CN203238141U - Sewage biological treatment membrane filtration system - Google Patents
Sewage biological treatment membrane filtration system Download PDFInfo
- Publication number
- CN203238141U CN203238141U CN2013202674724U CN201320267472U CN203238141U CN 203238141 U CN203238141 U CN 203238141U CN 2013202674724 U CN2013202674724 U CN 2013202674724U CN 201320267472 U CN201320267472 U CN 201320267472U CN 203238141 U CN203238141 U CN 203238141U
- Authority
- CN
- China
- Prior art keywords
- pool
- membrane
- sewage
- aeration
- pipeline
- 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
- 239000010865 sewage Substances 0.000 title claims abstract description 60
- 238000005374 membrane filtration Methods 0.000 title claims abstract description 16
- 239000012528 membrane Substances 0.000 claims abstract description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 238000005273 aeration Methods 0.000 claims abstract description 36
- 238000004140 cleaning Methods 0.000 claims abstract description 17
- 238000005192 partition Methods 0.000 claims abstract description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 12
- 229910052760 oxygen Inorganic materials 0.000 claims description 12
- 239000001301 oxygen Substances 0.000 claims description 12
- 239000000945 filler Substances 0.000 claims description 9
- 230000002000 scavenging effect Effects 0.000 claims 2
- 239000000463 material Substances 0.000 claims 1
- 238000012856 packing Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 14
- 230000001105 regulatory effect Effects 0.000 abstract description 12
- 238000005516 engineering process Methods 0.000 abstract description 9
- 238000004062 sedimentation Methods 0.000 abstract description 8
- 238000001914 filtration Methods 0.000 abstract description 5
- 238000005842 biochemical reaction Methods 0.000 abstract description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 17
- 229910052698 phosphorus Inorganic materials 0.000 description 17
- 239000011574 phosphorus Substances 0.000 description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 16
- 229910052757 nitrogen Inorganic materials 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 244000005700 microbiome Species 0.000 description 7
- 239000005416 organic matter Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 239000010802 sludge Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000012459 cleaning agent Substances 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 230000004060 metabolic process Effects 0.000 description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
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
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本实用新型公开了一种污水生物处理膜过滤系统,包括依次接通的格栅井、调节池、缺氧池、好氧池、膜过滤池及清水池;所述膜过滤池内设置有膜组件,膜组件的上部集水管通过管道与抽吸泵连接,膜组件的下部通过管道与清洗鼓风机连接;所述膜过滤池的底部设置有曝气盘,且曝气盘通过管道与曝气鼓风机连接;所述好氧池与膜过滤池之间的隔墙底部设置有轴流泵。本实用新型优化污水处理的工艺,这是一种反应器少、步骤少、效率高的污水处理生化反应池系统,同时利用内循环反硝化技术对污水进行脱氮除磷处理,直接在水池中采用膜组件过滤出水,无需沉淀池,占地面积小。
The utility model discloses a sewage biological treatment membrane filtration system, which comprises a grid well, a regulating pool, an anoxic pool, an aerobic pool, a membrane filtering pool and a clean water pool which are sequentially connected; the membrane filtering pool is provided with membrane components , the upper water collection pipe of the membrane module is connected with the suction pump through the pipeline, and the lower part of the membrane module is connected with the cleaning blower through the pipeline; the bottom of the membrane filter tank is provided with an aeration pan, and the aeration pan is connected with the aeration blower through the pipeline ; The bottom of the partition wall between the aerobic pool and the membrane filter pool is provided with an axial flow pump. The utility model optimizes the process of sewage treatment, which is a biochemical reaction pool system for sewage treatment with few reactors, few steps and high efficiency. At the same time, the internal circulation denitrification technology is used to denitrify and dephosphorize the sewage, directly in the pool The membrane module is used to filter the water, no sedimentation tank is required, and the floor space is small.
Description
技术领域 technical field
本实用新型涉及污水处理技术领域,具体涉及一种污水生物处理膜过滤系统。 The utility model relates to the technical field of sewage treatment, in particular to a sewage biological treatment membrane filtration system.
