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Method for preparing 1-naphthylamine from 1-nitronaphthalene

A nitronaphthalene and nitronaphthalene catalyzed technology, which is applied in the preparation of amino compounds, chemical instruments and methods, and the preparation of organic compounds, can solve the problems of large amount of reaction by-products, inability to store, and changes in catalytic activity, and achieve simplification Production technology, the effect of obvious cost advantages

Inactive Publication Date: 2009-05-20
甘肃中科药源生物工程股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] 1) Very inconvenient to use
Because the active component of the Raney nickel catalyst for catalytic hydrogenation is skeleton nickel, but skeleton nickel is extremely easy to catch fire in the air and cannot be preserved. It can only be used as a commodity in the form of nickel-aluminum alloy powder. Dissolve the aluminum, wash it and add it to the reaction system under the condition of isolating the air; in addition, the catalytic activity of Raney nickel often changes greatly due to different treatment conditions (such as alkali dissolution and washing conditions)
[0004]2) When Raney nickel catalyst is used, the amount of by-products of the reaction is large and the product yield is low
The hydrogenation of the Raney nickel catalyst to transform the nitro group into an amino group often requires a higher temperature, generally the required temperature is higher than 100 ° C, and the product amino compound generated by hydrogenation is easy to generate by-products at a temperature higher than 100 ° C ( It is called tar in the industry, which reduces the yield of the product on the one hand, and may also affect the normal progress of the reaction on the other hand.
[0005]3) Catalyst consumption is high
Due to the low catalytic activity of Raney nickel, the amount of catalyst that needs to be added is relatively large. On the other hand, because the recovery of the catalyst is extremely difficult, the consumption of the catalyst is too large, resulting in high production costs.
[0006]4) There are huge potential safety hazards in production
Because Raney nickel is easy to catch fire when it sees air, a fire will occur if there is a little carelessness in operation; at the same time, there is hydrogen in the hydrogenation workshop, which is very easy to explode

Method used

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Embodiment

[0012] Embodiment: the method for preparing 1-naphthylamine by catalytic hydrogenation of 1-nitronaphthalene

[0013] First add 100 grams of 1-nitrobenzene in the reaction kettle, then add ethanol with a concentration of 95% of 20% of the mass of 1-nitrobenzene, and then add a supported catalyst of 3 to 6% of the mass of 1-nitronaphthalene , close the reaction kettle, completely replace the air in the reaction kettle with hydrogen, then keep the inside of the kettle at normal pressure (about 0.1MPa), and start heating and stirring. After the temperature reaches 60°C, hydrogen is introduced into the kettle to keep the pressure inside the kettle until 1.0 ~ 3.0MPa (the test shows that the optimum pressure should be about 1.5MPa), start the hydrogenation reaction, during the hydrogenation process, the temperature in the kettle is kept in the range of 60 ~ 90 ° C, and the conversion rate is about 3 to 8 hours after the hydrogenation Promptly reach 95~99%, then separate reaction mi...

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Abstract

The invention discloses a method for preparing 1-naphthylamine by using 1-nitro-naphthalene. The method is that the 1-nitrobenzene is added into a kettle firstly and then ethanol and a supported catalyst are added; the kettle is closed and air in the kettle is displaced by using hydrogen; then normal pressure is maintained in the kettle and heating and mixing are carried out; the hydrogen is introduced into the kettle after temperature in the kettle reaches 60 DEG C so as to lead the pressure in the kettle to be maintained at 1.0 MPa to 3.0 MPa and then hydrogenation reaction is started; a conversion ratio can reach 95 percent to 99 percent after the hydrogenation for about 3 hours to 8 hours and then a reacted mixture and the catalyst are separated out; the catalyst separated is returned to the kettle for continuous use to supplement the lost catalyst; reaction product separation is carried out to the reacted mixture which is a clear solution so as to obtain the 1-naphthylamine.

Description

technical field [0001] The invention relates to a method for preparing 1-naphthylamine from 1-nitronaphthalene. Background technique [0002] The reduction of nitro compounds to amino compounds was first prepared by the method of iron powder and hydrochloric acid. This method is seriously polluting, and it is a process route that will be abolished in the near future as stipulated by the state. In recent years, most of this kind of production uses Raney nickel catalysts. , that is, the conversion of nitro to amino groups is realized by catalytic hydrogenation using Raney nickel as a catalyst, but the use of Raney nickel catalysts for catalytic hydrogenation has the following disadvantages: [0003] 1) It is extremely inconvenient to use. Because the active component of the Raney nickel catalyst for catalytic hydrogenation is skeleton nickel, but skeleton nickel is extremely easy to catch fire in the air and cannot be stored. It can only be used as a commodity in the form of ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C211/58C07C209/36
Inventor 马建泰常青
Owner 甘肃中科药源生物工程股份有限公司
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