1. The utility model provides a need not to throw device of organic waste water of electro-Fenton treatment of adding medicament which characterized in that includes:

a reactor;

an anode positioned within the reactor;

the cathode assembly comprises a first cathode and a second cathode, and the first cathode and the second cathode are both positioned in the reactor;

and the positive electrode of the power supply is electrically connected with the anode, and the negative electrode of the power supply is electrically connected with the first cathode and the second cathode respectively.

2. The apparatus for electro-Fenton treatment of organic wastewater without adding chemicals according to claim 1, further comprising an aerator and an air pump, wherein the aerator is located at the bottom of the reactor, the air pump is located outside the reactor, and the air pump is communicated with the aerator.

3. The apparatus for electro-Fenton treatment of organic wastewater without adding chemicals according to claim 1, wherein a water inlet pipe is provided at one end of the reactor, and a water outlet pipe is provided at the other end of the reactor, and a water inlet pump is provided on the water inlet pipe.

4. The apparatus for electro-Fenton treatment of organic wastewater without dosing of chemicals according to claim 1, wherein said anode is one of a metal electrode, a boron doped diamond electrode, a graphite electrode or a dimensionally stable electrode.

5. The apparatus for electro-Fenton treatment of organic wastewater without dosing pharmaceutical agents of claim 1, wherein said first cathode is a carbon cloth electrode or a carbon cloth electrode with a PEDOT layer deposited on the surface; the second cathode is a stainless steel mesh.

6. The apparatus for electro-Fenton treatment of organic wastewater without dosing pharmaceutical agents of claim 1, wherein said first cathode and said second cathode are each in a roll shape.

7. A method for treating wastewater by using the device for treating organic wastewater by electro-Fenton without adding medicament according to any one of claims 1 to 6, which comprises the following steps:

adding organic wastewater to be treated into a reactor;

connecting the anode with the positive pole of a power supply, and respectively connecting the first cathode and the second cathode with the negative pole of the power supply;

controlling the voltage of the anode, the first electrode and the second electrode to electrolyze the organic wastewater;

wherein H is generated on the first cathode during electrolysis₂O₂A second cathode pair H₂O₂Carrying out activation H₂O₂OH is produced.

8. The method for treating wastewater by using an apparatus for electro-Fenton treatment of organic wastewater without adding chemical agent according to claim 7, wherein if the apparatus for electro-Fenton treatment of organic wastewater without adding chemical agent comprises an aerator and an air pump, the air pump is further started during the electrolysis process, and the air pump and the aerator are used for aerating the organic wastewater.

Background

With the development of industry, the variety and quantity of organic waste water are rapidly increased, and the organic components contained in the waste water are more and more complex. At present, although the biological method generally used for treating organic wastewater has low cost, the biological method has poor effect in the case of some organic pollutants which are difficult to biodegrade. The Fenton method is an advanced oxidation technology, and the generated hydroxyl radical (. OH) has strong oxidizability and can oxidize most organic matters to achieve the purpose of degradation.

In the conventional Fenton process, ferrous ions (Fe)²⁺) And hydrogen peroxide (H)₂O₂) The reaction generates hydroxyl radicals. In the actual operation process, ferrous ions and hydrogen peroxide are required to be continuously added to ensure the continuous reaction. This also involves problems with cost of chemicals, transportation and storage of hydrogen peroxide and secondary contamination of the effluent.

The generation of electro-fenton technology overcomes these problems to some extent, and its principle can be roughly divided into two categories: (1) the technology of continuously generating ferrous iron by reducing ferric iron through a cathode and activating the added hydrogen peroxide to generate free radicals reduces the dosage of an iron agent, but still depends on the addition of the hydrogen peroxide; (2) the other electro-Fenton technology utilizes oxygen reduction to continuously generate hydrogen peroxide in situ and generate hydroxyl radicals under the action of a catalyst so as to oxidize and decompose pollutants, and the electro-Fenton method still depends on added ferrous iron or ferrous iron released by a sacrificial anode and still has the problems of secondary pollution such as iron mud, effluent chromaticity and the like.

