- Name
- 1,2-Ethanediol
- InChI
- InChI=1S/C2H6O2/c3-1-2-4/h3-4H,1-2H2
- InChI Key
- LYCAIKOWRPUZTN-UHFFFAOYSA-N
- Formula
- C2H6O2
- SMILES
- OCCO
- Mol. Weight (g/mol)
- 62.07
- CAS
- 107-21-1
- Name
- Formamide, N,N-dimethyl-
- InChI
- InChI=1S/C3H7NO/c1-4(2)3-5/h3H,1-2H3
- InChI Key
- ZMXDDKWLCZADIW-UHFFFAOYSA-N
- Formula
- C3H7NO
- SMILES
- CN(C)C=O
- Mol. Weight (g/mol)
- 73.09
- CAS
- 68-12-2
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
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Datasets
- η - Viscosity, Pa*s (2)
- Molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
- csound,fluid - Speed of Sound, m/s (2)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of 1,2-Ethanediol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.5408 | 0.0031 |
| 298.15 | 0.2929 | 0.3824 | 0.0036 |
| 298.15 | 0.4825 | 0.2799 | 0.0037 |
| 298.15 | 0.6152 | 0.2081 | 0.0035 |
| 298.15 | 0.7132 | 0.1551 | 0.0032 |
| 298.15 | 0.7886 | 0.1143 | 0.0029 |
| 298.15 | 0.8484 | 0.0820 | 0.0024 |
| 298.15 | 0.8969 | 0.0557 | 0.0020 |
| 298.15 | 0.9372 | 0.0339 | 0.0017 |
| 298.15 | 0.9711 | 0.0156 | 0.0013 |
| 298.15 | 1.0000 | 0.0000 | 0.0009 |
| 308.15 | 0.0000 | 0.5408 | 0.0025 |
| 308.15 | 0.2929 | 0.3824 | 0.0027 |
| 308.15 | 0.4825 | 0.2799 | 0.0027 |
| 308.15 | 0.6152 | 0.2081 | 0.0026 |
| 308.15 | 0.7132 | 0.1551 | 0.0024 |
| 308.15 | 0.7886 | 0.1143 | 0.0022 |
| 308.15 | 0.8484 | 0.0820 | 0.0019 |
| 308.15 | 0.8969 | 0.0557 | 0.0015 |
| 308.15 | 0.9372 | 0.0339 | 0.0013 |
| 308.15 | 0.9711 | 0.0156 | 0.0011 |
| 308.15 | 1.0000 | 0.0000 | 0.0007 |
| 318.15 | 0.0000 | 0.5408 | 0.0020 |
| 318.15 | 0.2929 | 0.3824 | 0.0022 |
| 318.15 | 0.4825 | 0.2799 | 0.0022 |
| 318.15 | 0.6152 | 0.2081 | 0.0021 |
| 318.15 | 0.7132 | 0.1551 | 0.0019 |
| 318.15 | 0.7886 | 0.1143 | 0.0018 |
| 318.15 | 0.8484 | 0.0820 | 0.0015 |
| 318.15 | 0.8969 | 0.0557 | 0.0013 |
| 318.15 | 0.9372 | 0.0339 | 0.0011 |
| 318.15 | 0.9711 | 0.0156 | 0.0009 |
| 318.15 | 1.0000 | 0.0000 | 0.0006 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of 1,2-Ethanediol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.5408 | 0.0031 |
| 298.15 | 0.2929 | 0.3824 | 0.0036 |
