CN209428226U - A kind of sludge dual reflux AOA biofilm treatment apparatus applied to sewage water denitrification - Google Patents
A kind of sludge dual reflux AOA biofilm treatment apparatus applied to sewage water denitrification Download PDFInfo
- Publication number
- CN209428226U CN209428226U CN201821970922.5U CN201821970922U CN209428226U CN 209428226 U CN209428226 U CN 209428226U CN 201821970922 U CN201821970922 U CN 201821970922U CN 209428226 U CN209428226 U CN 209428226U
- Authority
- CN
- China
- Prior art keywords
- connect
- sludge
- tank
- sewage
- water
- 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
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及污水处理技术领域,具体来说,涉及一种应用于污水脱氮的污泥双回流AOA生物膜处理装置。The utility model relates to the technical field of sewage treatment, in particular to a sludge double-reflux AOA biofilm treatment device applied to sewage denitrification.
背景技术Background technique
随着人们生活水平的提高,水体富营养化的现象日益严重,这主要是因为大量富含氮、磷等元素的生活污水和工业废水排放到河流、湖泊等自然水体中,超出了水体自净能力。水质发生恶化,对人们的生产生活以及可持续发展造成了严重的影响。因此,水体富营养化问题已经引起了广泛的关注和重视。近年来,我国已投入大量资金治理太湖、滇池等水体的富营养化。然而,要想恢复到污染前的状况仍然十分困难。解决水体富营养化问题的根本方法,在于对污水进行深度脱氮除磷后再排放到自然水体。目前,如何在实现高效脱氮除磷的同时降低能耗、费用,对污水生物处理具有重要意义。With the improvement of people's living standards, the phenomenon of water eutrophication is becoming more and more serious, mainly because a large amount of domestic sewage and industrial wastewater rich in nitrogen, phosphorus and other elements are discharged into natural water bodies such as rivers and lakes, which exceeds the self-purification capacity of water bodies. . The deterioration of water quality has seriously affected people's production and life and sustainable development. Therefore, the problem of water eutrophication has attracted extensive attention and attention. In recent years, my country has invested a lot of money to control the eutrophication of water bodies such as Taihu Lake and Dianchi Lake. However, it is still very difficult to restore the situation before pollution. The fundamental method to solve the problem of water eutrophication is to carry out deep denitrification and phosphorus removal of sewage and then discharge it into natural water bodies. At present, how to reduce energy consumption and cost while achieving efficient nitrogen and phosphorus removal is of great significance to sewage biological treatment.
实用新型内容Utility model content
针对相关技术中的上述技术问题,本实用新型提出一种应用于污水脱氮的污泥双回流AOA生物膜处理装置,能够克服现有技术的上述不足。Aiming at the above-mentioned technical problems in the related art, the utility model proposes a sludge double-reflux AOA biofilm treatment device applied to sewage denitrification, which can overcome the above-mentioned shortcomings of the prior art.
为实现上述技术目的,本实用新型的技术方案是这样实现的:For realizing above-mentioned technical purpose, technical scheme of the present utility model is realized like this:
一种应用于污水脱氮的污泥双回流AOA(厌氧/好氧/缺氧)生物膜处理装置,包括原水箱,所述原水箱通过进水管与进水泵的进水口连接,所述进水泵的出水口与厌氧池连接,所述厌氧池与好氧池连接,所述好氧池与缺氧池连接,所述厌氧池与二沉池连接,所述二沉池的底部分别通过与污泥回流管相连的污泥回流泵连接所述厌氧池和所述缺氧池,所述二沉池的上部设有出水管,所述缺氧池中设有生物填料。A sludge double-reflux AOA (anaerobic/aerobic/anoxic) biofilm treatment device applied to sewage denitrification, including a raw water tank, the raw water tank is connected to the water inlet of the water inlet pump through a water inlet pipe, and the inlet The water outlet of the water pump is connected with the anaerobic tank, the anaerobic tank is connected with the aerobic tank, the aerobic tank is connected with the anoxic tank, the anaerobic tank is connected with the secondary sedimentation tank, and the bottom of the secondary sedimentation tank The anaerobic tank and the anoxic tank are respectively connected through a sludge return pump connected with a sludge return pipe, the upper part of the secondary settling tank is provided with an outlet pipe, and the anoxic tank is provided with biological fillers.
进一步的,所述厌氧池、缺氧池均设有搅拌装置。Further, the anaerobic pool and anoxic pool are equipped with stirring devices.
进一步的,所述好氧池底部设有微孔曝气装置,所述微孔曝气装置通过气体流量计与气泵连接。Further, a microporous aeration device is provided at the bottom of the aerobic tank, and the microporous aeration device is connected to an air pump through a gas flow meter.
本实用新型的有益效果:The beneficial effects of the utility model:
(1)采用AOA生物膜形式对污水进行处理,此工艺与传统A2/O工艺对比,取消了硝化液回流,降低了运行成本;(1) The waste water is treated in the form of AOA biofilm. Compared with the traditional A 2 /O process, this process cancels the return flow of nitrifying liquid and reduces the operating cost;
(2)通过采用污泥双回流,提高了缺氧池的污泥浓度,使得活性污泥的内源反硝化速率加快,提高了污水处理过程中降解氮素的能力,使得出水指标优于排放标准。(2) By adopting double sludge return flow, the sludge concentration in the anoxic tank is increased, the endogenous denitrification rate of activated sludge is accelerated, and the ability to degrade nitrogen in the sewage treatment process is improved, so that the effluent index is better than that of the discharge standard.
(3)曝气池体积大幅减小,节省曝气能耗费用。(3) The volume of the aeration tank is greatly reduced, saving energy consumption for aeration.
(4)污泥停留时间长、剩余污泥微量或少量、耐受水质水量变化能力强、不存在MBR的膜污染问题,无需清洗;其二沉池出水后结合加磁絮凝沉淀池净水系统,对于市政污水,出水CODcr低于20-30mg/L、氨氮低于1mg/L、TN低于10mg/L,TP低于0.5mg/;总能耗低,耗气量省,维修维护少,运行成本远低于MBR;无需增添碳源(利用污水、污泥自身碳源);(4) Long sludge residence time, trace or small amount of residual sludge, strong ability to withstand changes in water quality and water volume, no MBR membrane pollution problem, no need to clean; the secondary sedimentation tank is combined with a magnetic flocculation sedimentation tank water purification system , for municipal sewage, the effluent CODcr is lower than 20-30mg/L, the ammonia nitrogen is lower than 1mg/L, the TN is lower than 10mg/L, and the TP is lower than 0.5mg/L; the total energy consumption is low, the gas consumption is low, the maintenance is less, and the operation The cost is much lower than MBR; there is no need to add carbon sources (using sewage and sludge carbon sources);
(5)本处理装置适于工程应用,适用于各种规模的污水处理厂新建及改造,该技术先进,节省投资、运行经济,出水水质好;(5) This treatment device is suitable for engineering applications, and is suitable for new construction and renovation of sewage treatment plants of various scales. The technology is advanced, investment is saved, operation is economical, and the effluent water quality is good;
(6)本处理装置能够实现污水深度脱氮,解决活性污泥浓度低的问题,并具有结构简单,污水处理效果好、效率高,适用于实际工程改造的特点。(6) This treatment device can realize deep denitrification of sewage, solve the problem of low concentration of activated sludge, and has the characteristics of simple structure, good sewage treatment effect and high efficiency, and is suitable for actual engineering transformation.
附图说明Description of drawings
为了更清楚地说明本实用新型实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本实用新型的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the accompanying drawings required in the embodiments will be briefly introduced below. Obviously, the accompanying drawings in the following description are only the present invention. For some embodiments of the present invention, those of ordinary skill in the art can also obtain other drawings based on these drawings on the premise of not paying creative efforts.
图1是根据本实用新型实施例所述的一种应用于污水脱氮的污泥双回流AOA生物膜处理装置的结构示意图;Fig. 1 is a schematic structural view of a sludge double-reflux AOA biofilm treatment device applied to sewage denitrification according to an embodiment of the present invention;
图中:1、原水箱,2、进水管,3、进水泵,4、搅拌装置,5、厌氧池,6、好氧池,7、气泵,8、气体流量计,9、微孔曝气装置,10、缺氧池,11、生物填料,12、二沉池,13、污泥回流管,14、污泥回流泵,15、出水管。In the figure: 1. Raw water tank, 2. Water inlet pipe, 3. Water inlet pump, 4. Stirring device, 5. Anaerobic tank, 6. Aerobic tank, 7. Air pump, 8. Gas flow meter, 9. Microporous exposure Gas device, 10, anoxic tank, 11, biological filler, 12, secondary settling tank, 13, sludge return pipe, 14, sludge return pump, 15, outlet pipe.
具体实施方式Detailed ways
下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本实用新型一部分实施例,而不是全部的实施例。基于本实用新型中的实施例,本领域普通技术人员所获得的所有其他实施例,都属于本实用新型保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of them. example. All other embodiments obtained by persons of ordinary skill in the art based on the embodiments of the present invention belong to the protection scope of the present invention.
如图1所示,根据本实用新型实施例所述的一种应用于污水脱氮的污泥双回流AOA生物膜处理装置,包括原水箱1,所述原水箱1通过进水管2与进水泵3的进水口连接,所述进水泵3的出水口与厌氧池5连接,所述厌氧池5与好氧池6连接,所述好氧池6与缺氧池10连接,所述厌氧池10与二沉池12连接,所述二沉池12的底部分别通过与污泥回流管13相连的污泥回流泵14连接所述厌氧池5和所述缺氧池10,所述二沉12的上部设有出水管15。所述厌氧池5、缺氧池10均设有搅拌装置4。所述好氧池6底部设有微孔曝气装置9,所述微孔曝气装置9通过气体流量计8与气泵7连接。所述缺氧池10中设有生物填料11。As shown in Figure 1, a sludge double-reflux AOA biofilm treatment device applied to sewage denitrification according to the embodiment of the utility model includes a raw water tank 1, and the raw water tank 1 is connected to the water inlet pump through the water inlet pipe 2. 3, the water outlet of the water inlet pump 3 is connected to the anaerobic pool 5, the anaerobic pool 5 is connected to the aerobic pool 6, the aerobic pool 6 is connected to the anoxic pool 10, and the anaerobic pool 6 is connected to the anoxic pool 10. The oxygen tank 10 is connected with the secondary settling tank 12, and the bottom of the secondary settling tank 12 is connected with the anaerobic tank 5 and the anoxic tank 10 through the sludge return pump 14 connected with the sludge return pipe 13 respectively. The top of the secondary sink 12 is provided with an outlet pipe 15 . Both the anaerobic tank 5 and the anoxic tank 10 are equipped with a stirring device 4 . A microporous aeration device 9 is provided at the bottom of the aerobic tank 6 , and the microporous aeration device 9 is connected to an air pump 7 through a gas flow meter 8 . The anoxic tank 10 is provided with a biological filler 11 .
为了方便理解本实用新型的上述技术方案,以下通过具体使用方式上对本实用新型的上述技术方案进行详细说明。In order to facilitate the understanding of the above-mentioned technical solution of the present utility model, the above-mentioned technical solution of the present utility model will be described in detail below through specific usage modes.
在具体使用时,首先,污水通过进水管2与进水泵3由原水箱1进入反应器厌氧池5,通过搅拌装置4与反应器中的活性污泥充分混合,在此阶段微生物主要将污水中的有机物贮存到细胞内;然后混合污泥进入好氧池6,通过气泵7、气体流量计8与微孔曝气装置9提供的溶解氧,污泥中的硝化菌进行硝化反应,将污水中的氨氮转化为硝酸盐氮或亚硝酸盐氮;最后进入反应器的缺氧池10,其中搅拌装置4使得系统中污泥处于混合状态,通过内源反硝化细菌及生物填料11上的厌氧氨氧化菌将污水中的氮素转化为氮气排放至空气中,从而实现污水脱氮过程。In specific use, first, the sewage enters the anaerobic tank 5 of the reactor from the raw water tank 1 through the water inlet pipe 2 and the water inlet pump 3, and is fully mixed with the activated sludge in the reactor by the stirring device 4. At this stage, the microorganisms mainly convert the sewage The organic matter in the sludge is stored in the cells; then the mixed sludge enters the aerobic tank 6, and the dissolved oxygen provided by the air pump 7, the gas flow meter 8 and the microporous aeration device 9, the nitrifying bacteria in the sludge carry out the nitrification reaction, and the sewage The ammonia nitrogen in the system is converted into nitrate nitrogen or nitrite nitrogen; finally enters the anoxic tank 10 of the reactor, where the stirring device 4 makes the sludge in the system in a mixed state, through the endogenous denitrifying bacteria and the anaerobic denitrification on the biological filler 11 The ammonium oxidizing bacteria convert the nitrogen in the sewage into nitrogen and discharge it into the air, thereby realizing the denitrification process of the sewage.
