Mixture of Benzene + 1-Propanol + Ethyl Acetate

Datasets

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

Viscosity, Pa*s [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Propanol (2) - Liquid	Mole fraction of Ethyl Acetate (3) - Liquid	Viscosity, Pa*s - Liquid
0.1875	0.6083	0.0005
0.1925	0.4062	0.0005
0.2175	0.2031	0.0005
0.2362	0.3843	0.0005
0.2460	0.5645	0.0005
0.3828	0.1603	0.0006
0.4010	0.3013	0.0007
0.4212	0.4333	0.0006
0.4572	0.2733	0.0007
0.4676	0.3986	0.0007
0.4913	0.1321	0.0007
0.4963	0.2533	0.0007
0.5222	0.3577	0.0007
0.5444	0.1183	0.0008
0.6377	0.1822	0.0009
0.6579	0.0888	0.0009
0.6854	0.1584	0.0010
0.7009	0.2239	0.0010
0.7339	0.0691	0.0011
0.7461	0.1901	0.0011
0.7479	0.0655	0.0011
0.7531	0.1242	0.0011
0.7549	0.1834	0.0011
0.7860	0.0556	0.0012
0.7964	0.1024	0.0012
0.8120	0.1407	0.0012
0.8187	0.0471	0.0012
0.8370	0.0821	0.0013
0.8443	0.0404	0.0013
0.8483	0.0763	0.0013
0.8613	0.1038	0.0013
0.8627	0.1028	0.0013
0.9090	0.0236	0.0014
0.9121	0.0658	0.0015
0.9544	0.0118	0.0016
0.9569	0.0323	0.0016
0.9618	0.0192	0.0016

Viscosity, Pa*s [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Propanol (2) - Liquid	Mole fraction of Ethyl Acetate (3) - Liquid	Viscosity, Pa*s - Liquid
0.1875	0.6083	0.0005
0.1925	0.4062	0.0005
0.2175	0.2031	0.0005
0.2362	0.3843	0.0005
0.2460	0.5645	0.0005
0.3828	0.1603	0.0006
0.4010	0.3013	0.0007
0.4212	0.4333	0.0006
0.4572	0.2733	0.0007
0.4676	0.3986	0.0007
0.4913	0.1321	0.0007
0.4963	0.2533	0.0007
0.5222	0.3577	0.0007
0.5444	0.1183	0.0008
0.6377	0.1822	0.0009
0.6579	0.0888	0.0009
0.6854	0.1584	0.0010
0.7009	0.2239	0.0010
0.7339	0.0691	0.0011
0.7461	0.1901	0.0011
0.7479	0.0655	0.0011
0.7531	0.1242	0.0011
0.7549	0.1834	0.0011
0.7860	0.0556	0.0012
0.7964	0.1024	0.0012
0.8120	0.1407	0.0012
0.8187	0.0471	0.0012
0.8370	0.0821	0.0013
0.8443	0.0404	0.0013
0.8483	0.0763	0.0013
0.8613	0.1038	0.0013
0.8627	0.1028	0.0013
0.9090	0.0236	0.0014
0.9121	0.0658	0.0015
0.9544	0.0118	0.0016
0.9569	0.0323	0.0016
0.9618	0.0192	0.0016

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Propanol (2) - Liquid	Mole fraction of Ethyl Acetate (3) - Liquid	Mass density, kg/m3 - Liquid
0.1875	0.6082	868.41
0.1925	0.4062	863.82
0.2362	0.3843	860.55
0.2460	0.5644	863.84
0.4010	0.3013	847.98
0.4212	0.4333	849.64
0.4572	0.2733	843.61
0.4676	0.3986	845.74
0.4963	0.2533	840.48
0.5222	0.3577	841.06
0.6377	0.1822	828.87
0.6854	0.1584	824.76
0.7009	0.2239	825.05
0.7461	0.1901	820.83
0.7531	0.1242	818.85
0.7549	0.1834	820.05
0.7964	0.1024	814.98
0.8120	0.1407	814.62
0.8370	0.0821	811.27
0.8483	0.0763	810.23
0.8613	0.1038	809.8
0.8627	0.1028	809.67
0.9121	0.0658	804.71
0.9569	0.0323	800.13
0.9618	0.0192	799.39

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Propanol (2) - Liquid	Mole fraction of Ethyl Acetate (3) - Liquid	Mass density, kg/m3 - Liquid
0.1875	0.6082	868.41
0.1925	0.4062	863.82
0.2362	0.3843	860.55
0.2460	0.5644	863.84
0.4010	0.3013	847.98
0.4212	0.4333	849.64
0.4572	0.2733	843.61
0.4676	0.3986	845.74
0.4963	0.2533	840.48
0.5222	0.3577	841.06
0.6377	0.1822	828.87
0.6854	0.1584	824.76
0.7009	0.2239	825.05
0.7461	0.1901	820.83
0.7531	0.1242	818.85
0.7549	0.1834	820.05
0.7964	0.1024	814.98
0.8120	0.1407	814.62
0.8370	0.0821	811.27
0.8483	0.0763	810.23
0.8613	0.1038	809.8
0.8627	0.1028	809.67
0.9121	0.0658	804.71
0.9569	0.0323	800.13
0.9618	0.0192	799.39

Sources

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