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Production method of 3,5-di-tert-butyl-4-hydroxybenzoic acid

A technology of hydroxybenzoic acid and di-tert-butylphenol, which is applied in the direction of chemical instruments and methods, carboxylate preparation, carboxylate preparation, etc., can solve the problems of easy coking of products, increased cost, and difficult industrialization of the process, so as to avoid Effects of local overheating and coking, reducing equipment cost and increasing product yield

Active Publication Date: 2018-12-28
安徽新秀化学股份有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In the traditional process, the dry 2,6-di-tert-butylphenol alkali metal salt powder is reacted with carbon dioxide to prepare 3,5-di-tert-butyl-4-hydroxybenzoic acid. This process has many disadvantages: 2, The powder of 6-di-tert-butylphenol alkali metal salt is prone to spontaneous combustion and has a high risk; the gas-solid reaction requires special transmission equipment and a special gas-solid stirring paddle, and the equipment cost is high; the gas-solid reaction has poor heat transfer and the product The problem of easy coking, the product yield is low
However, phenolic compounds do not azeotrope with water, and an additional azeotropic dehydrating agent needs to be added when removing water, which increases the cost; phenolic compounds generally have higher viscosity, and the power cost is higher when the phenolic compound is used as a solvent for the reaction ; Excessive phenolic compounds are easily oxidized during recycling, resulting in a decline in the quality of phenolic compounds and an increase in cost
[0008] Patent CN1289760A once mentioned a process for synthesizing salicylic acid with octanol as a solvent. However, octanol has a high boiling point and needs to be carried out in a vacuum environment when preparing sodium phenate, which increases the cost of the process. At the same time, under vacuum environment The loss rate of octanol is also high; at the same time, Stanescu and Achenie mentioned in the article "An in-silico study of solvent effects on the Kolbe–Schmitt reaction using a DFT method", that the solvent in the Kolbe-Schmitt reaction The greater the polarity, the lower the conversion rate of the reaction, and the larger polarity of octanol makes the yield of salicylic acid prepared by this method not high
[0009] Wei Wanmao mentioned in the article "Research on the production process of 3,5-di-tert-butyl-4-hydroxybenzoic acid" that DMF was used as a solvent to carry out the Kolber-Schmidt reaction. However, DMF is miscible with water, making the follow-up treatment very difficult. Trouble; DMF is a nitrogen-containing solvent, which pollutes a lot and is not conducive to environmental protection
[0010] Patent EP0834494A reports a catalyst that can promote the reaction of NaOH and 2,6-di-tert-butylphenol: 1,3-dimethyl-2-imidazolinone, but 1,3-dimethyl-2-imidazole Phenones are expensive and difficult to recycle
[0011] Another part of the literature has reported that alkali metal salts of alcohols are used as reactants to synthesize alkali metal salts of phenolic substances, but the cost of alkali metal salts of alcohols is high, difficult to preserve, and the process is difficult to industrialize

Method used

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  • Production method of 3,5-di-tert-butyl-4-hydroxybenzoic acid

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Embodiment 1

[0048] Embodiment 1, a kind of preparation technology of 3,5-di-tert-butyl-4-hydroxybenzoic acid with toluene as solvent, carries out the following steps successively:

[0049] A. Add 412g 2,6-di-tert-butylphenol (2mol), 50% (mass) potassium hydroxide aqueous solution 235g (2.1mol KOH), toluene 920g (10mol) to the reaction kettle protected with nitrogen, and the reaction kettle There is a water separator with cold hydrazine on it, which is used to reflux toluene and discharge water. After reacting for 4 hours under nitrogen protection and reflux conditions, the reaction product is a suspension of potassium phenate and toluene;

[0050] B. After the potassium phenate preparation is completed, close the water-distributing equipment, feed dry carbon dioxide (that is, moisture content≤0.01%) in the kettle, and the pressure of carbon dioxide is 2.5MPa, and keep continuously feeding carbon dioxide in the kettle to Keep the pressure inside the kettle stable;

[0051] C. Heat the re...

Embodiment 2

[0055] Embodiment 2, a kind of preparation technology of 3,5-di-tert-butyl-4-hydroxybenzoic acid with toluene as solvent, carries out the following steps successively:

[0056] A. Add 618g 2,6-di-tert-butylphenol (3mol), 60% (mass) potassium hydroxide aqueous solution 309g (3.3mol KOH), toluene 2760g (30mol) to the reaction kettle protected by nitrogen, and the reaction kettle There is a water separator with cold hydrazine on it, which is used to reflux toluene and discharge water. After reacting for 3 hours under nitrogen protection and reflux conditions, the reaction product is a suspension of potassium phenate and toluene;

[0057] B. After the preparation of potassium phenolate is completed, close the water-distributing equipment, feed dry carbon dioxide into the kettle, the pressure of carbon dioxide is 1.5MPa, and keep feeding carbon dioxide continuously into the kettle to maintain the pressure stability in the kettle;

[0058] C. Heat the reactor to 100°C, react for 8 ...

Embodiment 3

[0062] Embodiment 3, a kind of preparation technology that takes toluene as solvent 3,5-di-tert-butyl-4-hydroxybenzoic acid, carries out the following steps successively:

[0063] A. Add 206g 2,6-di-tert-butylphenol (1mol), 147g (1.05mol KOH) of 40% (mass) potassium hydroxide aqueous solution, 736g (8mol) of toluene to the reactor that has been protected with nitrogen, and the reactor There is a water separator with cold hydrazine on it, which is used to reflux toluene and discharge water. After reacting for 2 hours under nitrogen protection and reflux conditions, the reaction product is a suspension of potassium phenate and toluene;

[0064] B. After the potassium phenol salt is prepared, close the water-distributing equipment, feed dry carbon dioxide into the kettle, the pressure of carbon dioxide is 2.0MPa, and keep feeding carbon dioxide into the kettle continuously to maintain the pressure stability in the kettle;

[0065] C. Heat the reactor to 120°C, react for 10 hours...

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Abstract

The invention discloses a production method of 3,5-di-tert-butyl-4-hydroxybenzoic acid. The production method sequentially comprises the steps as follows: 2,6-di-tert-butylphenol, a potassium hydroxide aqueous solution and toluene are added to a reactor under protection of nitrogen to be subjected to a reflux reaction under a water distribution condition; CO2 is introduced into the reactor until the pressure is 0.1-3.0 MPa, a Kolbe-Schmitt reaction is conducted under a pressure holding condition, after the reaction, corresponding aftertreatment is carried out, and a crude product of 3,5-di-tert-butyl-4-hydroxybenzoic acid is obtained. The method has short reaction time and high conversion rate, has obvious advantages as compared with traditional gas-solid processes and existing solvent-process synthesis processes and is suitable for further industrialization.

Description

technical field [0001] The invention relates to a novel process for producing 3,5-di-tert-butyl-4-hydroxybenzoic acid. Background technique [0002] 3,5-di-tert-butyl-4-hydroxyphenyl compound has anti-inflammatory, anti-virus and anti-tumor effects, and is an important pharmaceutical and chemical intermediate. 3,5-di-tert-butyl-4-hydroxybenzoic acid and its derivatives are also widely used antioxidants and ultraviolet absorbers, as well as intermediates for the synthesis of mosquito killers, and can also be used for the synthesis of 3 ,5-di-tert-butyl-4-hydroxybenzoic acid-2',4'-di-tert-butylphenyl ester and 3,5-di-tert-butyl-4-hydroxybenzoic acid n-hexadecyl, 3,5 -Di-tert-butyl-4-hydroxybenzoic acid n-octadecyl ester and other widely used antioxidants, light stabilizers and UV absorbers in the fields of plastics, rubber and photocurable coatings. [0003] The known production method of 3,5-di-tert-butyl-4-hydroxybenzoic acid is to react 2,6-di-tert-butylphenol with alkali...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C65/03C07C51/15C07C51/02C07C39/235C07C37/66
CPCC07C37/66C07C51/02C07C51/15C07C39/235C07C65/03
Inventor 钱超潘琦王轲吴春业张秀秀
Owner 安徽新秀化学股份有限公司
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