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Process for synthesizing diacetylmonoxime ethyl ether by continuous reactions in microtube

A butanone oxime internal reaction technology, applied in the field of continuous microtube internal reaction synthesis of butanone oxime ether, can solve the problems of long operation time, low equipment utilization rate, excessive progress, etc., achieve mass transfer and heat transfer process enhancement, Effects of reduced operating time and cost and stable operation time

Active Publication Date: 2014-08-13
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the yield of butanone oxime ethyl ether reaches 92.65%, because diethyl sulfate is active in nature, it is especially easy to decompose in water. In the intermittent reaction, it is necessary to adopt the method feeding of diethyl sulfate continuously and slowly, which is complicated to operate and difficult to control. Long operating time, high cost and low equipment utilization
The temperature of the reaction system is easy to rise rapidly, the reaction may be excessive, and the product quality is unstable
Due to the long reaction time, the unreacted excess diethyl sulfate is almost completely decomposed, resulting in waste of raw materials and equipment corrosion
Does not meet the requirements of industrial production

Method used

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  • Process for synthesizing diacetylmonoxime ethyl ether by continuous reactions in microtube
  • Process for synthesizing diacetylmonoxime ethyl ether by continuous reactions in microtube

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Experimental program
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Effect test

Embodiment 1

[0028] The inner diameter of the microtube reactor is 2.1mm and the length is 5m.

[0029] Butanone oxime, diethyl sulfate, and 18% aqueous sodium hydroxide solution are in a material ratio of 1:1.25:1.15. Feed continuously, the reaction temperature is 30°C, and the residence time is 20min. The reaction product is collected by low-temperature condensation, and the oil phase is obtained after the product is separated and separated, and the residual organic matter in the water phase is extracted and recovered with an extractant. The product was analyzed by gas chromatography with GC1690 gas chromatograph. The chromatographic column is a GsBP-INOWAX (specification: 30m×0.32mm×0.25μm) type capillary column, FID detector, and n-butanol is used as the internal standard for quantitative calculation. Analysis method, the same below. The conversion rate of butanone oxime is 83.41%, the yield of butanone oxime ethyl ether is 16.80%, and the selectivity is 16.80%.

Embodiment 2

[0031] The inner diameter of the microtube reactor is 2.1mm and the length is 5m.

[0032] Butanone oxime, diethyl sulfate, and 18% aqueous sodium hydroxide solution are in a ratio of 1:1:1. Feed continuously, the reaction temperature is 30°C, and the residence time is 3min. The reaction product is collected by low-temperature condensation, the product is separated and separated to obtain the oil phase, and the residual organic matter in the water phase is extracted and recovered with an extractant, and the product is analyzed by gas chromatography. The conversion rate of butanone oxime is 87.64%, the yield of butanone oxime ethyl ether is 15.81%, and the selectivity is 18.04%.

Embodiment 3

[0034] The inner diameter of the microtube reactor is 1mm and the length is 20m.

[0035] Butanone oxime, diethyl sulfate, and 18% aqueous sodium hydroxide solution are in a ratio of 1:1:1. Feed continuously, the reaction temperature is 40°C, and the residence time is 60min. The reaction product is collected by low-temperature condensation, the product is separated and separated to obtain the oil phase, and the residual organic matter in the water phase is extracted and recovered with an extractant, and the product is analyzed by gas chromatography. The conversion rate of butanone oxime is 77.87%, the yield of butanone oxime ethyl ether is 53.10%, and the selectivity is 68.19%.

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Abstract

The invention discloses a process for synthesizing butanone oxime ethyl ether through continuous microtube reaction. The process adopts continuous microtube reaction technology, under the conditions of temperature 30-45℃, pressure 0.1MPa and strong base, butanone oxime and diethyl sulfate are reacted to directly synthesize butanone oxime ethyl ether; the strong base is hydrogen Sodium oxide, potassium hydroxide or alcohol amine compounds. In this process, diethyl sulfate, lye and butanone oxime are respectively fed by precision micropumps, butanone oxime is mixed with lye and diethyl sulfate in turn, and then reacted in a microtube reactor. After the heater, it is condensed and collected at low temperature, the chromatographic separator is left to stand for stratification, the water phase is extracted and separated by a micro-extraction tower, and the oil phase product containing butanone oxime ether is purified by rectification in a rectification tower to obtain the final product butanone oxime ether. The process has high selectivity of butanone oxime ethyl ether, can significantly enhance mass transfer and heat transfer, effectively avoid the hydrolysis of diethyl sulfate, has simple process, long stable operation time, low cost, is easy to scale up, and meets the requirements of industrial production.

Description

technical field [0001] The invention relates to a process for synthesizing butanone oxime ethyl ether through continuous microtube reaction, belonging to the technical field of fine chemicals. Background technique [0002] Oxime ethers are organic synthesis intermediates with high added value, which can be used to synthesize a series of new pharmaceutical and pesticide products. Oxime O-alkylation batch reaction directly synthesizes oxime ether, using oxime and alkylating reagent in the presence of a strong base, the reaction is difficult to control the temperature of the system, the utilization rate of the alkylating reagent is not high, and the product quality is unstable question. For example, in the reaction of using diethyl sulfate as an ethylating reagent to synthesize butanone oxime ethyl ether ["Zhejiang Chemical Industry", 2012], the reaction condition is that the ratio of the amount of butanone oxime, diethyl sulfate and sodium hydroxide is 1:1.3:1, diethyl sulfa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C251/38C07C249/12
Inventor 朱明乔王萌卢建刚刘建青陈幼坚
Owner ZHEJIANG UNIV
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