Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Tetraglyme (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1772 | 280.19 |
| 0.2006 | 281.10 |
| 0.2046 | 281.10 |
| 0.2247 | 281.40 |
| 0.2495 | 281.73 |
| 0.2749 | 281.79 |
| 0.2772 | 281.89 |
| 0.2994 | 281.89 |
| 0.3241 | 281.77 |
| 0.3516 | 281.83 |
| 0.3527 | 281.78 |
| 0.3661 | 281.87 |
| 0.3717 | 281.77 |
| 0.3973 | 281.67 |
| 0.4003 | 281.68 |
| 0.4238 | 281.70 |
| 0.4266 | 281.69 |
| 0.4274 | 281.57 |
| 0.4494 | 281.40 |
| 0.4750 | 281.09 |
| 0.4753 | 281.19 |
| 0.4992 | 280.78 |
| 0.4995 | 280.87 |
| 0.5263 | 280.29 |
| 0.5534 | 279.73 |
| 0.5767 | 279.09 |
| 0.6056 | 278.09 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Tetraglyme (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1772 | 280.19 |
| 0.2006 | 281.10 |
| 0.2046 | 281.10 |
| 0.2247 | 281.40 |
| 0.2495 | 281.73 |
| 0.2749 | 281.79 |
| 0.2772 | 281.89 |
| 0.2994 | 281.89 |
| 0.3241 | 281.77 |
| 0.3516 | 281.83 |
| 0.3527 | 281.78 |
| 0.3661 | 281.87 |
| 0.3717 | 281.77 |
| 0.3973 | 281.67 |
| 0.4003 | 281.68 |
| 0.4238 | 281.70 |
| 0.4266 | 281.69 |
| 0.4274 | 281.57 |
| 0.4494 | 281.40 |
| 0.4750 | 281.09 |
| 0.4753 | 281.19 |
| 0.4992 | 280.78 |
| 0.4995 | 280.87 |
| 0.5263 | 280.29 |
| 0.5534 | 279.73 |
| 0.5767 | 279.09 |
| 0.6056 | 278.09 |