WO2023178966A1 - Modular multi-stage biochemical-filtering sewage treatment system - Google Patents

Modular multi-stage biochemical-filtering sewage treatment system Download PDF

Info

Publication number
WO2023178966A1
WO2023178966A1 PCT/CN2022/121626 CN2022121626W WO2023178966A1 WO 2023178966 A1 WO2023178966 A1 WO 2023178966A1 CN 2022121626 W CN2022121626 W CN 2022121626W WO 2023178966 A1 WO2023178966 A1 WO 2023178966A1
Authority
WO
WIPO (PCT)
Prior art keywords
biochemical
area
sewage treatment
zone
filtration
Prior art date
Application number
PCT/CN2022/121626
Other languages
French (fr)
Chinese (zh)
Inventor
汤丁丁
程飞跃
周艳
赵皇
秦雄
郑碧娟
王媛
Original Assignee
中建三局绿色产业投资有限公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 中建三局绿色产业投资有限公司 filed Critical 中建三局绿色产业投资有限公司
Publication of WO2023178966A1 publication Critical patent/WO2023178966A1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/302Nitrification and denitrification treatment
    • C02F3/303Nitrification and denitrification treatment characterised by the nitrification
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/302Nitrification and denitrification treatment
    • C02F3/305Nitrification and denitrification treatment characterised by the denitrification
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Definitions

  • the sewage treatment system proposed by the present invention performs alternating biochemical and filtration treatment of sewage by utilizing biochemical zones and filtration zones arranged at intervals, and at the same time, flexible fillers that can promote the denitrification effect are provided inside the filtration zone to improve the denitrification effect.
  • a sewage treatment area can also be added as needed.
  • Figure 1 is a schematic structural diagram of the modular multi-stage biochemical-filtration sewage treatment system of the present invention

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

Provided in the present invention is a modular multi-stage biochemical-filtering sewage treatment system, comprising at least one sewage treatment area, wherein each sewage treatment area comprises a first biochemical area, a first filtering area, a second biochemical area and a second filtering area which are sequentially in communication; one side of the first biochemical area is connected to a water inlet; a tail end of the second filtering area is connected to a clean water area; the tail end of the clean water area is provided with a water outlet; and the bottoms of the first biochemical area and the second biochemical area are provided with an aeration device. The sewage treatment system can integrate biochemical sewage treatment and mud-water separation; the first biochemical area is an anoxic area, and the second biochemical area is an aerobic zone, such that a multi-stage biochemical-filtrating treatment can be achieved; and in practical application, the number of sewage treatment areas can be adjusted according to the characteristics of sewage in an area to be subjected to treatment, thereby improving the practicability of the treatment system. By the above means, a biochemical sewage treatment and mud-water separation can be integrated without providing a sedimentation tank, thereby effectively reducing the cost of a sewage treatment process.

Description

模块化多级生化-过滤污水处理系统Modular multi-stage biochemical-filtration sewage treatment system 技术领域Technical field
本发明涉及污水处理技术领域,尤其涉及一种模块化多级生化-过滤污水处理系统。The invention relates to the technical field of sewage treatment, and in particular to a modular multi-stage biochemical-filtration sewage treatment system.
背景技术Background technique
目前,我国农村污水生物处理在实际运行过程中或存在成本高、运行维护工作量大以及运行不稳定等问题。通常使用最多的AAO、AO系列工艺,往往需要较高的污泥回流比与消化液回流比,以保证系统具有足够的污泥浓度和TN去除效果,现有的回流方式主要是水泵回流和气提回流,而水泵回流对于农村污水处理规模偏小的情况,存在设备选取困难,而且会导致运营管理难度大、设备运行能耗高的问题;而采用气提回流的方式,虽可以实现一台风机满足曝气和回流的需求,但是回流过程往往难以控制回流比,且回流介质需要大量空气作为动力,对回流液的溶解氧影响较大,难以保证生物脱氮除磷对溶解氧的需求。At present, the actual operation process of biological treatment of rural sewage in my country may have problems such as high cost, heavy operation and maintenance workload, and unstable operation. The most commonly used AAO and AO series processes often require a higher sludge reflux ratio and digestion liquid reflux ratio to ensure that the system has sufficient sludge concentration and TN removal effect. The existing reflux methods are mainly water pump reflux and gas stripping. Return flow, and water pump return flow will cause difficulties in equipment selection for rural sewage treatment on a small scale, and will lead to problems such as difficult operation and management and high energy consumption of equipment operation; while using air lift return flow, although a fan can be used It meets the needs of aeration and reflux, but it is often difficult to control the reflux ratio during the reflux process, and the reflux medium requires a large amount of air as power, which has a greater impact on the dissolved oxygen of the reflux liquid, making it difficult to ensure the dissolved oxygen demand for biological denitrification and phosphorus removal.
