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High-yield production process for 1,3-diphenyl propanedione compound

A technology for the production of diphenylpropanedione, which is applied in the separation/purification of carbonyl compounds, the preparation of carbon-based compounds, and the preparation of organic compounds. problems, to achieve the effect of strong market competitiveness, reduction of by-products and three wastes, and reduction of side reactions and impurities

Active Publication Date: 2019-02-05
ANHUI SHENGNUOBEI CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, sodium amide is prone to side reactions such as ammonolysis in the reaction process, and the product yield is low; sodium hydride and sodium react violently with water, and the safety hazard is very large in the production process, and the requirements for equipment are also high; and sodium amide and hydrogenation Sodium is expensive, the cost required for large-scale production is high, and there is no price advantage in the market
[0005] (2) Condensation of p-tert-butylbenzaldehyde and p-methoxyacetophenone under the action of sodium methoxide to generate 3-[4-tert-butylphenyl]-1-(4-methoxyphenyl)-2 -propene-1-one; then through halogen addition, sodium methoxide dehalogenation synthesis (Synthetic Chemistry, 2008,16(3):342-343; Eur.Pat.Appl.994092), the yield of this method is higher, but Bromine or chlorine gas is needed in the synthesis of this method, which not only requires high equipment, but also causes serious harm to people and the environment.
[0006] (3) Using p-tert-butylacetophenone and p-methoxybenzoyl chloride as raw materials, carry out acylation reaction to generate avobenzone (WO2006100225). In this method of synthesis, CuCl needs to be used as a catalyst, and the reaction time is up to 20h , post-processing is cumbersome, and more toxic reagents such as chloroform are needed
[0007] The above-mentioned methods all have their own advantages and disadvantages. Therefore, it is still necessary to continue to explore new synthetic methods to meet the industry's demand for high-quality, low-priced 1,3-diphenylpropanedione compounds

Method used

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  • High-yield production process for 1,3-diphenyl propanedione compound

Examples

Experimental program
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Effect test

Embodiment 1

[0086] Add 800g toluene (toluene), 24g sodium methylate, 6g 32% liquid potassium methylate solution and 80g p-tert-butylbenzoic acid methylate Esters, fractionate methanol while raising the temperature until the temperature of the kettle reaches 105-108°C;

[0087] Start to drop the mixed solution composed of 60g p-methoxyacetophenone and 80g toluene, and at the same time fractionate the methanol produced by reaction from the top of the rectifying column to keep the temperature of the kettle at 105-108°C, and the dropping time is controlled at 1.5h. After the dropwise addition is completed, keep the reaction for 2 hours. During the heat preservation process, the methanol by-product of the reaction is continuously fractionated from the top of the rectification column to maintain the temperature of the kettle at 105-108°C.

[0088] After the reaction was finished, add 120 g of 10 (weight) % dilute sulfuric acid aqueous solution, stir and wash and then separate the water layer, ...

Embodiment 2

[0092] Add 800g of toluene, 12g of sodium methoxide, and 80g of methyl p-tert-butylbenzoate in a reaction kettle with a rectification column (stacked θ-ring stainless steel filler, 20 theoretical plates), fractionate methanol while raising the temperature, and reach the temperature of the kettle. Reach 105~108℃;

[0093] Start to drop the mixed solution composed of 60g p-methoxyacetophenone and 80g toluene, and at the same time fractionate the methanol produced by reaction from the top of the rectifying column to keep the temperature of the kettle at 105-108°C, and the dropping time is controlled at After 1.5h, 6g32% liquid potassium methylate solution was added dropwise for 0.5h. After the dropwise addition is completed, add 12 g of sodium methoxide again, and keep the reaction for 2 hours. During the heat preservation process, the methanol by-product of the reaction is continuously fractionated from the top of the rectification column to maintain the temperature of the kettl...

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Abstract

The invention discloses a high-yield production process for a 1,3-diphenyl propanedione compound. The production process comprises the steps that a benzoate compound A, a catalyst and a solvent I areadded into a reaction kettle, then an acetophenone compound B is dropwise added into the reaction kettle at the set temperature for reaction, and after reaction, a final product is prepared through acidification, washing, desolvation and recrystallization. The production process has the characteristics that a mixed basic catalyst is adopted, compared with sodium methylate and a traditional process, the yield is increased by 10-15% and is greater than or equal to 85.0%, the production operation is easy, the environmental pollution is small, the product color is light, the distinctive aromatic odor is achieved, the quality is good, the market competitiveness is high, and the industrialization promotion is easy.

Description

technical field [0001] The invention relates to the field of fine chemicals, in particular to a production process for high-yield 1,3-diphenylpropanedione compounds. Background technique [0002] In recent years, the amount of ultraviolet radiation has been increasing with the destruction of the ozone layer. Among them, the near ultraviolet light of 320-400nm (UV-A for short) will cause radiation damage to the human body, induce gene mutation and cause skin cancer. In order to protect the human body from excessive ultraviolet radiation, ultraviolet absorbers with safe and efficient absorption of ultraviolet radiation are widely used in cosmetics, hair care products, fabric treatment and detergents. UV absorbers include known 1,3-diphenylpropanedione compounds such as butylmethoxydibenzoylmethane (Parsol 1789, avobenzone), which is a compound used exclusively in skin care cosmetics. An anti-UV-A ultraviolet light absorber, Parsol 1789 was originally developed and produced by...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C45/45C07C49/84C07C45/82C07C45/78
CPCC07C45/455C07C45/78C07C45/82C07C49/84
Inventor 刘启发王荣吴军杨健
Owner ANHUI SHENGNUOBEI CHEM TECH
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