Mixture of 1-Butanol + 1-Hexanol

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 (1) [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0495	0.1614
0.1000	0.2848
0.1503	0.4161
0.1995	0.5143
0.2526	0.6047
0.2998	0.6699
0.3474	0.7279
0.3987	0.7774
0.4480	0.8112
0.4998	0.8508
0.5497	0.8736
0.6008	0.8969
0.6500	0.9193
0.7007	0.9348
0.7515	0.9508
0.8002	0.9627
0.8498	0.9732
0.8994	0.9821
0.9459	0.9916

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

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0495	0.1614
0.1000	0.2848
0.1503	0.4161
0.1995	0.5143
0.2526	0.6047
0.2998	0.6699
0.3474	0.7279
0.3987	0.7774
0.4480	0.8112
0.4998	0.8508
0.5497	0.8736
0.6008	0.8969
0.6500	0.9193
0.7007	0.9348
0.7515	0.9508
0.8002	0.9627
0.8498	0.9732
0.8994	0.9821
0.9459	0.9916

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Butanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0543	1.4148
0.0990	1.4142
0.2042	1.4126
0.2993	1.4111
0.4052	1.4094
0.4994	1.4078
0.5938	1.406
0.7005	1.4038
0.8004	1.4017
0.9003	1.3997
0.9499	1.3985

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Butanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0543	1.4148
0.0990	1.4142
0.2042	1.4126
0.2993	1.4111
0.4052	1.4094
0.4994	1.4078
0.5938	1.406
0.7005	1.4038
0.8004	1.4017
0.9003	1.3997
0.9499	1.3985

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0543	815.53
0.0990	815.22
0.2042	814.42
0.2993	813.64
0.4052	812.7
0.4994	811.8
0.5938	810.85
0.7005	809.72
0.8004	808.58
0.9003	807.35
0.9499	806.7

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0543	815.53
0.0990	815.22
0.2042	814.42
0.2993	813.64
0.4052	812.7
0.4994	811.8
0.5938	810.85
0.7005	809.72
0.8004	808.58
0.9003	807.35
0.9499	806.7

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0495	3.00
0.1000	3.30
0.1503	3.80
0.1995	4.20
0.2526	4.80
0.2998	5.30
0.3474	5.90
0.3987	6.50
0.4480	7.00
0.4998	7.70
0.5497	8.30
0.6008	8.90
0.6500	9.60
0.7007	10.10
0.7515	10.80
0.8002	11.40
0.8498	12.00
0.8994	12.50
0.9459	13.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0495	3.00
0.1000	3.30
0.1503	3.80
0.1995	4.20
0.2526	4.80
0.2998	5.30
0.3474	5.90
0.3987	6.50
0.4480	7.00
0.4998	7.70
0.5497	8.30
0.6008	8.90
0.6500	9.60
0.7007	10.10
0.7515	10.80
0.8002	11.40
0.8498	12.00
0.8994	12.50
0.9459	13.00

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of 1-Butanol (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0543	-0.0000
0.0990	-1.0400e-08
0.2042	-1.4700e-08
0.2993	-1.5400e-08
0.4052	-1.4100e-08
0.4994	-1.2000e-08
0.5938	-1.0200e-08
0.7005	-0.0000
0.8004	-0.0000
0.9003	-0.0000
0.9499	-0.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of 1-Butanol (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0543	-0.0000
0.0990	-1.0400e-08
0.2042	-1.4700e-08
0.2993	-1.5400e-08
0.4052	-1.4100e-08
0.4994	-1.2000e-08
0.5938	-1.0200e-08
0.7005	-0.0000
0.8004	-0.0000
0.9003	-0.0000
0.9499	-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