Therefore, how to realize the electro-Fenton technology without adding hydrogen peroxide and an iron agent and completely avoiding secondary pollution is still a great difficulty in the prior electro-Fenton technology.

Disclosure of Invention

In view of the above, the present invention provides an apparatus and a method for treating organic wastewater by electro-fenton without adding chemicals, so as to solve or partially solve the technical problems in the prior art.

In a first aspect, the present invention provides an apparatus for treating organic wastewater by electro-fenton without adding chemicals, comprising:

a reactor;

an anode positioned within the reactor;

the cathode assembly comprises a first cathode and a second cathode, and the first cathode and the second cathode are both positioned in the reactor;

and the positive electrode of the power supply is electrically connected with the anode, and the negative electrode of the power supply is electrically connected with the first cathode and the second cathode respectively.

Preferably, the device for treating organic wastewater by electro-fenton without adding a medicament further comprises an aerator and an air pump, wherein the aerator is positioned at the bottom of the reactor, the air pump is positioned outside the reactor, and the air pump is communicated with the aerator.

Preferably, need not to add the device of the organic waste water of electro-fenton treatment of medicament, reactor one end is equipped with the inlet tube, the other end is equipped with the outlet pipe, be equipped with the intake pump on the inlet tube.

Preferably, in the device for treating organic wastewater by electro-fenton without adding a medicament, the anode is one of a metal electrode, a boron-doped diamond electrode, a graphite electrode or a dimensionally stable electrode.

Preferably, in the device for treating organic wastewater by electro-fenton without adding chemicals, the first cathode is a carbon cloth electrode or a carbon cloth electrode with a PEDOT layer deposited on the surface; the second cathode is a stainless steel mesh.

Preferably, in the device for treating organic wastewater by electro-fenton without adding a chemical agent, the first cathode and the second cathode are both in a roll shape.

In a second aspect, the invention further provides a method for treating wastewater by using the device for treating organic wastewater by electro-fenton without adding a medicament, which comprises the following steps:

adding organic wastewater to be treated into a reactor;

connecting the anode with the positive pole of a power supply, and respectively connecting the first cathode and the second cathode with the negative pole of the power supply;

controlling the voltage of the anode, the first electrode and the second electrode to electrolyze the organic wastewater;

wherein H is generated on the first cathode during electrolysis₂O₂A second cathode pair H₂O₂Carrying out activation H₂O₂OH is produced.

Preferably, in the method for treating wastewater by using the device for treating organic wastewater by electro-fenton without adding a chemical, if the device for treating organic wastewater by electro-fenton without adding a chemical comprises an aerator and an air pump, the air pump is started in the electrolysis process, and the air pump and the aerator are used for aerating the organic wastewater.

Compared with the prior art, the device and the method for treating organic wastewater by electro-Fenton without adding medicament have the following beneficial effects:

(1) the device for treating organic wastewater by electro-Fenton without adding medicament comprises a first cathode and a second cathode, adopts a double-cathode structure and produces H₂O₂And activation of H₂O₂The task of producing OH is shared by different cathodes, has more pertinence and can improve the yield of H₂O₂And activation of H₂O₂The efficiency of producing OH is improved, and the degradation efficiency of the organic wastewater is further improved;

(2) according to the device for treating organic wastewater by electro-Fenton without adding medicament, the first cathode is a carbon cloth electrode or a carbon cloth electrode with a PEDOT layer deposited on the surface, oxygen can be reduced into hydrogen peroxide by two electronic ways through the cathode so as to achieve the purpose of in-situ generation, and the electrode has high specific surface area and adsorption sites, so that the oxygen utilization efficiency can be improved, and H can be increased₂O₂The yield of (a); the second cathode is made of stainless steel net for activating H₂O₂OH (hydroxyl free radical) is generated, and the generated OH has strong oxidizability and can oxidize and decompose organic pollutants in the wastewater, so that the aim of removing is fulfilled;

