Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 303.15 | 413.74 |
| 313.15 | 382.52 |
| 323.15 | 340.01 |
| 333.15 | 315.78 |
| 343.15 | 268.43 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
|---|---|
| 303.15 | 413.74 |
| 313.15 | 382.52 |
| 323.15 | 340.01 |
| 333.15 | 315.78 |
| 343.15 | 268.43 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 1 |
|---|---|
| 303.20 | 0.9960 |
| 313.20 | 0.9960 |
| 317.20 | 0.9950 |
| 322.20 | 0.9950 |
| 327.20 | 0.9950 |
| 331.20 | 0.9950 |
| 335.20 | 0.9940 |
| 338.20 | 0.9940 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 2 |
|---|---|
| 303.20 | 0.0120 |
| 313.20 | 0.0130 |
| 317.20 | 0.0140 |
| 322.20 | 0.0130 |
| 327.20 | 0.0140 |
| 331.20 | 0.0150 |
| 335.20 | 0.0160 |
| 338.20 | 0.0160 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 1 |
|---|---|
| 303.20 | 0.9960 |
| 313.20 | 0.9960 |
| 317.20 | 0.9950 |
| 322.20 | 0.9950 |
| 327.20 | 0.9950 |
| 331.20 | 0.9950 |
| 335.20 | 0.9940 |
| 338.20 | 0.9940 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 2 |
|---|---|
| 303.20 | 0.0120 |
| 313.20 | 0.0130 |
| 317.20 | 0.0140 |
| 322.20 | 0.0130 |
| 327.20 | 0.0140 |
| 331.20 | 0.0150 |
| 335.20 | 0.0160 |
| 338.20 | 0.0160 |