Production method of high-purity 2-chloro-5-trifluoromethylpyridine
A technology for trifluoromethylpyridine and crude trifluoromethylpyridine, which is applied in the production field of 2-chloro-5-trifluoromethylpyridine, can solve the problems of many by-products, difficult purification, similar properties and the like, and achieves production The effect of good capacity, high product purity and stable yield
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Embodiment 1
[0023] (1) Under the action of silica-aluminum trioxide-chromium trioxide catalyst, acrolein and propionaldehyde are used as raw materials, after gasification, react with ammonia gas at 440°C for 1 hour, and the yield is not less than 65% 3-picoline.
[0024] (2) After the co-gasification of 3-picoline and carbon tetrachloride, react under chlorine atmosphere to obtain 2-chloro-5-trichloromethylpyridine, under the catalyst is mercuric oxide, carry out fluorine substitution with hydrogen fluoride, The yield of crude 2-chloro-5-trifluoromethylpyridine was not less than 85%.
[0025] (3) After heating and melting the crude 2-chloro-5-trifluoromethylpyridine at a rate of 0.5 °C / min to 29 °C, it was placed in a low-temperature constant temperature device for refrigeration and circulation, and cooled at a rate of 0.07 °C / min Crystallize at 14°C, separate to obtain recrystallization, sweat the recrystallization at 27°C, repeat the process of melting, recrystallization and sweating t...
Embodiment 2
[0027] (1) Under the action of silica-aluminum trioxide-chromium trioxide catalyst, acrolein and propionaldehyde are used as raw materials, after gasification, react with ammonia gas at 445°C for 3 hours, and the yield is not less than 65% 3-picoline.
[0028] (2) After the co-gasification of 3-picoline and carbon tetrachloride, react under chlorine atmosphere to obtain 2-chloro-5-trichloromethylpyridine, under the catalyst is mercuric oxide, carry out fluorine substitution with hydrogen fluoride, The yield of crude 2-chloro-5-trifluoromethylpyridine was not less than 85%.
[0029] (3) After heating and melting the crude 2-chloro-5-trifluoromethylpyridine at a rate of 0.7 °C / min to 33 °C, it was placed in a low-temperature constant temperature device for refrigeration and circulation, and cooled at a rate of 0.07 °C / min Crystallize at 22°C, separate to obtain recrystallization, sweat the recrystallization at 30°C, repeat the process of melting, recrystallization and sweating ...
Embodiment 3
[0031] (1) Under the action of silica-aluminum trioxide-chromium trioxide catalyst, acrolein and propionaldehyde are used as raw materials, after gasification, react with ammonia gas at 442°C for 2 hours, and the yield is not less than 65% 3-picoline.
[0032] (2) After the co-gasification of 3-picoline and carbon tetrachloride, react under chlorine atmosphere to obtain 2-chloro-5-trichloromethylpyridine, under the catalyst is mercuric oxide, carry out fluorine substitution with hydrogen fluoride, The yield of crude 2-chloro-5-trifluoromethylpyridine was not less than 85%.
[0033] (3) After heating and melting the crude 2-chloro-5-trifluoromethylpyridine at a rate of 0.6 °C / min to 30 °C, it was placed in a low-temperature constant temperature device for refrigeration and circulation, and cooled at a rate of 0.07 °C / min Crystallize at 16°C, separate to obtain recrystallization, sweat the recrystallization at 28°C, repeat the process of melting, recrystallization and sweating ...
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