Mixture of Aniline + 2-Pentanol

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0040
293.15	0.0811	0.0036
293.15	0.1599	0.0032
293.15	0.2399	0.0030
293.15	0.3500	0.0028
293.15	0.4400	0.0027
293.15	0.5600	0.0027
293.15	0.6500	0.0027
293.15	0.7400	0.0029
293.15	0.8499	0.0033
293.15	0.9363	0.0038
293.15	1.0000	0.0044
298.15	0.0000	0.0034
298.15	0.0811	0.0030
298.15	0.1599	0.0027
298.15	0.2399	0.0025
298.15	0.3500	0.0024
298.15	0.4400	0.0023
298.15	0.5600	0.0023
298.15	0.6500	0.0023
298.15	0.7400	0.0025
298.15	0.8499	0.0029
298.15	0.9363	0.0033
298.15	1.0000	0.0038
303.15	0.0000	0.0029
303.15	0.0811	0.0026
303.15	0.1599	0.0023
303.15	0.2399	0.0021
303.15	0.3500	0.0019
303.15	0.4400	0.0019
303.15	0.5600	0.0018
303.15	0.6500	0.0019
303.15	0.7400	0.0020
303.15	0.8499	0.0024
303.15	0.9363	0.0027
303.15	1.0000	0.0031
308.15	0.0000	0.0025
308.15	0.0811	0.0022
308.15	0.1599	0.0020
308.15	0.2399	0.0018
308.15	0.3500	0.0016
308.15	0.4400	0.0016
308.15	0.5600	0.0016
308.15	0.6500	0.0016
308.15	0.7400	0.0018
308.15	0.8499	0.0021
308.15	0.9363	0.0024
308.15	1.0000	0.0027
313.15	0.0000	0.0020
313.15	0.0811	0.0018
313.15	0.1599	0.0016
313.15	0.2399	0.0015
313.15	0.3500	0.0014
313.15	0.4400	0.0014
313.15	0.5600	0.0014
313.15	0.6500	0.0015
313.15	0.7400	0.0016
313.15	0.8499	0.0019
313.15	0.9363	0.0022
313.15	1.0000	0.0024
318.15	0.0000	0.0016
318.15	0.0811	0.0015
318.15	0.1599	0.0013
318.15	0.2399	0.0013
318.15	0.3500	0.0012
318.15	0.4400	0.0012
318.15	0.5600	0.0012
318.15	0.6500	0.0013
318.15	0.7400	0.0014
318.15	0.8499	0.0017
318.15	0.9363	0.0019
318.15	1.0000	0.0021
323.15	0.0000	0.0013
323.15	0.0811	0.0012
323.15	0.1599	0.0011
323.15	0.2399	0.0011
323.15	0.3500	0.0010
323.15	0.4400	0.0010
323.15	0.5600	0.0011
323.15	0.6500	0.0012
323.15	0.7400	0.0013
323.15	0.8499	0.0015
323.15	0.9363	0.0018
323.15	1.0000	0.0020

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0040
293.15	0.0811	0.0036
293.15	0.1599	0.0032
293.15	0.2399	0.0030
293.15	0.3500	0.0028
293.15	0.4400	0.0027
293.15	0.5600	0.0027
293.15	0.6500	0.0027
293.15	0.7400	0.0029
293.15	0.8499	0.0033
293.15	0.9363	0.0038
293.15	1.0000	0.0044
298.15	0.0000	0.0034
298.15	0.0811	0.0030
298.15	0.1599	0.0027
298.15	0.2399	0.0025
298.15	0.3500	0.0024
298.15	0.4400	0.0023
298.15	0.5600	0.0023
298.15	0.6500	0.0023
298.15	0.7400	0.0025
298.15	0.8499	0.0029
298.15	0.9363	0.0033
298.15	1.0000	0.0038
303.15	0.0000	0.0029
303.15	0.0811	0.0026
303.15	0.1599	0.0023
303.15	0.2399	0.0021
303.15	0.3500	0.0019
303.15	0.4400	0.0019
303.15	0.5600	0.0018
303.15	0.6500	0.0019
303.15	0.7400	0.0020
303.15	0.8499	0.0024
303.15	0.9363	0.0027
303.15	1.0000	0.0031
308.15	0.0000	0.0025
308.15	0.0811	0.0022
308.15	0.1599	0.0020
308.15	0.2399	0.0018
308.15	0.3500	0.0016
308.15	0.4400	0.0016
308.15	0.5600	0.0016
308.15	0.6500	0.0016
308.15	0.7400	0.0018
308.15	0.8499	0.0021
308.15	0.9363	0.0024
308.15	1.0000	0.0027
313.15	0.0000	0.0020
313.15	0.0811	0.0018
313.15	0.1599	0.0016
313.15	0.2399	0.0015
313.15	0.3500	0.0014
313.15	0.4400	0.0014
313.15	0.5600	0.0014
313.15	0.6500	0.0015
313.15	0.7400	0.0016
313.15	0.8499	0.0019
313.15	0.9363	0.0022
313.15	1.0000	0.0024
318.15	0.0000	0.0016
318.15	0.0811	0.0015
318.15	0.1599	0.0013
318.15	0.2399	0.0013
318.15	0.3500	0.0012
318.15	0.4400	0.0012
318.15	0.5600	0.0012
318.15	0.6500	0.0013
318.15	0.7400	0.0014
318.15	0.8499	0.0017
318.15	0.9363	0.0019
318.15	1.0000	0.0021
323.15	0.0000	0.0013
323.15	0.0811	0.0012
323.15	0.1599	0.0011
323.15	0.2399	0.0011
323.15	0.3500	0.0010
323.15	0.4400	0.0010
323.15	0.5600	0.0011
323.15	0.6500	0.0012
323.15	0.7400	0.0013
323.15	0.8499	0.0015
323.15	0.9363	0.0018
323.15	1.0000	0.0020

