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Method for preparing o-phenylenediamine by catalytic hydrogenation of ortho-nitroaniline with supported nickel catalyst

A technology of o-nitroaniline and o-phenylenediamine, which is applied in the field of preparing o-phenylenediamine by catalyzing the hydrogenation of o-nitroaniline with a supported nickel catalyst, which can solve the problems of inability to preserve, large amount of reaction by-products, and low product yield and other issues, achieving obvious cost advantages and simplifying the production process

Inactive Publication Date: 2017-06-27
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 the 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 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 large
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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Examples

Experimental program
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Effect test

Embodiment

[0012] Embodiment: the method for preparing o-phenylenediamine from o-nitroaniline

[0013] First add 100 grams of o-nitroaniline to the reaction kettle, then add 95% ethanol with a concentration of 4 times the mass of o-nitroaniline, and then add a supported catalyst of 10 to 15% of the mass of o-nitroaniline, and seal the reaction Reactor, completely replace the air in the reactor with hydrogen, then keep the inside of the reactor at normal pressure (about 0.1MPa), and start heating and stirring. After the temperature reaches 60°C, put hydrogen into the reactor to keep the pressure inside the reactor at 1.0-3.0 MPa (the test shows that the optimum pressure should be about 1.5MPa), the hydrogenation reaction starts, and the temperature in the kettle is kept in the range of 70-95°C during the hydrogenation process, and the conversion rate reaches 88% after hydrogenation for about 0.5 to 1.5 hours. ~ 90%, then separate the reaction mixture and the catalyst, the separated cataly...

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Abstract

The invention relates to a method for preparing o-phenylenediamine by catalytic hydrogenation of ortho-nitroaniline with a supported nickel catalyst. The invention discloses a method for preparing o-phenylenediamine through catalytic hydrogenation of ortho-nitroaniline. The method comprises the following steps: firstly adding ortho-nitroaniline into a reaction kettle, then adding ethanol and a supported catalyst, sealing the reaction kettle, completely replacing the air in the reaction kettle with hydrogen, then maintaining the interior of the reaction kettle to be at normal pressure (0.1MPa), starting to heat and stir, introducing hydrogen into the reaction kettle after temperature reaches 60 DEG C, maintaining the pressure in the kettle to be 1.0-3.0MPa, and starting to carry out hydrogenation reaction, wherein conversion rate reaches more than 99% after hydrogenation is carried out for about 0.5-1.5 hours; then separating out a reaction mixture and a catalyst, returning the catalyst which is separated out to the reaction kettle to be continuously used, and supplementing the catalyst in amount of loss; and carrying out reaction product separation on the reaction mixture, namely clear liquid, so that the o-phenylenediamine is obtained.

Description

technical field [0001] The invention relates to a method for preparing o-phenylenediamine through catalytic hydrogenation of o-nitroaniline. 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) 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 comm...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C211/51C07C209/34B01J23/755
CPCC07C209/34B01J23/755B01J35/393B01J35/394B01J35/633B01J35/615C07C211/51
Inventor 常青
Owner 甘肃中科药源生物工程股份有限公司
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