Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
|---|---|
| 298.20 | 0.9996 |
| 303.20 | 0.9996 |
| 308.20 | 0.9996 |
| 313.20 | 0.9996 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 298.20 | 0.1081 |
| 303.20 | 0.1081 |
| 308.20 | 0.1081 |
| 313.20 | 0.1081 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
|---|---|
| 298.15 | 0.9999 |
| 303.15 | 0.9860 |
| 308.15 | 0.9948 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 298.15 | 0.0245 |
| 303.15 | 0.0204 |
| 308.15 | 0.0303 |
Operational conditions:
| Mass fraction of Water (2) - Liquid mixture 1 |
|---|
| 0.0121 |
| 0.9987 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 1 |
|---|---|
| 293.15 | 0.1204 |
| 313.15 | 0.1651 |
| 303.15 | 0.1376 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 293.15 | 0.9988 |
| 313.15 | 0.9990 |
| 303.15 | 0.9988 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of 1-Hexanol, 2-ethyl- (1) - Liquid |
|---|---|
| 273.25 | 0.0797 |
| 298.15 | 1.905 |
| 311.15 | 4.0942 |
| 332.15 | 100.18 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
|---|---|
| 298.20 | 0.9996 |
| 303.20 | 0.9996 |
| 308.20 | 0.9996 |
| 313.20 | 0.9996 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 298.20 | 0.1081 |
| 303.20 | 0.1081 |
| 308.20 | 0.1081 |
| 313.20 | 0.1081 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
|---|---|
| 298.15 | 0.9999 |
| 303.15 | 0.9860 |
| 308.15 | 0.9948 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 298.15 | 0.0245 |
| 303.15 | 0.0204 |
| 308.15 | 0.0303 |
Operational conditions:
| Mass fraction of Water (2) - Liquid mixture 1 |
|---|
| 0.0121 |
| 0.9987 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 1 |
|---|---|
| 293.15 | 0.1204 |
| 313.15 | 0.1651 |
| 303.15 | 0.1376 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 293.15 | 0.9988 |
| 313.15 | 0.9990 |
| 303.15 | 0.9988 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of 1-Hexanol, 2-ethyl- (1) - Liquid |
|---|---|
| 273.25 | 0.0797 |
| 298.15 | 1.905 |
| 311.15 | 4.0942 |
| 332.15 | 100.18 |