Mixture of Decane + Tetrahydrofuran

Datasets

1. Excess molar enthalpy (molar enthalpy (2)
2. T_boil - Boiling temperature at pressure P, K (2)

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101.325 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500	0.1552
0.0999	0.3031
0.1500	0.4350
0.2000	0.5471
0.2503	0.6456
0.3000	0.7312
0.3498	0.8044
0.4002	0.8643
0.4509	0.8958
0.4999	0.9208
0.5499	0.9295
0.6002	0.9219
0.6501	0.8925
0.7003	0.8437
0.7502	0.7740
0.8003	0.6783
0.8502	0.5606
0.9011	0.4102
0.9500	0.2281

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101.325 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500	0.1552
0.0999	0.3031
0.1500	0.4350
0.2000	0.5471
0.2503	0.6456
0.3000	0.7312
0.3498	0.8044
0.4002	0.8643
0.4509	0.8958
0.4999	0.9208
0.5499	0.9295
0.6002	0.9219
0.6501	0.8925
0.7003	0.8437
0.7502	0.7740
0.8003	0.6783
0.8502	0.5606
0.9011	0.4102
0.9500	0.2281

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	445.25
0.2859	380.85
0.4447	364.95
0.5457	357.55
0.7828	345.15
0.9057	340.95
1.0000	337.55

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	445.25
0.2859	380.85
0.4447	364.95
0.5457	357.55
0.7828	345.15
0.9057	340.95
1.0000	337.55

Sources

• Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
• Excess Enthalpies of the Ternary Mixtures: Tetrahydrofuran + (Hexane or Cyclohexane) + Decane at 298.15K