Process for producing 2-chloro-3,3,3-trifluoropropene
A technology for trifluoropropene and fluorine-containing alkane, which is applied in the field of preparing 2-chloro-3,3,3-trifluoropropene, can solve the problem of complicated operation, no economical and applicable method for HCFO-1233xf, unsuitable for industrial production, etc. problems to achieve high yields
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Embodiment 1
[0061] A 50 wt% potassium hydroxide aqueous solution (1,000 g) and a phase transfer catalyst Aliquat 336 (trade name, manufactured by Aldrich) (trioctylmethylammonium chloride (TOMAC)) (3.0 g) were added to a device equipped for measuring the reaction thermometer, thermometer for measuring the temperature at the top of the distillation column, dropping funnel, Oldershaw column (five trays), distillation head, cold finger trap with dry ice / acetone, and receiver in a 1 L three-necked flask. The resulting mixture was cooled to 10°C in a water bath. While stirring the cooled mixture with a magnetic stirrer, 1,2-dichloro-3,3,3-trifluoropropane (HCFC-243db) (700 g, 4.2 mol) was added dropwise from the dropping funnel, thereby The temperature is kept at 20°C or lower. When the temperature inside the reactor reached 14°C or higher, gas was generated. When the temperature at the top of the distillation column reaches 13°C, the reflux ratio (return:distillate) changes from total refl...
Embodiment 2
[0063] The same reaction was carried out in the same manner as in Example 1, except that 220 g (1.32 mol) of 2-dichloro-3,3,3-trifluoropropane (HCFC-243db), 95 g of 60 wt % sodium hydroxide aqueous solution were used , and 1.0 g of Aliquat 336 (manufactured by Aldrich). Thus, 174 g of a fraction containing the target 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) was obtained. The purity by gas chromatographic analysis was 99.1%; therefore, the yield at this point was 96%.
Embodiment 3
[0065] The same reaction was carried out in the same manner as in Example 1, except that 180 g (1.08 mol) of 2-dichloro-3,3,3-trifluoropropane (HCFC-243db), 280 g of 50 wt % aqueous potassium hydroxide , and 30.0g replace the aprotic polar solvent of the phase transfer catalyst, that is, dimethylacetamide. Thus, 108 g of a fraction containing 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) was obtained. The purity by gas chromatographic analysis was 99.0%; therefore, the yield at this point was 89%.
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