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Process for extracting and washing cyclohexane oxime

A technology of cyclohexanone oxime and water extraction, which is applied in oxime preparation, organic chemistry, etc., can solve the problems of increasing cost and increasing difficulty, and achieve the effects of reducing water and electricity, saving equipment investment, and simplifying the refining process

Active Publication Date: 2011-01-26
河北美邦工程科技股份有限公司
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  • Abstract
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  • Application Information

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Problems solved by technology

[0003] Chinese patent CN101781232A discloses a preparation process of cyclohexanone oxime. Although the refining process of cyclohexanone oxime has been simplified, because cyclohexanone oxime is changed from one step to two steps, and the second step is hydroxylamine oxime, this It will undoubtedly increase the difficulty and cost for enterprises without hydroxylamine preparation

Method used

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  • Process for extracting and washing cyclohexane oxime
  • Process for extracting and washing cyclohexane oxime

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Embodiment 1

[0017] Embodiment 1: as figure 1 Shown, technological process of the present invention is as follows:

[0018] a. Put 37550kg / h cyclohexane and 30150kg / h cyclohexanone oxime aqueous solution into the supergravity centrifugal extractor A respectively, and control the temperature at 45-55°C for extraction;

[0019] b. When the mass concentration of cyclohexanone oxime in the cyclohexanone oxime aqueous solution is less than 1%, the organic phase coming out from the extractor A at this time is about 50500kg / h, and is washed with 5000kg / h desalted water to remove the salt ions therein;

[0020] c. when the mass concentration of salt ions in the organic phase in step b is less than 0.001%, the washed organic phase is subjected to hydrocyclone separation and gravity sedimentation separation to obtain a cyclohexane solution of about 50300kg / h cyclohexanone oxime;

[0021] d. After mixing about 17200kg / h of the water phase from the extractor A in step b and about 5050kg / h of the wate...

Embodiment 2

[0022] Embodiment 2: the difference between this embodiment and embodiment 1 is that n-hexane replaces cyclohexane as the extraction agent.

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Abstract

The invention discloses a process for extracting and washing cyclohexane oxime. The process comprises the following steps of: extracting an extractant and aqueous solution of cyclohexane oxime in a weight part ratio of 1:1 to 2:1 at the temperature of between 45 and 55 DEG C; washing an organic phase obtained by the extraction with desalted water when the mass concentration of the cyclohexane oxime is less than 1 percent so as to remove salt ions in the cyclohexane oxime solution; mixing a water phase obtained after washing and a water phase obtained by extraction, and extracting the mixture by using a cyclohexane or hexane extractant in a weight part ratio of 0.5:1 at the temperature of between 45 and 55 DEG C so as to recycle the cyclohexane oxime in the mixture; and sequentially performing hydraulic cyclone separation and gravity settling separation on the washed organic phase when the mass concentration of the salt ions in the organic phase is less than 0.0001 percent so as to obtain the cyclohexane oxime. The process does not need a rectification process; the purity of the obtained cyclohexane oxime is high; beckmann rearrangement can be directly performed in the next process so as to prepare caprolactam; and for 100,000 t / a of cyclohexanone oxime devices, the process can save one-time equipment investment by about 20 to 30 million and can reduce energy consumption such as water, electricity, steam and the like by about 30 to 40 million.

Description

technical field [0001] The invention relates to a process for refining cyclohexanone oxime, which is further a process for refining an aqueous solution of cyclohexanone oxime through two-step extraction and washing. Background technique [0002] Cyclohexanone oxime is an isomer of caprolactam, and industrially generally use cyclohexanone oxime Beckmann rearrangement to produce caprolactam. In order to obtain high-quality caprolactam, the industry requires high purity of cyclohexanone oxime, generally requiring more than 99.9% (WT). To obtain high-purity cyclohexanone oxime, in addition to extracting and washing the aqueous solution of cyclohexanone oxime produced by the reaction, it is also necessary to carry out rectification regeneration of the extractant and rectification purification of cyclohexanone oxime. The increase of these processes, on the one hand, requires an increase in investment in disposable equipment, and more importantly, increases the regular operating c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C251/44C07C249/14
Inventor 赵承军张玉新
Owner 河北美邦工程科技股份有限公司
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