CN201923929U - Reclaimed water recycling treatment system - Google Patents
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- CN201923929U CN201923929U CN2011200272455U CN201120027245U CN201923929U CN 201923929 U CN201923929 U CN 201923929U CN 2011200272455 U CN2011200272455 U CN 2011200272455U CN 201120027245 U CN201120027245 U CN 201120027245U CN 201923929 U CN201923929 U CN 201923929U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 36
- 238000004064 recycling Methods 0.000 title abstract description 8
- 239000010802 sludge Substances 0.000 claims abstract description 41
- 239000012528 membrane Substances 0.000 claims abstract description 20
- 230000003647 oxidation Effects 0.000 claims abstract description 7
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 7
- 230000001105 regulatory effect Effects 0.000 claims description 9
- 238000004062 sedimentation Methods 0.000 claims description 9
- 238000000034 method Methods 0.000 abstract description 10
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 239000010865 sewage Substances 0.000 description 23
- 230000000694 effects Effects 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000003851 biochemical process Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
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- 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
Description
技术领域technical field
本实用新型涉及污水处理技术领域,尤其涉及一种中水回用处理系统。The utility model relates to the technical field of sewage treatment, in particular to a reclaimed water treatment system.
背景技术Background technique
污水工程为公司基础设施项目,它既是生产部门必不可少的生产条件,又是改善环境的必要条件,目前企业、酒店等现有的污水处理系统,是将污水处理达标后排入地表水体或接入城市污水处理系统。但水资源日渐短缺,如何更好的利用水资源是环保和可持续发展的大问题,同时从用水成本等角度考虑,企业对污水回收利用也是非常必要的。Sewage engineering is an infrastructure project of the company. It is not only an indispensable production condition for the production department, but also a necessary condition for improving the environment. At present, the existing sewage treatment systems of enterprises, hotels, etc. are to discharge sewage into surface water bodies or Access to urban sewage treatment system. However, water resources are becoming increasingly scarce. How to make better use of water resources is a major issue for environmental protection and sustainable development. At the same time, considering the cost of water use, it is also very necessary for enterprises to recycle sewage.
对污水回收利用,将污水处理达标后用于对水质要求不高的地方如回用至冲厕、道路清扫、消防、绿化、车辆冲洗等,除了减少环境污染外,每年可减少大量的水量消耗,并节省了排污费用,具有良好的经济效益。但现有的生化工艺无法稳定达到标准要求,并存在流程长、能耗高、占地面积大等问题,影响了废水回收的推广应用。For sewage recycling, the sewage treatment can be used in places that do not require high water quality, such as reuse for toilet flushing, road cleaning, fire protection, greening, vehicle washing, etc. In addition to reducing environmental pollution, it can reduce a large amount of water consumption every year , and save the cost of sewage, with good economic benefits. However, the existing biochemical process cannot meet the standard requirements stably, and there are problems such as long process, high energy consumption, and large floor area, which affect the popularization and application of wastewater recycling.
实用新型内容Utility model content
本实用新型就是为了解决上述现有技术存在的问题而提供一种中水回用处理系统,经处理后回用部分和外排部分出水水质均可达到国家标准,实现废水回用,并且流程简单、运行稳定、能耗低,占地面积小。The utility model is to provide a reclaimed water reuse treatment system in order to solve the problems existing in the above-mentioned prior art. After treatment, the water quality of the reused part and the effluent part can reach the national standard, realize the reuse of waste water, and the process is simple , stable operation, low energy consumption and small footprint.
