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Oxidation system for producing hydrogen peroxide

An oxidation system, hydrogen peroxide technology, applied in the direction of peroxide/peroxy hydrate/peroxyacid/superoxide/ozonide, inorganic chemistry, chemical instruments and methods, etc., can solve the problem of low output and systematic production The cycle is not stable enough, the oxidation yield is low, etc.

Active Publication Date: 2010-09-22
YANGZHOU HUITONG CHEM ENG TECHN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Its disadvantages are: the oxidation yield of the existing oxidation system is low, the oxidation of the hydrogenated liquid is incomplete, the yield is low, and the production cycle of the system is not stable enough

Method used

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  • Oxidation system for producing hydrogen peroxide
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Embodiment Construction

[0011] As shown in the figure, it is a working principle diagram of an oxidation system for hydrogen peroxide production. The oxidation system includes a phosphoric acid configuration tank V1201, an oxidation tower composed of upper tower T1201A, middle tower T1201B and lower tower T1201C, and compressed air Filter X1201, oxidizing liquid gas-liquid separator V1202, oxidizing liquid coolers E1201A and E1201B, oxidizing liquid tail gas cooler E1202, aromatic hydrocarbon intermediate receiving tank V1203, oxidizing liquid storage tank V1204; outlet of phosphoric acid configuration tank V1201 is connected with the hydrogenation liquid source together The inlet of the hydrogenation liquid pump P1101 is connected, the outlet of the hydrogenation liquid pump P1101 is connected to the bottom of the upper tower T1201A, the inlet of the compressed air filter X1201 is connected to the compressed air source, and the outlet of the compressed air filter X1201 is divided into two ways, one way...

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PUM

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Abstract

The invention discloses an oxidation system for producing hydrogen peroxide in the field of chemical equipment. In the oxidation system, the outlet of a phosphoric acid preparation tank and a hydride source are communicated with the inlet of a hydride pump; the outlet of the hydride pump is communicated with the bottom of an upper tower; the inlet of a compressed air filter is communicated with a compressed air source; the outlet of the compressed air filter is divided into two paths, one path is communicated with the bottom of the upper tower, and the other path is communicated with the bottom of a lower tower; the number of oxidizing solution coolers is two; an oxidizing solution outlet at the top of the upper tower is communicated with the bottom of a middle tower after passing through one oxidizing solution cooler; an oxidizing solution outlet at the top of the middle tower is communicated with the bottom of the lower tower after passing through the other oxidizing solution cooler; and the tail gas at the tops of the middle and upper towers can be condensed for recycling. When the system works, main reaction is performed in the upper and middle towers and complete oxidation reaction is performed in the lower tower, so that hydride can be more fully oxidized and the yield can be improved. The oxidation system is particularly used for producing the hydrogen peroxide.

Description

Technical field [0001] The invention relates to a production equipment for hydrogen peroxide, in particular to a production equipment for the hydrogenation process in the production of hydrogen peroxide by an anthraquinone method. Background technique [0002] At present, the main production method of hydrogen peroxide is the anthraquinone method. After extensive research and improvement by companies in various countries, this method has become the most dominant method for producing hydrogen peroxide in the world, almost completely replacing the electrolysis method. This method uses anthraquinone derivatives (mainly 2-alkylanthraquinone) as a catalyst carrier. In the presence of a catalyst, 2-alkylanthraquinone (AQ) dissolved in a suitable organic solvent is hydrogenated with hydrogen to generate the corresponding 的2-alkylhydroanthraquinone (HAQ). After the HAQ in the solvent is separated from the catalyst, it can be oxidized with air or oxygen-enriched gas to generate H2O2, and ...

Claims

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Application Information

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IPC IPC(8): C01B15/023
CPCC01B15/023
Inventor 陈纪兴
Owner YANGZHOU HUITONG CHEM ENG TECHN
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