Mixture of 1-Butanol + Butane, 1-chloro-

Datasets

1. η - Viscosity, Pa*s (4)
2. n₀ - Refractive index (Na D-line) (2)
3. ρ_l - Mass density, kg/m3 (4)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0005
288.15	0.0500	0.0005
288.15	0.1000	0.0005
288.15	0.2000	0.0006
288.15	0.3000	0.0007
288.15	0.4000	0.0008
288.15	0.5000	0.0010
288.15	0.6000	0.0012
288.15	0.7000	0.0015
288.15	0.8000	0.0020
288.15	0.9000	0.0026
288.15	0.9500	0.0030
288.15	1.0000	0.0034
298.15	0.0000	0.0004
298.15	0.0500	0.0004
298.15	0.1000	0.0005
298.15	0.2000	0.0005
298.15	0.3000	0.0006
298.15	0.4000	0.0007
298.15	0.5000	0.0008
298.15	0.6000	0.0010
298.15	0.7000	0.0012
298.15	0.8000	0.0016
298.15	0.9000	0.0020
298.15	0.9500	0.0023
298.15	1.0000	0.0026
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
308.15	0.2000	0.0004
308.15	0.3000	0.0005
308.15	0.4000	0.0006
308.15	0.5000	0.0007
308.15	0.6000	0.0008
308.15	0.7000	0.0010
308.15	0.8000	0.0013
308.15	0.9000	0.0016
308.15	0.9500	0.0018
308.15	1.0000	0.0020

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0949	0.0005
288.15	0.1964	0.0006
288.15	0.2961	0.0007
288.15	0.3949	0.0008
288.15	0.4941	0.0009
288.15	0.5915	0.0012
288.15	0.6954	0.0015
288.15	0.7940	0.0019
288.15	0.8920	0.0025
298.15	0.0949	0.0005
298.15	0.1964	0.0005
298.15	0.2961	0.0006
298.15	0.3949	0.0007
298.15	0.4941	0.0008
298.15	0.5915	0.0010
298.15	0.6954	0.0012
298.15	0.7940	0.0015
298.15	0.8920	0.0020
308.15	0.0949	0.0004
308.15	0.1964	0.0004
308.15	0.2961	0.0005
308.15	0.3949	0.0006
308.15	0.4941	0.0007
308.15	0.5915	0.0008
308.15	0.6954	0.0010
308.15	0.7940	0.0012
308.15	0.8920	0.0015
318.15	0.0949	0.0004
318.15	0.1964	0.0004
318.15	0.2961	0.0004
318.15	0.3949	0.0005
318.15	0.4941	0.0006
318.15	0.5915	0.0007
318.15	0.6954	0.0008
318.15	0.7940	0.0010
318.15	0.8920	0.0012

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0005
288.15	0.0500	0.0005
288.15	0.1000	0.0005
288.15	0.2000	0.0006
288.15	0.3000	0.0007
288.15	0.4000	0.0008
288.15	0.5000	0.0010
288.15	0.6000	0.0012
288.15	0.7000	0.0015
288.15	0.8000	0.0020
288.15	0.9000	0.0026
288.15	0.9500	0.0030
288.15	1.0000	0.0034
298.15	0.0000	0.0004
298.15	0.0500	0.0004
298.15	0.1000	0.0005
298.15	0.2000	0.0005
298.15	0.3000	0.0006
298.15	0.4000	0.0007
298.15	0.5000	0.0008
298.15	0.6000	0.0010
298.15	0.7000	0.0012
298.15	0.8000	0.0016
298.15	0.9000	0.0020
298.15	0.9500	0.0023
298.15	1.0000	0.0026
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
308.15	0.2000	0.0004
308.15	0.3000	0.0005
308.15	0.4000	0.0006
308.15	0.5000	0.0007
308.15	0.6000	0.0008
308.15	0.7000	0.0010
308.15	0.8000	0.0013
308.15	0.9000	0.0016
308.15	0.9500	0.0018
308.15	1.0000	0.0020