(3) the method for treating the organic wastewater by electro-Fenton adopts the device for treating the organic wastewater without adding the medicament to control the voltage or the current of the anode, the first electrode and the second electrode so as to carry out electrolytic treatment on the organic wastewater, and H is generated on the first cathode in the electrolytic process₂O₂Generating active H on the second cathode₂O₂The generated OH has strong oxidizability and can oxidize and decompose organic pollutants in the wastewater, thereby achieving the purpose of removing the pollutants in the organic wastewaterThe object of (a); the organic wastewater treatment method does not need to add medicament, and can continuously generate H in situ by only depending on electric power, oxygen and even air₂O₂OH is blended, the operation is simple, and the action condition is mild; the method for treating the organic wastewater does not need to add Fe serving as a catalyst of the traditional Fenton method²⁺And the effluent has no secondary pollution and no sludge amount, and is convenient to treat.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. It is obvious that the drawings in the following description are only some embodiments of the invention, and that for a person skilled in the art, other drawings can be derived from them without inventive effort.

FIG. 1 is a schematic structural diagram of an apparatus for electro-Fenton treatment of organic wastewater without adding chemicals according to one embodiment of the present invention;

FIG. 2 is a schematic view showing the structure of an apparatus for electro-Fenton treatment of organic wastewater without adding chemicals according to another embodiment of the present invention;

fig. 3 is a schematic structural diagram of the first cathode and the second cathode in roll shapes according to one embodiment of the present invention.

Detailed Description

In the following, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention.

The embodiment of the application provides a device that need not to add electro-fenton of medicament and handle organic waste water, as shown in fig. 1, includes:

a reactor 1;

an anode 2 located within the reactor 1;

the cathode assembly comprises a first cathode 3 and a second cathode 4, and the first cathode 3 and the second cathode 4 are both positioned in the reactor 1;

and a power supply 7, the anode of which is electrically connected with the anode 2, and the cathode of the power supply 7 is electrically connected with the first cathode 3 and the second cathode 4 respectively.

In the embodiment of the present application, the reactor 1 is a conventional reaction apparatus, and an anode 2, a first cathode 3, and a second cathode 4 are disposed in the reactor 1; the power supply is a direct current power supply and at least comprises a positive end and at least two negative ends, the anode 2 is connected with the positive end of the power supply, and the first cathode 3 and the second cathode 4 are respectively connected with the negative ends of the power supply.

In some embodiments, the reactor further comprises an aerator 5 and an air pump 6, wherein the aerator 5 is positioned at the bottom of the reactor 1, the air pump 6 is positioned outside the reactor 1, and the air pump 6 is communicated with the aerator 5. In the embodiment of the application, the aerator 6 is a necessary device for aeration and oxygenation, and can be specifically divided into an underwater aerator, and the underwater aerator mainly comprises a microporous aerator and a jet aerator; the air pump 6 is communicated with the aerator 5, and oxygen is generated after the air pump 6 works and is sprayed out for aeration through the aerator 5.

In some embodiments, as shown in fig. 2, the reactor 1 has a water inlet pipe 8 at one end and a water outlet pipe 10 at the other end, and the water inlet pipe 8 is provided with a water inlet pump 9.

In this application embodiment, through setting up inlet tube 8, set up intake pump 9 simultaneously on inlet tube 8, at the during operation, pending organic waste water passes through inlet tube 8 and goes into the electrolytic reaction in going into reactor 1 under the effect of intake pump 9, and the waste water after the electrolytic reaction is convenient for continuous production like this outside outlet pipe 10 discharge reactor 1.

In some embodiments, the anode is one of a metal electrode, a boron-doped diamond electrode, a graphite electrode, or a dimensionally stable electrode; specifically, the metal electrode may be a platinum electrode, the dimensionally stable electrode may be a DSA anode, and the DSA anode may be a dimensionally stable anode having a metal such as titanium or tantalum as a matrix and covered with a transition metal oxide film.

