Mixture of 1,2-Ethanediol + Benzyl alcohol
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
ρl - Mass density, kg/m3 (2)
-
γ - Surface tension liquid-gas, N/m (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101.32 (Liquid)
- Temperature, K = 308.15 (Liquid)
Mole fraction of 1,2-Ethanediol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0719 |
0.1157 |
0.1341 |
0.1712 |
0.1886 |
0.2017 |
0.2365 |
0.2090 |
0.3173 |
0.2143 |
0.3826 |
0.2105 |
0.4817 |
0.2010 |
0.5533 |
0.1912 |
0.6502 |
0.1680 |
0.7361 |
0.1383 |
0.7880 |
0.1180 |
0.8480 |
0.0860 |
0.8815 |
0.0712 |
0.9177 |
0.0477 |
0.9370 |
0.0366 |
0.9571 |
0.0252 |
0.9781 |
0.0125 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101.32 (Liquid)
- Temperature, K = 308.15 (Liquid)
Mole fraction of 1,2-Ethanediol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0719 |
0.1157 |
0.1341 |
0.1712 |
0.1886 |
0.2017 |
0.2365 |
0.2090 |
0.3173 |
0.2143 |
0.3826 |
0.2105 |
0.4817 |
0.2010 |
0.5533 |
0.1912 |
0.6502 |
0.1680 |
0.7361 |
0.1383 |
0.7880 |
0.1180 |
0.8480 |
0.0860 |
0.8815 |
0.0712 |
0.9177 |
0.0477 |
0.9370 |
0.0366 |
0.9571 |
0.0252 |
0.9781 |
0.0125 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101.32 (Liquid)
- Temperature, K = 308.15 (Liquid)
Mole fraction of 1,2-Ethanediol (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0395 |
1035.06 |
0.1313 |
1038.54 |
0.2622 |
1044.29 |
0.3189 |
1047.1 |
0.4645 |
1055.28 |
0.5057 |
1057.9 |
0.6090 |
1065.04 |
0.6863 |
1071.03 |
0.7371 |
1075.32 |
0.8097 |
1081.99 |
0.8790 |
1088.96 |
0.9638 |
1098.48 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101.32 (Liquid)
- Temperature, K = 308.15 (Liquid)
Mole fraction of 1,2-Ethanediol (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0395 |
1035.06 |
0.1313 |
1038.54 |
0.2622 |
1044.29 |
0.3189 |
1047.1 |
0.4645 |
1055.28 |
0.5057 |
1057.9 |
0.6090 |
1065.04 |
0.6863 |
1071.03 |
0.7371 |
1075.32 |
0.8097 |
1081.99 |
0.8790 |
1088.96 |
0.9638 |
1098.48 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Benzyl alcohol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0484 |
293.15 |
0.0319 |
0.0478 |
293.15 |
0.0535 |
0.0474 |
293.15 |
0.0727 |
0.0471 |
293.15 |
0.0854 |
0.0467 |
293.15 |
0.1118 |
0.0459 |
293.15 |
0.2060 |
0.0441 |
293.15 |
0.2633 |
0.0429 |
293.15 |
0.3883 |
0.0415 |
293.15 |
0.5596 |
0.0406 |
293.15 |
0.7394 |
0.0394 |
