Mixture of 1-Butanol + Carbon Tetrachloride

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)
3. Binary diffusion coefficient, m2/s (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon Tetrachloride (2) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0023
303.15	0.0954	0.0020
303.15	0.1918	0.0017
303.15	0.2891	0.0015
303.15	0.3875	0.0014
303.15	0.4869	0.0012
303.15	0.5874	0.0012
303.15	0.6889	0.0011
303.15	0.7401	0.0010
303.15	0.7915	0.0010
303.15	0.8432	0.0010
303.15	0.8952	0.0010
303.15	0.9475	0.0009
303.15	1.0000	0.0009
308.15	0.0000	0.0019
308.15	0.0954	0.0017
308.15	0.1918	0.0014
308.15	0.2891	0.0013
308.15	0.3875	0.0012
308.15	0.4869	0.0011
308.15	0.5874	0.0011
308.15	0.6889	0.0010
308.15	0.7401	0.0010
308.15	0.7915	0.0010
308.15	0.8432	0.0009
308.15	0.8952	0.0009
308.15	0.9475	0.0009
308.15	1.0000	0.0008
313.15	0.0000	0.0017
313.15	0.0954	0.0015
313.15	0.1918	0.0013
313.15	0.2891	0.0012
313.15	0.3875	0.0011
313.15	0.4869	0.0010
313.15	0.5874	0.0010
313.15	0.6889	0.0010
313.15	0.7401	0.0009
313.15	0.7915	0.0009
313.15	0.8432	0.0009
313.15	0.8952	0.0009
313.15	0.9475	0.0008
313.15	1.0000	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon Tetrachloride (2) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0023
303.15	0.0954	0.0020
303.15	0.1918	0.0017
303.15	0.2891	0.0015
303.15	0.3875	0.0014
303.15	0.4869	0.0012
303.15	0.5874	0.0012
303.15	0.6889	0.0011
303.15	0.7401	0.0010
303.15	0.7915	0.0010
303.15	0.8432	0.0010
303.15	0.8952	0.0010
303.15	0.9475	0.0009
303.15	1.0000	0.0009
308.15	0.0000	0.0019
308.15	0.0954	0.0017
308.15	0.1918	0.0014
308.15	0.2891	0.0013
308.15	0.3875	0.0012
308.15	0.4869	0.0011
308.15	0.5874	0.0011
308.15	0.6889	0.0010
308.15	0.7401	0.0010
308.15	0.7915	0.0010
308.15	0.8432	0.0009
308.15	0.8952	0.0009
308.15	0.9475	0.0009
308.15	1.0000	0.0008
313.15	0.0000	0.0017
313.15	0.0954	0.0015
313.15	0.1918	0.0013
313.15	0.2891	0.0012
313.15	0.3875	0.0011
313.15	0.4869	0.0010
313.15	0.5874	0.0010
313.15	0.6889	0.0010
313.15	0.7401	0.0009
313.15	0.7915	0.0009
313.15	0.8432	0.0009
313.15	0.8952	0.0009
313.15	0.9475	0.0008
313.15	1.0000	0.0008

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon Tetrachloride (2) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	805.7
303.15	0.0954	885.0
303.15	0.1918	964.8
303.15	0.2891	1044.5
303.15	0.3875	1123.5
303.15	0.4869	1201.2
303.15	0.5874	1277.3
303.15	0.6889	1352.2
303.15	0.7401	1389.9
303.15	0.7915	1427.1
303.15	0.8432	1463.6
303.15	0.8952	1501.2
303.15	0.9475	1538.9
303.15	1.0000	1580.6
308.15	0.0000	797.2
308.15	0.0954	876.0
308.15	0.1918	955.5
308.15	0.2891	1034.7
308.15	0.3875	1113.8
308.15	0.4869	1191.8
308.15	0.5874	1268.5
308.15	0.6889	1344.8
308.15	0.7401	1382.7
308.15	0.7915	1420.2
308.15	0.8432	1457.8
308.15	0.8952	1495.7
308.15	0.9475	1534.3
308.15	1.0000	1575.7
313.15	0.0000	795.5
313.15	0.0954	873.9
313.15	0.1918	953.0
313.15	0.2891	1031.7
313.15	0.3875	1110.1
313.15	0.4869	1187.6
313.15	0.5874	1264.2
313.15	0.6889	1340.9
313.15	0.7401	1378.8
313.15	0.7915	1415.9
313.15	0.8432	1454.2
313.15	0.8952	1491.8
313.15	0.9475	1530.5
313.15	1.0000	1571.3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon Tetrachloride (2) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	805.7
303.15	0.0954	885.0
303.15	0.1918	964.8
303.15	0.2891	1044.5
303.15	0.3875	1123.5
303.15	0.4869	1201.2
303.15	0.5874	1277.3
303.15	0.6889	1352.2
303.15	0.7401	1389.9
303.15	0.7915	1427.1
303.15	0.8432	1463.6
303.15	0.8952	1501.2
303.15	0.9475	1538.9
303.15	1.0000	1580.6
308.15	0.0000	797.2
308.15	0.0954	876.0
308.15	0.1918	955.5
308.15	0.2891	1034.7
308.15	0.3875	1113.8
308.15	0.4869	1191.8
308.15	0.5874	1268.5
308.15	0.6889	1344.8
308.15	0.7401	1382.7
308.15	0.7915	1420.2
308.15	0.8432	1457.8
308.15	0.8952	1495.7
308.15	0.9475	1534.3
308.15	1.0000	1575.7
313.15	0.0000	795.5
313.15	0.0954	873.9
313.15	0.1918	953.0
313.15	0.2891	1031.7
313.15	0.3875	1110.1
313.15	0.4869	1187.6
313.15	0.5874	1264.2
313.15	0.6889	1340.9
313.15	0.7401	1378.8
313.15	0.7915	1415.9
313.15	0.8432	1454.2
313.15	0.8952	1491.8
313.15	0.9475	1530.5
313.15	1.0000	1571.3

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
298.15	0.0000	0.0000
298.15	0.0300	0.0000
298.15	0.1000	0.0000
298.15	0.3000	0.0000
298.15	0.5000	0.0000
298.15	0.7000	0.0000
298.15	0.9000	0.0000
298.15	0.9700	0.0000
298.15	1.0000	0.0000
308.15	0.0000	0.0000
308.15	0.0300	0.0000
308.15	0.1000	0.0000
308.15	0.3000	0.0000
308.15	0.5000	0.0000
308.15	0.7000	0.0000
308.15	0.9000	0.0000
308.15	0.9700	0.0000
308.15	1.0000	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
298.15	0.0000	0.0000
298.15	0.0300	0.0000
298.15	0.1000	0.0000
298.15	0.3000	0.0000
298.15	0.5000	0.0000
298.15	0.7000	0.0000
298.15	0.9000	0.0000
298.15	0.9700	0.0000
298.15	1.0000	0.0000
308.15	0.0000	0.0000
308.15	0.0300	0.0000
308.15	0.1000	0.0000
308.15	0.3000	0.0000
308.15	0.5000	0.0000
308.15	0.7000	0.0000
308.15	0.9000	0.0000
308.15	0.9700	0.0000
308.15	1.0000	0.0000

Sources

• Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems