O-phenylenediamine medium-pressure catalytic hydrogenation process

A technology for o-phenylenediamine and catalytic hydrogenation, which is applied in the fields of organic chemistry, amino compound preparation, chemical instruments and methods, etc., can solve the problems of high production cost, serious environmental pollution, and difficult to treat waste water and residue, and achieves reduction of synthesis cost. , The effect of low reaction temperature and water pollution reduction

Inactive Publication Date: 2014-05-14
NANTONG BOTAO CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the production process of alkali sulfide reduction is simple, the product yield is low and the cost is high. In particular, a large amount of waste water and residue generated is difficult to handle, and the environmental pollution is quite serious. It will gradually face the trend of being eliminated in the future; catalytic hydrogenation to prepare o-phenylenediamine The advanced technology has the advantages of good product quality, high yield, and less "three wastes", but it needs to add expensive catalysts in the preparation process, which cannot be applied mechanically, and the production cost is high

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] Put o-nitroaniline 500g, water 1000ml, catalyst 5% palladium charcoal 2g into 3000ml autoclave respectively, close the autoclave, open nitrogen to replace the air mixed in the autoclave repeatedly. Repeat the above replacement with hydrogen for more than 5 times. After the replacement is completed, raise the temperature and heat to 90°C, control the temperature between 90 and 100°C, control the hydrogen pressure at 1.0Mpa, and react for 2 hours. Close the inlet valve, observe the heat release of the reaction and the drop of the hydrogen pressure. If the pressure does not drop and the temperature does not rise, it means that the reaction has been completed. Continue to keep the pressure and stir the reaction for 0.5 hours. After the reaction is completed, lower the temperature slightly, replace the hydrogen in the kettle with nitrogen, discharge the material while it is hot, filter out the catalyst and use it mechanically, cool the filtrate, and precipitate crystals. Phe...

Embodiment 2

[0015] Put o-nitroaniline 500g, water 1500ml, catalyst 5% palladium charcoal 10g into 3000ml autoclave respectively, close the autoclave, turn on the nitrogen gas to replace the mixed air in the autoclave repeatedly, each time it is required to reach 0.2Mpa, then vent, and replace repeatedly for 5 Repeat the above replacement with hydrogen for more than 5 times. After the replacement is completed, raise the temperature and heat to 90°C, control the temperature between 90 and 100°C, control the hydrogen pressure at 1.0Mpa, and react for 2 hours. Close the inlet valve, observe the heat release of the reaction and the drop of the hydrogen pressure. If the pressure does not drop and the temperature does not rise, it means that the reaction has been completed. Continue to keep the pressure and stir the reaction for 0.5 hours. After the reaction is completed, lower the temperature slightly, replace the hydrogen in the kettle with nitrogen, discharge the material while it is hot, filt...

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PUM

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Abstract

The invention discloses an o-phenylenediamine medium-pressure catalytic hydrogenation process which is characterized by comprising the following steps: adding ortho-nitroaniline as a raw material, water as a solvent and 5% of palladium-carbon as a catalyst into a pressure kettle, repeatedly replacing the air inside the kettle through nitrogen, subsequently emptying the kettle, further repeating the replacement by using hydrogen, after the replacement is accomplished, raising the temperature, heating, reacting for 2 hours, after the reaction is accomplished, keeping the pressure, reacting for 0.5 hour, after the reaction is accomplished, cooling down, replacing the hydrogen inside the kettle by using nitrogen, discharging the material in hot, filtering the catalyst for further application, cooling down the filtrate to separate out crystal, cooling down and filtering to obtain a product, namely, the o-phenylenediamine, refeeding the filtrate into a next batch for being used as process water for repeated circulation. The further application situation of the catalyst is good, the reaction temperature is low, the pressure is small, the synthesis cost is greatly lowered, and in addition the process water is repeatedly applied, and the wastewater is discharged for only once after the process water is applied for multiple times, so that the water pollution is greatly reduced.

Description

technical field [0001] The invention relates to a process for preparing o-phenylenediamine, in particular to a process for preparing o-phenylenediamine through medium-pressure catalytic hydrogenation. Background technique [0002] O-phenylenediamine is a white crystalline solid. It is an important fine chemical intermediate. It is mainly used as a pesticide intermediate. It is the raw material for carbendazim and thiophanate-methyl. It is also a dye intermediate for the production of cationic dyes and Vat dyes can also be used to produce rubber antioxidants, fur dyes, developers and surfactants. [0003] At present, there are many industrial synthesis methods of o-phenylenediamine, and there are many synthetic routes and methods: mainly including alkali sulfide reduction and catalytic hydrogenation. Although the production process of alkali sulfide reduction is simple, the product yield is low and the cost is high. In particular, the large amount of waste water and residue ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C211/51C07C209/36
Inventor 黄海波黄海涛黄奎生王宏李桂萍黄雪平
Owner NANTONG BOTAO CHEM
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