Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2155 | 317.80 |
0.2833 | 322.70 |
0.3312 | 326.60 |
0.3652 | 328.70 |
0.4002 | 330.50 |
0.4317 | 331.90 |
0.4672 | 333.10 |
0.5104 | 334.00 |
0.5225 | 334.30 |
0.5527 | 334.70 |
0.5771 | 334.90 |
0.6028 | 334.80 |
0.6128 | 335.00 |
0.6223 | 335.00 |
0.6250 | 334.80 |
0.6499 | 334.90 |
0.6632 | 334.70 |
0.6721 | 334.80 |
0.7050 | 334.90 |
0.7220 | 334.70 |
0.7396 | 334.40 |
0.7631 | 334.20 |
0.7852 | 333.40 |
0.8024 | 332.20 |
0.8195 | 331.00 |
0.8390 | 328.50 |
0.8541 | 326.00 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2155 | 317.80 |
0.2833 | 322.70 |
0.3312 | 326.60 |
0.3652 | 328.70 |
0.4002 | 330.50 |
0.4317 | 331.90 |
0.4672 | 333.10 |
0.5104 | 334.00 |
0.5225 | 334.30 |
0.5527 | 334.70 |
0.5771 | 334.90 |
0.6028 | 334.80 |
0.6128 | 335.00 |
0.6223 | 335.00 |
0.6250 | 334.80 |
0.6499 | 334.90 |
0.6632 | 334.70 |
0.6721 | 334.80 |
0.7050 | 334.90 |
0.7220 | 334.70 |
0.7396 | 334.40 |
0.7631 | 334.20 |
0.7852 | 333.40 |
0.8024 | 332.20 |
0.8195 | 331.00 |
0.8390 | 328.50 |
0.8541 | 326.00 |