Mixture of Dimethyl Sulfoxide + 1-Hexanol
Datasets
-
Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
-
γ - Surface tension liquid-gas, N/m (2)
Molar heat capacity at constant pressure, J/K/mol
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 0.1102 |
239.90 |
| 0.1949 |
231.70 |
| 0.2888 |
222.50 |
| 0.3759 |
216.50 |
| 0.4388 |
211.50 |
| 0.5350 |
199.20 |
| 0.5365 |
199.40 |
| 0.6311 |
190.40 |
| 0.7339 |
181.80 |
| 0.8062 |
171.00 |
| 0.8704 |
164.70 |
| 0.9359 |
158.80 |
Molar heat capacity at constant pressure, J/K/mol
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 0.1102 |
239.90 |
| 0.1949 |
231.70 |
| 0.2888 |
222.50 |
| 0.3759 |
216.50 |
| 0.4388 |
211.50 |
| 0.5350 |
199.20 |
| 0.5365 |
199.40 |
| 0.6311 |
190.40 |
| 0.7339 |
181.80 |
| 0.8062 |
171.00 |
| 0.8704 |
164.70 |
| 0.9359 |
158.80 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0682 |
0.3610 |
| 0.1277 |
0.6400 |
| 0.1801 |
0.8470 |
| 0.2265 |
1.008 |
| 0.3053 |
1.197 |
| 0.3694 |
1.297 |
| 0.4677 |
1.36 |
| 0.5394 |
1.363 |
| 0.6374 |
1.283 |
| 0.7251 |
1.165 |
| 0.7786 |
1.036 |
| 0.8406 |
0.8650 |
| 0.8755 |
0.7460 |
| 0.9134 |
0.5600 |
| 0.9336 |
0.4540 |
| 0.9547 |
0.3310 |
| 0.9768 |
0.1810 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0682 |
0.3610 |
| 0.1277 |
0.6400 |
| 0.1801 |
0.8470 |
| 0.2265 |
1.008 |
| 0.3053 |
1.197 |
| 0.3694 |
1.297 |
| 0.4677 |
1.36 |
| 0.5394 |
1.363 |
| 0.6374 |
1.283 |
| 0.7251 |
1.165 |
| 0.7786 |
1.036 |
| 0.8406 |
0.8650 |
| 0.8755 |
0.7460 |
| 0.9134 |
0.5600 |
| 0.9336 |
0.4540 |
| 0.9547 |
0.3310 |
| 0.9768 |
0.1810 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.0000 |
1.4134 |
| 0.1336 |
1.4149 |
| 0.2712 |
1.4185 |
| 0.3808 |
1.4216 |
| 0.4814 |
1.4259 |
| 0.5762 |
1.4311 |
| 0.6660 |
1.4372 |
| 0.7650 |
1.4448 |
| 0.8480 |
1.4535 |
| 0.9246 |
1.4629 |
| 1.0000 |
1.4751 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.0000 |
1.4134 |
| 0.1336 |
1.4149 |
| 0.2712 |
1.4185 |
| 0.3808 |
1.4216 |
| 0.4814 |
1.4259 |
| 0.5762 |
1.4311 |
| 0.6660 |
1.4372 |
| 0.7650 |
1.4448 |
| 0.8480 |
1.4535 |
| 0.9246 |
1.4629 |
| 1.0000 |
1.4751 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
811.8 |
| 0.1336 |
832.6 |
| 0.2712 |
857.6 |
| 0.3808 |
880.7 |
| 0.4814 |
904.6 |
| 0.5762 |
929.7 |
| 0.6660 |
956.3 |
| 0.7650 |
989.2 |
| 0.8480 |
1021.1 |
| 0.9246 |
1054.7 |
| 1.0000 |
1094.9 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
811.8 |
| 0.1336 |
832.6 |
| 0.2712 |
857.6 |
| 0.3808 |
880.7 |
| 0.4814 |
904.6 |
| 0.5762 |
929.7 |
| 0.6660 |
956.3 |
| 0.7650 |
989.2 |
| 0.8480 |
1021.1 |
| 0.9246 |
1054.7 |
| 1.0000 |
1094.9 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Speed of sound, m/s - Liquid |
| 0.0000 |
1282.0 |
| 0.1336 |
1300.8 |
| 0.2712 |
1311.6 |
| 0.3808 |
1325.3 |
| 0.4814 |
1336.5 |
| 0.5762 |
1349.5 |
| 0.6660 |
1368.0 |
| 0.7650 |
1395.0 |
| 0.8480 |
1420.5 |
| 0.9246 |
1448.5 |
| 1.0000 |
1490.9 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of Dimethyl Sulfoxide (1) - Liquid |
Speed of sound, m/s - Liquid |
| 0.0000 |
1282.0 |
| 0.1336 |
1300.8 |
| 0.2712 |
1311.6 |
| 0.3808 |
1325.3 |
| 0.4814 |
1336.5 |
| 0.5762 |
1349.5 |
| 0.6660 |
1368.0 |
| 0.7650 |
1395.0 |
| 0.8480 |
1420.5 |
| 0.9246 |
1448.5 |
| 1.0000 |
1490.9 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1-Hexanol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 288.15 |
