CN206940627U - A kind of electric Fenton water treatment facilities - Google Patents
A kind of electric Fenton water treatment facilities Download PDFInfo
- Publication number
- CN206940627U CN206940627U CN201720610850.2U CN201720610850U CN206940627U CN 206940627 U CN206940627 U CN 206940627U CN 201720610850 U CN201720610850 U CN 201720610850U CN 206940627 U CN206940627 U CN 206940627U
- Authority
- CN
- China
- Prior art keywords
- electrolytic cell
- fenton
- water treatment
- treatment facilities
- negative electrode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses a kind of electric Fenton water treatment facilities, including housing, in the electrolytic cell of enclosure interior, the Fenton reactor being connected with electrolytic cell, three parallel relative electrodes are provided with electrolytic cell, the first anode and second plate are helicoidal structure, negative electrode is loose structure, the negative electrode includes graphite cake, it is arranged on graphite cake both sides and the adsorption layer being connected with graphite cake, temperature sensor is provided with the Fenton reactor, temperature controller, the hull outside is provided with water pump, control module, the signal input part of the iron ion sensor signal output end and control module that are arranged on water outlet connects, the water pump signal input is connected with control module signal output part.The utility model uses said structure, and caused sediment will not pollute solution in electrolytic cell after reaction, while carry out detection in real time and regulation and control in time to iron concentration after solution temperature and reaction.
Description
Technical field
The invention belongs to sewage disposal technology, and in particular to a kind of fragrant degree water treatment facilities of electricity.
Background technology
The annual environmental aspect publication issued according to State Environmental Protection Administration, China's total amount of sewage discharge in 2011 are 659.2
Hundred million tons, wherein discharged volume of industrial waste water is 230.9 hundred million tons.Wherein textile industry/printing and dyeing class waste water year yield is about 2,500,000,000 tons, work
The sludge of industry discharge of wastewater also reaches ten million ton every year.Due to containing fibrous raw material entrainment in itself and adding in dyeing waste water
Slurry, finish, dyestuff and chemical assistant for being used during work etc. so that dyeing waste water has COD height, colourity deep, difficult biological
The features such as degraded and component, physicochemical property change more.
In sewage disposal technology, the most significant feature of advanced oxidation water process is can to produce hydroxyl radical free radical（•OH）, by
There is high oxidizing potential in OH, can be with the organic pollution in waste water without quick chain reaction selectively occurs, by difficulty
The larger molecular organicses of biochemical degradation are converted into the micromolecular compound of bio-degradable, or even are finally broken down into CO2、H2O etc.
Simple inorganic molecule, so as to be greatly enhanced the biodegradability of bio-refractory waste water or realize directly degraded.Wherein, Fenton
Oxidation technology is the efficient water technology that a kind of Quick Oxidation removes removal organic polluter, is with a wide range of applications.Use iron
Plate or steel plate do sacrificial anode, under electric field action, Anodic Stripping Fe2+；O2In negative electrode（Oxygen diffusion cathode）Upper generation bielectron
Reduction reaction（In acid condition）Generate H2O2.Fenton reagent reaction, H are produced in solution2O2It is catalytically decomposed as OH, Fe2+
It is oxidized to Fe3+ .Conventional electrolysis product is the alternate vertical plate structure of multigroup both positive and negative polarity, the upper and lower baffling of solution or level
Staggeredly baffling, anode all use iron anode so that the iron ion inside solution increases, and it is anti-Fenton to occur immediately in electrolytic cell
Should, caused sediment can pollute electrolytic cell, be unfavorable for sewage disposal.In addition, the catalyst in Fenton's reaction in solution needs
To carry out at a suitable temperature.
Administer at present in place of some equal Shortcomings of solution method and apparatus of high-concentration hardly-degradable dyeing waste water, and face to face
When facing combined pollution, lack systematicness, the solution and technical equipment of relevance.
Utility model content
The invention provides a kind of electric Fenton water treatment facilities, solves multi-group electrode plate sun in existing electric Fenton water process
Effect is poor at pole, the alternate constitution water of negative electrode, and iron concentration can not be real in the solution temperature and solution in water treatment procedure
When the problem of being monitored and controlled, it is right by Fenton's reaction process lasting in electrolyzer electric chemical reaction and Fenton reactor
Sewage is pre-processed.Meanwhile the temperature of solution and the situation of water process are carried out by temperature controller, control module real-time
Monitoring.
The present invention to achieve the above object, adopts the following technical scheme that：A kind of electric Fenton water treatment facilities, including housing,
It is characterized in that the electrolytic cell being connected with water inlet, the Fenton reactor being connected with electrolytic cell, institute are provided with the housing
Fenton reactor is stated to be connected with delivery port, be provided with the electrolytic cell three it is parallel relative and mutually hung down with solution flow direction
Straight electrode, the electrode sequentially consist of the first anode, negative electrode, second plate, the first anode and second plate
Be helicoidal structure, the negative electrode is loose structure and to be connected with the negative pole of two dc sources, the first anode and its
In dc source positive pole connection, the second plate is connected with the positive pole of another dc source, and the negative electrode includes
Graphite cake, graphite cake both sides and the adsorption layer being connected with graphite cake are arranged on, temperature biography is provided with the Fenton reactor
Sensor, the temperature controller for being connected with sensor signal output end and being regulated and controled to solution temperature, the hull outside are set
Water pump, control module are equipped with, the signal of the iron ion sensor signal output end and control module that are arranged on water outlet inputs
End connection, the water pump signal input are connected with control module signal output part.
The Fenton reactor is provided with permeable membrane above electrolytic cell between the Fenton reactor and electrolytic cell.
The electrode is vertical with housing sidewall to be fixedly connected, and the distance between described two adjacent electrodes are identical.
The first anode is located at bottom of electrolytic tank, negative electrode is located in the middle part of electrolytic cell, second plate is located at upper part of the electrolytic cell.
The first anode includes stud, and the surface of the stud includes tin, antimony, iridium, the compound of platinum coated with one layer
Coating.
The second plate is iron electrode.
The thickness of the negative electrode is 100mm.
The adsorption layer is alveolate texture of the surface by the coating processing of tetrafluoroethene point-like.
The filler of supplement iron ion is placed with Fenton reactor.
Housing bottom is provided with the aerating system that blower fan provides source of oxygen for negative electrode, and the blower fan is arranged on housing
Outside.
The present invention compared with prior art, has advantages below and beneficial effect：
Compared with prior art, the present invention is simple in construction, and water treatment efficiency is notable.With traditional motor product structure not
Together, the present invention uses three electrodes, two anodes and a negative electrode, can be right respectively by the circuit design of three electrode dual power supplies
Two groups of pole plates carry out voltage, current regulation, effectively control Fe2+With H2O2Concentration and yield, required for obtaining Fenton's reaction
Optimum proportioning；Anode is helical structure, and negative electrode is loose structure, and the design of three electrodes makes reactant（Such as organic molecule,
Oxygen molecule etc.）Electrode surface is easily contacted, and then improves reaction probabilities and water treatment efficiency；Extending cathode thickness reaches
100mm, cathode area is considerably increased, there is very high electrochemistry formated H2O2, while the surface of negative electrode is through polytetrafluoroethylene (PTFE)
Point-like coating handle, make its loose structure surface formed water-repellent layer, formed in this region this region formed profuse solid-liquid-
Gas three phase boundary, make a large amount of oxygen molecule absorption in population cathode surface；The first anode is titanium-based layer anode, organic in waste water
Thing pollutes molecule by anode direct electrochemical oxidation, improves electric Fenton device treatment effeciency；Between electrolytic cell and Fenton reactor
Permeable membrane is provided with, is that sediment precipitates without the electrode in contaminated electrode groove in the reactor；Control module, temperature inductor
And temperature controller, implementing monitoring and adjustment are carried out to solution temperature, in addition, iron ion inductor and water pump, can detect water
The situation of processing, according to iron concentration situation, the water of water outlet is flowed back into electrolytic cell by water pump, by flowing back,
Treatment effeciency is improved, big yield additionally aids the suspension and renewal electrode surface taken away in reactor, prevents equipment from blocking.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model.
