Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Diisopropyl ether (1) - Gas | Mole fraction of Diisopropyl ether (1) - Liquid |
|---|---|
| 0.0000 | 0.0000 |
| 0.2230 | 0.0300 |
| 0.3110 | 0.0450 |
| 0.3980 | 0.0630 |
| 0.5030 | 0.0890 |
| 0.5820 | 0.1170 |
| 0.6410 | 0.1410 |
| 0.6650 | 0.1530 |
| 0.6990 | 0.1690 |
| 0.7650 | 0.2130 |
| 0.8040 | 0.2410 |
| 0.8470 | 0.2930 |
| 0.8760 | 0.3450 |
| 0.8940 | 0.3920 |
| 0.9150 | 0.4630 |
| 0.9300 | 0.5170 |
| 0.9400 | 0.5750 |
| 0.9520 | 0.6430 |
| 0.9600 | 0.7010 |
| 0.9680 | 0.7600 |
| 0.9760 | 0.8200 |
| 0.9830 | 0.8780 |
| 0.9910 | 0.9390 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Diisopropyl ether (1) - Gas | Mole fraction of Diisopropyl ether (1) - Liquid |
|---|---|
| 0.0000 | 0.0000 |
| 0.2230 | 0.0300 |
| 0.3110 | 0.0450 |
| 0.3980 | 0.0630 |
| 0.5030 | 0.0890 |
| 0.5820 | 0.1170 |
| 0.6410 | 0.1410 |
| 0.6650 | 0.1530 |
| 0.6990 | 0.1690 |
| 0.7650 | 0.2130 |
| 0.8040 | 0.2410 |
| 0.8470 | 0.2930 |
| 0.8760 | 0.3450 |
| 0.8940 | 0.3920 |
| 0.9150 | 0.4630 |
| 0.9300 | 0.5170 |
| 0.9400 | 0.5750 |
| 0.9520 | 0.6430 |
| 0.9600 | 0.7010 |
| 0.9680 | 0.7600 |
| 0.9760 | 0.8200 |
| 0.9830 | 0.8780 |
| 0.9910 | 0.9390 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Diisopropyl ether (1) - Gas | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 404.63 |
| 0.2230 | 398.06 |
| 0.3110 | 395.14 |
| 0.3980 | 391.80 |
| 0.5030 | 387.66 |
| 0.5820 | 383.84 |
| 0.6410 | 380.61 |
| 0.6650 | 379.19 |
| 0.6990 | 377.18 |
| 0.7650 | 372.36 |
| 0.8040 | 369.30 |
| 0.8470 | 365.15 |
| 0.8760 | 361.96 |
| 0.8940 | 359.49 |
| 0.9150 | 356.56 |
| 0.9300 | 354.30 |
| 0.9400 | 352.33 |
| 0.9520 | 350.56 |
| 0.9600 | 348.90 |
| 0.9680 | 347.37 |
| 0.9760 | 345.86 |
| 0.9830 | 344.44 |
| 0.9910 | 342.96 |
| 1.0000 | 341.49 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Diisopropyl ether (1) - Gas | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 404.63 |
| 0.2230 | 398.06 |
| 0.3110 | 395.14 |
| 0.3980 | 391.80 |
| 0.5030 | 387.66 |
| 0.5820 | 383.84 |
| 0.6410 | 380.61 |
| 0.6650 | 379.19 |
| 0.6990 | 377.18 |
| 0.7650 | 372.36 |
| 0.8040 | 369.30 |
| 0.8470 | 365.15 |
| 0.8760 | 361.96 |
| 0.8940 | 359.49 |
| 0.9150 | 356.56 |
| 0.9300 | 354.30 |
| 0.9400 | 352.33 |
| 0.9520 | 350.56 |
| 0.9600 | 348.90 |
| 0.9680 | 347.37 |
| 0.9760 | 345.86 |
| 0.9830 | 344.44 |
| 0.9910 | 342.96 |
| 1.0000 | 341.49 |