生物法污水处理工艺过程中,由于未使用化学产品,而是利用生物制剂中的天然微生物将污水中的污染物进行去除,该过程具有处理效率高、出水质量好、不会对环境造成二次污染等优势。其中,生物法处理工艺中应用得最多的是膜生物反应器和生态处理措施,膜生物反应器能够避免污泥回流,延长污泥泥龄,提高污泥浓度,且处理效果较好,但是该工艺的投资和运行成本生态处理措施高,且需要相关专业人员进行管理,因此不适用于农村地区;生态处理措施的能耗低且运行管理简单,但是由于生态处理工艺的处理负荷普遍较低,导致设备占地面积大,且填料堵塞问题难以解决,造成人工湿地难以长期稳定运行;在低温区域,人工湿地处理效果大打折扣。In the biological sewage treatment process, because no chemical products are used, natural microorganisms in biological agents are used to remove pollutants in the sewage. This process has high treatment efficiency, good effluent quality, and will not cause secondary damage to the environment. pollution and other advantages. Among them, membrane bioreactors and ecological treatment measures are most commonly used in biological treatment processes. Membrane bioreactors can avoid sludge backflow, extend sludge age, increase sludge concentration, and have better treatment effects. However, this The investment and operation costs of the process are high, and ecological treatment measures require relevant professionals to manage, so they are not suitable for rural areas; ecological treatment measures have low energy consumption and simple operation and management, but because the treatment load of ecological treatment processes is generally low, As a result, the equipment occupies a large area, and the problem of filler clogging is difficult to solve, making it difficult for the artificial wetland to operate stably for a long time; in low-temperature areas, the treatment effect of the artificial wetland is greatly reduced.
现有技术中,申请号为201510902437.9,公开日为2018年8月28日,名称为“一种一体化污水处理装置”的发明专利中通过在箱体的长度方向依次依次设置泥水混合区-一级生化区-二级生化区,并利用回流机构将部分污泥和二级生化区中部分混合液重新回流到泥水混合区进而返回一级生化区形成循环,二级生化区中回流的硝化液在缺氧的一级生化区中发生反硝化反应,去除总氮,提高污水处理能力;另外,泥水混合区使回流的污泥、进水和二级生化区回流的混合液混合后从泥水混合区的隔板溢出进入一级生化区,一方面起到了缓冲水流的作用并使液体的混合更为充分。上述技术方案中,通过使硝化液回流促进一级生化区的反硝化反应,以此提高污水处理能力。上述过程虽然可以提升污水处理能力,但是生化区之间的循环过程并不能有效将污水中的污泥除去,而利用硝化液回流促进反硝化反应的过程的脱氮效果并不高。In the existing technology, the application number is 201510902437.9, and the publication date is August 28, 2018. In the invention patent titled "An integrated sewage treatment device", mud-water mixing zones are successively set up in the length direction of the box - a The first-level biochemical zone - the second-level biochemical zone, and uses the backflow mechanism to return part of the sludge and part of the mixed liquid in the second-level biochemical zone to the mud-water mixing zone and then back to the first-level biochemical zone to form a cycle. The nitrification liquid returned in the second-level biochemical zone Denitrification occurs in the anoxic primary biochemical zone to remove total nitrogen and improve sewage treatment capacity; in addition, the mud-water mixing zone mixes the returning sludge, incoming water and the mixed liquid returning from the secondary biochemical zone and then mixes the mud and water. The partition of the zone overflows into the first-level biochemical zone, which on the one hand plays the role of buffering the water flow and making the liquid more fully mixed. In the above technical solution, the denitrification reaction in the primary biochemical zone is promoted by refluxing the nitrification liquid, thereby improving the sewage treatment capacity. Although the above process can improve the sewage treatment capacity, the circulation process between the biochemical zones cannot effectively remove the sludge in the sewage, and the denitrification effect of the process of using nitrification liquid backflow to promote the denitrification reaction is not high.