Wherein：1st, housing, 2, electrolytic cell, 3, Fenton reactor, 4, the first anode, 5, second plate, 6, negative electrode, 7, infiltration
Film, 8, water inlet, 9, delivery port.
Embodiment
In order to make the purpose , technical scheme and advantage of the present invention be clearer, it is right below in conjunction with drawings and Examples
The present invention is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, and
It is not used in the restriction present invention.
As shown in figure 1, a kind of electric Fenton water treatment facilities, including housing, it is provided with what is be connected with water inlet in housing
Electrolytic cell, the Fenton reactor being connected with delivery port, electrolytic cell are connected with Fenton reactor, and housing bottom is provided with aeration system
System, aerating system are connected with water inlet, and aerating system includes providing the source of oxygen needed by external fan for negative electrode.Fenton is anti-
Device is answered in the top of electrolytic cell, and permeable membrane is provided between electrolytic cell and Fenton reactor.The function of electrolytic cell is electrification
Learn and produce Fe2+And H2O2, the function of Fenton reactor is to carry out lasting Fenton's reaction.Electrolytic cell can set multigroup, cooperation
Fenton reactor uses.
Three parallel relative electrodes are provided with electrolytic cell, electrode and the direction that solution in electrolytic cell flows are perpendicular,
Electrode is sequentially consisted of in the first anode of bottom of electrolytic tank, the in a cell negative electrode in portion, in upper part of the electrolytic cell
Two anodes.Three electrodes are vertical with housing sidewall to be fixedly connected, and the distance between adjacent electrode is identical.Two anodes are set
It is set to and obtains higher H2O2Yield, but if two anodes use iron plate, it will produce two problems：First, Fe2+It is excessive；Two
It is to produce Fenton's reaction immediately in electrolytic cell, Fe2+Fe is converted into quickly3+, three dimensional particles group's negative electrode is polluted, reduces reaction
Efficiency, to a large amount of iron cements are brought in electrolytic cell, excessive, the too fast loss that results in blockage with anode.Therefore second plate is iron sun
Pole, the first anode are titanium-based layer anode, and stud surface is coated with more kinds of catalysis oxygen of the Sn-Sb-Ir-Ta with high oxygen separated overpotential
Change matter coatings, under electric field action, its surface produces great amount of hydroxy group free radical（•OH）, the organic pollutant molecule in waste water
Direct electrochemical oxidation and the degradation reaction by hydroxyl radical free radical indirect oxidation occurs in anode surface.Negative electrode is by porous graphite plate
Formed with the adsorption layer that porous graphite plate both sides are connected with graphite cake is arranged on, adsorption layer is surface by the painting of tetrafluoroethene point-like
The alveolate texture of processing is applied, adsorption layer is closely connected with graphite cake, forms extending cathode, and extension thickness reaches 100mm, greatly
Cathode area is increased, there is very high electrochemistry formated H2O2Efficiency.
