Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of Acetonitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.3499 | 373.38 |
0.4017 | 378.51 |
0.4496 | 382.58 |
0.4977 | 386.02 |
0.5341 | 388.58 |
0.5647 | 389.92 |
0.5981 | 391.30 |
0.7003 | 393.65 |
0.7219 | 393.83 |
0.7501 | 394.10 |
0.7636 | 394.16 |
0.7757 | 394.26 |
0.7857 | 394.27 |
0.8014 | 394.18 |
0.8417 | 393.53 |
0.8620 | 393.06 |
0.8831 | 391.73 |
0.9014 | 390.22 |
0.9183 | 386.91 |
0.9318 | 382.72 |
0.9519 | 373.72 |
0.9605 | 368.13 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of Acetonitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.3499 | 373.38 |
0.4017 | 378.51 |
0.4496 | 382.58 |
0.4977 | 386.02 |
0.5341 | 388.58 |
0.5647 | 389.92 |
0.5981 | 391.30 |
0.7003 | 393.65 |
0.7219 | 393.83 |
0.7501 | 394.10 |
0.7636 | 394.16 |
0.7757 | 394.26 |
0.7857 | 394.27 |
0.8014 | 394.18 |
0.8417 | 393.53 |
0.8620 | 393.06 |
0.8831 | 391.73 |
0.9014 | 390.22 |
0.9183 | 386.91 |
0.9318 | 382.72 |
0.9519 | 373.72 |
0.9605 | 368.13 |