Operational condition: Pressure, kPa = 97.3 (Liquid)
Mole fraction of Tetrahydropyran (2) - Gas | Mole fraction of Tetrahydropyran (2) - Liquid |
---|---|
0.0924 | 0.0227 |
0.2245 | 0.0602 |
0.3013 | 0.0853 |
0.4096 | 0.1267 |
0.5263 | 0.1823 |
0.6369 | 0.2512 |
0.7096 | 0.3101 |
0.7372 | 0.3364 |
0.7667 | 0.3680 |
0.8072 | 0.4185 |
0.8528 | 0.4899 |
0.8739 | 0.5299 |
0.9043 | 0.5979 |
0.9263 | 0.6582 |
0.9489 | 0.7336 |
0.9626 | 0.7891 |
0.9775 | 0.8599 |
0.9814 | 0.8810 |
0.9886 | 0.9231 |
0.9957 | 0.9690 |
0.9973 | 0.9802 |
Operational condition: Pressure, kPa = 97.3 (Liquid)
Mole fraction of Tetrahydropyran (2) - Gas | Mole fraction of Tetrahydropyran (2) - Liquid |
---|---|
0.0924 | 0.0227 |
0.2245 | 0.0602 |
0.3013 | 0.0853 |
0.4096 | 0.1267 |
0.5263 | 0.1823 |
0.6369 | 0.2512 |
0.7096 | 0.3101 |
0.7372 | 0.3364 |
0.7667 | 0.3680 |
0.8072 | 0.4185 |
0.8528 | 0.4899 |
0.8739 | 0.5299 |
0.9043 | 0.5979 |
0.9263 | 0.6582 |
0.9489 | 0.7336 |
0.9626 | 0.7891 |
0.9775 | 0.8599 |
0.9814 | 0.8810 |
0.9886 | 0.9231 |
0.9957 | 0.9690 |
0.9973 | 0.9802 |
Operational condition: Pressure, kPa = 97.3 (Liquid)
Mole fraction of Tetrahydropyran (2) - Gas | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0924 | 421.32 |
0.2245 | 416.96 |
0.3013 | 414.08 |
0.4096 | 409.65 |
0.5263 | 404.24 |
0.6369 | 398.15 |
0.7096 | 393.51 |
0.7372 | 391.55 |
0.7667 | 389.36 |
0.8072 | 386.07 |
0.8528 | 381.85 |
0.8739 | 379.69 |
0.9043 | 376.20 |
0.9263 | 373.35 |
0.9489 | 370.05 |
0.9626 | 367.81 |
0.9775 | 365.15 |
0.9814 | 364.41 |
0.9886 | 362.88 |
0.9957 | 361.30 |
0.9973 | 360.85 |
Operational condition: Pressure, kPa = 97.3 (Liquid)
Mole fraction of Tetrahydropyran (2) - Gas | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0924 | 421.32 |
0.2245 | 416.96 |
0.3013 | 414.08 |
0.4096 | 409.65 |
0.5263 | 404.24 |
0.6369 | 398.15 |
0.7096 | 393.51 |
0.7372 | 391.55 |
0.7667 | 389.36 |
0.8072 | 386.07 |
0.8528 | 381.85 |
0.8739 | 379.69 |
0.9043 | 376.20 |
0.9263 | 373.35 |
0.9489 | 370.05 |
0.9626 | 367.81 |
0.9775 | 365.15 |
0.9814 | 364.41 |
0.9886 | 362.88 |
0.9957 | 361.30 |
0.9973 | 360.85 |