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Electro-Fenton method for in-situ production of hydrogen peroxide or degradation of organic pollutants by composite cathode combining cathode aeration and cathode modification

A technology of organic pollutants and composite cathodes, applied in water pollutants, oxidized water/sewage treatment, water aeration, etc., can solve the problems of low hydrogen peroxide production and restricted applications, achieve good application prospects, save electric energy, and produce high rate effect

Pending Publication Date: 2022-01-07
BEIJING UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

It can be used as a cathode material for electro-Fenton technology, but the yield of hydrogen peroxide produced by electrocatalysis of graphite felt cathode material is not high, which restricts its application in electro-Fenton system. Another factor restricting the yield of hydrogen peroxide is the oxygen content of the cathode, oxygen It is difficult to reach the cathode in the solution due to the limitation of solubility and mass transfer diffusion. Therefore, a simple and cheap composite cathode is developed that can not only improve the electrocatalytic activity of graphite felt, but also reduce the mass transfer resistance of oxygen near the cathode. The production rate of Fenton's hydrogen peroxide is very important to promote its popularization and application in the degradation of organic wastewater

Method used

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  • Electro-Fenton method for in-situ production of hydrogen peroxide or degradation of organic pollutants by composite cathode combining cathode aeration and cathode modification
  • Electro-Fenton method for in-situ production of hydrogen peroxide or degradation of organic pollutants by composite cathode combining cathode aeration and cathode modification
  • Electro-Fenton method for in-situ production of hydrogen peroxide or degradation of organic pollutants by composite cathode combining cathode aeration and cathode modification

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0024] Example 1: Hydrogen peroxide yield experiment

[0025] Cut the graphite felt with a thickness of 5mm into a square with a size of 5cm×6cm, ultrasonically clean it with acetone for 30min to remove the surface stains on the graphite felt, and then ultrasonically clean it with deionized water three times to remove residual acetone; dry it in an oven at 80°C for 12h, Record as pre-treated graphite felt; weigh 0.2g conductive carbon black and dissolve it in 30ml deionized water, add 0.4ml polytetrafluoroethylene and ultrasonically mix it for 30min at the same time; impregnate the graphite felt pretreated with acetone and deionized water into In the above mixed solution, ultrasonically impregnate for 30 minutes, move into an oven and dry at 80° C. for 3 hours; finally, calcine at 360° C. for 1 hour in an air atmosphere, and store the prepared cathode in vacuum for future use. The prepared modified cathode is used for the cathode catalytic layer, the stainless steel mesh is th...

example 2

[0026] Example 2: Stability experiment of hydrogen peroxide produced by composite cathode

[0027] Cut the graphite felt with a thickness of 5mm into a square with a size of 5cm×6cm, ultrasonically clean it with acetone for 30min to remove the surface stains on the graphite felt, and then ultrasonically clean it with deionized water three times to remove residual acetone; dry it in an oven at 80°C for 12h, Record as pre-treated graphite felt; weigh 0.2g conductive carbon black and dissolve it in 30ml deionized water, add 0.4ml polytetrafluoroethylene and ultrasonically mix it for 30min at the same time; impregnate the graphite felt pretreated with acetone and deionized water into In the above mixed solution, ultrasonically impregnate for 30 minutes, move into an oven and dry at 80° C. for 3 hours; finally, calcine at 360° C. for 1 hour in an air atmosphere, and store the prepared cathode in vacuum for future use. The prepared modified cathode is used for the cathode catalytic ...

example 3

[0028] Example 3: Removal effect of composite cathode on FA simulated wastewater

[0029] Cut the graphite felt with a thickness of 5mm into a square with a size of 5cm×6cm, ultrasonically clean it with acetone for 30min to remove the surface stains on the graphite felt, and then ultrasonically clean it with deionized water three times to remove residual acetone; dry it in an oven at 80°C for 12h, Record as pre-treated graphite felt; weigh 0.2g conductive carbon black and dissolve it in 30ml deionized water, add 0.4ml polytetrafluoroethylene and ultrasonically mix it for 30min at the same time; impregnate the graphite felt pretreated with acetone and deionized water into In the above mixed solution, ultrasonically impregnate for 30 minutes, move into an oven and dry at 80° C. for 3 hours; finally, calcine at 360° C. for 1 hour in an air atmosphere, and store the prepared cathode in vacuum for future use. The prepared modified cathode is used for the cathode catalytic layer, th...

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Abstract

The invention relates to an electro-Fenton method for in-situ production of hydrogen peroxide or degradation of organic pollutants by a composite cathode combining cathode aeration and cathode modification. According to the invention, the composite cathode is composed of a catalysis layer, a conductive layer and an aeration layer, and can effectively improve the hydrogen peroxide yield or degrade the organic pollutant, wherein the cathode catalysis layer adopts a carbon black and polytetrafluoroethylene modified graphite felt cathode, the conductive layer is a metal plate or a metal porous plate, the aeration layer is a microporous aeration plate or a microporous aeration filter membrane, air or oxygen reaches the cathode catalysis layer through the microporous aeration plate or the microporous aeration filter membrane, and when a composite cathode catalysis layer uses 0.2 g of carbon black and 0.4 mL of polytetrafluoroethylene modified graphite felt, the accumulation amount of hydrogen peroxide can reach 492 mg / L in 120 min, and when the composite cathode is used for treating a fulvic acid solution, the fulvic acid removal rate is 85.37% in 30 min; the cathode modification and cathode aeration methods are simple; the preparation material of the modified cathode is low in price; the composite cathode is stable in property and long in service life; and the composite cathode is high in hydrogen peroxide yield and good in organic pollutant removal effect.

Description

technical field [0001] The invention relates to an electro-Fenton method for producing hydrogen peroxide in situ or degrading organic pollutants by a composite cathode combining cathode aeration and cathode modification, and belongs to the field of electrochemical water treatment. Background technique [0002] The rapid increase in the amount of urban garbage has made the treatment of landfill leachate an urgent problem to be solved. The nanofiltration membrane and reverse osmosis membrane technology is recommended as the advanced treatment process of landfill leachate, which has been adopted in a large number of landfills. Although membrane technology can remove most of the pollutants, it will produce about 20% to 30% of the membrane filtration concentrate, especially the nanofiltration membrane concentrate, which has high COD, large chroma, and poor biodegradability. A high concentration of refractory organic wastewater. The total dissolved organic matter in the concentr...

Claims

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Application Information

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IPC IPC(8): C02F1/467C02F1/72C02F7/00C02F101/30
CPCC02F1/4672C02F1/722C02F7/00C02F2305/026C02F2101/30Y02W10/10
Inventor 秦侠李廷慧
Owner BEIJING UNIV OF TECH