Mixture of Nonanal + Ethanol

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 Nonanal (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0011
298.15	0.1034	0.0011
298.15	0.2039	0.0011
298.15	0.2930	0.0012
298.15	0.3939	0.0012
298.15	0.5045	0.0012
298.15	0.5943	0.0013
298.15	0.7116	0.0013
298.15	0.7855	0.0013
298.15	0.8980	0.0014
298.15	1.0000	0.0014
308.15	0.0000	0.0009
308.15	0.1034	0.0009
308.15	0.2039	0.0010
308.15	0.2930	0.0010
308.15	0.3939	0.0010
308.15	0.5045	0.0011
308.15	0.5943	0.0011
308.15	0.7116	0.0011
308.15	0.7855	0.0012
308.15	0.8980	0.0012
308.15	1.0000	0.0013
318.15	0.0000	0.0008
318.15	0.1034	0.0008
318.15	0.2039	0.0008
318.15	0.2930	0.0009
318.15	0.3939	0.0009
318.15	0.5045	0.0009
318.15	0.5943	0.0010
318.15	0.7116	0.0010
318.15	0.7855	0.0010
318.15	0.8980	0.0011
318.15	1.0000	0.0011

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Nonanal (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0011
298.15	0.1034	0.0011
298.15	0.2039	0.0011
298.15	0.2930	0.0012
298.15	0.3939	0.0012
298.15	0.5045	0.0012
298.15	0.5943	0.0013
298.15	0.7116	0.0013
298.15	0.7855	0.0013
298.15	0.8980	0.0014
298.15	1.0000	0.0014
308.15	0.0000	0.0009
308.15	0.1034	0.0009
308.15	0.2039	0.0010
308.15	0.2930	0.0010
308.15	0.3939	0.0010
308.15	0.5045	0.0011
308.15	0.5943	0.0011
308.15	0.7116	0.0011
308.15	0.7855	0.0012
308.15	0.8980	0.0012
308.15	1.0000	0.0013
318.15	0.0000	0.0008
318.15	0.1034	0.0008
318.15	0.2039	0.0008
318.15	0.2930	0.0009
318.15	0.3939	0.0009
318.15	0.5045	0.0009
318.15	0.5943	0.0010
318.15	0.7116	0.0010
318.15	0.7855	0.0010
318.15	0.8980	0.0011
318.15	1.0000	0.0011

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Nonanal (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	785.08
298.15	0.1034	787.7
298.15	0.2039	790.72
298.15	0.2930	793.79
298.15	0.3939	797.7
298.15	0.5045	802.52
298.15	0.5943	806.85
298.15	0.7116	813.07
298.15	0.7855	817.31
298.15	0.8980	824.25
298.15	1.0000	831.04
308.15	0.0000	778.09
308.15	0.1034	780.37
308.15	0.2039	782.99
308.15	0.2930	785.65
308.15	0.3939	789.05
308.15	0.5045	793.24
308.15	0.5943	797.0
308.15	0.7116	802.4
308.15	0.7855	806.08
308.15	0.8980	812.11
308.15	1.0000	818.01
318.15	0.0000	763.91
318.15	0.1034	766.24
318.15	0.2039	768.92
318.15	0.2930	771.64
318.15	0.3939	775.11
318.15	0.5045	779.4
318.15	0.5943	783.24
318.15	0.7116	788.76
318.15	0.7855	792.53
318.15	0.8980	798.69
318.15	1.0000	804.72

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Nonanal (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	785.08
298.15	0.1034	787.7
298.15	0.2039	790.72
298.15	0.2930	793.79
298.15	0.3939	797.7
298.15	0.5045	802.52
298.15	0.5943	806.85
298.15	0.7116	813.07
298.15	0.7855	817.31
298.15	0.8980	824.25
298.15	1.0000	831.04
308.15	0.0000	778.09
308.15	0.1034	780.37
308.15	0.2039	782.99
308.15	0.2930	785.65
308.15	0.3939	789.05
308.15	0.5045	793.24
308.15	0.5943	797.0
308.15	0.7116	802.4
308.15	0.7855	806.08
308.15	0.8980	812.11
308.15	1.0000	818.01
318.15	0.0000	763.91
318.15	0.1034	766.24
318.15	0.2039	768.92
318.15	0.2930	771.64
318.15	0.3939	775.11
318.15	0.5045	779.4
318.15	0.5943	783.24
318.15	0.7116	788.76
318.15	0.7855	792.53
318.15	0.8980	798.69
318.15	1.0000	804.72

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)