Mixture of Benzene + Diisopropyl ether + Heptane

Datasets

1. Excess molar enthalpy (molar enthalpy (2)

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

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Benzene (1) - Liquid	Mole fraction of Heptane (3) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2196	0.6650	0.1335
0.1953	0.5920	0.2364
0.1722	0.5220	0.3493
0.1455	0.4410	0.3856
0.1117	0.3390	0.3853
0.0876	0.2660	0.3520
0.0532	0.1610	0.2489
0.0349	0.1060	0.1600
0.4450	0.4450	0.2390
0.3980	0.3980	0.3792
0.3530	0.3530	0.4653
0.3000	0.3000	0.5303
0.2330	0.2330	0.5268
0.1830	0.1830	0.4555
0.1120	0.1120	0.2893
0.0740	0.0740	0.1730
0.6790	0.2170	0.3325
0.6110	0.1960	0.4911
0.5460	0.1740	0.5856
0.4670	0.1490	0.6290
0.3650	0.1170	0.5793
0.2900	0.0930	0.4899
0.1790	0.0570	0.2610
0.1180	0.0380	0.1559

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

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Benzene (1) - Liquid	Mole fraction of Heptane (3) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2196	0.6650	0.1335
0.1953	0.5920	0.2364
0.1722	0.5220	0.3493
0.1455	0.4410	0.3856
0.1117	0.3390	0.3853
0.0876	0.2660	0.3520
0.0532	0.1610	0.2489
0.0349	0.1060	0.1600
0.4450	0.4450	0.2390
0.3980	0.3980	0.3792
0.3530	0.3530	0.4653
0.3000	0.3000	0.5303
0.2330	0.2330	0.5268
0.1830	0.1830	0.4555
0.1120	0.1120	0.2893
0.0740	0.0740	0.1730
0.6790	0.2170	0.3325
0.6110	0.1960	0.4911
0.5460	0.1740	0.5856
0.4670	0.1490	0.6290
0.3650	0.1170	0.5793
0.2900	0.0930	0.4899
0.1790	0.0570	0.2610
0.1180	0.0380	0.1559

Sources

• Correlation and prediction of the phase behavior and thermal properties of binary and ternary systems of 2,2 -oxybis[propane] + benzene, toluene, cyclohexane or n-heptane