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Separation method of propylene oxidation products epoxypropane, acrolein and acetone

A technology for the oxidation of propylene oxide and propylene, which is applied in the separation of acrolein and acetone, and in the field of propylene oxidation product propylene oxide, which can solve the problems of low relative volatility, large theoretical plate number and reflux ratio, and difficulty in applying chromatographic methods to industrial scale, etc. problems, to achieve the effect of high recovery rate and great application prospect

Inactive Publication Date: 2020-05-05
山东联创产业发展集团股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The structures of the three are similar, especially acrolein and acetone have similar boiling points and polarities. Although they do not form azeotropes, but because the relative volatility is very small, if ordinary rectification is used to separate the two, it is desirable to obtain higher quality For the products, the required number of theoretical boards and the reflow ratio are very large, which is economically unfeasible
[0003] Chinese patent CN201810852178.7 discloses a separation method and determination method of acrolein and acetone, which are volatiles in automotive interior parts. A liquid chromatography column is used for the detection of the two, but the chromatography method is difficult to apply on an industrial scale
[0004] For the separation process of a single material, U.S.9,115,067 proposes a method for producing acrolein, which adopts a conventional rectification process with side stream extraction to purify acrolein, but because water is used in the process to quench the reaction gas phase output, and Acrolein and water are azeotropic, so only acrolein with a purity of 93.45% can be obtained at the side line near the top of the tower, which is difficult to meet the application requirements

Method used

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  • Separation method of propylene oxidation products epoxypropane, acrolein and acetone
  • Separation method of propylene oxidation products epoxypropane, acrolein and acetone
  • Separation method of propylene oxidation products epoxypropane, acrolein and acetone

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] The material to be separated is a mixture of propylene oxide, acrolein and acetone with a mass ratio of 5:1:0.9. The material enters the propylene oxide tower C-101 from the 30th theoretical plate. The tower has 45 theoretical plates in total. The operating pressure at the top of the tower is 0.2MPa, the reflux ratio is 3.5, the temperature at the top of the tower is 54.9°C, and the temperature at the bottom of the tower is 76.3°C. The propylene oxide with a purity of 99.8% is obtained at the top of the tower, and the product recovery rate reaches 98.9%.

[0027] The materials in the propylene oxide tower and tower are mainly acrolein and acetone, and ethylene glycol is used as the extraction agent. The two enter the extractive distillation tower in two ways, and adopt atmospheric distillation. The material to be separated is fed from the 20th theoretical plate, the extractant is added from the 5th plate, and the feed flow ratio of the extractant to the raw material is ...

Embodiment 2

[0030] The same system to be separated as in Example 1 was selected, and the material to be separated was a mixture of propylene oxide, acrolein, and acetone, with a mass ratio of 5:1:0.9. The material enters the propylene oxide tower C-101 from the 25th theoretical plate. The tower has 40 theoretical plates in total. The operating pressure at the top of the tower is normal pressure, the reflux ratio is 2.71, the temperature at the top of the tower is 34.2°C, and the temperature at the bottom of the tower is 54.4°C. The propylene oxide product with a purity of 99.9% is obtained at the top of the tower, and the product recovery rate reaches 98.5%.

[0031] The materials in the propylene oxide tower and tower are mainly acrolein and acetone, and N,N-dimethyldiamide (DMF) is used as the extractant, and the two enter the extractive distillation tower in two ways, and adopt atmospheric distillation. Wherein, the extractive distillation column C-102 has 50 theoretical plates, and th...

Embodiment 3

[0034] Select the same system to be separated as in Example 1, and the material to be separated is a mixture of propylene oxide, acrolein, and acetone, with a mass ratio of 5:1:0.9. The material enters the propylene oxide tower C-101 from the 25th theoretical plate. The tower has 40 theoretical plates in total. The operating pressure at the top of the tower is normal pressure, the reflux ratio is 2.85, the temperature at the top of the tower is 34.2°C, and the temperature at the bottom of the tower is 54.4°C. The propylene oxide with a purity of 99.9% is obtained at the top of the tower, and the product recovery rate reaches 98.5%.

[0035] The materials in the propylene oxide tower and tower tank are mainly acrolein and acetone, and ethylene glycol is used as the extraction agent. The two enter the extractive distillation tower in two ways, and adopt atmospheric distillation. Wherein, the extractive distillation column C-102 has 37 theoretical plates, and the material to be s...

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Abstract

The invention relates to a separation method of propylene oxidation products epoxypropane, acrolein and acetone, and belongs to the technical field of propylene oxidation product separation. Materialsto be separated enter an epoxypropane separation tower from the middle section of a tower section for rectification separation, epoxypropane is extracted from the top of the tower, and acrolein and acetone extracted from the bottom of the tower enter an extractive distillation tower; a mixture of the to-be-separated materials acrolein and acetone and an extraction agent are divided into two pathsto enter the extractive distillation tower for extractive distillation separation, and acetone is extracted from the top of the tower; the acrolein and the extraction agent distilled from the tower kettle enter a solvent recovery tower to be subjected to rectification separation, the acrolein is extracted from the tower top, and the extraction agent is extracted from the tower kettle; and the extraction agent is recycled back to the extractive distillation tower for use. The method is scientific and reasonable in design, high-purity and high-recovery-rate separation of the materials is achieved, more economical separation is achieved on the basis of comprehensively considering process cost such as energy consumption and material consumption, and the method has a large application prospectin industry.

Description

technical field [0001] The invention relates to a method for separating propylene oxide products, acrolein and acetone, belonging to the technical field of separation of propylene oxidation products. Background technique [0002] As a bulk industrial process, propylene oxidation has important uses, and the main products include propylene oxide, acrolein, acetone, etc. The structures of the three are similar, especially acrolein and acetone have similar boiling points and polarities. Although they do not form azeotropes, but because the relative volatility is very small, if ordinary rectification is used to separate the two, it is desirable to obtain higher quality The required number of theoretical boards and the reflow ratio of the products are very large, which is not economically feasible. [0003] Chinese patent CN201810852178.7 discloses a separation method and determination method of acrolein and acetone, which are volatiles in automotive interior parts. The detection...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D303/04C07D301/32C07C45/82C07C45/83C07C49/08C07C47/22B01D3/14B01D3/40
CPCB01D3/146B01D3/40C07C45/82C07C45/83C07D301/32C07D303/04C07C49/08C07C47/22
Inventor 王结祥李洪国关磊杨洪涛
Owner 山东联创产业发展集团股份有限公司
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