In some embodiments, the first cathode is a carbon cloth electrode (CC) or a carbon with a PEDOT layer deposited on the surfaceA cloth electrode (PEDOT/CC); the second cathode is a stainless steel mesh. Specifically, the PEDOT is poly 3, 4-ethylenedioxythiophene, and the PEDOT layer can be deposited on the surface of the carbon cloth in an electrochemical deposition mode. In the embodiment of the application, the first cathode is a carbon cloth electrode (CC) or a carbon cloth electrode (PEDOT/CC) with a PEDOT layer deposited on the surface, the cathode can reduce oxygen to hydrogen peroxide through two electron paths to achieve the purpose of in-situ generation, and the electrode has high specific surface area and adsorption sites, can improve oxygen utilization efficiency and increase H₂O₂The yield of (a); the second cathode is made of stainless steel net for activating H₂O₂OH (hydroxyl radical) is generated, and the generated OH has strong oxidizability and can oxidize and decompose organic pollutants in the wastewater, thereby achieving the aim of removing.

Specifically, the reaction occurring at the first cathode is: o is₂+2H⁺+2e^-→H₂O₂

The reaction taking place at the second cathode is: h₂O₂+e^-→·OH+OH^-。

Specifically, in some embodiments, a carbon cloth electrode (PEDOT/CC) with a PEDOT layer deposited on the surface thereof is prepared by:

a1, soaking the carbon cloth in a nitric acid solution with the mass fraction of 60-68% for 2-4 hours to improve the hydrophilicity of the carbon cloth and remove impurities on the surface of the carbon cloth;

a2, placing the carbon cloth in 50-60% ethanol water solution for ultrasonic treatment for 10-20 min, and then drying;

a3, 0.1-0.2 mol/L LiClO₄And taking an acetonitrile solution of 0.01-0.03 mol/L of EDOT (3, 4-ethylenedioxythiophene) monomer as an electrolyte, taking carbon cloth as a working electrode, taking a Pt electrode as a counter electrode, taking a silver/silver chloride electrode as a reference electrode, and carrying out constant potential electrodeposition by adopting a three-electrode system, wherein the potential of the working electrode is set to be 1.2V, and the deposition time is set to be 200s, so that the carbon cloth electrode (PEDOT/CC) with the PEDOT layer deposited on the surface is prepared.

In some embodiments, as shown in fig. 3, the first cathode and the second cathode are both in the shape of a roll. In the embodiment of the application, the first cathode and the second cathode are both in a coiled roll shape, the surface area of the electrodes is enlarged, the volume is not increased, and the gas diffusion effect and the contact area with water flow can be well enhanced. It is understood that the electrode in the embodiment of the present application has a roll shape, that is, the electrode is wound like roll paper.

Specifically, in some embodiments, the first cathode and the second cathode are rolled for 5-6 layers, and after the first cathode and the second cathode are rolled, as shown in fig. 3, when viewed from the cross section of the cathode, the inner diameter is 0.4-0.6 cm, the distance between layers is 0.2-0.3 cm, and the outer diameter is 3-4 cm. Based on the same inventive concept, the embodiment of the application also provides a method for treating wastewater by using the device for treating organic wastewater by electro-Fenton without adding a medicament, which comprises the following steps:

s1, adding organic wastewater to be treated into the reactor;

s2, connecting the anode with the positive pole of a power supply, and respectively connecting the first cathode and the second cathode with the negative pole of the power supply;

s3, controlling the voltage of the anode, the first electrode and the second electrode, and electrolyzing the organic wastewater;

wherein H is generated on the first cathode during electrolysis₂O₂Wherein H is generated on the first cathode during electrolysis₂O₂A second cathode pair H₂O₂Carrying out activation H₂O₂OH is produced.

