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Ozone/hydrogen peroxide synergistic oxidation high-salinity wastewater treatment method

A high-salt wastewater treatment method technology, applied in the direction of oxidation water/sewage treatment, magnetic field/electric field water/sewage treatment, flocculation/sedimentation water/sewage treatment, etc., can solve the problem that organic matter is not easy to decompose, catalytic reaction is hindered, and catalysts are difficult to recycle and other problems to achieve the effect of reducing the dosage of medicine

Pending Publication Date: 2021-12-10
中广核环保产业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The Fenton process is generally applicable to the situation where the COD concentration is around 10,000 mg / L. If the COD of the wastewater is too high, multi-stage oxidation purification treatment is required, and the Fenton process has no advantage
[0004] However, in the process of treating high-salt wastewater by the Fenton process, the cost of electric energy and chemical reagents is high, and there are problems such as high requirements for reaction conditions (pH, temperature, etc.), and difficult recovery of catalysts.
Fenton advanced oxidation technology is greatly affected by pH in the wastewater treatment process. When the acidity is strong, the H in the solution + Concentration is too high, hydrogen peroxide as H 3 o 2+ The form is stable, and the organic matter is not easy to decompose in the strong acidic environment, Fe 3+ Cannot be successfully reduced to Fe 2+ , the catalytic reaction is hindered, more iron-containing sludge is produced, and the effluent is colored

Method used

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  • Ozone/hydrogen peroxide synergistic oxidation high-salinity wastewater treatment method
  • Ozone/hydrogen peroxide synergistic oxidation high-salinity wastewater treatment method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Put 50mL of high-salt wastewater in the oxidation reactor, apply radio frequency microwave, ultraviolet, hydrogen peroxide and ozone to the high-salt wastewater in the oxidation reactor at the same time, the treatment time is >12H, and the frequency of radio frequency electromagnetic wave is 300KHz.

[0028] Test conclusion: the high-salt wastewater in the oxidation reactor becomes colorless, the ammonia nitrogen does not change, and the COD<1000mg / L. During the activation treatment of ozone / hydrogen peroxide, the radio frequency electric field can effectively treat high-salt wastewater without causing loss of ammonia nitrogen.

Embodiment 2

[0030] Put 50mL of high-salt wastewater into the oxidation reactor, apply radio frequency microwave, hydrogen peroxide and dissolved gas to the high-salt wastewater in the oxidation reactor at the same time, the treatment time is >12H, and the frequency of radio frequency electromagnetic wave is 300KHz.

[0031] Test conclusions: (1) Dissolved air ozone radio frequency advanced oxidation technology can effectively treat chemical wastewater; (2) To remove individual cases, the TOC / COD degradation rate is basically maintained between 50% and 60%.

Embodiment 3

[0033] Put 50mL of high-salt wastewater in the oxidation reactor, apply plug-in radio frequency, hydrogen peroxide and ozone to the high-salt wastewater in the oxidation reactor at the same time, the treatment time is >12H, and the frequency of radio frequency electromagnetic wave is 300KHz. Plug-in radio settings such as figure 2 As shown, the high-salt wastewater treatment device includes an oxidation reactor 10 provided with a water inlet 100 and a water outlet 102, a radio frequency activation device 20 connected to the oxidation reactor 10, and a precipitation device 30 connected to the water outlet 102, wherein the oxidation The reactor 10 is provided with several radio frequency radiation terminals 200 distributed at intervals, and the radio frequency radiation terminals 200 are respectively connected with the radio frequency activation device 20 .

[0034] Test conclusion: The newly developed plug-in device has been tested and confirmed that the processing capacity ha...

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Abstract

The invention discloses an ozone / hydrogen peroxide synergistic oxidation high-salinity wastewater treatment method. The method comprises the following steps: 1) putting high-salinity wastewater into an oxidation reactor; and 2) performing catalytic oxidation reaction on the high-salinity wastewater through ozone / hydrogen peroxide activation treatment, and applying a radio frequency electric field to the oxidation reactor. Compared with the prior art, the ozone / hydrogen peroxide synergistic oxidation high-salinity wastewater treatment method has the following advantages that radio frequency electric field coupling ozone / hydrogen peroxide catalytic oxidation is adopted, the agent dosage can be reduced by 50% or above, the method is not sensitive to the pH value, the pH does not need to be adjusted in the treatment process, impurity ions such as Fe are not introduced, and the method is suitable for the industry with salt recovery requirements.

Description

technical field [0001] The invention belongs to the technical field of waste water treatment, and more specifically, the invention relates to a high-salt waste water treatment method based on the coordinated oxidation of ozone / hydrogen peroxide. Background technique [0002] In coking, printing and dyeing, pharmaceutical, petrochemical and other industrial production processes, a large amount of high-salt wastewater containing toxic organic substances will be produced. High-salt wastewater cannot be directly removed by biochemical treatment. It is usually necessary to crystallize and separate the industrial salt in the wastewater before processing. Biochemical treatment leads to the generation of toxic industrial waste salt, which cannot be recycled as a resource. In addition, because organic matter in high-salt wastewater contains formaldehyde, alcohols, and refractory, high-boiling phenolic substances, conventional catalytic oxidation cannot be processed. [0003] As a ne...

Claims

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Application Information

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IPC IPC(8): C02F9/14C02F1/78C02F1/72C02F1/48
CPCC02F9/00C02F1/78C02F1/722C02F1/725C02F1/48C02F1/025C02F1/52C02F1/24C02F7/00C02F3/00
Inventor 石艳春安瑞吴详木
Owner 中广核环保产业有限公司
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