Method for preparing 2-chloro-3,3,3-trifluoropropene by gas-phase fluorination
A gas-phase fluorination and trifluoropropene technology, applied in the field of preparing HCFO-1233xf, can solve the problems of low reaction yield and many reaction steps, etc.
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[0013] Preparation of fluorination catalyst:
[0014] Calcium oxalate and gamma ferric hydroxide are uniformly mixed according to their mass ratio of 40:60, pressed and molded to obtain a catalyst precursor, and after roasting at 380°C, fluorinated with hydrogen fluoride gas at 350°C to obtain a fluorination catalyst. The gamma ferric hydroxide used in the present invention can be obtained by the following method: dissolve the soluble salt of ferric iron in water, add a precipitating agent at 50-60°C, control the pH of the solution between 7.0-7.5, and precipitate After filtering, washing and drying, gamma ferric hydroxide is obtained; the soluble salt of ferric iron mentioned above can be ferric nitrate, ferric sulfate, ferric chloride or ferric oxalate, preferably ferric nitrate; precipitating agent can be ammonia, sodium hydroxide, carbonic acid Sodium, sodium bicarbonate or ammonia water, preferably ammonia water.
[0015] The temperature for the fluorination treatment of...
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 is charged, and HF and HCFC-1231 are introduced to react, and the molar ratio of HF / HCFC-1231 is controlled to be 15:1, the contact time is 10 seconds, the reaction temperature is 200°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 HCFC-1231 is 100% by gas chromatography analysis. HCFO-1233xf The selectivity is 99.0%.
Embodiment 2
[0021] The operation is basically the same as in Example 1, except that the reaction temperature is changed to 160° 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 HCFC-1231 to react, control the molar ratio of HF / HCFC-1231 to 15:1, the contact time is 10 seconds, the reaction temperature is 160°C, after 20 hours of reaction, the reaction product is washed with water and alkali to remove HCl and HF, the conversion rate of HCFC-1231 was 96% by gas chromatography analysis, and the selectivity of HCFO-1233xf was 96.0%.
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