The operating current of three electrodes is provided by two dc sources, and negative electrode is connected with the negative pole of two dc sources, the
One anode is connected with the positive pole of one of dc source, and second plate is connected with the positive pole of another dc source.Two sun
Extremely helicoidal structure, negative electrode are that loose structure, helical structure and loose structure have bigger surface area than slab construction, with
Water engaging surface product increase.By the circuit design of three electrode dual power supplies, voltage, current regulation can be carried out to two groups of pole plates respectively,
Effectively control Fe2+With H2O2Concentration and yield, to obtain the optimum proportioning required for Fenton's reaction.Regulation input three dimensional particles
The total current of group's extending cathode, can obtain the H for meeting water process requirement in the solution2O2；By adjusting on input iron anode
Electric current, the H for meeting water process requirement can be obtained in the solution2O2With Fe2+Solubility ratio.Typically require H2O2With Fe2+ The ratio between
More than 1.5（Mol ratio）, therefore the current requirements on iron anode are less than the total current on negative electrode.Traditional Fenton's reaction due to
FeSO4It is disposable it is excessive add, excessive Fe2+Fe is oxidized to quickly3+, sludge quantity and solution colourity are added, and can not
Ensure the lasting generation of Fenton reagent so that reaction efficiency is low, and the present apparatus overcomes this drawback, sustainable generation Fe2+。
Be provided with Fenton reactor temperature sensor, the temperature controller that solution temperature is adjusted, supplement iron from
The filler of son, the hull outside are provided with water pump, control module, are arranged on the iron ion sensor signal output of water outlet
End is connected with the signal input part of control module, and water pump signal input is connected with control module signal output part.TEMP
Device is monitored in real time to solution temperature, and when solution temperature is less than optimal reaction temperature, temperature controller adds to solution
Heat treatment；When solution temperature is higher than optimal reaction temperature, temperature controller carries out cooling processing to solution, allows solution temperature to begin
Optimum temperature range is maintained at eventually, and the activity of catalyst is optimal.The iron ion sensor of water outlet can detect reaction after it is molten
Iron concentration in liquid, the water that Fenton reactor comes out realize a large amount of backflows by water pump.Control module is according to iron concentration
The capacity of returns of water pump is controlled, backflow can make the Fe formed after Fenton's reaction3+Fe is reduced in negative electrode2+, while unreacted is complete
Oxidant by backflow, can improve water treatment efficiency, a large amount of water are also helped with anti-with the waste water fast reaction just entered
The suspension in device is answered, electrode surface is updated, prevents equipment from blocking.
Fenton water process can combine with plasma water processing, and plasma water process is to utilize nanosecond first（ns）Pulse is situated between
Matter barrier discharge, produce room-temperature plasma.Because ns rising edge of a pulses are precipitous, in ns magnitudes（Pulsewidth stage discharge off electricity
Stream）, only transient current will not produce substantial amounts of heat, can form room-temperature plasma, produce mass efficient active material
Reduce energy consumption again simultaneously.In order to control active principle caused by chain reaction, by adjusting the air humidity of discharge gas,
I.e. control enters the amount of hydrone in discharge gas, to improve OH and H2O2Yield and the efficiency of processing.
For the first anode under electric field action, surface produces great amount of hydroxy group free radical, after waste water is from water inlet into electrolytic cell,
Organic pollutant molecule occurs on first anode surface first to be reacted by anode direct electrochemical oxidation and by between hydroxyl radical free radical
The degradation reaction of oxidation is connect, cathode porous body structure surface enters polytetrafluoroethylene (PTFE) point-like coating processing and forms water-repellent layer, and work is herein
Region forms extremely abundant solid-liquid-gas-three phase boundary, makes substantial amounts of oxygen molecule absorption in the adsorption layer table of population negative electrode
Face, the electronics of external circuit offer is provided, oxygen molecule is electrochemically reduced to H202 .Meanwhile hydrone occurs for the first anode
The side reaction for producing oxygen is decomposed by anode electrochemical, oxygen caused by side reaction is upward together with air stream, cloudy into extension
Pole reaction zone.Fe caused by the first anode2+Electrolytic cell is left, into Fenton reactor, avoids Fe caused by Fenton's reaction3+
Precipitation is produced in electrolytic cell.Fenton's reaction needs the regular hour, and Fenton reactor can ensure the time that reaction needs, Fenton production
Raw Fe (OH)3, Fe (OH)3Sludge caused by flocculation precipitates separation in deep reaction device, will not pollute electrolytic tank electrode, together
When, the filler of Fenton reactor kind placement, persistently supplement Fe2+, make the high-efficiency continuous progress of reaction.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
All any modification, equivalent and improvement made within the spirit and principle of utility model etc., should be included in the utility model
Protection domain within.
