CN203866098U - High-efficiency anaerobic and aerobic integrated reactor - Google Patents
High-efficiency anaerobic and aerobic integrated reactor Download PDFInfo
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- CN203866098U CN203866098U CN201420279605.4U CN201420279605U CN203866098U CN 203866098 U CN203866098 U CN 203866098U CN 201420279605 U CN201420279605 U CN 201420279605U CN 203866098 U CN203866098 U CN 203866098U
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Abstract
The utility model belongs to the technical field of sewage treatment, and discloses a high-efficiency anaerobic and aerobic integrated reactor. The anaerobic and aerobic integrated reactor is in a cylindrical structure, and comprises an anaerobic baffled reactor and a biological aerated filter, wherein the biological aerated filter is arranged in the center of the cylindrical structure; the anaerobic baffled reactor is arranged on an outer ring of the biological aerated filter, and divided into an A compartment, a B compartment, a C compartment and a D compartment via partition plates; the D compartment of the anaerobic baffled reactor is provided with a connecting pipe; the connecting pipe is connected with the biological aerated filter; and a gate valve capable of controlling sewage backflow after anaerobic treatment is arranged on the partition plate between the A compartment and the D compartment. The anaerobic and aerobic integrated reactor is in the cylindrical structure, and is provided with the gate valve capable of controlling the sewage backflow after the anaerobic treatment, so that the acid resistance of the anaerobic reactor is improved.
Description
Technical field
The utility model belongs to technical field of sewage, is specifically related to a kind of efficient anaerobic-aerobic integratedization reactor.
Background technology
At present aspect the biological treatment of organic waste water, often adopting anaerobic process or the large class of aerobic method two.Anaerobic process has that accretion rate is slow, the residence time is long, container volume is large, influence factor is many, high cost unfavorable factor, aerobic method is obvious to BOD removal effect, but colourity and COD clearance are low, and the high working cost of aerobic method and the not solution of excess sludge handling problems.In view of the feature of above two kinds of methods, the aerobic coupling technique of anaerobism one becomes the main flow technique of the various high-concentration industrial-waters of current processing and sanitary sewage.
Anaerobic Methods in Treating is developed so far the history of existing more than 100 year.At first, Anaerobic Methods in Treating is mainly used in the digestion process of mud; Since the seventies, anaerobic waste water treatment technology is because it has reduced investment, working cost is low and can produce the advantages such as energy (biogas) that can provide recycling, and obtain sending out faster the development into representative, and there is a collection of anaerobic reactor treatment technology that can be detained a large amount of microbial solids with up flow anaerobic sludge blanket reactor (UASB), but UASB technical requirements is high, and granular sludge is stricter to processing requirement; Since the eighties in 20th century, people, being fully recognized that on the basis of advantage that UASB reactor for treatment technique is unique and existing deficiency, have developed some new and effective anaerobic reactor anaerobic baffled reactors.The similar a plurality of UASB reactors connection of its structure, in reactor, microorganism, with flow process alternation step by step, has ideally been realized the multistage process thought of SMPA phase-splitting, thereby has had preferably contaminant removal capacity.
Compare with other Anaerobic biotreatment method, the most obvious advantage of ABR technique is not need special consideration Gas-solid-liquid separater, due to repeatedly upper and lower baffling effect of current in reactor, having improved sludge microbe body contacts with the mixing of processed wastewater room, in compartment, formed the microorganism chain of stable performance, population no-float, to adapt to the current water quality situation of the different compartments that flows through, organism is by the dissimilar microbiological deterioration in different compartments, promoted formation and the growth of granule sludge, reactor can long-time running and is not needed spoil disposal.By reactor, reasonably design, ABR technique also can realize integrated two-phase or multiphase treating processes in a reactor, this is also that other anaerobic technique is incomparable, yet acidifying problem has become the bottleneck that the high efficiency anaerobic reactors such as restriction ABR are promoted, and how the anti-souring ability of enhancing reactor has become the focus that high-load anaerobic reactor is researched and developed.Adopt sewage backflow can avoid reactor front end compartment to cause pH value to reduce the acidifying phenomenon causing because producing more VFA, can regulate basicity, the granulating of accelerate sludge, shortens the reactor start-up time, improves the output of methane; Also can dilute the hazardous and noxious substances in water inlet, thereby improve treatment effect, reduce acidifying risk.In addition, ABR reactor is a kind of as Anaerobic treatment technique, although although organism is had to higher processing rate, but in reactor water outlet, still contain a large amount of organism, water outlet can not reach emission standard, often after anaerobic reactor, need to add aerobic treatment, further remove the organism in anaerobic reactor water outlet.
