Mixture of Ethanamine, N-ethyl- + 2-Butanol

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanamine, N-ethyl- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0037
293.15	0.0221	0.0035
293.15	0.0810	0.0030
293.15	0.1601	0.0025
293.15	0.2400	0.0020
293.15	0.3494	0.0016
293.15	0.4395	0.0013
293.15	0.5602	0.0010
293.15	0.6500	0.0008
293.15	0.7400	0.0007
293.15	0.8503	0.0005
293.15	0.9400	0.0004
293.15	0.9871	0.0003
293.15	1.0000	0.0003
298.15	0.0000	0.0031
298.15	0.0221	0.0029
298.15	0.0810	0.0025
298.15	0.1601	0.0021
298.15	0.2400	0.0018
298.15	0.3494	0.0014
298.15	0.4395	0.0011
298.15	0.5602	0.0009
298.15	0.6500	0.0007
298.15	0.7400	0.0006
298.15	0.8503	0.0004
298.15	0.9400	0.0004
298.15	0.9871	0.0003
298.15	1.0000	0.0003
303.15	0.0000	0.0025
303.15	0.0221	0.0024
303.15	0.0810	0.0021
303.15	0.1601	0.0018
303.15	0.2400	0.0015
303.15	0.3494	0.0012
303.15	0.4395	0.0010
303.15	0.5602	0.0008
303.15	0.6500	0.0006
303.15	0.7400	0.0005
303.15	0.8503	0.0004
303.15	0.9400	0.0003
303.15	0.9871	0.0003
303.15	1.0000	0.0003
308.15	0.0000	0.0021
308.15	0.0221	0.0020
308.15	0.0810	0.0018
308.15	0.1601	0.0016
308.15	0.2400	0.0013
308.15	0.3494	0.0010
308.15	0.4395	0.0009
308.15	0.5602	0.0007
308.15	0.6500	0.0006
308.15	0.7400	0.0005
308.15	0.8503	0.0004
308.15	0.9400	0.0003
308.15	0.9871	0.0003
308.15	1.0000	0.0003
313.15	0.0000	0.0018
313.15	0.0221	0.0017
313.15	0.0810	0.0015
313.15	0.1601	0.0013
313.15	0.2400	0.0011
313.15	0.3494	0.0009
313.15	0.4395	0.0008
313.15	0.5602	0.0006
313.15	0.6500	0.0005
313.15	0.7400	0.0004
313.15	0.8503	0.0004
313.15	0.9400	0.0003
313.15	0.9871	0.0003
313.15	1.0000	0.0003
318.15	0.0000	0.0015
318.15	0.0221	0.0015
318.15	0.0810	0.0013
318.15	0.1601	0.0012
318.15	0.2400	0.0010
318.15	0.3494	0.0008
318.15	0.4395	0.0007
318.15	0.5602	0.0006
318.15	0.6500	0.0005
318.15	0.7400	0.0004
318.15	0.8503	0.0003
318.15	0.9400	0.0003
318.15	0.9871	0.0003
318.15	1.0000	0.0002
323.15	0.0000	0.0013
323.15	0.0221	0.0013
323.15	0.0810	0.0012
323.15	0.1601	0.0010
323.15	0.2400	0.0009
323.15	0.3494	0.0008
323.15	0.4395	0.0007
323.15	0.5602	0.0005
323.15	0.6500	0.0005
323.15	0.7400	0.0004
323.15	0.8503	0.0003
323.15	0.9400	0.0003
323.15	0.9871	0.0002
323.15	1.0000	0.0002

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanamine, N-ethyl- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	806.7
293.15	0.0221	805.4
293.15	0.0810	801.7
293.15	0.1601	796.2
293.15	0.2400	789.9
293.15	0.3494	780.4
293.15	0.4395	771.7
293.15	0.5602	759.1
293.15	0.6500	749.0
293.15	0.7400	738.3
293.15	0.8503	724.4
293.15	0.9400	712.8
293.15	0.9871	706.5
293.15	1.0000	704.8
298.15	0.0000	802.7
298.15	0.0221	801.4
298.15	0.0810	797.6
298.15	0.1601	792.0
298.15	0.2400	785.8
298.15	0.3494	776.1
298.15	0.4395	767.3
298.15	0.5602	754.5
298.15	0.6500	744.3
298.15	0.7400	733.4
298.15	0.8503	719.3
298.15	0.9400	707.5
298.15	0.9871	701.1
298.15	1.0000	699.3
303.15	0.0000	798.4
303.15	0.0221	797.1
303.15	0.0810	793.2
303.15	0.1601	787.7
303.15	0.2400	781.3
303.15	0.3494	771.6
303.15	0.4395	762.8
303.15	0.5602	749.9
303.15	0.6500	739.5
303.15	0.7400	728.5
303.15	0.8503	714.3
303.15	0.9400	702.3
303.15	0.9871	695.8
303.15	1.0000	694.0
308.15	0.0000	794.1
308.15	0.0221	792.8
308.15	0.0810	789.0
308.15	0.1601	783.4
308.15	0.2400	777.1
308.15	0.3494	767.3
308.15	0.4395	758.4
308.15	0.5602	745.4
308.15	0.6500	734.8
308.15	0.7400	723.6
308.15	0.8503	709.2
308.15	0.9400	697.0
308.15	0.9871	690.5
308.15	1.0000	688.7
313.15	0.0000	789.8
313.15	0.0221	788.5
313.15	0.0810	784.8
313.15	0.1601	779.1
313.15	0.2400	772.7
313.15	0.3494	762.9
313.15	0.4395	753.8
313.15	0.5602	740.6
313.15	0.6500	730.0
313.15	0.7400	718.7
313.15	0.8503	704.2
313.15	0.9400	691.9
313.15	0.9871	685.1
313.15	1.0000	683.3
318.15	0.0000	785.2
318.15	0.0221	783.8
318.15	0.0810	779.9
318.15	0.1601	774.2
318.15	0.2400	767.9
318.15	0.3494	758.0
318.15	0.4395	748.9
318.15	0.5602	735.6
318.15	0.6500	724.8
318.15	0.7400	713.4
318.15	0.8503	698.7
318.15	0.9400	686.3
318.15	0.9871	679.4
318.15	1.0000	677.5
323.15	0.0000	780.6
323.15	0.0221	779.3
323.15	0.0810	775.9
323.15	0.1601	770.2
323.15	0.2400	763.7
323.15	0.3494	753.7
323.15	0.4395	744.5
323.15	0.5602	731.0
323.15	0.6500	719.9
323.15	0.7400	708.3
323.15	0.8503	693.4
323.15	0.9400	680.7
323.15	0.9871	674.0
323.15	1.0000	672.1

Sources

• Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model

Note: These property values are available through the Cheméo API. A free account gives you an access key.