| 298.15 | 0.4825 | 0.2799 | 0.0037 |
| 298.15 | 0.6152 | 0.2081 | 0.0035 |
| 298.15 | 0.7132 | 0.1551 | 0.0032 |
| 298.15 | 0.7886 | 0.1143 | 0.0029 |
| 298.15 | 0.8484 | 0.0820 | 0.0024 |
| 298.15 | 0.8969 | 0.0557 | 0.0020 |
| 298.15 | 0.9372 | 0.0339 | 0.0017 |
| 298.15 | 0.9711 | 0.0156 | 0.0013 |
| 298.15 | 1.0000 | 0.0000 | 0.0009 |
| 308.15 | 0.0000 | 0.5408 | 0.0025 |
| 308.15 | 0.2929 | 0.3824 | 0.0027 |
| 308.15 | 0.4825 | 0.2799 | 0.0027 |
| 308.15 | 0.6152 | 0.2081 | 0.0026 |
| 308.15 | 0.7132 | 0.1551 | 0.0024 |
| 308.15 | 0.7886 | 0.1143 | 0.0022 |
| 308.15 | 0.8484 | 0.0820 | 0.0019 |
| 308.15 | 0.8969 | 0.0557 | 0.0015 |
| 308.15 | 0.9372 | 0.0339 | 0.0013 |
| 308.15 | 0.9711 | 0.0156 | 0.0011 |
| 308.15 | 1.0000 | 0.0000 | 0.0007 |
| 318.15 | 0.0000 | 0.5408 | 0.0020 |
| 318.15 | 0.2929 | 0.3824 | 0.0022 |
| 318.15 | 0.4825 | 0.2799 | 0.0022 |
| 318.15 | 0.6152 | 0.2081 | 0.0021 |
| 318.15 | 0.7132 | 0.1551 | 0.0019 |
| 318.15 | 0.7886 | 0.1143 | 0.0018 |
| 318.15 | 0.8484 | 0.0820 | 0.0015 |
| 318.15 | 0.8969 | 0.0557 | 0.0013 |
| 318.15 | 0.9372 | 0.0339 | 0.0011 |
| 318.15 | 0.9711 | 0.0156 | 0.0009 |
| 318.15 | 1.0000 | 0.0000 | 0.0006 |
Molar enthalpy of dilution, kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Solvent: Molality, mol/kg of 1,2-Ethanediol (1) - Liquid | Initial molality of solute, mol/kg - Liquid | Final molality of solute, mol/kg - Liquid | Molar enthalpy of dilution, kJ/mol - Liquid |
| 0.0000 | 2.0169 | 0.3593 | -0.9852 |
| 0.0000 | 2.0169 | 0.4010 | -0.9654 |
| 0.0000 | 2.0169 | 0.4523 | -0.9364 |
| 0.0000 | 2.0169 | 0.5181 | -0.8843 |
| 0.0000 | 2.0169 | 0.6084 | -0.8293 |
| 0.0000 | 2.0169 | 0.7388 | -0.7389 |
| 0.0000 | 2.0169 | 1.1403 | -0.4962 |
| 0.0000 | 2.0169 | 1.281 | -0.4106 |
| 0.0000 | 2.0169 | 1.3817 | -0.3547 |
| 0.0000 | 2.0169 | 1.4569 | -0.3113 |
| 0.0000 | 2.0169 | 1.5164 | -0.2818 |
| 0.0000 | 2.0169 | 1.5655 | -0.2507 |
| 0.5000 | 1.9945 | 0.3971 | -0.9124 |
| 0.5000 | 1.9945 | 0.4478 | -0.8773 |
| 0.5000 | 1.9945 | 0.5129 | -0.8418 |
| 0.5000 | 1.9945 | 0.6023 | -0.7827 |
| 0.5000 | 1.9945 | 0.7314 | -0.7018 |
| 0.5000 | 1.9945 | 0.9271 | -0.5858 |
| 0.5000 | 1.9945 | 1.1284 | -0.4648 |
