CN215327589U - BDD electrolysis, ozone, hydrogen peroxide solution oxidation unite water treatment facilities - Google Patents
BDD electrolysis, ozone, hydrogen peroxide solution oxidation unite water treatment facilities Download PDFInfo
- Publication number
- CN215327589U CN215327589U CN202121625147.1U CN202121625147U CN215327589U CN 215327589 U CN215327589 U CN 215327589U CN 202121625147 U CN202121625147 U CN 202121625147U CN 215327589 U CN215327589 U CN 215327589U
- Authority
- CN
- China
- Prior art keywords
- electrolysis
- hydrogen peroxide
- ozone
- bdd
- pipeline
- 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
Images
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment, which comprises an electrolysis box, wherein an electrolysis auxiliary mechanism is arranged in the electrolysis box; the electrolysis complementary unit includes a plurality of sprayers, and is a plurality of the sprayer top all is fixed and is equipped with the distributing pipe, the inside inlet channel that is equipped with of electrolysis box, electrolysis box one side is equipped with the circulating line, be equipped with the circulating pump on the circulating line, the pipeline is thrown to the fixed hydrogen peroxide that is equipped with on the inlet channel, hydrogen peroxide is thrown and is thrown pipeline input and be connected with hydrogen peroxide and throw and add the pump, electrolysis box one side is equipped with ozone aeration pipeline. According to the utility model, strong oxidants rich in active oxygen atoms, such as ozone and hydrogen peroxide, are added through the electrolysis auxiliary mechanism, and under the electrolysis action of the BDD electrode plate, the active negative monovalent oxygen atoms can promote the decomposition of organic matters to finally generate carbon dioxide, so that no secondary pollution is generated, the purification effect is good, the purification efficiency is improved, and the purification cost is reduced.
Description
Technical Field
The utility model relates to the technical field of wastewater treatment, in particular to BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment.
Background
The BDD electrolysis process adopts a diamond boron-doped material as an anode of an electrode, macromolecular organic matters can be gradually degraded under the action of electrification, pollutants are degraded by the electrode in toxic and harmful wastewater with high-concentration organic matters, high ammonia nitrogen and complex components, and particularly when the BDD electrolysis efficiency is rapidly reduced or even the organic matters cannot be degraded when the BDD electrolysis process meets macromolecules such as benzenes, heterocycles and the like with carbon atom content more than 8 in the organic matters.
At present, most of electrolytic equipment is low in electrolytic efficiency of part of macromolecular organic matters such as benzene and heterocycle and even the condition that the organic matters cannot be electrolyzed is generated in actual use, so that other processing equipment is required to be arranged for purifying the part of macromolecular organic matters such as benzene and heterocycle, the process is complex, and the purification cost is high.
Therefore, it is necessary to invent a BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment device to solve the problems.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment, which is characterized in that strong oxidants rich in active oxygen atoms, such as ozone and hydrogen peroxide, are added through an electrolysis auxiliary mechanism, and under the electrolysis action of a BDD electrode slice, active negative monovalent oxygen atoms can promote organic matters to be decomposed to finally generate carbon dioxide, so that secondary pollution is avoided, the purification effect is good, the purification efficiency is improved, and the purification cost is reduced, thereby overcoming the defects in the technology.
