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Method for preparing 2,5-dimethoxy-4-chloroaniline by hydrogenation reduction

A dimethoxy, chloroaniline technology, applied in chemical instruments and methods, preparation of organic compounds, preparation of aminohydroxy compounds, etc., can solve the problems of difficult quality assurance, high price, poor reaction selectivity, etc., and achieves energy reduction. The effect of waste, reducing production cost and reducing environmental pollution

Inactive Publication Date: 2012-02-08
河北彩客新材料科技股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The hydrogenation process of Raney nickel is often used to passivate the activity of the catalyst by adding dehalogenation inhibitors. The disadvantage of this method is that the introduction of additives cannot effectively prevent the loss of halogens, and the reaction selectivity is relatively poor; Without additives, the product often needs to be post-treated to improve the purity, the production cost is high, and the quality is difficult to guarantee
The hydrogenation process using Pt / C, due to the high price of Pt / C catalyst, makes the product cost too high to participate in the market competition

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Add 600Kg of 2,5-dimethoxy-4-chloronitrobenzene and methanol three times the weight of the nitro substance into a 1000ml stirred tank, and stir at room temperature for beating. The material in the beating kettle is pumped into a 5000ml reaction kettle, 90Kg of Raney nickel catalyst is added in the beating kettle, and the lid of the kettle is sealed.

[0019] Replace the reactor with a nitrogen atmosphere, feed hydrogen to 1.2 MPa, raise the temperature to 200°C, and maintain this condition for about 40 minutes to react. The hydrogen mass flow meter shows that the cumulative flow rate reaches 2 / 3 of the theoretical total hydrogen consumption, and stop the hydrogen flow. , reduce the reaction temperature to 50°C, and reduce the hydrogen pressure to about 0.8Mpa, continue to feed hydrogen, and maintain the reaction conditions until the pressure no longer drops.

[0020] Filter the reaction solution into the analysis tank, add ice water, and wait for the temperature of the ...

Embodiment 2

[0022] Add 560Kg of 2,5-dimethoxy-4-chloronitrobenzene and 20 times the weight of ethanol into a 15000ml stirring reactor, and stir at normal temperature for beating. The material in the beating kettle is pumped into the reaction kettle of 15000ml, and 2.8Kg Pd / C catalyst is added in the beating kettle, and the still cover is sealed.

[0023] Replace the reactor with a nitrogen atmosphere, feed hydrogen to 2.0MPa, raise the temperature to 120°C, and maintain this condition for about 50 minutes. The hydrogen mass flow meter shows that the cumulative flow rate reaches 2 / 3 of the theoretical total hydrogen consumption. Reaction temperature to 80°C, and reduce the pressure of hydrogen to about 0.3Mpa, continue to feed hydrogen, maintain the reaction conditions until the pressure no longer drops.

[0024] Filter the reaction solution into the analysis tank, add ice water, and wait for the temperature of the analysis tank to drop to about 10°C to obtain the product through plate and...

Embodiment 3

[0026] Add 300Kg of 2,5-dimethoxy-4-chloronitrobenzene and 8 times the weight of toluene into a 5000ml stirred reactor, and stir at normal temperature for beating. The material in the beating kettle is pumped into the reaction kettle of 5000ml, and the palladium-carbon catalyst is added in the beating kettle, and the still lid is sealed.

[0027] Replace the reactor with a nitrogen atmosphere, feed hydrogen to 1.5MPa, raise the temperature to 180°C, and maintain this condition for about 40 minutes. When the hydrogen mass flowmeter shows that the cumulative flow rate reaches 2 / 3 of the theoretical total hydrogen consumption, reduce the reaction temperature to 50°C, then reduce the hydrogen pressure to about 0.3Mpa, continue to feed hydrogen, and maintain this reaction condition until the pressure no longer drops .

[0028] Filter the reaction solution into the analysis tank, add ice water, and wait for the temperature of the analysis tank to drop to about 10°C to obtain the pr...

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PUM

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Abstract

The invention provides a method for preparing 2,5-dimethoxy-4-chloroaniline by hydrogenation reduction, which comprises the following steps: (1) beating and dissolving a raw material of 2,5-dimethoxy-4-chloro nitrobenzene; (2) adding a catalyst and the material into a hydrogenation reactor, performing a relatively high temperature high pressure hydrogenation reaction in the early stage of the reaction; (3) transferring the material in the reaction of step (2) into a relatively low temperature low pressure reaction state; (4) after the reaction is complete, filtering the catalyst; (5) cooling and precipitating the material; (6) performing pressure filtration and precipitating the material to obtain the product. In the invention, the reduction process of 2,5-dimethoxy-4-chloroaniline is controlled to have two stages of a high temperature high pressure stage and a low temperature low pressure stage, which effectively controlled the dechlorination reaction, and realizes the selective reduction of nitro groups. Hydrogen reduction is adopted instead of iron powder reduction, which avoids the generation of a lot of iron mud, and reduces environment pollution.

Description

technical field [0001] The invention relates to a method for preparing haloaniline through hydrogenation reduction of halogenated nitrobenzene, in particular to a method for preparing 2,5-dimethoxy-4-chloroaniline through hydrogenation reduction. Background technique [0002] As an important chloroaniline, 2,5-dimethoxy-4-chloroaniline is an important organic pigment intermediate, which can be used to prepare permanent yellow HR (dye index number C.I.Pigment Yellow83 (21108)) And permanent peach red FBB-B (dye index number C.I.Pigment Red 146 (12485)), used for advanced ink and plastic products. At present, the industrial production of 2,5-dimethoxy-4-chloroaniline in the world adopts iron powder reduction process, which has high energy consumption, large amount of waste water, and activated carbon decolorization of the product. The process route Long, the production process is cumbersome, and a large amount of iron sludge is produced, which causes serious pollution to the ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C217/84C07C213/02
Inventor 崔来友刘江宁何树明刘静艳赵清涛于万朋晋平
Owner 河北彩客新材料科技股份有限公司
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