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 |