Mixture of 1,3-Propanediamine, N,N-diethyl- + Cyclohexane
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Excess molar volume, m3/mol (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 1,3-Propanediamine, N,N-diethyl- (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.1022 |
0.5900 |
| 0.2027 |
0.8740 |
| 0.3028 |
1.024 |
| 0.3197 |
1.034 |
| 0.3519 |
1.051 |
| 0.3953 |
1.068 |
| 0.4070 |
1.074 |
| 0.4449 |
1.075 |
| 0.4943 |
1.064 |
| 0.5061 |
1.065 |
| 0.5307 |
1.038 |
| 0.5351 |
1.037 |
| 0.5595 |
1.017 |
| 0.5741 |
0.9980 |
| 0.6073 |
0.9520 |
| 0.6523 |
0.8790 |
| 0.7017 |
0.7840 |
| 0.7997 |
0.5480 |
| 0.8696 |
0.3500 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.1022 |
0.5900 |
| 0.2027 |
0.8740 |
| 0.3028 |
1.024 |
| 0.3197 |
1.034 |
| 0.3519 |
1.051 |
| 0.3953 |
1.068 |
| 0.4070 |
1.074 |
| 0.4449 |
1.075 |
| 0.4943 |
1.064 |
| 0.5061 |
1.065 |
| 0.5307 |
1.038 |
| 0.5351 |
1.037 |
| 0.5595 |
1.017 |
| 0.5741 |
0.9980 |
| 0.6073 |
0.9520 |
| 0.6523 |
0.8790 |
| 0.7017 |
0.7840 |
| 0.7997 |
0.5480 |
| 0.8696 |
0.3500 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.1013 |
273.15 |
3.43 |
| 0.1013 |
283.15 |
5.84 |
| 0.1013 |
293.15 |
9.52 |
| 0.1013 |
303.15 |
14.92 |
| 0.1013 |
313.15 |
22.59 |
| 0.1013 |
323.15 |
33.17 |
| 0.1013 |
333.15 |
47.41 |
| 0.1013 |
343.15 |
66.06 |
| 0.1013 |
353.15 |
90.08 |
| 0.1013 |
363.15 |
120.38 |
| 0.2177 |
273.15 |
3.12 |
| 0.2177 |
283.15 |
5.31 |
| 0.2177 |
293.15 |
8.65 |
| 0.2177 |
303.15 |
13.54 |
| 0.2177 |
313.15 |
20.48 |
| 0.2177 |
323.15 |
30.03 |
| 0.2177 |
333.15 |
42.72 |
| 0.2177 |
343.15 |
59.66 |
| 0.2177 |
353.15 |
81.24 |
| 0.2177 |
363.15 |
108.86 |
| 0.3209 |
273.15 |
2.89 |
| 0.3209 |
283.15 |
4.86 |
| 0.3209 |
293.15 |
7.84 |
| 0.3209 |
303.15 |
12.19 |
| 0.3209 |
313.15 |
18.34 |
| 0.3209 |
323.15 |
26.80 |
| 0.3209 |
333.15 |
38.34 |
| 0.3209 |
343.15 |
53.03 |
| 0.3209 |
353.15 |
72.16 |
| 0.3209 |
363.15 |
96.31 |
| 0.4535 |
273.15 |
2.51 |
| 0.4535 |
283.15 |
4.21 |
| 0.4535 |
293.15 |
6.75 |
| 0.4535 |
303.15 |
10.46 |
| 0.4535 |
313.15 |
15.66 |
| 0.4535 |
323.15 |
22.79 |
| 0.4535 |
333.15 |
32.22 |
| 0.4535 |
343.15 |
44.71 |
| 0.4535 |
353.15 |
60.60 |
| 0.4535 |
363.15 |
80.57 |
| 0.6559 |
273.15 |
1.77 |
| 0.6559 |
283.15 |
2.93 |
| 0.6559 |
293.15 |
4.66 |
| 0.6559 |
303.15 |
7.16 |
| 0.6559 |
313.15 |
10.67 |
| 0.6559 |
323.15 |
15.55 |
| 0.6559 |
333.15 |
21.75 |
| 0.6559 |
343.15 |
30.15 |
| 0.6559 |
353.15 |
40.79 |
| 0.6559 |
363.15 |
54.17 |
| 0.8455 |
273.15 |
0.87 |
| 0.8455 |
283.15 |
1.42 |
