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 |
---|---|
0.5610 | 289.54 |
0.5660 | 289.67 |
0.5806 | 290.16 |
0.5913 | 290.51 |
0.5932 | 290.52 |
0.5993 | 290.69 |
0.6119 | 291.04 |
0.6206 | 291.27 |
0.6323 | 291.57 |
0.6392 | 291.71 |
0.6663 | 292.03 |
0.6786 | 292.16 |
0.7070 | 292.35 |
0.7124 | 292.35 |
0.7137 | 292.37 |
0.7213 | 292.38 |
0.7380 | 292.46 |
0.7524 | 292.48 |
0.7731 | 292.44 |
0.7835 | 292.41 |
0.7986 | 292.30 |
0.8126 | 292.21 |
0.8210 | 292.10 |
0.8328 | 291.88 |
0.8481 | 291.53 |
0.8486 | 291.45 |
0.8519 | 291.35 |
0.8551 | 291.22 |
0.8712 | 290.48 |
0.8844 | 289.57 |
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 |
---|---|
0.5610 | 289.54 |
0.5660 | 289.67 |
0.5806 | 290.16 |
0.5913 | 290.51 |
0.5932 | 290.52 |
0.5993 | 290.69 |
0.6119 | 291.04 |
0.6206 | 291.27 |
0.6323 | 291.57 |
0.6392 | 291.71 |
0.6663 | 292.03 |
0.6786 | 292.16 |
0.7070 | 292.35 |
0.7124 | 292.35 |
0.7137 | 292.37 |
0.7213 | 292.38 |
0.7380 | 292.46 |
0.7524 | 292.48 |
0.7731 | 292.44 |
0.7835 | 292.41 |
0.7986 | 292.30 |
0.8126 | 292.21 |
0.8210 | 292.10 |
0.8328 | 291.88 |
0.8481 | 291.53 |
0.8486 | 291.45 |
0.8519 | 291.35 |
0.8551 | 291.22 |
0.8712 | 290.48 |
0.8844 | 289.57 |