Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Di-n-propyl ether (2) - Liquid | Mole fraction of Di-n-propyl ether (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0320 | 0.1320 |
| 0.0670 | 0.2520 |
| 0.1040 | 0.3620 |
| 0.1440 | 0.4600 |
| 0.1890 | 0.5450 |
| 0.2290 | 0.6100 |
| 0.2700 | 0.6660 |
| 0.3130 | 0.7150 |
| 0.3720 | 0.7660 |
| 0.4190 | 0.8050 |
| 0.4700 | 0.8370 |
| 0.5240 | 0.8650 |
| 0.5770 | 0.8890 |
| 0.6350 | 0.9090 |
| 0.6950 | 0.9300 |
| 0.7520 | 0.9460 |
| 0.8080 | 0.9610 |
| 0.8710 | 0.9760 |
| 0.9350 | 0.9880 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Di-n-propyl ether (2) - Liquid | Mole fraction of Di-n-propyl ether (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0320 | 0.1320 |
| 0.0670 | 0.2520 |
| 0.1040 | 0.3620 |
| 0.1440 | 0.4600 |
| 0.1890 | 0.5450 |
| 0.2290 | 0.6100 |
| 0.2700 | 0.6660 |
| 0.3130 | 0.7150 |
| 0.3720 | 0.7660 |
| 0.4190 | 0.8050 |
| 0.4700 | 0.8370 |
| 0.5240 | 0.8650 |
| 0.5770 | 0.8890 |
| 0.6350 | 0.9090 |
| 0.6950 | 0.9300 |
| 0.7520 | 0.9460 |
| 0.8080 | 0.9610 |
| 0.8710 | 0.9760 |
| 0.9350 | 0.9880 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Di-n-propyl ether (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 418.69 |
| 0.0320 | 414.60 |
| 0.0670 | 411.00 |
| 0.1040 | 407.34 |
| 0.1440 | 403.83 |
| 0.1890 | 400.63 |
| 0.2290 | 397.01 |
| 0.2700 | 394.02 |
| 0.3130 | 391.00 |
| 0.3720 | 387.75 |
| 0.4190 | 384.91 |
| 0.4700 | 382.40 |
| 0.5240 | 379.61 |
| 0.5770 | 377.39 |
| 0.6350 | 375.10 |
| 0.6950 | 372.70 |
| 0.7520 | 370.75 |
| 0.8080 | 368.77 |
| 0.8710 | 366.83 |
| 0.9350 | 365.00 |
| 1.0000 | 363.16 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Di-n-propyl ether (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 418.69 |
| 0.0320 | 414.60 |
| 0.0670 | 411.00 |
| 0.1040 | 407.34 |
| 0.1440 | 403.83 |
| 0.1890 | 400.63 |
| 0.2290 | 397.01 |
| 0.2700 | 394.02 |
| 0.3130 | 391.00 |
| 0.3720 | 387.75 |
| 0.4190 | 384.91 |
| 0.4700 | 382.40 |
| 0.5240 | 379.61 |
| 0.5770 | 377.39 |
| 0.6350 | 375.10 |
| 0.6950 | 372.70 |
| 0.7520 | 370.75 |
| 0.8080 | 368.77 |
| 0.8710 | 366.83 |
| 0.9350 | 365.00 |
| 1.0000 | 363.16 |