现有技术中,公开号为CN213739096U的实用新型中设置了一种一体式高效污水处理设备,上述设备包括设备外墙,设备外墙的内部被板体分隔成若干个隔间,包括依次连接的厌氧区、第一缺氧区、第一好氧区、第二缺氧区、第二好氧区、沉淀澄清区和高效纤维过滤器;污水一部分进入厌氧区中酸化处理,出水进入第一缺氧区中处理,出水进入第一好氧区中处理;污水另一部分和第一好氧区的出水一同进入第二缺氧区中处理,出水进入第二好氧区中处理,出水进入沉淀澄清区,向沉淀澄清区加入除磷剂除磷,在沉淀澄清区中泥水分离,出水进入高效纤维过滤器中过滤,出水进行消毒。上述技术方案虽然可以对污水高效处理,但是沉淀区以及过滤器增大了设备的占地面积,同时,在设备的末端设置过滤器的方式,需要使污泥回流来实现泥水分离,如此一来,降低了污水处理的效率,增大了污水处理系统的运行能耗和运营维护管理难度。In the prior art, the utility model with publication number CN213739096U is provided with an integrated high-efficiency sewage treatment equipment. The above-mentioned equipment includes an equipment outer wall. The interior of the equipment outer wall is divided into several compartments by a plate body, including sequentially connected Anaerobic zone, first anoxic zone, first aerobic zone, second anoxic zone, second aerobic zone, sedimentation and clarification zone and high-efficiency fiber filter; part of the sewage enters the anaerobic zone for acidification treatment, and the effluent enters the third It is processed in an anoxic zone, and the effluent enters the first aerobic zone for treatment; the other part of the sewage enters the second anoxic zone for treatment together with the effluent from the first aerobic zone, and the effluent enters the second aerobic zone for treatment, and the effluent enters In the sedimentation and clarification area, phosphorus removal agent is added to the sedimentation and clarification area to remove phosphorus. In the sedimentation and clarification area, the mud and water are separated, and the effluent enters the high-efficiency fiber filter for filtration, and the effluent is disinfected. Although the above technical solution can efficiently treat sewage, the sedimentation area and filter increase the floor area of the equipment. At the same time, setting the filter at the end of the equipment requires the sludge to flow back to achieve mud-water separation. , reducing the efficiency of sewage treatment, increasing the operating energy consumption and difficulty of operation, maintenance and management of the sewage treatment system.
有鉴于此,有必要设计一种改进的模块化多级生化-过滤污水处理系统,以解决上述问题。In view of this, it is necessary to design an improved modular multi-stage biochemical-filtration sewage treatment system to solve the above problems.
发明内容Contents of the invention
本发明的目的在于提供一种模块化多级生化-过滤污水处理系统。The purpose of the present invention is to provide a modular multi-stage biochemical-filtration sewage treatment system.
为实现上述发明目的,本发明提供了一种模块化多级生化-过滤污水处理系统,所述污水处理系统至少包括一个污水处理区,所述污水处理区包括依次连通的第一生化区、第一过滤区、第二生化区及第二过滤区;In order to achieve the above-mentioned object of the invention, the present invention provides a modular multi-stage biochemical-filtration sewage treatment system. The sewage treatment system includes at least one sewage treatment area. The sewage treatment area includes a first biochemical area, a third biochemical area, and a third sewage treatment area that are connected in sequence. a filtration area, a second biochemical area and a second filtration area;
所述第一生化区的一侧与进水口连接,所述第二过滤区的末端与清水区相连,所述清水区的末端设有出水口,所述第一生化区和所述第二生化区的底部设置曝气装置,所述污水处理系统能够实现污水生化处理和泥水分离一体化。One side of the first biochemical zone is connected to the water inlet, the end of the second filter zone is connected to the clean water zone, and the end of the clean water zone is provided with a water outlet. The first biochemical zone and the second biochemical zone An aeration device is installed at the bottom of the zone, and the sewage treatment system can integrate sewage biochemical treatment and mud-water separation.
优选的,所述第一生化区为缺氧区,所述第二生化区为好氧区。Preferably, the first biochemical zone is an anoxic zone, and the second biochemical zone is an aerobic zone.