0.0276 |
0.0388 |
| 288.15 |
0.0786 |
0.0342 |
| 288.15 |
0.1661 |
0.0318 |
| 288.15 |
0.2701 |
0.0298 |
| 288.15 |
0.3741 |
0.0287 |
| 288.15 |
0.4687 |
0.0279 |
| 288.15 |
0.5385 |
0.0275 |
| 288.15 |
0.5921 |
0.0270 |
| 288.15 |
0.6345 |
0.0265 |
| 288.15 |
0.7511 |
0.0260 |
| 288.15 |
0.9512 |
0.0255 |
| 298.15 |
0.0276 |
0.0376 |
| 298.15 |
0.0786 |
0.0336 |
| 298.15 |
0.1661 |
0.0307 |
| 298.15 |
0.2701 |
0.0293 |
| 298.15 |
0.3741 |
0.0279 |
| 298.15 |
0.4687 |
0.0273 |
| 298.15 |
0.5385 |
0.0268 |
| 298.15 |
0.5921 |
0.0262 |
| 298.15 |
0.6345 |
0.0261 |
| 298.15 |
0.7511 |
0.0259 |
| 298.15 |
0.9512 |
0.0251 |
| 308.15 |
0.0276 |
0.0375 |
| 308.15 |
0.0786 |
0.0340 |
| 308.15 |
0.1661 |
0.0310 |
| 308.15 |
0.2701 |
0.0289 |
| 308.15 |
0.3741 |
0.0277 |
| 308.15 |
0.4687 |
0.0267 |
| 308.15 |
0.5385 |
0.0263 |
| 308.15 |
0.5921 |
0.0259 |
| 308.15 |
0.6345 |
0.0256 |
| 308.15 |
0.7511 |
0.0252 |
| 308.15 |
0.9512 |
0.0248 |
| 318.15 |
0.0276 |
0.0367 |
| 318.15 |
0.0786 |
0.0334 |
| 318.15 |
0.1661 |
0.0301 |
| 318.15 |
0.2701 |
0.0282 |
| 318.15 |
0.3741 |
0.0269 |
| 318.15 |
0.4687 |
0.0262 |
| 318.15 |
0.5385 |
0.0256 |
| 318.15 |
0.5921 |
0.0251 |
| 318.15 |
0.6345 |
0.0247 |
| 318.15 |
0.7511 |
0.0244 |
| 318.15 |
0.9512 |
0.0241 |
| 328.15 |
0.0276 |
0.0352 |
| 328.15 |
0.0786 |
0.0327 |
| 328.15 |
0.1661 |
0.0290 |
| 328.15 |
0.2701 |
0.0275 |
| 328.15 |
0.3741 |
0.0262 |
| 328.15 |
0.4687 |
0.0254 |
| 328.15 |
0.5385 |
0.0250 |
| 328.15 |
0.5921 |
0.0243 |
| 328.15 |
0.6345 |
0.0240 |
| 328.15 |
0.7511 |
0.0238 |
| 328.15 |
0.9512 |
0.0231 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1-Hexanol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 288.15 |
0.0276 |
0.0388 |
| 288.15 |
0.0786 |
0.0342 |
| 288.15 |
0.1661 |
0.0318 |
| 288.15 |
0.2701 |
0.0298 |
| 288.15 |
0.3741 |
0.0287 |
| 288.15 |
0.4687 |
0.0279 |
| 288.15 |
0.5385 |
0.0275 |
| 288.15 |
0.5921 |
0.0270 |
| 288.15 |
0.6345 |
0.0265 |
| 288.15 |
0.7511 |
0.0260 |
| 288.15 |
0.9512 |
0.0255 |
| 298.15 |
0.0276 |
0.0376 |
| 298.15 |
0.0786 |
0.0336 |
| 298.15 |
0.1661 |
0.0307 |
| 298.15 |
0.2701 |
0.0293 |
| 298.15 |
0.3741 |
0.0279 |
| 298.15 |
0.4687 |
0.0273 |
| 298.15 |
0.5385 |
0.0268 |
| 298.15 |
0.5921 |
0.0262 |
| 298.15 |
0.6345 |
0.0261 |
| 298.15 |
0.7511 |
0.0259 |
| 298.15 |
0.9512 |
0.0251 |
| 308.15 |
0.0276 |
0.0375 |
| 308.15 |
0.0786 |
0.0340 |
| 308.15 |
0.1661 |
0.0310 |
| 308.15 |
0.2701 |
0.0289 |
| 308.15 |
0.3741 |
0.0277 |
| 308.15 |
0.4687 |
0.0267 |
| 308.15 |
0.5385 |
0.0263 |
| 308.15 |
0.5921 |
0.0259 |
| 308.15 |
0.6345 |
0.0256 |
| 308.15 |
0.7511 |
0.0252 |
| 308.15 |
0.9512 |
0.0248 |
| 318.15 |
0.0276 |
0.0367 |
| 318.15 |
0.0786 |
0.0334 |
| 318.15 |
0.1661 |
0.0301 |
| 318.15 |
0.2701 |
0.0282 |
| 318.15 |
0.3741 |
0.0269 |
| 318.15 |
0.4687 |
0.0262 |
| 318.15 |
0.5385 |
0.0256 |
| 318.15 |
0.5921 |
0.0251 |
| 318.15 |
0.6345 |
0.0247 |
| 318.15 |
0.7511 |
0.0244 |
| 318.15 |
0.9512 |
0.0241 |
| 328.15 |
0.0276 |
0.0352 |
| 328.15 |
0.0786 |
0.0327 |
| 328.15 |
0.1661 |
0.0290 |
| 328.15 |
0.2701 |
0.0275 |
| 328.15 |
0.3741 |
0.0262 |
| 328.15 |
0.4687 |
0.0254 |
| 328.15 |
0.5385 |
0.0250 |
| 328.15 |
0.5921 |
0.0243 |
| 328.15 |
0.6345 |
0.0240 |
| 328.15 |
0.7511 |
0.0238 |
| 328.15 |
0.9512 |
0.0231 |
Sources