CN202519126U - Square aerated biofilter reactor integrating denitrification dephosphorization functions - Google Patents
Square aerated biofilter reactor integrating denitrification dephosphorization functions Download PDFInfo
- Publication number
- CN202519126U CN202519126U CN2012200059251U CN201220005925U CN202519126U CN 202519126 U CN202519126 U CN 202519126U CN 2012200059251 U CN2012200059251 U CN 2012200059251U CN 201220005925 U CN201220005925 U CN 201220005925U CN 202519126 U CN202519126 U CN 202519126U
- Authority
- CN
- China
- Prior art keywords
- square
- sewage
- vertical sedimentation
- pipe
- aerated
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model belongs to the field of sewage treatment and relates to a square aerated biofilter reactor integrating denitrification and dephosphorization functions. The reactor can be produced industrially and can be applied to factories and enterprises with a small quantity of sewage and used for the treatment of urban sewage. The reactor comprises a regulation cell (1); the regulation cell (1) is connected with a vertical sedimentation cell (5) by a sewage metering pump (2); a pipe connecting the sewage metering pump (2) and the vertical sedimentation cell (5) is provided with a pipe-type static mixer (4); the bottom part of the vertical sedimentation cell (5) is connected with a sludge discharging pipe (19); discharged water at the upper part of the vertical sedimentation cell overflows into a square aerated biofilter (6); the bottom part of the square aerated biofilter (6) is provided with an aerated tray (12), an aerated pipe (11), a back-washing water inlet pipe (15) and a water outlet pipe (9); an air compressor (10) is connected with the aerated pipe (11); a back-washing pump (14) is connected with the back-washing water inlet pipe (15); the vertical sedimentation cell (5) is arranged in the square aerated biofilter (6); and, filling inside the square aerated biofilter (6) is calcium carbonate-type biological filling. The reactor provided by the utility model is simple and compact in structure; and, the aim of sewage purification is realized by carrying out the chemical sedimentation dephosphorization, the physical interception and the biological oxidization treatment on the sewage.
Description
Technical field
The present invention relates to a kind of integration denitrification and dephosphorization square BAF reactor drum, can be used for the treatment unit of municipal wastewater.
Background technology
The removal of nitrogen and phosphorus has caused people's extensive concern in the sewage, and denitrogenation dephosphorizing research has great significance to water environment protection.Wastewater treatment in China factory denitrification dephosphorization technique ubiquity the energy consumption height at present, efficient is low and the shortcoming of fluctuation of service.To this present situation, research is fit to China's national situation and cost-effective denitrification dephosphorization technique and method, particularly develops the COD oxidation with minimum, minimum CO
2Release, minimum excess sludge production, the recovery of phosphorus and the sustainable sewage disposal technology that the treating water reuse is target become imperative.
BAF is a kind of novel sewage disposal technology that grows up the America and Europe late 1980s; Have that processing efficiency height, floor space are little, capital construction and characteristics such as working cost is low, convenient management and capacity of resisting impact load are strong, at the organic matter removal of sewage, nitrated deammoniation, denitrification denitrogenation application promise in clinical practice is arranged.
The phosphor in sewage nutrition content increases, and be disposed to natural water after the WWT and still contain a large amount of phosphorus, be the major cause that causes eutrophication.Can know from present research; BAF is owing to lack necessary alternately anaerobism one aerobic condition of biological phosphate-eliminating; It has been generally acknowledged that the single-stage BAF only depends on biological assimilation and physical filtering dephosphorization efficiency by using to be everlasting about 20% under the conventional operation condition, reach as high as 35%.The dephosphorization efficiency by using of single-stage BAF is the technical barrier of its practical applications of puzzlement always.This patent has improved the effect of BAF denitrogenation dephosphorizing effectively with chemical precipitation and being integral of BAF organic assembling denitrogenation dephosphorizing reactor drum.
Summary of the invention
The utility model purpose is to solve the low problem of dephosphorization efficiency by using that above-mentioned BAF exists, and a kind of integration denitrification and dephosphorization square BAF reactor drum is provided.Reactor drum comprises equalizing tank (1); Equalizing tank is connected with vertical sedimentation basin (5) through Sewage metering pump (2); On the pipeline section that connects Sewage metering pump (2) and vertical sedimentation basin (5), tubular static mixer (4) is installed; Vertical sedimentation basin (5) bottom is connected to shore pipe (19), and the water outlet overflow of vertical sedimentation basin top gets into square BAF (6), and aeration plate (12), aeration tube (11), back flushing water inlet pipe (15), rising pipe (9) are installed in square BAF (6) bottom; Air (10) is connected with aeration tube (11); Backwash pump (14) is connected with back flushing water inlet pipe (15), and vertical sedimentation basin (5) places square BAF (6) inside, and square BAF (6) inner stuffing is a lime carbonate type biofilter material.
