CN202046977U - Anaerobic-aerobic integrated reactor - Google Patents
Anaerobic-aerobic integrated reactor Download PDFInfo
- Publication number
- CN202046977U CN202046977U CN2011201660477U CN201120166047U CN202046977U CN 202046977 U CN202046977 U CN 202046977U CN 2011201660477 U CN2011201660477 U CN 2011201660477U CN 201120166047 U CN201120166047 U CN 201120166047U CN 202046977 U CN202046977 U CN 202046977U
- Authority
- CN
- China
- Prior art keywords
- reactor
- anaerobic
- abr
- baf
- aerobic
- 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
- 238000005192 partition Methods 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 238000005273 aeration Methods 0.000 claims description 5
- 238000012856 packing Methods 0.000 claims description 3
- 239000010865 sewage Substances 0.000 abstract description 19
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 13
- 238000011001 backwashing Methods 0.000 description 8
- 239000005416 organic matter Substances 0.000 description 7
- 239000010802 sludge Substances 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 241001148470 aerobic bacillus Species 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
本实用新型公开了一种厌氧-好氧一体化反应器,属污水处理装置。包括壳体,壳体的内腔用隔板分隔成两个室,一个是厌氧折流板反应器ABR,另一个是曝气生物滤池反应器BAF,两者中间通过连接管将厌氧折流板反应器ABR和曝气生物滤池反应器BAF连通构成一体;所述的连接管的两端分别连接在厌氧折流板反应器ABR和曝气生物滤池反应器BAF的上部。有益效果是结构简单、管理方便、处理效能高、接触时间长、出水水质好、占地面积小,降低了工程投资等优点的一体化反应器。
The utility model discloses an anaerobic-aerobic integrated reactor, which belongs to a sewage treatment device. Including the shell, the inner cavity of the shell is divided into two chambers with a partition, one is the anaerobic baffle reactor ABR, and the other is the aerated biological filter reactor BAF, and the anaerobic reactor is connected through a connecting pipe between the two chambers. The baffle reactor ABR and the biological aerated filter reactor BAF are connected to form a whole; the two ends of the connecting pipe are respectively connected to the upper parts of the anaerobic baffle reactor ABR and the biological aerated filter reactor BAF. The beneficial effect is that the integrated reactor has the advantages of simple structure, convenient management, high treatment efficiency, long contact time, good effluent quality, small occupied area, and reduced engineering investment.
Description
技术领域 technical field
本实用新型涉及一种污水处理装置,具体是一种厌氧-好氧一体化反应器。主要适用于处理各种有机废水,尤其是高浓度有机废水。The utility model relates to a sewage treatment device, in particular to an anaerobic-aerobic integrated reactor. It is mainly suitable for treating various organic wastewater, especially high-concentration organic wastewater.
背景技术 Background technique
目前在有机废水的生物处理方面常采用厌氧法或好氧法两大类,相对于好氧法,厌氧处理具有很多优点,例如污泥产率低、能耗低、可回收沼气等。但目前常用的厌氧生物处理法存在各种问题或缺陷,如应用最为广泛的升流式厌氧污泥床(UASB)需要复杂的三相分离器、在低温条件下或启动初期或处理低浓度有机废水时处理效率低下。At present, anaerobic or aerobic methods are often used in the biological treatment of organic wastewater. Compared with aerobic methods, anaerobic treatment has many advantages, such as low sludge yield, low energy consumption, and recyclable biogas. However, there are various problems or defects in the commonly used anaerobic biological treatment methods. For example, the most widely used upflow anaerobic sludge bed (UASB) requires a complicated three-phase separator, and it is difficult to obtain a solid waste under low temperature conditions or at the beginning of start-up or when the treatment process is low. The treatment efficiency is low when the concentration of organic wastewater is high.
