CN219567747U - Organic wastewater treatment equipment - Google Patents
Organic wastewater treatment equipment Download PDFInfo
- Publication number
- CN219567747U CN219567747U CN202320544621.0U CN202320544621U CN219567747U CN 219567747 U CN219567747 U CN 219567747U CN 202320544621 U CN202320544621 U CN 202320544621U CN 219567747 U CN219567747 U CN 219567747U
- Authority
- CN
- China
- Prior art keywords
- cylinder
- vertical
- strong oxidation
- outlet
- adsorption
- 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
Classifications
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Physical Water Treatments (AREA)
Abstract
An organic wastewater treatment device belongs to the technical field of water treatment, and particularly relates to an organic wastewater treatment device. The utility model provides organic wastewater treatment equipment with good treatment effect. The utility model comprises a hydrogen peroxide storage tank and a sewage storage tank, and is characterized in that the lower outlet of the hydrogen peroxide storage tank is connected with the inlet of a hydrogen peroxide water outlet valve, the lower outlet of the sewage storage tank is connected with the inlet of a sewage water outlet valve, the outlet of the hydrogen peroxide water outlet valve is connected with the first inlet of a mixer, the outlet of the sewage water outlet valve is connected with the second inlet of the mixer, the outlet of the mixer is connected with the inlet of an adsorption module, the outlet of the adsorption module is connected with the inlet of a strong oxidation module through an adsorption main valve, and the outlet of the strong oxidation module is connected with the inlet of a photocatalysis module.
Description
Technical Field
The utility model belongs to the technical field of water treatment, and particularly relates to an organic wastewater treatment device.
Background
China is a large country of livestock and poultry farming, and according to investigation, 3581 counties related to the livestock and poultry farming in 2022 China are provided in 2015 by water pollution control action plan, so that the livestock and poultry farming gradually goes to highly intensive, specialized and regional development from traditional decentralized and small-scale home feeding. The livestock and poultry raising wastewater is paid attention to because the wastewater is rich in high-concentration organic matters, ammonia nitrogen and suspended particles.
The COD, total nitrogen and total phosphorus discharged by the livestock and poultry breeding industry are higher than the water pollutant discharge amount of the industrial pollution source by about 46.67%, 19.61% and 37.95% in the national water pollutant discharge amount, and the livestock and poultry breeding industry becomes a main pollution source of agricultural non-point source pollution, and if the livestock and poultry breeding industry is not effectively treated, the livestock and poultry breeding industry not only endangers the ecological environment, but also threatens the health of human beings, and is the problem to be solved urgently at present.
At present, the methods for treating livestock and poultry breeding wastewater at home and abroad mainly comprise a physical method, a biological method and a natural treatment method. The physical method for removing pollutants is limited in variety, is mainly used for removing solid pollutants such as inorganic particles, precipitates, suspended matters and the like and a small amount of organic pollutants in wastewater, and has no method for removing most of soluble pollutants in wastewater. The biological method has good ecological effect, but the biological method has some limitations, and firstly, the treatment efficiency is unstable and can be influenced by various factors such as the availability of the nutrient of the wastewater, the self-adsorption mechanism of the organism, the operation condition and the like. Meanwhile, the biological treatment efficiency is greatly influenced by seasons, the removing effect in summer is best, and the effect in winter is poor. Secondly, the biological method has the defects of large occupied area, long starting time, need of supplementing carbon sources, slow repairing process, low nitrogen and phosphorus removal efficiency and the like, and the popularization and the application of the biological method are severely limited. How to combine the advantages of the different methods becomes critical for technical innovation and device development.
Disclosure of Invention
The utility model aims at the problems and provides organic wastewater treatment equipment with good treatment effect.
In order to achieve the purpose, the utility model adopts the following technical scheme that the device comprises a hydrogen peroxide storage tank and a sewage storage tank, and is characterized in that the lower outlet of the hydrogen peroxide storage tank is connected with an inlet of a hydrogen peroxide water outlet valve, the lower outlet of the sewage storage tank is connected with an inlet of a sewage water outlet valve, the outlet of the hydrogen peroxide water outlet valve is connected with a first inlet of a mixer, the outlet of the sewage water outlet valve is connected with a second inlet of the mixer, the outlet of the mixer is connected with an inlet of an adsorption module, the outlet of the adsorption module is connected with an inlet of a strong oxidation module through an adsorption main valve, and the outlet of the strong oxidation module is connected with an inlet of a photocatalysis module.
As a preferable scheme, the air outlet of the strong oxidation module is connected with the air inlet end of the air duct through a strong oxidation valve, and the air outlet of the photocatalysis module is connected with the air inlet end of the air duct through a photocatalysis valve; the air outlet end of the air duct is arranged at the lower part in the exhaust gas tank, a port plug is arranged at the upper port of the exhaust gas tank, and the air duct and the exhaust pipe penetrate through the port plug; the air inlet end of the exhaust pipe is arranged at the upper part in the exhaust gas tank, and the air outlet end of the exhaust pipe is arranged at the outer part of the exhaust gas tank.
As another preferable scheme, the air outlet end of the exhaust pipe is connected with a defoamer.
As another preferable scheme, the liquid outlet of the photocatalysis module is connected with the inlet of the water quality detection control device, the reflux port of the water quality detection control device is connected with the inlet of the first three-way valve through a reflux pipe, the inlet of the strong oxidation module is connected with the first outlet of the first three-way valve, and the second outlet of the first three-way valve is connected with the upper water return port of the reclaimed water storage tank; the lower outlet of the reclaimed water storage tank is connected with the inlet of the reclaimed water outlet valve, and the outlet of the reclaimed water outlet valve is connected with the first inlet of the mixer.
As another preferable scheme, the water quality detection control device comprises a COD detector and a second three-way valve, wherein the liquid outlet of the photocatalysis module is connected with the liquid inlet of the second three-way valve through a detection channel of the COD detector, the first liquid outlet of the second three-way valve is connected with a return pipe, and the second liquid outlet of the second three-way valve is a standard-closing treated water outlet.
As another preferable scheme, the adsorption module comprises an upper tank body and a lower tank body, wherein an inlet at the lower end of the upper tank body is connected with an outlet at the upper end of the lower tank body, and an inlet at the lower end of the lower tank body is connected with an outlet of a mixer;
the middle parts of the upper tank body and the lower tank body are vertical middle adsorption cylinders, the upper ends of the vertical middle adsorption cylinders are connected with the large bottom side of the lower end of the upper adsorption round platform cylinder, the lower ends of the vertical middle adsorption cylinders are connected with the large bottom side of the upper end of the lower adsorption round platform cylinder, the small bottom side of the upper end of the upper adsorption round platform cylinder is connected with the lower end of the vertical upper adsorption cylinder, and the small bottom side of the lower end of the lower adsorption round platform cylinder is connected with the upper end of the vertical lower adsorption cylinder;
the middle part of the lower end of the vertical lower adsorption cylinder of the lower tank body is an inlet of the adsorption module, and the middle part of the upper end of the vertical upper adsorption cylinder of the upper tank body is an outlet of the adsorption module;
the junction of vertical well adsorption cylinder and last adsorption round platform section of thick bamboo lower extreme is provided with and adsorbs the orifice plate, and the junction of vertical well adsorption cylinder and lower adsorption round platform section of thick bamboo upper end is provided with down and adsorbs the orifice plate.
As another preferable scheme, the upper tank body and the lower tank body are combined into a plurality of groups which are connected in series, and the adjacent groups are connected through adsorption branch valves.
As another preferable scheme, the middle part of the strong oxidation module is a vertical strong oxidation cylinder, the upper end of the vertical strong oxidation cylinder is connected with the large bottom side of the lower end of the upper strong oxidation round platform cylinder, the lower end of the vertical strong oxidation cylinder is connected with the large bottom side of the upper end of the lower strong oxidation round platform cylinder, the small bottom side of the upper end of the upper strong oxidation round platform cylinder is connected with the lower end of the vertical upper strong oxidation cylinder, and the small bottom side of the lower end of the lower strong oxidation round platform cylinder is connected with the upper end of the vertical lower strong oxidation cylinder;
the middle part of the lower end of the vertical lower strong oxidation cylinder is provided with an inlet of the strong oxidation module, and the middle part of the upper end of the vertical upper strong oxidation cylinder is provided with an outlet of the strong oxidation module;
an upper strong oxidation pore plate is arranged at the joint of the upper end of the vertical strong oxidation cylinder and the lower end of the upper strong oxidation round platform cylinder, and a lower strong oxidation pore plate is arranged at the joint of the lower end of the vertical strong oxidation cylinder and the upper end of the lower strong oxidation round platform cylinder.
As another preferable scheme, the combination of the strong oxidation module and the strong oxidation valve is a plurality of groups connected in series.
Secondly, the middle part of the photocatalysis module is a vertical photocatalysis cylinder, the upper end of the vertical photocatalysis cylinder is connected with the big bottom side of the lower end of the upper photocatalysis round platform cylinder, the lower end of the vertical photocatalysis cylinder is connected with the big bottom side of the upper end of the lower photocatalysis round platform cylinder, the small bottom side of the upper photocatalysis round platform cylinder is connected with the lower end of the vertical upper photocatalysis cylinder, and the small bottom side of the lower photocatalysis round platform cylinder is connected with the upper end of the vertical lower photocatalysis cylinder;
the middle part of the lower end of the vertical lower photocatalytic cylinder is an inlet of the photocatalytic module, and the middle part of the upper end of the vertical upper photocatalytic cylinder is an outlet of the photocatalytic module;
an upper photocatalysis pore plate is arranged at the joint of the upper end of the vertical photocatalysis cylinder and the lower end of the upper photocatalysis round platform cylinder, and a lower photocatalysis pore plate is arranged at the joint of the lower end of the vertical photocatalysis cylinder and the upper end of the lower photocatalysis round platform cylinder.
In addition, the combination of the photocatalysis module and the photocatalysis valve is a plurality of groups connected in series.
The utility model has the beneficial effects that.
The hydrogen peroxide storage tank of the utility model carries out precipitation treatment on sewage, thereby creating better conditions for the first-step adsorption.
The utility model organically combines the adsorption method, the strong oxidation method and the photocatalysis method. The adsorption module plays a role in stabilizing concentration fluctuation, the strong oxidation module plays a role in degrading organic matters, and the photocatalysis module is used for treating residual organic matters and hydrogen peroxide.
The utility model is a chemical treatment mode, is not affected by seasons, and has strong adaptability and high treatment efficiency.
The utility model adopts a modularized structure, can carry out modularized assembly (increase and decrease of the number of modules) according to water quality and water quantity, has flexible use and wide application range.
Drawings
The utility model is further described below with reference to the drawings and the detailed description. The scope of the present utility model is not limited to the following description.
Fig. 1 is a schematic diagram of the structure of the present utility model.
In the figure, 1 is a reclaimed water storage tank, 2 is a hydrogen peroxide storage tank, 3 is a sewage storage tank, 4 is a sewage outlet valve, 5 is a hydrogen peroxide outlet valve, 6 is a reclaimed water outlet valve, 7 is a mixer, 8 is a lower tank body, 9 is an upper tank body, 10 is an adsorption branch valve, 11 is an adsorption main valve, 12 is an adsorption module, 13 is a strong oxidation module, 14 is a photocatalysis module, 15 is a vertical strong oxidation cylinder, 16 is a first three-way valve, 17 is a strong oxidation valve, 18 is a photocatalysis valve, 19 is an air duct, 20 is a vertical photocatalysis cylinder, 21 is a water quality detection control device, 22 is a standard combination treatment water outlet, 23 is a reflux pipe, 24 is a defoamer, and 25 is an exhaust gas tank.
Detailed Description
As shown in the figure, the sewage treatment device comprises a hydrogen peroxide storage tank 2 and a sewage storage tank 3 (sewage can be led into the sewage storage tank 3 through a sewage pipeline), wherein the lower outlet of the hydrogen peroxide storage tank 2 is connected with the inlet of a hydrogen peroxide water outlet valve 5, the lower outlet of the sewage storage tank 3 is connected with the inlet of a sewage water outlet valve 4, the outlet of the hydrogen peroxide water outlet valve 5 is connected with the first inlet of a mixer 7, the outlet of the sewage water outlet valve 4 is connected with the second inlet of the mixer 7, the outlet of the mixer 7 (which can be a UPVC material mixer) is connected with the inlet of an adsorption module 12, the outlet of the adsorption module 12 is connected with the inlet of a strong oxidation module 13 through an adsorption main valve 11, and the outlet of the strong oxidation module 13 is connected with the inlet of a photocatalysis module 14.
The gas outlet of the strong oxidation module 13 is connected with the gas inlet end of the gas guide pipe 19 through the strong oxidation valve 17, the gas outlet of the photocatalysis module 14 is connected with the gas inlet end of the gas guide pipe 19 through the photocatalysis valve 18, the gas outlet end of the gas guide pipe 19 is arranged at the inner lower part of the waste gas tank 25 (the waste gas tank 25 can be filled with paraffin oil containing carbon powder, absorbing smell in waste gas and deodorizing), a mouth plug is arranged at the upper port of the waste gas tank 25, and the gas guide pipe 19 and the exhaust pipe pass through the mouth plug; the air inlet end of the exhaust pipe is arranged at the upper part in the exhaust gas tank 25, and the air outlet end of the exhaust pipe is arranged outside the exhaust gas tank 25.
The exhaust pipe air outlet end is connected with a defoamer 24. The defoamer 24 can adopt an extrusion steel wire ball structure, and can extrude 1 kg of steel wire balls into balls under the pressure of 5MPa (the extruded balls can be wrapped by a screen frame, and a connecting port of the screen frame can be in threaded connection with the air outlet end of the exhaust pipe).
The liquid outlet of the photocatalysis module 14 is connected with the inlet of the water quality detection control device 21, the reflux port of the water quality detection control device 21 is connected with the inlet of the first three-way valve 16 through a reflux pipe 23, the inlet of the strong oxidation module 13 is connected with the first outlet of the first three-way valve 16, and the second outlet of the first three-way valve 16 is connected with the upper water return port of the reclaimed water storage tank 1;
the lower outlet of the reclaimed water storage tank 1 is connected with the inlet of the reclaimed water outlet valve 6, and the outlet of the reclaimed water outlet valve 6 is connected with the first inlet of the mixer 7.
The water quality detection control device 21 comprises a COD detector and a second three-way valve, the liquid outlet of the photocatalysis module 14 is connected with the liquid inlet of the second three-way valve through a detection channel of the COD detector, the first liquid outlet of the second three-way valve is connected with the return pipe 23, and the second liquid outlet of the second three-way valve is a standard-closing treated water outlet 22 (namely the standard-closing treated water outlet of the water quality detection control device 21).
The detection data of the COD detector can be sent to a control center, and the control center can control each valve.
The second three-way valve can be controlled according to the detection data of the COD detector. The qualified treated water is discharged through the standard-combining treated water discharge outlet 22, and the unqualified treated water is returned to the inlet of the reclaimed water storage tank 1 or the strong oxidation module 13 through the return pipe 23.
The adsorption module 12 comprises an upper tank body 9 and a lower tank body 8 (adopting the structures of the upper tank body 9 and the lower tank body 8 to increase the reaction progression and enhance the treatment effect), wherein the inlet at the lower end of the upper tank body 9 is connected with the outlet at the upper end of the lower tank body 8, and the inlet at the lower end of the lower tank body 8 is connected with the outlet of the mixer 7;
the middle parts of the upper tank body 9 and the lower tank body 8 are vertical middle adsorption cylinders, the upper ends of the vertical middle adsorption cylinders are connected with the large bottom side of the lower end of the upper adsorption round table cylinder, the lower ends of the vertical middle adsorption cylinders are connected with the large bottom side of the upper end of the lower adsorption round table cylinder, the small bottom side of the upper end of the upper adsorption round table cylinder is connected with the lower end of the vertical upper adsorption cylinder, and the small bottom side of the lower end of the lower adsorption round table cylinder is connected with the upper end of the vertical lower adsorption cylinder;
the middle part of the lower end of the vertical lower adsorption cylinder of the lower tank body 8 is provided with an inlet of the adsorption module 12, and the middle part of the upper end of the vertical upper adsorption cylinder of the upper tank body 9 is provided with an outlet of the adsorption module 12;
the junction of vertical well adsorption cylinder and last adsorption round platform section of thick bamboo lower extreme is provided with and adsorbs the orifice plate, and the junction of vertical well adsorption cylinder and lower adsorption round platform section of thick bamboo upper end is provided with down and adsorbs the orifice plate.
The adsorption pore plate can prevent the adsorption material from flowing out along with water, and the aperture of the adsorption pore plate can be 1 mm-3 mm.
The upper tank 9 and the lower tank 8 are combined into a plurality of groups which are connected in series (improving the adsorption effect), and the adjacent groups are connected through an adsorption branch valve 10.
The combination of the upper tank body 9 and the lower tank body 8 is two groups.
The middle part of the strong oxidation module 13 is a vertical strong oxidation cylinder 15, the upper end of the vertical strong oxidation cylinder 15 is connected with the big bottom side of the lower end of the upper strong oxidation round platform cylinder, the lower end of the vertical strong oxidation cylinder is connected with the big bottom side of the upper end of the lower strong oxidation round platform cylinder, the small bottom side of the upper end of the upper strong oxidation round platform cylinder is connected with the lower end of the vertical strong oxidation cylinder, and the small bottom side of the lower end of the lower strong oxidation round platform cylinder is connected with the upper end of the vertical lower strong oxidation cylinder;
the middle part of the lower end of the vertical lower strong oxidation cylinder is provided with an inlet of the strong oxidation module 13, and the middle part of the upper end of the vertical upper strong oxidation cylinder is provided with an outlet of the strong oxidation module 13;
an upper strong oxidation pore plate is arranged at the joint of the upper end of the vertical strong oxidation cylinder 15 and the lower end of the upper strong oxidation round platform cylinder, and a lower strong oxidation pore plate is arranged at the joint of the lower end of the vertical strong oxidation cylinder 15 and the upper end of the lower strong oxidation round platform cylinder.
The strong oxidation pore plate can prevent the strong oxidation materials from flowing out along with water.
The combination of the strong oxidation module 13 and the strong oxidation valve 17 is a plurality of groups connected in series.
The middle part of the photocatalysis module 14 is a vertical photocatalysis cylinder 20, the upper end of the vertical photocatalysis cylinder 20 is connected with the big bottom side of the lower end of the upper photocatalysis round platform cylinder, the lower end of the vertical photocatalysis cylinder is connected with the big bottom side of the upper end of the lower photocatalysis round platform cylinder, the small bottom side of the upper end of the upper photocatalysis round platform cylinder is connected with the lower end of the vertical upper photocatalysis cylinder, and the small bottom side of the lower photocatalysis round platform cylinder is connected with the upper end of the vertical lower photocatalysis cylinder;
the middle part of the lower end of the vertical lower photocatalytic cylinder is an inlet of the photocatalytic module 14, and the middle part of the upper end of the vertical upper photocatalytic cylinder is an outlet of the photocatalytic module 14;
an upper photocatalytic pore plate is arranged at the joint of the upper end of the vertical photocatalytic cylinder 20 and the lower end of the upper photocatalytic round platform cylinder, and a lower photocatalytic pore plate is arranged at the joint of the lower end of the vertical photocatalytic cylinder 20 and the upper end of the lower photocatalytic round platform cylinder.
The photocatalytic pore plate can prevent photocatalytic materials from flowing out along with water.
The combination of the photocatalytic module 14 and the photocatalytic valve 18 is a plurality of groups connected in series (to enhance the photocatalytic effect).
An ultraviolet lamp tube may be disposed at the inner center or on the inner side wall of the vertical photocatalytic cylinder 20. The outer side of the ultraviolet lamp tube can be provided with a protective net. The power supply circuit of the ultraviolet lamp tube is arranged in a conventional way.
The adsorption material can be activated carbon or Al 2 O 3 And (3) filling.
The strong oxidation material can be sodium sulfate block.
The photocatalytic material can be bulk TiO 2 Or Fe (Fe) 3 C。
Material inlets with sealing doors may be provided on the cylinders 8, 9, 15, 20.
It should be understood that the foregoing detailed description of the present utility model is provided for illustration only and is not limited to the technical solutions described in the embodiments of the present utility model, and those skilled in the art should understand that the present utility model may be modified or substituted for the same technical effects; as long as the use requirement is met, the utility model is within the protection scope of the utility model.
Claims (10)
1. The utility model provides an organic wastewater treatment equipment, including hydrogen peroxide solution storage tank and sewage storage tank, its characterized in that hydrogen peroxide solution storage tank's lower part export links to each other with the hydrogen peroxide solution outlet valve import, and the lower part export of sewage storage tank links to each other with the sewage outlet valve import, and hydrogen peroxide solution outlet valve export links to each other with the first import of blender, and the sewage outlet valve export links to each other with the second import of blender, and the export of blender links to each other with adsorption module's import, and adsorption module's export links to each other with the import of strong oxidation module through the absorption master valve, and the export of strong oxidation module links to each other with photocatalysis module's import.
2. The organic wastewater treatment device according to claim 1, wherein the gas outlet of the strong oxidation module is connected with the gas inlet end of the gas guide pipe through a strong oxidation valve, and the gas outlet of the photocatalysis module is connected with the gas inlet end of the gas guide pipe through a photocatalysis valve; the air outlet end of the air duct is arranged at the lower part in the exhaust gas tank, a port plug is arranged at the upper port of the exhaust gas tank, and the air duct and the exhaust pipe penetrate through the port plug; the air inlet end of the exhaust pipe is arranged at the upper part in the exhaust gas tank, and the air outlet end of the exhaust pipe is arranged at the outer part of the exhaust gas tank.
3. An organic wastewater treatment device according to claim 2, wherein the exhaust pipe is connected with a defoamer at the exhaust end.
4. The organic wastewater treatment equipment according to claim 1, wherein the liquid outlet of the photocatalysis module is connected with the inlet of the water quality detection control device, the reflux port of the water quality detection control device is connected with the inlet of the first three-way valve through a reflux pipe, the inlet of the strong oxidation module is connected with the first outlet of the first three-way valve, and the second outlet of the first three-way valve is connected with the upper water return port of the reclaimed water storage tank; the lower outlet of the reclaimed water storage tank is connected with the inlet of the reclaimed water outlet valve, and the outlet of the reclaimed water outlet valve is connected with the first inlet of the mixer.
5. The device for treating organic wastewater according to claim 4, wherein the water quality detection control device comprises a COD detector and a second three-way valve, the liquid outlet of the photocatalysis module is connected with the liquid inlet of the second three-way valve through a detection channel of the COD detector, the first liquid outlet of the second three-way valve is connected with the return pipe, and the second liquid outlet of the second three-way valve is a standard-closed treated water outlet.
6. An organic wastewater treatment device according to claim 1, wherein the adsorption module comprises an upper tank body and a lower tank body, wherein an inlet at the lower end of the upper tank body is connected with an outlet at the upper end of the lower tank body, and an inlet at the lower end of the lower tank body is connected with an outlet of the mixer;
the middle parts of the upper tank body and the lower tank body are vertical middle adsorption cylinders, the upper ends of the vertical middle adsorption cylinders are connected with the large bottom side of the lower end of the upper adsorption round platform cylinder, the lower ends of the vertical middle adsorption cylinders are connected with the large bottom side of the upper end of the lower adsorption round platform cylinder, the small bottom side of the upper end of the upper adsorption round platform cylinder is connected with the lower end of the vertical upper adsorption cylinder, and the small bottom side of the lower end of the lower adsorption round platform cylinder is connected with the upper end of the vertical lower adsorption cylinder;
the middle part of the lower end of the vertical lower adsorption cylinder of the lower tank body is an inlet of the adsorption module, and the middle part of the upper end of the vertical upper adsorption cylinder of the upper tank body is an outlet of the adsorption module;
the junction of vertical well adsorption cylinder and last adsorption round platform section of thick bamboo lower extreme is provided with and adsorbs the orifice plate, and the junction of vertical well adsorption cylinder and lower adsorption round platform section of thick bamboo upper end is provided with down and adsorbs the orifice plate.
7. The organic wastewater treatment device according to claim 6, wherein the upper tank body and the lower tank body are combined into a plurality of groups connected in series, and adjacent groups are connected through adsorption branch valves.
8. The organic wastewater treatment device according to claim 1, wherein the middle part of the strong oxidation module is a vertical strong oxidation cylinder, the upper end of the vertical strong oxidation cylinder is connected with the bottom side of the lower end of the upper strong oxidation round platform cylinder, the lower end of the vertical strong oxidation cylinder is connected with the bottom side of the upper end of the lower strong oxidation round platform cylinder, the small bottom side of the upper end of the upper strong oxidation round platform cylinder is connected with the lower end of the vertical strong oxidation cylinder, and the small bottom side of the lower end of the lower strong oxidation round platform cylinder is connected with the upper end of the vertical lower strong oxidation cylinder;
the middle part of the lower end of the vertical lower strong oxidation cylinder is provided with an inlet of the strong oxidation module, and the middle part of the upper end of the vertical upper strong oxidation cylinder is provided with an outlet of the strong oxidation module;
an upper strong oxidation pore plate is arranged at the joint of the upper end of the vertical strong oxidation cylinder and the lower end of the upper strong oxidation round platform cylinder, and a lower strong oxidation pore plate is arranged at the joint of the lower end of the vertical strong oxidation cylinder and the upper end of the lower strong oxidation round platform cylinder.
9. An organic wastewater treatment plant according to claim 2, wherein the combination of the strong oxidation module and the strong oxidation valve is in series.
10. The organic wastewater treatment equipment according to claim 1, wherein the middle part of the photocatalysis module is a vertical photocatalysis cylinder, the upper end of the vertical photocatalysis cylinder is connected with the big bottom side of the lower end of the upper photocatalysis round platform cylinder, the lower end of the vertical photocatalysis cylinder is connected with the big bottom side of the upper end of the lower photocatalysis round platform cylinder, the small bottom side of the upper photocatalysis round platform cylinder is connected with the lower end of the vertical photocatalysis cylinder, and the small bottom side of the lower photocatalysis round platform cylinder is connected with the upper end of the vertical lower photocatalysis cylinder;
the middle part of the lower end of the vertical lower photocatalytic cylinder is an inlet of the photocatalytic module, and the middle part of the upper end of the vertical upper photocatalytic cylinder is an outlet of the photocatalytic module;
an upper photocatalysis pore plate is arranged at the joint of the upper end of the vertical photocatalysis cylinder and the lower end of the upper photocatalysis round platform cylinder, and a lower photocatalysis pore plate is arranged at the joint of the lower end of the vertical photocatalysis cylinder and the upper end of the lower photocatalysis round platform cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320544621.0U CN219567747U (en) | 2023-03-20 | 2023-03-20 | Organic wastewater treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320544621.0U CN219567747U (en) | 2023-03-20 | 2023-03-20 | Organic wastewater treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219567747U true CN219567747U (en) | 2023-08-22 |
Family
ID=87671240
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320544621.0U Active CN219567747U (en) | 2023-03-20 | 2023-03-20 | Organic wastewater treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219567747U (en) |
-
2023
- 2023-03-20 CN CN202320544621.0U patent/CN219567747U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104628226B (en) | Plant's garbage total system | |
| CN203878024U (en) | Wastewater treatment system for culture farm | |
| CN107473471B (en) | Sewage purification treatment device | |
| CN103253823B (en) | Method and system for realizing efficient wastewater treatment and waste methane gas oxidation together via artificial wetland | |
| CN106554129A (en) | Integral synchronous nitration denitrification sewage-treatment plant | |
| CN108271730A (en) | A kind of low-carbon zero-emission industrial circulating water cultivating system based on anaerobic denitrifying | |
| CN201301254Y (en) | Buried type oligodynamic sewage treatment device | |
| CN110720420A (en) | Take water farming systems of anaerobism denitrification facility | |
| CN214142004U (en) | Treatment system of decentralized sewage | |
| CN219567747U (en) | Organic wastewater treatment equipment | |
| CN104291444A (en) | System and method for treatment of contact hydrolysis-algae micro-aeration composite wastewater | |
| CN107511068A (en) | A kind of intelligent and high-efficiency clarifier on pig farm | |
| CN110713315A (en) | Special sewage treatment device for sewage plant in villages and towns and treatment method thereof | |
| CN214571174U (en) | High ammonia-nitrogen concentration deodorization effluent disposal system | |
| CN212334937U (en) | Intelligent integrated sewage treatment equipment | |
| CN210215090U (en) | Small-size water purifier of vehicular | |
| CN210945164U (en) | Drinking water removes ammonia nitrogen device | |
| CN109399859A (en) | A kind of sewage disposal system using electrolysis method joint biological treatment | |
| CN208500689U (en) | A kind of sewage-treatment plant for agricultural breeding | |
| CN208136037U (en) | A kind of new bio nitrogen fixation process processing high ammonia-nitrogen wastewater complexes | |
| CN112142260A (en) | Treatment system and method for decentralized sewage | |
| CN206680352U (en) | A kind of new MBR integrated water treatment equipments | |
| CN202139113U (en) | Carbon fiber-composite membrane bioreactor | |
| CN201268654Y (en) | Ozone disinfection and downflow type aerating biological filter integrated sewage treating device | |
| CN205347135U (en) | Sewage treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |