Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid | Mole fraction of Hexadecanoic acid, ethyl ester (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
| 0.0990 | 0.0862 | 283.09 |
| 0.2337 | 0.0988 | 279.18 |
| 0.2945 | 0.1423 | 277.04 |
| 0.4436 | 0.1011 | 272.92 |
| 0.4884 | 0.1151 | 272.00 |
| 0.5809 | 0.1363 | 270.09 |
| 0.6683 | 0.1406 | 268.66 |
| 0.7858 | 0.1016 | 267.25 |
| 0.1260 | 0.2015 | 280.54 |
| 0.2060 | 0.2068 | 278.98 |
| 0.3042 | 0.2078 | 277.25 |
| 0.4109 | 0.1962 | 274.69 |
| 0.4994 | 0.1985 | 272.57 |
| 0.5979 | 0.1995 | 270.30 |
| 0.7090 | 0.1995 | 278.00 |
| 0.1085 | 0.3020 | 282.07 |
| 0.1911 | 0.3163 | 281.33 |
| 0.3131 | 0.2958 | 279.07 |
| 0.3874 | 0.3085 | 282.19 |
| 0.4892 | 0.3005 | 282.93 |
| 0.5813 | 0.3036 | 283.03 |
| 0.1270 | 0.3838 | 283.28 |
| 0.2118 | 0.3937 | 285.05 |
| 0.3074 | 0.4103 | 286.36 |
| 0.3967 | 0.3694 | 285.49 |
| 0.4717 | 0.4370 | 286.95 |
| 0.0936 | 0.5113 | 287.85 |
| 0.1965 | 0.4807 | 287.74 |
| 0.3087 | 0.5157 | 289.15 |
| 0.3643 | 0.5203 | 289.15 |
| 0.1301 | 0.5929 | 290.82 |
| 0.1934 | 0.5886 | 290.93 |
| 0.2886 | 0.5416 | 289.96 |
| 0.1312 | 0.6668 | 292.59 |
| 0.1857 | 0.6926 | 293.20 |
| 0.1030 | 0.8026 | 295.25 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid | Mole fraction of Hexadecanoic acid, ethyl ester (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
| 0.0990 | 0.0862 | 283.09 |
| 0.2337 | 0.0988 | 279.18 |
| 0.2945 | 0.1423 | 277.04 |
| 0.4436 | 0.1011 | 272.92 |
| 0.4884 | 0.1151 | 272.00 |
| 0.5809 | 0.1363 | 270.09 |
| 0.6683 | 0.1406 | 268.66 |
| 0.7858 | 0.1016 | 267.25 |
| 0.1260 | 0.2015 | 280.54 |
| 0.2060 | 0.2068 | 278.98 |
| 0.3042 | 0.2078 | 277.25 |
| 0.4109 | 0.1962 | 274.69 |
| 0.4994 | 0.1985 | 272.57 |
| 0.5979 | 0.1995 | 270.30 |
| 0.7090 | 0.1995 | 278.00 |
| 0.1085 | 0.3020 | 282.07 |
| 0.1911 | 0.3163 | 281.33 |
| 0.3131 | 0.2958 | 279.07 |
| 0.3874 | 0.3085 | 282.19 |
| 0.4892 | 0.3005 | 282.93 |
| 0.5813 | 0.3036 | 283.03 |
| 0.1270 | 0.3838 | 283.28 |
| 0.2118 | 0.3937 | 285.05 |
| 0.3074 | 0.4103 | 286.36 |
| 0.3967 | 0.3694 | 285.49 |
| 0.4717 | 0.4370 | 286.95 |
| 0.0936 | 0.5113 | 287.85 |
| 0.1965 | 0.4807 | 287.74 |
| 0.3087 | 0.5157 | 289.15 |
| 0.3643 | 0.5203 | 289.15 |
| 0.1301 | 0.5929 | 290.82 |
| 0.1934 | 0.5886 | 290.93 |
| 0.2886 | 0.5416 | 289.96 |
| 0.1312 | 0.6668 | 292.59 |
| 0.1857 | 0.6926 | 293.20 |
| 0.1030 | 0.8026 | 295.25 |