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Preparation method of aminocaprolactam

A technology of caprolactam and crude caprolactam, which is applied in the preparation of lactam, chemical instruments and methods, organic chemistry, etc., can solve the problem of liquid phase rearrangement process with small processing capacity, harm to the environment and human health, and non-oleum catalyzed It can realize industrialization and other problems, and achieve the effect of easy control and realization of control

Active Publication Date: 2008-02-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] Although the conversion rate of cyclohexanone oxime and the selectivity of caprolactam in some patents are relatively high, due to economic and technical reasons, the liquid phase rearrangement process catalyzed by non-oleum has not been industrialized so far.
[0008] At present, the main problems faced in the development of the liquid-phase Beckmann rearrangement process are: (1) Inventa's acetic anhydride and acetic acid catalytic rearrangement process uses ion exchange resins to adsorb and separate caprolactam, and the processing capacity is small; (2) in the ionic liquid homogeneous system or in an ionic liquid / organic solvent two-phase system, with phosphorus-containing compounds (P 2 o 5 , PCl 3 , PCl 5 or POCl 3 ) carry out the rearrangement reaction for the catalyst, all generate the complex with strong binding force with the phosphorus-containing compound, and be difficult to separate the caprolactam of free state from the ionic liquid, the recycle use difficulty of ionic liquid and catalyst; (3) rearrangement The neutralization step in ammonia after the reaction will by-produce ammonium sulfate or other ammonium salts, and cause the catalyst to be unable or difficult to recycle; (4) some catalysts (such as phosphorus-containing compounds or SO 3 etc.) will endanger the environment and human health

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] This embodiment illustrates that the present invention can be used in [bmim]BF 4 performed in a homogeneous system.

[0039] First add hydrophilic [bmim]BF to a 100ml Erlenmeyer flask 4 40ml of ionic liquid and 15ml of acetic anhydride to obtain the ionic liquid solution of acetic anhydride, then add [bmim]BF to a 250ml round bottom flask 4 50ml of ionic liquid and 10g of cyclohexanone oxime, the temperature of the oil bath is controlled at 70°C, magnetic stirring, and then the prepared ionic liquid solution of acetic anhydride is added dropwise, and reacted for 10 minutes to obtain an ionic liquid solution containing CPL, acetic anhydride and acetic acid. The ionic liquid solution was extracted with toluene, and the relative content of each substance in the toluene solution was analyzed by gas chromatography. The conversion rate of cyclohexanone oxime was 100.0%, the selectivity of caprolactam was 97.9%, and the total selectivity of caprolactam and cyclohexanone was ...

Embodiment 2

[0044] This example illustrates that the present invention can be used in hydrophobic [bmim][PF 6 ] implemented in .

[0045] First add [bmim][PF to a 50ml test tube 6 ] ionic liquid 25ml and cyclohexanone oxime 1.0g, heat up to 120 ℃, obtain the ionic liquid solution of cyclohexanone oxime, then add [bmim][PF 6 ] 30ml of ionic liquid and 1.5ml of acetic anhydride to obtain an ionic liquid solution of acetic anhydride, the temperature of the oil bath was controlled at 120°C, and magnetic stirring was performed, and then the prepared ionic liquid solution of cyclohexanone oxime was added dropwise and reacted for 3 minutes. The conversion rate of cyclohexanone oxime was 100.0%, and the selectivity of caprolactam was 85.4%.

Embodiment 3

[0047] This example illustrates that the present invention can be used in hydrophobic [C 12 mim][(CF 3 SO 2 ) 2 N] implemented in a homogeneous system.

[0048] First add hydrophilic [C 12 mim][(CF 3 SO 2 ) 2 N] ionic liquid 15ml and acetic anhydride 15ml, obtain the ionic liquid solution of acetic anhydride. In a 100ml round bottom flask add [C 12 mim][(CF 3 SO 2 ) 2 N] 15ml of ionic liquid and 10 grams of cyclohexanone oxime, oil bath temperature control 30 ℃, magnetic stirring, the prepared ionic liquid solution of acetic anhydride was added dropwise, and reacted for 60min. The conversion rate of cyclohexanone oxime was 100.0%, and the selectivity of caprolactam was 91.6%.

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PUM

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Abstract

The invention discloses a preparation process for caprolactam which is characterized in that the acetic anhydride acts as the catalyzer to make a Beckmann rearrangement reaction of cyclohexanone oxime in ionic liquid homogeneous system , then the orgainic solvent is used to extract the ionic liquid and fully transfer the cyclohexanone oxime and the catalyzer into the organic solvent, finally the separation of the cyclohexanone oxime and the catalyzer is realized by the extraction to the solvent.

Description

technical field [0001] The invention relates to a method for preparing organic chemical raw materials, more specifically to a method for preparing caprolactam through Beckmann rearrangement reaction of cyclohexanone oxime. Background technique [0002] Caprolactam is a widely used important organic chemical raw material. About 90% of caprolactam in the world is prepared from cyclohexanone oxime through Beckmann rearrangement reaction. The traditional Beckmann rearrangement reaction process is: use oleum to make cyclohexanone oxime form caprolactam salt of sulfuric acid, in order to obtain a high yield of caprolactam, it is necessary to add excess nicotinic acid, and then neutralize the mixture with ammonia water to obtain ammonium sulfate and caprolactam. In a typical industrial rearrangement process, the conversion of cyclohexanone oxime is almost 100%, the selectivity to caprolactam is 99%, yielding 1.3-1.8 kg ammonium sulfate / kg oxime (or 1.0-1.3 mol oxime). This traditi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D201/04C07D223/10
Inventor 张伟吴巍闵恩泽
Owner CHINA PETROLEUM & CHEM CORP
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