| 0.5000 | 1.9945 | 1.2676 | -0.3883 |
| 0.5000 | 1.9945 | 1.3671 | -0.3349 |
| 0.5000 | 1.9945 | 1.4413 | -0.2909 |
| 0.5000 | 1.9945 | 1.5002 | -0.2608 |
| 0.5000 | 1.9945 | 1.5487 | -0.2337 |
| 0.9979 | 1.9768 | 0.3529 | -0.8925 |
| 0.9979 | 1.9768 | 0.3938 | -0.8697 |
| 0.9979 | 1.9768 | 0.4441 | -0.8404 |
| 0.9979 | 1.9768 | 0.5087 | -0.8009 |
| 0.9979 | 1.9768 | 0.5973 | -0.7466 |
| 0.9979 | 1.9768 | 0.7253 | -0.6671 |
| 0.9979 | 1.9768 | 0.9193 | -0.5551 |
| 0.9979 | 1.9768 | 1.1188 | -0.4446 |
| 0.9979 | 1.9768 | 1.2567 | -0.3701 |
| 0.9979 | 1.9768 | 1.3553 | -0.3164 |
| 0.9979 | 1.9768 | 1.4289 | -0.2770 |
| 0.9979 | 1.9768 | 1.4872 | -0.2478 |
| 0.9979 | 1.9768 | 1.5353 | -0.2217 |
| 1.4968 | 1.9772 | 0.3539 | -0.8419 |
| 1.4968 | 1.9772 | 0.3949 | -0.8137 |
| 1.4968 | 1.9772 | 0.4453 | -0.7912 |
| 1.4968 | 1.9772 | 0.5100 | -0.7550 |
| 1.4968 | 1.9772 | 0.5988 | -0.7028 |
| 1.4968 | 1.9772 | 0.7269 | -0.6304 |
| 1.4968 | 1.9772 | 0.9211 | -0.5226 |
| 1.4968 | 1.9772 | 1.1206 | -0.4198 |
| 1.4968 | 1.9772 | 1.2584 | -0.3489 |
| 1.4968 | 1.9772 | 1.357 | -0.2985 |
| 1.4968 | 1.9772 | 1.4305 | -0.2625 |
| 1.4968 | 1.9772 | 1.4887 | -0.2339 |
| 1.4968 | 1.9772 | 1.5367 | -0.2096 |
| 1.8034 | 1.9785 | 0.3546 | -0.8184 |
| 1.8034 | 1.9785 | 0.3957 | -0.7839 |
| 1.8034 | 1.9785 | 0.4462 | -0.7677 |
| 1.8034 | 1.9785 | 0.5110 | -0.7291 |
| 1.8034 | 1.9785 | 0.5999 | -0.6841 |
| 1.8034 | 1.9785 | 0.7281 | -0.6105 |
| 1.8034 | 1.9785 | 0.9224 | -0.5104 |
| 1.8034 | 1.9785 | 1.1221 | -0.4062 |
| 1.8034 | 1.9785 | 1.26 | -0.3388 |
| 1.8034 | 1.9785 | 1.3585 | -0.2904 |
| 1.8034 | 1.9785 | 1.432 | -0.2537 |
| 1.8034 | 1.9785 | 1.4903 | -0.2269 |
| 1.8034 | 1.9785 | 1.5382 | -0.2041 |
| 2.0628 | 1.9644 | 0.3509 | -0.7850 |
| 2.0628 | 1.9644 | 0.3915 | -0.7616 |
| 2.0628 | 1.9644 | 0.4416 | -0.7405 |
| 2.0628 | 1.9644 | 0.5058 | -0.7054 |
| 2.0628 | 1.9644 | 0.5939 | -0.6599 |
| 2.0628 | 1.9644 | 0.7210 | -0.5881 |
| 2.0628 | 1.9644 | 0.9138 | -0.4907 |
| 2.0628 | 1.9644 | 1.1121 | -0.3905 |
| 2.0628 | 1.9644 | 1.2491 | -0.3258 |
| 2.0628 | 1.9644 | 1.3471 | -0.2800 |
| 2.0628 | 1.9644 | 1.4202 | -0.2439 |
| 2.0628 | 1.9644 | 1.4781 | -0.2185 |
| 2.0628 | 1.9644 | 1.5259 | -0.1960 |
