Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Methyl formate (1) - Liquid | Mole fraction of Methyl formate (1) - Gas |
|---|---|
| 0.0101 | 0.1907 |
| 0.0197 | 0.3458 |
| 0.0311 | 0.4651 |
| 0.0500 | 0.6208 |
| 0.0698 | 0.7104 |
| 0.0895 | 0.7874 |
| 0.1190 | 0.8400 |
| 0.1778 | 0.9019 |
| 0.2967 | 0.9638 |
| 0.3705 | 0.9718 |
| 0.4425 | 0.9762 |
| 0.5336 | 0.9844 |
| 0.5753 | 0.9864 |
| 0.6758 | 0.9868 |
| 0.7657 | 0.9895 |
| 0.8492 | 0.9902 |
| 0.8814 | 0.9924 |
| 0.9072 | 0.9944 |
| 0.9397 | 0.9958 |
| 0.9665 | 0.9975 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Methyl formate (1) - Liquid | Mole fraction of Methyl formate (1) - Gas |
|---|---|
| 0.0101 | 0.1907 |
| 0.0197 | 0.3458 |
| 0.0311 | 0.4651 |
| 0.0500 | 0.6208 |
| 0.0698 | 0.7104 |
| 0.0895 | 0.7874 |
| 0.1190 | 0.8400 |
| 0.1778 | 0.9019 |
| 0.2967 | 0.9638 |
| 0.3705 | 0.9718 |
| 0.4425 | 0.9762 |
| 0.5336 | 0.9844 |
| 0.5753 | 0.9864 |
| 0.6758 | 0.9868 |
| 0.7657 | 0.9895 |
| 0.8492 | 0.9902 |
| 0.8814 | 0.9924 |
| 0.9072 | 0.9944 |
| 0.9397 | 0.9958 |
| 0.9665 | 0.9975 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Methyl formate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0101 | 401.32 |
| 0.0197 | 395.33 |
| 0.0311 | 387.52 |
| 0.0500 | 379.06 |
| 0.0698 | 370.68 |
| 0.0895 | 364.08 |
| 0.1190 | 355.69 |
| 0.1778 | 343.44 |
| 0.2967 | 328.37 |
| 0.3705 | 321.71 |
| 0.4425 | 318.41 |
| 0.5336 | 314.47 |
| 0.5753 | 312.33 |
| 0.6758 | 309.43 |
| 0.7657 | 307.66 |
| 0.8492 | 307.02 |
| 0.8814 | 306.61 |
| 0.9072 | 306.41 |
| 0.9397 | 306.27 |
| 0.9665 | 305.70 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Methyl formate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0101 | 401.32 |
| 0.0197 | 395.33 |
| 0.0311 | 387.52 |
| 0.0500 | 379.06 |
| 0.0698 | 370.68 |
| 0.0895 | 364.08 |
| 0.1190 | 355.69 |
| 0.1778 | 343.44 |
| 0.2967 | 328.37 |
| 0.3705 | 321.71 |
| 0.4425 | 318.41 |
| 0.5336 | 314.47 |
| 0.5753 | 312.33 |
| 0.6758 | 309.43 |
| 0.7657 | 307.66 |
| 0.8492 | 307.02 |
| 0.8814 | 306.61 |
| 0.9072 | 306.41 |
| 0.9397 | 306.27 |
| 0.9665 | 305.70 |