It should be noted that, the organic wastewater treatment method provided by the embodiment of the present application adopts the above device for treating organic wastewater without adding chemical agent, specifically, the organic wastewater to be treated is added into a reactor, then the anode is connected to the positive electrode of a power supply, the first cathode and the second cathode are respectively connected to the negative electrode of the power supply, and the voltage or current of the anode, the first electrode and the second electrode is controlled according to the condition of the pollutants in the organic wastewater, so as to perform electrolytic treatment on the organic wastewater, and during the electrolytic process, H is generated on the first cathode₂O₂Generating active H on the second cathode₂O₂OH, the generated OH has strong oxidizing property and can be oxidized and decomposedOrganic pollutants in the wastewater, thereby achieving the purpose of removing the pollutants in the organic wastewater. The organic wastewater treatment method does not need to add medicament, and can continuously generate H in situ by only depending on electric power, oxygen and even air₂O₂OH is blended, the operation is simple, and the action condition is mild; the method for treating the organic wastewater does not need to add Fe serving as a catalyst of the traditional Fenton method²⁺The effluent has no secondary pollution and no sludge amount, and is convenient to treat; this application uses a double cathode structure to produce H₂O₂And activation of H₂O₂The task of producing OH is shared by different cathodes, has more pertinence and can improve the yield of H₂O₂And activation of H₂O₂Efficiency of OH production.

In some embodiments, if the device for treating organic wastewater by electro-Fenton without adding a chemical agent comprises an aerator and an air pump, the air pump is also started during the electrolysis process, and the air pump and the aerator are used for aerating the organic wastewater. In practice, the flow rate is controlled to be 40-80 ml/min by using an air pump, and then the aeration rate is controlled.

In some embodiments, if the device for treating organic wastewater by electro-fenton without adding a chemical comprises a water inlet pipe, a water outlet pipe and a water inlet pump, the water inlet pump is started, organic wastewater to be treated is pumped into the reactor through the water inlet pipe, the treated wastewater is discharged through the water outlet pipe, and the flow of the organic wastewater entering the reactor can be controlled through the water inlet pump.

The method for treating organic wastewater by electro-Fenton according to the present application is further described below with reference to specific examples.

Example 1

The embodiment of the application provides a method for treating organic wastewater by electro-Fenton, which adopts a device shown in the attached figure 1, and comprises the following steps:

s1, adding organic wastewater into the reactor;

s2, connecting the anode with the positive pole of a power supply, and respectively connecting the first cathode and the second cathode with the negative pole of the power supply;

s3, controlling the voltage of the anode, the first electrode and the second electrode, and electrolyzing the organic wastewater;

wherein the anode is a platinum electrode, the first electrode is Carbon Cloth (CC), and the second cathode is a stainless steel mesh (type 304); the organic wastewater is 50ml of 0.05mol/L sodium sulfate solution, and the sodium sulfate solution contains 50mg/L rhodamine B; adjusting the pH value of the organic wastewater to 3 before electrolysis, controlling the first cathode voltage to be-0.9V and the second cathode voltage to be-0.8V during electrolysis, controlling the anode voltage to be 1.9V, starting an air pump during electrolysis, aerating the organic wastewater by an aerator, and controlling the aeration flow to be 50ml/min by the air pump.

The method for treating organic wastewater in example 1 was tested for rhodamine B decolorization rate and solution COD degradation rate within 120min of electrolysis, and the results are shown in table 1 below.

The rhodamine B decolorization rate detection method comprises the steps of sampling at a specific time point and measuring absorbance by adopting an ultraviolet spectrophotometer. The maximum absorption wavelength of rhodamine B is 552nm, and specifically, the target pollutant decolorization rate is calculated by adopting the following formula: decolorization ratio ═ A₀-A_t)/A₀100%, wherein: a. the₀Initial absorbance value, A_t-the absorbance value at the reaction time t.

