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 |
|---|---|
| 0.2732 | 283.08 |
| 0.3262 | 286.09 |
| 0.3506 | 287.09 |
| 0.3522 | 286.99 |
| 0.3777 | 287.90 |
| 0.4017 | 288.48 |
| 0.4280 | 289.11 |
| 0.4751 | 289.68 |
| 0.5227 | 289.79 |
| 0.5466 | 289.89 |
| 0.5749 | 289.80 |
| 0.5773 | 289.80 |
| 0.5996 | 289.91 |
| 0.6475 | 289.89 |
| 0.6498 | 289.77 |
| 0.6760 | 289.69 |
| 0.7004 | 289.28 |
| 0.7241 | 288.94 |
| 0.7378 | 288.69 |
| 0.7525 | 288.21 |
| 0.7754 | 287.41 |
| 0.8255 | 284.20 |
| 0.8519 | 281.53 |
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 |
|---|---|
| 0.2732 | 283.08 |
| 0.3262 | 286.09 |
| 0.3506 | 287.09 |
| 0.3522 | 286.99 |
| 0.3777 | 287.90 |
| 0.4017 | 288.48 |
| 0.4280 | 289.11 |
| 0.4751 | 289.68 |
| 0.5227 | 289.79 |
| 0.5466 | 289.89 |
| 0.5749 | 289.80 |
| 0.5773 | 289.80 |
| 0.5996 | 289.91 |
| 0.6475 | 289.89 |
| 0.6498 | 289.77 |
| 0.6760 | 289.69 |
| 0.7004 | 289.28 |
| 0.7241 | 288.94 |
| 0.7378 | 288.69 |
| 0.7525 | 288.21 |
| 0.7754 | 287.41 |
| 0.8255 | 284.20 |
| 0.8519 | 281.53 |