Mixture of Ethanol, 2,2'-oxybis- + 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
Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	303.15	0.0225
0.0970	303.15	0.0191
0.1980	303.15	0.0163
0.3190	303.15	0.0138
0.4140	303.15	0.0122
0.4990	303.15	0.0112
0.6140	303.15	0.0102
0.6980	303.15	0.0097
0.7890	303.15	0.0094
0.8870	303.15	0.0094
1.0000	303.15	0.0104
0.0000	313.15	0.0149
0.0970	313.15	0.0129
0.1980	313.15	0.0112
0.3190	313.15	0.0096
0.4140	313.15	0.0087
0.4990	313.15	0.0081
0.6140	313.15	0.0075
0.6980	313.15	0.0073
0.7890	313.15	0.0071
0.8870	313.15	0.0072
1.0000	313.15	0.0081
0.0000	323.15	0.0104
0.0970	323.15	0.0091
0.1980	323.15	0.0080
0.3190	323.15	0.0070
0.4140	323.15	0.0065
0.4990	323.15	0.0061
0.6140	323.15	0.0057
0.6980	323.15	0.0056
0.7890	323.15	0.0055
0.8870	323.15	0.0057
1.0000	323.15	0.0065
0.0000	333.15	0.0076
0.0970	333.15	0.0067
0.1980	333.15	0.0060
0.3190	333.15	0.0053
0.4140	333.15	0.0050
0.4990	333.15	0.0047
0.6140	333.15	0.0045
0.6980	333.15	0.0045
0.7890	333.15	0.0045
0.8870	333.15	0.0046
1.0000	333.15	0.0052
0.0000	343.15	0.0057
0.0970	343.15	0.0052
0.1980	343.15	0.0046
0.3190	343.15	0.0042
0.4140	343.15	0.0039
0.4990	343.15	0.0038
0.6140	343.15	0.0036
0.6980	343.15	0.0036
0.7890	343.15	0.0037
0.8870	343.15	0.0038
1.0000	343.15	0.0043

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	303.15	0.0225
0.0970	303.15	0.0191
0.1980	303.15	0.0163
0.3190	303.15	0.0138
0.4140	303.15	0.0122
0.4990	303.15	0.0112
0.6140	303.15	0.0102
0.6980	303.15	0.0097
0.7890	303.15	0.0094
0.8870	303.15	0.0094
1.0000	303.15	0.0104
0.0000	313.15	0.0149
0.0970	313.15	0.0129
0.1980	313.15	0.0112
0.3190	313.15	0.0096
0.4140	313.15	0.0087
0.4990	313.15	0.0081
0.6140	313.15	0.0075
0.6980	313.15	0.0073
0.7890	313.15	0.0071
0.8870	313.15	0.0072
1.0000	313.15	0.0081
0.0000	323.15	0.0104
0.0970	323.15	0.0091
0.1980	323.15	0.0080
0.3190	323.15	0.0070
0.4140	323.15	0.0065
0.4990	323.15	0.0061
0.6140	323.15	0.0057
0.6980	323.15	0.0056
0.7890	323.15	0.0055
0.8870	323.15	0.0057
1.0000	323.15	0.0065
0.0000	333.15	0.0076
0.0970	333.15	0.0067
0.1980	333.15	0.0060
0.3190	333.15	0.0053
0.4140	333.15	0.0050
0.4990	333.15	0.0047
0.6140	333.15	0.0045
0.6980	333.15	0.0045
0.7890	333.15	0.0045
0.8870	333.15	0.0046
1.0000	333.15	0.0052
0.0000	343.15	0.0057
0.0970	343.15	0.0052
0.1980	343.15	0.0046
0.3190	343.15	0.0042
0.4140	343.15	0.0039
0.4990	343.15	0.0038
0.6140	343.15	0.0036
0.6980	343.15	0.0036
0.7890	343.15	0.0037
0.8870	343.15	0.0038
1.0000	343.15	0.0043

