Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Heptane (2) - Liquid |
|---|---|
| 303.15 | 580.21 |
| 313.15 | 527.48 |
| 323.15 | 450.11 |
| 333.15 | 385.89 |
| 343.15 | 304.34 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Heptane (2) - Liquid |
|---|---|
| 303.15 | 580.21 |
| 313.15 | 527.48 |
| 323.15 | 450.11 |
| 333.15 | 385.89 |
| 343.15 | 304.34 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 |
|---|---|
| 308.20 | 0.9960 |
| 313.20 | 0.9970 |
| 323.20 | 0.9970 |
| 328.20 | 0.9960 |
| 333.20 | 0.9960 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 2 |
|---|---|
| 308.20 | 0.0100 |
| 313.20 | 0.0100 |
| 323.20 | 0.0100 |
| 328.20 | 0.0110 |
| 333.20 | 0.0110 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 |
|---|---|
| 308.20 | 0.9960 |
| 313.20 | 0.9970 |
| 323.20 | 0.9970 |
| 328.20 | 0.9960 |
| 333.20 | 0.9960 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 2 |
|---|---|
| 308.20 | 0.0100 |
| 313.20 | 0.0100 |
| 323.20 | 0.0100 |
| 328.20 | 0.0110 |
| 333.20 | 0.0110 |