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Synthesis method of halogen acetone

A synthesis method, acetone technology, applied in chemical instruments and methods, preparation of carbon-based compounds, preparation of organic compounds, etc., can solve problems such as high price of auxiliary catalysts, strong acidity of trifluoroacetic acid, increased synthesis costs, etc., and achieve operating costs Low, high selectivity, high productivity effect

Inactive Publication Date: 2012-02-01
NANTONG BAOKAI CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0015] The disadvantage of this synthesis method is that the raw materials are not easy to obtain, and the cost is high; trifluoroacetic acid is strong in acidity, and there is a certain danger in the production operation.
[0016] To sum up, these reactions or some auxiliary catalysts, raw materials have higher market prices, resulting in higher synthesis costs; or some reaction conditions are relatively harsh; therefore, we have innovated a new and more ideal synthesis method

Method used

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  • Synthesis method of halogen acetone
  • Synthesis method of halogen acetone
  • Synthesis method of halogen acetone

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preparation example Construction

[0025] The synthetic method step of halogenated acetone is as follows:

[0026] The synthesis method of halogenated acetone adopts a reactive distillation device, the height ratio of the reaction section of the reactive distillation device to the rectification section is 1:3 to 1:6, and 0.1 equivalent to 2 equivalents of water is added to the bottom of the reactive distillation device, and heated to 95 ℃ ~ 100 ℃, add ethyl haloacetoacetate in the middle of the reaction section, the molar ratio of ethyl haloacetoacetate to water is 1:1 ~ 1:2.5, and fill the reaction section with strong acidic cation exchange resin as a catalyst , ethyl haloacetoacetate reacts with water vapor after being catalyzed by the reaction section, and is separated by the rectification section. The product haloacetone is collected at the top of the rectification section, and the product collection bottle is placed in a freezing bath at -10°C to -60°C. The collected product was greater than 99% pure.

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Embodiment 1

[0036] Design the tower tank as a 20L reactor, the height ratio of the reaction section to the rectification section is 1:6, add 0.1 equivalent of water to the bottom of the reaction distillation device, heat to 100°C, add ethyl trifluoroacetoacetate in the middle of the reaction section, three The molar ratio of ethyl fluoroacetoacetate to water is 1:2.5. The reaction section is filled with strong acidic cation exchange resin NKC-9. After being catalyzed in the reaction section, ethyl trifluoroacetoacetate reacts with water vapor and is separated by the rectification section. , the product trifluoroacetone was collected at the top of the rectification section, and the product collection bottle was placed in a -60°C freezing bath. The collected product had a purity of 99.5% and a yield of 95%.

Embodiment 2

[0038] Design the tower kettle as a 20L reactor, the height ratio of the reaction section to the rectification section is 1:3, add 2 equivalents of water to the bottom of the reaction distillation device, heat to 100°C, add ethyl trifluoroacetoacetate in the middle of the reaction section, three The molar ratio of ethyl fluoroacetoacetate to water is 1:1. The reaction section is filled with strong acidic cation exchange resin NKC-9. After being catalyzed in the reaction section, ethyl trifluoroacetoacetate reacts with water vapor and is separated by the rectification section. , the product trifluoroacetone was collected at the top of the rectification section, and the product collection bottle was placed in a -40°C freezing bath. The collected product had a purity of 99.2% and a yield of 92%.

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Abstract

The invention discloses a synthesis method of halogen acetone. The method comprises the following steps of: selecting a reactive rectification device, wherein the height ratio of the reaction section to the rectification section of the reactive rectification device is 1:3-1:6; adding 0.1 to 2 equivalent water to the bottom of the reactive rectification device, heating the water to the temperature of between 95 and 100 DEG C, and adding halogenated ethyl acetoacetate to the middle part of the reaction section, wherein the molar ratio of the halogenated ethyl acetoacetate to the water is 1:1-1:2.5; and filling strongly acidic cation exchange resin serving as a catalyst into the reaction section, reacting the halogenated ethyl acetoacetate and water vapor after the halogenated ethyl acetoacetate is catalyzed at the reaction section, performing separation at the rectification section, collecting the halogen acetone product at the top of the rectification section, and putting a product collecting bottle in a freezing bath of 10 DEG C below zero to 60 DEG C below zero, wherein the purity of the collected product is more than 99 percent. Because the reactive rectification device is used for continuously producing the halogen acetone, the method has the advantages of high selectivity, high conversion rate, high production capacity, high product purity, simplicity and convenience in operation and low energy consumption; the reagent is easily obtained; the adopted catalyst can be reused; and the method is clean, environmentally-friendly, safe and reliable.

Description

technical field [0001] The present invention relates to a compound synthesis method, in particular to a synthesis method of halogenated acetone. Background technique [0002] Halogenated acetones, especially fluorinated acetones, are important pharmaceutical synthesis intermediates. It can participate in a variety of organic synthesis reactions, especially in the synthesis of fluorine-containing medicines, pesticides and dyes, and is one of the important intermediates of fluorine-containing fine chemicals. [0003] There are now methods for synthesizing related halogenated acetones, as follows: [0004] Masanori Tsukamoto, Saitama et al. (US6774266) used 3-halo-1,1,1,3-tetrafluoroacetone as a raw material for a gas phase reduction reaction. Using metal palladium as a catalyst, the raw materials are vaporized with hydrogen and passed through the catalyst palladium to react to generate trifluoroacetone. The reaction formula is as follows (Ⅱ): [0005] [0006] The disa...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C49/167C07C49/16C07C45/65
CPCY02P20/10Y02P20/584
Inventor 程桂林孟博许茂乾
Owner NANTONG BAOKAI CHEM
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