Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of Aniline, N-methyl- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.5071 | 283.85 |
0.5276 | 284.56 |
0.5365 | 284.86 |
0.5492 | 285.21 |
0.5616 | 285.50 |
0.5787 | 285.84 |
0.5873 | 286.12 |
0.6041 | 286.30 |
0.6298 | 286.56 |
0.6415 | 286.68 |
0.6596 | 286.77 |
0.6739 | 286.82 |
0.6991 | 286.89 |
0.7096 | 286.90 |
0.7231 | 286.93 |
0.7327 | 286.92 |
0.7434 | 286.86 |
0.7560 | 286.80 |
0.7663 | 286.72 |
0.7772 | 286.67 |
0.7871 | 286.59 |
0.8035 | 286.35 |
0.8168 | 286.11 |
0.8325 | 285.62 |
0.8437 | 285.15 |
0.8636 | 283.97 |
0.8756 | 282.99 |
0.8935 | 280.90 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of Aniline, N-methyl- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.5071 | 283.85 |
0.5276 | 284.56 |
0.5365 | 284.86 |
0.5492 | 285.21 |
0.5616 | 285.50 |
0.5787 | 285.84 |
0.5873 | 286.12 |
0.6041 | 286.30 |
0.6298 | 286.56 |
0.6415 | 286.68 |
0.6596 | 286.77 |
0.6739 | 286.82 |
0.6991 | 286.89 |
0.7096 | 286.90 |
0.7231 | 286.93 |
0.7327 | 286.92 |
0.7434 | 286.86 |
0.7560 | 286.80 |
0.7663 | 286.72 |
0.7772 | 286.67 |
0.7871 | 286.59 |
0.8035 | 286.35 |
0.8168 | 286.11 |
0.8325 | 285.62 |
0.8437 | 285.15 |
0.8636 | 283.97 |
0.8756 | 282.99 |
0.8935 | 280.90 |