背景技术 Background technique
污水生物处理是用生物学的方法处理污水的总称,在污水生物处理应用中最广泛的技术之一,污水生物处理主要借助微生物的分解作用把污水中有机物转化为简单的无机物,使污水得到净化,按对氧气需求情况可分为厌氧生物处理和好氧生物处理两大类。 Sewage biological treatment is a general term for treating sewage with biological methods. It is one of the most widely used technologies in sewage biological treatment. Sewage biological treatment mainly uses the decomposition of microorganisms to convert organic matter in sewage into simple inorganic substances, so that sewage can be obtained Purification can be divided into two categories: anaerobic biological treatment and aerobic biological treatment according to the demand for oxygen.
在污水处理过程中对氮磷去除尤为重要,氮磷过量排放引起起的水体的富营氧化,依然是水污染存在的重大问题,污水处理不再仅以去除有机物(COD等)为目的,而是既要去除有机物又要脱氮除磷,减小水体富营氧化,传统的生物脱氮除磷技术,包括A/0、改良A/0、氧化沟等工艺,虽普遍具有脱氮除磷效果,但是反应器多,工艺复杂,能耗高,为了同时取得较好的脱氮除磷效果,需要增加污泥回流或外加碳源,不但增加了工艺运行费用,而且产生了大量的剩余污泥。反硝化脱氮除磷技术近年已有一定发展,它以硝酸根代替氧气作为除磷时的电子受体,由反硝化聚磷菌将脱氮与除磷过程合二为一,可以克服传统工艺脱氮除磷之间的矛盾,降低曝气量,减少污泥排量,为高效节能及可持续发展的脱氮除磷工艺,这是目前城市污水脱氮除磷技术研究的热点和必然趋势。关于反硝化脱氮除磷工艺技术,现在也有很多研究,虽然目前方法大都能够取得较好的处理效果,但工艺中普遍存在要用多个沉淀池对反硝化聚磷菌进行沉淀分离,存在反应器多,步骤多,反应器有效容积小,效率低、不便操作等诸多不足之处。 The removal of nitrogen and phosphorus is particularly important in the process of sewage treatment. The eutrophic oxidation of water caused by excessive discharge of nitrogen and phosphorus is still a major problem in water pollution. Sewage treatment is no longer only for the purpose of removing organic matter (COD, etc.), but It is necessary to remove both organic matter and nitrogen and phosphorus, and reduce eutrophication and oxidation of water bodies. Traditional biological nitrogen and phosphorus removal technologies, including A/0, improved A/0, oxidation ditch and other processes, are generally effective in nitrogen and phosphorus removal. However, there are many reactors, complex processes, and high energy consumption. In order to achieve better nitrogen and phosphorus removal effects at the same time, it is necessary to increase sludge reflux or add carbon sources, which not only increases the operating costs of the process, but also produces a large amount of residual pollution. mud. Denitrification, denitrification and phosphorus removal technology has been developed in recent years. It uses nitrate instead of oxygen as the electron acceptor for phosphorus removal, and denitrification and phosphorus accumulation bacteria combine the denitrification and phosphorus removal processes into one, which can overcome the traditional process. The contradiction between denitrification and phosphorus removal, reducing aeration and reducing sludge discharge, is a highly efficient, energy-saving and sustainable denitrification and phosphorus removal process. This is the current research hotspot and inevitable trend of urban sewage denitrification and phosphorus removal technology. . There are a lot of studies on denitrification denitrification and phosphorus removal technology. Although most of the current methods can achieve better treatment effects, it is common in the process to use multiple sedimentation tanks to separate denitrification phosphorus accumulating bacteria. There are many devices, many steps, small effective volume of the reactor, low efficiency, inconvenient operation and many other shortcomings.