In order to achieve the above purpose, the utility model provides the following technical scheme: a BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment device comprises an electrolytic tank, a sealing top plate and a biochemical treatment tank, wherein the sealing top plate is arranged at the top end of the electrolytic tank, the sealing top plate and the electrolytic tank are fixedly connected through a plurality of bolts, the biochemical treatment tank is arranged on one side of the electrolytic tank, and an electrolysis auxiliary mechanism is arranged inside the electrolytic tank;
the electrolysis auxiliary mechanism comprises a plurality of sprayers, the sprayers are all arranged inside an electrolytic tank, water distribution pipes are fixedly arranged at the top ends of the sprayers, a water inlet pipeline is arranged inside the electrolytic tank, the top ends of the water distribution pipes are all fixedly connected with the bottom end of the water inlet pipeline, one end of the water inlet pipeline extends to the outer end of the electrolytic tank, a circulating pipeline is arranged on one side of the electrolytic tank, a circulating pump is arranged on the circulating pipeline, the top end of the circulating pipeline is fixedly connected with the bottom end of the water inlet pipeline, the water inlet pipeline is arranged at the output end of the circulating pump, a hydrogen peroxide adding pipeline is fixedly arranged on the water inlet pipeline and is arranged on one side of the circulating pipeline, a hydrogen peroxide adding pump is connected to the input end of the hydrogen peroxide adding pipeline, a hot steam air channel is arranged inside the electrolytic tank, and the top end of the hot steam air channel penetrates through a sealing top plate and extends to the top end of the sealing top plate, the water inlet pipeline is arranged on the outer ring of the hot steam air channel, an ozone aeration pipeline is arranged on one side of the electrolytic tank and extends into the electrolytic tank, a plurality of aeration discs are fixedly arranged at the top end of the ozone aeration pipeline, a steam conveying pipeline is fixedly arranged at the top end of the hot steam air channel, and one end of the steam conveying pipeline is fixedly connected with the top end of the biochemical treatment tank.
Preferably, a plurality of BDD electrode plates are embedded into the inner wall of the electrolytic tank, the number of the BDD electrode plates is consistent with that of the sprayers, the BDD electrode plates are arranged on one sides of the sprayers respectively, and the aeration discs are arranged at the bottoms of the BDD electrode plates respectively.
Preferably, a funnel is fixedly arranged at the bottom end of the electrolytic tank.
Preferably, a waste water discharge pipeline is fixedly arranged at the bottom end of the funnel, and a switch valve is arranged on the waste water discharge pipeline.
Preferably, hot vapour wind channel outer end is equipped with first cooling air inlet line, hot vapour wind channel outer end is equipped with second cooling air inlet line, second cooling air inlet line is established at first cooling air inlet line top, first cooling air inlet line and second cooling air inlet line one end all extend to the electrolysis box outer end, hot vapour wind channel rear end is fixed and is equipped with the comdenstion water discharge pipeline, the comdenstion water discharge pipeline output is established inside the electrolysis box, the comdenstion water discharge pipeline is established in first cooling air inlet line bottom.
Preferably, a plurality of steam holes are formed in the hot steam air channel, the steam holes are formed in the top of the second cooling air inlet pipeline, the steam holes are formed in the inner portion of the electrolytic tank, a demister is fixedly arranged in the hot steam air channel, and the demister is arranged at the tops of the steam holes.
Preferably, one side of the biochemical treatment tank is provided with a biochemical tank aeration pipeline, and one end of the biochemical tank aeration pipeline extends into the biochemical treatment tank.
