Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Butane (1) - Liquid |
|---|---|
| 259.98 | 3.48 |
| 270.02 | 3.4 |
| 280.00 | 3.36 |
| 290.00 | 3.26 |
| 300.00 | 3.15 |
| 310.01 | 3.04 |
| 320.00 | 2.92 |
| 330.01 | 2.79 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Butane (1) - Liquid |
|---|---|
| 259.98 | 3.48 |
| 270.02 | 3.4 |
| 280.00 | 3.36 |
| 290.00 | 3.26 |
| 300.00 | 3.15 |
| 310.01 | 3.04 |
| 320.00 | 2.92 |
| 330.01 | 2.79 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Butane (1) - Liquid |
|---|---|
| 259.98 | 207.0 |
| 270.02 | 301.0 |
| 280.00 | 426.0 |
| 290.00 | 580.0 |
| 300.00 | 750.0 |
| 310.01 | 960.0 |
| 320.00 | 1190.0 |
| 330.01 | 1440.0 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Butane (1) - Liquid |
|---|---|
| 259.98 | 207.0 |
| 270.02 | 301.0 |
| 280.00 | 426.0 |
| 290.00 | 580.0 |
| 300.00 | 750.0 |
| 310.01 | 960.0 |
| 320.00 | 1190.0 |
| 330.01 | 1440.0 |