Mixture of Ethane, 1,2-dibromo- + Ethyl Acetate

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 Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0529	0.0259
0.1142	0.0398
0.1754	0.0463
0.2376	0.0433
0.2976	0.0379
0.3548	0.0269
0.4086	0.0117
0.4579	-0.0047
0.5045	-0.0213
0.5360	-0.0344
0.5453	-0.0367
0.5935	-0.0555
0.6556	-0.0699
0.7113	-0.0736
0.7914	-0.0672
0.8635	-0.0499
0.9367	-0.0252

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

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0529	0.0259
0.1142	0.0398
0.1754	0.0463
0.2376	0.0433
0.2976	0.0379
0.3548	0.0269
0.4086	0.0117
0.4579	-0.0047
0.5045	-0.0213
0.5360	-0.0344
0.5453	-0.0367
0.5935	-0.0555
0.6556	-0.0699
0.7113	-0.0736
0.7914	-0.0672
0.8635	-0.0499
0.9367	-0.0252

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.0526	2091.79
0.1032	2019.48
0.1562	1945.11
0.2107	1869.55
0.2686	1790.65
0.4371	1568.65
0.4987	1490.07
0.6182	1341.18
0.6799	1266.02
0.7399	1194.16
0.8065	1115.57
0.8705	1041.22
0.9341	968.46

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.0526	2091.79
0.1032	2019.48
0.1562	1945.11
0.2107	1869.55
0.2686	1790.65
0.4371	1568.65
0.4987	1490.07
0.6182	1341.18
0.6799	1266.02
0.7399	1194.16
0.8065	1115.57
0.8705	1041.22
0.9341	968.46

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