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 |
| 0.0290 | 0.2060 |
| 0.0660 | 0.3790 |
| 0.1000 | 0.4900 |
| 0.1400 | 0.5750 |
| 0.1800 | 0.6330 |
| 0.2280 | 0.6790 |
| 0.2680 | 0.7110 |
| 0.3110 | 0.7440 |
| 0.3610 | 0.7820 |
| 0.4130 | 0.8060 |
| 0.4630 | 0.8230 |
| 0.5200 | 0.8380 |
| 0.5760 | 0.8510 |
| 0.6350 | 0.8660 |
| 0.6900 | 0.8800 |
| 0.7650 | 0.8950 |
| 0.8230 | 0.9120 |
| 0.8770 | 0.9310 |
| 0.9370 | 0.9590 |
| 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 |
| 0.0290 | 0.2060 |
| 0.0660 | 0.3790 |
| 0.1000 | 0.4900 |
| 0.1400 | 0.5750 |
| 0.1800 | 0.6330 |
| 0.2280 | 0.6790 |
| 0.2680 | 0.7110 |
| 0.3110 | 0.7440 |
| 0.3610 | 0.7820 |
| 0.4130 | 0.8060 |
| 0.4630 | 0.8230 |
| 0.5200 | 0.8380 |
| 0.5760 | 0.8510 |
| 0.6350 | 0.8660 |
| 0.6900 | 0.8800 |
| 0.7650 | 0.8950 |
| 0.8230 | 0.9120 |
| 0.8770 | 0.9310 |
| 0.9370 | 0.9590 |
| 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 | 407.95 |
| 0.0290 | 400.36 |
| 0.0660 | 393.98 |
| 0.1000 | 389.46 |
| 0.1400 | 385.26 |
| 0.1800 | 382.04 |
| 0.2280 | 379.28 |
| 0.2680 | 377.06 |
| 0.3110 | 375.07 |
| 0.3610 | 373.34 |
| 0.4130 | 371.78 |
| 0.4630 | 370.77 |
| 0.5200 | 369.67 |
| 0.5760 | 368.51 |
| 0.6350 | 367.50 |
| 0.6900 | 366.68 |
| 0.7650 | 365.76 |
| 0.8230 | 365.00 |
| 0.8770 | 364.36 |
| 0.9370 | 363.63 |
| 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 | 407.95 |
| 0.0290 | 400.36 |
| 0.0660 | 393.98 |
| 0.1000 | 389.46 |
| 0.1400 | 385.26 |
| 0.1800 | 382.04 |
| 0.2280 | 379.28 |
| 0.2680 | 377.06 |
| 0.3110 | 375.07 |
| 0.3610 | 373.34 |
| 0.4130 | 371.78 |
| 0.4630 | 370.77 |
| 0.5200 | 369.67 |
| 0.5760 | 368.51 |
| 0.6350 | 367.50 |
| 0.6900 | 366.68 |
| 0.7650 | 365.76 |
| 0.8230 | 365.00 |
| 0.8770 | 364.36 |
| 0.9370 | 363.63 |
| 1.0000 | 363.16 |