污水经过生物处理后,需要沉淀和过滤处理,现有采用的技术是沉淀池,但是生物处理后的污水沉淀效果不佳,常常需要加入药剂,并且占地面积较大。 After biological treatment, sewage needs sedimentation and filtration treatment. The existing technology is sedimentation tank, but the sedimentation effect of sewage after biological treatment is not good, often needs to add chemicals, and occupies a large area.
实用新型内容 Utility model content
本实用新型的目的在于克服现有技术的不足,提供了一种污水生物处理膜过滤系统,优化污水处理的工艺,这是一种反应器少、步骤少、效率高的污水处理生化反应池系统,同时利用内循环反硝化技术对污水进行脱氮除磷处理,直接在水池中采用膜组件过滤出水,无需沉淀池,占地面积小。 The purpose of the utility model is to overcome the deficiencies of the prior art and provide a sewage biological treatment membrane filtration system to optimize the process of sewage treatment. This is a biochemical reaction tank system for sewage treatment with fewer reactors, fewer steps and high efficiency. , At the same time, the internal circulation denitrification technology is used to denitrify and dephosphorize the sewage, and the membrane module is used to filter the water directly in the pool, without the need for a sedimentation tank, and the footprint is small.
本实用新型的目的主要通过以下技术方案实现:一种污水生物处理膜过滤系统,包括依次接通的格栅井、调节池、缺氧池、好氧池、膜过滤池及清水池;所述膜过滤池内设置有膜组件,膜组件的上部集水管通过管道与抽吸泵连接,膜组件的下部通过管道与清洗鼓风机连接;所述膜过滤池的底部设置有曝气盘,且曝气盘通过管道与曝气鼓风机连接;所述好氧池与膜过滤池之间的隔墙底部设置有轴流泵。 The purpose of this utility model is mainly achieved through the following technical proposals: a membrane filtration system for sewage biological treatment, including grid wells, regulating tanks, anoxic tanks, aerobic tanks, membrane filter tanks and clear water tanks connected in sequence; Membrane modules are installed in the membrane filter tank, the upper water collection pipe of the membrane module is connected with the suction pump through the pipeline, and the lower part of the membrane module is connected with the cleaning blower through the pipeline; the bottom of the membrane filter tank is provided with an aeration plate, and the aeration plate It is connected with an aeration blower through a pipeline; an axial flow pump is arranged at the bottom of the partition wall between the aerobic tank and the membrane filter tank.
所述缺氧池内设置有弹性生物填料,缺氧池的底部设置有布水管,且布水管通过管道与调节池底部的提升泵连接。 The anoxic pool is provided with elastic biological filler, and the bottom of the anoxic pool is provided with a water distribution pipe, and the water distribution pipe is connected to the lifting pump at the bottom of the regulating pool through a pipeline.
所述好氧池内设置有组合生物填料,好氧池的底部设置有曝气管,且曝气管通过管道与曝气鼓风机连接。 The aerobic tank is provided with combined biological filler, and the bottom of the aerobic tank is provided with an aeration pipe, and the aeration pipe is connected with an aeration blower through a pipeline.
所述好氧池内设置有溶解氧仪。 A dissolved oxygen meter is arranged in the aerobic pool.
进一步的,所述清水池内底部设置有清洗泵,且清洗泵通过清洗管与膜组件的上部连接。 Further, a cleaning pump is provided at the inner bottom of the clear water tank, and the cleaning pump is connected to the upper part of the membrane module through a cleaning pipe.
