Continuous production method and device for preparing propionic acid through air oxidation of propionaldehyde

An air oxidation and production method technology, applied in chemical instruments and methods, preparation of organic compounds, preparation of carboxylate, etc., can solve the problems of large external circulation, increase the complexity of the process, unsafe, etc., and achieve the intrinsic safety of the process High performance, high reaction conversion rate and product selectivity, and low environmental pollution

Inactive Publication Date: 2016-01-20
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method uses external circulation heat exchange to remove the heat of reaction, which increases the complexity of the process. Due to the large amount of external circulation (generally more than 20 times the amount

Method used

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  • Continuous production method and device for preparing propionic acid through air oxidation of propionaldehyde
  • Continuous production method and device for preparing propionic acid through air oxidation of propionaldehyde
  • Continuous production method and device for preparing propionic acid through air oxidation of propionaldehyde

Examples

Experimental program
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Embodiment 1

[0050]

Embodiment 2

[0052]

Embodiment 3

[0055] temperature reflex reaction pressure Oxygen aldehyde ratio dwell time Conversion rates selectivity yield 70℃ 1.0MPaG 0.58 3.17hr 92.26% 94.87% 87.52% 80℃ 1.0MPaG 0.57 3.17hr 92.06% 93.63% 86.20% 90℃ 1.0MPaG 0.52 3.17hr 88.70% 93.40% 82.84%

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Abstract

The invention relates to a continuous production method and device for preparing propionic acid through air oxidation of propionaldehyde. The method comprises the steps that propionaldehyde enters a reactor through a liquid phase inlet in the bottom of a first-order oxidation reactor and makes contact with and is mixed with some compressed air, a majority of propionaldehyde in the raw material is converted into propionic acid through an oxidation reactor, a first-order oxidation product containing a small amount of propionaldehyde continuously enters a second-order or multi-order oxidation reactor and is continuously subjected to the oxidation reaction with the compressed air, and finally the propionic acid with the high-purity is generated. The device comprises two or more oxidation reactors connected in series, a condenser is arranged on the top of each oxidation reactor, and gas phase pipelines and backflow pipelines are arranged between the oxidation reactors for connection. A tail gas processing device is arranged behind each oxidation reactor. A gas phase pipeline is arranged between each condenser and the corresponding tail gas processing device for connection. The reaction conditions are mild, the product yield is high, the product quality is good, the propionaldehyde conversion rate is larger than 98.5%, the selectivity of the propionic acid is larger than 97.5%, and the product purity is larger than 99.5%.

Description

technical field [0001] The invention is a production process for preparing propionic acid through continuous oxidation reaction using propionaldehyde and air as raw materials; in particular, it relates to a continuous production method and device for preparing propionic acid by air oxidation of propionaldehyde. Background technique [0002] Propionic acid is a colorless and transparent liquid with a strong pungent odor, which is miscible with water, ethanol, ether, chloroform and other organic acids, and can be used to prepare propionate, ester, acid chloride, amide and acid anhydride. Propionic acid esters are important solvents and spices, and propionyl chloride and propionic anhydride are important pesticide and pharmaceutical intermediates. Propionic acid and its derivatives have been widely used in agriculture, textile, food, medicine and other industries, and its use is expanding, and its consumption is increasing year by year. [0003] At present, there are three kin...

Claims

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Application Information

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IPC IPC(8): C07C51/235C07C53/122
CPCC07C51/235C07C53/122
Inventor 张绍军马海洪石建明陶然陈勇强
Owner TIANJIN UNIV
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