| 2.4784 | 1.9847 | 0.3538 | -0.7629 |
| 2.4784 | 1.9847 | 0.3948 | -0.7365 |
| 2.4784 | 1.9847 | 0.4453 | -0.7130 |
| 2.4784 | 1.9847 | 0.5101 | -0.6787 |
| 2.4784 | 1.9847 | 0.5990 | -0.6382 |
| 2.4784 | 1.9847 | 0.7274 | -0.5665 |
| 2.4784 | 1.9847 | 0.9221 | -0.4718 |
| 2.4784 | 1.9847 | 1.1224 | -0.3782 |
| 2.4784 | 1.9847 | 1.2609 | -0.3135 |
| 2.4784 | 1.9847 | 1.36 | -0.2682 |
| 2.4784 | 1.9847 | 1.4339 | -0.2362 |
| 2.4784 | 1.9847 | 1.4925 | -0.2097 |
| 2.4784 | 1.9847 | 1.5408 | -0.1888 |
| 3.0034 | 1.9779 | 0.3523 | -0.7265 |
| 3.0034 | 1.9779 | 0.3932 | -0.7034 |
| 3.0034 | 1.9779 | 0.4434 | -0.6773 |
| 3.0034 | 1.9779 | 0.5080 | -0.6473 |
| 3.0034 | 1.9779 | 0.5966 | -0.6012 |
| 3.0034 | 1.9779 | 0.7245 | -0.5368 |
| 3.0034 | 1.9779 | 0.9185 | -0.4461 |
| 3.0034 | 1.9779 | 1.1181 | -0.3576 |
| 3.0034 | 1.9779 | 1.2562 | -0.2956 |
| 3.0034 | 1.9779 | 1.355 | -0.2524 |
| 3.0034 | 1.9779 | 1.4286 | -0.2199 |
| 3.0034 | 1.9779 | 1.4871 | -0.1943 |
| 3.0034 | 1.9779 | 1.5352 | -0.1745 |
| 3.9755 | 1.9784 | 0.3526 | -0.6470 |
| 3.9755 | 1.9784 | 0.3935 | -0.6346 |
| 3.9755 | 1.9784 | 0.4438 | -0.6138 |
| 3.9755 | 1.9784 | 0.5084 | -0.5819 |
| 3.9755 | 1.9784 | 0.5970 | -0.5439 |
| 3.9755 | 1.9784 | 0.7250 | -0.4840 |
| 3.9755 | 1.9784 | 0.9191 | -0.4014 |
| 3.9755 | 1.9784 | 1.1188 | -0.3208 |
| 3.9755 | 1.9784 | 1.2568 | -0.2667 |
| 3.9755 | 1.9784 | 1.3556 | -0.2269 |
| 3.9755 | 1.9784 | 1.4293 | -0.1985 |
| 3.9755 | 1.9784 | 1.4877 | -0.1772 |
| 3.9755 | 1.9784 | 1.5359 | -0.1582 |
| 4.9755 | 1.9986 | 0.3561 | -0.5834 |
| 4.9755 | 1.9986 | 0.3974 | -0.5705 |
| 4.9755 | 1.9986 | 0.4482 | -0.5545 |
| 4.9755 | 1.9986 | 0.5134 | -0.5233 |
| 4.9755 | 1.9986 | 0.6029 | -0.4903 |
| 4.9755 | 1.9986 | 0.7321 | -0.4368 |
| 4.9755 | 1.9986 | 0.9282 | -0.3615 |
| 4.9755 | 1.9986 | 1.1299 | -0.2870 |
| 4.9755 | 1.9986 | 1.2694 | -0.2388 |
| 4.9755 | 1.9986 | 1.3692 | -0.2029 |
| 4.9755 | 1.9986 | 1.4437 | -0.1772 |
| 4.9755 | 1.9986 | 1.5027 | -0.1579 |
| 4.9755 | 1.9986 | 1.5513 | -0.1409 |
Molar enthalpy of dilution, kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Solvent: Molality, mol/kg of 1,2-Ethanediol (1) - Liquid | Initial molality of solute, mol/kg - Liquid | Final molality of solute, mol/kg - Liquid | Molar enthalpy of dilution, kJ/mol - Liquid |
