Oxidation-extraction technology for production of hydrogen peroxide by anthraquinone process

A technology of hydrogen peroxide and anthraquinone method, applied in the directions of peroxide/peroxyhydrate/peroxyacid/superoxide/ozone, inorganic chemistry, chemical instruments and methods, etc., which can solve the problem of wall thickness and pressure level equipment There are no significant advantages in investment, low reaction rate in the oxidation process, and reduced oxidation yield, etc., to achieve the effect of improving oxidation reaction rate and extraction efficiency, improving oxidation rate and extraction efficiency, and improving oxidation yield

Active Publication Date: 2017-05-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In the whole production process of hydrogen peroxide, the oxidation process of hydroanthraquinone is an automatic oxidation reaction between air and hydrogenated liquid in the oxidation reactor. The reaction process is carried out between the hydrogenated liquid and a large amount of air. During the gas-liquid reaction, Due to the high resistance of the gas-liquid two-phase interface, and the reaction process uses oxygen in the air, which only accounts for 21%, resulting in low reaction rate, long reaction time, decomposition of hydrogen peroxide, and low oxidation yield in the oxidation process. , serious side reactions and other adverse effects, so how to increase the oxidation reaction rate and reduce the oxidation time is of great significance to improve the production efficiency of hydrogen peroxide
[0004] The existing oxidation tower for the production of hydrogen peroxide by the anthraquinone method is generally divided into two sections, the upper section and the lower section. There is an apparent series process between the two section towers. The air reacts with the oxidized liquid reacted in the upper tower. In each tower, the hydrogenated liquid and air enter from the bottom of the tower and flow upward to gradually undergo oxidatio

Method used

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  • Oxidation-extraction technology for production of hydrogen peroxide by anthraquinone process

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Embodiment 1

[0032] Set up an oxidation-extraction reactor, the hydrogenation liquid and air are introduced from the bottom of the reactor, the extractant (pure water) is introduced through the middle and upper part, and after gas-liquid reaction-extraction separation-gas-liquid separation, the working liquid at the top enters the working liquid / In the hydrogen peroxide separator, the hydrogen peroxide at the bottom enters the hydrogen peroxide / working fluid separator. The oxidation-extraction reactor has a diameter of 300mm, a height of 2400mm, and a total volume of 0.17m 3 . Working fluid / hydrogen peroxide separator has a diameter of 150mm and a length of 450mm. The hydrogen peroxide / working fluid separator has a diameter of 50mm and a length of 150mm. The gas-liquid separator on the upper part of the oxidation-extraction reactor is a cyclone separation component structure. The flow rate of hydrogenated liquid is 0.29m 3 / h, the amount of air added 12Nm 3 / h, the amount of pure wat...

Embodiment 2

[0034] Set up two oxidation-extraction reactors, first introduce all the hydrogenated liquid and part of the air into the bottom of the primary oxidation-extraction reactor, the two will undergo co-current oxidation reaction from bottom to top in the reactor, and the middle and upper part will introduce secondary oxidation - The extraction agent from the extraction reactor, after oxidation reaction-extraction separation-gas-liquid separation, the hydrogenated liquid (oxidized liquid) separated in the middle and upper part is introduced into the bottom of the secondary oxidation-extraction reactor, the gas phase separated from the top and the bottom The separated hydrogen peroxide is led out of the device respectively; in the secondary oxidation-extraction reactor, the extractant (pure water) is introduced into the upper part, and the hydrogen produced in the secondary oxidation-extraction reactor is 2 o 2 It is extracted gradually, and enters the top of the primary oxidation-e...

Embodiment 3

[0036] In the three-stage oxidation / extraction reactor, all the hydrogenated liquid and part of the air are first introduced into the bottom of the primary oxidation-extraction reactor, and the two are co-currently oxidized from bottom to top in the reactor, and the middle and upper part are introduced into the secondary oxidation / extraction reactor. The extraction agent from the extraction reactor, after oxidation reaction-extraction separation-gas-liquid separation, the hydrogenated liquid (oxidized liquid) separated in the middle and upper part is introduced into the bottom of the secondary oxidation-extraction reactor, and the gas phase separated from the top is separated from the bottom The outgoing hydrogen peroxide is drawn out of the device respectively; in the secondary oxidation-extraction reactor, the extraction agent from the third-stage oxidation-extraction reactor is introduced into the middle and upper part, and at the same time, part of the oxygen-containing gas ...

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Abstract

The invention discloses an oxidation-extraction technology for production of hydrogen peroxide by anthraquinone process. The oxidation-extraction technology for production of hydrogen peroxide by anthraquinone process comprises the following contents: (1) introducing hydrogenation liquid and oxygen-containing gas from the bottom of an oxidation-extraction reactor to carry out concurrent-flow oxidation reaction from the bottom to the top inside the reactor so as to continuously generate H2O2; (2) introducing an extraction agent through the upper middle part of the oxidation-extraction reactor while the reaction in the step (1) is carried out, letting the extraction agent flow from the top to the bottom in the reactor, and gradually extracting out the H2O2 generated by the oxidation reaction; and (3) carrying out gas-liquid separation on the material from the bottom to the top, removing residual moisture with a working solution and flowing out, settling the material from the top to the bottom in the settling section, removing the residual working solution in water, and purifying or concentrating to obtain a hydrogen peroxide product. According to the technology, the two processes of oxidation and extraction are coupled to each other. The oxidation reaction is carried out while extraction of H2O2 is conducted. Meanwhile, oxidation reaction rate and extraction efficiency are enhanced, the technological process is simplified, and the technology is beneficial to save investments and reduce energy consumption.

Description

technical field [0001] The invention relates to an oxidation-extraction process for producing hydrogen peroxide by an anthraquinone method. Background technique [0002] At present, the methods for producing hydrogen peroxide by anthraquinone method in domestic industry include suspension nickel catalyst technology, fixed bed palladium catalyst technology, fluidized bed technology, etc., wherein the fixed bed palladium catalyst technology of anthraquinone method is because of its low investment, high output and easy operation. Simple and the palladium catalyst used has the advantages of less consumption, high activity, easy regeneration and safe use, and has become the mainstream of domestic hydrogen peroxide production technology. Anthraquinone method fixed-bed palladium catalyst technology: use 2-ethylanthraquinone as the carrier, and use aromatic hydrocarbon and trioctyl phosphate as the solvent to prepare a mixed liquid working fluid. The working fluid is hydrogenated w...

Claims

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Application Information

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IPC IPC(8): C01B15/013
Inventor 杨秀娜阮宗琳齐慧敏王海波王昊晨
Owner CHINA PETROLEUM & CHEM CORP
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