Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Di-n-propyl ether (1) - Liquid | Mole fraction of Di-n-propyl ether (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0330 | 0.1810 |
| 0.0480 | 0.2430 |
| 0.0730 | 0.3420 |
| 0.1160 | 0.4780 |
| 0.1460 | 0.5510 |
| 0.1880 | 0.6460 |
| 0.2240 | 0.6880 |
| 0.2650 | 0.7360 |
| 0.3200 | 0.7800 |
| 0.3670 | 0.8080 |
| 0.4210 | 0.8360 |
| 0.4700 | 0.8560 |
| 0.5350 | 0.8750 |
| 0.5930 | 0.8910 |
| 0.6490 | 0.9060 |
| 0.7080 | 0.9190 |
| 0.7650 | 0.9290 |
| 0.8290 | 0.9420 |
| 0.8850 | 0.9570 |
| 0.9460 | 0.9750 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Di-n-propyl ether (1) - Liquid | Mole fraction of Di-n-propyl ether (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0330 | 0.1810 |
| 0.0480 | 0.2430 |
| 0.0730 | 0.3420 |
| 0.1160 | 0.4780 |
| 0.1460 | 0.5510 |
| 0.1880 | 0.6460 |
| 0.2240 | 0.6880 |
| 0.2650 | 0.7360 |
| 0.3200 | 0.7800 |
| 0.3670 | 0.8080 |
| 0.4210 | 0.8360 |
| 0.4700 | 0.8560 |
| 0.5350 | 0.8750 |
| 0.5930 | 0.8910 |
| 0.6490 | 0.9060 |
| 0.7080 | 0.9190 |
| 0.7650 | 0.9290 |
| 0.8290 | 0.9420 |
| 0.8850 | 0.9570 |
| 0.9460 | 0.9750 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Di-n-propyl ether (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 410.62 |
| 0.0330 | 406.05 |
| 0.0480 | 404.00 |
| 0.0730 | 400.79 |
| 0.1160 | 396.65 |
| 0.1460 | 393.30 |
| 0.1880 | 389.38 |
| 0.2240 | 386.60 |
| 0.2650 | 383.96 |
| 0.3200 | 380.87 |
| 0.3670 | 378.67 |
| 0.4210 | 376.35 |
| 0.4700 | 374.79 |
| 0.5350 | 372.49 |
| 0.5930 | 370.96 |
| 0.6490 | 369.57 |
| 0.7080 | 368.38 |
| 0.7650 | 367.16 |
| 0.8290 | 365.94 |
| 0.8850 | 364.85 |
| 0.9460 | 363.56 |
| 1.0000 | 363.16 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Di-n-propyl ether (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 410.62 |
| 0.0330 | 406.05 |
| 0.0480 | 404.00 |
| 0.0730 | 400.79 |
| 0.1160 | 396.65 |
| 0.1460 | 393.30 |
| 0.1880 | 389.38 |
| 0.2240 | 386.60 |
| 0.2650 | 383.96 |
| 0.3200 | 380.87 |
| 0.3670 | 378.67 |
| 0.4210 | 376.35 |
| 0.4700 | 374.79 |
| 0.5350 | 372.49 |
| 0.5930 | 370.96 |
| 0.6490 | 369.57 |
| 0.7080 | 368.38 |
| 0.7650 | 367.16 |
| 0.8290 | 365.94 |
| 0.8850 | 364.85 |
| 0.9460 | 363.56 |
| 1.0000 | 363.16 |