Mixture of Dimethyl Sulfoxide + Tetrahydrofuran
Datasets
-
Activity coefficient (2)
-
Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
-
η - Viscosity, Pa*s (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
ρl - Mass density, kg/m3 (2)
Activity coefficient of Tetrahydrofuran (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Activity coefficient of Tetrahydrofuran (2) - Liquid |
| 298.15 |
0.0000 |
3.32 |
Activity coefficient of Tetrahydrofuran (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Activity coefficient of Tetrahydrofuran (2) - Liquid |
| 298.15 |
0.0000 |
3.32 |
Molar heat capacity at constant pressure, J/K/mol
[ref]
Operational conditions:
- Temperature, K = 308.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 0.0807 |
132.90 |
| 0.1171 |
133.60 |
| 0.2353 |
135.90 |
| 0.3233 |
137.70 |
| 0.4932 |
141.40 |
| 0.5284 |
142.30 |
| 0.5833 |
143.60 |
| 0.6359 |
144.90 |
| 0.7298 |
147.20 |
| 0.8269 |
149.80 |
| 0.8930 |
151.60 |
| 0.9507 |
153.20 |
Molar heat capacity at constant pressure, J/K/mol
[ref]
Operational conditions:
- Temperature, K = 308.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 0.0807 |
132.90 |
| 0.1171 |
133.60 |
| 0.2353 |
135.90 |
| 0.3233 |
137.70 |
| 0.4932 |
141.40 |
| 0.5284 |
142.30 |
| 0.5833 |
143.60 |
| 0.6359 |
144.90 |
| 0.7298 |
147.20 |
| 0.8269 |
149.80 |
| 0.8930 |
151.60 |
| 0.9507 |
153.20 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mass fraction of Tetrahydrofuran (2) - Liquid |
Viscosity, Pa*s - Liquid |
| 0.0000 |
0.0020 |
| 0.2500 |
0.0015 |
| 0.5000 |
0.0011 |
| 0.7500 |
0.0007 |
| 1.0000 |
0.0005 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mass fraction of Tetrahydrofuran (2) - Liquid |
Viscosity, Pa*s - Liquid |
| 0.0000 |
0.0020 |
| 0.2500 |
0.0015 |
| 0.5000 |
0.0011 |
| 0.7500 |
0.0007 |
| 1.0000 |
0.0005 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 308.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0457 |
0.2130 |
| 0.0875 |
0.3720 |
| 0.1257 |
0.4900 |
| 0.1608 |
0.5790 |
| 0.2233 |
0.6990 |
| 0.2771 |
0.7650 |
| 0.3651 |
0.8530 |
| 0.4339 |
0.8700 |
| 0.5349 |
0.8740 |
| 0.6332 |
0.8390 |
| 0.6970 |
0.7730 |
| 0.7753 |
0.6820 |
| 0.8215 |
0.5880 |
| 0.8735 |
0.4740 |
| 0.9020 |
0.4000 |
| 0.9325 |
0.2910 |
| 0.9650 |
0.1630 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 308.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0457 |
0.2130 |
| 0.0875 |
0.3720 |
| 0.1257 |
0.4900 |
| 0.1608 |
0.5790 |
| 0.2233 |
0.6990 |
| 0.2771 |
0.7650 |
| 0.3651 |
0.8530 |
| 0.4339 |
0.8700 |
| 0.5349 |
0.8740 |
| 0.6332 |
0.8390 |
| 0.6970 |
0.7730 |
| 0.7753 |
0.6820 |
| 0.8215 |
0.5880 |
| 0.8735 |
0.4740 |
| 0.9020 |
0.4000 |
| 0.9325 |
0.2910 |
| 0.9650 |
0.1630 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mass fraction of Tetrahydrofuran (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
1095.8 |
| 0.2500 |
1036.7 |
| 0.5000 |
984.7 |
| 0.7500 |
934.0 |
| 1.0000 |
881.1 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mass fraction of Tetrahydrofuran (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
1095.8 |
| 0.2500 |
1036.7 |
| 0.5000 |
984.7 |
| 0.7500 |
934.0 |
| 1.0000 |
881.1 |
Sources