Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Butane (1) - Liquid |
|---|---|
| 270.02 | 2.79 |
| 280.00 | 2.73 |
| 290.00 | 2.7 |
| 300.00 | 2.64 |
| 310.00 | 2.56 |
| 320.00 | 2.5 |
| 330.00 | 2.42 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Butane (1) - Liquid |
|---|---|
| 270.02 | 2.79 |
| 280.00 | 2.73 |
| 290.00 | 2.7 |
| 300.00 | 2.64 |
| 310.00 | 2.56 |
| 320.00 | 2.5 |
| 330.00 | 2.42 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Butane (1) - Liquid |
|---|---|
| 270.02 | 247.0 |
| 280.00 | 347.0 |
| 290.00 | 476.0 |
| 300.00 | 630.0 |
| 310.00 | 810.0 |
| 320.00 | 1020.0 |
| 330.00 | 1250.0 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Butane (1) - Liquid |
|---|---|
| 270.02 | 247.0 |
| 280.00 | 347.0 |
| 290.00 | 476.0 |
| 300.00 | 630.0 |
| 310.00 | 810.0 |
| 320.00 | 1020.0 |
| 330.00 | 1250.0 |