CN214654275U - Micro-electrolysis catalytic oxidation system for difficult-degradation chemical organic wastewater - Google Patents
Micro-electrolysis catalytic oxidation system for difficult-degradation chemical organic wastewater Download PDFInfo
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- CN214654275U CN214654275U CN202022564571.1U CN202022564571U CN214654275U CN 214654275 U CN214654275 U CN 214654275U CN 202022564571 U CN202022564571 U CN 202022564571U CN 214654275 U CN214654275 U CN 214654275U
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- 239000000126 substance Substances 0.000 title claims abstract description 23
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 15
- 230000003647 oxidation Effects 0.000 title claims abstract description 15
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 15
- 238000006731 degradation reaction Methods 0.000 title claims abstract description 13
- 238000005868 electrolysis reaction Methods 0.000 title claims description 12
- 239000002351 wastewater Substances 0.000 title claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000010865 sewage Substances 0.000 claims abstract description 41
- 230000015556 catabolic process Effects 0.000 claims abstract description 11
- 239000010815 organic waste Substances 0.000 claims abstract description 4
- 238000005273 aeration Methods 0.000 claims description 31
- 238000003756 stirring Methods 0.000 claims description 17
- 238000001914 filtration Methods 0.000 claims description 16
- 238000005276 aerator Methods 0.000 claims description 13
- 238000005192 partition Methods 0.000 claims description 8
- 229910001220 stainless steel Inorganic materials 0.000 claims description 7
- 230000005611 electricity Effects 0.000 abstract description 6
- 230000009467 reduction Effects 0.000 abstract description 6
- 238000004134 energy conservation Methods 0.000 abstract description 5
- 230000004044 response Effects 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 description 8
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 description 6
- 239000010935 stainless steel Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 239000010802 sludge Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 230000002265 prevention Effects 0.000 description 4
- 230000000087 stabilizing effect Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000013049 sediment Substances 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- QNRATNLHPGXHMA-XZHTYLCXSA-N (r)-(6-ethoxyquinolin-4-yl)-[(2s,4s,5r)-5-ethyl-1-azabicyclo[2.2.2]octan-2-yl]methanol;hydrochloride Chemical compound Cl.C([C@H]([C@H](C1)CC)C2)CN1[C@@H]2[C@H](O)C1=CC=NC2=CC=C(OCC)C=C21 QNRATNLHPGXHMA-XZHTYLCXSA-N 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000009941 weaving Methods 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/20—Climate change mitigation technologies for sector-wide applications using renewable energy
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Abstract
The utility model discloses a little electrolytic catalytic oxidation system for difficult degradation chemical industry organic waste water, its technical scheme main points are: including tower body and baffle, the lower extreme left and right sides fixedly connected with pylon of tower body, the board is placed to the outside fixedly connected with of tower body, the upper end fixed mounting who places the board has the battery, the upper end fixedly connected with mounting bracket of placing the board, the mounting bracket is established directly over the battery, the upper end fixedly connected with generator of mounting bracket. The sewage tank is provided with a water inlet, the water flow passes through the water turbine, the impeller of the water turbine rotates, the kinetic energy generated by the water turbine is transmitted to the generator, the generator can generate electricity, the storage battery stores energy after the electricity is generated, and then the electricity can be supplied to the first motor and the second motor, so that the equipment can be effectively protected, the energy can be saved, the emission can be reduced, and the active response of China can greatly promote energy conservation and reduction.
Description
Technical Field
The utility model relates to a chemical industry equipment field, in particular to a little electrolytic catalytic oxidation system for difficult degradation chemical industry organic waste water.
Background
With the rapid development of economy, the pollutant discharge amount of the chemical industry is increased rapidly, and particularly, the chemical oxygen demand which indicates the quality of sewage is increased or decreased, so that the water environment is further deteriorated. Therefore, the requirement of reducing the total amount of the chemical oxygen demand cannot be met by improving the standard discharge rate of the industrial wastewater by adopting the conventional method, and the total discharge amount of the chemical oxygen demand in 2005 is reduced by less than 10% compared with 2001 when the chemical oxygen demand in each ton of wastewater is reduced by nearly 32%.
However, conventional organic wastewater difficult to degrade is treated by biological decomposition or pure physical treatment, but if the micro-electrolysis catalytic oxidation system cannot effectively aerate the sewage, the reaction is insufficient, and the treatment effect is poor, in recent years, energy conservation and emission reduction are vigorously advocated in China, and in addition, energy consumption of large water pump equipment adopted by the existing degradation system is too large, so that the energy conservation and emission reduction cannot be effectively carried out.
SUMMERY OF THE UTILITY MODEL
To the problem mentioned in the background art, the utility model aims at providing a little electrolytic catalytic oxidation system for difficult degradation chemical industry organic waste water to solve the problem mentioned in the background art.
The above technical purpose of the present invention can be achieved by the following technical solutions:
a micro-electrolysis catalytic oxidation system for refractory chemical organic wastewater comprises a tower body and a partition plate, wherein tower columns are fixedly connected to the left side and the right side of the lower end of the tower body, a placing plate is fixedly connected to the outer side of the tower body, a storage battery is fixedly mounted at the upper end of the placing plate, a mounting frame is fixedly connected to the upper end of the placing plate and is arranged right above the storage battery, a generator is fixedly connected to the upper end of the mounting frame, a sewage tank is fixedly connected to the upper end of the placing plate, a water inlet is formed in the upper end of the sewage tank, a water turbine is arranged inside the sewage tank, the outer side of the sewage tank is fixedly connected with a pipeline tower body, the inner side of the tower body is provided with the partition plate, a filter tower and an aeration tank are respectively arranged on the inner side of the tower body through the partition plate, a first motor is fixedly connected to the upper end of the filter tower, and a stirring rod is fixedly connected to the inner side of the first motor, which extends into the filter tower, the inboard fixedly connected with of puddler stirs the board, the lower extreme fixedly connected with scum pipe of filtering tower, the outside of scum pipe is equipped with the valve, the outside of baffle is equipped with the filter screen, the inboard of aeration tank is equipped with the second motor, the inboard bottom of aeration tank is equipped with the whirl aerator, the outside of aeration tank is equipped with the delivery port.
Through adopting above-mentioned technical scheme, through setting up generator and battery and hydraulic turbine, can be through the hydroenergy conversion with sewage discharge for the electric energy, through setting up first motor and puddler and stirring the board, can stir the filtration to the inboard sewage of filter tower, through setting up whirl aerator and second motor in aeration tank's inboard, can carry out holistic aeration to sewage.
Preferably, the lower end of the tower column is fixedly connected with a stabilizing foot, and the opposite side of the tower column is fixedly connected with a fixing plate.
Through adopting above-mentioned technical scheme, stabilize foot and fixed plate through setting up, can strengthen fixedly to the lower extreme of tower body.
Preferably, the right side of the sewage tank is fixedly connected with a water pipe, and the other end of the water pipe is fixedly connected with the filtering tower.
Through adopting above-mentioned technical scheme, be connected through setting up water pipe and filtering tower and can be with sewage water conservancy diversion to filtering tower in the middle of.
Preferably, an inclined hopper is arranged on the inner side of the filtering tower, and the hopper surface of the inclined hopper is inclined by 52 degrees.
Through adopting above-mentioned technical scheme, through setting up the tipping bucket in the inboard of filtering tower, can conveniently clear up the precipitate.
Preferably, the filter screen is formed by weaving stainless steel wires, the filter screen is provided with two layers, and meshes of the filter screen are rhombic.
By adopting the technical scheme, the diamond-shaped filter screen woven by stainless steel can prevent the filter screen from being corroded.
Preferably, the inner side walls of the aeration tank and the filter tower are both provided with an anticorrosive layer and an anti-permeation layer, and the anticorrosive layer covers the anti-permeation layer.
Through adopting above-mentioned technical scheme, can carry out chemical protection to the tower body through setting up anticorrosive coating and prevention of seepage permeable layer, improve the life of tower body.
Preferably, the water turbine and the generator are electrically connected through a wire, the generator and the storage battery are electrically connected through a wire, and the storage battery is electrically connected with the first motor and the second motor respectively through wires.
Through adopting above-mentioned technical scheme, pass through the wire with the hydraulic turbine and generator and battery and first motor and second motor and be connected, can reduce the energy consumption through the environmental protection energy.
