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A kind of cyclohexanone ammoximation method

A technology of cyclohexanone ammonia oxime and cyclohexanone, which is applied in oxime preparation, organic chemistry, etc., can solve the problems of poor separation effect, serious influence of catalyst diffusion, and easy clogging of catalyst, so as to reduce subsequent separation cost, The mass transfer effect between phases is good, and the effect of solving the problem of easy deactivation of the catalyst

Active Publication Date: 2018-01-05
CHINA TIANCHEN ENG +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] 1. The current preparation method of cyclohexanone oxime is generally a liquid phase reaction. The titanium-containing catalyst is placed in a strong alkaline environment for a long time, which cannot avoid the dissolution of the skeleton silicon on the catalyst, resulting in the ineffective loss of the catalyst, shortening the service life of the catalyst, and affecting ammonia oxime. Stable operation of chemical reaction system;
[0007] 2. The liquid-solid phase reaction has the disadvantage of large mass transfer resistance, and the phenomenon of catalyst diffusion is seriously affected;
[0008] 3. In order to effectively solve the above-mentioned catalyst diffusion phenomenon and maintain good catalytic reaction conditions, titanium-containing catalysts can be prepared into nanoscale. However, although this can ensure suitable catalytic activity, it also brings another technical defect, that is To separate the catalyst from the liquid phase raw material in the slurry bed reactor, it is necessary to use an expensive membrane separation device, which increases the cost of subsequent separation and the phenomenon of membrane plugging is unavoidable;
[0009] 4. In the ammoximation reaction, most of them will install a porous plate in the reactor to effectively separate the catalyst, but the separation effect is not good, not only the catalyst is easy to block the orifice plate, but also causes great inconvenience to subsequent maintenance and replacement;
[0010] 5. The effective utilization rate of hydrogen peroxide is generally not high

Method used

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  • A kind of cyclohexanone ammoximation method
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] Embodiment 1 (comparative example)

[0042]With reference to the reaction method disclosed in the prior art (patent CN1432560A), the cyclohexanone ammoximation reaction process is designed by itself. Wherein, the raw material ratio is: the molar ratio of hydrogen peroxide to cyclohexanone is 1.1:1, and the molar ratio of ammonia to cyclohexanone is 2.3:1. The reaction conditions are as follows: the temperature is 90° C., the absolute pressure is 0.4 MPa, the catalyst is 3 g (40 mesh) of titanium-silicon molecular sieve formed by tableting, and the contact time between the reaction raw material and the catalyst is 60 minutes. The slurry after the reaction is centrifuged, and the separated catalyst is dried, calcined and weighed. The reaction results are shown in Table 1.

[0043] Table 1

[0044]

[0045] Catalyst mass after reaction: 2.5g.

[0046] This example verifies that in the traditional liquid-phase ammoximation reaction, there is the problem of complicate...

Embodiment 2

[0048] All reaction parameters and raw material ratios were kept constant in Example 1. In a fixed bed reactor, just follow the attached figure 1 The procedure for cyclohexanone ammoximation test is carried out. The dispersion method of the raw material mixture is high-pressure dispersion, nitrogen is used as the inert gas carrier gas, the boost pressure is 0.1 MPa, and the volume ratio of nitrogen carrier gas to ammonia is 10:1. The reaction results are shown in Table 2.

[0049] Table 2

[0050]

[0051] Catalyst mass after reaction: 3g.

[0052] This example successfully demonstrates that in the solid-phase reaction of ammonia oximation gas, the product and the catalyst can be separated in situ, there is no problem of catalyst loss, the life of the catalyst is greatly extended, and the effective utilization rate of hydrogen peroxide is as high as 90%.

Embodiment 3

[0054] Repeat Example 2, just replace the oximation reactor with a fluidized bed reactor. The pressure of the booster gas is 0.6MPa, and the catalyst is TS-1 after spray granulation, which is mixed with SiO in the binder 2 The weight ratio of the catalyst is 60:40, the particle size range is 20-120 μm, and the loading amount of the catalyst is 50 g, accounting for about 80% of the total particle weight. The modulation reaction temperature is 120° C., the reaction pressure is normal pressure, helium is used as carrier gas, and the volume ratio of helium to ammonia is 60:1. The reaction results are shown in Table 3.

[0055] table 3

[0056]

[0057] Catalyst mass after reaction: 49.5 g.

[0058] There is basically no loss of the catalyst, the service life of the catalyst is greatly extended, and the effective utilization rate of hydrogen peroxide is as high as 90%.

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Abstract

The invention innovatively provides a cyclohexanone ammoximation method. The method comprises steps as follows: hydrogen peroxide, an inhibitor of hydrogen peroxide, cyclohexanone and a low-carbon alcohol aid are mixed in a certain proportion to form a mixed liquid, and the mixed liquid is sent to the top of an oximation reactor to be dispersed into 1-200 mu m fine particles; mixed gas of inert gas and ammonia gas is preheated and sent into the oximation reactor to be contacted with the dispersed fine particles, and the dispersed fine particles are further gasified; the gasified fine particles and ammonia gas are placed on a titanium-containing catalyst in the oximation reactor for a cyclohexanone ammoximation reaction, the reacted mixture is separated, and a product is obtained. The problems that a catalyst in the prior art is easily inactivated, follow-up separation is difficult, membrane blocking is serious, the effective utilization rate of hydrogen peroxide is lower and the like can be effectively solved, and the cyclohexanone ammoximation method has broad and good industrial prospect.

Description

technical field [0001] The invention belongs to the technical field of catalytic synthesis of organic chemicals, and relates to a method for preparing cyclohexanone oxime by using a titanium-containing catalyst, and further explains that it is about a gas-solid phase cyclohexanone ammoximation reaction to prepare cyclohexanone oxime Methods. Background technique [0002] Cyclohexanone oxime is an important chemical synthesis intermediate, which can synthesize caprolactam (CPL) through Beckmann rearrangement reaction, and is a key intermediate in the production of caprolactam. Caprolactam can be polymerized to produce nylon-6, and nylon-6 can be further processed into nylon fibers, engineering plastics and plastic films. [0003] At present, there are three process routes for industrial production of caprolactam: (1) Cyclohexanone-hydroxylamine production route, including traditional Raschig process, DSM / HPO process, BASF-NO reduction process, Inventa-NO reduction process, A...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C249/04C07C251/44
CPCC07C249/04C07C251/44
Inventor 孙承宇耿玉侠马国栋赵文平
Owner CHINA TIANCHEN ENG
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