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Preparation method of 2-methyl-3-methoxybenzoic acid

A technology of methoxybenzoic acid and hydroxybenzoic acid, which is applied in the field of compound preparation, can solve the problems of long reaction time, increased energy consumption, and high risk factor, and achieves the effects of determining the feasibility of the solution, simplifying the production process, and reducing the production cost.

Pending Publication Date: 2022-04-19
山东友道化学有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] CN107778167A discloses taking 2,6-dichlorotoluene as raw material to obtain the method for 2-methyl-3-methoxybenzoic acid through two-step reaction, the purity of the 2-methyl-3-methoxybenzoic acid that obtains is the highest can It can reach 99.6%, but the reaction time of the first step in the disclosed two-step reaction is as long as ten hours and involves the treatment of copper salt and rectification and recovery of the solvent. The second step reaction conditions are harsh and the reaction time is longer. For industrial production, there are problems of low production efficiency and high equipment input costs
CN111018693A discloses a kind of reaction with solid sodium methylate, dimethyl sulfoxide and 2,6-dichlorotoluene, drips methyl substituting agent, makes intermediate 2-methyl-3-chloroanisole, and then React with toluene, tetrahydrofuran and magnesium chips, and pass in carbon dioxide gas to prepare 2-methyl-3-methoxybenzoic acid, with a yield of about 88% and a purity of up to 99.6%, but the synthesis process is complex and involves many Sub-distillation, the process takes a long time, the production efficiency is low, and the energy consumption is high
CN106946685A discloses a method for preparing 2-methyl-3-methoxybenzoic acid using 3-chloro-o-xylene as a starting material through oxidation and alkylation. The purity of the product can reach up to 99%. However, the first step of oxidation involves the recovery and reuse of catalysts and the rectification and recovery of solvents, and the risk factor of oxygen oxidation is high. The second step of alkylation involves the treatment of copper salts and the rectification and recovery of solvents. The process is complicated. , high energy consumption
[0004] Although the above-mentioned patent applications can all obtain 2-methyl-3-methoxybenzoic acid of higher purity, due to the complex process flow, high energy consumption, low production efficiency and other shortcomings, industrialized production cannot be realized. Currently, the commonly used industrialized The method used in the production is to produce 2-methyl-3-methoxybenzoic acid by hydroxylation and hydrolysis of 2-methyl-3-hydroxybenzoic acid as raw material. In "Synthesis of Methoxyfenozide" The method for preparing 2-methyl-3-methoxybenzoic acid by alkylation and hydrolysis of 2-methyl-3-methoxybenzoic acid is mentioned in , and 7.9g (0.05mol) 3-hydroxyl -2-Methylbenzoic acid and 13.4g (0.1mol) 30% sodium hydroxide solution, stirred for 0.5h, then 15.8g (0.125mol) dimethyl sulfate was added dropwise, while 6.7g (0.05mol) 30% Sodium hydroxide solution, control the drop rate, keep the alkaline system, and the reaction temperature is 40-45 ° C. After the dropwise addition, keep the temperature for 1h, then add 6.7g (0.05mol) 30% sodium hydroxide solution to the system, and heat up to 60°C, stir for 0.5h, cool to room temperature, add dropwise an appropriate amount of hydrochloric acid, adjust pH = 1-2, then cool to 5-10°C, keep stirring for 0.5h, filter, wash the filter cake twice with cold water, and dry to obtain a solid Product 3-methoxy-2-methylbenzoic acid 8.3g, HPLC purity 96.1%, yield 96.1%
[0005] The above-mentioned 2-methyl-3-hydroxybenzoic acid is used as a raw material, and dimethyl sulfate is an alkylating agent, and the method for preparing 2-methyl-3-methoxybenzoic acid through alkylation hydrolysis is widely used in industry. Products with higher purity cannot be directly obtained, and further purification through recrystallization and other post-treatment processes is required. Even simple recrystallization as a post-treatment method still cannot obtain products with a purity that meets the requirements. Solvents also increase energy consumption

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  • Preparation method of 2-methyl-3-methoxybenzoic acid

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Effect test

Embodiment 1

[0077] The present embodiment provides a method for preparing 2-methyl-3-hydroxybenzoic acid.

[0078] (1) Raw material 2-methyl-3-hydroxybenzoic acid and 20% sodium hydroxide solution was prepared in a compound kettle in accordance with the molar ratio of 2-methyl-3-hydroxybenzoic acid and sodium hydroxide of 1:2.5 to obtain a sodium phenolic solution;

[0079] (2) The sodium phenolic solution is transported by the first feed pump at a flow rate of 18.17kg / min to the microchannel reactor with a holding liquid capacity of 1L and the dimethyl sulfate conveyed by the second feed pump is reacted in contact with the microchannel reactor at a temperature of 50 ° C to form an alkylation reaction liquid, wherein the molar ratio of raw materials to dimethyl sulfate is 1:2.4, the alkylation reaction solution stays in the microchannel reactor for 3 seconds and then transfers to the aging reactor, while the same molar amount of 20% sodium hydroxide solution with the raw material is 4.57kg / T...

Embodiment 2

[0083] The present embodiment provides a method for preparing 2-methyl-3-hydroxybenzoic acid.

[0084] (1) The raw material 2-methyl-3-hydroxybenzoic acid is added to the ingredient kettle, and the water is stirred to add 30% sodium hydroxide solution to form a sodium phenolic solution, of which the molar ratio of raw material to sodium hydroxide is 1:4, and the mass ratio of sodium hydroxide to water is 20:100;

[0085] (2) The sodium phenolic solution is transported by the first feed pump at a flow rate of 26.53kg / min to the microchannel reactor with a holding liquid capacity of 5L and the dimethyl sulfate transported by the second feed pump is in contact with the reaction at a temperature of 55 ° C in the microchannel reactor to form an alkylation reaction liquid, wherein the molar ratio of raw materials to dimethyl sulfate is 1:2.5, and the alkylation reaction liquid stays in the microchannel reactor for 10 seconds and then transfers to the aging reactor, and is further aged f...

Embodiment 3

[0089] The present embodiment provides a method for preparing 2-methyl-3-hydroxybenzoic acid.

[0090] (1) Raw material 2-methyl-3-hydroxybenzoic acid and 20% sodium hydroxide solution in accordance with the molar ratio of 2-methyl 3-hydroxybenzoic acid and sodium hydroxide is 1:5 to form a sodium phenol solution;

[0091] (2) The sodium phenolic solution is transported by the first feed pump at a flow rate of 32.1kg / min to the microchannel reactor with a liquid holding capacity of 40L and the dimethyl sulfate transported by the second feed pump is reacted in contact with the microchannel reactor at a temperature of 60 ° C to form an alkylation reaction solution, wherein the molar ratio of raw materials to dimethyl sulfate is 1:2.2, and the alkylation reaction solution stays in the microchannel reactor for 120s;

[0092] (3) The alkyl reaction solution flows into the hydrolysis reaction unit of the hydrolysis reaction unit through the pipeline, and the 30% sodium hydroxide solutio...

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Abstract

The invention relates to a preparation method of 2-methyl-3-methoxybenzoic acid, which comprises the following steps: (1) respectively feeding a sodium phenolate solution formed by 2-methyl-3-hydroxybenzoic acid, sodium hydroxide and water and dimethyl sulfate into an alkylation reaction unit through different conveying units, and carrying out alkylation reaction at 50-90 DEG C, an alkylation reaction solution is obtained; and (2) an alkylation reaction liquid flowing out of the alkylation reaction unit enters a hydrolysis reaction unit for a hydrolysis reaction, and a hydrolysate containing 2-methyl-3-methoxybenzoic acid sodium is obtained. According to the preparation method carried out in the continuous production device, the production process is simplified, refining steps such as recrystallization are avoided, the production cost is reduced, and the scheme is actually feasible after industrial production application, and the preparation method can be applied to industrial continuous production.

Description

Technical field [0001] The present disclosure relates to the field of compound preparation techniques, in particular to a method of preparing 2- methyl-3-methoxybenzoic acid. Background [0002] 2-Methyl-3-methoxybenzoic acid is an important intermediate in pharmaceutical and pesticide chemicals, especially the key intermediate of methoxenylhydrazide, and the minimum content standard for this product is currently available at 98.5%, and the content standard for most enterprises is 99%. [0003] CN107778167A discloses a method of obtaining 2-methyl-3-methoxybenzoic acid by a two-step reaction of 2,6-dichlorotoluene as raw material, The purity of the obtained 2-methyl-3-methoxybenzoic acid can reach up to 99.6%, but the first step of the disclosed two-step reaction has a reaction time of up to ten hours and involves the treatment of copper salts and the distillation recovery of solvents, the second step reaction conditions are harsh and the reaction time is long, if used for indus...

Claims

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Application Information

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IPC IPC(8): C07C51/41C07C51/02C07C65/21C07C67/10C07C69/92C07C65/03
CPCC07C51/412C07C51/02C07C67/10C07C65/03C07C69/92C07C65/21
Inventor 王兵杨宝玉王玉杰郭秋雨张萍李日翔
Owner 山东友道化学有限公司
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