本实用新型的目的通过以下技术方案来实现:The purpose of this utility model is achieved through the following technical solutions:
一种中水回用处理系统,包括回用部分和外排部分,所述回用部分包括依次连通的调节池、缺氧池、MBR池和清水池,所述MBR池通过排泥管连通污泥池;所述外排部分包括依次连通的调节池、第二缺氧池、接触氧化池和二沉池,所述二沉池通过排泥管连通污泥池,二沉池的出水外排。A treatment system for reclaimed water, comprising a reusing part and an external discharge part, the reusing part includes a regulating tank, an anoxic tank, an MBR tank and a clear water tank connected in sequence, and the MBR tank is connected to the sewage through a sludge discharge pipe. Mud pond; the effluent part includes a regulating pond, a second anoxic pond, a contact oxidation pond and a secondary settling pond connected in sequence, and the secondary settling pond is connected to the sludge pond through a sludge discharge pipe, and the effluent of the secondary settling pond is discharged .
所述MBR池的膜生物反应器采用浸没式平板膜组件。The membrane bioreactor of the MBR pool adopts a submerged flat-plate membrane module.
所述调节池前端设置格栅池。A grid pool is arranged at the front end of the adjustment pool.
与现有技术相比,本实用新型具有以下有益效果:Compared with the prior art, the utility model has the following beneficial effects:
本实用新型提供的一种中水回用处理系统流程简单、性能可靠、运行稳定、能耗低,占地面积小,出水水质好、污泥量少,实现废水回用,减少环境污染,具有良好的环境效益和经济效益。The utility model provides a reclaimed water reuse treatment system with simple flow, reliable performance, stable operation, low energy consumption, small floor area, good effluent quality, and less sludge volume, which realizes waste water reuse and reduces environmental pollution. Good environmental and economic benefits.
其中中水回用部分处理水质优良、出水稳定、SS<3 mg/L,同时可截留水中的细菌和大肠杆菌,处理效果好。由于污泥泥龄长,可以大大提高难降解有机物的去除率,对高BOD浓度的污水也可以取得理想的处理效果。可以在高容积负荷、低污泥负荷、长泥龄条件下运行,产生剩余污泥量少,从而降低了污泥处理设施的费用。Among them, the reclaimed water reuse part has excellent water quality, stable effluent, SS<3 mg/L, and can intercept bacteria and E. coli in the water at the same time, and the treatment effect is good. Due to the long sludge age, the removal rate of refractory organic matter can be greatly improved, and the ideal treatment effect can also be achieved for sewage with high BOD concentration. It can operate under the conditions of high volume load, low sludge load and long sludge age, and produces less residual sludge, thus reducing the cost of sludge treatment facilities.
外排部分在继承了传统接触氧化工艺效果良好、运行稳定、操作管理方便等优点的同时,又具有抗负荷性强、产泥量相对少,以及脱氨氮效果好等优点。While inheriting the advantages of the traditional contact oxidation process, such as good effect, stable operation, and convenient operation and management, the external discharge part also has the advantages of strong load resistance, relatively small sludge production, and good ammonia nitrogen removal effect.
附图说明Description of drawings
图1为本实用新型一实施例的流程示意图。Fig. 1 is a schematic flow chart of an embodiment of the present invention.
具体实施方式Detailed ways
下面结合附图详细描述本实用新型。Describe the utility model in detail below in conjunction with accompanying drawing.
如图1所示,一种中水回用处理系统,包括回用部分和外排部分,回用部分包括依次连通的调节池1、缺氧池2、MBR池3和清水池4,MBR池3通过排泥管连通污泥池5;外排部分包括依次连通的调节池1、第二缺氧池6、接触氧化池7和二沉池8,二沉池8通过排泥管连通污泥池5,二沉池8的出水外排。As shown in Figure 1, a reclaimed water reuse treatment system includes a reuse part and an external discharge part. The reuse part includes a regulating pool 1, an anoxic pool 2, an MBR pool 3 and a clean water pool 4 connected in sequence, and the MBR pool 3 Connect to the sludge tank 5 through the sludge discharge pipe; the external discharge part includes the adjustment tank 1, the second anoxic tank 6, the contact oxidation tank 7 and the secondary sedimentation tank 8 connected in sequence, and the secondary sedimentation tank 8 is connected to the sludge through the sludge discharge pipe Pond 5, the effluent of secondary sedimentation tank 8 is discharged.
