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Catalyst separation device for cyclohexanone ammoximation reaction

A separation device and catalyst technology, which is applied in the direction of filtration separation, separation method, oxime preparation, etc., can solve the problems of reduced effective volume of reaction kettle, unfavorable continuous production, increased equipment investment, etc., to reduce quantity and investment, increase Large volume, effect of reducing load

Inactive Publication Date: 2014-02-05
SHEN MA INDUSTRY CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the above-mentioned methods have solved the problem of catalyst separation in the reaction solution, the built-in membrane filter causes the effective volume of the reactor to decrease and increases the investment in equipment.
Using static filtration, the separation effect is too slow, which is not conducive to continuous production

Method used

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  • Catalyst separation device for cyclohexanone ammoximation reaction
  • Catalyst separation device for cyclohexanone ammoximation reaction

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] used in this experiment figure 1 The flow shown carries out the cyclohexanone ammoximation reaction catalyst separation. Ammoximation reaction charging amount is as shown in table 1:

[0037] name

Feed unit

temperature

Cyclohexanone

28.77kg / h

room temperature

tert-butanol

81.71kg / h

room temperature

35%wt hydrogen peroxide

31.34kg / h

room temperature

liquid ammonia

5.48kg / h

room temperature

[0038] Table 1 Feed amount of oximation reaction

[0039] The catalyst concentration of the reaction liquid output pump 29 is 3%. The membrane filter 21 is backflushed every 2-3 minutes.

Embodiment 2

[0041] In this experiment, for the convenience of comparison, the figure 2 In the process shown, the cyclohexanone ammoximation catalyst is separated, that is, a suspension separator 25 is added, and the rest of the conditions are the same as in Experiment 1.

[0042] In this experiment, the catalyst concentration of the reaction liquid output pump 29 is 3%, and the catalyst concentration of the liquid delivery pump 26 at the top of the hydrocyclone separator 25 is 0.8%. The membrane filter 21 is recoiled approximately every 40 minutes, and the recoil frequency of the membrane filter is greatly reduced.

[0043] In summary, the catalyst separation device provided by the present invention is suitable for the cyclohexanone ammoximation reaction and its catalyst separation. Since the membrane filter is placed outside, the volume of the reactor is increased, and a pre-filtration device is added at the same time, which reduces the membrane filtration rate. The load of the filter ...

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Abstract

The invention discloses a catalyst separation device for cyclohexanone ammoximation reaction. The catalyst separation device comprises a reaction system and an outer filter cycling system, wherein the reaction system is connected with the outer filter cycling system through a pipeline; the reaction system comprises a reaction tank body and a stirrer which is arranged inside the tank body, the tank body is also provided with a raw material inlet and a reaction liquid outlet; the outer filter cycling system comprises a membrane filter and a heat exchanger, the membrane filter comprises a membrane filter inlet, a filter liquid outlet, a clear liquid outlet and a back-washing inlet, and the heat exchanger comprises a heat exchanger outlet and a heat exchanger inlet; the reaction liquid outlet is connected with the membrane filter inlet, the filter liquid outlet of the membrane filter is connected with the heat exchanger inlet, and the heat exchanger outlet is connected with the raw material inlet. The catalyst separation device is suitable for the cyclohexanone ammoximation reaction and for separating the catalyst, and a pre-filtering device is added, so that the load of the membrane filter can be reduced, and not only can the continuity for filtering the catalyst be guaranteed, but also the quantity and investment of the membrane filter pipes can be reduced.

Description

technical field [0001] The invention relates to a catalyst separation device, in particular to a catalyst separation device for the ammoximation reaction of cyclohexanone, which belongs to the technical field of chemical industry. Background technique [0002] Cyclohexanone oxime is an important intermediate for the preparation of caprolactam. At present, the methods for preparing cyclohexanone oxime in the world mainly include hydroxylamine sulfate method (HSO method), nitric oxide reduction method (NO method), hydroxylamine phosphate method (HPO method) and ammonia oximation method (HAO method). Among them, the HSO method and the NO method have complex processes and low-value ammonium sulfate by-products; although the HPO method does not produce ammonium sulfate by-products, the process requires fine craftsmanship, the operation is difficult, and there is NO x Produced, there is an environmental protection problem. At present, cyclohexanone oxime is mainly prepared by cy...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/10B01D35/02B01D36/04C07C249/08C07C251/42
Inventor 张电子李磊郑晓广李识寒王大勇景国耀禹保卫余保银杜卫民张恒超庞向川孙超伟任文杰吴华文刘国学窦晓勇
Owner SHEN MA INDUSTRY CO LTD
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