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Process for preparing N,N-dimethyl-1,3-propane diamine through continuous method

A technology for the reaction of dimethylaminopropionitrile and dimethylaminopropionitrile, which is applied to the preparation of amino compounds, the preparation of organic compounds, chemical instruments and methods, etc., can solve the problems of low yield, achieve long life, less waste, Ease of continuous production

Active Publication Date: 2013-10-02
DALIAN UNIV OF TECH
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  • Abstract
  • Description
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Problems solved by technology

[0005] The second method (CN102026956A) is to obtain N,N,N',N'-substituted 1,3-propylenediamine by reacting acrolein and dimethylamine at 4°C, 0~3MPa, and the obtained mixture is mixed with ammonia gas N,N-dimethyl-1,3-propanediamine is reacted with hydrogen in the presence of a catalyst at 40-400°C and 6MPa, and the yield is about 91%. This method is green and environmentally friendly, but the yield is relatively low. The first method is low

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  • Process for preparing N,N-dimethyl-1,3-propane diamine through continuous method
  • Process for preparing N,N-dimethyl-1,3-propane diamine through continuous method
  • Process for preparing N,N-dimethyl-1,3-propane diamine through continuous method

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Abstract

The invention discloses a process for preparing N,N-dimethyl-1,3-propane diamine through a continuous method and belongs to the field of organic chemical industry. The process comprises the following steps: by taking dimethylamine and acrylonitrile as raw materials, continuously preparing dimethylamino propionitrile by employing a fixed bed, wherein the molar ratio of dimethylamine to acrylonitrile is (10:1)-(1:1), the reaction temperature is 10-120 DEG C, the air speed is 0.1-10h<-1>, and the conversion rate of the acrylonitrile and the selectivity of the dimethylamino propionitrile are over 99 percent; and allowing the obtained dimethylamino propionitrile intermediate to directly enter a second fixed bed reactor for hydrogenating without any purification treatment, wherein the hydrogenation pressure is 3-10 MPa, a Raney-Ni catalyst is used, an alcoholic solution promoter with 0.1-10 percent of alkali is matched, the air speed is 0.1-4h<-1>, and the yield of N,N-dimethyl-1,3-propane diamine is not lower than 93 percent. The process for preparing N,N-dimethyl-1,3-propane diamine is simple, stable in quality, energy-saving and environment-friendly and is suitable for large-scale production.

Description

technical field [0001] The invention belongs to the technical field of organic chemical industry and relates to a process for preparing N,N-dimethyl-1,3-propanediamine by continuous method Background technique [0002] N,N-Dimethyl-1,3-propanediamine belongs to lower aliphatic diamine and is an important chemical intermediate widely used in the preparation of detergents, surfactants, textiles, lubricating oil additives, gasoline additives, Preservatives, moisturizing agents, foaming agents, etc. With the advancement of science and technology and social development, the scope of application of DMAPA has also been expanding accordingly, and the market demand has also increased year by year. Therefore, N,N-dimethyl-1,3-propanediamine is a very potential organic chemical intermediate. [0003] There are two main methods for preparing N,N-dimethyl-1,3-propanediamine. The first one uses acrylonitrile and dimethylamine as raw materials to prepare N,N-dimethyl-1,3-propanediamine;...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C211/11C07C209/48
Inventor 孟庆伟邓朝芳都健李亚楠卿海
Owner DALIAN UNIV OF TECH
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