Operational conditions:
Temperature, K - Liquid | Activity coefficient of Ethylbenzene (2) - Liquid |
---|---|
333.20 | 8.63 |
348.20 | 8.21 |
363.20 | 7.86 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of Ethylbenzene (2) - Liquid |
---|---|
323.15 | 10.8636 |
333.15 | 10.2807 |
343.15 | 9.7303 |
353.15 | 9.1046 |
363.15 | 8.7188 |
373.10 | 8.3906 |
383.15 | 7.942 |
393.15 | 7.7208 |
Operational conditions:
Temperature, K - Liquid | Activity coefficient of Ethylbenzene (2) - Liquid |
---|---|
333.20 | 8.63 |
348.20 | 8.21 |
363.20 | 7.86 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of Ethylbenzene (2) - Liquid |
---|---|
323.15 | 10.8636 |
333.15 | 10.2807 |
343.15 | 9.7303 |
353.15 | 9.1046 |
363.15 | 8.7188 |
373.10 | 8.3906 |
383.15 | 7.942 |
393.15 | 7.7208 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Triethylene glycol (1) - Liquid mixture 1 |
---|---|
366.55 | 0.0870 |
369.05 | 0.0970 |
371.55 | 0.1080 |
374.65 | 0.1230 |
377.15 | 0.1420 |
379.95 | 0.1680 |
382.15 | 0.2060 |
383.55 | 0.2330 |
384.05 | 0.2670 |
384.55 | 0.3130 |
384.25 | 0.3780 |
383.15 | 0.4760 |
381.15 | 0.5320 |
373.15 | 0.6030 |
356.15 | 0.6950 |
298.15 | 0.8200 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Triethylene glycol (1) - Liquid mixture 1 |
---|---|
366.55 | 0.0870 |
369.05 | 0.0970 |
371.55 | 0.1080 |
374.65 | 0.1230 |
377.15 | 0.1420 |
379.95 | 0.1680 |
382.15 | 0.2060 |
383.55 | 0.2330 |
384.05 | 0.2670 |
384.55 | 0.3130 |
384.25 | 0.3780 |
383.15 | 0.4760 |
381.15 | 0.5320 |
373.15 | 0.6030 |
356.15 | 0.6950 |
298.15 | 0.8200 |