Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Ethyl Acetate (2) - Liquid mixture 1 |
---|---|
303.20 | 0.9880 |
308.20 | 0.9870 |
313.20 | 0.9850 |
319.20 | 0.9830 |
323.20 | 0.9780 |
325.20 | 0.9790 |
334.20 | 0.9700 |
343.20 | 0.9660 |
348.20 | 0.9620 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Ethyl Acetate (2) - Liquid mixture 2 |
---|---|
303.20 | 0.0450 |
308.20 | 0.0460 |
313.20 | 0.0480 |
319.20 | 0.0490 |
323.20 | 0.0490 |
325.20 | 0.0500 |
334.20 | 0.0520 |
343.20 | 0.0530 |
348.20 | 0.0540 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Ethyl Acetate (2) - Liquid mixture 1 |
---|---|
303.20 | 0.9880 |
308.20 | 0.9870 |
313.20 | 0.9850 |
319.20 | 0.9830 |
323.20 | 0.9780 |
325.20 | 0.9790 |
334.20 | 0.9700 |
343.20 | 0.9660 |
348.20 | 0.9620 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Ethyl Acetate (2) - Liquid mixture 2 |
---|---|
303.20 | 0.0450 |
308.20 | 0.0460 |
313.20 | 0.0480 |
319.20 | 0.0490 |
323.20 | 0.0490 |
325.20 | 0.0500 |
334.20 | 0.0520 |
343.20 | 0.0530 |
348.20 | 0.0540 |