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 |