Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Diisopropyl ether (1) - Liquid | Mole fraction of Diisopropyl ether (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0020 | 0.1020 |
| 0.0040 | 0.1350 |
| 0.0090 | 0.2560 |
| 0.0220 | 0.4260 |
| 0.0610 | 0.6950 |
| 0.1020 | 0.7980 |
| 0.1580 | 0.8790 |
| 0.1950 | 0.9060 |
| 0.2250 | 0.9130 |
| 0.2880 | 0.9350 |
| 0.3420 | 0.9390 |
| 0.3930 | 0.9400 |
| 0.4460 | 0.9450 |
| 0.5020 | 0.9520 |
| 0.5690 | 0.9610 |
| 0.6220 | 0.9660 |
| 0.6860 | 0.9710 |
| 0.7340 | 0.9720 |
| 0.8320 | 0.9830 |
| 0.9160 | 0.9910 |
| 0.9490 | 0.9940 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Diisopropyl ether (1) - Liquid | Mole fraction of Diisopropyl ether (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0020 | 0.1020 |
| 0.0040 | 0.1350 |
| 0.0090 | 0.2560 |
| 0.0220 | 0.4260 |
| 0.0610 | 0.6950 |
| 0.1020 | 0.7980 |
| 0.1580 | 0.8790 |
| 0.1950 | 0.9060 |
| 0.2250 | 0.9130 |
| 0.2880 | 0.9350 |
| 0.3420 | 0.9390 |
| 0.3930 | 0.9400 |
| 0.4460 | 0.9450 |
| 0.5020 | 0.9520 |
| 0.5690 | 0.9610 |
| 0.6220 | 0.9660 |
| 0.6860 | 0.9710 |
| 0.7340 | 0.9720 |
| 0.8320 | 0.9830 |
| 0.9160 | 0.9910 |
| 0.9490 | 0.9940 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Diisopropyl ether (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 440.31 |
| 0.0020 | 437.04 |
| 0.0040 | 435.32 |
| 0.0090 | 429.41 |
| 0.0220 | 421.68 |
| 0.0610 | 401.27 |
| 0.1020 | 388.26 |
| 0.1580 | 375.56 |
| 0.1950 | 368.99 |
| 0.2250 | 364.66 |
| 0.2880 | 355.89 |
| 0.3420 | 351.54 |
| 0.3930 | 348.94 |
| 0.4460 | 346.82 |
| 0.5020 | 345.69 |
| 0.5690 | 344.57 |
| 0.6220 | 343.99 |
| 0.6860 | 343.61 |
| 0.7340 | 343.13 |
| 0.8320 | 342.43 |
| 0.9160 | 342.34 |
| 0.9490 | 342.08 |
| 1.0000 | 341.51 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Diisopropyl ether (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 440.31 |
| 0.0020 | 437.04 |
| 0.0040 | 435.32 |
| 0.0090 | 429.41 |
| 0.0220 | 421.68 |
| 0.0610 | 401.27 |
| 0.1020 | 388.26 |
| 0.1580 | 375.56 |
| 0.1950 | 368.99 |
| 0.2250 | 364.66 |
| 0.2880 | 355.89 |
| 0.3420 | 351.54 |
| 0.3930 | 348.94 |
| 0.4460 | 346.82 |
| 0.5020 | 345.69 |
| 0.5690 | 344.57 |
| 0.6220 | 343.99 |
| 0.6860 | 343.61 |
| 0.7340 | 343.13 |
| 0.8320 | 342.43 |
| 0.9160 | 342.34 |
| 0.9490 | 342.08 |
| 1.0000 | 341.51 |