Mixture of 1-Butanol, 3-methyl- + 1-Butanol

Datasets

1. Mole fraction (2)
2. n₀ - Refractive index (Na D-line) (2)
3. ρ_l - Mass density, kg/m3 (2)
4. Vapor or sublimation pressure, kPa (2)
5. Excess molar volume, m3/mol (2)

Mole fraction of 1-Butanol (2) [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol (2) - Liquid	Mole fraction of 1-Butanol (2) - Gas
0.0502	0.0973
0.1007	0.1852
0.1507	0.2573
0.2006	0.3203
0.2497	0.3829
0.2995	0.4409
0.3497	0.5007
0.4028	0.5526
0.4509	0.5951
0.5004	0.6375
0.5511	0.6795
0.6001	0.7246
0.6500	0.7676
0.6998	0.8042
0.7497	0.8385
0.8002	0.8722
0.8499	0.9101
0.9003	0.9394
0.9499	0.9706

Mole fraction of 1-Butanol (2) [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol (2) - Liquid	Mole fraction of 1-Butanol (2) - Gas
0.0502	0.0973
0.1007	0.1852
0.1507	0.2573
0.2006	0.3203
0.2497	0.3829
0.2995	0.4409
0.3497	0.5007
0.4028	0.5526
0.4509	0.5951
0.5004	0.6375
0.5511	0.6795
0.6001	0.7246
0.6500	0.7676
0.6998	0.8042
0.7497	0.8385
0.8002	0.8722
0.8499	0.9101
0.9003	0.9394
0.9499	0.9706

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0498	1.4056
0.0999	1.4053
0.1999	1.4045
0.3000	1.4037
0.4000	1.4029
0.4999	1.402
0.6016	1.4009
0.7015	1.3998
0.7999	1.3988
0.9007	1.3981
0.9506	1.3978

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0498	1.4056
0.0999	1.4053
0.1999	1.4045
0.3000	1.4037
0.4000	1.4029
0.4999	1.402
0.6016	1.4009
0.7015	1.3998
0.7999	1.3988
0.9007	1.3981
0.9506	1.3978

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0498	808.87
0.0999	808.78
0.1999	808.58
0.3000	808.35
0.4000	808.09
0.4999	807.81
0.6016	807.5
0.7015	807.16
0.7999	806.8
0.9007	806.41
0.9506	806.21

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0498	808.87
0.0999	808.78
0.1999	808.58
0.3000	808.35
0.4000	808.09
0.4999	807.81
0.6016	807.5
0.7015	807.16
0.7999	806.8
0.9007	806.41
0.9506	806.21

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0502	7.80
0.1007	8.20
0.1507	8.50
0.2006	8.90
0.2497	9.20
0.2995	9.50
0.3497	9.80
0.4028	10.10
0.4509	10.40
0.5004	10.70
0.5511	10.90
0.6001	11.20
0.6500	11.50
0.6998	11.80
0.7497	12.10
0.8002	12.40
0.8499	12.70
0.9003	13.00
0.9499	13.20

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0502	7.80
0.1007	8.20
0.1507	8.50
0.2006	8.90
0.2497	9.20
0.2995	9.50
0.3497	9.80
0.4028	10.10
0.4509	10.40
0.5004	10.70
0.5511	10.90
0.6001	11.20
0.6500	11.50
0.6998	11.80
0.7497	12.10
0.8002	12.40
0.8499	12.70
0.9003	13.00
0.9499	13.20

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0498	-0.0000
0.0999	-1.2800e-08
0.1999	-2.0100e-08
0.3000	-2.4500e-08
0.4000	-2.6600e-08
0.4999	-2.6900e-08
0.6016	-2.5000e-08
0.7015	-2.1000e-08
0.7999	-1.4600e-08
0.9007	-0.0000
0.9506	-0.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0498	-0.0000
0.0999	-1.2800e-08
0.1999	-2.0100e-08
0.3000	-2.4500e-08
0.4000	-2.6600e-08
0.4999	-2.6900e-08
0.6016	-2.5000e-08
0.7015	-2.1000e-08
0.7999	-1.4600e-08
0.9007	-0.0000
0.9506	-0.0000

Sources

• Isothermal vapor-liquid equilibria, excess molar volume and the deviation of refractive indices for binary mixtures of 1-butanol, 1- hexanol, 3-methyl-1-butanol and butyl acetate