Mixture of Ethanol + Hexanal

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Hexanal (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0011
298.15	0.1094	0.0011
298.15	0.2049	0.0010
298.15	0.3226	0.0010
298.15	0.4037	0.0010
298.15	0.5027	0.0009
298.15	0.6207	0.0009
298.15	0.7108	0.0009
298.15	0.8100	0.0009
298.15	0.9226	0.0008
298.15	1.0000	0.0008
308.15	0.0000	0.0009
308.15	0.1094	0.0009
308.15	0.2049	0.0009
308.15	0.3226	0.0008
308.15	0.4037	0.0008
308.15	0.5027	0.0008
308.15	0.6207	0.0008
308.15	0.7108	0.0008
308.15	0.8100	0.0007
308.15	0.9226	0.0007
308.15	1.0000	0.0007
318.15	0.0000	0.0008
318.15	0.1094	0.0008
318.15	0.2049	0.0007
318.15	0.3226	0.0007
318.15	0.4037	0.0007
318.15	0.5027	0.0007
318.15	0.6207	0.0007
318.15	0.7108	0.0007
318.15	0.8100	0.0007
318.15	0.9226	0.0006
318.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Hexanal (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0011
298.15	0.1094	0.0011
298.15	0.2049	0.0010
298.15	0.3226	0.0010
298.15	0.4037	0.0010
298.15	0.5027	0.0009
298.15	0.6207	0.0009
298.15	0.7108	0.0009
298.15	0.8100	0.0009
298.15	0.9226	0.0008
298.15	1.0000	0.0008
308.15	0.0000	0.0009
308.15	0.1094	0.0009
308.15	0.2049	0.0009
308.15	0.3226	0.0008
308.15	0.4037	0.0008
308.15	0.5027	0.0008
308.15	0.6207	0.0008
308.15	0.7108	0.0008
308.15	0.8100	0.0007
308.15	0.9226	0.0007
308.15	1.0000	0.0007
318.15	0.0000	0.0008
318.15	0.1094	0.0008
318.15	0.2049	0.0007
318.15	0.3226	0.0007
318.15	0.4037	0.0007
318.15	0.5027	0.0007
318.15	0.6207	0.0007
318.15	0.7108	0.0007
318.15	0.8100	0.0007
318.15	0.9226	0.0006
318.15	1.0000	0.0006

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Hexanal (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	785.08
298.15	0.1094	788.0
298.15	0.2049	791.01
298.15	0.3226	795.33
298.15	0.4037	798.69
298.15	0.5027	803.22
298.15	0.6207	809.24
298.15	0.7108	814.29
298.15	0.8100	820.3
298.15	0.9226	827.69
298.15	1.0000	833.12
308.15	0.0000	778.09
308.15	0.1094	780.57
308.15	0.2049	783.13
308.15	0.3226	786.81
308.15	0.4037	789.67
308.15	0.5027	793.52
308.15	0.6207	798.64
308.15	0.7108	802.93
308.15	0.8100	808.04
308.15	0.9226	814.32
308.15	1.0000	818.94
318.15	0.0000	763.91
318.15	0.1094	766.36
318.15	0.2049	768.9
318.15	0.3226	772.53
318.15	0.4037	775.36
318.15	0.5027	779.17
318.15	0.6207	784.23
318.15	0.7108	788.47
318.15	0.8100	793.53
318.15	0.9226	799.74
318.15	1.0000	804.31

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Hexanal (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	785.08
298.15	0.1094	788.0
298.15	0.2049	791.01
298.15	0.3226	795.33
298.15	0.4037	798.69
298.15	0.5027	803.22
298.15	0.6207	809.24
298.15	0.7108	814.29
298.15	0.8100	820.3
298.15	0.9226	827.69
298.15	1.0000	833.12
308.15	0.0000	778.09
308.15	0.1094	780.57
308.15	0.2049	783.13
308.15	0.3226	786.81
308.15	0.4037	789.67
308.15	0.5027	793.52
308.15	0.6207	798.64
308.15	0.7108	802.93
308.15	0.8100	808.04
308.15	0.9226	814.32
308.15	1.0000	818.94
318.15	0.0000	763.91
318.15	0.1094	766.36
318.15	0.2049	768.9
318.15	0.3226	772.53
318.15	0.4037	775.36
318.15	0.5027	779.17
318.15	0.6207	784.23
318.15	0.7108	788.47
318.15	0.8100	793.53
318.15	0.9226	799.74
318.15	1.0000	804.31

Sources

• Density and Viscosity of Several Aldehydes Fragrance Compounds in Their Binary Mixtures with Ethanol at (298.15 K, 308.15 K, and 318.15 K)