Mixture of 1-Butanol, 3-methyl- + 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, 3-methyl- (1) [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Mole fraction of 1-Butanol, 3-methyl- (1) - Gas
0.0476	0.2079
0.0798	0.3378
0.1041	0.4250
0.1499	0.5229
0.1996	0.5957
0.2495	0.6457
0.3007	0.6835
0.3503	0.7227
0.4009	0.7514
0.4592	0.7860
0.4997	0.8017
0.5526	0.8172
0.6008	0.8249
0.6494	0.8396
0.6947	0.8476
0.7489	0.8544
0.7967	0.8575
0.8543	0.8595
0.8991	0.8656
0.9502	0.8800
0.9804	0.9036

Mole fraction of 1-Butanol, 3-methyl- (1) [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Mole fraction of 1-Butanol, 3-methyl- (1) - Gas
0.0476	0.2079
0.0798	0.3378
0.1041	0.4250
0.1499	0.5229
0.1996	0.5957
0.2495	0.6457
0.3007	0.6835
0.3503	0.7227
0.4009	0.7514
0.4592	0.7860
0.4997	0.8017
0.5526	0.8172
0.6008	0.8249
0.6494	0.8396
0.6947	0.8476
0.7489	0.8544
0.7967	0.8575
0.8543	0.8595
0.8991	0.8656
0.9502	0.8800
0.9804	0.9036

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0496	1.4154
0.0997	1.4149
0.2005	1.414
0.3003	1.4131
0.3986	1.4121
0.4998	1.4111
0.6001	1.4101
0.7002	1.4091
0.8000	1.4081
0.8998	1.4069
0.9504	1.4064

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0496	1.4154
0.0997	1.4149
0.2005	1.414
0.3003	1.4131
0.3986	1.4121
0.4998	1.4111
0.6001	1.4101
0.7002	1.4091
0.8000	1.4081
0.8998	1.4069
0.9504	1.4064

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0496	815.43
0.0997	815.12
0.2005	814.49
0.3003	813.86
0.3986	813.22
0.4998	812.55
0.6001	811.87
0.7002	811.17
0.8000	810.46
0.8998	809.73
0.9504	809.35

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0496	815.43
0.0997	815.12
0.2005	814.49
0.3003	813.86
0.3986	813.22
0.4998	812.55
0.6001	811.87
0.7002	811.17
0.8000	810.46
0.8998	809.73
0.9504	809.35

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0476	3.20
0.0798	3.60
0.1041	3.90
0.1499	4.50
0.1996	5.00
0.2495	5.50
0.3007	6.00
0.3503	6.40
0.4009	6.70
0.4592	7.10
0.4997	7.40
0.5526	7.60
0.6008	7.80
0.6494	8.00
0.6947	8.10
0.7489	8.20
0.7967	8.30
0.8543	8.30
0.8991	8.30
0.9502	8.20
0.9804	8.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 343.2 (Gas)

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0476	3.20
0.0798	3.60
0.1041	3.90
0.1499	4.50
0.1996	5.00
0.2495	5.50
0.3007	6.00
0.3503	6.40
0.4009	6.70
0.4592	7.10
0.4997	7.40
0.5526	7.60
0.6008	7.80
0.6494	8.00
0.6947	8.10
0.7489	8.20
0.7967	8.30
0.8543	8.30
0.8991	8.30
0.9502	8.20
0.9804	8.00

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0496	0.0000
0.0997	0.0000
0.2005	0.0000
0.3003	0.0000
0.3986	0.0000
0.4998	0.0000
0.6001	0.0000
0.7002	0.0000
0.8000	0.0000
0.8998	0.0000
0.9504	0.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0496	0.0000
0.0997	0.0000
0.2005	0.0000
0.3003	0.0000
0.3986	0.0000
0.4998	0.0000
0.6001	0.0000
0.7002	0.0000
0.8000	0.0000
0.8998	0.0000
0.9504	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