Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of Ethanol, 2-phenoxy- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2089 | 361.59 |
0.2389 | 363.41 |
0.2618 | 364.76 |
0.2810 | 365.64 |
0.3007 | 366.37 |
0.3379 | 367.02 |
0.3741 | 367.38 |
0.3954 | 367.52 |
0.4232 | 367.54 |
0.4297 | 367.53 |
0.4511 | 367.59 |
0.4602 | 367.56 |
0.4752 | 367.54 |
0.4976 | 367.60 |
0.5112 | 367.45 |
0.5250 | 367.35 |
0.5466 | 367.28 |
0.5926 | 366.41 |
0.6273 | 365.13 |
0.6537 | 363.48 |
0.6858 | 361.45 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of Ethanol, 2-phenoxy- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2089 | 361.59 |
0.2389 | 363.41 |
0.2618 | 364.76 |
0.2810 | 365.64 |
0.3007 | 366.37 |
0.3379 | 367.02 |
0.3741 | 367.38 |
0.3954 | 367.52 |
0.4232 | 367.54 |
0.4297 | 367.53 |
0.4511 | 367.59 |
0.4602 | 367.56 |
0.4752 | 367.54 |
0.4976 | 367.60 |
0.5112 | 367.45 |
0.5250 | 367.35 |
0.5466 | 367.28 |
0.5926 | 366.41 |
0.6273 | 365.13 |
0.6537 | 363.48 |
0.6858 | 361.45 |