| 0.0000 | 2.0169 | 0.3593 | -0.9852 |
| 0.0000 | 2.0169 | 0.4010 | -0.9654 |
| 0.0000 | 2.0169 | 0.4523 | -0.9364 |
| 0.0000 | 2.0169 | 0.5181 | -0.8843 |
| 0.0000 | 2.0169 | 0.6084 | -0.8293 |
| 0.0000 | 2.0169 | 0.7388 | -0.7389 |
| 0.0000 | 2.0169 | 1.1403 | -0.4962 |
| 0.0000 | 2.0169 | 1.281 | -0.4106 |
| 0.0000 | 2.0169 | 1.3817 | -0.3547 |
| 0.0000 | 2.0169 | 1.4569 | -0.3113 |
| 0.0000 | 2.0169 | 1.5164 | -0.2818 |
| 0.0000 | 2.0169 | 1.5655 | -0.2507 |
| 0.5000 | 1.9945 | 0.3971 | -0.9124 |
| 0.5000 | 1.9945 | 0.4478 | -0.8773 |
| 0.5000 | 1.9945 | 0.5129 | -0.8418 |
| 0.5000 | 1.9945 | 0.6023 | -0.7827 |
| 0.5000 | 1.9945 | 0.7314 | -0.7018 |
| 0.5000 | 1.9945 | 0.9271 | -0.5858 |
| 0.5000 | 1.9945 | 1.1284 | -0.4648 |
| 0.5000 | 1.9945 | 1.2676 | -0.3883 |
| 0.5000 | 1.9945 | 1.3671 | -0.3349 |
| 0.5000 | 1.9945 | 1.4413 | -0.2909 |
| 0.5000 | 1.9945 | 1.5002 | -0.2608 |
| 0.5000 | 1.9945 | 1.5487 | -0.2337 |
| 0.9979 | 1.9768 | 0.3529 | -0.8925 |
| 0.9979 | 1.9768 | 0.3938 | -0.8697 |
| 0.9979 | 1.9768 | 0.4441 | -0.8404 |
| 0.9979 | 1.9768 | 0.5087 | -0.8009 |
| 0.9979 | 1.9768 | 0.5973 | -0.7466 |
| 0.9979 | 1.9768 | 0.7253 | -0.6671 |
| 0.9979 | 1.9768 | 0.9193 | -0.5551 |
| 0.9979 | 1.9768 | 1.1188 | -0.4446 |
| 0.9979 | 1.9768 | 1.2567 | -0.3701 |
| 0.9979 | 1.9768 | 1.3553 | -0.3164 |
| 0.9979 | 1.9768 | 1.4289 | -0.2770 |
| 0.9979 | 1.9768 | 1.4872 | -0.2478 |
| 0.9979 | 1.9768 | 1.5353 | -0.2217 |
| 1.4968 | 1.9772 | 0.3539 | -0.8419 |
| 1.4968 | 1.9772 | 0.3949 | -0.8137 |
| 1.4968 | 1.9772 | 0.4453 | -0.7912 |
| 1.4968 | 1.9772 | 0.5100 | -0.7550 |
| 1.4968 | 1.9772 | 0.5988 | -0.7028 |
| 1.4968 | 1.9772 | 0.7269 | -0.6304 |
| 1.4968 | 1.9772 | 0.9211 | -0.5226 |
| 1.4968 | 1.9772 | 1.1206 | -0.4198 |
| 1.4968 | 1.9772 | 1.2584 | -0.3489 |
| 1.4968 | 1.9772 | 1.357 | -0.2985 |
| 1.4968 | 1.9772 | 1.4305 | -0.2625 |
| 1.4968 | 1.9772 | 1.4887 | -0.2339 |
| 1.4968 | 1.9772 | 1.5367 | -0.2096 |
| 1.8034 | 1.9785 | 0.3546 | -0.8184 |
| 1.8034 | 1.9785 | 0.3957 | -0.7839 |
| 1.8034 | 1.9785 | 0.4462 | -0.7677 |
| 1.8034 | 1.9785 | 0.5110 | -0.7291 |
| 1.8034 | 1.9785 | 0.5999 | -0.6841 |
| 1.8034 | 1.9785 | 0.7281 | -0.6105 |
| 1.8034 | 1.9785 | 0.9224 | -0.5104 |
| 1.8034 | 1.9785 | 1.1221 | -0.4062 |
| 1.8034 | 1.9785 | 1.26 | -0.3388 |
| 1.8034 | 1.9785 | 1.3585 | -0.2904 |
| 1.8034 | 1.9785 | 1.432 | -0.2537 |
| 1.8034 | 1.9785 | 1.4903 | -0.2269 |
| 1.8034 | 1.9785 | 1.5382 | -0.2041 |
| 2.0628 | 1.9644 | 0.3509 | -0.7850 |
| 2.0628 | 1.9644 | 0.3915 | -0.7616 |
| 2.0628 | 1.9644 | 0.4416 | -0.7405 |
| 2.0628 | 1.9644 | 0.5058 | -0.7054 |
| 2.0628 | 1.9644 | 0.5939 | -0.6599 |
| 2.0628 | 1.9644 | 0.7210 | -0.5881 |
| 2.0628 | 1.9644 | 0.9138 | -0.4907 |
| 2.0628 | 1.9644 | 1.1121 | -0.3905 |
| 2.0628 | 1.9644 | 1.2491 | -0.3258 |
| 2.0628 | 1.9644 | 1.3471 | -0.2800 |
| 2.0628 | 1.9644 | 1.4202 | -0.2439 |
| 2.0628 | 1.9644 | 1.4781 | -0.2185 |
| 2.0628 | 1.9644 | 1.5259 | -0.1960 |
| 2.4784 | 1.9847 | 0.3538 | -0.7629 |
| 2.4784 | 1.9847 | 0.3948 | -0.7365 |
| 2.4784 | 1.9847 | 0.4453 | -0.7130 |
| 2.4784 | 1.9847 | 0.5101 | -0.6787 |
| 2.4784 | 1.9847 | 0.5990 | -0.6382 |
| 2.4784 | 1.9847 | 0.7274 | -0.5665 |
| 2.4784 | 1.9847 | 0.9221 | -0.4718 |
| 2.4784 | 1.9847 | 1.1224 | -0.3782 |
| 2.4784 | 1.9847 | 1.2609 | -0.3135 |
| 2.4784 | 1.9847 | 1.36 | -0.2682 |
| 2.4784 | 1.9847 | 1.4339 | -0.2362 |
| 2.4784 | 1.9847 | 1.4925 | -0.2097 |
| 2.4784 | 1.9847 | 1.5408 | -0.1888 |
| 3.0034 | 1.9779 | 0.3523 | -0.7265 |
| 3.0034 | 1.9779 | 0.3932 | -0.7034 |
| 3.0034 | 1.9779 | 0.4434 | -0.6773 |
| 3.0034 | 1.9779 | 0.5080 | -0.6473 |
| 3.0034 | 1.9779 | 0.5966 | -0.6012 |
| 3.0034 | 1.9779 | 0.7245 | -0.5368 |
| 3.0034 | 1.9779 | 0.9185 | -0.4461 |
| 3.0034 | 1.9779 | 1.1181 | -0.3576 |
| 3.0034 | 1.9779 | 1.2562 | -0.2956 |
| 3.0034 | 1.9779 | 1.355 | -0.2524 |
| 3.0034 | 1.9779 | 1.4286 | -0.2199 |
| 3.0034 | 1.9779 | 1.4871 | -0.1943 |
| 3.0034 | 1.9779 | 1.5352 | -0.1745 |
| 3.9755 | 1.9784 | 0.3526 | -0.6470 |
| 3.9755 | 1.9784 | 0.3935 | -0.6346 |
| 3.9755 | 1.9784 | 0.4438 | -0.6138 |
| 3.9755 | 1.9784 | 0.5084 | -0.5819 |
| 3.9755 | 1.9784 | 0.5970 | -0.5439 |
| 3.9755 | 1.9784 | 0.7250 | -0.4840 |
| 3.9755 | 1.9784 | 0.9191 | -0.4014 |
| 3.9755 | 1.9784 | 1.1188 | -0.3208 |
| 3.9755 | 1.9784 | 1.2568 | -0.2667 |
| 3.9755 | 1.9784 | 1.3556 | -0.2269 |
| 3.9755 | 1.9784 | 1.4293 | -0.1985 |
| 3.9755 | 1.9784 | 1.4877 | -0.1772 |
| 3.9755 | 1.9784 | 1.5359 | -0.1582 |
| 4.9755 | 1.9986 | 0.3561 | -0.5834 |
| 4.9755 | 1.9986 | 0.3974 | -0.5705 |
| 4.9755 | 1.9986 | 0.4482 | -0.5545 |
| 4.9755 | 1.9986 | 0.5134 | -0.5233 |
| 4.9755 | 1.9986 | 0.6029 | -0.4903 |
| 4.9755 | 1.9986 | 0.7321 | -0.4368 |
| 4.9755 | 1.9986 | 0.9282 | -0.3615 |
| 4.9755 | 1.9986 | 1.1299 | -0.2870 |
| 4.9755 | 1.9986 | 1.2694 | -0.2388 |
| 4.9755 | 1.9986 | 1.3692 | -0.2029 |
| 4.9755 | 1.9986 | 1.4437 | -0.1772 |
| 4.9755 | 1.9986 | 1.5027 | -0.1579 |
| 4.9755 | 1.9986 | 1.5513 | -0.1409 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of 1,2-Ethanediol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 0.5408 | 1024.8 |
| 298.15 | 0.2929 | 0.3824 | 1027.9 |
| 298.15 | 0.4825 | 0.2799 | 1029.4 |
| 298.15 | 0.6152 | 0.2081 | 1030.1 |
| 298.15 | 0.7132 | 0.1551 | 1029.1 |
| 298.15 | 0.7886 | 0.1143 | 1025.9 |
| 298.15 | 0.8484 | 0.0820 | 1022.2 |
| 298.15 | 0.8969 | 0.0557 | 1015.6 |
| 298.15 | 0.9372 | 0.0339 | 1009.4 |
| 298.15 | 0.9711 | 0.0156 | 1002.8 |
| 298.15 | 1.0000 | 0.0000 | 997.1 |
| 308.15 | 0.0000 | 0.5408 | 1016.8 |
| 308.15 | 0.2929 | 0.3824 | 1020.0 |
| 308.15 | 0.4825 | 0.2799 | 1023.4 |
| 308.15 | 0.6152 | 0.2081 | 1023.7 |
| 308.15 | 0.7132 | 0.1551 | 1021.4 |
| 308.15 | 0.7886 | 0.1143 | 1018.5 |
| 308.15 | 0.8484 | 0.0820 | 1014.9 |
| 308.15 | 0.8969 | 0.0557 | 1010.2 |
| 308.15 | 0.9372 | 0.0339 | 1004.1 |
| 308.15 | 0.9711 | 0.0156 | 998.5 |
| 308.15 | 1.0000 | 0.0000 | 994.1 |
| 318.15 | 0.0000 | 0.5408 | 1008.2 |
| 318.15 | 0.2929 | 0.3824 | 1011.1 |
| 318.15 | 0.4825 | 0.2799 | 1014.6 |
| 318.15 | 0.6152 | 0.2081 | 1016.0 |
| 318.15 | 0.7132 | 0.1551 | 1014.7 |
| 318.15 | 0.7886 | 0.1143 | 1011.6 |
| 318.15 | 0.8484 | 0.0820 | 1007.9 |
| 318.15 | 0.8969 | 0.0557 | 1003.0 |
| 318.15 | 0.9372 | 0.0339 | 997.9 |
| 318.15 | 0.9711 | 0.0156 | 993.7 |
| 318.15 | 1.0000 | 0.0000 | 990.3 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of 1,2-Ethanediol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 0.5408 | 1024.8 |
| 298.15 | 0.2929 | 0.3824 | 1027.9 |
| 298.15 | 0.4825 | 0.2799 | 1029.4 |
| 298.15 | 0.6152 | 0.2081 | 1030.1 |
| 298.15 | 0.7132 | 0.1551 | 1029.1 |
| 298.15 | 0.7886 | 0.1143 | 1025.9 |
| 298.15 | 0.8484 | 0.0820 | 1022.2 |
| 298.15 | 0.8969 | 0.0557 | 1015.6 |
| 298.15 | 0.9372 | 0.0339 | 1009.4 |
| 298.15 | 0.9711 | 0.0156 | 1002.8 |
| 298.15 | 1.0000 | 0.0000 | 997.1 |
| 308.15 | 0.0000 | 0.5408 | 1016.8 |
| 308.15 | 0.2929 | 0.3824 | 1020.0 |
| 308.15 | 0.4825 | 0.2799 | 1023.4 |
| 308.15 | 0.6152 | 0.2081 | 1023.7 |
| 308.15 | 0.7132 | 0.1551 | 1021.4 |
| 308.15 | 0.7886 | 0.1143 | 1018.5 |
| 308.15 | 0.8484 | 0.0820 | 1014.9 |
| 308.15 | 0.8969 | 0.0557 | 1010.2 |
| 308.15 | 0.9372 | 0.0339 | 1004.1 |
| 308.15 | 0.9711 | 0.0156 | 998.5 |
| 308.15 | 1.0000 | 0.0000 | 994.1 |
| 318.15 | 0.0000 | 0.5408 | 1008.2 |
| 318.15 | 0.2929 | 0.3824 | 1011.1 |
| 318.15 | 0.4825 | 0.2799 | 1014.6 |
| 318.15 | 0.6152 | 0.2081 | 1016.0 |
| 318.15 | 0.7132 | 0.1551 | 1014.7 |
| 318.15 | 0.7886 | 0.1143 | 1011.6 |
| 318.15 | 0.8484 | 0.0820 | 1007.9 |
| 318.15 | 0.8969 | 0.0557 | 1003.0 |
| 318.15 | 0.9372 | 0.0339 | 997.9 |
| 318.15 | 0.9711 | 0.0156 | 993.7 |
| 318.15 | 1.0000 | 0.0000 | 990.3 |
Speed of sound, m/s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Water (3) - Liquid | Mole fraction of 1,2-Ethanediol (1) - Liquid | Speed of sound, m/s - Liquid |
| 0.0000 | 0.5408 | 1584.4 |
| 0.2929 | 0.3824 | 1650.9 |
| 0.4825 | 0.2799 | 1688.8 |
| 0.6152 | 0.2081 | 1713.8 |
| 0.7132 | 0.1551 | 1733.4 |
| 0.7886 | 0.1143 | 1752.5 |
| 0.8484 | 0.0820 | 1756.6 |
| 0.8969 | 0.0557 | 1705.3 |
| 0.9372 | 0.0339 | 1641.9 |
| 0.9711 | 0.0156 | 1576.5 |
| 1.0000 | 0.0000 | 1498.0 |
Speed of sound, m/s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Water (3) - Liquid | Mole fraction of 1,2-Ethanediol (1) - Liquid | Speed of sound, m/s - Liquid |
| 0.0000 | 0.5408 | 1584.4 |
| 0.2929 | 0.3824 | 1650.9 |
| 0.4825 | 0.2799 | 1688.8 |
| 0.6152 | 0.2081 | 1713.8 |
| 0.7132 | 0.1551 | 1733.4 |
| 0.7886 | 0.1143 | 1752.5 |
| 0.8484 | 0.0820 | 1756.6 |
| 0.8969 | 0.0557 | 1705.3 |
| 0.9372 | 0.0339 | 1641.9 |
| 0.9711 | 0.0156 | 1576.5 |
| 1.0000 | 0.0000 | 1498.0 |