In the technical scheme, the utility model provides the following technical effects and advantages:
1. hydrogen peroxide is conveyed to the inside of a water inlet pipeline through a hydrogen peroxide adding pump and a hydrogen peroxide adding pipeline, a mixed solution of wastewater and hydrogen peroxide is conveyed to the inside of an electrolytic tank through the water inlet pipeline, ozone is added to the inside of the electrolytic tank through an ozone aeration pipeline and an aeration disc, added strong oxidants such as ozone, hydrogen peroxide and the like which are rich in active oxygen atoms can directly oxidize micromolecule organic matters, macromolecule organic matters in a critical decomposition state are directly combined with oxygen atoms to become micromolecule organic matters, carbon in pollutants is finally oxidized into carbon dioxide and oxidized into ammonia nitrogen, hydrogen and oxygen are combined into water, other ionic state simple substances form salt, the purpose of finally purifying the pollutants is achieved, the wastewater can be subjected to electrolytic treatment through the work of a BDD electrode plate, a circulating pump and a circulating pipeline convey the wastewater to the water inlet pipeline again, the water inlet pipeline and a plurality of water distribution pipes convey the wastewater to a plurality of sprayers, the solution is conveyed and sprayed on the BDD electrode plate through a plurality of sprayers, and the electrolysis purification of the wastewater can be carried out in a circulating way, compared with the prior art, strong oxidants rich in active oxygen atoms, such as ozone, hydrogen peroxide and the like, can be added, and under the electrolysis action of the BDD electrode plate, the active negative monovalent oxygen atoms can promote the decomposition of organic matters and finally generate carbon dioxide, so that the secondary pollution is not generated, the purification effect is good, the purification efficiency is improved, and the purification cost is reduced;
2. through the funnel, the ooff valve on waste water discharge pipeline and the waste water discharge pipeline, be used for discharging waste water, produced hot vapor can get into inside the hot vapor wind channel through the steam vent during electrolysis, first cooling air inlet line and second cooling air inlet line all are used for carrying the outside cooling air entering hot vapor wind channel, so that carry out cooling treatment to the inside hot vapor that gets into the hot vapor wind channel, the comdenstion water discharge pipe is used for discharging condensate to the electrolysis incasement portion, so that carry out electrolysis once more to the condensate, the defroster is used for the defogging, biochemical pond aeration pipeline's effect is used for carrying out aeration treatment to biochemical treatment pond inside, thereby avoid biochemical treatment pond inside bottom to have the precipitate.
Drawings
In order to more clearly illustrate the embodiments of the present application or technical solutions in the prior art, the drawings needed to be used in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments described in the present invention, and other drawings can be obtained by those skilled in the art according to the drawings.
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is an exploded view of the hot vapor duct of the present invention;
FIG. 3 is a top view of an electrolytic tank of the present invention;
fig. 4 is a perspective view of a first aeration pipe and an aeration output head according to the present invention;
fig. 5 is a perspective view of an electrode sheet and a sprayer of the present invention.
Description of reference numerals:
1 electrolytic tank, 2 hot steam air channel, 3 sealing top plate, 4 funnel, 5 first cooling air inlet pipeline, 6 second cooling air inlet pipeline, 7 demister, 8 steam delivery pipeline, 9 steam hole, 10 ozone aeration pipeline, 11 biochemical tank aeration pipeline, 12 aeration disc, 13 waste water discharge pipeline, 14BDD electrode slice, 15 sprinkler, 16 water distribution pipe, 17 water inlet pipeline, 18 circulation pipeline, 19 circulation pump, 20 condensate water discharge pipeline, 21 biochemical treatment tank, 22 hydrogen peroxide adding pipeline, 23 hydrogen peroxide adding pump.
Detailed Description
In order to make the technical solutions of the present invention better understood, those skilled in the art will now describe the present invention in further detail with reference to the accompanying drawings.