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0949	0.0005
288.15	0.1964	0.0006
288.15	0.2961	0.0007
288.15	0.3949	0.0008
288.15	0.4941	0.0009
288.15	0.5915	0.0012
288.15	0.6954	0.0015
288.15	0.7940	0.0019
288.15	0.8920	0.0025
298.15	0.0949	0.0005
298.15	0.1964	0.0005
298.15	0.2961	0.0006
298.15	0.3949	0.0007
298.15	0.4941	0.0008
298.15	0.5915	0.0010
298.15	0.6954	0.0012
298.15	0.7940	0.0015
298.15	0.8920	0.0020
308.15	0.0949	0.0004
308.15	0.1964	0.0004
308.15	0.2961	0.0005
308.15	0.3949	0.0006
308.15	0.4941	0.0007
308.15	0.5915	0.0008
308.15	0.6954	0.0010
308.15	0.7940	0.0012
308.15	0.8920	0.0015
318.15	0.0949	0.0004
318.15	0.1964	0.0004
318.15	0.2961	0.0004
318.15	0.3949	0.0005
318.15	0.4941	0.0006
318.15	0.5915	0.0007
318.15	0.6954	0.0008
318.15	0.7940	0.0010
318.15	0.8920	0.0012

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4045
288.15	0.0500	1.4041
288.15	0.1000	1.4039
288.15	0.2000	1.4035
288.15	0.3000	1.4031
288.15	0.4000	1.4029
288.15	0.5000	1.4027
288.15	0.6000	1.4024
288.15	0.7000	1.4022
288.15	0.8000	1.4019
288.15	0.9000	1.4016
288.15	0.9500	1.4013
288.15	1.0000	1.401
298.15	0.0000	1.3993
298.15	0.0500	1.3989
298.15	0.1000	1.3987
298.15	0.2000	1.3984
298.15	0.3000	1.3982
298.15	0.4000	1.3981
298.15	0.5000	1.398
298.15	0.6000	1.3979
298.15	0.7000	1.3978
298.15	0.8000	1.3977
298.15	0.9000	1.3975
298.15	0.9500	1.3974
298.15	1.0000	1.3972
308.15	0.0000	1.3941
308.15	0.0500	1.3936
308.15	0.1000	1.3934
308.15	0.2000	1.3932
308.15	0.3000	1.3931
308.15	0.4000	1.3931
308.15	0.5000	1.3932
308.15	0.6000	1.3932
308.15	0.7000	1.3933
308.15	0.8000	1.3933
308.15	0.9000	1.3933
308.15	0.9500	1.3933
308.15	1.0000	1.3932

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4045
288.15	0.0500	1.4041
288.15	0.1000	1.4039
288.15	0.2000	1.4035
288.15	0.3000	1.4031
288.15	0.4000	1.4029
288.15	0.5000	1.4027
288.15	0.6000	1.4024
288.15	0.7000	1.4022
288.15	0.8000	1.4019
288.15	0.9000	1.4016
288.15	0.9500	1.4013
288.15	1.0000	1.401
298.15	0.0000	1.3993
298.15	0.0500	1.3989
298.15	0.1000	1.3987
298.15	0.2000	1.3984
298.15	0.3000	1.3982
298.15	0.4000	1.3981
298.15	0.5000	1.398
298.15	0.6000	1.3979
298.15	0.7000	1.3978
298.15	0.8000	1.3977
298.15	0.9000	1.3975
298.15	0.9500	1.3974
298.15	1.0000	1.3972
308.15	0.0000	1.3941
308.15	0.0500	1.3936
308.15	0.1000	1.3934
308.15	0.2000	1.3932
308.15	0.3000	1.3931
308.15	0.4000	1.3931
308.15	0.5000	1.3932
308.15	0.6000	1.3932
308.15	0.7000	1.3933
308.15	0.8000	1.3933
308.15	0.9000	1.3933
308.15	0.9500	1.3933
308.15	1.0000	1.3932