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	809.3
293.15	0.0811	824.5
293.15	0.1599	839.5
293.15	0.2399	855.0
293.15	0.3500	877.0
293.15	0.4400	895.5
293.15	0.5600	920.8
293.15	0.6500	940.4
293.15	0.7400	960.5
293.15	0.8499	985.8
293.15	0.9363	1006.3
293.15	1.0000	1021.7
298.15	0.0000	805.3
298.15	0.0811	820.3
298.15	0.1599	835.3
298.15	0.2399	850.8
298.15	0.3500	872.7
298.15	0.4400	891.1
298.15	0.5600	916.4
298.15	0.6500	935.9
298.15	0.7400	956.0
298.15	0.8499	981.4
298.15	0.9363	1001.9
298.15	1.0000	1017.4
303.15	0.0000	801.2
303.15	0.0811	816.1
303.15	0.1599	831.0
303.15	0.2399	846.5
303.15	0.3500	868.3
303.15	0.4400	886.7
303.15	0.5600	912.0
303.15	0.6500	931.6
303.15	0.7400	951.7
303.15	0.8499	977.0
303.15	0.9363	997.6
303.15	1.0000	1013.2
308.15	0.0000	797.0
308.15	0.0811	811.8
308.15	0.1599	826.7
308.15	0.2399	842.1
308.15	0.3500	863.9
308.15	0.4400	882.3
308.15	0.5600	907.6
308.15	0.6500	927.1
308.15	0.7400	947.2
308.15	0.8499	972.7
308.15	0.9363	993.3
308.15	1.0000	1009.0
313.15	0.0000	792.7
313.15	0.0811	807.5
313.15	0.1599	822.3
313.15	0.2399	837.6
313.15	0.3500	859.4
313.15	0.4400	877.8
313.15	0.5600	903.0
313.15	0.6500	922.6
313.15	0.7400	942.8
313.15	0.8499	968.2
313.15	0.9363	989.0
313.15	1.0000	1004.7
318.15	0.0000	788.4
318.15	0.0811	803.1
318.15	0.1599	817.9
318.15	0.2399	833.2
318.15	0.3500	854.9
318.15	0.4400	873.3
318.15	0.5600	898.6
318.15	0.6500	918.1
318.15	0.7400	938.3
318.15	0.8499	963.8
318.15	0.9363	984.6
318.15	1.0000	1000.4
323.15	0.0000	784.0
323.15	0.0811	798.7
323.15	0.1599	813.3
323.15	0.2399	828.6
323.15	0.3500	850.2
323.15	0.4400	868.5
323.15	0.5600	893.7
323.15	0.6500	913.3
323.15	0.7400	933.4
323.15	0.8499	958.9
323.15	0.9363	979.7
323.15	1.0000	995.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	809.3
293.15	0.0811	824.5
293.15	0.1599	839.5
293.15	0.2399	855.0
293.15	0.3500	877.0
293.15	0.4400	895.5
293.15	0.5600	920.8
293.15	0.6500	940.4
293.15	0.7400	960.5
293.15	0.8499	985.8
293.15	0.9363	1006.3
293.15	1.0000	1021.7
298.15	0.0000	805.3
298.15	0.0811	820.3
298.15	0.1599	835.3
298.15	0.2399	850.8
298.15	0.3500	872.7
298.15	0.4400	891.1
298.15	0.5600	916.4
298.15	0.6500	935.9
298.15	0.7400	956.0
298.15	0.8499	981.4
298.15	0.9363	1001.9
298.15	1.0000	1017.4
303.15	0.0000	801.2
303.15	0.0811	816.1
303.15	0.1599	831.0
303.15	0.2399	846.5
303.15	0.3500	868.3
303.15	0.4400	886.7
303.15	0.5600	912.0
303.15	0.6500	931.6
303.15	0.7400	951.7
303.15	0.8499	977.0
303.15	0.9363	997.6
303.15	1.0000	1013.2
308.15	0.0000	797.0
308.15	0.0811	811.8
308.15	0.1599	826.7
308.15	0.2399	842.1
308.15	0.3500	863.9
308.15	0.4400	882.3
308.15	0.5600	907.6
308.15	0.6500	927.1
308.15	0.7400	947.2
308.15	0.8499	972.7
308.15	0.9363	993.3
308.15	1.0000	1009.0
313.15	0.0000	792.7
313.15	0.0811	807.5
313.15	0.1599	822.3
313.15	0.2399	837.6
313.15	0.3500	859.4
313.15	0.4400	877.8
313.15	0.5600	903.0
313.15	0.6500	922.6
313.15	0.7400	942.8
313.15	0.8499	968.2
313.15	0.9363	989.0
313.15	1.0000	1004.7
318.15	0.0000	788.4
318.15	0.0811	803.1
318.15	0.1599	817.9
318.15	0.2399	833.2
318.15	0.3500	854.9
318.15	0.4400	873.3
318.15	0.5600	898.6
318.15	0.6500	918.1
318.15	0.7400	938.3
318.15	0.8499	963.8
318.15	0.9363	984.6
318.15	1.0000	1000.4
323.15	0.0000	784.0
323.15	0.0811	798.7
323.15	0.1599	813.3
323.15	0.2399	828.6
323.15	0.3500	850.2
323.15	0.4400	868.5
323.15	0.5600	893.7
323.15	0.6500	913.3
323.15	0.7400	933.4
323.15	0.8499	958.9
323.15	0.9363	979.7
323.15	1.0000	995.5

Sources

• Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline