Mixture of 1-Hexene + Propane, 2-methoxy-2-methyl- + Furan, tetrahydro-2-methyl-

Datasets

1. Excess molar enthalpy (molar enthalpy (2)

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Fixed		Measured
Solvent: Amount ratio of component to other component of binary solvent of Furan, tetrahydro-2-methyl- (3) - Liquid	Mole fraction of 1-Hexene (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.3291	0.0500	0.0300
0.3291	0.1000	0.0575
0.3291	0.1557	0.0861
0.3291	0.2002	0.1060
0.3291	0.2499	0.1250
0.3291	0.3002	0.1409
0.3291	0.3496	0.1535
0.3291	0.3997	0.1629
0.3291	0.4502	0.1674
0.3291	0.4996	0.1688
0.3291	0.5500	0.1678
0.3291	0.6001	0.1653
0.3291	0.6498	0.1572
0.3291	0.6998	0.1469
0.3291	0.7506	0.1320
0.3291	0.7991	0.1151
0.3291	0.8499	0.0921
0.3291	0.8999	0.0652
0.3291	0.9500	0.0353
0.9948	0.0499	0.0307
0.9948	0.0999	0.0623
0.9948	0.1511	0.0898
0.9948	0.2000	0.1133
0.9948	0.2502	0.1346
0.9948	0.3005	0.1497
0.9948	0.3502	0.1643
0.9948	0.4003	0.1755
0.9948	0.4498	0.1799
0.9948	0.4994	0.1873
0.9948	0.5499	0.1842
0.9948	0.5996	0.1781
0.9948	0.6496	0.1704
0.9948	0.6998	0.1592
0.9948	0.7495	0.1439
0.9948	0.8003	0.1239
0.9948	0.8499	0.0990
0.9948	0.8999	0.0701
0.9948	0.9500	0.0388
2.9463	0.0499	0.0321
2.9463	0.1001	0.0654
2.9463	0.1497	0.0950
2.9463	0.1997	0.1202
2.9463	0.2502	0.1418
2.9463	0.3004	0.1619
2.9463	0.3503	0.1770
2.9463	0.3998	0.1868
2.9463	0.4504	0.1953
2.9463	0.4997	0.1973
2.9463	0.5499	0.1964
2.9463	0.6002	0.1920
2.9463	0.6497	0.1820
2.9463	0.6997	0.1712
2.9463	0.7500	0.1539
2.9463	0.7999	0.1328
2.9463	0.8498	0.1072
2.9463	0.8999	0.0764
2.9463	0.9500	0.0400

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Fixed		Measured
Solvent: Amount ratio of component to other component of binary solvent of Furan, tetrahydro-2-methyl- (3) - Liquid	Mole fraction of 1-Hexene (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.3291	0.0500	0.0300
0.3291	0.1000	0.0575
0.3291	0.1557	0.0861
0.3291	0.2002	0.1060
0.3291	0.2499	0.1250
0.3291	0.3002	0.1409
0.3291	0.3496	0.1535
0.3291	0.3997	0.1629
0.3291	0.4502	0.1674
0.3291	0.4996	0.1688
0.3291	0.5500	0.1678
0.3291	0.6001	0.1653
0.3291	0.6498	0.1572
0.3291	0.6998	0.1469
0.3291	0.7506	0.1320
0.3291	0.7991	0.1151
0.3291	0.8499	0.0921
0.3291	0.8999	0.0652
0.3291	0.9500	0.0353
0.9948	0.0499	0.0307
0.9948	0.0999	0.0623
0.9948	0.1511	0.0898
0.9948	0.2000	0.1133
0.9948	0.2502	0.1346
0.9948	0.3005	0.1497
0.9948	0.3502	0.1643
0.9948	0.4003	0.1755
0.9948	0.4498	0.1799
0.9948	0.4994	0.1873
0.9948	0.5499	0.1842
0.9948	0.5996	0.1781
0.9948	0.6496	0.1704
0.9948	0.6998	0.1592
0.9948	0.7495	0.1439
0.9948	0.8003	0.1239
0.9948	0.8499	0.0990
0.9948	0.8999	0.0701
0.9948	0.9500	0.0388
2.9463	0.0499	0.0321
2.9463	0.1001	0.0654
2.9463	0.1497	0.0950
2.9463	0.1997	0.1202
2.9463	0.2502	0.1418
2.9463	0.3004	0.1619
2.9463	0.3503	0.1770
2.9463	0.3998	0.1868
2.9463	0.4504	0.1953
2.9463	0.4997	0.1973
2.9463	0.5499	0.1964
2.9463	0.6002	0.1920
2.9463	0.6497	0.1820
2.9463	0.6997	0.1712
2.9463	0.7500	0.1539
2.9463	0.7999	0.1328
2.9463	0.8498	0.1072
2.9463	0.8999	0.0764
2.9463	0.9500	0.0400

Sources

• Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.