本实用新型的工作原理:将需要处理的污水首先从进水管进入格栅井,格栅机将污水中较大悬浮物去除,然后进入调节池,将水质、水量不均匀的污水在调节池中停留一定的时间,使污水在调节池内充分混合,以保证后续处理构筑物均匀、稳定运行,经过调节池处理的污水通过提升泵抽入缺氧池,污水通过布水管均匀分布在缺氧池中,在缺氧池中除去部分悬浮物并降低污水的SS、BOD、COD等负荷指标,缺氧池将大分子物质转化为小分子物质,将环状结构转化为链状结构,进一步提高了废水的BOD/COD比,增加了废水的可生化性,为后续的好氧生化处理创造条件,弹性生物填料有利于微生物生长。 The working principle of the utility model: the sewage to be treated first enters the grid well from the water inlet pipe, the grid machine removes the larger suspended matter in the sewage, and then enters the regulating pool, and the sewage with uneven water quality and water volume is placed in the regulating pool Stay for a certain period of time to fully mix the sewage in the regulating tank to ensure the uniform and stable operation of the subsequent treatment structures. The sewage treated in the regulating tank is pumped into the anoxic pool through the lifting pump, and the sewage is evenly distributed in the anoxic pool through the water distribution pipe. In the anoxic pool, part of the suspended matter is removed and the load indicators such as SS, BOD, and COD of the sewage are reduced. The anoxic pool converts macromolecular substances into small molecular substances, and converts ring structures into chain structures, further improving the waste water. The BOD/COD ratio increases the biodegradability of wastewater and creates conditions for subsequent aerobic biochemical treatment. The elastic biofiller is conducive to the growth of microorganisms.
然后污水进入好氧池和膜过滤池,好氧池内设置有组合生物填料,好氧池的底部设置有曝气管,且曝气管通过管道与曝气鼓风机连接,向好氧池和膜过滤池中鼓入空气,曝气管和曝气盘将空气分散为微小气泡,增加了水中的溶解氧,溶解氧仪可以实时检测水中溶解氧,控制鼓入空气量。好氧池内利用栖息其内组合生物填料表面上生物膜的吸附作用和微生物的代谢作用来达到净化污水的目的,生物膜中的微生物在有氧的条件下将污水中的一部分有机物用于合成新的细胞,将另一部分有机物进行分解代谢以便获得细胞合成所需的能量,其最终产物是二氧化碳和水等稳定物质。轴流泵将膜过滤池内的污水回流到好氧池,同时回流泵将底部部分污泥回流,从而提高了污水生物处理的脱氮除磷效果。 Then the sewage enters the aerobic tank and the membrane filter tank. The aerobic tank is equipped with a combined biological filler, and the bottom of the aerobic tank is provided with an aeration tube, and the aeration tube is connected to the aeration blower through a pipeline, and the aerobic tank and the membrane filter Air is blown into the pool, and the aeration tube and aeration disc disperse the air into tiny bubbles, increasing the dissolved oxygen in the water. The dissolved oxygen meter can detect the dissolved oxygen in the water in real time and control the amount of air blown in. In the aerobic pool, the adsorption of the biofilm on the surface of the composite biofiller and the metabolism of microorganisms are used to purify the sewage. The microorganisms in the biofilm use part of the organic matter in the sewage under aerobic conditions to synthesize new catabolize another part of organic matter in order to obtain the energy needed for cell synthesis, and the final products are stable substances such as carbon dioxide and water. The axial flow pump returns the sewage in the membrane filter tank to the aerobic tank, and at the same time, the return pump returns the bottom part of the sludge, thereby improving the nitrogen and phosphorus removal effect of sewage biological treatment.
生化后的污水在膜过滤池中,膜组件通过抽吸泵将清水从膜过滤池抽入清水池中,完成对污水的生物处理,膜组件的标称孔径为0.1微米。膜组件需要清洗时,启动清洗泵和清洗鼓风机对膜组件进行气水清洗,加药装置加入清洗药剂,恢复膜组件的过滤效果。 The biochemical sewage is in the membrane filter tank, and the membrane module pumps the clean water from the membrane filter tank into the clean water tank through the suction pump to complete the biological treatment of the sewage. The nominal pore size of the membrane module is 0.1 micron. When the membrane module needs to be cleaned, the cleaning pump and cleaning blower are started to clean the membrane module with air and water, and the dosing device adds cleaning agents to restore the filtration effect of the membrane module.
与现有技术相比,本实用新型具有以下有益效果:本实用新型污水生物处理膜过滤装置优化污水处理的工艺,可缩短污水处理的工艺流程,这是一种反应器少、步骤少、效率高的污水处理生化反应池系统;同时利用内循环反硝化技术对污水进行脱氮除磷处理,减少传统污泥回流、减小了曝气量;设置了单独的膜过滤池,直接在水池中采用膜组件过滤出水,无需沉淀池,占地面积小,减少后续沉淀池药剂使用;耐冲击负荷强,运行稳定。 Compared with the prior art, the utility model has the following beneficial effects: the sewage biological treatment membrane filtration device of the utility model optimizes the process of sewage treatment, and can shorten the process flow of sewage treatment. High biochemical reaction tank system for sewage treatment; at the same time, the internal circulation denitrification technology is used to denitrify and dephosphorize the sewage, reducing the return of traditional sludge and reducing the amount of aeration; a separate membrane filter tank is set up, directly in the pool The membrane module is used to filter the water, no sedimentation tank is required, the floor area is small, and the use of chemicals in the subsequent sedimentation tank is reduced; the impact load is strong and the operation is stable.
附图说明 Description of drawings
图1为本实用新型的结构示意图; Fig. 1 is the structural representation of the utility model;
图2为本实用新型的俯视图。 Fig. 2 is a top view of the utility model.
附图中附图标记所对应的名称为:1、进水管,2、格栅井,3、格栅机,4、调节池,5、提升泵,6、流量计,7、缺氧池,8、好氧池,9、溶解氧仪,10、布水管,11、弹性生物填料,12、组合生物填料,13、曝气管,14、回流泵,15、膜过滤池,16、轴流泵,17、曝气盘,18、曝气鼓风机,19、膜组件,20、清洗鼓风机,21、抽吸泵,22、清水池,23、出水管,24、清洗泵,25、清洗管,26、加药装置。 The names corresponding to the reference signs in the attached drawings are: 1. water inlet pipe, 2. grid well, 3. grid machine, 4. regulating tank, 5. lift pump, 6. flow meter, 7. anoxic tank, 8. Aerobic tank, 9. Dissolved oxygen meter, 10. Water distribution pipe, 11. Elastic biological filler, 12. Combined biological filler, 13. Aeration tube, 14. Return pump, 15. Membrane filter tank, 16. Axial flow Pump, 17, aeration disc, 18, aeration blower, 19, membrane module, 20, cleaning blower, 21, suction pump, 22, clean water tank, 23, outlet pipe, 24, cleaning pump, 25, cleaning pipe, 26. Dosing device.
具体实施方式 Detailed ways
下面结合实施例及附图对本实用新型作进一步的详细说明,但本实用新型的实施方式不限于此。 The utility model will be further described in detail below in conjunction with the embodiments and accompanying drawings, but the implementation of the utility model is not limited thereto.
实施例:如图1、图2所示,一种污水生物处理膜过滤系统,包括依次接通的格栅井2、调节池4、缺氧池7、好氧池8、膜过滤池15及清水池22;所述膜过滤池15内设置有膜组件19,膜组件19的上部集水管通过管道与抽吸泵21连接,膜组件19的下部通过管道与清洗鼓风机20连接;所述膜过滤池15的底部设置有曝气盘17,且曝气盘17通过管道与曝气鼓风机18连接;所述好氧池8与膜过滤池15之间的隔墙底部设置有轴流泵16。
Embodiment: as shown in Fig. 1, Fig. 2, a kind of sewage biological treatment membrane filtration system, comprises grid well 2, regulating pond 4, anoxic pond 7, aerobic pond 8, membrane filter pond 15 and Clean water pool 22; said membrane filter tank 15 is provided with membrane module 19, the upper water collection pipe of membrane module 19 is connected with
所述缺氧池7内设置有弹性生物填料11,缺氧池7的底部设置有布水管10,且布水管10通过管道与调节池4底部的提升泵5连接。
The anoxic pool 7 is provided with an elastic
所述好氧池8内设置有组合生物填料12,好氧池8的底部设置有曝气管13,且曝气管13通过管道与曝气鼓风机18连接。
The aerobic tank 8 is provided with a combined biological filler 12, and the bottom of the aerobic tank 8 is provided with an
所述好氧池8内设置有溶解氧仪9。 The aerobic pool 8 is provided with a dissolved oxygen meter 9 .