The utility model provides BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment as shown in figures 1-5, which comprises an electrolytic tank 1, a sealing top plate 3 and a biochemical treatment tank 21, wherein the sealing top plate 3 is arranged at the top end of the electrolytic tank 1, the sealing top plate 3 and the electrolytic tank 1 are fixedly connected through a plurality of bolts, the biochemical treatment tank 21 is arranged at one side of the electrolytic tank 1, and an electrolysis auxiliary mechanism is arranged in the electrolytic tank 1;
the electrolysis auxiliary mechanism comprises a plurality of sprayers 15, a plurality of the sprayers 15 are all arranged inside an electrolytic tank 1, a plurality of the sprayers 15 are arranged at the top ends of the sprayers 16, a water inlet pipeline 17 is arranged inside the electrolytic tank 1, a plurality of the top ends of the water inlet pipeline 16 are all fixedly connected with the bottom end of the water inlet pipeline 17, one end of the water inlet pipeline 17 extends to the outer end of the electrolytic tank 1, a circulating pipeline 18 is arranged on one side of the electrolytic tank 1, a circulating pump 19 is arranged on the circulating pipeline 18, the top end of the circulating pipeline 18 is fixedly connected with the bottom end of the water inlet pipeline 17, the water inlet pipeline 17 is arranged at the output end of the circulating pump 19, a hydrogen peroxide adding pipeline 22 is fixedly arranged on the water inlet pipeline 17, the hydrogen peroxide adding pipeline 22 is arranged on one side of the circulating pipeline 18, the input end of the hydrogen peroxide adding pipeline 22 is connected with a hydrogen peroxide adding pump 23, and hot air channel steam 2 is arranged inside the electrolytic tank 1, the top end of the hot steam air duct 2 penetrates through the sealing top plate 3 and extends to the top end of the sealing top plate 3, the water inlet pipeline 17 is arranged on the outer ring of the hot steam air duct 2, the ozone aeration pipeline 10 is arranged on one side of the electrolytic tank 1 and extends to the inside of the electrolytic tank 1, the top end of the ozone aeration pipeline 10 is fixedly provided with a plurality of aeration discs 12, the top end of the hot steam air duct 2 is fixedly provided with a steam conveying pipeline 8, and one end of the steam conveying pipeline 8 is fixedly connected with the top end of the biochemical treatment tank 21.
The embedding has a plurality of BDD electrode slices 14 on the 1 inner wall of electrolysis box, and is a plurality of BDD electrode slice 14 and a plurality of sprinkler 15 quantity are unanimous, and is a plurality of BDD electrode slice 14 is established respectively in a plurality of sprinklers 15 one side, and the external negative and positive pole power of BDD electrode slice 14 can carry out electrolysis treatment to waste water through BDD electrode slice 14, and sprinkler 15 is to spray waste water circulation on BDD electrode slice 14 to make sprinkler 15 and waste water fully contact, so that BDD electrode slice 14 carries out electrolysis treatment to waste water, and is a plurality of aeration dish 12 is established respectively in a plurality of BDD electrode slice 14 bottoms, and aeration mixing ozone directly sweeps BDD electrode slice 14, intensive mixing.
The implementation mode is specifically as follows: when the device is used, the hydrogen peroxide is conveyed to the inside of the water inlet pipeline 17 through the hydrogen peroxide feeding pump 23 and the hydrogen peroxide feeding pipeline 22, the mixed solution of wastewater and hydrogen peroxide is conveyed to the inside of the electrolytic tank 1 through the water inlet pipeline 17, ozone is fed into the electrolytic tank 1 through the ozone aeration pipeline 10 and the aeration disc 12, the fed strong oxidants such as ozone, hydrogen peroxide and the like which are rich in active oxygen atoms can directly oxidize micromolecule organic matters, macromolecular organic matters in a critical decomposition state are directly combined with oxygen atoms to become micromolecule organic matters, carbon in pollutants is finally oxidized into carbon dioxide, ammonia nitrogen is oxidized into nitrogen, hydrogen and oxygen are combined into water, other ionic state simple substances form salt, the purpose of final purification of the pollutants is achieved, then the BDD 14 is connected with an external cathode and anode power supply, and the BDD electrode plate 14 can be in work, the BDD electrode plate 14 can carry out electrolytic treatment on the wastewater, meanwhile, a circulating pump 19 can be started, the circulating pump 19 can utilize a circulating pipeline 18 to extract liquid in the electrolytic tank 1 when working, at the moment, the liquid can be conveyed to a water inlet pipeline 17 again through the circulating pipeline 18 and the circulating pump 19, conveyed to each water distribution pipe 16 through the water inlet pipeline 17 and then conveyed to a sprayer 15 through a single water distribution pipe 16, the solution is conveyed and sprayed on the BDD electrode plate 14 through the sprayer 15, the solution can be fully contacted with the BDD electrode plate 14, so that electrolytic treatment can be better carried out, the wastewater can be electrolyzed and purified through circulation, an ozone aeration pipeline 10 and an aeration disc 12 are used for injecting ozone into the wastewater, so that the ozone and electrolytic reaction are full, strong oxidants such as ozone, hydrogen peroxide and the like which are rich in active oxygen atoms are added through an electrolysis auxiliary mechanism, under the electrolytic action of the BDD electrode plate 14, active negative oxygen atom can promote the organic matter to decompose, finally generate carbon dioxide, do not produce secondary pollution, purifying effect is good, improve purification efficiency, reduce purification cost, most electrolysis equipment that this embodiment has specifically solved and has existed among the prior art is to some benzene class, macromolecule organic matter electrolysis inefficiency such as heterocycle, the condition of unable electrolysis organic matter appears even, consequently to some benzene class, macromolecule organic matter such as heterocycle still need set up other processing equipment and carry out purification treatment, the technology is loaded down with trivial details, the problem that purification cost is high.