To sum up, the utility model discloses mainly have following beneficial effect:
firstly, water enters through a water inlet on the sewage tank, when water flows through a water turbine, an impeller of the water turbine rotates, the water turbine transmits generated kinetic energy to a generator, the generator can generate electricity, after the electricity is generated, a storage battery stores the energy, then the first motor and the second motor can be supplied with the electricity, so that the equipment can effectively perform environmental protection, energy conservation and emission reduction, and further actively respond to the call of energetically advocating energy conservation and reduction in China;
second, at first this equipment adopts open-air aeration tank, after the aeration tank that sewage passed through the filter screen and got into, because the operation of second motor, the oxygen ion in the air that makes sewage can be abundant contacts and aerates, and owing to set up the whirl aerator in the bottom of aeration tank, through this kind of mode of combining from top to bottom, can be with the unnecessary gas of aquatic and volatile substances release to the air in to improve waste water treatment's reaction effect.
Drawings
Fig. 1 is a schematic structural diagram of the present invention;
fig. 2 is a schematic view of an electrical connection module according to the present invention;
fig. 3 is a cross-sectional view of the paddle of the present invention.
Reference numerals: 1. a stabilizing foot; 2. a tower column; 3. a tower body; 4. an aeration tank; 5. a second motor; 6. A filter screen; 7. a stirring rod; 8. a first motor; 9. a filtration tower; 10. a sewage tank; 11. a generator; 12. a storage battery; 13. placing the plate; 14. a water turbine; 15. a stirring plate; 16. an inclined hopper; 17. a valve; 18. A slag discharge pipe; 19. a rotational flow aerator; 20. a fixing plate; 21. a water inlet; 22. a partition plate; 23. a water outlet; 24. a mounting frame; 151. a mixture of carbon and iron.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Examples
Referring to fig. 1-3, a micro-electrolysis catalytic oxidation system for refractory chemical organic wastewater, comprising a tower body 3 and a partition 22, wherein tower columns 2 are fixedly connected to the left and right sides of the lower end of the tower body 3, a placing plate 13 is fixedly connected to the outer side of the tower body 3, a storage battery 12 is fixedly mounted at the upper end of the placing plate 13, a mounting frame 24 is fixedly connected to the upper end of the placing plate 13, the mounting frame 24 is arranged right above the storage battery 12, a generator 11 is fixedly connected to the upper end of the mounting frame 24, the generator 11 is DH-01, a sewage tank 10 is fixedly connected to the upper end of the placing plate 13, a water inlet 21 is arranged at the upper end of the sewage tank 10, a water turbine 14 is arranged inside the sewage tank 10, the water turbine 14 is 9108-, the inner side of the tower body 3 is provided with a clapboard 22, the inner side of the tower body 3 is respectively provided with a filter tower 9 and an aeration tank 4 through the clapboard 22, the activated sludge is arranged in the aeration tank 4, the use and decontamination effect of the activated sludge matched with the rotational flow aerator 19 is better, a first motor 8 is fixedly connected with the upper end of the filter tower 9, the output end of the first motor 8 extends into the inner side of the filter tower 9 and is fixedly connected with a stirring rod 7, the inner side of the stirring rod 7 is fixedly connected with a stirring plate 15, the lower end of the filter tower 9 is fixedly connected with a slag discharge pipe 18, a valve 17 is arranged on the outer side of the slag discharge pipe 18, a filter screen 6 is arranged on the outer side of the clapboard 22, the inner side of the aeration tank 4 is provided with a second motor 5, the bottom of the inner side of the aeration tank 4 is provided with a rotational flow aerator 19, the type of the rotational flow aerator 19 is 215mm, and a water outlet 23 is arranged on the outer side of the aeration tank 4.
With reference to fig. 1, for the purpose of better stabilization of the tower body 3; the lower end of the tower column 2 is fixedly connected with a stabilizing foot 1, and the opposite side of the tower column 2 is fixedly connected with a fixing plate 20; by arranging the fixing plate 20 and the stabilizing leg 1 on the tower column 2 at the lower end of the tower body 3, the tower body 3 can be more stable.
Referring to fig. 1, for the purpose of guiding sewage in a sewage tank 10; the right side of the sewage tank 10 is fixedly connected with a water pipe, and the other end of the water pipe is fixedly connected with the filtering tower 9; by providing a water pipe between the sewage tank 10 and the filtration tower 9, sewage can be guided into the interior of the filtration tower 9.
Referring to fig. 1 to 3, for the purpose of improving the sewage treatment effect; a plurality of micropores are formed in the outer side of the stirring plate 15 at equal intervals, a carbon-iron mixture 151 is arranged on the inner side of the stirring plate 15, the carbon-iron mixture 151 is spherical, and the carbon-iron mixture (151) is specifically composed of activated carbon and scrap iron; by providing the micro-porous and carbon-iron mixture 151 on the inner side of the stirring plate 15, Cu2+ and Pb2+ can be removed.
Referring to fig. 1, for the purpose of facilitating the cleaning of the sediment in the filtration tower 9; an inclined hopper 16 is arranged on the inner side of the filtering tower 9, and the hopper surface of the inclined hopper 16 is inclined by 52 degrees; through setting up the tipping bucket 16 in the inboard of filter tower 9, the sediment can remove the heavy end to the fill end along the tipping bucket 16, and the cooperation is arranged the cinder notch and can be conveniently cleared up the sediment.
Referring to fig. 1, in order for the filter screen 6 to have the purpose of corrosion-resistant filtration; the filter screen 6 is formed by weaving stainless steel wires, two layers of the filter screen 6 are arranged, and meshes of the filter screen 6 are rhombic; through the rhombus filter screen 6 that adopts stainless steel to weave, because the infiltration corrosivity of sewage can be reduced to the material of stainless steel, and then can prevent filter screen 6 corrosion.
With reference to fig. 1, for the purpose of increasing the service life of the tower body 3; the inner side walls of the aeration tank 4 and the filter tower 9 are both provided with an anticorrosive layer and an anti-permeation layer, and the anticorrosive layer covers the anti-permeation layer; through setting up the prevention of seepage permeable blanket in the inboard of tower body 3, can avoid water pressure too big, lead to rivers to permeate out the outside of tower body 3, through setting up the anticorrosive coating in the outside of prevention of seepage permeable blanket, can reduce the erosion of sewage to the prevention of seepage permeable blanket.
Referring to fig. 2, for the purpose of reducing power consumption; the water turbine 14 is electrically connected with the generator 11 through a conducting wire, the generator 11 is electrically connected with the storage battery 12 through a conducting wire, and the storage battery 12 is electrically connected with the first motor 8 and the second motor 5 through conducting wires respectively; by connecting the water turbine 14 with the generator 11, the storage battery 12, the first motor 8 and the second motor 5 through leads, the water energy is converted into mechanical energy, and then the mechanical energy is converted into electric energy, so that the energy consumption can be reduced.
The use principle and the advantages are as follows: firstly, sewage enters through a water inlet 21 of a sewage tank 10, a water flow drives a water turbine 14 to rotate, the water turbine 14 generates mechanical energy through rotation, the mechanical energy drives a generator 11 to operate, the generator 11 generates electric energy through operation to charge a storage battery 12, the storage battery 12 can respectively supply power to a first motor 8 and a second motor 5 of equipment after being electrified, so that the environmental protection, energy saving and emission reduction can be actively carried out in response to the call of the country, after the sewage enters a filter tower 9 through a water pipe of the sewage tank 10, the first motor 8 drives a stirring plate 15 on a stirring rod 7 to rotate, as a plurality of micropores and a carbon-iron mixture 151 are arranged on the stirring plate 15, the sewage can effectively remove Cu2+ and Pb2+ through the contact of the micropores and the carbon-iron mixture 151 in the stirring process, and after the sewage passes through the filter tower 9, the sewage enters an aeration tank 4 along a double-layer stainless steel filter screen 6 on a partition plate 22, aeration tank 4 at first adopts the open air pond, can be with the aquatic in unnecessary gas and volatile substances release to the air, the use of cooperation second motor 5 can make aeration tank 4 first aeration effect better, because aeration tank 4's inboard is equipped with activated sludge, aeration tank 4's lower half bottom adopts spiral-flow aerator 19, density is greater than the air of water and can rises rapidly when air gets into spiral-flow aerator 19 bottom, make spiral-flow aerator 19's inside produce stronger negative pressure, make activated sludge and sewage be crowded into spiral-flow aerator 19 by water pressure simultaneously, carry out the high-efficient mixture, and rotary cutter in spiral-flow aerator 19 can cut the microparticle, thereby can make activated sludge and sewage carry out abundant contact and decontaminate, through aeration tank 4's high-efficient aeration, can be with sewage treatment's better.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (7)
1. The utility model provides a little electrolysis catalytic oxidation system for difficult degradation chemical industry organic waste water, includes tower body (3) and baffle (22), its characterized in that: the tower comprises a tower body (3), tower columns (2) are fixedly connected to the left and right sides of the lower end of the tower body (3), a placing plate (13) is fixedly connected to the outer side of the tower body (3), a storage battery (12) is fixedly mounted at the upper end of the placing plate (13), a mounting frame (24) is fixedly connected to the upper end of the placing plate (13), the mounting frame (24) is arranged right above the storage battery (12), a generator (11) is fixedly connected to the upper end of the mounting frame (24), a sewage tank (10) is fixedly connected to the upper end of the placing plate (13), a water inlet (21) is formed in the upper end of the sewage tank (10), a water turbine (14) is arranged inside the sewage tank (10), the outer side of the tower body (10) is fixedly connected through a pipeline (3), a partition plate (22) is arranged on the inner side of the tower body (3), and a filter tower (9) and an aeration tank (4) are respectively arranged on the inner side of the tower body (3) through the partition plate (22), the utility model discloses an aeration tank, including the upper end fixedly connected with of straining tower (9), the first motor of upper end fixedly connected with (8) of straining tower (9), the inboard fixedly connected with puddler (7) of straining tower (9) are stretched into to the output of first motor (8), the inboard fixedly connected with of puddler (7) stirs board (15), the lower extreme fixedly connected with scum pipe (18) of straining tower (9), the outside of scum pipe (18) is equipped with valve (17), the outside of baffle (22) is equipped with filter screen (6), the inboard of aeration tank (4) is equipped with second motor (5), the inboard bottom of aeration tank (4) is equipped with whirl aerator (19), the outside of aeration tank (4) is equipped with delivery port (23).
2. The micro-electrolysis catalytic oxidation system for the degradation-resistant chemical organic wastewater according to claim 1, characterized in that: the lower extreme fixedly connected with of pylon (2) stabilizes foot (1), the offside fixedly connected with fixed plate (20) of pylon (2).
3. The micro-electrolysis catalytic oxidation system for the degradation-resistant chemical organic wastewater according to claim 1, characterized in that: the right side of the sewage tank (10) is fixedly connected with a water pipe, and the other end of the water pipe is fixedly connected with the filtering tower (9).
4. The micro-electrolysis catalytic oxidation system for the degradation-resistant chemical organic wastewater according to claim 1, characterized in that: an inclined hopper (16) is arranged on the inner side of the filtering tower (9), and the hopper surface of the inclined hopper (16) is inclined by 52 degrees.
5. The micro-electrolysis catalytic oxidation system for the degradation-resistant chemical organic wastewater according to claim 1, characterized in that: the filter screen (6) is woven for the stainless steel wire and forms, filter screen (6) are equipped with two-layer altogether, the mesh of filter screen (6) is the rhombus.
6. The micro-electrolysis catalytic oxidation system for the degradation-resistant chemical organic wastewater according to claim 1, characterized in that: the inner side walls of the aeration tank (4) and the filter tower (9) are both provided with an anticorrosive layer and an anti-seepage layer, and the anticorrosive layer covers the anti-seepage layer.
7. The micro-electrolysis catalytic oxidation system for the degradation-resistant chemical organic wastewater according to claim 1, characterized in that: the water turbine (14) is electrically connected with the generator (11) through a conducting wire, the generator (11) is electrically connected with the storage battery (12) through a conducting wire, and the storage battery (12) is electrically connected with the first motor (8) and the second motor (5) through conducting wires respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022564571.1U CN214654275U (en) | 2020-11-09 | 2020-11-09 | Micro-electrolysis catalytic oxidation system for difficult-degradation chemical organic wastewater |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022564571.1U CN214654275U (en) | 2020-11-09 | 2020-11-09 | Micro-electrolysis catalytic oxidation system for difficult-degradation chemical organic wastewater |
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| CN202022564571.1U Expired - Fee Related CN214654275U (en) | 2020-11-09 | 2020-11-09 | Micro-electrolysis catalytic oxidation system for difficult-degradation chemical organic wastewater |
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Granted publication date: 20211109 |