BAF (BAF) is the aerobic sewage treatment process rising the phase at the beginning of the nineties in last century, it has the advantages that to integrate bio-oxidation and hold back suspended substance, save post precipitation pond, have that volumetric loading is high, hydraulic detention time is short, initial cost is few, effluent quality advantages of higher.
The aerobic coupling technique of anaerobism one can make the poor polymer substance of biodegradability in waste water, at anaerobism section generation acidication, becomes small molecules, thereby improves wastewater biodegradability, for aerobic treatment creates conditions.But the floor space of biological treatment structures is generally larger, and structure is not compact, and its application and development are restricted.
Utility model content
In order to solve the shortcoming and defect part of prior art, primary and foremost purpose of the present utility model is to provide a kind of efficient anaerobic-aerobic integratedization reactor.
The utility model object is achieved through the following technical solutions:
A kind of efficient anaerobic-aerobic integratedization reactor, comprise anaerobic baffled reactor (ABR) and BAF (BAF), described anaerobic-aerobic integrated reactor is cylindrical structural, BAF (BAF) is located at the central position of cylinder type, its open top, BAF sets gradually annular water distribution groove from top to bottom, filter material layer and supporting layer, aerating apparatus is set, the external aeration tube of aerating apparatus in supporting layer; Anaerobic baffled reactor (ABR) is in the outer ring of BAF (BAF), its top arranges the cover plate that guarantees anaerobic environment, anaerobic baffled reactor is divided into A, B, C, tetra-compartments of D by dividing plate, compartment is cascaded structure, each compartment is all divided into lower current area and ascending zone by traverse baffle, and alternative arrangement, the push-pull valve can control sewage backflow after anaerobic treatment is set on the dividing plate between compartment A and compartment D, compartment D arranges pipe connecting and is communicated with BAF.
It is 1/3 position of dividing plate height that described push-pull valve is arranged on from the distance of dividing plate upper end, and lower than pipe connecting height.
Triangle effluent weir is set, to improve the stability of water outlet on the inwall of described annular water distribution groove.
Described BAF also arranges back-purge system, and back-purge system is comprised of the back flushing water inlet pipe of supporting layer bottom and the back flushing rising pipe on distributing trough top.
Described ABR is equipped with the gas extractor of collecting biogas in top, and gas extractor is located at the ascending zone central position of each compartment cover, external gas extractor.
Described BAF (BAF) is 1:1.5 with the volume ratio of anaerobic baffled reactor (ABR).
The lower current area of described anaerobic baffled reactor (ABR) compartment and the volume ratio of ascending zone are 1:3.
The upwards bending from the horizontal by 45 ° of angles of described traverse baffle bottom.
Principle of work of the present utility model is: sewage enters lower current area and the ascending zone of compartment A successively from the water inlet pipe of anaerobic baffled reactor, and successively by compartment B, compartment C and compartment D, in the process of anaerobic baffled reactor of flowing through, there is anaerobic reaction in sewage, through the degraded of anerobe, the organic concentration in sewage reduces greatly.A sewage part through anaerobic treatment is back in compartment A by push-pull valve, reflux ratio is 0.5, another part is entered in the annular water distribution groove of BAF (BAF) by pipe connecting, in distributing trough, sewage flows out from triangle effluent weir, evenly flows from top to bottom, and aerating apparatus is to reactor oxygenation, for aerobic bacteria provides oxygen, the aerobic microbiological being attached on filter material layer decomposes remaining organism in sewage, the Pollutant levels in sewage is further reduced, and reach emission request.Water after processing is flowed out by the rising pipe of BAF bottom.When biofilm thickness on filter material layer is blocked up, carry out back flushing, first the water inlet pipe of anaerobic baffled reactor stops into water, close pipe connecting, open the valve on back flushing rising pipe, backwashing water is intake by back flushing water inlet pipe, and backwashing water flows to distributing trough from bottom to top and discharges outside pond by back flushing rising pipe.