| 0.8455 |
293.15 |
2.26 |
| 0.8455 |
303.15 |
3.48 |
| 0.8455 |
313.15 |
5.21 |
| 0.8455 |
323.15 |
7.61 |
| 0.8455 |
333.15 |
11.00 |
| 0.8455 |
343.15 |
15.21 |
| 0.8455 |
353.15 |
20.87 |
| 0.8455 |
363.15 |
28.13 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.1013 |
273.15 |
3.43 |
| 0.1013 |
283.15 |
5.84 |
| 0.1013 |
293.15 |
9.52 |
| 0.1013 |
303.15 |
14.92 |
| 0.1013 |
313.15 |
22.59 |
| 0.1013 |
323.15 |
33.17 |
| 0.1013 |
333.15 |
47.41 |
| 0.1013 |
343.15 |
66.06 |
| 0.1013 |
353.15 |
90.08 |
| 0.1013 |
363.15 |
120.38 |
| 0.2177 |
273.15 |
3.12 |
| 0.2177 |
283.15 |
5.31 |
| 0.2177 |
293.15 |
8.65 |
| 0.2177 |
303.15 |
13.54 |
| 0.2177 |
313.15 |
20.48 |
| 0.2177 |
323.15 |
30.03 |
| 0.2177 |
333.15 |
42.72 |
| 0.2177 |
343.15 |
59.66 |
| 0.2177 |
353.15 |
81.24 |
| 0.2177 |
363.15 |
108.86 |
| 0.3209 |
273.15 |
2.89 |
| 0.3209 |
283.15 |
4.86 |
| 0.3209 |
293.15 |
7.84 |
| 0.3209 |
303.15 |
12.19 |
| 0.3209 |
313.15 |
18.34 |
| 0.3209 |
323.15 |
26.80 |
| 0.3209 |
333.15 |
38.34 |
| 0.3209 |
343.15 |
53.03 |
| 0.3209 |
353.15 |
72.16 |
| 0.3209 |
363.15 |
96.31 |
| 0.4535 |
273.15 |
2.51 |
| 0.4535 |
283.15 |
4.21 |
| 0.4535 |
293.15 |
6.75 |
| 0.4535 |
303.15 |
10.46 |
| 0.4535 |
313.15 |
15.66 |
| 0.4535 |
323.15 |
22.79 |
| 0.4535 |
333.15 |
32.22 |
| 0.4535 |
343.15 |
44.71 |
| 0.4535 |
353.15 |
60.60 |
| 0.4535 |
363.15 |
80.57 |
| 0.6559 |
273.15 |
1.77 |
| 0.6559 |
283.15 |
2.93 |
| 0.6559 |
293.15 |
4.66 |
| 0.6559 |
303.15 |
7.16 |
| 0.6559 |
313.15 |
10.67 |
| 0.6559 |
323.15 |
15.55 |
| 0.6559 |
333.15 |
21.75 |
| 0.6559 |
343.15 |
30.15 |
| 0.6559 |
353.15 |
40.79 |
| 0.6559 |
363.15 |
54.17 |
| 0.8455 |
273.15 |
0.87 |
| 0.8455 |
283.15 |
1.42 |
| 0.8455 |
293.15 |
2.26 |
| 0.8455 |
303.15 |
3.48 |
| 0.8455 |
313.15 |
5.21 |
| 0.8455 |
323.15 |
7.61 |
| 0.8455 |
333.15 |
11.00 |
| 0.8455 |
343.15 |
15.21 |
| 0.8455 |
353.15 |
20.87 |
| 0.8455 |
363.15 |
28.13 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
| 0.1130 |
4.5930e-07 |
| 0.2100 |
6.7620e-07 |
| 0.3035 |
7.8040e-07 |
| 0.4030 |
8.0160e-07 |
| 0.4990 |
7.5670e-07 |
| 0.6008 |
6.7850e-07 |
| 0.7025 |
5.3620e-07 |
| 0.7965 |
3.6920e-07 |
| 0.8911 |
2.5450e-07 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of 1,3-Propanediamine, N,N-diethyl- (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
| 0.1130 |
4.5930e-07 |
| 0.2100 |
6.7620e-07 |
| 0.3035 |
7.8040e-07 |
| 0.4030 |
8.0160e-07 |
| 0.4990 |
7.5670e-07 |
| 0.6008 |
6.7850e-07 |
| 0.7025 |
5.3620e-07 |
| 0.7965 |
3.6920e-07 |
| 0.8911 |
2.5450e-07 |
Sources