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Method for treating organic wastewater by catalytic oxidation of a two-phase oxidant system

A technology of organic wastewater and catalytic oxidation, which is applied in the direction of oxidized water/sewage treatment, chemical instruments and methods, water/sewage treatment, etc., can solve the problems of complex operation and high cost, improve degradation rate, reduce impact, and improve catalytic oxidation efficiency effect

Active Publication Date: 2020-09-18
HUAZHONG UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] In view of the above defects or improvement needs of the prior art, the present invention provides a method for the catalytic oxidation treatment of organic wastewater by a two-phase oxidant system, the purpose of which is to use a hydrotalcite structure quaternary catalyst loaded with transition metal oxides to synergistically activate the catalyst Gas-phase oxidant ozone and liquid-phase oxidant persulfate are used to treat organic wastewater through a two-phase oxidant catalytic system. Since the supported quaternary hydrotalcite structure catalyst has a good activation effect on the two-phase oxidant catalytic system, the present invention can adopt a one-step The simple operation process of the method achieves a high organic matter removal effect, thereby solving the technical problems of complicated operation and high cost in the prior art related to ozone oxidation treatment of wastewater

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  • Method for treating organic wastewater by catalytic oxidation of a two-phase oxidant system
  • Method for treating organic wastewater by catalytic oxidation of a two-phase oxidant system
  • Method for treating organic wastewater by catalytic oxidation of a two-phase oxidant system

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Effect test

Embodiment 1

[0053] Take 12mL of prepared ozone stock solution (13.5±0.5mg / L) in a brown sealed glass bottle, add 8mL of prepared 2,4-D stock solution (100ppm), add catalyst 3mg, PMS 2mM, let the mixture Stir at constant temperature at 25°C and react for 60 minutes. The degradation efficiencies of different catalysts for 2,4-D are shown in Table 1. The ozone stock solution adopts an ozone generator, and an ozone stream is passed into the water at a rate of 8 g / h for 8 to 10 minutes to obtain an ozone stock solution with a concentration of 13.5±0.5 mg / L.

[0054] It can be seen from Table 1 that the surface hydroxyl density of the LDH structure catalyst supporting transition metal oxide is high, and the reaction efficiency is also significantly enhanced. It can be seen from the table that the removal efficiency of organic matter is significantly enhanced by the LDH catalyst loaded with Cu and Co oxides. The LDH structure catalyst composed of MgAl greatly increases the surface hydroxyl den...

Embodiment 2

[0060] Using CuCoMgAl and FeCoMgAl catalysts with different transition metal ratios as heterogeneous catalysts, the experiment described in Example 1 was carried out, and the reaction time was 60 minutes. The degradation efficiencies of catalysts with different transition metal ratios to 2,4-D are shown in Table 2.

[0061] Table 2 The degradation efficiency of catalysts with different transition metal ratios to 2,4-D

[0062]

[0063] It can be seen from Table 2 that different transition metal ratios have a significant impact on the catalytic efficiency of the catalyst, but compared with the ternary and binary catalysts in Example 1, they all have better catalytic efficiency. It shows that the transition metal plays an important role in the catalytic activity of the catalyst, and the quaternary catalyst has a better catalytic effect than the ternary and binary catalysts.

Embodiment 3

[0065] On the basis of Example 1, the concentrations of the liquid-phase oxidant PMS and the gas-phase oxidant ozone were respectively changed, and 3 mg of the CuCoMgAl catalyst in Example 1 was added, and the reaction time was 60 minutes. The degradation efficiencies of 2,4-D with different concentrations of oxidants are shown in Table 3.

[0066] Table 3 Degradation efficiency of 2,4-D with different concentrations of oxidants

[0067]

[0068] It can be seen from Table 3 that the concentration of oxidant has a significant impact on the degradation efficiency of 2,4-D, but when the PMS concentration is above 1.5mM and the ozone concentration is above 11mg / L, a good treatment effect can be achieved, greatly reducing the response cost.

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Abstract

The invention belongs to the technical field of advanced oxidation technologies for treating wastewater, and particularly relates to a method for catalytic oxidation treatment of organic wastewater through a two-phase oxidant system. The organic wastewater is taken as a treatment object, a liquid-phase oxidant persulfate solution and a gas-phase oxidant ozone form the two-phase oxidant system, andthe efficient activation of the oxidants and the degradation of pollutants are achieved through a catalyst with a supported quaternary hydrotalcites structure; since the catalyst with the supported quaternary hydrotalcites structure has good catalytic performance for the two-phase oxidant, the actual wastewater treatment processes can be reduced, and a very high organic matter removal effect canbe achieved.

Description

technical field [0001] The invention belongs to the technical field of wastewater treatment by advanced oxidation technology, and more specifically relates to a method for catalytic oxidation treatment of organic wastewater by a two-phase oxidant system. Background technique [0002] Advanced oxidation technology (AOPs), because of its high-performance free radicals that can degrade persistent organic pollutants, has the characteristics of strong oxidation ability and fast reaction rate, and has remained popular in recent years. But at the same time, it also has some shortcomings. [0003] In the process of treating complex organic wastewater, a single treatment technology often has problems such as poor treatment effect and high cost. Some advanced oxidation technologies such as Fenton oxidation are greatly affected by the pH of wastewater, and supercritical water oxidation technology also has higher requirements on temperature and pressure. Therefore, different combinati...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/72C02F1/78C02F101/30
CPCC02F1/725C02F1/78C02F2101/30
Inventor 陈朱琦朱静怡王启亮周新全汪佳
Owner HUAZHONG UNIV OF SCI & TECH