使用时,污水先收集后输送到调节池中。由于污水中含有较大颗粒和悬浮杂质,为保护处理系统设备正常运行、防止管路堵塞,在调节池前端设置格栅池9,对颗粒和悬浮杂质进行有效拦截,经过格栅拦截后的污水自流入调节池。调节池调节污水水量和均匀水质,以提高系统的抗冲击性能,配污水提升泵,由液位计自动控制水泵的启闭,将污水提升到后续反应单元。When in use, the sewage is collected first and then transported to the regulating tank. Since the sewage contains large particles and suspended impurities, in order to protect the normal operation of the treatment system equipment and prevent pipeline blockage, a grid pool 9 is installed at the front end of the regulating tank to effectively intercept the particles and suspended impurities. The sewage after being intercepted by the grid Self-flow into the adjustment pool. The regulating tank adjusts the sewage water volume and uniform water quality to improve the impact resistance of the system. It is equipped with a sewage lifting pump, and the liquid level gauge automatically controls the opening and closing of the water pump to lift the sewage to the subsequent reaction unit.
污水进入缺氧池,不仅可以提高B/C比,利于后续处理,而且本身可以利用反硝化脱氮,有一定的去除有机物的能力,并可为后续处理减轻负担。Sewage entering the anoxic tank can not only increase the B/C ratio, which is beneficial to subsequent treatment, but also can use denitrification to remove nitrogen, has a certain ability to remove organic matter, and can reduce the burden on subsequent treatment.
然后污水进入MBR池,膜生物反应器为核心工艺,膜生物反应器(Membrane Bioreactor,MBR)是一种将高效膜分离技术与传统活性污泥法相结合的新型高效污水处理工艺,它用具有独特结构的浸没式膜组件置于曝气池中,经过好氧曝气和生物处理后的水,由泵通过滤膜过滤后抽出。它与传统污水处理方法具有很大区别,取代了传统生化工艺中二沉池和三级处理工艺。由于膜的存在大大提高了系统固液分离的能力,从而使系统出水水质和容积负荷都得到大幅度提高,出水可达到杂用水标准。由于膜的过滤作用,微生物被完全截留在生物反应器中,实现了水力停留时间与活性污泥泥龄的彻底分离,消除了传统活性污泥法中污泥膨胀问题。膜生物反应器具有对污染物去除效率高、硝化能力强、出水水质稳定、剩余污泥产量低、设备紧凑、操作简单等优点。MBR池的膜生物反应器采用浸没式平板膜组件。平板膜具有以下优点:a.膜抗污染能力强、使用寿命长,为5-10年,平时不产生更换费用;b.膜清洗周期长;c.清洗操作非常简便,可在线清洗;d.运行更稳定,水质更好;e.低压(抽吸或重力)出水,能耗低,运行费用更省;平板膜的应用能保证系统能长时期稳定、安全运行。Then the sewage enters the MBR tank, and the membrane bioreactor is the core process. The membrane bioreactor (Membrane Bioreactor, MBR) is a new type of high-efficiency sewage treatment process that combines high-efficiency membrane separation technology with traditional activated sludge. The submerged membrane module of the structure is placed in the aeration tank, and the water after aerobic aeration and biological treatment is pumped out after being filtered through the filter membrane by the pump. It is very different from the traditional sewage treatment method, replacing the secondary sedimentation tank and the tertiary treatment process in the traditional biochemical process. Due to the existence of the membrane, the solid-liquid separation ability of the system is greatly improved, so that the system effluent water quality and volume load are greatly improved, and the effluent water can reach the miscellaneous water standard. Due to the filtration effect of the membrane, the microorganisms are completely trapped in the bioreactor, which realizes the complete separation of the hydraulic retention time and the sludge age of the activated sludge, and eliminates the sludge bulking problem in the traditional activated sludge method. Membrane bioreactor has the advantages of high pollutant removal efficiency, strong nitrification ability, stable effluent quality, low residual sludge output, compact equipment, and simple operation. The membrane bioreactor of the MBR pool adopts a submerged flat membrane module. The flat membrane has the following advantages: a. The membrane has strong anti-pollution ability and long service life, which is 5-10 years, and usually does not generate replacement costs; b. The membrane cleaning cycle is long; c. The cleaning operation is very simple and can be cleaned online; d. More stable operation and better water quality; e. Low-pressure (suction or gravity) water discharge, low energy consumption, and lower operating costs; the application of flat membranes can ensure long-term stable and safe operation of the system.
