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Production technology and equipment system for improving quality and yield of cyclohexanone oxime

A technology of cyclohexanone oxime and production process, which is applied in the field of preparation of cyclohexanone oxime, can solve problems such as non-compliance, low conversion rate of cyclohexanone oxime, and increase of hydrogen peroxide, so as to reduce unit consumption and increase effective conversion rate , the effect of improving quality

Pending Publication Date: 2020-02-18
长沙兴和新材料有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Toluene, cyclohexanone and cyclohexyl imine are recovered from the top of the tower, and cyclohexanone oxime (purity 99%-99.5%) containing impurities such as dipolycyclohexyl imine and octahydrophenazine goes out from the tower kettle, and then Entering the Beckman rearrangement and translocation process may easily cause the volatile base index of subsequent caprolactam products to fail
Therefore, the conversion rate of cyclohexanone in the traditional direct ammoximation process is low, resulting in high unit consumption of cyclohexanone, and because cyclohexanone is converted into cyclohexyl imine, the polycyclic rings produced in the rectification process Substances such as hexylimine and swahydrophenazine lead to the poor quality of cyclohexanone oxime, which in turn leads to the quality of caprolactam not reaching the world-class level
Increasing the amount of hydrogen peroxide and ammonia in the oximation reaction can alleviate this problem to some extent, but excessive hydrogen peroxide is not stable, and ammonia will be oxidized to nitrogen oxides, which will pollute the environment. It increases the safety risk of industrial implementation, which is not in line with the current direction of my country's development of green and safe chemical industry
[0011] CN101781232A discloses a preparation process of cyclohexanone oxime, which combines two oximation reactions to solve the problem of incomplete conversion rate of cyclohexanone directly through ammoximation of cyclohexanone, but they also think that one-step oximation The conversion rate can reach or exceed 99.5%, and it is not recognized that the conversion rate of cyclohexanone oximation is actually low due to the existence of cyclohexyl imine
Moreover, in the second oximation reaction, although an excessive amount of aqueous solution of hydroxylamine sulfate was used, the pH was not adjusted simultaneously during the reaction, so that although the concentration of hydroxylamine salt in the reaction system was high, the actual part of the oximation reaction actually participated The concentration of free hydroxylamine is not high, and the sulfuric acid by-product of the oximation reaction is not neutralized in time, which will cause the system to become more and more acidic
Experiments have proved that under strong acidic conditions, this method cannot increase the conversion rate of oximation of cyclohexanone, but may lose cyclohexanone oxime, so that the secondary oximation of this process cannot increase the total cyclohexanone oxime transformation rate, so the patent has been in the unapplied stage

Method used

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  • Production technology and equipment system for improving quality and yield of cyclohexanone oxime
  • Production technology and equipment system for improving quality and yield of cyclohexanone oxime
  • Production technology and equipment system for improving quality and yield of cyclohexanone oxime

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Effect test

Embodiment 1

[0057] refer to figure 1 , the equipment system of the present embodiment includes: a direct ammonia oximation reactor 10, a membrane separator 20, a tert-butanol recovery tower 80, an organic solvent extraction tower 30, a secondary oximation reactor 40 and a toluene recovery through pipelines in sequence. Tower 90;

[0058] The direct ammoximation reactor 10 is connected with a reaction liquid line 11 and a tail gas discharge line 13, which is connected to the membrane separator 20 through the reaction liquid line 11;

[0059] The membrane separator 20 is connected with a catalyst circulation line 21 and a reaction clear liquid line 22, which is connected to the direct ammoximation reactor 10 through the catalyst circulation line 21, and is recovered with tert-butanol through the reaction clear liquid line 22. The tower 80 is connected, the catalyst circulation pipeline 21 is connected with the reaction material pipeline 12, and the catalyst circulation pipeline 21 is conne...

Embodiment 2

[0071] refer to figure 2 , The equipment system of this embodiment includes: a direct ammoximation reactor 10, a membrane separator 20, an organic solvent extraction tower 30 and a secondary ammoximation reactor 40 connected through pipelines in sequence;

[0072] The direct ammoximation reactor 10 is connected to a reaction liquid line 11 and a tail gas discharge line 13, and is connected to a membrane separator 20 through the reaction liquid line 11;

[0073] The membrane separator 20 is connected with a catalyst circulation line 21 and a reaction clear liquid line 22, which is connected to the direct ammoximation reactor 10 through the catalyst circulation line 21, and connected to the organic solvent extraction tower through the reaction clear liquid line 22. 30 connection, the catalyst circulation pipeline 21 is connected with a reaction material pipeline 12, and the catalyst circulation pipeline 21 is connected with a catalyst recovery pipeline 23;

[0074] The organic...

Embodiment 3

[0082] refer to image 3 , the equipment system of the present embodiment includes: a direct ammonia oximation reactor 10, a membrane separator 20, a tert-butanol recovery tower 80, an organic solvent extraction tower 30, a secondary oximation reactor 40 and toluene recovery through pipelines in sequence. Tower 90;

[0083] The direct ammoximation reactor 10 is connected with a reaction liquid line 11 and a tail gas discharge line 13, which is connected to the membrane separator 20 through the reaction liquid line 11;

[0084] The membrane separator 20 is connected with a catalyst circulation line 21 and a reaction clear liquid line 22, which is connected to the direct ammoximation reactor 10 through the catalyst circulation line 21, and is recovered with tert-butanol through the reaction clear liquid line 22. The tower 80 is connected, the catalyst circulation pipeline 21 is connected with the reaction material pipeline 12, and the catalyst circulation pipeline 21 is connect...

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Abstract

The invention discloses a production technology and equipment system for improving the quality and yield of cyclohexanone oxime. According to the production technology, special ammoximation conditionsare adopted, under the assistance of secondary oximation, the cyclohexanone oximation conversion rate is effectively increased without increasing the consumption amount of hydrogen peroxide, and theyield and quality of cyclohexanone oxime are improved. The equipment system comprises following components communicated by pipelines: a direct ammoximation reactor, a membrane separator, an organic solvent extraction column, and a secondary oximation reactor. The production technology and the structure of the equipment system are simple; the operation is safe; high quality cyclohexanone oxime canbe prepared, and the yield is high.

Description

technical field [0001] The invention belongs to the field of preparation of cyclohexanone oxime, in particular to a production process and equipment system for improving the quality and yield of cyclohexanone oxime. Background technique [0002] At present, caprolactam is mainly prepared from cyclohexanone oxime through Beckmann rearrangement and translocation. The main processes for preparing cyclohexanone oxime include Raschig method (hydroxylamine sulfate method), HPO method (hydroxylamine phosphate method), NO reduction method and direct ammonia Oximation method. The Raschig method uses cyclohexanone and hydroxylamine sulfate to carry out oximation reaction to obtain cyclohexanone oxime. Among them, hydroxylamine sulfate is prepared by reducing ammonium nitrite with sulfur dioxide. This process is very mature and is the earliest successful process route. However, due to the large amount of ammonium sulfate by-product, the quality of hydroxylamine sulfate obtained is ave...

Claims

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Application Information

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IPC IPC(8): C07C249/08C07C249/04C07C251/44
CPCC07C249/08C07C249/04C07C249/02C07C2601/14C07C251/44C07C251/20
Inventor 肖藻生肖有昌师太平
Owner 长沙兴和新材料有限公司
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