以北京某污水厂进水为处理对象,具体水质如下:COD为100-250mg/L, NH4 +为30-35 mg/L,NO3 - ≤1.1 mg/L,NO2 - ≤0.4 mg/L。试验结果表明:运行稳定后,城市污水通过污泥双回流AOA生物膜处理装置厌氧段后COD为35-45 mg/L,NH4 +为15-18 mg/L,NO3 -为0-0.2mg/L,NO2 - 为0-0.2 mg/L;经过好氧段后NH4 +为0-1.0 mg/L,NO3 -为10-15 mg/L,NO2 - 为0-5mg/L;最后经过缺氧段后COD为30-45 mg/L,NH4 +为0-1.0 mg/L,NO3 -为0-8.0 mg/L,NO2 - 为0-0.5 mg/L;试验结果说明出水TN、TP等污染物均实现了深度处理,稳定达到国家一级A排放标准。Taking the influent of a sewage plant in Beijing as the treatment object, the specific water quality is as follows: COD is 100-250mg/L, NH 4 + is 30-35 mg/L, NO 3 - ≤1.1 mg/L, NO 2 - ≤0.4 mg/L L. The test results show that after the operation is stable, the COD of urban sewage after passing through the anaerobic section of the sludge double-reflux AOA biofilm treatment device is 35-45 mg/L, the NH 4 + is 15-18 mg/L, and the NO 3 - is 0- 0.2mg/L, NO 2 - is 0-0.2 mg/L; NH 4 + is 0-1.0 mg/L after aerobic stage, NO 3 - is 10-15 mg/L, NO 2 - is 0-5mg /L; after the last anoxic stage, COD is 30-45 mg/L, NH 4 + is 0-1.0 mg/L, NO 3 - is 0-8.0 mg/L, NO 2 - is 0-0.5 mg/L ; The test results show that the pollutants such as TN and TP in the effluent have been treated in depth, and they have reached the national first-class A discharge standard stably.
综上所述,借助于本实用新型的上述技术方案,通过微生物硝化反硝化反应对污水进行处理,从而到污水脱氮的目的,该装置结构简单,对生活污水处理效果好、效率高。To sum up, with the help of the above technical solution of the utility model, sewage is treated through microbial nitrification and denitrification reaction, so as to achieve the purpose of sewage denitrification. The device has a simple structure, good effect and high efficiency on domestic sewage treatment.
以上所述仅为本实用新型的较佳实施例而已,并不用以限制本实用新型,凡在本实用新型的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。The above descriptions are only preferred embodiments of the present utility model, and are not intended to limit the present utility model. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present utility model shall be included in the Within the protection scope of the present utility model.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821970922.5U CN209428226U (en) | 2018-11-28 | 2018-11-28 | A kind of sludge dual reflux AOA biofilm treatment apparatus applied to sewage water denitrification |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821970922.5U CN209428226U (en) | 2018-11-28 | 2018-11-28 | A kind of sludge dual reflux AOA biofilm treatment apparatus applied to sewage water denitrification |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209428226U true CN209428226U (en) | 2019-09-24 |
Family
ID=67968342
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821970922.5U Active CN209428226U (en) | 2018-11-28 | 2018-11-28 | A kind of sludge dual reflux AOA biofilm treatment apparatus applied to sewage water denitrification |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209428226U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111875051A (en) * | 2020-09-08 | 2020-11-03 | 青岛太平洋化工装备有限公司 | Internal reflux fluidized denitrification reactor and sewage denitrification and phosphorus removal treatment system |
| CN113443711A (en) * | 2021-07-28 | 2021-09-28 | 北控水务(中国)投资有限公司 | AOA process enhanced sludge sedimentation treatment system and control method |
| CN114455706A (en) * | 2021-12-21 | 2022-05-10 | 江苏裕隆环保有限公司 | Two mud backward flow AOA degree of depth denitrogenation systems of sewage |
| CN116143284A (en) * | 2022-09-08 | 2023-05-23 | 北京工业大学 | Device and method for realizing double-short-path coupling anaerobic ammonium oxidation denitrification through mixed sludge fermentation in continuous flow AOA process |
| CN117509890A (en) * | 2023-11-21 | 2024-02-06 | 北京工业大学 | An integrated pollutant separation and treatment process based on vibrating membrane separation equipment |
| CN119371036A (en) * | 2024-11-22 | 2025-01-28 | 广东北控环保装备有限公司 | AOA assembled sewage treatment equipment with adjustable single and double reflux |
-
2018
- 2018-11-28 CN CN201821970922.5U patent/CN209428226U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111875051A (en) * | 2020-09-08 | 2020-11-03 | 青岛太平洋化工装备有限公司 | Internal reflux fluidized denitrification reactor and sewage denitrification and phosphorus removal treatment system |
| CN113443711A (en) * | 2021-07-28 | 2021-09-28 | 北控水务(中国)投资有限公司 | AOA process enhanced sludge sedimentation treatment system and control method |
| CN114455706A (en) * | 2021-12-21 | 2022-05-10 | 江苏裕隆环保有限公司 | Two mud backward flow AOA degree of depth denitrogenation systems of sewage |
| CN116143284A (en) * | 2022-09-08 | 2023-05-23 | 北京工业大学 | Device and method for realizing double-short-path coupling anaerobic ammonium oxidation denitrification through mixed sludge fermentation in continuous flow AOA process |
| CN116143284B (en) * | 2022-09-08 | 2024-04-26 | 北京工业大学 | Device and method for realizing double short-range coupling anaerobic ammonia oxidation denitrification in continuous flow AOA (anaerobic organic light emitting diode) process through mixed sludge fermentation product |
| CN117509890A (en) * | 2023-11-21 | 2024-02-06 | 北京工业大学 | An integrated pollutant separation and treatment process based on vibrating membrane separation equipment |
| CN119371036A (en) * | 2024-11-22 | 2025-01-28 | 广东北控环保装备有限公司 | AOA assembled sewage treatment equipment with adjustable single and double reflux |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN209428226U (en) | A kind of sludge dual reflux AOA biofilm treatment apparatus applied to sewage water denitrification | |
| CN105461178B (en) | The system and method that short distance nitration Anammox is followed by short-cut denitrification Anammox Treating Municipal Sewage | |
| CN103641272B (en) | High concentrated organic wastewater and percolate zero-discharge treatment system | |
| CN102633359B (en) | Method for treating total nitrogen of nitrogen-containing chemical wastewater | |
| CN103395937B (en) | Processing device and processing method applicable to high-ammonia-nitrogen agricultural wastewater | |
| CN103058460B (en) | A/O (anoxic/oxic) flow separation and magnetic flocculation integrated sewage treatment device and method | |
| CN105036489B (en) | Livestock/poultry culture wastewater deep denitrification and dephosphorization standard treatment device and process | |
| CN107032489A (en) | Realize the method that the short distance Anammoxs of continuous stream AOA half couple endogenous denitrification | |
| CN102627375A (en) | Integrated treatment method and integrated treatment device for polluted river and lake water | |
| CN112250176A (en) | Device and method for integrated short-range nitrification coupled with anammox denitrification and phosphorus removal to achieve deep nitrogen and phosphorus removal from urban sewage | |
| CN210711178U (en) | Pharmaceutical intermediate production wastewater membrane processing system | |
| CN102531290B (en) | Method and device for sludge digestive fluid two-level biological denitrification | |
| CN104512963A (en) | Integral multistage simultaneous nitrification and denitrification biological membrane system denitrification method and device | |
| CN101767903A (en) | Method for simultaneously nitrifying and denitrifying garbage percolate in SBR reactor | |
| CN110372096A (en) | The processing method of garbage leachate | |
| CN209989143U (en) | Denitrifying phosphorus removal coupling vibration oxygen deficiency MBR device | |
| CN101863592B (en) | Leachate treatment method for small town household refuse landfill sites | |
| CN110407418A (en) | A device and method for deep denitrification of sulfate-containing natural rubber processing wastewater | |
| CN102060416A (en) | Method for treating low-temperature city sewage by using anoxic-oxic moving bed biomembrane reactors | |
| CN109231673B (en) | A/O combined micro-electric field-Fe/C reinforced dephosphorization device and application thereof | |
| CN101269878A (en) | Separation process of return sludge to improve phosphorus and nitrogen removal efficiency in sewage treatment | |
| CN205011584U (en) | Sewage treatment system based on MBR | |
| CN201406361Y (en) | A landfill leachate wastewater treatment device | |
| CN104828942B (en) | A kind of new municipal sewage denitrogenation dephosphorizing handling process | |
| CN205313182U (en) | Sewage treatment plant sludge treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 101101 Beijing Tongzhou District, Xinhua West Street, No. 60 Courtyard, No. 2 Building, 7th Floor, 701 Co-patentee after: Beijing University of Technology Patentee after: Guotou xinkaishui Environmental Investment Co.,Ltd. Address before: 101101 Beijing Tongzhou District, Xinhua West Street, No. 60 Courtyard, No. 2 Building, 7th Floor, 701 Co-patentee before: Beijing University of Technology Patentee before: XINKAI WATER ENVIRONMENT INVESTMENT Co.,Ltd. |