Mixture of 1-Pentanol + 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-Pentanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
0.0525	0.7158	0.0005
0.0561	0.2271	0.0006
0.0612	0.4683	0.0005
0.0837	0.4571	0.0006
0.0900	0.2189	0.0007
0.0909	0.6868	0.0005
0.1348	0.6536	0.0006
0.1442	0.4269	0.0006
0.1623	0.2015	0.0007
0.1673	0.6291	0.0006
0.1853	0.4064	0.0006
0.2114	0.1897	0.0008
0.2403	0.5739	0.0006
0.2642	0.3671	0.0007
0.2759	0.1742	0.0008
0.2964	0.5316	0.0007
0.3012	0.3486	0.0007
0.3187	0.1639	0.0009
0.3373	0.5007	0.0007
0.3621	0.3182	0.0008
0.3886	0.1471	0.0009
0.3958	0.4565	0.0007
0.4028	0.1437	0.0010
0.4036	0.2975	0.0008
0.4588	0.2700	0.0009
0.4593	0.1301	0.0010
0.4658	0.4036	0.0008
0.5511	0.2239	0.0010
0.5986	0.0966	0.0013
0.6871	0.2364	0.0012
0.7892	0.1052	0.0017
0.7947	0.0494	0.0019
0.8818	0.0893	0.0020

Viscosity, Pa*s [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Pentanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
0.0525	0.7158	0.0005
0.0561	0.2271	0.0006
0.0612	0.4683	0.0005
0.0837	0.4571	0.0006
0.0900	0.2189	0.0007
0.0909	0.6868	0.0005
0.1348	0.6536	0.0006
0.1442	0.4269	0.0006
0.1623	0.2015	0.0007
0.1673	0.6291	0.0006
0.1853	0.4064	0.0006
0.2114	0.1897	0.0008
0.2403	0.5739	0.0006
0.2642	0.3671	0.0007
0.2759	0.1742	0.0008
0.2964	0.5316	0.0007
0.3012	0.3486	0.0007
0.3187	0.1639	0.0009
0.3373	0.5007	0.0007
0.3621	0.3182	0.0008
0.3886	0.1471	0.0009
0.3958	0.4565	0.0007
0.4028	0.1437	0.0010
0.4036	0.2975	0.0008
0.4588	0.2700	0.0009
0.4593	0.1301	0.0010
0.4658	0.4036	0.0008
0.5511	0.2239	0.0010
0.5986	0.0966	0.0013
0.6871	0.2364	0.0012
0.7892	0.1052	0.0017
0.7947	0.0494	0.0019
0.8818	0.0893	0.0020

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Pentanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.1104	0.4407	813.97
0.1139	0.6683	843.03
0.1212	0.2236	791.67
0.1868	0.2069	792.18
0.1941	0.6078	838.89
0.1998	0.3970	812.77
0.2907	0.3519	811.45
0.2979	0.1786	793.27
0.2987	0.5289	833.66
0.3700	0.3125	810.26
0.3878	0.1557	794.18
0.3929	0.4579	829.09
0.4327	0.2404	804.86
0.4612	0.4064	825.79
0.5186	0.1225	795.59
0.5435	0.2265	807.81
0.5511	0.2227	807.69
0.5869	0.3116	819.81
0.5920	0.1038	796.43
0.6871	0.2360	815.12
0.7022	0.0758	797.74
0.7053	0.1447	805.34
0.7892	0.1046	804.39
0.7932	0.1560	810.37
0.7947	0.0522	798.83
0.8818	0.0891	806.51
0.8837	0.0577	803.09
0.8908	0.0278	800.14

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Pentanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.1104	0.4407	813.97
0.1139	0.6683	843.03
0.1212	0.2236	791.67
0.1868	0.2069	792.18
0.1941	0.6078	838.89
0.1998	0.3970	812.77
0.2907	0.3519	811.45
0.2979	0.1786	793.27
0.2987	0.5289	833.66
0.3700	0.3125	810.26
0.3878	0.1557	794.18
0.3929	0.4579	829.09
0.4327	0.2404	804.86
0.4612	0.4064	825.79
0.5186	0.1225	795.59
0.5435	0.2265	807.81
0.5511	0.2227	807.69
0.5869	0.3116	819.81
0.5920	0.1038	796.43
0.6871	0.2360	815.12
0.7022	0.0758	797.74
0.7053	0.1447	805.34
0.7892	0.1046	804.39
0.7932	0.1560	810.37
0.7947	0.0522	798.83
0.8818	0.0891	806.51
0.8837	0.0577	803.09
0.8908	0.0278	800.14

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