Operational conditions:
Temperature, K - Liquid | Activity coefficient of Ethanol (1) - Liquid |
---|---|
340.19 | 1.927 |
348.01 | 1.802 |
358.23 | 1.624 |
Operational conditions:
Temperature, K - Liquid | Activity coefficient of Ethanol (1) - Liquid |
---|---|
340.19 | 1.927 |
348.01 | 1.802 |
358.23 | 1.624 |
Operational condition: Pressure, kPa = 100 (Liquid)
Mole fraction of n-Hexadecanoic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0682 | 307.27 |
0.1133 | 311.76 |
0.2034 | 317.46 |
0.2844 | 320.97 |
0.3657 | 324.04 |
0.5824 | 330.06 |
0.7899 | 334.39 |
0.8628 | 334.98 |
0.9031 | 335.59 |
1.0000 | 336.13 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of n-Hexadecanoic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0128 | 292.15 |
0.0170 | 295.35 |
0.0232 | 297.85 |
0.0393 | 302.75 |
0.0454 | 304.15 |
0.0565 | 306.25 |
0.0679 | 307.65 |
0.0929 | 310.05 |
0.1210 | 312.35 |
0.1425 | 313.75 |
0.1642 | 315.15 |
0.2053 | 317.05 |
0.2513 | 319.25 |
0.3241 | 321.55 |
0.3950 | 323.65 |
Operational condition: Pressure, kPa = 100 (Liquid)
Mole fraction of n-Hexadecanoic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0682 | 307.27 |
0.1133 | 311.76 |
0.2034 | 317.46 |
0.2844 | 320.97 |
0.3657 | 324.04 |
0.5824 | 330.06 |
0.7899 | 334.39 |
0.8628 | 334.98 |
0.9031 | 335.59 |
1.0000 | 336.13 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of n-Hexadecanoic acid (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0128 | 292.15 |
0.0170 | 295.35 |
0.0232 | 297.85 |
0.0393 | 302.75 |
0.0454 | 304.15 |
0.0565 | 306.25 |
0.0679 | 307.65 |
0.0929 | 310.05 |
0.1210 | 312.35 |
0.1425 | 313.75 |
0.1642 | 315.15 |
0.2053 | 317.05 |
0.2513 | 319.25 |
0.3241 | 321.55 |
0.3950 | 323.65 |