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	892.2
288.15	0.0500	888.0
288.15	0.1000	884.3
288.15	0.2000	877.0
288.15	0.3000	869.7
288.15	0.4000	862.4
288.15	0.5000	854.9
288.15	0.6000	847.3
288.15	0.7000	839.4
288.15	0.8000	831.2
288.15	0.9000	822.6
288.15	0.9500	818.1
288.15	1.0000	813.5
298.15	0.0000	881.0
298.15	0.0500	876.9
298.15	0.1000	873.3
298.15	0.2000	866.3
298.15	0.3000	859.4
298.15	0.4000	852.4
298.15	0.5000	845.3
298.15	0.6000	838.0
298.15	0.7000	830.5
298.15	0.8000	822.7
298.15	0.9000	814.5
298.15	0.9500	810.3
298.15	1.0000	805.9
308.15	0.0000	869.7
308.15	0.0500	865.7
308.15	0.1000	862.3
308.15	0.2000	855.5
308.15	0.3000	848.9
308.15	0.4000	842.2
308.15	0.5000	835.4
308.15	0.6000	828.6
308.15	0.7000	821.5
308.15	0.8000	814.1
308.15	0.9000	806.3
308.15	0.9500	802.3
308.15	1.0000	798.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0620	886.96
288.15	0.1027	883.98
288.15	0.1383	881.38
288.15	0.2032	876.67
288.15	0.2597	872.57
288.15	0.2859	870.67
288.15	0.3764	864.06
288.15	0.3967	862.58
288.15	0.4541	858.3
288.15	0.4822	856.17
288.15	0.5076	854.25
288.15	0.5466	851.25
288.15	0.5818	848.53
288.15	0.6332	844.49
288.15	0.6747	841.19
288.15	0.7342	836.4
288.15	0.7698	833.49
288.15	0.8509	826.62
288.15	0.9022	822.13
288.15	0.9582	817.04
308.15	0.1056	861.88
308.15	0.1979	855.62
308.15	0.2842	849.82
308.15	0.3908	842.67
308.15	0.4964	835.5
308.15	0.5913	828.95
308.15	0.6908	821.85
308.15	0.7917	814.48
308.15	0.9003	806.19
318.15	0.0612	853.78
318.15	0.0913	851.66
318.15	0.1849	845.48
318.15	0.2759	839.66
318.15	0.3836	832.82
318.15	0.4858	826.26
318.15	0.5859	819.71
318.15	0.6868	812.99
318.15	0.7868	806.09
318.15	0.8906	798.56

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	892.2
288.15	0.0500	888.0
288.15	0.1000	884.3
288.15	0.2000	877.0
288.15	0.3000	869.7
288.15	0.4000	862.4
288.15	0.5000	854.9
288.15	0.6000	847.3
288.15	0.7000	839.4
288.15	0.8000	831.2
288.15	0.9000	822.6
288.15	0.9500	818.1
288.15	1.0000	813.5
298.15	0.0000	881.0
298.15	0.0500	876.9
298.15	0.1000	873.3
298.15	0.2000	866.3
298.15	0.3000	859.4
298.15	0.4000	852.4
298.15	0.5000	845.3
298.15	0.6000	838.0
298.15	0.7000	830.5
298.15	0.8000	822.7
298.15	0.9000	814.5
298.15	0.9500	810.3
298.15	1.0000	805.9
308.15	0.0000	869.7
308.15	0.0500	865.7
308.15	0.1000	862.3
308.15	0.2000	855.5
308.15	0.3000	848.9
308.15	0.4000	842.2
308.15	0.5000	835.4
308.15	0.6000	828.6
308.15	0.7000	821.5
308.15	0.8000	814.1
308.15	0.9000	806.3
308.15	0.9500	802.3
308.15	1.0000	798.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0620	886.96
288.15	0.1027	883.98
288.15	0.1383	881.38
288.15	0.2032	876.67
288.15	0.2597	872.57
288.15	0.2859	870.67
288.15	0.3764	864.06
288.15	0.3967	862.58
288.15	0.4541	858.3
288.15	0.4822	856.17
288.15	0.5076	854.25
288.15	0.5466	851.25
288.15	0.5818	848.53
288.15	0.6332	844.49
288.15	0.6747	841.19
288.15	0.7342	836.4
288.15	0.7698	833.49
288.15	0.8509	826.62
288.15	0.9022	822.13
288.15	0.9582	817.04
308.15	0.1056	861.88
308.15	0.1979	855.62
308.15	0.2842	849.82
308.15	0.3908	842.67
308.15	0.4964	835.5
308.15	0.5913	828.95
308.15	0.6908	821.85
308.15	0.7917	814.48
308.15	0.9003	806.19
318.15	0.0612	853.78
318.15	0.0913	851.66
318.15	0.1849	845.48
318.15	0.2759	839.66
318.15	0.3836	832.82
318.15	0.4858	826.26
318.15	0.5859	819.71
318.15	0.6868	812.99
318.15	0.7868	806.09
318.15	0.8906	798.56

Sources

• Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
• Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures