Mixture of 1-Butanol + Ethyl Acetate + 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-Butanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
0.0538	0.4748	0.0005
0.0544	0.7088	0.0004
0.0611	0.2246	0.0006
0.0901	0.2177	0.0006
0.1030	0.6723	0.0005
0.1047	0.4493	0.0005
0.1535	0.6345	0.0005
0.1692	0.1988	0.0007
0.1959	0.6027	0.0005
0.2088	0.1893	0.0007
0.2584	0.5559	0.0006
0.2632	0.3697	0.0006
0.2866	0.1707	0.0008
0.2883	0.3571	0.0006
0.3127	0.3449	0.0006
0.3146	0.3439	0.0006
0.3258	0.1613	0.0008
0.3313	0.5012	0.0006
0.3935	0.4546	0.0007
0.3954	0.3034	0.0007
0.4021	0.1430	0.0009
0.4272	0.4293	0.0007
0.4473	0.2773	0.0008
0.4658	0.1278	0.0009
0.4856	0.2581	0.0008
0.4883	0.3835	0.0008
0.5008	0.1194	0.0010
0.6281	0.2788	0.0009
0.6393	0.1810	0.0010
0.6417	0.0857	0.0012
0.8220	0.0426	0.0016
0.8268	0.1298	0.0014
0.8282	0.0862	0.0015

Viscosity, Pa*s [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
0.0538	0.4748	0.0005
0.0544	0.7088	0.0004
0.0611	0.2246	0.0006
0.0901	0.2177	0.0006
0.1030	0.6723	0.0005
0.1047	0.4493	0.0005
0.1535	0.6345	0.0005
0.1692	0.1988	0.0007
0.1959	0.6027	0.0005
0.2088	0.1893	0.0007
0.2584	0.5559	0.0006
0.2632	0.3697	0.0006
0.2866	0.1707	0.0008
0.2883	0.3571	0.0006
0.3127	0.3449	0.0006
0.3146	0.3439	0.0006
0.3258	0.1613	0.0008
0.3313	0.5012	0.0006
0.3935	0.4546	0.0007
0.3954	0.3034	0.0007
0.4021	0.1430	0.0009
0.4272	0.4293	0.0007
0.4473	0.2773	0.0008
0.4658	0.1278	0.0009
0.4856	0.2581	0.0008
0.4883	0.3835	0.0008
0.5008	0.1194	0.0010
0.6281	0.2788	0.0009
0.6393	0.1810	0.0010
0.6417	0.0857	0.0012
0.8220	0.0426	0.0016
0.8268	0.1298	0.0014
0.8282	0.0862	0.0015

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.1247	0.2223	791.53
0.1291	0.4112	811.53
0.1612	0.6177	839.26
0.2325	0.3624	810.38
0.2423	0.1925	792.48
0.2896	0.5231	833.58
0.3371	0.3130	809.2
0.3404	0.4858	831.33
0.3414	0.1673	793.38
0.3445	0.1665	793.37
0.4191	0.4278	827.91
0.4306	0.2688	808.19
0.4599	0.3977	826.17
0.5268	0.2234	807.09
0.5343	0.3430	822.88
0.5728	0.1085	795.62
0.6281	0.2739	818.76
0.6393	0.1703	805.81
0.6417	0.0910	796.36
0.7255	0.2021	814.41
0.7291	0.1279	804.82
0.7356	0.0672	797.62
0.8220	0.0452	798.85
0.8268	0.1275	809.75
0.8282	0.0811	803.7
0.9029	0.0458	802.88
0.9169	0.0211	800.42

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.1247	0.2223	791.53
0.1291	0.4112	811.53
0.1612	0.6177	839.26
0.2325	0.3624	810.38
0.2423	0.1925	792.48
0.2896	0.5231	833.58
0.3371	0.3130	809.2
0.3404	0.4858	831.33
0.3414	0.1673	793.38
0.3445	0.1665	793.37
0.4191	0.4278	827.91
0.4306	0.2688	808.19
0.4599	0.3977	826.17
0.5268	0.2234	807.09
0.5343	0.3430	822.88
0.5728	0.1085	795.62
0.6281	0.2739	818.76
0.6393	0.1703	805.81
0.6417	0.0910	796.36
0.7255	0.2021	814.41
0.7291	0.1279	804.82
0.7356	0.0672	797.62
0.8220	0.0452	798.85
0.8268	0.1275	809.75
0.8282	0.0811	803.7
0.9029	0.0458	802.88
0.9169	0.0211	800.42

Sources

• Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model