Operational conditions:
Temperature, K - Liquid | Activity coefficient of Isopropyl Alcohol (1) - Liquid |
---|---|
340.19 | 1.468 |
348.01 | 1.408 |
358.32 | 1.291 |
Operational conditions:
Temperature, K - Liquid | Activity coefficient of Isopropyl Alcohol (1) - Liquid |
---|---|
340.19 | 1.468 |
348.01 | 1.408 |
358.32 | 1.291 |
Operational condition: Pressure, kPa = 100 (Liquid)
Mole fraction of n-Hexadecanoic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0890 | 305.41 |
0.2117 | 314.74 |
0.3146 | 319.42 |
0.3782 | 322.04 |
0.4904 | 327.15 |
0.5673 | 328.87 |
0.6796 | 330.71 |
0.7898 | 331.76 |
0.8744 | 334.48 |
1.0000 | 336.13 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of n-Hexadecanoic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0270 | 291.75 |
0.0325 | 293.65 |
0.0416 | 296.25 |
0.0581 | 299.95 |
0.0889 | 304.25 |
0.1135 | 306.65 |
0.1525 | 309.85 |
0.2103 | 313.85 |
0.2617 | 316.75 |
0.3168 | 319.35 |
0.3801 | 321.75 |
Operational condition: Pressure, kPa = 100 (Liquid)
Mole fraction of n-Hexadecanoic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0890 | 305.41 |
0.2117 | 314.74 |
0.3146 | 319.42 |
0.3782 | 322.04 |
0.4904 | 327.15 |
0.5673 | 328.87 |
0.6796 | 330.71 |
0.7898 | 331.76 |
0.8744 | 334.48 |
1.0000 | 336.13 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of n-Hexadecanoic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0270 | 291.75 |
0.0325 | 293.65 |
0.0416 | 296.25 |
0.0581 | 299.95 |
0.0889 | 304.25 |
0.1135 | 306.65 |
0.1525 | 309.85 |
0.2103 | 313.85 |
0.2617 | 316.75 |
0.3168 | 319.35 |
0.3801 | 321.75 |