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Method for preparing 1,1,1,3,3,3-hexafluoroacetone by gas phase fluorination

A gas-phase fluorination and hexafluoroacetone technology, applied in the preparation of carbon-based compounds, chemical instruments and methods, preparation of organic compounds, etc., can solve the problems of difficult separation of products, high reaction temperature, production and use of human and environmental hazards, etc. , to achieve the effect of safety and environmental protection, simple preparation process and low production cost

Active Publication Date: 2015-06-17
XIAN MODERN CHEM RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the catalysts used in this method are all chromium-based catalysts, which have the problems of high reaction temperature, low product yield, and difficult separation of products, which limit its industrial application.
In addition, it has been proved that chromium compounds are toxic and can cause damage to the human digestive tract and kidneys, and high-valent chromium has a strong carcinogenic effect, and its production and use will cause harm to humans and the environment. At the same time, the thermal stability of chromium-containing catalysts is poor , the catalytic activity of the catalyst at high temperature cannot be guaranteed

Method used

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  • Method for preparing 1,1,1,3,3,3-hexafluoroacetone by gas phase fluorination

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] 64.8g of Fe(NO 3 ) 3 and 1.06 g of CuCl 2 Dissolved in 100ml of distilled water to make an impregnation solution, then 100g of Al 2 o 3 The carrier is placed in the impregnation solution, and after immersion for 12 hours, it is dried on a rotary evaporator at 80°C, and the water is evaporated to dryness to obtain a fluorination catalyst in which the weight of the Fe element is 15% of the weight of the carrier and the weight of the Cu element is 0.5% of the weight of the carrier. the precursor body. The precursor of the fluorination catalyst was roasted in a muffle furnace at 350°C for 8 hours, then loaded into a tubular reactor, heated to 200°C, fed with hydrogen fluoride gas for fluorination for 1 hour, and then heated at a rate of 1°C / min to Continue fluorination at 350°C for 8 hours to obtain a fluorination catalyst.

[0033] Add 60 ml of the fluorination catalyst prepared by the above method into a carbon steel pipe with an inner diameter of 38mm, feed HF and 1...

Embodiment 2

[0035] The present embodiment carries out according to the same step as embodiment 1, and the difference is that Fe(NO 3 ) 3 The amount was changed to 43.2g, the drying temperature was changed to 50°C, and the calcination temperature was changed to 450°C to obtain a fluorinated catalyst precursor in which the weight of the Fe element was 10% of the weight of the carrier, and the weight of the Cu element was 0.5% of the weight of the carrier. The product of this embodiment is analyzed by gas chromatography, and the conversion rate of 1,1,1,3,3,3-hexachloroacetone is 63%, and the selectivity of 1,1,1,3,3,3-hexafluoroacetone It is 96.1%.

Embodiment 3

[0037] The present embodiment carries out according to the same step as embodiment 1, and the difference is that Fe(NO 3 ) 3 Change it to 15.5g of iron acetate to prepare a fluorination catalyst precursor in which the weight of Fe element is 5% of the weight of the carrier, and the weight of Cu element is 0.5% of the weight of the carrier. The product of the present embodiment is analyzed by gas chromatography, and the conversion rate of 1,1,1,3,3,3-hexachloroacetone is 60%, and the selectivity of 1,1,1,3,3,3-hexafluoroacetone 95.8%.

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Abstract

The invention discloses a method for preparing 1,1,1,3,3,3-hexafluoroacetone by gas phase fluorination. The method comprises that 1,1,1,3,3,3-hexachloroacetone as a raw material undergoes a one-step gas phase fluorination reaction in the presence of a fluorination catalyst at a reaction temperature of 300 DEG C to produce 1,1,1,3,3,3-hexafluoroacetone, wherein a mole ratio of hydrogen fluoride to the organic matter is 10: 1 and contact time is 10s. The fluorination catalyst is a ferric compound-loaded catalyst. A preparation method of the fluorination catalyst comprises utilizing alumina, magnesium oxide or calcium oxide as carriers, dipping the carriers in an iron soluble salt and one of soluble salts of metal cocatalysts such as copper, manganese, zinc, nickel, cobalt and lanthanum to obtain a catalyst precursor with a mass ratio of iron to the carriers of 2-20% and cocatalyst content of 0.5-2wt%, and carrying out drying, roasting and HF fluorination. The prepared fluorination catalyst has the characteristics of environment-friendliness, low price, good catalytic activity, good stability and regeneration easiness. The method realizes high-selectivity synthesis of the 1,1,1,3,3,3-hexafluoroacetone.

Description

technical field [0001] The present invention relates to a kind of preparation method of 1,1,1,3,3,3-hexafluoroacetone, especially to a kind of using hydrogen fluoride and 1,1,1,3,3,3-hexachloroacetone as raw materials, in The invention relates to a preparation method for obtaining 1,1,1,3,3,3-hexafluoroacetone by gas-phase fluorination reaction in the presence of a fluorination catalyst. Background technique [0002] Hexafluoroacetone (CF 3 COCF 3 ,HFA) is the simplest perfluoroketone compound, and it is also an important fluorine-containing intermediate with a wide range of uses. At present, hexafluoroacetone has been widely used in the fields of medicine, pesticide and synthetic materials, especially as a raw material for the synthesis of polymer materials in special fields, which has profound significance. [0003] French patent FR1372549 reported that under the action of a catalyst composed of a trivalent chromium compound, at 350-450°C, hexachloroacetone and hydrogen...

Claims

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Application Information

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IPC IPC(8): C07C49/167C07C45/63
CPCC07C45/63C07C49/167
Inventor 吕剑秦越张振华张伟李春迎魏阿宝毛伟杨志强陆居有王博袁俊
Owner XIAN MODERN CHEM RES INST
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