Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass fraction of Triethylene glycol, hexyl ether (2) - Liquid mixture 1 |
|---|---|
| 323.15 | 0.0231 |
| 333.15 | 0.0143 |
| 343.15 | 0.0129 |
| 353.15 | 0.0121 |
| 363.15 | 0.0121 |
| 373.15 | 0.0125 |
| 383.15 | 0.0129 |
| 393.15 | 0.0136 |
| 403.15 | 0.0150 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mass fraction of Triethylene glycol, hexyl ether (2) - Liquid mixture 2 |
|---|---|
| 323.15 | 0.4000 |
| 333.15 | 0.5690 |
| 343.15 | 0.6550 |
| 353.15 | 0.7070 |
| 363.15 | 0.7380 |
| 373.15 | 0.7590 |
| 383.15 | 0.7690 |
| 393.15 | 0.7730 |
| 403.15 | 0.7750 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass fraction of Triethylene glycol, hexyl ether (2) - Liquid mixture 1 |
|---|---|
| 323.15 | 0.0231 |
| 333.15 | 0.0143 |
| 343.15 | 0.0129 |
| 353.15 | 0.0121 |
| 363.15 | 0.0121 |
| 373.15 | 0.0125 |
| 383.15 | 0.0129 |
| 393.15 | 0.0136 |
| 403.15 | 0.0150 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mass fraction of Triethylene glycol, hexyl ether (2) - Liquid mixture 2 |
|---|---|
| 323.15 | 0.4000 |
| 333.15 | 0.5690 |
| 343.15 | 0.6550 |
| 353.15 | 0.7070 |
| 363.15 | 0.7380 |
| 373.15 | 0.7590 |
| 383.15 | 0.7690 |
| 393.15 | 0.7730 |
| 403.15 | 0.7750 |