The utility model provides BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment as shown in figures 1-5, wherein a funnel 4 is fixedly arranged at the bottom end of an electrolysis box 1, and the funnel 4 is used for connecting and fixing a wastewater discharge pipeline 13.
The 4 bottom mounting of funnel is equipped with waste water discharge pipeline 13, be equipped with the ooff valve on the waste water discharge pipeline 13, waste water discharge pipeline 13 is used for discharging waste water.
The outer end of the hot steam air duct 2 is provided with a first cooling air inlet pipeline 5, the outer end of the hot steam air duct 2 is provided with a second cooling air inlet pipeline 6, the second cooling air inlet pipeline 6 is arranged at the top of the first cooling air inlet pipeline 5, one end of each of the first cooling air inlet pipeline 5 and the second cooling air inlet pipeline 6 extends to the outer end of the electrolytic box 1, the rear end of the hot steam air duct 2 is fixedly provided with a condensate water discharge pipeline 20, the output end of the condensate water discharge pipeline 20 is arranged inside the electrolytic box 1, the condensate water discharge pipeline 20 is arranged at the bottom of the first cooling air inlet pipeline 5, the first cooling air inlet pipeline 5 and the second cooling air inlet pipeline 6 are used for conveying external cooling air into the hot steam air duct 2 so as to cool hot steam entering the hot steam air duct 2, and the condensate water discharge pipeline 20 is used for discharging condensate liquid into the electrolytic box 1, so as to facilitate the re-electrolysis of the condensate.
The hot steam air duct 2 is provided with a plurality of steam holes 9, the steam holes 9 are all arranged at the top of the second cooling air inlet pipeline 6, the steam holes 9 are all arranged inside the electrolytic box 1, the demister 7 is fixedly arranged inside the hot steam air duct 2, the demister 7 is arranged at the top of the steam holes 9, hot steam generated during electrolysis can enter the hot steam air duct 2 through the steam holes 9, and the demister 7 is used for demisting.
While certain exemplary embodiments of the present invention have been described above by way of illustration only, it will be apparent to those of ordinary skill in the art that the described embodiments may be modified in various different ways without departing from the spirit and scope of the utility model. Accordingly, the drawings and description are illustrative in nature and should not be construed as limiting the scope of the utility model.
