- 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
- Furfural
- InChI
- InChI=1S/C5H4O2/c6-4-5-2-1-3-7-5/h1-4H
- InChI Key
- HYBBIBNJHNGZAN-UHFFFAOYSA-N
- Formula
- C5H4O2
- SMILES
- O=Cc1ccco1
- Mol. Weight (g/mol)
- 96.08
- CAS
- 98-01-1
Datasets
Activity coefficient of n-Hexane (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 278.15 | 31.9 |
| 298.15 | 27.8 |
Activity coefficient of n-Hexane (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 298.15 | 25.6 |
| 298.15 | 25.3 |
| 308.15 | 23.6 |
| 308.15 | 22.8 |
| 318.15 | 22.2 |
| 318.15 | 21.2 |
Activity coefficient of n-Hexane (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 278.15 | 31.9 |
| 298.15 | 27.8 |
Activity coefficient of n-Hexane (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 298.15 | 25.6 |
| 298.15 | 25.3 |
| 308.15 | 23.6 |
| 308.15 | 22.8 |
| 318.15 | 22.2 |
| 318.15 | 21.2 |
Mole fraction of Furfural (2) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Furfural (2) - Liquid mixture 1 |
|---|---|
| 295.10 | 0.0430 |
| 298.50 | 0.0540 |
| 303.16 | 0.0640 |
| 313.44 | 0.0850 |
| 318.20 | 0.0930 |
| 328.20 | 0.1170 |
| 338.20 | 0.1500 |
Mole fraction of Furfural (2) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Furfural (2) - Liquid mixture 2 |
|---|---|
| 295.10 | 0.9310 |
| 298.50 | 0.9300 |
| 303.16 | 0.9200 |
| 313.44 | 0.9050 |
| 318.20 | 0.9000 |
| 328.20 | 0.8720 |
| 338.20 | 0.8410 |
Mole fraction of Furfural (2) [ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid mixture 1)
- Temperature, K = 298.15 (Liquid mixture 1)
| Mole fraction of Furfural (2) - Liquid mixture 1 |
|---|
| 0.0460 |
| 0.9330 |
Mole fraction of Furfural (2) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Furfural (2) - Liquid mixture 1 |
|---|---|
| 295.10 | 0.0430 |
| 298.50 | 0.0540 |
| 303.16 | 0.0640 |
| 313.44 | 0.0850 |
| 318.20 | 0.0930 |
| 328.20 | 0.1170 |
| 338.20 | 0.1500 |
Mole fraction of Furfural (2) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Furfural (2) - Liquid mixture 2 |
|---|---|
| 295.10 | 0.9310 |
| 298.50 | 0.9300 |
| 303.16 | 0.9200 |
| 313.44 | 0.9050 |
| 318.20 | 0.9000 |
| 328.20 | 0.8720 |
| 338.20 | 0.8410 |
Mole fraction of Furfural (2) [ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid mixture 1)
- Temperature, K = 298.15 (Liquid mixture 1)
| Mole fraction of Furfural (2) - Liquid mixture 1 |
|---|
| 0.0460 |
| 0.9330 |
Sources
- Equilibrium data and GC-PC SAFT predictions for furanic extraction
- The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
- Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) K
- Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K