Mixture of Ethanol + Octanal

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 Octanal (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0011
298.15	0.1077	0.0011
298.15	0.2019	0.0011
298.15	0.3178	0.0011
298.15	0.3977	0.0011
298.15	0.4952	0.0011
298.15	0.6115	0.0012
298.15	0.7003	0.0012
298.15	0.7980	0.0012
298.15	0.9089	0.0012
298.15	1.0000	0.0012
308.15	0.0000	0.0009
308.15	0.1077	0.0009
308.15	0.2019	0.0009
308.15	0.3178	0.0009
308.15	0.3977	0.0010
308.15	0.4952	0.0010
308.15	0.6115	0.0010
308.15	0.7003	0.0010
308.15	0.7980	0.0010
308.15	0.9089	0.0011
308.15	1.0000	0.0011
318.15	0.0000	0.0008
318.15	0.1077	0.0008
318.15	0.2019	0.0008
318.15	0.3178	0.0008
318.15	0.3977	0.0008
318.15	0.4952	0.0009
318.15	0.6115	0.0009
318.15	0.7003	0.0009
318.15	0.7980	0.0009
318.15	0.9089	0.0009
318.15	1.0000	0.0010

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Octanal (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0011
298.15	0.1077	0.0011
298.15	0.2019	0.0011
298.15	0.3178	0.0011
298.15	0.3977	0.0011
298.15	0.4952	0.0011
298.15	0.6115	0.0012
298.15	0.7003	0.0012
298.15	0.7980	0.0012
298.15	0.9089	0.0012
298.15	1.0000	0.0012
308.15	0.0000	0.0009
308.15	0.1077	0.0009
308.15	0.2019	0.0009
308.15	0.3178	0.0009
308.15	0.3977	0.0010
308.15	0.4952	0.0010
308.15	0.6115	0.0010
308.15	0.7003	0.0010
308.15	0.7980	0.0010
308.15	0.9089	0.0011
308.15	1.0000	0.0011
318.15	0.0000	0.0008
318.15	0.1077	0.0008
318.15	0.2019	0.0008
318.15	0.3178	0.0008
318.15	0.3977	0.0008
318.15	0.4952	0.0009
318.15	0.6115	0.0009
318.15	0.7003	0.0009
318.15	0.7980	0.0009
318.15	0.9089	0.0009
318.15	1.0000	0.0010

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Octanal (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	785.08
298.15	0.1077	787.23
298.15	0.2019	789.45
298.15	0.3178	792.62
298.15	0.3977	795.08
298.15	0.4952	798.4
298.15	0.6115	802.81
298.15	0.7003	806.51
298.15	0.7980	810.9
298.15	0.9089	816.3
298.15	1.0000	821.07
308.15	0.0000	778.09
308.15	0.1077	779.83
308.15	0.2019	781.64
308.15	0.3178	784.21
308.15	0.3977	786.22
308.15	0.4952	788.92
308.15	0.6115	792.5
308.15	0.7003	795.5
308.15	0.7980	799.07
308.15	0.9089	803.46
308.15	1.0000	807.34
318.15	0.0000	763.91
318.15	0.1077	765.7
318.15	0.2019	767.54
318.15	0.3178	770.18
318.15	0.3977	772.23
318.15	0.4952	774.99
318.15	0.6115	778.66
318.15	0.7003	781.74
318.15	0.7980	785.39
318.15	0.9089	789.88
318.15	1.0000	793.85

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Octanal (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	785.08
298.15	0.1077	787.23
298.15	0.2019	789.45
298.15	0.3178	792.62
298.15	0.3977	795.08
298.15	0.4952	798.4
298.15	0.6115	802.81
298.15	0.7003	806.51
298.15	0.7980	810.9
298.15	0.9089	816.3
298.15	1.0000	821.07
308.15	0.0000	778.09
308.15	0.1077	779.83
308.15	0.2019	781.64
308.15	0.3178	784.21
308.15	0.3977	786.22
308.15	0.4952	788.92
308.15	0.6115	792.5
308.15	0.7003	795.5
308.15	0.7980	799.07
308.15	0.9089	803.46
308.15	1.0000	807.34
318.15	0.0000	763.91
318.15	0.1077	765.7
318.15	0.2019	767.54
318.15	0.3178	770.18
318.15	0.3977	772.23
318.15	0.4952	774.99
318.15	0.6115	778.66
318.15	0.7003	781.74
318.15	0.7980	785.39
318.15	0.9089	789.88
318.15	1.0000	793.85

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)