Device tool of the present utility model has the following advantages and beneficial effect:
(1) efficient anaerobic of the present utility model-aerobic integratedization reactor is cylindrical structural, BAF (BAF) is located at the central position of cylinder type, anaerobic baffled reactor (ABR) is in the outer ring of BAF (BAF), realized the integrated of anaerobism structures, aerobic structures, guaranteeing under water quality treatment prerequisite up to standard, reduce the floor space of structures, saved construction investment;
(2) setting of efficient anaerobic of the present utility model-aerobic integratedization reactor can be controlled the push-pull valve of sewage backflow after anaerobic treatment, improved the capacity antacid of anaerobic reactor, be convenient to operational management, carrying out that can also rapid stimulation anaerobic reaction, improves biogas output.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model efficient anaerobic-aerobic integratedization reactor;
Fig. 2 is the deployed configuration schematic diagram of the anaerobic baffled reactor (ABR) of the utility model efficient anaerobic-aerobic integratedization reactor;
Fig. 3 is the structural representation of the BAF (BAF) of anaerobic-aerobic integrated reactor of the present utility model;
Description of reference numerals is as follows: 1 is water inlet pipe; 2 is the outer wall of ABR; 3,5,7,9 is traverse baffle; 4,6,8,10 is compartment dividing plate; 11 is pipe connecting; 12 is the inwall of ABR, the 13 annular water distribution grooves that are BAF; 14 for being provided with the annular water distribution groove inwall of triangle effluent weir; 15 is the back flushing rising pipe of BAF; 16,17,18,19 gas extractors that are ABR; 20 is push-pull valve; 21 is filter material layer, and 22 is supporting layer, and 23 is aerating apparatus, and 24 is aeration tube, and 25 is back flushing water inlet pipe; A, B, C, D are respectively four compartments of ABR, and A1, B1, C1, D1 are respectively the lower current area of compartment A, B, C, D; E is the pond body of BAF (BAF).
Embodiment
Below in conjunction with embodiment, the utility model is described in further detail, but embodiment of the present utility model is not limited to this.
Embodiment 1
As Fig. 1, shown in Fig. 2 and Fig. 3, a kind of efficient anaerobic-aerobic integratedization reactor of the present embodiment, comprise anaerobic baffled reactor (ABR) and BAF (BAF), described anaerobic-aerobic integrated reactor is cylindrical structural, and BAF is located at the central position of cylinder type, and ABR is in the outer ring of BAF, the volume ratio of BAF and ABR is 1:1.5, ABR is surrounded by reactor outer wall 2 and reactor wall 12, and reactor outer wall is provided with water inlet pipe 1, and ABR is by dividing plate 4, 6, 8, 10 are divided into A, B, C, tetra-compartments of D, compartment is cascaded structure, four compartments are respectively by traverse baffle 3, 5, 7, 9 are divided into lower current area and ascending zone, and alternative arrangement, the upwards bending from the horizontal by 45 ° of angles of traverse baffle bottom, the lower current area being separated by traverse baffle and the volume ratio of ascending zone are 1:3, ABR top arranges the cover plate that guarantees anaerobic environment, and on cover plate, four compartment ascending zone central positions arrange respectively gas extractor 16, 17, 18, the compartment D of 19, ABR arranges pipe connecting 11 and is communicated with BAF, and the push-pull valve 20 can control sewage backflow after anaerobic treatment is set on dividing plate 10, and it is 1/3 position of dividing plate height that push-pull valve is arranged on from the distance of dividing plate upper end, and lower than pipe connecting height, the BAF pond body E of open top sets gradually annular water distribution groove 13, filter material layer 21 and supporting layer 22 from top to bottom, annular water distribution groove is surrounded by ABR reactor wall 12 and the distributing trough inwall 14 that is provided with triangle effluent weir, aerating apparatus 23 is set, the external aeration tube 24 of aerating apparatus in supporting layer, BAF also arranges back-purge system, and back-purge system is comprised of the back flushing water inlet pipe 25 of supporting layer bottom and the back flushing rising pipe 15 on distributing trough top.
