Datasets
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Excess molar enthalpy (molar enthalpy (4)
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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 Diisopropyl ether (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0890 |
0.0450 |
0.1400 |
0.1179 |
0.1920 |
0.1952 |
0.2540 |
0.2893 |
0.3090 |
0.3654 |
0.3390 |
0.3996 |
0.3750 |
0.4185 |
0.4310 |
0.4445 |
0.5050 |
0.4623 |
0.6010 |
0.4598 |
0.6370 |
0.4606 |
0.7030 |
0.4421 |
0.7690 |
0.4140 |
0.8040 |
0.3963 |
0.8440 |
0.3582 |
0.9230 |
0.2381 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.5000 |
101.00 |
303.15 |
0.4669 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
Mole fraction of Diisopropyl ether (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0890 |
0.0450 |
0.1400 |
0.1179 |
0.1920 |
0.1952 |
0.2540 |
0.2893 |
0.3090 |
0.3654 |
0.3390 |
0.3996 |
0.3750 |
0.4185 |
0.4310 |
0.4445 |
0.5050 |
0.4623 |
0.6010 |
0.4598 |
0.6370 |
0.4606 |
0.7030 |
0.4421 |
0.7690 |
0.4140 |
0.8040 |
0.3963 |
0.8440 |
0.3582 |
0.9230 |
0.2381 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.5000 |
101.00 |
303.15 |
0.4669 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Diisopropyl ether (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
4.00 |
0.0582 |
8.05 |
0.1047 |
10.98 |
0.1562 |
13.89 |
0.2026 |
16.20 |
0.2497 |
18.30 |
0.3012 |
20.33 |
0.3027 |
20.39 |
0.3486 |
21.98 |
0.3998 |
23.59 |
0.4041 |
23.74 |
0.4445 |
24.85 |
0.4511 |
25.06 |
0.4993 |
26.27 |
0.5013 |
26.34 |
0.5492 |
27.45 |
0.5516 |
27.52 |
0.5998 |
28.56 |
0.6037 |
28.65 |
0.6484 |
29.57 |
0.6870 |
30.32 |
0.7004 |
30.59 |
0.7506 |
31.59 |
0.8008 |
32.58 |
0.8502 |
33.59 |
0.9006 |
34.68 |
0.9505 |
35.85 |
1.0000 |
37.11 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Diisopropyl ether (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
4.00 |
0.0582 |
8.05 |
0.1047 |
10.98 |
0.1562 |
13.89 |
0.2026 |
16.20 |
0.2497 |
18.30 |
0.3012 |
20.33 |
0.3027 |
20.39 |
0.3486 |
21.98 |
0.3998 |
23.59 |
0.4041 |
23.74 |
0.4445 |
24.85 |
0.4511 |
25.06 |
0.4993 |
26.27 |
0.5013 |
26.34 |
0.5492 |
27.45 |
0.5516 |
27.52 |
0.5998 |
28.56 |
0.6037 |
28.65 |
0.6484 |
29.57 |
0.6870 |
30.32 |
0.7004 |
30.59 |
0.7506 |
31.59 |
0.8008 |
32.58 |
0.8502 |
33.59 |
0.9006 |
34.68 |
0.9505 |
35.85 |
1.0000 |
37.11 |
Sources