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Hydroxyl radical preparation device, hydroxyl radical preparation method and hydroxyl radical solution

A preparation device and free radical technology, which is applied in chemical instruments and methods, water treatment of special compounds, water pollutants, etc., can solve the problem of cumbersome preparation or preparation steps of hydroxyl radicals, low production efficiency, and low concentration of hydroxyl radicals and other problems, to achieve the effect of reliable industrial application, simple and effective preparation

Active Publication Date: 2021-06-15
北京启元汇通水务科技股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The main purpose of the present invention is to provide a preparation device for hydroxyl radicals, a preparation method thereof, and a hydroxyl radical solution, so as to solve the cumbersome preparation or preparation steps of hydroxyl radicals in the prior art, or the production efficiency is low, and The problem with the lower concentration of resulting hydroxyl radicals

Method used

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  • Hydroxyl radical preparation device, hydroxyl radical preparation method and hydroxyl radical solution

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preparation example Construction

[0043] According to another aspect of the present invention, there is also provided a method for preparing hydroxyl radicals, the preparation method comprising the following steps: S1, under pressurized conditions, dissolving at least part of ozone in the first part of hydrogen peroxide and reacting with it once , to obtain the reaction solution gas liquid; S2, pass the reaction solution gas liquid into the second part of hydrogen peroxide, and release unreacted ozone in the form of bubbles in the second part of hydrogen peroxide water under normal pressure conditions and undergo a secondary reaction to obtain Hydroxyl radical solution.

[0044] Pressurization can provide the pressure environment required for the primary reaction of ozone and hydrogen peroxide, and promote the ozone O 3 The primary reaction of consuming and generating hydroxyl radical OH can be carried forward more efficiently and continuously, and more ozone O 3 Continuously dissolved in hydrogen peroxide H ...

Embodiment 1

[0060] use figure 1 The setup shown produces hydroxyl radicals:

[0061] Ozone gas and the first part of hydrogen peroxide solution are introduced into the airtight dissolving tank through the ozone machine and the hydrogen peroxide storage tank, and O 3 +2H 2 o 2 →2HO·+2O 2 +H 2 O reacts to obtain the reaction solution gas liquid;

[0062] The reaction gas solution is released into the normal pressure dissolved gas pressure release tank through the pressure release part, and the unreacted ozone in the reaction gas solution is released to form an emulsified gas-water mixture with microbubbles with a cell diameter of 20-40 μm. Mix with the second part of hydrogen peroxide solution (the consumption of the second part of hydrogen peroxide is 4 times of the amount of ozone passed through in step S1), O 3 +4H 2 o 2 →2HO·+3O 2 +3H 2 O reacts to obtain a hydroxyl radical solution;

[0063] The obtained hydroxyl radical solution is cooled and stored in a hydroxyl radical st...

Embodiment 2

[0069] The only difference with Example 1 is that the weight concentration of the first and second parts of the hydrogen peroxide solution is 50%.

[0070] The weight concentration of the hydroxyl radical solution is about 30%.

[0071] Add the hydroxyl radical solution according to the feed ratio of sewage COD value and hydroxyl radical amount of 1:1, add 400mg\L 30% of the above hydroxyl radical solution to the industrial sewage with sewage COD of 400mg\L, fully stir After a certain reaction time, the pollutants in the industrial sewage are greatly degraded, and the COD concentration reaches a level of ≤40.

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Abstract

The invention provides a hydroxyl radical preparation device, a hydroxyl radical preparation method and a hydroxyl radical solution. The device comprises a pressurized reaction unit and a normal-pressure reaction unit, the pressurized reaction unit is provided with an ozone inlet, a first hydrogen peroxide inlet and a reaction dissolved gas liquid outlet, and the pressurized reaction unit is used for carrying out primary reaction on ozone and hydrogen peroxide in a pressurized state; the normal-pressure reaction unit comprises a reaction shell and a release part arranged in the reaction shell, the reaction dissolved gas liquid outlet is connected with the normal-pressure reaction unit through a first conveying pipeline, the first conveying pipeline penetrates through the reaction shell and is connected with the release part, and the release part is provided with a plurality of release holes; and the normal-pressure reaction unit is used for enabling reaction dissolved gas liquid to be further subjected to secondary reaction with hydrogen peroxide under normal pressure to obtain a hydroxyl radical solution. By applying the device provided by the invention, the hydroxyl free radical solution with higher concentration can be more effectively prepared through the synergistic effect of the pressurizing unit and the normal pressure unit.

Description

technical field [0001] The invention relates to the field of chemical industry, in particular to a hydroxyl radical preparation device, a preparation method thereof, and a hydroxyl radical solution. Background technique [0002] Hydroxyl radical is recognized as a strong oxidizing substance with an oxidation potential of 2.85eV, second only to fluorine (F 2 ) of 2.87eV, much higher than hydrogen peroxide (H 2 o 2 )1.78eV and ozone (O 3 ) of 2.07eV. The strong oxidative properties of hydroxyl radicals make it applicable to many fields of industrial production, especially in the field of sewage treatment. According to statistics, in 2017, the total discharge of wastewater in the country was 77.74 billion tons, of which the discharge of industrial wastewater was 18.29 billion tons, accounting for 23.52% of the total discharge of wastewater. There are a large amount of difficult-to-treat industrial wastewater in industrial wastewater, such as petrochemical, coal coke chemic...

Claims

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Application Information

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IPC IPC(8): C02F1/78C02F1/72C02F101/30
CPCC02F1/78C02F1/722C02F2305/023C02F2101/30
Inventor 宋金成虞彤乌力更
Owner 北京启元汇通水务科技股份有限公司