厌氧折流板反应器(ABR)是上世纪80年代开发的一种高效厌氧反应器,ABR是一个由多隔室组成的高效新型反应器,ABR反应器是一种连续流的多隔室结构,污水依次流经各隔室而得到降解,反应器每个隔室都有一个厌氧污泥层,其功能与UASB反应区类似,不同的是ABR反应器不设置三相分离器。其工艺既有生物截留能力强、运行管理方便、性能可靠等优点。但ABR反应器作为厌氧生物处理工艺的一种,具有厌氧生物处理的共性,即对有机物虽然有着较高的处理率,但反应器出水中仍旧含有大量的有机物,出水不能达到排放标准,往往在厌氧反应器后需要加好氧处理,进一步去除厌氧反应器出水中的有机物。Anaerobic Baffled Reactor (ABR) is a high-efficiency anaerobic reactor developed in the 1980s. ABR is a high-efficiency new reactor composed of multiple compartments. The structure of the chamber, the sewage flows through each compartment in turn to be degraded, each compartment of the reactor has an anaerobic sludge layer, its function is similar to that of the UASB reaction zone, the difference is that the ABR reactor does not have a three-phase separator. The process has the advantages of strong biological interception capacity, convenient operation and management, and reliable performance. However, as a kind of anaerobic biological treatment process, the ABR reactor has the commonality of anaerobic biological treatment, that is, although it has a high treatment rate for organic matter, the effluent of the reactor still contains a large amount of organic matter, and the effluent cannot meet the discharge standard. It is often necessary to add aerobic treatment after the anaerobic reactor to further remove the organic matter in the effluent of the anaerobic reactor.
曝气生物滤池(BAF)是上世纪90年代初期兴起的好氧污水处理工艺,它具有集生物氧化和截留悬浮物于一体的特点,节省后续沉淀池,具有容积负荷高、水力停留时间短、基建投资少、出水水质高等有点。Biological aerated filter (BAF) is an aerobic sewage treatment process that emerged in the early 1990s. It has the characteristics of integrating biological oxidation and intercepting suspended solids, saves subsequent sedimentation tanks, and has high volume load and short hydraulic retention time. , less investment in infrastructure, and high quality of effluent water.
工程上处理有机废水普遍采用的是厌氧-好氧组合工艺,但现行的厌氧-好氧组合工艺往往是单独的两套设备,投资与占地均较大,并且厌氧反应器与好氧反应器一般采用直接结合使得设备容易产生短流,影响处理效果。The anaerobic-aerobic combined process is commonly used in engineering to treat organic wastewater, but the current anaerobic-aerobic combined process is often two separate sets of equipment, which requires a large investment and land occupation, and the anaerobic reactor and good Oxygen reactors generally adopt direct coupling, which makes the equipment prone to short flow and affects the treatment effect.
发明内容 Contents of the invention
为解决厌氧-好氧组合工艺设备存在的上述问题与缺陷,本实用新型提供一种厌氧-好氧一体化反应器,是将ABR反应器和BAF反应器处理污水的一体化反应器。该装置结构简单、管理方便、处理效能高、接触时间长、出水水质好、占地面积小,降低了工程投资等优点的一体化反应器。In order to solve the above-mentioned problems and defects of anaerobic-aerobic combined process equipment, the utility model provides an anaerobic-aerobic integrated reactor, which is an integrated reactor for treating sewage with ABR reactor and BAF reactor. The device is an integrated reactor with simple structure, convenient management, high treatment efficiency, long contact time, good effluent quality, small footprint, and reduced engineering investment.
本实用新型采用如下技术方案实现的:一种厌氧-好氧一体化反应器,包括壳体,壳体的内腔用隔板分隔成两个室,一个是厌氧厌氧折流板反应器ABR,另一个是曝气生物滤池反应器BAF,两者中间通过连接管将厌氧折流板反应器ABR和曝气生物滤池反应器BAF连通构成一体;所述的连接管的两端分别连接在厌氧折流板反应器ABR和曝气生物滤池反应器BAF的上部。The utility model is realized by adopting the following technical scheme: an anaerobic-aerobic integrated reactor, including a shell, the inner cavity of the shell is divided into two chambers by a partition, one is an anaerobic anaerobic baffle plate reaction The other is the biological aerated filter reactor BAF, and the anaerobic baffle reactor ABR and the biological aerated filter reactor BAF are connected through a connecting pipe to form a whole; the two connecting pipes The ends are respectively connected to the upper part of the anaerobic baffle reactor ABR and the biological aerated filter reactor BAF.
