Synthetic method of p-trifluoromethylaniline

A technology of trifluoromethylaniline and p-chlorotrifluorotoluene is applied in the field of synthesis of p-trifluoromethylaniline, can solve the problems of high process energy consumption, high potassium fluoride consumption, uneconomical process and the like, and achieves environmental friendliness , the effect of low price and low production cost

Inactive Publication Date: 2008-11-05
太仓中化环保化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] US4096185 has proposed with p-chlorobenzotrifluorotoluene raw material, and cuprous chloride is cocatalyst, and potassium fluoride is main catalyst direct high-pressure ammonolysis and prepares the method for p-aminobenzotrifluorotoluene, but, there is following shortcoming in this method: (1) fluorine Potassium chloride consumption is high, and the process is uneconomical; (2) it is difficult to obtain higher selectivity while ensuring a higher p-chlorobenzotrifluoride conversion; (3) the reaction temperature is high, and the process energy consumption is high
[0005] Chinese patent 200610040453.2 discloses a method of directly high-pressure ammonolysis of p-chlorobenzotrifluoride to synthesize p-aminobenzotrifluoride. Although the conversion rate of the ammonolysis reaction is relatively high, there is still the problem of relatively high catalyst prices

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Add 400g p-chlorobenzotrifluoride, 12g cuprous chloride, 10g potassium fluoride, 50g composite phase transfer catalyst (including 20g tetramethylammonium bromide, 10g benzyltriphenylphosphonium bromide) in the autoclave of 3L successively And 20g polyethylene glycol 400), sulfolane (solvent) 600g, sodium carbonate 60g, after replacing with nitrogen 3 times, feed 200g of liquid ammonia, then react at 150°C and pressure 8-10MPa for 9-10h. After the reaction is over, the excess liquid ammonia is absorbed into ammonia water, and the solid residue is filtered out at the same time. The filtrate is rectified to obtain 100g of p-trifluoromethylaniline product. At the same time, 250g of p-chlorobenzotrifluoride is recovered, and p-chlorobenzotrifluoride is transformed into The yield was 75%, and the actual yield of p-trifluoromethylaniline was 75%. The p-chlorobenzotrifluoride that reclaims and rectification remaining raffinate (sulfolane and composite phase-transfer catalyst) a...

Embodiment 2

[0024] To a 3L autoclave, add 400g p-chlorobenzotrifluoride, 12g cuprous chloride, 10g potassium fluoride, the raffinate after the rectification of Example 1, 60g sodium carbonate successively, and after nitrogen replacement for 3 times, feed 200g liquid ammonia, and then react at 150°C for 9-10 hours under a pressure of 8-10 MPa. After reaction finishes, excessive liquid ammonia is absorbed as ammoniacal liquor with water, and solid residue is filtered out simultaneously, and filtrate rectification reclaims p-chlorobenzotrifluoride 252g and product p-trifluoromethylaniline 103g, raffinate (sulfolane and composite phase transfer catalyst) Apply to the next batch of reactions.

Embodiment 3

[0026] To the autoclave of 3L, add 400g p-chlorobenzotrifluoride, 12g cuprous chloride, 10g potassium fluoride, the remaining raffinate and sodium carbonate 60g of embodiment 2 rectification successively, after nitrogen replacement 3 times, pass into 200g liquid Ammonia, then react at 150°C for 9-10 hours under a pressure of 8-10 MPa. After reaction finishes, excessive liquid ammonia water absorption is ammoniacal liquor, filters out solid residue simultaneously, filtrate rectification, reclaims p-chlorobenzotrifluoride 249g and product p-trifluoromethylaniline 105g, raffinate (sulfolane and composite phase transfer catalyst) Apply to the next batch of reactions.

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PUM

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Abstract

The invention relates to a synthetic method of p-trifluoromethylaniline; p-chlorobenzotrifluoride and liquid ammonia generate an ammonolysis reaction to generate the p-trifluoromethylaniline under the action of a catalyst and an acid-binding agent; according to portion by weight, the components of the catalyst is: cuprous chloride of 1 to 10 portions, potassium fluoride of 2 to 30 portions and phase transfer catalyst of 5 to 30 portions; the adding amount of the catalyst is 8 to 70 percent of the p-chlorobenzotrifluoride (mass); the synthetic method of the invention adopts an effective compound catalyst to provide a synthetic scheme which has higher one way conversion rate and is economically practical in industry for the synthesis of the p-trifluoromethylaniline; the price of the catalyst used in the synthetic process is lower; furthermore, an organic solvent and the phase transfer catalyst can be recycled and reused; the manufacture cost is low; no waste water is discharged during the whole technique process; and the synthetic method of the invention is friendly to the environment.

Description

technical field [0001] The invention belongs to the technical field of organic synthesis, in particular to a synthesis method of p-trifluoromethylaniline. Background technique [0002] p-Trifluoromethylaniline is one of the important fine chemical products, which can be used to synthesize a variety of pesticides. With the deepening of research on new varieties of pesticides, its application range is becoming wider and wider. The product is chlorinated to obtain 2,6-dichloro-p-aminotrifluorotoluene, which is an important pesticide intermediate and is used in the pesticide industry to synthesize insecticides fipronil (fipronil) and fluoramine cyprothrin, flunzafenuron, fungicide fluazinam, herbicide butaflurane, etc. Among them, due to the introduction of fluorine-containing groups into its structure, fipronil has many outstanding advantages such as high efficiency, low toxicity, and low residue. [0003] There are many synthetic methods of p-trifluoromethylaniline, and ther...

Claims

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Application Information

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IPC IPC(8): C07C211/52C07C209/10B01J27/12B01J27/10
CPCY02P20/584
Inventor 任建纲宋芬倪平李忠王恩来
Owner 太仓中化环保化工有限公司
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