The synthetic method of two di-n-butylamine disulfide

A di-n-butylamine and synthesis method technology, applied in the direction of organic chemistry, can solve the problems of severe reaction exotherm, many by-products, high cost, etc., and achieve the effects of reducing the amount of feed, reducing the cost, and slowing down the exothermic speed

Active Publication Date: 2021-12-17
湖南海利常德农药化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this commonly used synthesis method has the following defects: (1) The reaction is exothermic violently, and the industry usually reacts at a lower temperature (<10°C), and the process safety is ensured by controlling the temperature of the cooling medium and the rate of addition; ( 2) There are many by-products, there are organic phase and water phase in the reaction solution, sulfur monochloride will be partially decomposed when it meets water, and by-products such as sulfur, sulfur dioxide (sulfurous acid), and hydrogen sulfide will be generated; (3) Based on making dinormal In consideration of the complete conversion of butylamine, an excess of 5% to 6% of sulfur monochloride is used in industry, and an excess of 10% to 30% of acid is applied, which is very costly

Method used

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Effect test

Embodiment 1

[0027] A kind of synthetic method of two di-n-butylamine disulfide of the present invention, comprises the following steps:

[0028] (1) Prepare a n-hexane solution of di-n-butylamine, the mass fraction of di-n-butylamine is 20wt.%. A n-hexane solution of sulfur monochloride is configured, and the mass fraction of sulfur monochloride is 20wt.%. The n-hexane solution of di-n-butylamine and the n-hexane solution of sulfur monochloride are respectively at the flow rates of 2.89g / min and 1.53g / min, that is, according to the molar ratio of sulfur monochloride / di-n-butylamine in the same time period The ratio of 0.5 is passed into the first reactor containing the reaction channel for high-speed mixing and initiation reaction. The reaction temperature is 40 ° C. During the process of passing through the reaction channel of the first reactor, di-n-butylamine and sulfur monochloride partly generate After the reaction, a reaction mixture solution is obtained, which contains bis-di-n-bu...

Embodiment 2

[0033] A kind of synthetic method of two di-n-butylamine disulfide of the present invention, comprises the following steps:

[0034] (1) Put the n-hexane solution of di-n-butylamine and the n-hexane solution of sulfur monochloride at the flow rates of 1.16g / min and 0.62g / min respectively, that is, the molar ratio of sulfur monochloride / di-n-butylamine is 0.51 Pass it into the first reactor for high-speed mixing and initiation reaction. The temperature of the reaction system is 30°C. Di-n-butylamine and sulfur monochloride partially react during the process of passing through the reaction channel of the first reactor to obtain a reaction mixture , the reaction mixture contains two di-n-butylamine disulfide, di-n-butylamine hydrochloride and sulfur monochloride.

[0035] (2) The reaction mixture obtained in step (1) is continuously passed into the second reactor, and at the same time, the sodium hydroxide solution with a flow rate of 1.78g / min is passed into the second reactor, ...

Embodiment 3

[0040] A kind of synthetic method of two di-n-butylamine disulfide of the present invention, comprises the following steps:

[0041] (1) Put the n-hexane solution of di-n-butylamine and the n-hexane solution of sulfur monochloride at the flow rates of 1.16g / min and 0.62g / min respectively, that is, the molar ratio of sulfur monochloride / di-n-butylamine is 0.51 Pass it into the first reactor for rapid mixing and initiation reaction. The temperature of the reaction system is 50°C. Di-n-butylamine and sulfur monochloride partially react during the process of passing through the reaction channel of the first reactor to obtain a reaction mixture , the reaction mixture contains two di-n-butylamine disulfide, di-n-butylamine hydrochloride and sulfur monochloride.

[0042] (2) The reaction mixture obtained in step (1) is continuously passed into the second reactor, and at the same time, the sodium hydroxide solution with a flow rate of 0.93g / min is passed into the second reactor, that ...

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Abstract

The invention discloses a synthesis method of bis-di-n-butylamine disulfide. The synthesis method comprises the following steps: (1) passing the organic solution of di-n-butylamine and the organic solution of sulfur monochloride into the reaction channel respectively The reaction is mixed and initiated in the first reactor, and a reaction mixture is obtained after a partial reaction occurs through the reaction channel of the first reactor; (2) The reaction mixture is continuously passed into the second reactor containing the reaction channel, and Sodium hydroxide solution is passed into the second reactor, and bis-di-n-butylamine disulfide is obtained after sufficient reaction. The continuous synthesis method of the present invention improves the yield of bis-di-n-butylamine disulfide, reduces the generation of by-products, reduces the feeding amount of sulfur monochloride and sodium hydroxide, and can greatly slow down the exothermic speed of reaction. It has the advantages of simple process, high production efficiency, low cost and high safety.

Description

technical field [0001] The invention belongs to the technical field of preparation of fine chemical products, and relates to a synthesis method of an important intermediate of carbosulfan, in particular to a continuous synthesis method of bis-di-n-butylamine disulfide. Background technique [0002] Bis-di-n-butylamine disulfide is an important intermediate of carbofuran’s sulfur-containing derivative carbosulfan. At present, the industry mainly uses di-n-butylamine and sulfur monochloride under the action of acid-binding agent sodium hydroxide. Low temperature batch preparation. However, this commonly used synthesis method has the following defects: (1) The reaction is exothermic violently, and the industry usually reacts at a lower temperature (<10°C), and the process safety is ensured by controlling the temperature of the cooling medium and the rate of addition; ( 2) There are many by-products, there are organic phase and water phase in the reaction solution, sulfur mo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C381/00
CPCC07C381/00
Inventor 刘源欧阳宇迪高恒旭兰世林陈郭芹程超杜升华
Owner 湖南海利常德农药化工有限公司
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