Claims (10)
1. a kind of electric Fenton water treatment facilities, including housing, it is characterised in that be provided with the housing and be connected with water inlet
Electrolytic cell, the Fenton reactor that is connected with electrolytic cell, the Fenton reactor is connected with delivery port, set in the electrolytic cell
Have three parallel relative and electrodes perpendicular with solution flow direction, the electrode sequentially consist of the first anode,
Negative electrode, second plate, the first anode and second plate are helicoidal structure, the negative electrode be loose structure and with two
The negative pole connection of dc source, the first anode be connected with the positive pole of one of dc source, the second plate and separately
The positive pole connection of one dc source, the negative electrode include graphite cake, are arranged on graphite cake both sides and the suction being connected with graphite cake
Attached layer, temperature sensor is provided with the Fenton reactor, is connected with sensor signal output end and solution temperature is entered
The temperature controller of row regulation and control, the hull outside are provided with water pump, control module, are arranged on the iron ion sensing of water outlet
Device signal output part and the signal input part of control module connect, the water pump signal input and control module signal output part
Connection.
2. a kind of electric Fenton water treatment facilities according to claim 1, it is characterised in that the Fenton reactor is being electrolysed
Above groove, permeable membrane is provided between the Fenton reactor and electrolytic cell.
3. a kind of electric Fenton water treatment facilities according to claim 1, it is characterised in that the electrode hangs down with housing sidewall
Directly it is fixedly connected, the distance between described two adjacent electrodes are identical.
4. a kind of electric Fenton water treatment facilities according to claim 3, it is characterised in that the first anode is positioned at electrolysis
Trench bottom, negative electrode are located in the middle part of electrolytic cell, second plate is located at upper part of the electrolytic cell.
A kind of 5. electric Fenton water treatment facilities according to claim 4, it is characterised in that the first anode includes stud,
The surface of the stud is coated with one layer of compound coat for including tin, antimony, iridium, platinum.
6. a kind of electric Fenton water treatment facilities according to claim 4, it is characterised in that the second plate is iron electrode.
7. a kind of electric Fenton water treatment facilities according to claim 4, it is characterised in that the thickness of the negative electrode is
100mm。
8. a kind of electric Fenton water treatment facilities according to claim 1, it is characterised in that the adsorption layer passes through for surface
The alveolate texture of tetrafluoroethene point-like coating processing.
9. a kind of electric Fenton water treatment facilities according to claim 1, it is characterised in that benefit is placed with Fenton reactor
Fill the filler of iron ion.
10. a kind of electric Fenton water treatment facilities according to claim 1, it is characterised in that be provided with housing bottom
Blower fan provides the aerating system of source of oxygen for negative electrode, and the blower fan is arranged on outside housing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720610850.2U CN206940627U (en) | 2017-05-27 | 2017-05-27 | A kind of electric Fenton water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720610850.2U CN206940627U (en) | 2017-05-27 | 2017-05-27 | A kind of electric Fenton water treatment facilities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206940627U true CN206940627U (en) | 2018-01-30 |
Family
ID=61362499
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720610850.2U Active CN206940627U (en) | 2017-05-27 | 2017-05-27 | A kind of electric Fenton water treatment facilities |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206940627U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108439671A (en) * | 2018-05-16 | 2018-08-24 | 武汉轻工大学 | A kind of electric Fenton of photovoltaic driving is from the system of maintenance and the method for aniline degradation waste water |
| CN110190520A (en) * | 2019-05-06 | 2019-08-30 | 邱庆彬 | A kind of nanometer water ion generating device |
| CN113149150A (en) * | 2021-04-25 | 2021-07-23 | 中国地质大学（武汉） | Activated carbon cathode electro-Fenton system and method for removing underground water halogenated hydrocarbons by using same |
