Mixture of Propane, 1,3-dibromo- + Butanoic acid, ethyl ester

Datasets

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

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

Operational conditions:

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

Mole fraction of Butanoic acid, ethyl ester (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0406	0.0221
0.0875	0.0343
0.1420	0.0379
0.1949	0.0348
0.2497	0.0241
0.3027	0.0073
0.3525	-0.0111
0.4005	-0.0306
0.4399	-0.0456
0.4453	-0.0477
0.4914	-0.0625
0.5444	-0.0715
0.6028	-0.0776
0.6668	-0.0794
0.7369	-0.0774
0.8067	-0.0673
0.8771	-0.0499

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

Operational conditions:

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

Mole fraction of Butanoic acid, ethyl ester (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0406	0.0221
0.0875	0.0343
0.1420	0.0379
0.1949	0.0348
0.2497	0.0241
0.3027	0.0073
0.3525	-0.0111
0.4005	-0.0306
0.4399	-0.0456
0.4453	-0.0477
0.4914	-0.0625
0.5444	-0.0715
0.6028	-0.0776
0.6668	-0.0794
0.7369	-0.0774
0.8067	-0.0673
0.8771	-0.0499

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, ethyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
0.0436	1908.9
0.0835	1854.01
0.1381	1781.05
0.1859	1719.07
0.2926	1586.65
0.4637	1389.88
0.5238	1324.96
0.6494	1195.57
0.7131	1133.02
0.7811	1068.34
0.8520	1003.1
0.9215	941.15

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, ethyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
0.0436	1908.9
0.0835	1854.01
0.1381	1781.05
0.1859	1719.07
0.2926	1586.65
0.4637	1389.88
0.5238	1324.96
0.6494	1195.57
0.7131	1133.02
0.7811	1068.34
0.8520	1003.1
0.9215	941.15

Sources

• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6