Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Nonanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 273.37 |
| 0.0964 | 271.21 |
| 0.1339 | 269.53 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Nonanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.2182 | 266.49 |
| 0.2712 | 268.26 |
| 0.3384 | 269.85 |
| 0.3888 | 270.57 |
| 0.4284 | 270.86 |
| 0.4837 | 271.05 |
| 0.5079 | 271.15 |
| 0.5347 | 271.12 |
| 0.6054 | 270.68 |
| 0.6408 | 270.15 |
| 0.6852 | 268.99 |
| 0.7423 | 266.92 |
| 0.8157 | 258.35 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Nonanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.8594 | 258.68 |
| 0.9446 | 266.04 |
| 1.0000 | 268.10 |
Operational conditions:
| Mole fraction of 1-Nonanol (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0489 | -1.7010e-07 |
| 0.1572 | -4.7420e-07 |
| 0.2155 | -6.3540e-07 |
| 0.2763 | -7.6610e-07 |
| 0.3283 | -8.7040e-07 |
| 0.3560 | -9.2770e-07 |
| 0.4125 | -1.0052e-06 |
| 0.4566 | -1.0434e-06 |
| 0.4998 | -1.0553e-06 |
| 0.5326 | -1.0570e-06 |
| 0.5732 | -1.0490e-06 |
| 0.6064 | -1.0157e-06 |
| 0.6370 | -9.7610e-07 |
| 0.6602 | -9.5110e-07 |
| 0.7321 | -8.0740e-07 |
| 0.7905 | -6.6290e-07 |
| 0.8753 | -4.3130e-07 |
| 0.9610 | -1.6610e-07 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.