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Novel process for synthesizing 2-cyano-4-nitrochlorobenzene through continuous nitration by solvent method

A technology of nitrochlorobenzene and solvent method, applied in the field of chemical production, can solve the problems of inability to realize continuous reaction, high safety risk level, affecting conversion rate, etc., to reduce reaction safety risk, facilitate reaction temperature control, and reduce waste water. The effect of emissions

Pending Publication Date: 2021-10-08
河北嘉泰化工科技有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This process has two major disadvantages: 1. The amount of waste acid produced is large. Every ton of 2-cyano-4-nitro-chlorinated benzene product produces 10 tons of 40% waste acid. This waste acid not only pollutes the environment, but also costs High, the cost of waste acid treatment accounts for 25% of the total cost of 2-cyano-4-nitrochlorobenzene products; 2. The nitration reaction is an exothermic reaction with a fast reaction rate, and poor temperature control will not only generate many nitro By-products such as substances and oxidation affect the conversion rate, and are likely to cause safety issues such as explosions
Therefore, intermittent nitration reaction is adopted, and there are many reaction materials, so it is not conducive to temperature control, and the safety risk is relatively large.
[0003] Chinese patent 2-cyano-4-nitroaniline new process for separation of nitrates in the production (application number: 201610251355.7), the patent uses the traditional process for nitration reaction, after the nitration reaction, the product is extracted to separate the product from the acid solution, Acid solution reuse. Although the patent can realize acid solution reuse, it still uses the traditional nitration reaction. On the one hand, continuous reaction cannot be realized, and the safety risk level is still high. On the other hand, sulfuric acid is still used to dissolve o-chlorobenzonitrile, and The introduction of water into the system reduces the acid concentration, and a large amount of acid still needs to be replenished in the process of acid reuse, so the reduction of acid is limited

Method used

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  • Novel process for synthesizing 2-cyano-4-nitrochlorobenzene through continuous nitration by solvent method

Examples

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Effect test

Embodiment 1

[0050] Get 500g of o-chlorobenzonitrile, dissolve it with 2000g of carbon tetrachloride, configure a benzonitrile solution with a mass content of 20%, configure a mixed acid nitrating agent with 98% sulfuric acid of 123g and 245.5g of 98% nitric acid, the sulfuric acid in the mixed acid nitrating agent The mass ratio of addition amount and nitric acid addition amount is 0.5:1, and benzonitrile solution and mixed acid nitrating agent are carried out nitration reaction in pipeline reactor, and the mass ratio of mixed acid nitrating agent and benzonitrile solution is 0.15:1, and reaction liquid reflux is 2 times that of the nitrating solution, the reaction temperature is controlled at 30°C, and the reaction residence time is 20min. Water and chlorobenzene are added to the nitrating solution, and the phases are separated after mixing evenly. The organic phase after the phase separation is evaporated to recover 99% tetrachloride Carbon, used again for dissolving o-chlorobenzonitrile...

Embodiment 2

[0053] Get 500g of o-chlorobenzonitrile, dissolve it with 750g of 2-methyltetrahydrofuran, configure a mass content of 40% benzonitrile solution, configure a mixed acid nitrating agent with oleum of 467.5g and 98% nitric acid of 234g, in the mixed acid nitrating agent The mass ratio of sulfuric acid addition and nitric acid addition is 2:1, and benzonitrile solution and mixed acid nitrating agent are carried out nitration reaction in microchannel reactor, and the mass ratio of mixed acid nitrating agent and benzonitrile solution is 0.56:1, and reaction liquid The reflux rate is 30 times that of the nitration solution, the reaction temperature is controlled at 0°C, and the reaction residence time is 20 minutes. Water and nitrobenzene are added to the nitration solution, and the phases are separated in a phase separator. The organic phase after phase separation is evaporated and recovered for 99 % of 2-methyltetrahydrofuran is used to dissolve o-chlorobenzonitrile again, and the ...

Embodiment 3

[0056] Get 500g of o-chlorobenzonitrile, dissolve it with 1000g of ethylene dichloride, configure a benzonitrile solution with a mass content of 33%, configure a mixed acid nitrating agent with 386g of oleum and 257g of 98% nitric acid, add sulfuric acid to the mixed acid nitrating agent The mass ratio of amount and nitric acid addition amount is 1.5:1, and benzonitrile solution and mixed acid nitrating agent are carried out nitration reaction in microchannel reactor, and the mass ratio of mixed acid nitrating agent and benzonitrile solution is 0.43:1, and reaction solution reflux It is 14 times that of the nitration solution, the reaction temperature is controlled at 10°C, and the reaction residence time is 20 minutes. Water and o-dichlorobenzene are added to the nitration solution, and the phases are separated in a phase separator. The organic phase after phase separation is evaporated and recovered 99% Dichloroethane is used to dissolve o-chlorobenzonitrile again, and the ev...

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Abstract

The invention provides a novel process for synthesizing 2-cyano-4-nitrochlorobenzene through continuous nitration by a solvent method. The process comprises the following steps of: 1, preparation of a benzonitrile solution: dissolving o-chlorobenzonitrile by using an organic solvent to prepare a benzonitrilesolution for later use; 2, preparation of a mixed acid nitrating agent; 3, nitration reaction: respectively pumping the benzonitrile solution in the step 1 and the mixed acid nitrating agent in the step 2 into a nitration reactor, and carrying out nitration reaction to generate a nitration liquid; 4, phase-splitting treatment: mixing the nitration liquid in the step 3 with water, adding a secondary solvent, uniformly mixing, and carrying out phase-splitting treatment; and 5, recovery of an the organic solvent: carrying out evaporation treatment on 2-cyano-4-nitro-chlorobenzene solution in the step 4, wherein the evaporation residue is a 2-cyano-4-nitro-chlorobenzene product.According to the method, an organic solvent is used for replacing sulfuric acid to dissolve o-chlorobenzonitrile, so that the amount of waste acid generated in the reaction process is greatly reduced; and by adopting a continuous nitration reaction, the safety risk level is reduced, and the product yield is improved.

Description

technical field [0001] The invention belongs to the technical field of chemical production, and in particular relates to a new process for synthesizing 2-cyano-4-nitrochlorobenzene by continuous nitration by solvent method. Background technique [0002] 2-cyano-4-nitro-aniline is an important intermediate of disperse dyes, and its synthesis process starts with o-chlorobenzonitrile 2-cyano-4-nitro-chlorinated benzene is generated for the nitration reaction of raw materials, and then 2-cyano-4-nitro-aniline is obtained through ammonolysis reaction. In the nitration reaction of o-chlorobenzonitrile, 98% About concentrated sulfuric acid is used as solvent acid to dissolve o-chlorobenzonitrile, and about 98% of concentrated sulfuric acid and about 98% of concentrated nitric acid are used to make a mixed acid nitrating agent, which is nitrated at a low temperature below 10°C, and 2-cyano-4- Nitrochlorobenzene. This process has two major disadvantages: 1. The amount of waste aci...

Claims

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Application Information

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IPC IPC(8): C07C253/30C07C255/50
CPCC07C253/30C07C255/50
Inventor 陈泽海马竞男张杰高林林郑兴亮代会利
Owner 河北嘉泰化工科技有限公司
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