293.15 |
0.9101 |
0.0393 |
293.15 |
1.0000 |
0.0391 |
298.15 |
0.0000 |
0.0480 |
298.15 |
0.0319 |
0.0474 |
298.15 |
0.0535 |
0.0470 |
298.15 |
0.0727 |
0.0467 |
298.15 |
0.0854 |
0.0462 |
298.15 |
0.1118 |
0.0454 |
298.15 |
0.2060 |
0.0436 |
298.15 |
0.2633 |
0.0424 |
298.15 |
0.3883 |
0.0411 |
298.15 |
0.5596 |
0.0402 |
298.15 |
0.7394 |
0.0389 |
298.15 |
0.9101 |
0.0388 |
298.15 |
1.0000 |
0.0386 |
303.15 |
0.0000 |
0.0476 |
303.15 |
0.0319 |
0.0469 |
303.15 |
0.0535 |
0.0465 |
303.15 |
0.0727 |
0.0461 |
303.15 |
0.0854 |
0.0458 |
303.15 |
0.1118 |
0.0449 |
303.15 |
0.2060 |
0.0431 |
303.15 |
0.2633 |
0.0419 |
303.15 |
0.3883 |
0.0406 |
303.15 |
0.5596 |
0.0397 |
303.15 |
0.7394 |
0.0384 |
303.15 |
0.9101 |
0.0383 |
303.15 |
1.0000 |
0.0381 |
308.15 |
0.0000 |
0.0472 |
308.15 |
0.0319 |
0.0465 |
308.15 |
0.0535 |
0.0461 |
308.15 |
0.0727 |
0.0457 |
308.15 |
0.0854 |
0.0453 |
308.15 |
0.1118 |
0.0445 |
308.15 |
0.2060 |
0.0426 |
308.15 |
0.2633 |
0.0414 |
308.15 |
0.3883 |
0.0401 |
308.15 |
0.5596 |
0.0392 |
308.15 |
0.7394 |
0.0379 |
308.15 |
0.9101 |
0.0378 |
308.15 |
1.0000 |
0.0376 |
313.15 |
0.0000 |
0.0468 |
313.15 |
0.0319 |
0.0461 |
313.15 |
0.0535 |
0.0457 |
313.15 |
0.0727 |
0.0453 |
313.15 |
0.0854 |
0.0449 |
313.15 |
0.1118 |
0.0440 |
313.15 |
0.2060 |
0.0421 |
313.15 |
0.2633 |
0.0408 |
313.15 |
0.3883 |
0.0397 |
313.15 |
0.5596 |
0.0388 |
313.15 |
0.7394 |
0.0375 |
313.15 |
0.9101 |
0.0374 |
313.15 |
1.0000 |
0.0372 |
318.15 |
0.0000 |
0.0464 |
318.15 |
0.0319 |
0.0457 |
318.15 |
0.0535 |
0.0452 |
318.15 |
0.0727 |
0.0449 |
318.15 |
0.0854 |
0.0444 |
318.15 |
0.1118 |
0.0435 |
318.15 |
0.2060 |
0.0417 |
318.15 |
0.2633 |
0.0404 |
318.15 |
0.3883 |
0.0392 |
318.15 |
0.5596 |
0.0383 |
318.15 |
0.7394 |
0.0370 |
318.15 |
0.9101 |
0.0368 |
318.15 |
1.0000 |
0.0366 |
323.15 |
0.0000 |
0.0460 |
323.15 |
0.0319 |
0.0453 |
323.15 |
0.0535 |
0.0448 |
323.15 |
0.0727 |
0.0443 |
323.15 |
0.0854 |
0.0439 |
323.15 |
0.1118 |
0.0431 |
323.15 |
0.2060 |
0.0412 |
323.15 |
0.2633 |
0.0399 |
323.15 |
0.3883 |
0.0388 |
323.15 |
0.5596 |
0.0378 |
323.15 |
0.7394 |
0.0365 |
323.15 |
0.9101 |
0.0364 |
323.15 |
1.0000 |
0.0362 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Benzyl alcohol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0484 |
293.15 |
0.0319 |
0.0478 |
293.15 |
0.0535 |
0.0474 |
293.15 |
0.0727 |