| CN113828631A (en) * | 2021-10-22 | 2021-12-24 | 南开大学 | Device and method for treating pesticide-polluted soil in ex-situ manner by electro-catalytic Fenton oxidation |
-
2017
- 2017-05-27 CN CN201720610850.2U patent/CN206940627U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108439671A (en) * | 2018-05-16 | 2018-08-24 | 武汉轻工大学 | A kind of electric Fenton of photovoltaic driving is from the system of maintenance and the method for aniline degradation waste water |
| CN108439671B (en) * | 2018-05-16 | 2021-05-07 | 武汉轻工大学 | Photovoltaic-driven electro-Fenton self-maintenance system and method for degrading aniline wastewater |
| CN110190520A (en) * | 2019-05-06 | 2019-08-30 | 邱庆彬 | A kind of nanometer water ion generating device |
| CN110190520B (en) * | 2019-05-06 | 2024-02-23 | 平流层复合水离子(深圳)有限公司 | Nanometer water ion generating device |
| CN113149150A (en) * | 2021-04-25 | 2021-07-23 | 中国地质大学（武汉） | Activated carbon cathode electro-Fenton system and method for removing underground water halogenated hydrocarbons by using same |
| CN113149150B (en) * | 2021-04-25 | 2023-02-24 | 中国地质大学（武汉） | Active carbon cathode electro-Fenton system and method for removing underground water halogenated hydrocarbons by using same |
| CN113828631A (en) * | 2021-10-22 | 2021-12-24 | 南开大学 | Device and method for treating pesticide-polluted soil in ex-situ manner by electro-catalytic Fenton oxidation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105884091B (en) | The wastewater treatment equipment that the electric Fenton that a kind of no solid waste generates is coupled with electrocatalytic oxidation | |
| CN206940627U (en) | A kind of electric Fenton water treatment facilities | |
| CN102139938B (en) | Electro-Fenton reaction waste water treatment equipment | |
| CN104176797B (en) | The organic wastewater with difficult degradation thereby apparatus for electrochemical treatment of a kind of low energy consumption and method | |
| CN107117690A (en) | Electrocatalytic oxidation handles the device and method of Recalcitrant chemicals | |
| CN104528889B (en) | A kind of multiple-unit integrated form electrolysis bath | |
| CN102070230A (en) | Method for removing organic matters in water by utilizing three-dimensional electrode electro-fenton and device thereof | |
| CN103193297A (en) | Sewage treatment method coupled with organic membrane and electro-Fenton catalytic technology | |
| CN106044960B (en) | A method of liquid being concentrated using three-diemsnional electrode processing landfill leachate | |
| CN101723533B (en) | Method for treating concentrated water produced by coking wastewater recycling process | |
| CN201325897Y (en) | Waste water treatment equipment of multi-dimensional electrode electrical catalytic reactor of horizontal electrode plate | |
| CN107200394A (en) | A kind of electro-catalysis ozone high grade oxidation membrane reactor wastewater treatment equipment and method | |
| CN105731604A (en) | Advanced treatment method for electroplating wastewater | |
| CN105271615A (en) | Electrochemical composite membrane bioreactor | |
| CN201971667U (en) | High-voltage pulsed electric coagulation equipment for treating organic wastewater | |
| CN101723532B (en) | System for treating concentrated water produced by coking wastewater recycling process | |
| CN205892821U (en) | A electrochemical reaction pool for polar plate interval that sewage treatment is adjustable | |
| CN208617437U (en) | A kind of three-level electrocatalysis oxidation apparatus of pair of Maotai-flavor liquor wastewater treatment | |
| CN110282706A (en) | A kind of Fenton oxidation reaction treating device | |
| CN101863534B (en) | Advanced treatment method for Dioscoreazingiberensis C.H.Wright wastewater | |
| CN113493238A (en) | Method for treating landfill leachate biochemical tail water by using three-dimensional electrode and persulfate advanced oxidation technology | |
| CN212102375U (en) | Gas field high concentration organic waste water electrochemical coupling treatment recycling device | |
| CN102126778A (en) | Groove-type device and method for treating organic wastewater by multiphase electro-catalytic oxidation | |
| CN111377535A (en) | Anaerobic forward osmosis membrane bioreactor process for oxidizing ammonia nitrogen by coupling electrochemistry | |
| CN104310671A (en) | Three-dimensional electrode electro-catalytic reactor wastewater treatment method employing intermittent power supply |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |