Mixture of Acetonitrile + Butane, 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 Butane, 2-ethoxy-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Gas
0.0000	343.94	0.0000
0.0092	343.08	0.0299
0.0154	343.08	0.0477
0.0221	343.11	0.0648
0.0290	343.11	0.0806
0.0364	343.04	0.0952
0.0510	343.10	0.1219
0.0704	343.05	0.1494
0.0891	343.06	0.1705
0.1086	343.05	0.1879
0.1288	343.11	0.2026
0.1499	343.06	0.2150
0.1790	343.06	0.2293
0.2067	343.09	0.2410
0.2342	343.08	0.2510
0.2825	343.08	0.2654
0.3192	343.09	0.2755
0.3619	343.11	0.2857
0.4028	343.06	0.2932
0.5447	343.01	0.3296
0.6016	343.05	0.3436
0.7063	343.12	0.3865
0.8216	343.11	0.4556
0.8680	343.03	0.5092
0.9296	343.16	0.6325
1.0000	343.12	1.0000

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

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Gas
0.0000	343.94	0.0000
0.0092	343.08	0.0299
0.0154	343.08	0.0477
0.0221	343.11	0.0648
0.0290	343.11	0.0806
0.0364	343.04	0.0952
0.0510	343.10	0.1219
0.0704	343.05	0.1494
0.0891	343.06	0.1705
0.1086	343.05	0.1879
0.1288	343.11	0.2026
0.1499	343.06	0.2150
0.1790	343.06	0.2293
0.2067	343.09	0.2410
0.2342	343.08	0.2510
0.2825	343.08	0.2654
0.3192	343.09	0.2755
0.3619	343.11	0.2857
0.4028	343.06	0.2932
0.5447	343.01	0.3296
0.6016	343.05	0.3436
0.7063	343.12	0.3865
0.8216	343.11	0.4556
0.8680	343.03	0.5092
0.9296	343.16	0.6325
1.0000	343.12	1.0000

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0990	298.40	0.3976
0.1996	298.40	0.6705
0.2996	298.40	0.8397
0.3985	298.41	0.9286
0.4976	298.41	0.9514
0.5980	298.41	0.9119
0.6974	298.41	0.8095
0.7984	298.40	0.6411
0.8971	298.40	0.3867

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0990	298.40	0.3976
0.1996	298.40	0.6705
0.2996	298.40	0.8397
0.3985	298.41	0.9286
0.4976	298.41	0.9514
0.5980	298.41	0.9119
0.6974	298.41	0.8095
0.7984	298.40	0.6411
0.8971	298.40	0.3867

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	343.94	71.24
0.0092	343.08	71.13
0.0154	343.08	72.27
0.0221	343.11	73.32
0.0290	343.11	74.34
0.0364	343.04	75.06
0.0510	343.10	76.75
0.0704	343.05	78.18
0.0891	343.06	79.35
0.1086	343.05	80.19
0.1288	343.11	81.05
0.1499	343.06	81.41
0.1790	343.06	81.85
0.2067	343.09	82.23
0.2342	343.08	82.27
0.2825	343.08	82.38
0.3192	343.09	82.27
0.3619	343.11	82.06
0.4028	343.06	81.54
0.5447	343.01	79.17
0.6016	343.05	77.93
0.7063	343.12	74.04
0.8216	343.11	66.37
0.8680	343.03	62.18
0.9296	343.16	53.60
1.0000	343.12	36.56

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	343.94	71.24
0.0092	343.08	71.13
0.0154	343.08	72.27
0.0221	343.11	73.32
0.0290	343.11	74.34
0.0364	343.04	75.06
0.0510	343.10	76.75
0.0704	343.05	78.18
0.0891	343.06	79.35
0.1086	343.05	80.19
0.1288	343.11	81.05
0.1499	343.06	81.41
0.1790	343.06	81.85
0.2067	343.09	82.23
0.2342	343.08	82.27
0.2825	343.08	82.38
0.3192	343.09	82.27
0.3619	343.11	82.06
0.4028	343.06	81.54
0.5447	343.01	79.17
0.6016	343.05	77.93
0.7063	343.12	74.04
0.8216	343.11	66.37
0.8680	343.03	62.18
0.9296	343.16	53.60
1.0000	343.12	36.56

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-ethoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.40	0.0990	774.5
298.40	0.1996	772.6
298.40	0.2996	770.7
298.41	0.3985	769.0
298.41	0.4976	767.5
298.41	0.5980	766.1
298.41	0.6974	764.8
298.40	0.7984	763.5
298.40	0.8971	762.3
298.15	1.0000	761.0
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 Butane, 2-ethoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.40	0.0990	774.5
298.40	0.1996	772.6
298.40	0.2996	770.7
298.41	0.3985	769.0
298.41	0.4976	767.5
298.41	0.5980	766.1
298.41	0.6974	764.8
298.40	0.7984	763.5
298.40	0.8971	762.3
298.15	1.0000	761.0
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