0.0471 |
293.15 |
0.0854 |
0.0467 |
293.15 |
0.1118 |
0.0459 |
293.15 |
0.2060 |
0.0441 |
293.15 |
0.2633 |
0.0429 |
293.15 |
0.3883 |
0.0415 |
293.15 |
0.5596 |
0.0406 |
293.15 |
0.7394 |
0.0394 |
293.15 |
0.9101 |
0.0393 |
293.15 |
1.0000 |
0.0391 |
298.15 |
0.0000 |
0.0480 |
298.15 |
0.0319 |
0.0474 |
298.15 |
0.0535 |
0.0470 |
298.15 |
0.0727 |
0.0467 |
298.15 |
0.0854 |
0.0462 |
298.15 |
0.1118 |
0.0454 |
298.15 |
0.2060 |
0.0436 |
298.15 |
0.2633 |
0.0424 |
298.15 |
0.3883 |
0.0411 |
298.15 |
0.5596 |
0.0402 |
298.15 |
0.7394 |
0.0389 |
298.15 |
0.9101 |
0.0388 |
298.15 |
1.0000 |
0.0386 |
303.15 |
0.0000 |
0.0476 |
303.15 |
0.0319 |
0.0469 |
303.15 |
0.0535 |
0.0465 |
303.15 |
0.0727 |
0.0461 |
303.15 |
0.0854 |
0.0458 |
303.15 |
0.1118 |
0.0449 |
303.15 |
0.2060 |
0.0431 |
303.15 |
0.2633 |
0.0419 |
303.15 |
0.3883 |
0.0406 |
303.15 |
0.5596 |
0.0397 |
303.15 |
0.7394 |
0.0384 |
303.15 |
0.9101 |
0.0383 |
303.15 |
1.0000 |
0.0381 |
308.15 |
0.0000 |
0.0472 |
308.15 |
0.0319 |
0.0465 |
308.15 |
0.0535 |
0.0461 |
308.15 |
0.0727 |
0.0457 |
308.15 |
0.0854 |
0.0453 |
308.15 |
0.1118 |
0.0445 |
308.15 |
0.2060 |
0.0426 |
308.15 |
0.2633 |
0.0414 |
308.15 |
0.3883 |
0.0401 |
308.15 |
0.5596 |
0.0392 |
308.15 |
0.7394 |
0.0379 |
308.15 |
0.9101 |
0.0378 |
308.15 |
1.0000 |
0.0376 |
313.15 |
0.0000 |
0.0468 |
313.15 |
0.0319 |
0.0461 |
313.15 |
0.0535 |
0.0457 |
313.15 |
0.0727 |
0.0453 |
313.15 |
0.0854 |
0.0449 |
313.15 |
0.1118 |
0.0440 |
313.15 |
0.2060 |
0.0421 |
313.15 |
0.2633 |
0.0408 |
313.15 |
0.3883 |
0.0397 |
313.15 |
0.5596 |
0.0388 |
313.15 |
0.7394 |
0.0375 |
313.15 |
0.9101 |
0.0374 |
313.15 |
1.0000 |
0.0372 |
318.15 |
0.0000 |
0.0464 |
318.15 |
0.0319 |
0.0457 |
318.15 |
0.0535 |
0.0452 |
318.15 |
0.0727 |
0.0449 |
318.15 |
0.0854 |
0.0444 |
318.15 |
0.1118 |
0.0435 |
318.15 |
0.2060 |
0.0417 |
318.15 |
0.2633 |
0.0404 |
318.15 |
0.3883 |
0.0392 |
318.15 |
0.5596 |
0.0383 |
318.15 |
0.7394 |
0.0370 |
318.15 |
0.9101 |
0.0368 |
318.15 |
1.0000 |
0.0366 |
323.15 |
0.0000 |
0.0460 |
323.15 |
0.0319 |
0.0453 |
323.15 |
0.0535 |
0.0448 |
323.15 |
0.0727 |
0.0443 |
323.15 |
0.0854 |
0.0439 |
323.15 |
0.1118 |
0.0431 |
323.15 |
0.2060 |
0.0412 |
323.15 |
0.2633 |
0.0399 |
323.15 |
0.3883 |
0.0388 |
323.15 |
0.5596 |
0.0378 |
323.15 |
0.7394 |
0.0365 |
323.15 |
0.9101 |
0.0364 |
323.15 |
1.0000 |
0.0362 |
Sources