Mixture of 1-Butanol + Butyl lactate

Datasets

1. Mole fraction (2)
2. ρ_l - Mass density, kg/m3 (2)
3. T_boil - Boiling temperature at pressure P, K (2)

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

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0000	0.0000
0.0175	0.1033
0.0712	0.3410
0.1487	0.5475
0.2029	0.6444
0.2636	0.7220
0.3376	0.7983
0.3773	0.8334
0.4049	0.8410
0.4556	0.8830
0.4941	0.8947
0.5113	0.8994
0.5357	0.9065
0.5835	0.9290
0.5940	0.9316
0.6699	0.9505
0.6887	0.9589
0.7218	0.9671
0.7534	0.9683
0.8587	0.9800
0.9106	0.9880
0.9238	0.9895
0.9398	0.9913
0.9536	0.9924
0.9667	0.9938
1.0000	1.0000

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

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0000	0.0000
0.0175	0.1033
0.0712	0.3410
0.1487	0.5475
0.2029	0.6444
0.2636	0.7220
0.3376	0.7983
0.3773	0.8334
0.4049	0.8410
0.4556	0.8830
0.4941	0.8947
0.5113	0.8994
0.5357	0.9065
0.5835	0.9290
0.5940	0.9316
0.6699	0.9505
0.6887	0.9589
0.7218	0.9671
0.7534	0.9683
0.8587	0.9800
0.9106	0.9880
0.9238	0.9895
0.9398	0.9913
0.9536	0.9924
0.9667	0.9938
1.0000	1.0000

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	982.178
0.0989	971.809
0.1806	962.459
0.2599	952.704
0.3973	933.863
0.5154	915.521
0.5669	906.818
0.6645	888.883
0.7069	880.503
0.7854	863.836
0.8546	847.901
0.9174	832.199
0.9728	817.297
1.0000	809.572

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	982.178
0.0989	971.809
0.1806	962.459
0.2599	952.704
0.3973	933.863
0.5154	915.521
0.5669	906.818
0.6645	888.883
0.7069	880.503
0.7854	863.836
0.8546	847.901
0.9174	832.199
0.9728	817.297
1.0000	809.572

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	460.75
0.0175	457.75
0.0712	448.89
0.1487	437.50
0.2029	431.27
0.2636	425.10
0.3376	419.40
0.3773	415.77
0.4049	414.45
0.4556	411.10
0.4941	409.19
0.5113	408.21
0.5357	407.10
0.5835	404.73
0.5940	404.17
0.6699	400.95
0.6887	400.00
0.7218	398.67
0.7534	397.60
0.8587	394.27
0.9106	392.77
0.9238	392.34
0.9398	391.99
0.9536	391.59
0.9667	391.35
1.0000	390.88

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	460.75
0.0175	457.75
0.0712	448.89
0.1487	437.50
0.2029	431.27
0.2636	425.10
0.3376	419.40
0.3773	415.77
0.4049	414.45
0.4556	411.10
0.4941	409.19
0.5113	408.21
0.5357	407.10
0.5835	404.73
0.5940	404.17
0.6699	400.95
0.6887	400.00
0.7218	398.67
0.7534	397.60
0.8587	394.27
0.9106	392.77
0.9238	392.34
0.9398	391.99
0.9536	391.59
0.9667	391.35
1.0000	390.88

Sources

• Vapor liquid equilibria and excess volumes of the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate at 101.325 kPa