Mixture of Aniline + Thiophene, tetrahydro-, 1,1-dioxide

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0102
303.15	0.1000	0.0091
303.15	0.1955	0.0082
303.15	0.3007	0.0073
303.15	0.3902	0.0066
303.15	0.4997	0.0059
303.15	0.6003	0.0052
303.15	0.7027	0.0047
303.15	0.7982	0.0042
303.15	0.8995	0.0037
303.15	1.0000	0.0032
308.15	0.0000	0.0089
308.15	0.1000	0.0080
308.15	0.1955	0.0072
308.15	0.3007	0.0064
308.15	0.3902	0.0058
308.15	0.4997	0.0051
308.15	0.6003	0.0046
308.15	0.7027	0.0040
308.15	0.7982	0.0036
308.15	0.8995	0.0032
308.15	1.0000	0.0028
313.15	0.0000	0.0079
313.15	0.1000	0.0070
313.15	0.1955	0.0063
313.15	0.3007	0.0056
313.15	0.3902	0.0051
313.15	0.4997	0.0045
313.15	0.6003	0.0040
313.15	0.7027	0.0035
313.15	0.7982	0.0031
313.15	0.8995	0.0027
313.15	1.0000	0.0024

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0102
303.15	0.1000	0.0091
303.15	0.1955	0.0082
303.15	0.3007	0.0073
303.15	0.3902	0.0066
303.15	0.4997	0.0059
303.15	0.6003	0.0052
303.15	0.7027	0.0047
303.15	0.7982	0.0042
303.15	0.8995	0.0037
303.15	1.0000	0.0032
308.15	0.0000	0.0089
308.15	0.1000	0.0080
308.15	0.1955	0.0072
308.15	0.3007	0.0064
308.15	0.3902	0.0058
308.15	0.4997	0.0051
308.15	0.6003	0.0046
308.15	0.7027	0.0040
308.15	0.7982	0.0036
308.15	0.8995	0.0032
308.15	1.0000	0.0028
313.15	0.0000	0.0079
313.15	0.1000	0.0070
313.15	0.1955	0.0063
313.15	0.3007	0.0056
313.15	0.3902	0.0051
313.15	0.4997	0.0045
313.15	0.6003	0.0040
313.15	0.7027	0.0035
313.15	0.7982	0.0031
313.15	0.8995	0.0027
313.15	1.0000	0.0024

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	1260.1
303.15	0.1000	1238.3
303.15	0.1955	1217.0
303.15	0.3007	1192.6
303.15	0.3902	1171.4
303.15	0.4997	1144.7
303.15	0.6003	1119.6
303.15	0.7027	1093.4
303.15	0.7982	1068.3
303.15	0.8995	1040.8
303.15	1.0000	1013.0
308.15	0.0000	1255.7
308.15	0.1000	1233.9
308.15	0.1955	1212.6
308.15	0.3007	1188.3
308.15	0.3902	1167.0
308.15	0.4997	1140.3
308.15	0.6003	1115.3
308.15	0.7027	1089.1
308.15	0.7982	1064.0
308.15	0.8995	1036.5
308.15	1.0000	1008.7
313.15	0.0000	1251.3
313.15	0.1000	1229.5
313.15	0.1955	1208.2
313.15	0.3007	1183.9
313.15	0.3902	1162.7
313.15	0.4997	1136.0
313.15	0.6003	1111.0
313.15	0.7027	1084.8
313.15	0.7982	1059.7
313.15	0.8995	1032.2
313.15	1.0000	1004.4

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	1260.1
303.15	0.1000	1238.3
303.15	0.1955	1217.0
303.15	0.3007	1192.6
303.15	0.3902	1171.4
303.15	0.4997	1144.7
303.15	0.6003	1119.6
303.15	0.7027	1093.4
303.15	0.7982	1068.3
303.15	0.8995	1040.8
303.15	1.0000	1013.0
308.15	0.0000	1255.7
308.15	0.1000	1233.9
308.15	0.1955	1212.6
308.15	0.3007	1188.3
308.15	0.3902	1167.0
308.15	0.4997	1140.3
308.15	0.6003	1115.3
308.15	0.7027	1089.1
308.15	0.7982	1064.0
308.15	0.8995	1036.5
308.15	1.0000	1008.7
313.15	0.0000	1251.3
313.15	0.1000	1229.5
313.15	0.1955	1208.2
313.15	0.3007	1183.9
313.15	0.3902	1162.7
313.15	0.4997	1136.0
313.15	0.6003	1111.0
313.15	0.7027	1084.8
313.15	0.7982	1059.7
313.15	0.8995	1032.2
313.15	1.0000	1004.4

Sources

• Volumetric and transport properties of binary liquid mixtures of sulfolane with aniline, N,N-dimethylaniline and N,N-diethylaniline at different temperatures and atmospheric pressure