The working process of the present embodiment efficient anaerobic-aerobic integratedization reactor is:
Sewage enters lower current area and the ascending zone of compartment A successively from the water inlet pipe of ABR, and successively by compartment B, compartment C and compartment D, in the process of ABR of flowing through, there is anaerobic reaction in sewage, the biogas that reaction produces is collected by gas extractor, through the degraded of anerobe, the organic concentration in sewage reduces greatly, a sewage part through anaerobic treatment is back in compartment A by push-pull valve, according to the discharge of sewage, adjusting the size of push-pull valve and control sewage backflow ratio is 0.5, another part is entered in the distributing trough of BAF by pipe connecting, in distributing trough, sewage flows out by water outlet V-notch weir, downward water distribution uniformity, aerating apparatus is to reactor oxygenation, for aerobic bacteria provides oxygen, the aerobic microbiological being attached on filter material layer decomposes remaining organism in sewage, Pollutant levels in sewage are further reduced, and reach emission request, water after processing is flowed out by the rising pipe of BAF bottom.When biofilm thickness on filter material layer is blocked up, carry out back flushing, first the water inlet pipe of anaerobic baffled reactor stops into water, close pipe connecting, open the valve on back flushing rising pipe, backwashing water is intake by back flushing water inlet pipe, and backwashing water flows to distributing trough from bottom to top and discharges outside pond by back flushing rising pipe.
Above-described embodiment is preferably embodiment of the utility model; but embodiment of the present utility model is not restricted to the described embodiments; other any do not deviate from change, the modification done under spirit of the present utility model and principle, substitutes, combination, simplify; all should be equivalent substitute mode, within being included in protection domain of the present utility model.
Claims (8)
1. efficient anaerobic-aerobic integratedization reactor, comprise anaerobic baffled reactor and BAF, it is characterized in that: described anaerobic-aerobic integrated reactor is cylindrical structural, BAF is located at the central position of cylindrical structure, its open top, BAF sets gradually annular water distribution groove from top to bottom, filter material layer and supporting layer, aerating apparatus is set, the external aeration tube of aerating apparatus in supporting layer; Anaerobic baffled reactor is in the outer ring of BAF, its top arranges the cover plate that guarantees anaerobic environment, anaerobic baffled reactor is divided into A, B, C, tetra-compartments of D by dividing plate, compartment is cascaded structure, each compartment is all divided into lower current area and ascending zone by traverse baffle, and alternative arrangement, the push-pull valve that can control sewage backflow is set on the dividing plate between compartment A and compartment D, compartment D arranges pipe connecting and is communicated with BAF.
2. a kind of efficient anaerobic-aerobic integratedization reactor according to claim 1, is characterized in that: it is 1/3 position of dividing plate height that described push-pull valve is arranged on from the distance of dividing plate upper end, and lower than pipe connecting height.
3. a kind of efficient anaerobic-aerobic integratedization reactor according to claim 1, is characterized in that: the triangle effluent weir that water distribution uniformity is set on the inwall of described annular water distribution groove.
4. a kind of efficient anaerobic-aerobic integratedization reactor according to claim 1, it is characterized in that: described BAF also arranges back-purge system, back-purge system is comprised of the back flushing water inlet pipe of supporting layer bottom and the back flushing rising pipe on distributing trough top.
5. a kind of efficient anaerobic-aerobic integratedization reactor according to claim 1, is characterized in that: the gas extractor of collecting biogas is housed in described anaerobic baffled reactor top blind flange, and gas extractor is positioned at each compartment ascending zone central position.
6. a kind of efficient anaerobic-aerobic integratedization reactor according to claim 1, is characterized in that: the volume ratio of described BAF and anaerobic baffled reactor is 1:1.5.
7. a kind of efficient anaerobic-aerobic integratedization reactor according to claim 1, is characterized in that: the lower current area of described anaerobic baffled reactor compartment and the volume ratio of ascending zone are 1:3.