According to GB11917-89, the method for determining COD is characterized by sampling at a specific time point according to the bichromate method for determining chemical oxygen demand of water quality, adding 0.025mol/L potassium bichromate, heating and refluxing by using a digestion instrument, adding ammonium ferrous sulfate standard solution for back dripping, and adopting the following calculation formula: COD (mg/L) ═ c (V)₁-V₂)*8000/V₀In the formula: c-ammonium ferrous sulfate standard titration solution concentration (mol/L), V₁Volume of ferrous ammonium sulfate standard titration solution consumed in blank experiments (ml), V₂Volume of ferrous ammonium sulfate standard titration solution consumed by the sample (ml), V₀Sample volume (ml), COD degradation rate calculation formula as follows: COD degradation rate (COD)₀-COD_t)/COD₀100%, wherein: COD₀Initial COD concentration, COD_tCOD concentration at reaction time t.

TABLE 1 rhodamine B decolorization and solution COD degradation for different electrolysis times

Example 2

The embodiment of the application provides a method for treating organic wastewater by electro-Fenton, which is the same as the embodiment 1, except that the first cathode is selected from carbon cloth (PEDOT/CC) with PEDOT growing on the surface, and the rest process conditions are the same as the embodiment 1. The preparation method of the first cathode specifically comprises the following steps: a1, soaking the carbon cloth in a nitric acid solution with the mass fraction of 65% for 2 h;

a2, placing the carbon cloth in 55% ethanol water solution by mass percent, carrying out ultrasonic treatment for 10min, and then drying;

a3, LiClO dissolved with 0.1mol/L₄And 0.01mol/L of EDOT monomer is used as electrolyte, carbon cloth is used as a working electrode, a Pt electrode is used as a counter electrode, a silver/silver chloride electrode is used as a reference electrode, a three-electrode system is adopted for constant potential electrodeposition, the potential of the working electrode is set to be 1.2V, and the deposition time is 200s, so that the carbon cloth electrode (PEDOT/CC) with the PEDOT layer deposited on the surface is prepared.

The method for treating organic wastewater in example 2 was tested for rhodamine B decolorization rate and solution COD degradation rate within 120min of electrolysis, and the results are shown in table 2 below.

TABLE 2 rhodamine B decolorization ratio and solution COD degradation ratio at different electrolysis times

Electrolysis time/min	Rhodamine B decolorization%	COD degradation/The
			10	42.901	13.504
20	72.939	20.761
			40	94.985	35.912
60	97.964	42.335
			90	99.255	60.312
120	99.702	78.816

Example 3

The embodiment of the application provides a method for treating organic wastewater by electro-Fenton, which adopts a device shown in the attached figure 2, and comprises the following steps:

s1, adding 30ml of organic wastewater into a reactor with the volume of 50 ml;

s2, connecting the anode with the positive pole of a power supply, and respectively connecting the first cathode and the second cathode with the negative pole of the power supply;

s3, controlling the voltage of the first electrode to be-0.9V and the voltage of the second electrode to be-0.8V, adding organic wastewater into the water inlet pipe, controlling the water inlet speed to be 1ml/min, electrolyzing the organic wastewater, and controlling the hydraulic retention time to be 50 min;

wherein the anode is a platinum electrode, the first electrode is a carbon cloth (PEDOT/CC) with PEDOT growing on the surface, and the second cathode is a stainless steel net (type 304); the organic wastewater is a sodium sulfate solution of 0.05mol/L, and the sodium sulfate solution contains 50mg/L rhodamine B; adjusting the pH value of the organic wastewater to 3 before electrolysis, starting an air pump during electrolysis, and aerating the organic wastewater by using an aerator.

The method for treating organic wastewater in example 3 was tested for rhodamine B decolorization rate and solution COD degradation rate within 120min of electrolysis, and the results are shown in table 3 below.

TABLE 3 rhodamine B decolorization ratio and solution COD degradation ratio at different electrolysis times

Electrolysis time/min	Rhodamine B decolorization%	COD degradation/The
			10	55.625	18.306
20	73.979	26.578
			40	71.273	34.657
60	67.067	40.157
			90	68.027	40.876
120	67.959	39.744

Example 4

The embodiment of the application provides a method for treating organic wastewater by electro-Fenton, which is the same as the embodiment 3 except that the first cathode and the second cathode are both in a roll shape as shown in FIG. 3, and the rest of the process conditions are the same as the embodiment 3. Specifically, the first cathode and the second cathode are coiled for 6 layers during the experiment, the inner diameter is about 0.5cm, the outer diameter is about 3cm, and the distance between each layer is about 0.3 cm.

