Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of 2,5,8,11-Tetraoxadodecane (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.2483 | 267.55 |
| 0.2541 | 267.76 |
| 0.2711 | 268.37 |
| 0.2986 | 269.31 |
| 0.3205 | 269.59 |
| 0.3216 | 269.72 |
| 0.3476 | 269.92 |
| 0.3732 | 270.13 |
| 0.3756 | 270.15 |
| 0.3994 | 270.28 |
| 0.4254 | 270.19 |
| 0.4266 | 270.22 |
| 0.4483 | 270.28 |
| 0.4754 | 270.22 |
| 0.4983 | 270.20 |
| 0.5233 | 270.13 |
| 0.5465 | 270.07 |
| 0.5736 | 270.01 |
| 0.5752 | 269.87 |
| 0.5758 | 270.01 |
| 0.6038 | 269.64 |
| 0.6221 | 269.31 |
| 0.6241 | 269.32 |
| 0.6510 | 268.81 |
| 0.7017 | 267.04 |
| 0.7023 | 267.05 |
| 0.7509 | 264.85 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of 2,5,8,11-Tetraoxadodecane (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.2483 | 267.55 |
| 0.2541 | 267.76 |
| 0.2711 | 268.37 |
| 0.2986 | 269.31 |
| 0.3205 | 269.59 |
| 0.3216 | 269.72 |
| 0.3476 | 269.92 |
| 0.3732 | 270.13 |
| 0.3756 | 270.15 |
| 0.3994 | 270.28 |
| 0.4254 | 270.19 |
| 0.4266 | 270.22 |
| 0.4483 | 270.28 |
| 0.4754 | 270.22 |
| 0.4983 | 270.20 |
| 0.5233 | 270.13 |
| 0.5465 | 270.07 |
| 0.5736 | 270.01 |
| 0.5752 | 269.87 |
| 0.5758 | 270.01 |
| 0.6038 | 269.64 |
| 0.6221 | 269.31 |
| 0.6241 | 269.32 |
| 0.6510 | 268.81 |
| 0.7017 | 267.04 |
| 0.7023 | 267.05 |
| 0.7509 | 264.85 |