Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Butanol, 2-methyl-, acetate (1) - Liquid | Mole fraction of 1-Butanol, 2-methyl-, acetate (1) - Gas |
|---|---|
| 0.0664 | 0.0989 |
| 0.1654 | 0.2336 |
| 0.2418 | 0.3283 |
| 0.2937 | 0.3885 |
| 0.3462 | 0.4464 |
| 0.4140 | 0.5173 |
| 0.4808 | 0.5828 |
| 0.5485 | 0.6453 |
| 0.6035 | 0.6941 |
| 0.6696 | 0.7501 |
| 0.7481 | 0.8135 |
| 0.8119 | 0.8631 |
| 0.8694 | 0.9062 |
| 0.9281 | 0.9491 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Butanol, 2-methyl-, acetate (1) - Liquid | Mole fraction of 1-Butanol, 2-methyl-, acetate (1) - Gas |
|---|---|
| 0.0664 | 0.0989 |
| 0.1654 | 0.2336 |
| 0.2418 | 0.3283 |
| 0.2937 | 0.3885 |
| 0.3462 | 0.4464 |
| 0.4140 | 0.5173 |
| 0.4808 | 0.5828 |
| 0.5485 | 0.6453 |
| 0.6035 | 0.6941 |
| 0.6696 | 0.7501 |
| 0.7481 | 0.8135 |
| 0.8119 | 0.8631 |
| 0.8694 | 0.9062 |
| 0.9281 | 0.9491 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Butanol, 2-methyl-, acetate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0664 | 423.46 |
| 0.1654 | 421.87 |
| 0.2418 | 420.60 |
| 0.2937 | 419.78 |
| 0.3462 | 419.15 |
| 0.4140 | 418.17 |
| 0.4808 | 417.40 |
| 0.5485 | 416.75 |
| 0.6035 | 415.91 |
| 0.6696 | 415.15 |
| 0.7481 | 414.37 |
| 0.8119 | 413.75 |
| 0.8694 | 413.15 |
| 0.9281 | 412.49 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Butanol, 2-methyl-, acetate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0664 | 423.46 |
| 0.1654 | 421.87 |
| 0.2418 | 420.60 |
| 0.2937 | 419.78 |
| 0.3462 | 419.15 |
| 0.4140 | 418.17 |
| 0.4808 | 417.40 |
| 0.5485 | 416.75 |
| 0.6035 | 415.91 |
| 0.6696 | 415.15 |
| 0.7481 | 414.37 |
| 0.8119 | 413.75 |
| 0.8694 | 413.15 |
| 0.9281 | 412.49 |