Mixture of Propanenitrile + 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	363.10	0.0000
0.0218	363.09	0.0582
0.0434	363.09	0.1029
0.0675	363.09	0.1453
0.0964	363.09	0.1936
0.1294	363.09	0.2342
0.1709	363.12	0.2756
0.2094	363.13	0.3090
0.2511	363.13	0.3385
0.2907	363.12	0.3635
0.3440	363.14	0.3931
0.3798	363.10	0.4108
0.4178	363.08	0.4296
0.4478	363.09	0.4444
0.4743	363.12	0.4536
0.5007	363.10	0.4682
0.5261	363.07	0.4814
0.5568	363.03	0.4953
0.5913	363.06	0.5126
0.6235	363.08	0.5286
0.6518	363.02	0.5437
0.6909	363.04	0.5660
0.7220	363.02	0.5854
0.7620	363.08	0.6114
0.7979	363.01	0.6383
0.8370	363.05	0.6739
0.8704	363.13	0.7143
0.9007	363.11	0.7519
0.9329	363.09	0.8112
0.9690	363.12	0.8948
0.9858	363.04	0.9471
1.0000	362.69	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	363.10	0.0000
0.0218	363.09	0.0582
0.0434	363.09	0.1029
0.0675	363.09	0.1453
0.0964	363.09	0.1936
0.1294	363.09	0.2342
0.1709	363.12	0.2756
0.2094	363.13	0.3090
0.2511	363.13	0.3385
0.2907	363.12	0.3635
0.3440	363.14	0.3931
0.3798	363.10	0.4108
0.4178	363.08	0.4296
0.4478	363.09	0.4444
0.4743	363.12	0.4536
0.5007	363.10	0.4682
0.5261	363.07	0.4814
0.5568	363.03	0.4953
0.5913	363.06	0.5126
0.6235	363.08	0.5286
0.6518	363.02	0.5437
0.6909	363.04	0.5660
0.7220	363.02	0.5854
0.7620	363.08	0.6114
0.7979	363.01	0.6383
0.8370	363.05	0.6739
0.8704	363.13	0.7143
0.9007	363.11	0.7519
0.9329	363.09	0.8112
0.9690	363.12	0.8948
0.9858	363.04	0.9471
1.0000	362.69	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
0.1000	298.40	0.2573
0.1991	298.40	0.4510
0.2988	298.39	0.5863
0.3991	298.40	0.6684
0.4975	298.39	0.7023
0.5990	298.39	0.6866
0.6987	298.40	0.6215
0.7991	298.40	0.5020
0.8976	298.41	0.3123

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
0.1000	298.40	0.2573
0.1991	298.40	0.4510
0.2988	298.39	0.5863
0.3991	298.40	0.6684
0.4975	298.39	0.7023
0.5990	298.39	0.6866
0.6987	298.40	0.6215
0.7991	298.40	0.5020
0.8976	298.41	0.3123

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	363.10	80.66
0.0218	363.09	84.24
0.0434	363.09	87.02
0.0675	363.09	89.78
0.0964	363.09	92.62
0.1294	363.09	95.24
0.1709	363.12	97.77
0.2094	363.13	99.54
0.2511	363.13	100.95
0.2907	363.12	101.81
0.3440	363.14	102.43
0.3798	363.10	102.61
0.4178	363.08	102.74
0.4478	363.09	102.78
0.4743	363.12	102.83
0.5007	363.10	102.72
0.5261	363.07	102.42
0.5568	363.03	102.01
0.5913	363.06	101.68
0.6235	363.08	101.11
0.6518	363.02	100.33
0.6909	363.04	99.23
0.7220	363.02	98.16
0.7620	363.08	96.65
0.7979	363.01	94.61
0.8370	363.05	92.39
0.8704	363.13	90.33
0.9007	363.11	87.34
0.9329	363.09	83.52
0.9690	363.12	77.82
0.9858	363.04	74.64
1.0000	363.10	71.73

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	363.10	80.66
0.0218	363.09	84.24
0.0434	363.09	87.02
0.0675	363.09	89.78
0.0964	363.09	92.62
0.1294	363.09	95.24
0.1709	363.12	97.77
0.2094	363.13	99.54
0.2511	363.13	100.95
0.2907	363.12	101.81
0.3440	363.14	102.43
0.3798	363.10	102.61
0.4178	363.08	102.74
0.4478	363.09	102.78
0.4743	363.12	102.83
0.5007	363.10	102.72
0.5261	363.07	102.42
0.5568	363.03	102.01
0.5913	363.06	101.68
0.6235	363.08	101.11
0.6518	363.02	100.33
0.6909	363.04	99.23
0.7220	363.02	98.16
0.7620	363.08	96.65
0.7979	363.01	94.61
0.8370	363.05	92.39
0.8704	363.13	90.33
0.9007	363.11	87.34
0.9329	363.09	83.52
0.9690	363.12	77.82
0.9858	363.04	74.64
1.0000	363.10	71.73

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	0.1000	774.3
298.40	0.1991	773.1
298.39	0.2988	771.5
298.40	0.3991	769.9
298.39	0.4975	768.3
298.39	0.5990	766.7
298.40	0.6987	765.3
298.40	0.7991	763.8
298.41	0.8976	762.4
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	0.1000	774.3
298.40	0.1991	773.1
298.39	0.2988	771.5
298.40	0.3991	769.9
298.39	0.4975	768.3
298.39	0.5990	766.7
298.40	0.6987	765.3
298.40	0.7991	763.8
298.41	0.8976	762.4
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