Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 273.37 |
| 0.0285 | 273.26 |
| 0.0535 | 272.93 |
| 0.0847 | 272.20 |
| 0.1097 | 271.87 |
| 0.1427 | 271.10 |
| 0.1709 | 270.72 |
| 0.1876 | 270.17 |
| 0.2277 | 269.27 |
| 0.2368 | 268.79 |
| 0.2486 | 268.45 |
| 0.2800 | 267.70 |
| 0.2934 | 267.27 |
| 0.3110 | 266.85 |
| 0.3395 | 266.17 |
| 0.3655 | 265.88 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.3949 | 266.03 |
| 0.4299 | 266.40 |
| 0.4567 | 266.85 |
| 0.4874 | 267.22 |
| 0.5161 | 267.32 |
| 0.5462 | 267.18 |
| 0.5778 | 266.77 |
| 0.6034 | 266.36 |
| 0.6338 | 265.71 |
| 0.6673 | 264.83 |
| 0.6892 | 264.10 |
| 0.7170 | 263.14 |
| 0.7437 | 261.93 |
| 0.7710 | 260.35 |
| 0.8031 | 258.35 |
| 0.8369 | 255.98 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.8713 | 253.88 |
| 0.8844 | 254.45 |
| 0.9022 | 255.15 |
| 0.9221 | 255.98 |
| 0.9381 | 256.60 |
| 0.9686 | 257.45 |
| 1.0000 | 258.03 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 273.37 |
| 0.0285 | 273.26 |
| 0.0535 | 272.93 |
| 0.0847 | 272.20 |
| 0.1097 | 271.87 |
| 0.1427 | 271.10 |
| 0.1709 | 270.72 |
| 0.1876 | 270.17 |
| 0.2277 | 269.27 |
| 0.2368 | 268.79 |
| 0.2486 | 268.45 |
| 0.2800 | 267.70 |
| 0.2934 | 267.27 |
| 0.3110 | 266.85 |
| 0.3395 | 266.17 |
| 0.3655 | 265.88 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.3949 | 266.03 |
| 0.4299 | 266.40 |
| 0.4567 | 266.85 |
| 0.4874 | 267.22 |
| 0.5161 | 267.32 |
| 0.5462 | 267.18 |
| 0.5778 | 266.77 |
| 0.6034 | 266.36 |
| 0.6338 | 265.71 |
| 0.6673 | 264.83 |
| 0.6892 | 264.10 |
| 0.7170 | 263.14 |
| 0.7437 | 261.93 |
| 0.7710 | 260.35 |
| 0.8031 | 258.35 |
| 0.8369 | 255.98 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Octanol (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.8713 | 253.88 |
| 0.8844 | 254.45 |
| 0.9022 | 255.15 |
| 0.9221 | 255.98 |
| 0.9381 | 256.60 |
| 0.9686 | 257.45 |
| 1.0000 | 258.03 |
Operational conditions:
| Mole fraction of 1-Octanol (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0430 | -1.9210e-07 |
| 0.1300 | -4.6250e-07 |
| 0.2358 | -7.2640e-07 |
| 0.3041 | -8.5810e-07 |
| 0.3470 | -9.3930e-07 |
| 0.4158 | -1.0244e-06 |
| 0.4571 | -1.0621e-06 |
| 0.5174 | -1.0712e-06 |
| 0.5540 | -1.0682e-06 |
| 0.5877 | -1.0515e-06 |
| 0.6385 | -1.0123e-06 |
| 0.7090 | -9.0340e-07 |
| 0.7589 | -8.0790e-07 |
| 0.8750 | -5.1020e-07 |
| 0.9290 | -3.2070e-07 |
| 0.9920 | -7.2400e-08 |
Operational conditions:
| Mole fraction of 1-Octanol (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0430 | -1.9210e-07 |
| 0.1300 | -4.6250e-07 |
| 0.2358 | -7.2640e-07 |
| 0.3041 | -8.5810e-07 |
| 0.3470 | -9.3930e-07 |
| 0.4158 | -1.0244e-06 |
| 0.4571 | -1.0621e-06 |
| 0.5174 | -1.0712e-06 |
| 0.5540 | -1.0682e-06 |
| 0.5877 | -1.0515e-06 |
| 0.6385 | -1.0123e-06 |
| 0.7090 | -9.0340e-07 |
| 0.7589 | -8.0790e-07 |
| 0.8750 | -5.1020e-07 |
| 0.9290 | -3.2070e-07 |
| 0.9920 | -7.2400e-08 |