Mixture of 1-Propanol + Triethylamine + Cyclohexane

Datasets

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

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of Triethylamine (2) - Liquid	Viscosity, Pa*s - Liquid
0.0414	0.8628	0.0004
0.0745	0.8506	0.0004
0.0792	0.7375	0.0004
0.1063	0.8477	0.0004
0.1135	0.6238	0.0005
0.1371	0.7250	0.0004
0.1463	0.5151	0.0005
0.1775	0.4183	0.0006
0.1980	0.6029	0.0005
0.2061	0.3169	0.0006
0.2087	0.7010	0.0005
0.2337	0.2254	0.0007
0.2510	0.4966	0.0006
0.2563	0.1505	0.0008
0.2793	0.0742	0.0008
0.2914	0.5825	0.0005
0.2982	0.4019	0.0006
0.3435	0.3111	0.0007
0.3684	0.4721	0.0006
0.3917	0.2144	0.0008
0.4279	0.1418	0.0009
0.4325	0.3803	0.0007
0.4716	0.0542	0.0010
0.4920	0.2950	0.0008
0.5586	0.1996	0.0009
0.6102	0.1257	0.0010
0.6578	0.0575	0.0011

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of Triethylamine (2) - Liquid	Viscosity, Pa*s - Liquid
0.0414	0.8628	0.0004
0.0745	0.8506	0.0004
0.0792	0.7375	0.0004
0.1063	0.8477	0.0004
0.1135	0.6238	0.0005
0.1371	0.7250	0.0004
0.1463	0.5151	0.0005
0.1775	0.4183	0.0006
0.1980	0.6029	0.0005
0.2061	0.3169	0.0006
0.2087	0.7010	0.0005
0.2337	0.2254	0.0007
0.2510	0.4966	0.0006
0.2563	0.1505	0.0008
0.2793	0.0742	0.0008
0.2914	0.5825	0.0005
0.2982	0.4019	0.0006
0.3435	0.3111	0.0007
0.3684	0.4721	0.0006
0.3917	0.2144	0.0008
0.4279	0.1418	0.0009
0.4325	0.3803	0.0007
0.4716	0.0542	0.0010
0.4920	0.2950	0.0008
0.5586	0.1996	0.0009
0.6102	0.1257	0.0010
0.6578	0.0575	0.0011

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 313.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of Triethylamine (2) - Liquid	Mass density, kg/m3 - Liquid
0.0414	0.8628	725.37
0.0745	0.8506	727.21
0.0792	0.7375	732.25
0.1063	0.8477	728.55
0.1135	0.6238	738.9
0.1371	0.7250	735.15
0.1463	0.5151	745.48
0.1775	0.4183	751.39
0.1980	0.6029	743.12
0.2061	0.3169	757.44
0.2087	0.7010	738.79
0.2337	0.2254	762.5
0.2510	0.4966	750.09
0.2563	0.1505	766.24
0.2793	0.0742	769.59
0.2914	0.5825	747.18
0.2982	0.4019	756.22
0.3435	0.3111	761.77
0.3684	0.4721	754.93
0.3917	0.2144	767.24
0.4279	0.1418	770.91
0.4325	0.3803	761.11
0.4716	0.0542	774.64
0.4920	0.2950	766.6
0.5586	0.1996	772.33
0.6102	0.1257	776.37
0.6578	0.0575	779.77

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 313.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of Triethylamine (2) - Liquid	Mass density, kg/m3 - Liquid
0.0414	0.8628	725.37
0.0745	0.8506	727.21
0.0792	0.7375	732.25
0.1063	0.8477	728.55
0.1135	0.6238	738.9
0.1371	0.7250	735.15
0.1463	0.5151	745.48
0.1775	0.4183	751.39
0.1980	0.6029	743.12
0.2061	0.3169	757.44
0.2087	0.7010	738.79
0.2337	0.2254	762.5
0.2510	0.4966	750.09
0.2563	0.1505	766.24
0.2793	0.0742	769.59
0.2914	0.5825	747.18
0.2982	0.4019	756.22
0.3435	0.3111	761.77
0.3684	0.4721	754.93
0.3917	0.2144	767.24
0.4279	0.1418	770.91
0.4325	0.3803	761.11
0.4716	0.0542	774.64
0.4920	0.2950	766.6
0.5586	0.1996	772.33
0.6102	0.1257	776.37
0.6578	0.0575	779.77

Sources

• Volumetric and transport properties of ternary mixtures containing 1-propanol, triethylamine or tri-n-butylamine and cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model