8. a kind of efficient anaerobic-aerobic integratedization reactor according to claim 1, is characterized in that: the upwards bending from the horizontal by 45 ° of angles of described traverse baffle bottom.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420279605.4U CN203866098U (en) | 2014-05-28 | 2014-05-28 | High-efficiency anaerobic and aerobic integrated reactor |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106379995A (en) * | 2016-08-31 | 2017-02-08 | 沈阳建筑大学建筑设计研究院 | Improved denitrification and phosphorous removing apparatus of A2O coupled biological rotating disc |
| CN106630151A (en) * | 2017-02-13 | 2017-05-10 | 广东益康生环保科技有限公司 | Integral breeding wastewater treatment device and method for treating breeding wastewater by using integral breeding wastewater treatment device |
| CN107935175A (en) * | 2017-12-20 | 2018-04-20 | 江苏蓝必盛化工环保股份有限公司 | A kind of ABR anaerobic reactors |
| CN108439598A (en) * | 2018-05-02 | 2018-08-24 | 长沙中联重科环境产业有限公司 | Integrated sewage treating apparatus |
| CN109867403A (en) * | 2017-12-01 | 2019-06-11 | 中国水利水电科学研究院 | A kind of processing unit and sewage water treatment method of dispersing type sewage |
| CN110818083A (en) * | 2019-12-03 | 2020-02-21 | 杭州师范大学 | Realize integral type reactor of resourceful denitrogenation sulphur removal |
| CN110845011A (en) * | 2019-12-17 | 2020-02-28 | 清华大学 | Multi-medium biological filter and distributed sewage treatment device |
| CN112537845A (en) * | 2020-12-02 | 2021-03-23 | 北京建筑大学 | Rural sewage anaerobic resource utilization system and method |
| CN114560594A (en) * | 2022-01-21 | 2022-05-31 | 清华大学 | Modular fast-assembling wetland sewage treatment device |
| CN110845011B (en) * | 2019-12-17 | 2024-06-07 | 吉林十亩恬源环境科技有限公司 | Multi-medium biological filter and distributed sewage treatment device |
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2014
- 2014-05-28 CN CN201420279605.4U patent/CN203866098U/en not_active Expired - Fee Related
Cited By (13)
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| CN106379995B (en) * | 2016-08-31 | 2022-09-27 | 沈阳建筑大学设计集团有限公司 | Improved A 2 O-coupled biological rotating disc denitrification dephosphorization device |
| CN106379995A (en) * | 2016-08-31 | 2017-02-08 | 沈阳建筑大学建筑设计研究院 | Improved denitrification and phosphorous removing apparatus of A2O coupled biological rotating disc |
| CN106630151A (en) * | 2017-02-13 | 2017-05-10 | 广东益康生环保科技有限公司 | Integral breeding wastewater treatment device and method for treating breeding wastewater by using integral breeding wastewater treatment device |
| CN109867403A (en) * | 2017-12-01 | 2019-06-11 | 中国水利水电科学研究院 | A kind of processing unit and sewage water treatment method of dispersing type sewage |
| CN109867403B (en) * | 2017-12-01 | 2023-09-22 | 中国水利水电科学研究院 | Decentralized sewage treatment device and sewage treatment method |
| CN107935175A (en) * | 2017-12-20 | 2018-04-20 | 江苏蓝必盛化工环保股份有限公司 | A kind of ABR anaerobic reactors |
| CN108439598A (en) * | 2018-05-02 | 2018-08-24 | 长沙中联重科环境产业有限公司 | Integrated sewage treating apparatus |
| CN110818083A (en) * | 2019-12-03 | 2020-02-21 | 杭州师范大学 | Realize integral type reactor of resourceful denitrogenation sulphur removal |
| CN110845011A (en) * | 2019-12-17 | 2020-02-28 | 清华大学 | Multi-medium biological filter and distributed sewage treatment device |
| CN110845011B (en) * | 2019-12-17 | 2024-06-07 | 吉林十亩恬源环境科技有限公司 | Multi-medium biological filter and distributed sewage treatment device |
| CN112537845B (en) * | 2020-12-02 | 2022-05-17 | 北京建筑大学 | Rural sewage anaerobic resource utilization system and method |
| CN112537845A (en) * | 2020-12-02 | 2021-03-23 | 北京建筑大学 | Rural sewage anaerobic resource utilization system and method |
| CN114560594A (en) * | 2022-01-21 | 2022-05-31 | 清华大学 | Modular fast-assembling wetland sewage treatment device |
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Granted publication date: 20141008 Termination date: 20170528 |