Method for preparing 2-chloro-3,3,3-trifluoropropene by gas-phase fluorination
A technology of trifluoropropene and gas phase fluorination, which is applied in the fields of dehydrohalogenation preparation, chemical instruments and methods, halogen substitution preparation, etc., and can solve the problems of many reaction steps and low yield of HCFO-1233xf
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[0015] Preparation of fluorination catalyst
[0016] Dissolve ferric chloride in water, react with precipitant ammonia water at 50°C, adjust the pH value of the reaction solution in the range of 7.0 to 7.5, make it fully precipitate under stirring conditions, and put the formed ferric hydroxide slurry Hot filtration followed by overnight drying at 120°C for 12 hours yielded γ-Fe(OH) 3 .
[0017] Calcium carbonate and γ-Fe(OH) 3 Mix evenly at a mass ratio of 60:40, press into tablets to form a catalyst precursor. The catalyst precursor was calcined in a muffle furnace at 450°C for 8 hours, then loaded into a tubular reactor, heated to 300°C, fed with hydrogen fluoride gas for fluorination for 1 hour, then raised to 400°C at a heating rate of 1°C / min, and continued After fluorination for 8 hours, a calcium fluoride-based fluorination catalyst was obtained.
Embodiment 1
[0019] In a nickel tube fixed-bed tubular reactor with an internal diameter of 38mm, 60ml of the above-mentioned calcium fluoride-based fluorination catalyst was charged, and HF and HCC-240ab were introduced to react, and the molar ratio of HF / HCC-240ab was controlled to be 15:1, the contact time is 10 seconds, the reaction temperature is 280 ° C, after 20 hours of reaction, the reaction product is washed with water and alkali to remove HCl and HF, and the conversion rate of HCC-240ab is 100% by gas chromatography analysis, and the conversion rate of HCFO-1233xf The selectivity was 94%.
Embodiment 2
[0021] The operation is basically the same as in Example 1, except that the reaction temperature is changed to 260° C., and 60 ml of the calcium fluoride-based fluorination catalyst prepared above is loaded into a nickel tube fixed-bed tubular reactor with an inner diameter of 38 mm. , feed HF and HCC-240ab to react, control the molar ratio of HF / HCC-240ab to 15:1, contact time is 10 seconds, reaction temperature is 260°C, after reaction for 20 hours, the reaction product is washed with water and alkali to remove HCl and HF, the conversion rate of HCC-240ab was 96% by gas chromatography analysis, and the selectivity of HCFO-1233xf was 92%.
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