Claims (7)
1. The utility model provides a BDD electrolysis, ozone, hydrogen peroxide solution oxidation unite water treatment facilities, includes electrolysis box (1), sealed roof (3) and biochemical treatment pond (21), establish on electrolysis box (1) top sealed roof (3), sealed roof (3) and electrolysis box (1) are fixed through a plurality of bolted connection, biochemical treatment pond (21) are established in electrolysis box (1) one side, its characterized in that: an electrolysis auxiliary mechanism is arranged in the electrolysis box (1);
the electrolysis auxiliary mechanism comprises a plurality of sprayers (15) which are arranged inside an electrolytic tank (1) in a plurality of ways, wherein the top ends of the sprayers (15) are fixedly provided with water distribution pipes (16), the electrolytic tank (1) is internally provided with water inlet pipes (17) which are arranged in a plurality of ways, the top ends of the water distribution pipes (16) are fixedly connected with the bottom end of the water inlet pipes (17), one ends of the water inlet pipes (17) extend to the outer end of the electrolytic tank (1), one side of the electrolytic tank (1) is provided with circulating pipes (18), circulating pipes (18) are provided with circulating pumps (19), the top ends of the circulating pipes (18) are fixedly connected with the bottom end of the water inlet pipes (17), the water inlet pipes (17) are arranged at the output end of the circulating pumps (19), hydrogen peroxide adding pipes (22) are fixedly arranged on the water inlet pipes (17), and the hydrogen peroxide adding pipes (22) are arranged on one side of the circulating pipes (18), the utility model discloses a hydrogen peroxide solution adding device, including electrolysis box (1), hydrogen peroxide solution adding pipeline (22), sealed roof (3) are passed on hot vapor air duct (2) top and are extended to sealed roof (3) top, inlet channel (17) are established in hot vapor air duct (2) outer lane, electrolysis box (1) one side is equipped with ozone aeration pipeline (10), ozone aeration pipeline (10) extend to inside electrolysis box (1), ozone aeration pipeline (10) top is fixed and is equipped with a plurality of aeration dish (12), hot vapor air duct (2) top is fixed and is equipped with steam conveying pipeline (8), steam conveying pipeline (8) one end and biochemical treatment pond (21) top fixed connection.
2. The BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment as claimed in claim 1, wherein: a plurality of BDD electrode slices (14) are embedded into the inner wall of the electrolytic tank (1), the number of the BDD electrode slices (14) is consistent with that of the sprayers (15), the BDD electrode slices (14) are arranged on one sides of the sprayers (15) respectively, and the aeration discs (12) are arranged at the bottoms of the BDD electrode slices (14) respectively.
3. The BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment as claimed in claim 1, wherein: the bottom end of the electrolytic tank (1) is fixedly provided with a funnel (4).
4. The BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment as claimed in claim 3, wherein: the bottom fixing of funnel (4) is equipped with waste water discharge pipe way (13), be equipped with the ooff valve on waste water discharge pipe way (13).
5. The BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment as claimed in claim 1, wherein: hot vapour wind channel (2) outer end is equipped with first cooling air inlet duct (5), hot vapour wind channel (2) outer end is equipped with second cooling air inlet duct (6), establish at first cooling air inlet duct (5) top second cooling air inlet duct (6), first cooling air inlet duct (5) and second cooling air inlet duct (6) one end all extend to electrolysis box (1) outer end, hot vapour wind channel (2) rear end is fixed and is equipped with comdenstion water discharge pipe way (20), comdenstion water discharge pipe way (20) output is established inside electrolysis box (1), comdenstion water discharge pipe way (20) are established in first cooling air inlet duct (5) bottom.
6. The BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment as claimed in claim 5, wherein: a plurality of steam holes (9) are formed in the hot steam air duct (2) and are multiple, the steam holes (9) are all formed in the top of the second cooling air inlet pipeline (6) and are multiple, the steam holes (9) are all formed in the electrolytic tank (1), a demister (7) is fixedly arranged in the hot steam air duct (2), and the demister (7) is arranged at the tops of the steam holes (9).