For addressing the above problem, the utility model comprises coagulation device, vertical sedimentation basin and square BAF.Coagulation device adopts tubular static mixer, is located on the former water water inlet pipe, is used for adding of coagulating agent.Vertical sedimentation basin top is that settling region, bottom are the mud district, is buffer zone between two districts, and water gets in the pond from pipe core from top to bottom, and the umbellate form baffle plate is established in the exit, makes water uniform distribution in the pond, and the bottom is connected to shore pipe.The top water outlet of vertical sedimentation basin gets into the square BAF through overflow all around, and the filter tank comprises supporting layer, packing area, air distribution and water distribution district and aerating apparatus.Aerating apparatus places the air distribution and water distribution district, and the air distribution and water distribution district is connected to aeration plate, rising pipe, back flushing water inlet pipe.
Described coagulation device is a tubular static mixer, simple in structure, advantages of small volume, do not need special occupied ground, install easily, less investment, long service life, mixing efficiency be high, reach moment to mix the purpose of saving the energy.
The water inlet of deposition part is that through the deposition part, SS content significantly reduces in the former water by the mixing liquid of sump pump pressurization through coagulation device, for follow-up square BAF provides best influent quality parameter, and gets rid of most of phosphorus in the water.
There are filtrating area and exhalant region in described biological filter; The built-in lime carbonate type of filtrating area biofilter material, the bottom supporting layer is a pebbles, the bottom links to each other with exhalant region through the porous supporting plate; Water after the precipitation process gets into the filter tank via overflow around the vertical sedimentation basin top; Even for aeration, be provided with aeration plate in the exhalant region, be connected with air through aeration tube.The distribution district of the exhalant region of bottom during as aeration, the water distributing area during also as back flushing, backwash tube links to each other with backwash water through the backwash pump pressurization.
The vertical sedimentation basin outer wall is a square, and BAF is built in its outside for square, and the outer wall of vertical sedimentation basin is as the inwall in filter tank, UNICOM not mutually, and vertical sedimentation basin water is by top overflow to filter tank, and the operation in two ponds is not disturbed mutually, and is stable.
The utility model compact construction, modular construction are convenient to the later stage reorganization and expansion, and equipment production, can be used for the less factory and enterprise of sewage quantity.Chemical precipitation dephosphorization, physics through to sewage is held back, is reached bio-oxidation and handles, and reaches the purpose of sewage purification, helps to protect environment, economizes on resources.
Description of drawings
Fig. 1 is the synoptic diagram of a kind of integration denitrification and dephosphorization square of the utility model BAF reactor drum.
Fig. 2 is an A-A sectional view among Fig. 1.
Among the figure: 1 equalizing tank, 2 Sewage metering pumps, 3 waste pipes, 4 tubular static mixers, 5 vertical sedimentation basins; 6 square BAFs, 7 fillers, 8 supporting layers, 9 rising pipes, 10 air; 11 aeration tubes, 12 aeration plates, 13 water tanks, 14 backwash pumps, 15 back flushing water pipes; 16 shore pipes, 17 mixing pits, 18 volume pumps, 19 chemical feed pipes, 20 back flushing rising pipes.
Embodiment
Accompanying drawing is a kind of specific embodiment of the utility model, and this embodiment comprises the equalizing tank 1 of collecting sewage, and equalizing tank 1 gets into vertical sedimentation basin 5 through Sewage metering pump 2 through waste pipe 3; The mixing pit 17 of preparation coagulating agent; Through the volume pump 18 of dosing coagulant, be connected with tubular static mixer 4, coagulating agent gets into vertical sedimentation basin 5 through 3 waste pipes behind the sewage thorough mixing in tubular static mixer; The vertical sedimentation basin bottom is connected to shore pipe 16; Water through after vertical sedimentation basin 5 processing gets into square BAF 6 through overflow, and the air distribution and water distribution district of bottom, square aeration tank is provided with aeration plate 12, and aeration plate is connected with air 10 through aeration tube 11; And backwash tube 15 is connected with backwashing pump 14, and top, aeration tank is connected to back flushing rising pipe 20.
Sewage in equalizing tank 1 regulating pondage and water quality, is got into vertical sedimentation basin 5 through Sewage metering pump 2 through 3 waste pipes.Tubular static mixer 4 is housed on the waste pipe, and coagulating agent gets into tubular static mixer through the pressurization of 18 volume pumps, coagulating agent warp 3 waste pipe vertical sedimentation basins 5 behind the sewage thorough mixing in static mixer; Carry out preliminary sedimentation, the vertical sedimentation basin bottom is connected to shore pipe 16, and the mud of post precipitation was intermittently discharged through certain cycle; Mud is transported through car after simple process, and the water after handling through vertical sedimentation basin 5 gets into square BAF 6 through overflow, ventilates in the aeration tank through air 10; For mikrobe provides competent oxygen; When reaching predetermined head loss, back flushing is carried out in the filter tank, at first carry out air purge by air 10; Opening backwash pump 14 pressurization then carries out air water to the filter tank and unites flushing; Close air 10 afterwards, with backwash pump 14 pressurizations the filter tank is washed, the water of back flushing is discharged through the back flushing rising pipe.
Claims (4)
1. integration denitrification and dephosphorization square BAF reactor drum; Reactor drum comprises equalizing tank (1); Equalizing tank is connected with vertical sedimentation basin (5) through Sewage metering pump (2); On the pipeline section that connects Sewage metering pump (2) and vertical sedimentation basin (5), tubular static mixer (4) is installed, vertical sedimentation basin (5) bottom is connected to shore pipe (19), and the water outlet overflow of vertical sedimentation basin top gets into square BAF (6).
2. integration denitrification and dephosphorization square BAF reactor drum as claimed in claim 1; It is characterized in that; Aeration plate (12), aeration tube (11), back flushing water inlet pipe (15), rising pipe (9) are installed in described square BAF (6) bottom; Air (10) is connected with aeration tube (11), and backwash pump (14) is connected with back flushing water inlet pipe (15).
3. integration denitrification and dephosphorization square BAF reactor drum as claimed in claim 1 is characterized in that vertical sedimentation basin (5) places square BAF (6) inside.
4. integration denitrification and dephosphorization square BAF reactor drum as claimed in claim 1 is characterized in that square BAF (6) inner stuffing is a lime carbonate type biofilter material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200059251U CN202519126U (en) | 2012-01-09 | 2012-01-09 | Square aerated biofilter reactor integrating denitrification dephosphorization functions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200059251U CN202519126U (en) | 2012-01-09 | 2012-01-09 | Square aerated biofilter reactor integrating denitrification dephosphorization functions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202519126U true CN202519126U (en) | 2012-11-07 |
Family
ID=47102086
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200059251U Expired - Fee Related CN202519126U (en) | 2012-01-09 | 2012-01-09 | Square aerated biofilter reactor integrating denitrification dephosphorization functions |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202519126U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288205A (en) * | 2013-06-19 | 2013-09-11 | 河南城建学院 | Integrated composite type bio-membrane reactor |
| CN104261508A (en) * | 2014-10-17 | 2015-01-07 | 北京昊业同宇科技有限公司 | Wastewater phosphorous removal equipment and method based on medium adsorption |
-
2012
- 2012-01-09 CN CN2012200059251U patent/CN202519126U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288205A (en) * | 2013-06-19 | 2013-09-11 | 河南城建学院 | Integrated composite type bio-membrane reactor |
| CN103288205B (en) * | 2013-06-19 | 2014-10-22 | 河南城建学院 | Integrated composite type bio-membrane reactor |
| CN104261508A (en) * | 2014-10-17 | 2015-01-07 | 北京昊业同宇科技有限公司 | Wastewater phosphorous removal equipment and method based on medium adsorption |
| CN104261508B (en) * | 2014-10-17 | 2016-01-13 | 北京昊业同宇科技有限公司 | Based on sewage dephosphorization equipment and the method for media adsorbs |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101618923B (en) | Wastewater treatment method | |
| CN102775025B (en) | Municipal life wastewater treatment system with high efficiency and low energy consumption | |
| CN201864644U (en) | Integrated denitrification and dephosphorization sewage treatment pond | |
| CN106116045A (en) | A kind of efficiently villages and small towns waste water treating and reutilizing device and technique thereof | |
| CN107253797A (en) | A kind of samll cities and towns' rural sewage treatment process | |
| CN206512058U (en) | A kind of efficient villages and small towns waste water treating and reutilizing device | |
| CN108178438A (en) | A kind of rural domestic sewage treatment system and purification method | |
| CN101618924B (en) | Wastewater treatment device | |
| CN103193360B (en) | Nitrogen and phosphorus removal integrated biological aerated filter water purification system and water purification method thereof | |
| CN115893750A (en) | Zero emission approaching system and method for treating high-concentration organic industrial wastewater | |
| CN108314255A (en) | A kind of efficient Chinese herbal medicine extraction sewage treatment process | |
| CN100500593C (en) | Combined type wastewater treatment method and equipment | |
| CN201751397U (en) | Sewage treatment device of ozone and aeration biological filter pool | |
| CN102040316A (en) | Method for purifying ecological compound sludge water body | |
| CN202519126U (en) | Square aerated biofilter reactor integrating denitrification dephosphorization functions | |
| CN103819062B (en) | MBR (membrane biological reactor) sewage treatment equipment for integrated fluidizing pool | |
| CN218146052U (en) | Biochemical and physical integrated treatment tank for village and town sewage A2O | |
| CN103193359B (en) | Deposition and biological filter combined water purification system | |
| CN114656104B (en) | Energy-saving self-circulation A3O-MBBR sewage treatment device and method thereof | |
| CN201648181U (en) | Pre-denitrification aeration biological filter | |
| CN202519125U (en) | Synergistic precipitation and biological filter combined reactor | |
| CN202519084U (en) | Porous steel slag filter material sink filter reactor | |
| CN204848603U (en) | Integration sewage advanced treatment unit | |
| CN210393887U (en) | Small-size sewage treatment integration equipment | |
| CN209702393U (en) | Modified form bio-contact oxidation integrated sewage treating apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121107 Termination date: 20150109 |
|
| EXPY | Termination of patent right or utility model |