Mixture of Formic acid, butyl ester + Hexane, 1,6-dichloro-

Datasets

1. Excess molar enthalpy (molar enthalpy (4)
2. ρ_l - Mass density, kg/m3 (4)

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

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0701	0.0539
0.1508	0.0949
0.2299	0.1246
0.3026	0.1389
0.3710	0.1416
0.4340	0.1349
0.4910	0.1216
0.5401	0.1065
0.5778	0.0923
0.6131	0.0835
0.6659	0.0722
0.7195	0.0668
0.7775	0.0573
0.8372	0.0441
0.8968	0.0290
0.9528	0.0131

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

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0950	0.0251
0.1874	0.0412
0.2768	0.0425
0.3583	0.0302
0.4321	0.0055
0.4949	-0.0291
0.5195	-0.0379
0.5526	-0.0541
0.5660	-0.0588
0.6160	-0.0777
0.6674	-0.0869
0.7246	-0.0856
0.7832	-0.0764
0.8346	-0.0657
0.8920	-0.0428
0.9474	-0.0247

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

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0701	0.0539
0.1508	0.0949
0.2299	0.1246
0.3026	0.1389
0.3710	0.1416
0.4340	0.1349
0.4910	0.1216
0.5401	0.1065
0.5778	0.0923
0.6131	0.0835
0.6659	0.0722
0.7195	0.0668
0.7775	0.0573
0.8372	0.0441
0.8968	0.0290
0.9528	0.0131

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

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0950	0.0251
0.1874	0.0412
0.2768	0.0425
0.3583	0.0302
0.4321	0.0055
0.4949	-0.0291
0.5195	-0.0379
0.5526	-0.0541
0.5660	-0.0588
0.6160	-0.0777
0.6674	-0.0869
0.7246	-0.0856
0.7832	-0.0764
0.8346	-0.0657
0.8920	-0.0428
0.9474	-0.0247

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0782	1052.81
0.1483	1042.74
0.2157	1032.73
0.2827	1022.46
0.3478	1012.18
0.4104	1002.02
0.5319	981.37
0.5893	971.18
0.6457	960.88
0.7539	940.28
0.8053	930.03
0.9044	909.61
0.9513	899.53

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0740	1053.56
0.1444	1043.66
0.2217	1032.43
0.2795	1023.76
0.3441	1013.82
0.4081	1003.67
0.5278	983.77
0.5860	973.68
0.6410	963.84
0.7020	952.63
0.7544	942.71
0.8560	922.68
0.9056	912.53
0.9528	902.59

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0782	1052.81
0.1483	1042.74
0.2157	1032.73
0.2827	1022.46
0.3478	1012.18
0.4104	1002.02
0.5319	981.37
0.5893	971.18
0.6457	960.88
0.7539	940.28
0.8053	930.03
0.9044	909.61
0.9513	899.53

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0740	1053.56
0.1444	1043.66
0.2217	1032.43
0.2795	1023.76
0.3441	1013.82
0.4081	1003.67
0.5278	983.77
0.5860	973.68
0.6410	963.84
0.7020	952.63
0.7544	942.71
0.8560	922.68
0.9056	912.53
0.9528	902.59

Sources

• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) V. Hex and Vex for 25 binary mixtures {xCu-1H2u-1CO2CH3 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6