- Name
- n-Hexane
- InChI
- InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
- InChI Key
- VLKZOEOYAKHREP-UHFFFAOYSA-N
- Formula
- C6H14
- SMILES
- CCCCCC
- Mol. Weight (g/mol)
- 86.18
- CAS
- 110-54-3
- 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
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Datasets
Activity coefficient of n-Hexane (1) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 313.20 | 97.8 |
| 332.10 | 88.1 |
| 353.50 | 80.6 |
Activity coefficient of n-Hexane (1) [ref]
Operational conditions:
- Mole fraction = 0 (Liquid)
- Pressure, kPa = 101.325 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 303.15 | 716.0 |
| 313.15 | 620.0 |
| 323.15 | 543.0 |
Activity coefficient of n-Hexane (1) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 313.20 | 97.8 |
| 332.10 | 88.1 |
| 353.50 | 80.6 |
Activity coefficient of n-Hexane (1) [ref]
Operational conditions:
- Mole fraction = 0 (Liquid)
- Pressure, kPa = 101.325 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 303.15 | 716.0 |
| 313.15 | 620.0 |
| 323.15 | 543.0 |
Mole fraction of n-Hexane (1) [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid mixture 1 | Pressure, kPa - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 1 |
| 298.20 | 101.00 | 0.0100 |
Mole fraction of 1,2-Ethanediol (2) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1 |
|---|---|
| 283.15 | 0.0000 |
| 303.15 | 0.0001 |
| 323.15 | 0.0004 |
Mole fraction of n-Hexane (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of n-Hexane (1) - Liquid mixture 2 |
|---|---|
| 283.15 | 0.0014 |
| 303.15 | 0.0018 |
| 323.15 | 0.0023 |
Mole fraction of n-Hexane (1) [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid mixture 1 | Pressure, kPa - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 1 |
| 298.20 | 101.00 | 0.0100 |
Mole fraction of 1,2-Ethanediol (2) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1 |
|---|---|
| 283.15 | 0.0000 |
| 303.15 | 0.0001 |
| 323.15 | 0.0004 |
Mole fraction of n-Hexane (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of n-Hexane (1) - Liquid mixture 2 |
|---|---|
| 283.15 | 0.0014 |
| 303.15 | 0.0018 |
| 323.15 | 0.0023 |
Sources
- Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
- Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
- Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
- Liquid-Liquid Equilibria for Monoethylene Glycol + Hexane and 2,2,4-Trimethylpentane, Water + Hexane and 2,2,4-Trimethylpentane, Monoethylene Glycol + Water + Hexane, and Monoethylene Glycol + Water + 2,2,4-Trimethylpentane in the Temperature Range between T = 283.15 K and T = 323.15 K