30.89 |
333.15 |
0.6788 |
23.87 |
333.15 |
0.8001 |
17.56 |
333.15 |
0.8994 |
11.87 |
343.15 |
0.1222 |
65.80 |
343.15 |
0.2567 |
59.30 |
343.15 |
0.3985 |
51.44 |
343.15 |
0.5410 |
43.04 |
343.15 |
0.6788 |
33.35 |
343.15 |
0.8001 |
24.74 |
343.15 |
0.8994 |
17.06 |
353.15 |
0.1222 |
89.93 |
353.15 |
0.2567 |
81.02 |
353.15 |
0.3985 |
70.17 |
353.15 |
0.5410 |
58.70 |
353.15 |
0.6788 |
45.63 |
353.15 |
0.8001 |
34.14 |
353.15 |
0.8994 |
24.02 |
363.15 |
0.1222 |
120.50 |
363.15 |
0.2567 |
108.52 |
363.15 |
0.3985 |
93.87 |
363.15 |
0.5410 |
78.55 |
363.15 |
0.6788 |
61.26 |
363.15 |
0.8001 |
46.23 |
363.15 |
0.8994 |
33.20 |
Sources