进一步的,所述清水池22内底部设置有清洗泵24,且清洗泵24通过清洗管25与膜组件19的上部连接。
Further, a
本实用新型在工作时,将需要处理的污水首先从进水管1进入格栅井2,格栅机3将污水中较大悬浮物去除,然后进入调节池4,将水质、水量不均匀的污水在调节池4中停留一定的时间,使污水在调节池4内充分混合,以保证后续处理构筑物均匀、稳定运行,经过调节池4处理的污水通过提升泵5抽入缺氧池7,污水通过布水管10均匀分布在缺氧池7中,在缺氧池7中除去部分悬浮物并降低污水的SS、BOD、COD等负荷指标,缺氧池7将大分子物质转化为小分子物质,将环状结构转化为链状结构,进一步提高了废水的BOD/COD比,增加了废水的可生化性,为后续的好氧生化处理创造条件,弹性生物填料11有利于微生物生长。
When the utility model is working, the sewage to be treated first enters the grid well 2 from the water inlet pipe 1, and the grid machine 3 removes larger suspended matter in the sewage, and then enters the regulating pool 4, and the sewage with uneven water quality and water volume Stay in the regulating tank 4 for a certain period of time, so that the sewage is fully mixed in the regulating tank 4 to ensure the uniform and stable operation of the follow-up treatment structures. The
然后污水进入好氧池8和膜过滤池15,好氧池8内设置有组合生物填料12,好氧池8的底部设置有曝气管13,且曝气管13通过管道与曝气鼓风机18连接,向好氧池8和膜过滤池15中鼓入空气,曝气管13和曝气盘17将空气分散为微小气泡,增加了水中的溶解氧,溶解氧仪9可以实时检测水中溶解氧,控制鼓入空气量。好氧池8内利用栖息其内组合生物填料12表面上生物膜的吸附作用和微生物的代谢作用来达到净化污水的目的,生物膜中的微生物在有氧的条件下将污水中的一部分有机物用于合成新的细胞,将另一部分有机物进行分解代谢以便获得细胞合成所需的能量,其最终产物是二氧化碳和水等稳定物质。轴流泵16将膜过滤池15内的污水回流到好氧池8,同时回流泵14将底部部分污泥回流,从而提高了污水生物处理的脱氮除磷效果。
Then the sewage enters the aerobic tank 8 and the membrane filter tank 15, the aerobic tank 8 is provided with a combined biological filler 12, the bottom of the aerobic tank 8 is provided with an
生化后的污水在膜过滤池15中,膜组件19通过抽吸泵21将清水从膜过滤池15抽入清水池22中,完成对污水的生物处理,膜组件19的标称孔径为0.1微米。膜组件19需要清洗时,启动清洗泵24和清洗鼓风机20对膜组件19进行气水清洗,加药装置26加入清洗药剂,恢复膜组件19的过滤效果。
The biochemical sewage is in the membrane filter tank 15, and the membrane module 19 draws clear water from the membrane filter tank 15 into the clean water tank 22 through the
如上所述,则能很好的实现本实用新型。 As mentioned above, the utility model can be well realized.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202674724U CN203238141U (en) | 2013-05-16 | 2013-05-16 | Sewage biological treatment membrane filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202674724U CN203238141U (en) | 2013-05-16 | 2013-05-16 | Sewage biological treatment membrane filtration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203238141U true CN203238141U (en) | 2013-10-16 |
Family
ID=49315460
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013202674724U Expired - Fee Related CN203238141U (en) | 2013-05-16 | 2013-05-16 | Sewage biological treatment membrane filtration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203238141U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103964632A (en) * | 2014-03-28 | 2014-08-06 | 宁波埃克钛能源科技有限公司 | Integrated sewage treatment device |
| CN104211207A (en) * | 2014-08-18 | 2014-12-17 | 山东每美食品有限公司 | Cyclic utilization apparatus for fermentation sewage |
| CN105036472A (en) * | 2015-07-30 | 2015-11-11 | 巨化集团技术中心 | Mixed chemical industrial wastewater enhanced biochemical treatment device and method thereof |
| CN110776197A (en) * | 2019-10-25 | 2020-02-11 | 华电水务膜分离科技(天津)有限公司 | Glycerol-containing wastewater treatment integrated device |
-
2013
- 2013-05-16 CN CN2013202674724U patent/CN203238141U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103964632A (en) * | 2014-03-28 | 2014-08-06 | 宁波埃克钛能源科技有限公司 | Integrated sewage treatment device |
| CN103964632B (en) * | 2014-03-28 | 2016-02-10 | 浙江埃克钛环境科技有限公司 | Sewage integrated treatment device |
| CN104211207A (en) * | 2014-08-18 | 2014-12-17 | 山东每美食品有限公司 | Cyclic utilization apparatus for fermentation sewage |
| CN104211207B (en) * | 2014-08-18 | 2016-01-20 | 山东每美生物科技有限公司 | A kind of fermentation sewage recycling device |
| CN105036472A (en) * | 2015-07-30 | 2015-11-11 | 巨化集团技术中心 | Mixed chemical industrial wastewater enhanced biochemical treatment device and method thereof |
| CN110776197A (en) * | 2019-10-25 | 2020-02-11 | 华电水务膜分离科技(天津)有限公司 | Glycerol-containing wastewater treatment integrated device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102583743B (en) | Dual-sludge denitrification dephosphorizing and denitrifying A/A-O device and method | |
| CN101234836A (en) | A landfill leachate treatment process | |
| CN205473208U (en) | Rural domestic sewage MBR of integral type and constructed wetland composite treatment device | |
| CN108249691B (en) | Integrated low-energy-consumption distributed village and town domestic sewage treatment system | |
| CN108178438A (en) | A kind of rural domestic sewage treatment system and purification method | |
| CN205501033U (en) | A compound improved generation purifier for distributed rural domestic sewage treatment system | |
| CN105668947A (en) | Sewage purification filter system | |
| CN204079721U (en) | A kind of sewage disposal device adopting pure oxygen aeration and remaining oxygen reuse | |
| CN103979681A (en) | Nitrification/denitrification integrated rural domestic sewage treatment system | |
| CN103232143B (en) | Ecological combined device for treating ammonia-nitrogen sewage | |
| CN202610021U (en) | External anaerobic membrane bioreactor | |
| CN205556397U (en) | A multistage bological aerated filter for quality of water purifies | |
| CN203238141U (en) | Sewage biological treatment membrane filtration system | |
| CN201614333U (en) | A decentralized sewage treatment device | |
| CN203238088U (en) | Aerobiotic nitration biological membrane-membrane bioreactor for removing endocrine disrupters in sewage | |
| CN103193360B (en) | Nitrogen and phosphorus removal integrated biological aerated filter water purification system and water purification method thereof | |
| CN203781915U (en) | Nitrification and denitrification integrated rural domestic sewage treatment system | |
| CN104761048A (en) | Water treatment apparatus based on membrane bioreactor (MBR) | |
| CN203582653U (en) | Livestock/fowl culture wastewater treatment system | |
| CN201648106U (en) | Coking wastewater flat-plate MBR treatment equipment | |
| CN205528307U (en) | High concentration organic wastewater equipment based on UASB -MBR | |
| CN101973630B (en) | Pressure pipe type sewage treatment reactor | |
| CN202658053U (en) | Buried sewage treatment device | |
| CN205275305U (en) | Membrane bioreactor | |
| CN203307173U (en) | Sewage treatment biological reaction device |
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: 20131016 Termination date: 20140516 |
