Mixture of Acetonitrile + Propane, 2-ethoxy-2-methyl-

Datasets

1. Mole fraction (2)
2. Excess molar enthalpy (molar enthalpy (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Propane, 2-ethoxy-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Gas
1.0000	332.26	1.0000
0.9270	333.12	0.8188
0.8693	333.14	0.7457
0.7883	333.04	0.6781
0.7355	333.05	0.6425
0.6466	333.03	0.6057
0.5742	333.08	0.5775
0.5118	333.07	0.5572
0.4640	333.09	0.5430
0.4106	333.07	0.5247
0.2959	333.08	0.4795
0.2891	333.06	0.4788
0.2788	333.09	0.4729
0.2719	333.04	0.4674
0.2712	333.06	0.4677
0.2437	333.14	0.4575
0.2307	333.12	0.4500
0.1745	333.07	0.4147
0.1229	333.01	0.3625
0.0808	333.05	0.2977
0.0560	333.07	0.2279
0.0025	333.08	0.0164
0.0000	333.57	0.0000

Mole fraction of Propane, 2-ethoxy-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Gas
1.0000	332.26	1.0000
0.9270	333.12	0.8188
0.8693	333.14	0.7457
0.7883	333.04	0.6781
0.7355	333.05	0.6425
0.6466	333.03	0.6057
0.5742	333.08	0.5775
0.5118	333.07	0.5572
0.4640	333.09	0.5430
0.4106	333.07	0.5247
0.2959	333.08	0.4795
0.2891	333.06	0.4788
0.2788	333.09	0.4729
0.2719	333.04	0.4674
0.2712	333.06	0.4677
0.2437	333.14	0.4575
0.2307	333.12	0.4500
0.1745	333.07	0.4147
0.1229	333.01	0.3625
0.0808	333.05	0.2977
0.0560	333.07	0.2279
0.0025	333.08	0.0164
0.0000	333.57	0.0000

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0996	298.41	0.2813
0.1989	298.41	0.4852
0.2993	298.41	0.6176
0.3982	298.41	0.6892
0.4984	298.42	0.7098
0.5994	298.42	0.6773
0.6994	298.42	0.5881
0.8010	298.42	0.4418
0.9009	298.42	0.2434

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0996	298.41	0.2813
0.1989	298.41	0.4852
0.2993	298.41	0.6176
0.3982	298.41	0.6892
0.4984	298.42	0.7098
0.5994	298.42	0.6773
0.6994	298.42	0.5881
0.8010	298.42	0.4418
0.9009	298.42	0.2434

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
1.0000	332.26	64.28
0.9270	333.12	75.33
0.8693	333.14	79.26
0.7883	333.04	82.15
0.7355	333.05	83.45
0.6466	333.03	84.32
0.5742	333.08	84.76
0.5118	333.07	84.53
0.4640	333.09	84.29
0.4106	333.07	83.65
0.2959	333.08	81.58
0.2891	333.06	81.29
0.2788	333.09	81.12
0.2719	333.04	80.74
0.2712	333.06	80.75
0.2437	333.14	79.94
0.2307	333.12	79.42
0.1745	333.07	76.44
0.1229	333.01	72.14
0.0808	333.05	67.20
0.0560	333.07	63.11
0.0025	333.08	49.85
0.0000	333.57	49.76

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
1.0000	332.26	64.28
0.9270	333.12	75.33
0.8693	333.14	79.26
0.7883	333.04	82.15
0.7355	333.05	83.45
0.6466	333.03	84.32
0.5742	333.08	84.76
0.5118	333.07	84.53
0.4640	333.09	84.29
0.4106	333.07	83.65
0.2959	333.08	81.58
0.2891	333.06	81.29
0.2788	333.09	81.12
0.2719	333.04	80.74
0.2712	333.06	80.75
0.2437	333.14	79.94
0.2307	333.12	79.42
0.1745	333.07	76.44
0.1229	333.01	72.14
0.0808	333.05	67.20
0.0560	333.07	63.11
0.0025	333.08	49.85
0.0000	333.57	49.76

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.41	0.0996	770.1
298.41	0.1989	764.5
298.41	0.2993	759.5
298.41	0.3982	755.1
298.42	0.4984	751.0
298.42	0.5994	747.3
298.42	0.6994	744.1
298.42	0.8010	740.8
298.42	0.9009	737.8
298.15	1.0000	735.0
298.15	0.0000	776.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.41	0.0996	770.1
298.41	0.1989	764.5
298.41	0.2993	759.5
298.41	0.3982	755.1
298.42	0.4984	751.0
298.42	0.5994	747.3
298.42	0.6994	744.1
298.42	0.8010	740.8
298.42	0.9009	737.8
298.15	1.0000	735.0
298.15	0.0000	776.0

Sources

• Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile