Mixture of Ethanol + Decanal

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 Decanal (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0011
298.15	0.1011	0.0011
298.15	0.2102	0.0012
298.15	0.3013	0.0012
298.15	0.4120	0.0013
298.15	0.5105	0.0013
298.15	0.5836	0.0013
298.15	0.6889	0.0014
298.15	0.8008	0.0015
298.15	0.9145	0.0015
298.15	1.0000	0.0016
308.15	0.0000	0.0009
308.15	0.1011	0.0009
308.15	0.2102	0.0010
308.15	0.3013	0.0010
308.15	0.4120	0.0011
308.15	0.5105	0.0011
308.15	0.5836	0.0012
308.15	0.6889	0.0012
308.15	0.8008	0.0013
308.15	0.9145	0.0014
308.15	1.0000	0.0014
318.15	0.0000	0.0008
318.15	0.1011	0.0008
318.15	0.2102	0.0009
318.15	0.3013	0.0009
318.15	0.4120	0.0009
318.15	0.5105	0.0010
318.15	0.5836	0.0010
318.15	0.6889	0.0011
318.15	0.8008	0.0012
318.15	0.9145	0.0012
318.15	1.0000	0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Decanal (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0011
298.15	0.1011	0.0011
298.15	0.2102	0.0012
298.15	0.3013	0.0012
298.15	0.4120	0.0013
298.15	0.5105	0.0013
298.15	0.5836	0.0013
298.15	0.6889	0.0014
298.15	0.8008	0.0015
298.15	0.9145	0.0015
298.15	1.0000	0.0016
308.15	0.0000	0.0009
308.15	0.1011	0.0009
308.15	0.2102	0.0010
308.15	0.3013	0.0010
308.15	0.4120	0.0011
308.15	0.5105	0.0011
308.15	0.5836	0.0012
308.15	0.6889	0.0012
308.15	0.8008	0.0013
308.15	0.9145	0.0014
308.15	1.0000	0.0014
318.15	0.0000	0.0008
318.15	0.1011	0.0008
318.15	0.2102	0.0009
318.15	0.3013	0.0009
318.15	0.4120	0.0009
318.15	0.5105	0.0010
318.15	0.5836	0.0010
318.15	0.6889	0.0011
318.15	0.8008	0.0012
318.15	0.9145	0.0012
318.15	1.0000	0.0013

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Decanal (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	785.08
298.15	0.1011	785.98
298.15	0.2102	787.14
298.15	0.3013	788.25
298.15	0.4120	789.78
298.15	0.5105	791.31
298.15	0.5836	792.55
298.15	0.6889	794.48
298.15	0.8008	796.73
298.15	0.9145	799.23
298.15	1.0000	801.24
308.15	0.0000	778.09
308.15	0.1011	778.7
308.15	0.2102	779.48
308.15	0.3013	780.24
308.15	0.4120	781.28
308.15	0.5105	782.32
308.15	0.5836	783.15
308.15	0.6889	784.47
308.15	0.8008	785.99
308.15	0.9145	787.68
308.15	1.0000	789.05
318.15	0.0000	763.91
318.15	0.1011	764.59
318.15	0.2102	765.47
318.15	0.3013	766.32
318.15	0.4120	767.48
318.15	0.5105	768.64
318.15	0.5836	769.58
318.15	0.6889	771.05
318.15	0.8008	772.76
318.15	0.9145	774.65
318.15	1.0000	776.18

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Decanal (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	785.08
298.15	0.1011	785.98
298.15	0.2102	787.14
298.15	0.3013	788.25
298.15	0.4120	789.78
298.15	0.5105	791.31
298.15	0.5836	792.55
298.15	0.6889	794.48
298.15	0.8008	796.73
298.15	0.9145	799.23
298.15	1.0000	801.24
308.15	0.0000	778.09
308.15	0.1011	778.7
308.15	0.2102	779.48
308.15	0.3013	780.24
308.15	0.4120	781.28
308.15	0.5105	782.32
308.15	0.5836	783.15
308.15	0.6889	784.47
308.15	0.8008	785.99
308.15	0.9145	787.68
308.15	1.0000	789.05
318.15	0.0000	763.91
318.15	0.1011	764.59
318.15	0.2102	765.47
318.15	0.3013	766.32
318.15	0.4120	767.48
318.15	0.5105	768.64
318.15	0.5836	769.58
318.15	0.6889	771.05
318.15	0.8008	772.76
318.15	0.9145	774.65
318.15	1.0000	776.18

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)