Method for preparing cyclohexanone serving as raw material of caprolactam from cyclohexene-hydration cyclohexanol

A technology for caprolactam and cyclohexanol, which is applied in the field of cyclohexanone, a raw material for preparing caprolactam from cyclohexanol by a hydration cyclohexene method, can solve the problems of high content of harmful impurities, difficulty in producing high-quality caprolactam, insufficient use methods, etc., and achieve side reactions. The effect of reducing energy consumption and improving quality

Inactive Publication Date: 2013-08-28
NANJING DELIFEI TECH CONSULTING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the hydration cyclohexene method cyclohexanone can produce the first-class product caprolactam, but it is still difficult to produce the superior product caprolactam. The reason is that the content of harmful impurities in the current hydration cyclohexene method cyclohexanone is still too high. There are still defects in the process of producing cyclohexanone from cyclohexanol, and the hydration cyclohexene method cyclohexanone produced by the current process method is used as the raw material of caprolactam.

Method used

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  • Method for preparing cyclohexanone serving as raw material of caprolactam from cyclohexene-hydration cyclohexanol
  • Method for preparing cyclohexanone serving as raw material of caprolactam from cyclohexene-hydration cyclohexanol
  • Method for preparing cyclohexanone serving as raw material of caprolactam from cyclohexene-hydration cyclohexanol

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Embodiment 1

[0052] see image 3, the hydration cyclohexene method cyclohexanol enters the cyclohexanol light component removal tower, when the methyl cyclopentanol content in the hydration cyclohexene method cyclohexanol is greater than 50ppm, the cyclohexanol light component removal tower adopts the Distillation tower; when the content of methylcyclopentanols in the hydration cyclohexene method cyclohexanol is less than 50ppm, the cyclohexanol light component removal tower adopts a flash tower (device). Most of the light component impurities such as 2-methylcyclopentanol and 3-methylcyclopentanol are separated from the top of the tower, and are discharged from the system after condensation, and the remaining gas goes to the light second tower.

[0053] The bottom liquid of the cyclohexanol removal light component tower is heated and vaporized by the vaporizer, and the heavy component that is not vaporized during the heating and vaporization process of cyclohexanol is sent to the cyclohex...

Embodiment 2

[0071] see Figure 4 and Figure 5 The cyclohexanone obtained by hydrogenation and dehydrogenation of qualified cyclohexane oxidation method cyclohexanone or phenol is added to the conventional method of hydration cyclohexene method cyclohexanone. The mixing ratio of the hydration cyclohexene method cyclohexanone of the conventional method and the qualified cyclohexane oxidation method cyclohexanone is usually less than 1:3, when the total alkyl chain ketone content and the alkyl chain ketone content in the mixed cyclohexanone are less than 50ppm , the quality of mixed cyclohexanone meets the requirements, and can be used to produce high-quality caprolactam. During specific implementation, the mixing ratio needs to be calculated and determined by analyzing the content of harmful impurities in two kinds of cyclohexanone; the mixing ratio of the hydration cyclohexene method cyclohexanone of the conventional method and the qualified phenol method cyclohexanone is usually less th...

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Abstract

The invention relates to a method for preparing cyclohexanone serving as a raw material of caprolactam from cyclohexene-hydration cyclohexanol. The method comprises the following steps of: (A) removing light components from the cyclohexene-hydration cyclohexanol in a cyclohexanol light component removal tower; (B) heating to vaporize the cyclohexene-hydration cyclohexanol so as to separate and remove heavy components; (C) carrying out dehydrogenation reaction on the cyclohexene-hydration cyclohexanol so as to convert the cyclohexene-hydration cyclohexanol into the cyclohexanone; (D) removing light components by a light component removal tower; (E) removing cyclohexanol and heavy components by a cyclohexanone tower; (F) grading cyclohexanone by a cyclohexanone grading tower; (G) removing heavy components by a cyclohexanol tower; (H) heating to vaporize the recovered cyclohexanol so as to separate and remove heavy components; (I) carrying out dehydrogenation reaction on the recovered cyclohexanol so as to convert the recovered cyclohexanol into the cyclohexanone; and (J) carrying out compressing and purifying treatment on byproduct hydrogen gas of the cyclohexanol dehydrogenation reaction. The method further comprises a process for mixing the cyclohexanone with qualified oxidation-method or phenol-method cyclohexanone. The method has the advantages that the energy consumption and the loop loss of the cyclohexanol are reduced, light-component impurities are removed effectively, and the content of harmful impurities in cyclohexene-hydration cyclohexanone is reduced to meet the requirements for the production of high-quality caprolactam.

Description

technical field [0001] The invention relates to a method for preparing caprolactam raw material cyclohexanone by hydrating cyclohexene method cyclohexanol. More specifically, it relates to a method for preparing cyclohexanone by hydrating cyclohexene method cyclohexanol and using hydrating cyclohexene method cyclohexanone as a raw material for producing caprolactam. technical background [0002] Cyclohexanone is an important organic chemical raw material, mainly used in the production of adipic acid and caprolactam, both of which are intermediates in the production of nylon. In industrial production, cyclohexanone produced by cyclohexane oxidation method or cyclohexanone obtained by hydrogenation and dehydrogenation of phenol is often used to produce caprolactam. In recent years, the production of cyclohexanone by cyclohexene hydration method has been successfully industrialized. The main process of this method is the partial hydrogenation of benzene to cyclohexene, the hyd...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C49/403C07C45/00C07C45/82C07C45/78C07D201/06
Inventor 王艳雄李惠萍
Owner NANJING DELIFEI TECH CONSULTING
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