The method for treating organic wastewater in example 4 was tested for rhodamine B decolorization rate and solution COD degradation rate within 120min of electrolysis, and the results are shown in table 4 below.

TABLE 4 rhodamine B decolorization ratio and solution COD degradation ratio at different electrolysis times

Example 5

The embodiment of the application provides a method for treating organic wastewater by electro-Fenton, which is the same as the embodiment 4, and is different from the embodiment 4 in that the organic wastewater is a 0.05mol/L sodium sulfate solution, the sodium sulfate solution contains 50mg/L atrazine, and other process conditions are the same as the embodiment 4.

The atrazine degradation rate and the solution COD degradation rate of the treatment method of organic wastewater in example 5 were tested within 120min of electrolysis, and the results are shown in table 5 below.

Wherein, the atrazine degradation rate is to determine the concentration by using a high performance liquid chromatography, sample at a specific time point, extract the atrazine in water by using trichloromethane, concentrate and determine the volume by using a high performance liquid chromatograph. The atrazine degradation rate is calculated by using the following formula: (c) degradation rate₀-c_t)/c₀100%, wherein: c. C₀-initial atrazine concentration; c. C_tAtrazine concentration at the reaction time t.

TABLE 5 atrazine degradation rate and solution COD degradation rate at different electrolysis times

Electrolysis time/min	Atrazine degradation rate/%)	COD degradation/The
			10	20.987	10.654
20	35.498	27.141
			40	53.697	40.215
60	65.489	42.556
			90	66.352	43.102
120	64.897	42.501

Example 6

Adding water into a reactor of the device for treating organic wastewater by electro-Fenton without adding a medicament shown in the attached drawing 1, starting an air pump, and aerating the organic wastewater by using an aerator, wherein a first electrode is carbon cloth (PEDOT/CC) with PEDOT growing on the surface, an anode is a platinum electrode, the anode is connected with a power supply anode, a first cathode is connected with a power supply cathode, the first cathode is controlled to electrolyze water under different voltages, and the hydrogen peroxide concentration and the current efficiency of the first cathode under different voltages are measured. Specifically, the method measures H at the maximum absorbance of 400 nm by using a titanium potassium oxalate spectrophotometry₂O₂The concentration of (A) is measured by sampling H produced during the reaction at different times₂O₂Concentrations, as shown in table 6.

TABLE 6 hydrogen peroxide concentration and Current efficiency at different voltages

voltage/V	Hydrogen peroxide concentration/mg.L-1	Current efficiency/%)
			-1.0	140.042	35.632
-0.9	243.067	77.011
			-0.8	216.307	73.914
-0.7	173.715	88.677

As can be seen from Table 6, H₂O₂The concentration increases and then decreases along with the voltage increase, the maximum hydrogen peroxide concentration is reached when the voltage of the first cathode is-0.9V, and the current efficiency can reach more than 75 percent.

As can be seen from the comparison of tables 1-2, the carbon cloth (PEDOT/CC) with PEDOT growing on the surface is selected as the first cathode in example 2, and the degradation effect on rhodamine B is better. As can be seen from the comparison of tables 1-2, the carbon cloth (PEDOT/CC) with PEDOT grown on the surface is selected as the first cathode in example 2, and the effect of degrading COD is better.

As can be seen from the comparison of tables 3 to 4, the carbon cloth (PEDOT/CC) with the wound roll shape and the PEDOT growing on the surface is selected as the first cathode in the embodiment 4, so that the degradation effect on rhodamine B is better.

As can be seen from the comparison in tables 3 to 4, the carbon cloth (PEDOT/CC) having PEDOT grown on the surface thereof in the roll shape was selected as the first cathode in example 4, and the effect of COD degradation was better.

The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.