Mixture of Acetic acid + 1,2-Ethanediol, monoacetate

Datasets

1. Excess molar enthalpy (molar enthalpy (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)

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

Operational conditions:

• Temperature, K = 323.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetic acid (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0798	-0.1010
0.1906	-0.2100
0.2919	-0.2660
0.4140	-0.2780
0.5236	-0.2410
0.6224	-0.1830
0.7332	-0.0931
0.8318	-0.0135
0.9203	0.0286

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

Operational conditions:

• Temperature, K = 323.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetic acid (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0798	-0.1010
0.1906	-0.2100
0.2919	-0.2660
0.4140	-0.2780
0.5236	-0.2410
0.6224	-0.1830
0.7332	-0.0931
0.8318	-0.0135
0.9203	0.0286

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 363.15 (Liquid)

Mole fraction of Acetic acid (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	2.23
0.0069	2.29
0.0137	2.35
0.0302	2.51
0.0888	3.16
0.2101	4.98
0.3269	7.53
0.4338	10.70
0.5302	14.31
0.6112	17.88
0.6761	21.10
0.7092	22.77
0.7831	26.70
0.8516	30.60
0.9139	34.30
0.9680	37.62
0.9912	39.08
0.9953	39.32
0.9976	39.45
1.0000	39.67

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 363.15 (Liquid)

Mole fraction of Acetic acid (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	2.23
0.0069	2.29
0.0137	2.35
0.0302	2.51
0.0888	3.16
0.2101	4.98
0.3269	7.53
0.4338	10.70
0.5302	14.31
0.6112	17.88
0.6761	21.10
0.7092	22.77
0.7831	26.70
0.8516	30.60
0.9139	34.30
0.9680	37.62
0.9912	39.08
0.9953	39.32
0.9976	39.45
1.0000	39.67

Sources

• Measurement of the thermodynamic properties for the reactive system ethylene glycol acetic acid