7. The BDD electrolysis, ozone and hydrogen peroxide oxidation combined water treatment equipment as claimed in claim 1, wherein: one side of the biochemical treatment tank (21) is provided with a biochemical tank aeration pipeline (11), and one end of the biochemical tank aeration pipeline (11) extends into the biochemical treatment tank (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121625147.1U CN215327589U (en) | 2021-07-16 | 2021-07-16 | BDD electrolysis, ozone, hydrogen peroxide solution oxidation unite water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121625147.1U CN215327589U (en) | 2021-07-16 | 2021-07-16 | BDD electrolysis, ozone, hydrogen peroxide solution oxidation unite water treatment facilities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215327589U true CN215327589U (en) | 2021-12-28 |
Family
ID=79567995
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121625147.1U Active CN215327589U (en) | 2021-07-16 | 2021-07-16 | BDD electrolysis, ozone, hydrogen peroxide solution oxidation unite water treatment facilities |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215327589U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114349176A (en) * | 2022-01-27 | 2022-04-15 | 欧秋香 | Artificial wetland for enhancing pollutant absorption of emergent aquatic plants and use method thereof |
| CN115180705A (en) * | 2022-06-23 | 2022-10-14 | 湖南新沃环境科技有限公司 | Organic wastewater treatment method and system |
| CN117303672A (en) * | 2023-11-28 | 2023-12-29 | 山东戴克生物科技有限公司 | Imidazole waste water treatment device |
-
2021
- 2021-07-16 CN CN202121625147.1U patent/CN215327589U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114349176A (en) * | 2022-01-27 | 2022-04-15 | 欧秋香 | Artificial wetland for enhancing pollutant absorption of emergent aquatic plants and use method thereof |
| CN115180705A (en) * | 2022-06-23 | 2022-10-14 | 湖南新沃环境科技有限公司 | Organic wastewater treatment method and system |
| CN115180705B (en) * | 2022-06-23 | 2023-09-29 | 湖南新沃环境科技有限公司 | Organic wastewater treatment method and treatment system |
| CN117303672A (en) * | 2023-11-28 | 2023-12-29 | 山东戴克生物科技有限公司 | Imidazole waste water treatment device |
| CN117303672B (en) * | 2023-11-28 | 2024-02-09 | 山东戴克生物科技有限公司 | Imidazole waste water treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN215327589U (en) | BDD electrolysis, ozone, hydrogen peroxide solution oxidation unite water treatment facilities | |
| CN208097776U (en) | A kind of device that VOCs exhaust gas is handled using ozone and solvent | |
| CN104003504B (en) | A kind of organic wastewater with difficult degradation thereby catalytic ozonation treatment unit and technique | |
| CN204607826U (en) | A kind of sludge ozone cracks reactor | |
| CN102863109A (en) | Ammonia-nitrogen wastewater treatment method and ammonia-nitrogen wastewater treatment device | |
| CN103553286B (en) | The sludge reduction method that a kind of electrochemistry/ClO 2 catalyzed oxidation is coupled | |
| CN102895864A (en) | Method and device for absorbing and purifying harmful gas through electrochemical oxidation | |
| CN212417513U (en) | Chemical waste gas treatment recovery system for environmental protection | |
| CN102583695B (en) | Ozone and hydrogen peroxide combination system for realizing slightly polluted water treatment | |
| CN201520693U (en) | Phenol wastewater treatment system | |
| CN217287903U (en) | High-efficient biological treatment device of waste gas | |
| CN103420528A (en) | Multi-stage bubbling oxidizing tower-type sewage treatment reactor | |
| CN204891600U (en) | Low temperature plasma - biological method combination waste gas treatment system | |
| CN213141505U (en) | Device for environment-friendly disinfection and sterilization of epidemic prevention equipment and public space | |
| CN210303140U (en) | Electrochemical deodorization spray tower | |
| CN107469586A (en) | A kind of plasma organic exhaust gas purifying system integrated with biofilter and method | |
| CN210656325U (en) | Waste water treatment device | |
| KR200425121Y1 (en) | A desalter of the organic waste containing salt | |
| CN210855603U (en) | High-efficient coal industry high concentration sewage pretreatment device | |
| CN206783384U (en) | A kind of water process ozone-oxidizing device | |
| KR101106129B1 (en) | A desalter of organicity waste including salt | |
| CN216073401U (en) | Device for removing pollutants in wastewater by electric coupling catalytic ozonation | |
| CN213643675U (en) | Special odor treatment system for recovering N-methyl pyrrolidone | |
| CN217312751U (en) | Biological deodorization equipment | |
| CN208234665U (en) | A kind of water treatment device by ozone oxidation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |