Datasets
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Upper consolute composition: mole fraction (2)
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Upper consolute temperature, K (2)
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Liquid-liquid equilibrium temperature, K (2)
Upper consolute composition: mole fraction of Aniline (1)
[ref]
Upper consolute composition: mole fraction of Aniline (1) - Liquid mixture 1 |
0.5280 |
Upper consolute composition: mole fraction of Aniline (1)
[ref]
Upper consolute composition: mole fraction of Aniline (1) - Liquid mixture 1 |
0.5280 |
Upper consolute temperature, K
[ref]
Upper consolute temperature, K - Liquid mixture 1 |
313.78 |
Upper consolute temperature, K
[ref]
Upper consolute temperature, K - Liquid mixture 1 |
313.78 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Mole fraction of Aniline (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.1011 |
292.15 |
0.1209 |
296.77 |
0.1521 |
300.95 |
0.1725 |
304.28 |
0.2008 |
306.33 |
0.2196 |
307.89 |
0.2562 |
309.45 |
0.2696 |
310.17 |
0.2931 |
310.88 |
0.3167 |
311.69 |
0.3412 |
312.22 |
0.3649 |
312.56 |
0.3994 |
313.15 |
0.4088 |
313.18 |
0.4142 |
313.28 |
0.4319 |
313.43 |
0.4426 |
313.53 |
0.4500 |
313.47 |
0.4625 |
313.58 |
0.4770 |
313.65 |
0.4973 |
313.73 |
0.5084 |
313.75 |
0.5131 |
313.76 |
0.5174 |
313.78 |
0.5194 |
313.76 |
0.5269 |
313.79 |
0.5280 |
313.78 |
0.5382 |
313.76 |
0.5574 |
313.66 |
0.5657 |
313.62 |
0.6034 |
313.33 |
0.6167 |
313.08 |
0.6354 |
312.89 |
0.6600 |
312.25 |
0.6781 |
311.82 |
0.7106 |
310.58 |
0.7309 |
309.59 |
0.7513 |
308.24 |
0.7721 |
306.67 |
0.7944 |
304.58 |
0.8116 |
302.60 |
0.8340 |
299.08 |
0.8608 |
294.17 |
0.8747 |
290.62 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Mole fraction of Aniline (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.1011 |
292.15 |
0.1209 |
296.77 |
0.1521 |
300.95 |
0.1725 |
304.28 |
0.2008 |
306.33 |
0.2196 |
307.89 |
0.2562 |
309.45 |
0.2696 |
310.17 |
0.2931 |
310.88 |
0.3167 |
311.69 |
0.3412 |
312.22 |
0.3649 |
312.56 |
0.3994 |
313.15 |
0.4088 |
313.18 |
0.4142 |
313.28 |
0.4319 |
313.43 |
0.4426 |
313.53 |
0.4500 |
313.47 |
0.4625 |
313.58 |
0.4770 |
313.65 |
0.4973 |
313.73 |
0.5084 |
313.75 |
0.5131 |
313.76 |
0.5174 |
313.78 |
0.5194 |
313.76 |
0.5269 |
313.79 |
0.5280 |
313.78 |
0.5382 |
313.76 |
0.5574 |
313.66 |
0.5657 |
313.62 |
0.6034 |
313.33 |
0.6167 |
313.08 |
0.6354 |
312.89 |
0.6600 |
312.25 |
0.6781 |
311.82 |
0.7106 |
310.58 |
0.7309 |
309.59 |
0.7513 |
308.24 |
0.7721 |
306.67 |
0.7944 |
304.58 |
0.8116 |
302.60 |
0.8340 |
299.08 |
0.8608 |
294.17 |
0.8747 |
290.62 |
Sources