经预处理的污水进入厌氧段的ABR反应器中,在此阶段发生厌氧反应,经过厌氧菌的降解使污水中的有机物浓度大大降低。经过厌氧处理的污水再经由连接装置进入到BAF反应器的顶端,污水自上向下流动,通过BAF反应器充氧,为好氧菌提供氧,好氧微生物分解污水中剩余的有机物,使污水中的污染物浓度进一步降低,并达到排放要求。The pretreated sewage enters the ABR reactor in the anaerobic section, where anaerobic reaction occurs, and the concentration of organic matter in the sewage is greatly reduced through the degradation of anaerobic bacteria. After anaerobic treatment, the sewage enters the top of the BAF reactor through the connection device. The sewage flows from top to bottom, and is oxygenated through the BAF reactor to provide oxygen for aerobic bacteria. The aerobic microorganisms decompose the remaining organic matter in the sewage, making the The concentration of pollutants in the sewage is further reduced and meets the discharge requirements.
本实用新型的有益效果是:The beneficial effects of the utility model are:
1、本实用新型将厌氧反应器和好氧反应器结合成为一体,反应器结构紧凑简单,降低了成本,减少了体积;1. The utility model combines the anaerobic reactor and the aerobic reactor into one, and the reactor has a compact and simple structure, which reduces the cost and volume;
2、在厌氧-好氧条件下,能够高效去除高浓度的有机废水,并且剩余污泥量少,可省去污泥沉淀池和剩余污泥处理步骤,节省基建费用和运行费用;2. Under anaerobic-aerobic conditions, it can efficiently remove high-concentration organic wastewater, and the amount of residual sludge is small, which can save sludge sedimentation tanks and residual sludge treatment steps, saving infrastructure costs and operating costs;
3、采用厌氧折流板反应器,该反应器内布置的竖向折流板,既起到了混合搅拌的作用,又增加了厌氧污泥与污水的接触时间,提高了处理效果。3. The anaerobic baffle reactor is adopted. The vertical baffles arranged in the reactor not only play the role of mixing and stirring, but also increase the contact time between anaerobic sludge and sewage, and improve the treatment effect.
4、本实用新型采用了ABR+BAF组合的处理工艺,可以处理高浓度的有机废水,处理效果好,能够有效保证出水水质。4. The utility model adopts the combined treatment process of ABR+BAF, which can treat high-concentration organic wastewater with good treatment effect and can effectively ensure the quality of effluent.
附图说明 Description of drawings
图1是本实用新型的厌氧-好氧一体化反应器剖面结构示意图。Fig. 1 is a schematic cross-sectional structure diagram of an anaerobic-aerobic integrated reactor of the present invention.
图2是本实用新型的厌氧-好氧一体化反应器平面结构示意图。Fig. 2 is a schematic plan view of the anaerobic-aerobic integrated reactor of the present invention.
图中:1、进水管,2、沼气收集装置,3、连通管,4、控制阀,5、反冲洗出水管,6、填料层,7、承托层,8、曝气装置,9、出水与反冲洗进水管,10、分隔板,11、折流板,12、厌氧折流板反应器ABR,13、曝气生物滤池反应器BAF,14、壳体。In the figure: 1. Water inlet pipe, 2. Biogas collection device, 3. Connecting pipe, 4. Control valve, 5. Backwash outlet pipe, 6. Packing layer, 7. Supporting layer, 8. Aeration device, 9. Outlet and backwash inlet pipes, 10, partition plate, 11, baffle plate, 12, anaerobic baffle plate reactor ABR, 13, biological aerated filter reactor BAF, 14, shell.
具体实施方式 Detailed ways
如图1、图2所示,本实用新型包括壳体14,壳体14为长方形,其内腔用隔板分隔成两个室,一个是厌氧折流板反应器ABR12,另一个是曝气生物滤池反应器BAF13,两者中间通过连接管3将厌氧折流板反应器ABR12和曝气生物滤池反应器BAF13连通构成一体;所述的连接管3的两端分别连接在厌氧折流板反应器ABR12和曝气生物滤池反应器BAF13的上部。As shown in Figure 1 and Figure 2, the utility model includes a housing 14, the housing 14 is rectangular, and its inner cavity is divided into two chambers with a partition, one is the anaerobic baffle reactor ABR12, and the other is the exposure chamber. Gas biological filter reactor BAF13, the anaerobic baffle reactor ABR12 and the biological aerated filter reactor BAF13 are connected through the connecting pipe 3 to form a whole; the two ends of the connecting pipe 3 are respectively connected to the anaerobic The upper part of oxygen baffle reactor ABR12 and biological aerated filter reactor BAF13.
在厌氧折流板反应器ABR 12反应器内设有3-5个分隔板10和数量对应的折流板11,本实施例设3个分隔板10将厌氧折流板反应器分隔成4个隔室。分隔板和折流板竖直安装,焊接在反应器的壳体14上,在反应器的一侧有进水口1,上部有沼气出气管。厌氧折流板反应器ABR 12的上方还安装有沼气收集装置2。In the anaerobic baffle reactor ABR 12 reactor, be provided with 3-5 dividing plates 10 and the corresponding baffles 11 of quantity, present embodiment establishes 3 dividing plates 10 and anaerobic baffled reactor Divided into 4 compartments. The partition plate and the baffle plate are installed vertically and welded on the shell 14 of the reactor. There is a water inlet 1 on one side of the reactor and a biogas outlet pipe on the top. A biogas collection device 2 is also installed above the anaerobic baffle reactor ABR 12.
曝气生物滤池反应器BAF13内安装有曝气装置8,自下向上依次装置有承托层7和填料层6。本实施例曝气装置8安装在底部。靠底部有出水与反冲洗进水管9,上部有反冲洗出水管5和控制反冲洗出水管的控制阀4。An aeration device 8 is installed in the biological aerated filter reactor BAF13, and a supporting layer 7 and a packing layer 6 are installed in sequence from bottom to top. In this embodiment, the aeration device 8 is installed at the bottom. Water outlet and backwashing water inlet pipe 9 are arranged by the bottom, and the backwashing water outlet pipe 5 and the control valve 4 controlling the backwashing water outlet pipe are arranged on the top.
污水处理过程为:经预处理的污水由进水管1进入厌氧段的ABR反应器中,污水依次流经四隔室的ABR反应器,在此阶段发生厌氧反应,经过厌氧菌的降解污水中的有机物浓度大大降低。经过厌氧处理的污水再经由连通管3进入到BAF反应器的顶端,污水自上向下流动,通过曝气充氧装置8向好氧段的BAF反应器充氧,为好氧菌提供氧,附着在填料上的好氧微生物则分解污水中剩余的有机物,是水中的污染物浓度进一步降低,并达到排放要求,经由出水管9出水;当填料上的生物膜厚度过厚时,可进行反冲洗,首先进水管1停止进水,并打开控制阀4,反冲洗进水管9进水进行反冲洗,反冲洗的出水由反冲洗出水管5排出。所述厌氧-好氧一体化反应器整体形状为矩形。The sewage treatment process is as follows: the pretreated sewage enters the ABR reactor in the anaerobic section from the inlet pipe 1, and the sewage flows through the four-compartment ABR reactor in turn, and anaerobic reaction occurs at this stage, and it is degraded by anaerobic bacteria. The concentration of organic matter in the sewage is greatly reduced. After anaerobic treatment, the sewage enters the top of the BAF reactor through the connecting pipe 3, and the sewage flows from top to bottom, and oxygenates the BAF reactor in the aerobic section through the aeration and oxygenation device 8 to provide oxygen for the aerobic bacteria. , the aerobic microorganisms attached to the filler decompose the remaining organic matter in the sewage, so that the concentration of pollutants in the water is further reduced, and the discharge requirements are met, and the water is discharged through the outlet pipe 9; when the thickness of the biofilm on the filler is too thick, it can be carried out For backwashing, at first the water inlet pipe 1 stops the water intake, and the control valve 4 is opened, the backwashing water inlet pipe 9 is fed with water for backwashing, and the backwashing water is discharged from the backwashing outlet pipe 5. The overall shape of the anaerobic-aerobic integrated reactor is rectangular.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201660477U CN202046977U (en) | 2011-05-16 | 2011-05-16 | Anaerobic-aerobic integrated reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201660477U CN202046977U (en) | 2011-05-16 | 2011-05-16 | Anaerobic-aerobic integrated reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202046977U true CN202046977U (en) | 2011-11-23 |
Family
ID=44987295
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201660477U Expired - Fee Related CN202046977U (en) | 2011-05-16 | 2011-05-16 | Anaerobic-aerobic integrated reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202046977U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104211268A (en) * | 2014-09-29 | 2014-12-17 | 洛阳绿仁环保设备有限公司 | Industrial wastewater treatment device |
| CN104609558A (en) * | 2015-01-30 | 2015-05-13 | 广西师范大学 | Partial nitrification-denitrification integrated ABR reactor |
| CN105712480A (en) * | 2016-05-09 | 2016-06-29 | 杨秉恭 | Biological treatment system applicable to medium-concentration and high-concentration organic waste water and water treatment method thereof |
| CN109851176A (en) * | 2019-03-22 | 2019-06-07 | 南京工业大学 | Anaerobic digestion and three-level MBBR combined process for treating organic wastewater |
-
2011
- 2011-05-16 CN CN2011201660477U patent/CN202046977U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104211268A (en) * | 2014-09-29 | 2014-12-17 | 洛阳绿仁环保设备有限公司 | Industrial wastewater treatment device |
| CN104609558A (en) * | 2015-01-30 | 2015-05-13 | 广西师范大学 | Partial nitrification-denitrification integrated ABR reactor |
| CN105712480A (en) * | 2016-05-09 | 2016-06-29 | 杨秉恭 | Biological treatment system applicable to medium-concentration and high-concentration organic waste water and water treatment method thereof |
| CN109851176A (en) * | 2019-03-22 | 2019-06-07 | 南京工业大学 | Anaerobic digestion and three-level MBBR combined process for treating organic wastewater |
| CN109851176B (en) * | 2019-03-22 | 2024-04-30 | 南京工业大学 | Anaerobic digestion and three-stage MBBR combined process for treating organic wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100465107C (en) | U-shaped flow biological aerated filter | |
| CN103951062B (en) | A kind of anaerobic-aerobic baffled reactor | |
| CN202131151U (en) | Efficient compound sewage treatment tower type bioreactor | |
| CN102502957B (en) | Internal recycle anaerobic membrane bioreactor with single reaction area | |
| CN102503044A (en) | Recycling system for treating community wastewater through combining membrane bioreactor and constructed wetland | |
| CN102951731B (en) | Airlift oxidation ditch type membrane bioreactor | |
| CN201395547Y (en) | A sewage treatment device | |
| CN103011404B (en) | Internal-mixing anaerobic reaction tank | |
| CN105347475B (en) | A kind of symmetrical built-in anaerobic membrane bioreactor | |
| CN115893662A (en) | Device and method for realizing deep denitrification of main stream and side stream sewage of sewage treatment plant based on double-short-range anaerobic ammonium oxidation combined with sludge fermentation | |
| CN202046977U (en) | Anaerobic-aerobic integrated reactor | |
| CN108328858A (en) | The recycling treatment system and method for train toilet waste collector fecaluria waste liquid | |
| CN202099166U (en) | Integrated circuit (IC) anaerobic reactor | |
| CN201424414Y (en) | A self-circulating anaerobic reactor and a sewage treatment device using the reactor | |
| CN201512461U (en) | Anaerobic and aerobic integrated water treatment bioreactor | |
| CN101386449A (en) | An anaerobic reactor for treating wastewater with high organic concentration and high solid content | |
| CN109775936B (en) | Low-energy-consumption domestic sewage treatment system | |
| CN220766703U (en) | Novel granular sludge membrane biological reaction device | |
| CN203007037U (en) | Internal mixing anaerobic reactor | |
| CN217947887U (en) | Waste water purification device | |
| CN106906127B (en) | An integrated anaerobic fermentation device for gas production and purification that can generate electricity independently | |
| CN212559635U (en) | Hybrid membrane biological anaerobic fermentation reactor for kitchen wastewater | |
| CN201021444Y (en) | High-efficiency composite sewage purification and reuse device | |
| CN105776652B (en) | A kind of residual sludge enhanced adsorption-membrane separation water treatment device and method | |
| CN204111412U (en) | A kind of circulating sludge bed anaerobic reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111123 Termination date: 20120516 |
