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Synthesis method of bis(di-n-butylamine) disulfide

A technology of bis-di-n-butylamine disulfide and di-n-butylamine, which is applied in the field of continuous synthesis of bis-di-n-butylamine disulfide, can solve the problems of many by-products, high cost, severe reaction heat release, etc., and achieve cost reduction , The heat release speed slows down and the effect of reducing the amount of feeding

Active Publication Date: 2020-05-12
湖南海利常德农药化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

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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Comparison scheme
Effect test

Embodiment 1

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

[0028] (1) The n-hexane solution of di-n-butylamine is prepared, and the mass fraction of di-n-butylamine is 20wt.%. The n-hexane solution of sulfur monochloride was prepared, and the mass fraction of sulfur monochloride was 20wt.%. With the n-hexane solution of di-n-butylamine and the n-hexane solution of sulfur monochloride respectively with the flow rate of 2.89g / min, 1.53g / min, namely according to the mol 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 to initiate the reaction, and the reaction temperature is 40 ° C. In the process of passing through the reaction channel of the first reactor, di-n-butylamine and sulfur monochloride are partially generated. After the reaction is carried out, a reaction mixture is obtained, and the reacti...

Embodiment 2

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

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

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

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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PUM

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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) respectively introducing an organic solution of di-n-butylamine and an organic solution of sulfur monochloride into a first reactor containing a reaction channel, mixing to initiate a reaction, and carrying out a partial reaction in the reaction channel of the firstreactor to obtain a reaction mixed solution; and (2) continuously introducing the reaction mixed solution into a second reactor containing a reaction channel, introducing a sodium hydroxide solutioninto the second reactor, and fully reacting to obtain bis(di-n-butylamine) disulfide. The continuous synthesis method improves the yield of bis(di-n-butylamine) disulfide, reduces the generation of byproducts, reduces the feeding amount of sulfur monochloride and sodium hydroxide, can greatly slow down the reaction heat release speed, and has the advantages of simple process flow, high productionefficiency, low cost, high safety and the like.

Description

technical field [0001] The invention belongs to the technical field of preparation of fine chemical products, and relates to a method for synthesizing an important intermediate of carbosulfan butylsulfide, in particular to a method for continuous synthesis of bis-n-butylamine disulfide. Background technique [0002] Di-n-butylamine disulfide is an important intermediate of carbosulfur-containing sulfur-containing derivative carbosulfan. At present, di-n-butylamine and sulfur monochloride are mainly used in industry to carry out the process 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 violently exothermic, and the reaction is usually performed at a lower temperature (<10 °C) in industry, and the process safety is ensured by controlling the temperature of the cooling medium and the dropping rate; ( 2) There are many by-products. There a...

Claims

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Application Information

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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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