Mixture of 1-Propanol + Ethyl Acetate + Cyclohexane

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 (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
0.0666	0.6980	0.0005
0.0722	0.2319	0.0006
0.0736	0.4861	0.0005
0.1302	0.2175	0.0006
0.1309	0.6499	0.0005
0.1441	0.4491	0.0005
0.1923	0.6040	0.0005
0.2062	0.1985	0.0006
0.2091	0.4150	0.0006
0.2496	0.5611	0.0005
0.2592	0.3887	0.0006
0.2637	0.1841	0.0007
0.3085	0.5171	0.0005
0.3187	0.3575	0.0006
0.3202	0.1700	0.0007
0.3407	0.1648	0.0007
0.3664	0.3325	0.0006
0.3684	0.4723	0.0006
0.3886	0.4572	0.0006
0.4314	0.1422	0.0008
0.4346	0.2967	0.0007
0.4539	0.4084	0.0006
0.4802	0.2727	0.0007
0.4907	0.1273	0.0008
0.5216	0.3577	0.0007
0.5295	0.2469	0.0007
0.5510	0.1123	0.0009
0.6717	0.2455	0.0009
0.6718	0.1722	0.0009
0.6794	0.0801	0.0011
0.8427	0.1176	0.0013
0.8447	0.0815	0.0013
0.8570	0.0359	0.0014

Viscosity, Pa*s [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Viscosity, Pa*s - Liquid
0.0666	0.6980	0.0005
0.0722	0.2319	0.0006
0.0736	0.4861	0.0005
0.1302	0.2175	0.0006
0.1309	0.6499	0.0005
0.1441	0.4491	0.0005
0.1923	0.6040	0.0005
0.2062	0.1985	0.0006
0.2091	0.4150	0.0006
0.2496	0.5611	0.0005
0.2592	0.3887	0.0006
0.2637	0.1841	0.0007
0.3085	0.5171	0.0005
0.3187	0.3575	0.0006
0.3202	0.1700	0.0007
0.3407	0.1648	0.0007
0.3664	0.3325	0.0006
0.3684	0.4723	0.0006
0.3886	0.4572	0.0006
0.4314	0.1422	0.0008
0.4346	0.2967	0.0007
0.4539	0.4084	0.0006
0.4802	0.2727	0.0007
0.4907	0.1273	0.0008
0.5216	0.3577	0.0007
0.5295	0.2469	0.0007
0.5510	0.1123	0.0009
0.6717	0.2455	0.0009
0.6718	0.1722	0.0009
0.6794	0.0801	0.0011
0.8427	0.1176	0.0013
0.8447	0.0815	0.0013
0.8570	0.0359	0.0014

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.1247	0.4593	816.71
0.1460	0.2135	790.53
0.1553	0.6316	841.08
0.2567	0.3900	814.15
0.2702	0.1825	790.78
0.2765	0.5410	835.59
0.3785	0.3261	811.64
0.3834	0.1542	791.09
0.4086	0.4423	829.4
0.4828	0.2714	809.42
0.4897	0.1276	791.55
0.5112	0.3655	824.39
0.5794	0.2207	807.16
0.5867	0.1033	791.92
0.6065	0.2943	819.49
0.6717	0.2455	815.92
0.6718	0.1722	804.93
0.6794	0.0801	792.48
0.7641	0.0590	793.02
0.7641	0.1764	810.57
0.7671	0.1222	802.45
0.8427	0.1176	805.83
0.8447	0.0815	800.25
0.8570	0.0358	793.79
0.9193	0.0603	800.98
0.9258	0.0389	797.86
0.9311	0.0172	794.72

Mass density, kg/m3 [ref]

Operational conditions:

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

Fixed		Measured
Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.1247	0.4593	816.71
0.1460	0.2135	790.53
0.1553	0.6316	841.08
0.2567	0.3900	814.15
0.2702	0.1825	790.78
0.2765	0.5410	835.59
0.3785	0.3261	811.64
0.3834	0.1542	791.09
0.4086	0.4423	829.4
0.4828	0.2714	809.42
0.4897	0.1276	791.55
0.5112	0.3655	824.39
0.5794	0.2207	807.16
0.5867	0.1033	791.92
0.6065	0.2943	819.49
0.6717	0.2455	815.92
0.6718	0.1722	804.93
0.6794	0.0801	792.48
0.7641	0.0590	793.02
0.7641	0.1764	810.57
0.7671	0.1222	802.45
0.8427	0.1176	805.83
0.8447	0.0815	800.25
0.8570	0.0358	793.79
0.9193	0.0603	800.98
0.9258	0.0389	797.86
0.9311	0.0172	794.72

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