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	303.15	1110.0
0.0970	303.15	1125.0
0.1980	303.15	1140.0
0.3190	303.15	1158.2
0.4140	303.15	1172.2
0.4990	303.15	1185.2
0.6140	303.15	1202.9
0.6980	303.15	1215.6
0.7890	303.15	1229.7
0.8870	303.15	1245.0
1.0000	303.15	1262.9
0.0000	313.15	1103.0
0.0970	313.15	1117.6
0.1980	313.15	1132.5
0.3190	313.15	1150.3
0.4140	313.15	1164.2
0.4990	313.15	1176.9
0.6140	313.15	1194.5
0.6980	313.15	1207.1
0.7890	313.15	1221.1
0.8870	313.15	1236.3
1.0000	313.15	1254.1
0.0000	323.15	1095.9
0.0970	323.15	1110.2
0.1980	323.15	1124.8
0.3190	323.15	1142.3
0.4140	323.15	1156.1
0.4990	323.15	1168.6
0.6140	323.15	1186.0
0.6980	323.15	1198.5
0.7890	323.15	1212.5
0.8870	323.15	1227.5
1.0000	323.15	1245.2
0.0000	333.15	1088.5
0.0970	333.15	1102.7
0.1980	333.15	1117.0
0.3190	333.15	1134.2
0.4140	333.15	1147.8
0.4990	333.15	1160.3
0.6140	333.15	1177.5
0.6980	333.15	1190.0
0.7890	333.15	1203.8
0.8870	333.15	1218.8
1.0000	333.15	1236.6
0.0000	343.15	1081.1
0.0970	343.15	1094.9
0.1980	343.15	1109.1
0.3190	343.15	1126.1
0.4140	343.15	1139.6
0.4990	343.15	1151.9
0.6140	343.15	1169.0
0.6980	343.15	1181.3
0.7890	343.15	1195.1
0.8870	343.15	1210.1
1.0000	343.15	1228.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	303.15	1110.0
0.0970	303.15	1125.0
0.1980	303.15	1140.0
0.3190	303.15	1158.2
0.4140	303.15	1172.2
0.4990	303.15	1185.2
0.6140	303.15	1202.9
0.6980	303.15	1215.6
0.7890	303.15	1229.7
0.8870	303.15	1245.0
1.0000	303.15	1262.9
0.0000	313.15	1103.0
0.0970	313.15	1117.6
0.1980	313.15	1132.5
0.3190	313.15	1150.3
0.4140	313.15	1164.2
0.4990	313.15	1176.9
0.6140	313.15	1194.5
0.6980	313.15	1207.1
0.7890	313.15	1221.1
0.8870	313.15	1236.3
1.0000	313.15	1254.1
0.0000	323.15	1095.9
0.0970	323.15	1110.2
0.1980	323.15	1124.8
0.3190	323.15	1142.3
0.4140	323.15	1156.1
0.4990	323.15	1168.6
0.6140	323.15	1186.0
0.6980	323.15	1198.5
0.7890	323.15	1212.5
0.8870	323.15	1227.5
1.0000	323.15	1245.2
0.0000	333.15	1088.5
0.0970	333.15	1102.7
0.1980	333.15	1117.0
0.3190	333.15	1134.2
0.4140	333.15	1147.8
0.4990	333.15	1160.3
0.6140	333.15	1177.5
0.6980	333.15	1190.0
0.7890	333.15	1203.8
0.8870	333.15	1218.8
1.0000	333.15	1236.6
0.0000	343.15	1081.1
0.0970	343.15	1094.9
0.1980	343.15	1109.1
0.3190	343.15	1126.1
0.4140	343.15	1139.6
0.4990	343.15	1151.9
0.6140	343.15	1169.0
0.6980	343.15	1181.3
0.7890	343.15	1195.1
0.8870	343.15	1210.1
1.0000	343.15	1228.1

Sources

• Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures