- 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
- 1-Hexanol
- InChI
- InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
- InChI Key
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N
- Formula
- C6H14O
- SMILES
- CCCCCCO
- Mol. Weight (g/mol)
- 102.17
- CAS
- 111-27-3
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Datasets
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0828 | 829.72 |
| 293.15 | 0.1585 | 840.78 |
| 293.15 | 0.2374 | 853.56 |
| 293.15 | 0.3265 | 869.87 |
| 293.15 | 0.4905 | 905.8 |
| 293.15 | 0.5445 | 919.79 |
| 293.15 | 0.5965 | 934.39 |
| 293.15 | 0.6932 | 965.41 |
| 293.15 | 0.7757 | 996.6 |
| 293.15 | 0.9053 | 1057.08 |
| 298.15 | 0.0828 | 826.21 |
| 298.15 | 0.1585 | 837.17 |
| 298.15 | 0.2374 | 849.99 |
| 298.15 | 0.3265 | 866.29 |
| 298.15 | 0.4905 | 902.2 |
| 298.15 | 0.5445 | 916.19 |
| 298.15 | 0.5965 | 930.83 |
| 298.15 | 0.6932 | 961.84 |
| 298.15 | 0.7757 | 993.11 |
| 298.15 | 0.9053 | 1053.67 |
| 303.15 | 0.0828 | 822.63 |
| 303.15 | 0.1585 | 833.58 |
| 303.15 | 0.2374 | 846.39 |
| 303.15 | 0.3265 | 862.69 |
| 303.15 | 0.4905 | 898.58 |
| 303.15 | 0.5445 | 912.56 |
| 303.15 | 0.5965 | 927.24 |
| 303.15 | 0.6932 | 958.23 |
| 303.15 | 0.7757 | 989.49 |
| 303.15 | 0.9053 | 1050.1 |
| 308.15 | 0.0828 | 819.02 |
| 308.15 | 0.1585 | 829.96 |
| 308.15 | 0.2374 | 842.67 |
| 308.15 | 0.3265 | 859.01 |
| 308.15 | 0.4905 | 894.88 |
| 308.15 | 0.5445 | 908.9 |
| 308.15 | 0.5965 | 923.53 |
| 308.15 | 0.6932 | 954.54 |
| 308.15 | 0.7757 | 985.79 |
| 308.15 | 0.9053 | 1046.52 |
| 313.15 | 0.0828 | 815.44 |
| 313.15 | 0.1585 | 826.33 |
| 313.15 | 0.2374 | 839.04 |
| 313.15 | 0.3265 | 855.36 |
| 313.15 | 0.4905 | 891.27 |
| 313.15 | 0.5445 | 905.23 |
| 313.15 | 0.5965 | 919.95 |
| 313.15 | 0.6932 | 950.95 |
| 313.15 | 0.7757 | 982.18 |
| 313.15 | 0.9053 | 1042.98 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0828 | 829.72 |
| 293.15 | 0.1585 | 840.78 |
| 293.15 | 0.2374 | 853.56 |
| 293.15 | 0.3265 | 869.87 |
| 293.15 | 0.4905 | 905.8 |
| 293.15 | 0.5445 | 919.79 |
| 293.15 | 0.5965 | 934.39 |
| 293.15 | 0.6932 | 965.41 |
| 293.15 | 0.7757 | 996.6 |
| 293.15 | 0.9053 | 1057.08 |
| 298.15 | 0.0828 | 826.21 |
| 298.15 | 0.1585 | 837.17 |
| 298.15 | 0.2374 | 849.99 |
| 298.15 | 0.3265 | 866.29 |
| 298.15 | 0.4905 | 902.2 |
| 298.15 | 0.5445 | 916.19 |
| 298.15 | 0.5965 | 930.83 |
| 298.15 | 0.6932 | 961.84 |
| 298.15 | 0.7757 | 993.11 |
| 298.15 | 0.9053 | 1053.67 |
| 303.15 | 0.0828 | 822.63 |
| 303.15 | 0.1585 | 833.58 |
| 303.15 | 0.2374 | 846.39 |
| 303.15 | 0.3265 | 862.69 |
| 303.15 | 0.4905 | 898.58 |
| 303.15 | 0.5445 | 912.56 |
| 303.15 | 0.5965 | 927.24 |
| 303.15 | 0.6932 | 958.23 |
| 303.15 | 0.7757 | 989.49 |
| 303.15 | 0.9053 | 1050.1 |
| 308.15 | 0.0828 | 819.02 |
| 308.15 | 0.1585 | 829.96 |
| 308.15 | 0.2374 | 842.67 |
| 308.15 | 0.3265 | 859.01 |
| 308.15 | 0.4905 | 894.88 |
| 308.15 | 0.5445 | 908.9 |
| 308.15 | 0.5965 | 923.53 |
| 308.15 | 0.6932 | 954.54 |
| 308.15 | 0.7757 | 985.79 |
| 308.15 | 0.9053 | 1046.52 |
| 313.15 | 0.0828 | 815.44 |
| 313.15 | 0.1585 | 826.33 |
| 313.15 | 0.2374 | 839.04 |
| 313.15 | 0.3265 | 855.36 |
| 313.15 | 0.4905 | 891.27 |
| 313.15 | 0.5445 | 905.23 |
| 313.15 | 0.5965 | 919.95 |
| 313.15 | 0.6932 | 950.95 |
| 313.15 | 0.7757 | 982.18 |
| 313.15 | 0.9053 | 1042.98 |
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 |
| 298.15 | 0.0000 | 0.0478 |
| 298.15 | 0.0429 | 0.0325 |
| 298.15 | 0.1009 | 0.0291 |
| 298.15 | 0.2761 | 0.0280 |
| 298.15 | 0.3098 | 0.0279 |
| 298.15 | 0.3500 | 0.0274 |
| 298.15 | 0.3942 | 0.0273 |
| 298.15 | 0.4468 | 0.0272 |
| 298.15 | 0.5079 | 0.0270 |
| 298.15 | 0.5405 | 0.0268 |
| 298.15 | 0.6061 | 0.0267 |
| 298.15 | 0.6452 | 0.0266 |
| 298.15 | 0.6897 | 0.0265 |
| 298.15 | 0.7407 | 0.0264 |
| 298.15 | 0.8000 | 0.0263 |
| 298.15 | 0.8333 | 0.0263 |
| 298.15 | 0.9091 | 0.0262 |
| 298.15 | 0.9524 | 0.0262 |
| 303.15 | 0.0000 | 0.0476 |
| 303.15 | 0.0429 | 0.0328 |
| 303.15 | 0.1009 | 0.0295 |
| 303.15 | 0.2761 | 0.0275 |
| 303.15 | 0.3098 | 0.0273 |
| 303.15 | 0.3500 | 0.0271 |
| 303.15 | 0.3942 | 0.0270 |
| 303.15 | 0.4468 | 0.0268 |
| 303.15 | 0.5079 | 0.0265 |
| 303.15 | 0.5405 | 0.0264 |
| 303.15 | 0.6061 | 0.0262 |
| 303.15 | 0.6452 | 0.0260 |
| 303.15 | 0.6897 | 0.0257 |
| 303.15 | 0.7407 | 0.0255 |
| 303.15 | 0.8000 | 0.0254 |
| 303.15 | 0.8333 | 0.0253 |
| 303.15 | 0.9091 | 0.0252 |
| 303.15 | 0.9524 | 0.0250 |
| 308.15 | 0.0000 | 0.0473 |
| 308.15 | 0.0429 | 0.0327 |
| 308.15 | 0.1009 | 0.0293 |
| 308.15 | 0.2761 | 0.0273 |
| 308.15 | 0.3098 | 0.0272 |
| 308.15 | 0.3500 | 0.0270 |
| 308.15 | 0.3942 | 0.0268 |
| 308.15 | 0.4468 | 0.0266 |
| 308.15 | 0.5079 | 0.0263 |
| 308.15 | 0.5405 | 0.0262 |
| 308.15 | 0.6061 | 0.0260 |
| 308.15 | 0.6452 | 0.0258 |
| 308.15 | 0.6897 | 0.0256 |
| 308.15 | 0.7407 | 0.0253 |
| 308.15 | 0.8000 | 0.0252 |
| 308.15 | 0.8333 | 0.0252 |
| 308.15 | 0.9091 | 0.0250 |
| 308.15 | 0.9524 | 0.0248 |
| 313.15 | 0.0000 | 0.0471 |
| 313.15 | 0.0429 | 0.0316 |
| 313.15 | 0.1009 | 0.0293 |
| 313.15 | 0.2761 | 0.0272 |
| 313.15 | 0.3098 | 0.0270 |
| 313.15 | 0.3500 | 0.0268 |
| 313.15 | 0.3942 | 0.0267 |
| 313.15 | 0.4468 | 0.0265 |
| 313.15 | 0.5079 | 0.0262 |
| 313.15 | 0.5405 | 0.0261 |
| 313.15 | 0.6061 | 0.0259 |
| 313.15 | 0.6452 | 0.0256 |
| 313.15 | 0.6897 | 0.0254 |
| 313.15 | 0.7407 | 0.0252 |
| 313.15 | 0.8000 | 0.0250 |
| 313.15 | 0.8333 | 0.0250 |
| 313.15 | 0.9091 | 0.0248 |
| 313.15 | 0.9524 | 0.0246 |
| 318.15 | 0.0000 | 0.0464 |
| 318.15 | 0.0429 | 0.0314 |
| 318.15 | 0.1009 | 0.0290 |
| 318.15 | 0.2761 | 0.0269 |
| 318.15 | 0.3098 | 0.0268 |
| 318.15 | 0.3500 | 0.0266 |
| 318.15 | 0.3942 | 0.0265 |
| 318.15 | 0.4468 | 0.0263 |
| 318.15 | 0.5079 | 0.0260 |
| 318.15 | 0.5405 | 0.0259 |
| 318.15 | 0.6061 | 0.0257 |
| 318.15 | 0.6452 | 0.0255 |
| 318.15 | 0.6897 | 0.0252 |
| 318.15 | 0.7407 | 0.0250 |
| 318.15 | 0.8000 | 0.0248 |
| 318.15 | 0.8333 | 0.0248 |
| 318.15 | 0.9091 | 0.0246 |
| 318.15 | 0.9524 | 0.0244 |
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 |
| 298.15 | 0.0000 | 0.0478 |
| 298.15 | 0.0429 | 0.0325 |
| 298.15 | 0.1009 | 0.0291 |
| 298.15 | 0.2761 | 0.0280 |
| 298.15 | 0.3098 | 0.0279 |
| 298.15 | 0.3500 | 0.0274 |
| 298.15 | 0.3942 | 0.0273 |
| 298.15 | 0.4468 | 0.0272 |
| 298.15 | 0.5079 | 0.0270 |
| 298.15 | 0.5405 | 0.0268 |
| 298.15 | 0.6061 | 0.0267 |
| 298.15 | 0.6452 | 0.0266 |
| 298.15 | 0.6897 | 0.0265 |
| 298.15 | 0.7407 | 0.0264 |
| 298.15 | 0.8000 | 0.0263 |
| 298.15 | 0.8333 | 0.0263 |
| 298.15 | 0.9091 | 0.0262 |
| 298.15 | 0.9524 | 0.0262 |
| 303.15 | 0.0000 | 0.0476 |
| 303.15 | 0.0429 | 0.0328 |
| 303.15 | 0.1009 | 0.0295 |
| 303.15 | 0.2761 | 0.0275 |
| 303.15 | 0.3098 | 0.0273 |
| 303.15 | 0.3500 | 0.0271 |
| 303.15 | 0.3942 | 0.0270 |
| 303.15 | 0.4468 | 0.0268 |
| 303.15 | 0.5079 | 0.0265 |
| 303.15 | 0.5405 | 0.0264 |
| 303.15 | 0.6061 | 0.0262 |
| 303.15 | 0.6452 | 0.0260 |
| 303.15 | 0.6897 | 0.0257 |
| 303.15 | 0.7407 | 0.0255 |
| 303.15 | 0.8000 | 0.0254 |
| 303.15 | 0.8333 | 0.0253 |
| 303.15 | 0.9091 | 0.0252 |
| 303.15 | 0.9524 | 0.0250 |
| 308.15 | 0.0000 | 0.0473 |
| 308.15 | 0.0429 | 0.0327 |
| 308.15 | 0.1009 | 0.0293 |
| 308.15 | 0.2761 | 0.0273 |
| 308.15 | 0.3098 | 0.0272 |
| 308.15 | 0.3500 | 0.0270 |
| 308.15 | 0.3942 | 0.0268 |
| 308.15 | 0.4468 | 0.0266 |
| 308.15 | 0.5079 | 0.0263 |
| 308.15 | 0.5405 | 0.0262 |
| 308.15 | 0.6061 | 0.0260 |
| 308.15 | 0.6452 | 0.0258 |
| 308.15 | 0.6897 | 0.0256 |
| 308.15 | 0.7407 | 0.0253 |
| 308.15 | 0.8000 | 0.0252 |
| 308.15 | 0.8333 | 0.0252 |
| 308.15 | 0.9091 | 0.0250 |
| 308.15 | 0.9524 | 0.0248 |
| 313.15 | 0.0000 | 0.0471 |
| 313.15 | 0.0429 | 0.0316 |
| 313.15 | 0.1009 | 0.0293 |
| 313.15 | 0.2761 | 0.0272 |
| 313.15 | 0.3098 | 0.0270 |
| 313.15 | 0.3500 | 0.0268 |
| 313.15 | 0.3942 | 0.0267 |
| 313.15 | 0.4468 | 0.0265 |
| 313.15 | 0.5079 | 0.0262 |
| 313.15 | 0.5405 | 0.0261 |
| 313.15 | 0.6061 | 0.0259 |
| 313.15 | 0.6452 | 0.0256 |
| 313.15 | 0.6897 | 0.0254 |
| 313.15 | 0.7407 | 0.0252 |
| 313.15 | 0.8000 | 0.0250 |
| 313.15 | 0.8333 | 0.0250 |
| 313.15 | 0.9091 | 0.0248 |
| 313.15 | 0.9524 | 0.0246 |
| 318.15 | 0.0000 | 0.0464 |
| 318.15 | 0.0429 | 0.0314 |
| 318.15 | 0.1009 | 0.0290 |
| 318.15 | 0.2761 | 0.0269 |
| 318.15 | 0.3098 | 0.0268 |
| 318.15 | 0.3500 | 0.0266 |
| 318.15 | 0.3942 | 0.0265 |
| 318.15 | 0.4468 | 0.0263 |
| 318.15 | 0.5079 | 0.0260 |
| 318.15 | 0.5405 | 0.0259 |
| 318.15 | 0.6061 | 0.0257 |
| 318.15 | 0.6452 | 0.0255 |
| 318.15 | 0.6897 | 0.0252 |
| 318.15 | 0.7407 | 0.0250 |
| 318.15 | 0.8000 | 0.0248 |
| 318.15 | 0.8333 | 0.0248 |
| 318.15 | 0.9091 | 0.0246 |
| 318.15 | 0.9524 | 0.0244 |
Sources
- Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
- Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)