MBR池的出水排入清水池待用,MBR池的污泥通过污泥泵和排泥管道排入污泥池,污泥池的污泥经消毒处理后外运。The effluent from the MBR tank is discharged into the clear water tank for use, and the sludge in the MBR tank is discharged into the sludge tank through the sludge pump and the sludge discharge pipe. The sludge in the sludge tank is sterilized and then transported outside.
对于收集的污水超出回用量的部分,进入外排部分,由调节池将污水提升到第二缺氧池,第二缺氧池的出水口连通接触氧化池,接触氧化池的出水口连通二沉池,二沉池的污泥通过污泥泵和排泥管道排入污泥池,污泥池的污泥经消毒处理后外运,二沉池的出水按照相关排放标准外排。For the part of the collected sewage that exceeds the amount of reuse, it enters the discharge part, and the sewage is lifted from the regulating tank to the second anoxic tank. The outlet of the second anoxic tank is connected to the contact oxidation tank, and the outlet of the contact oxidation tank is connected to the secondary sedimentation The sludge from the secondary sedimentation tank is discharged into the sludge tank through the sludge pump and the sludge discharge pipe. The sludge in the sludge tank is sterilized and then transported outside, and the effluent from the secondary sedimentation tank is discharged according to the relevant discharge standards.
以上公开的仅为本申请的几个具体实施例,但本申请并非局限于此,任何本领域的技术人员能思之的变化,都应落在本申请的保护范围内。The above disclosures are only a few specific embodiments of the present application, but the present application is not limited thereto, and any changes conceivable by those skilled in the art shall fall within the protection scope of the present application.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103739144A (en) * | 2013-11-15 | 2014-04-23 | 安徽省绿巨人环境技术有限公司 | Detergent synthesis wastewater treatment technology |
CN103922535A (en) * | 2013-01-16 | 2014-07-16 | 成都康洁水务有限公司 | Apparatus for processing reclaimed water in MBMBR |
CN103991962A (en) * | 2014-06-04 | 2014-08-20 | 上海理工大学 | ICAST (Intermittent or Cyclic Activated Sludge Technology) treatment method for recycling wastewater on sites and self-control and monitoring device thereof |
CN107235613A (en) * | 2017-08-14 | 2017-10-10 | 韩保洋 | A kind of compact simplified sewage disposal MBR film bioreactor devices |
-
2011
- 2011-01-27 CN CN2011200272455U patent/CN201923929U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103922535A (en) * | 2013-01-16 | 2014-07-16 | 成都康洁水务有限公司 | Apparatus for processing reclaimed water in MBMBR |
CN103922535B (en) * | 2013-01-16 | 2015-09-30 | 成都康洁水务有限公司 | A kind of MBMBR sewerage disposing device |
CN103739144A (en) * | 2013-11-15 | 2014-04-23 | 安徽省绿巨人环境技术有限公司 | Detergent synthesis wastewater treatment technology |
CN103991962A (en) * | 2014-06-04 | 2014-08-20 | 上海理工大学 | ICAST (Intermittent or Cyclic Activated Sludge Technology) treatment method for recycling wastewater on sites and self-control and monitoring device thereof |
CN107235613A (en) * | 2017-08-14 | 2017-10-10 | 韩保洋 | A kind of compact simplified sewage disposal MBR film bioreactor devices |
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