优选的,所述污水在所述第一生化区和所述第二生化区的停留时间均为2~6h。Preferably, the residence time of the sewage in the first biochemical zone and the second biochemical zone is both 2 to 6 hours.
优选的,所述第一过滤内并排设置若干可拆卸的过滤组件,所述过滤组件包括固定骨架和分别设置于所述固定骨架两侧的柔性填料。Preferably, several detachable filter assemblies are arranged side by side in the first filter, and the filter assemblies include a fixed frame and flexible fillers respectively provided on both sides of the fixed frame.
优选的,所述柔性填料的厚度为2~5cm。Preferably, the thickness of the flexible filler is 2 to 5 cm.
优选的,所述过滤组件的个数为1~20。Preferably, the number of filter components is 1 to 20.
优选的,所述第一过滤区内设有若干安装卡槽,所述固定骨架上的相应位置设有能够卡设于所述安装卡槽内的安装块。Preferably, the first filter area is provided with a plurality of installation slots, and corresponding positions on the fixed frame are provided with installation blocks that can be clamped in the installation slots.
优选的,所述安装卡槽的个数不小于所述安装块的个数。Preferably, the number of the installation slots is not less than the number of the installation blocks.
优选的,所述固定骨架为四边形,所述固定骨架内设有用于固定所述柔性填料的固定件。Preferably, the fixed frame is quadrangular, and a fixing piece for fixing the flexible filler is provided inside the fixed frame.
优选的,所述第一过滤区和所述第二过滤区为缺氧区。Preferably, the first filtration zone and the second filtration zone are anoxic zones.
本发明的有益效果是:The beneficial effects of the present invention are:
1、本发明提出的模块化多级生化-过滤污水处理系统,至少包括一个污水处理区,通过将污水处理区设置呈依次连通的第一生化区、第一过滤区、第二生化区及第二过滤区,并使第一生化区为缺氧区,第二生化区为好氧区, 可实现多级生化-过滤处理,从而可在不设置沉淀池,无需污泥回流和消化液回流,即可去除污水中的污染物和实现泥水分离。通过上述方式,减少了污水处理系统的占地面积,降低了污水处理系统的运行能耗和运营维护管理难度。1. The modular multi-stage biochemical-filtration sewage treatment system proposed by the present invention includes at least one sewage treatment area. The sewage treatment area is arranged in a sequentially connected first biochemical area, first filtration area, second biochemical area and third There are two filtration zones, and the first biochemical zone is an anoxic zone, and the second biochemical zone is an aerobic zone, which can realize multi-stage biochemical-filtration treatment, so that there is no need to set up a sedimentation tank, and there is no need for sludge reflux and digestive juice reflux. It can remove pollutants in sewage and achieve mud-water separation. Through the above method, the area occupied by the sewage treatment system is reduced, and the operating energy consumption and operation, maintenance and management difficulty of the sewage treatment system are reduced.
2、本发明提出的模块化多级生化-过滤污水处理系统,通过将第一生化区和第二生化区设置成缺氧区、好氧区交替状态,使过滤系统总体呈现多级AO形式,有助于强化脱氮效果;通过在每一级生化区的末端设置过滤区,可对生化处理后的污水经行过滤,使活性污泥被拦截在生化区,利于延长污泥泥龄,有助于硝化细菌繁殖,促进生物脱氮;通过在过滤区内设置多组可拆卸的过滤组件,同时以柔性填料实现过滤的目的,不仅便于对过滤组件进行安装和拆卸,还可在确保过滤效果的同时确保污水在过滤组件具有高的滤过通量,另外,由于污水是逐个经过过滤组件的,因此只会堵塞先经过的过滤组件,后续的过滤组件则不易出现堵塞,再者,可拆卸设置过滤组件的方式可在过滤组件出现堵塞的时候,将其与另一过滤区的末端的过滤组件进行更换,利用内部水进行反洗即可,也可通过离线清洗,上述过程有效解决了过滤组件被堵塞的问题,实现了过滤组件的再循环利用,有效提升了污水处理系统的实用性,此外,过滤组件上的柔性填料的外部好氧,内部局部缺氧,可实现反硝化脱氮和部分同步硝化脱氮功能。本发明提出的污水处理系统,通过利用间隔设置的生化区和过滤区来对污水进行交替的生化-过滤处理,同时在过滤区内部设置能够促进脱氮效果的柔性填料提升脱氮效果,此外,在实际应用中时,还可根据需要增设污水处理区,通过上述方式,有效提升了污水处理效率,并能不设置沉淀池就实现污水生化处理与泥水分离一体化,有效减少了污水处理过程成本。2. The modular multi-stage biochemical-filtration sewage treatment system proposed by the present invention makes the overall filtration system present a multi-stage AO form by setting the first biochemical zone and the second biochemical zone to alternate anoxic and aerobic zones. It helps to strengthen the denitrification effect; by setting up a filter area at the end of each level of biochemical zone, the sewage after biochemical treatment can be filtered, so that the activated sludge is intercepted in the biochemical zone, which is beneficial to prolonging the sludge age and has the effect of Helps the reproduction of nitrifying bacteria and promotes biological denitrification; by setting up multiple sets of detachable filter components in the filter area, and using flexible fillers to achieve the purpose of filtration, it not only facilitates the installation and disassembly of the filter components, but also ensures the filtration effect At the same time, it ensures that the sewage has a high filtration flux in the filter assembly. In addition, since the sewage passes through the filter assembly one by one, it will only block the filter assembly that passes through it first, and the subsequent filter assembly will not be easily clogged. Furthermore, it is removable The way to set up the filter component is that when the filter component is clogged, it can be replaced with the filter component at the end of another filter area, and the internal water can be used for backwashing, or it can be cleaned offline. The above process effectively solves the problem of filtration. The problem of blocked components has been solved, and the recycling of filter components has been realized, effectively improving the practicality of the sewage treatment system. In addition, the flexible filler on the filter component has external aerobic and internal local anoxia, which can realize denitrification, denitrification and denitrification. Partially synchronized nitrification and denitrification function. The sewage treatment system proposed by the present invention performs alternating biochemical and filtration treatment of sewage by utilizing biochemical zones and filtration zones arranged at intervals, and at the same time, flexible fillers that can promote the denitrification effect are provided inside the filtration zone to improve the denitrification effect. In addition, In actual applications, a sewage treatment area can also be added as needed. Through the above method, the sewage treatment efficiency is effectively improved, and the biochemical treatment of sewage and mud water separation can be integrated without setting up a sedimentation tank, effectively reducing the cost of the sewage treatment process. .
附图说明Description of the drawings
图1为本发明的模块化多级生化-过滤污水处理系统的结构示意图;Figure 1 is a schematic structural diagram of the modular multi-stage biochemical-filtration sewage treatment system of the present invention;
图2为图1中的过滤组件的结构示意图;Figure 2 is a schematic structural diagram of the filter assembly in Figure 1;
图3为图2中的单个过滤组件的结构示意图;Figure 3 is a schematic structural diagram of a single filter component in Figure 2;
图4为图3中的过滤组件的结构示意图;Figure 4 is a schematic structural diagram of the filter assembly in Figure 3;
图5为本发明的模块化多级生化-过滤污水处理系统的流程图;Figure 5 is a flow chart of the modular multi-stage biochemical-filtration sewage treatment system of the present invention;
附图标记如下:The reference numbers are as follows:
100、模块化多级生化-过滤污水处理系统;10、污水处理区;20、第一生化区;21、进水口;30、第一过滤区;31、过滤组件;311、固定骨架;312、柔性填料;40、第二生化区;50、第二过滤区;51、清水区;511、出水口;60、曝气装置。100. Modular multi-stage biochemical-filtration sewage treatment system; 10. Sewage treatment area; 20. First biochemical area; 21. Water inlet; 30. First filtration area; 31. Filter components; 311. Fixed frame; 312. Flexible filler; 40. Second biochemical zone; 50. Second filtration zone; 51. Clean water zone; 511. Water outlet; 60. Aeration device.
具体实施方式Detailed ways
为了使本发明的目的、技术方案和优点更加清楚,下面结合附图和具体实施例对本发明进行详细描述。In order to make the purpose, technical solutions and advantages of the present invention clearer, the present invention will be described in detail below with reference to the drawings and specific embodiments.
在此,还需要说明的是,为了避免因不必要的细节而模糊了本发明,在附图中仅仅示出了与本发明的方案密切相关的结构和/或处理步骤,而省略了与本发明关系不大的其他细节。Here, it should also be noted that, in order to avoid obscuring the present invention with unnecessary details, only the structures and/or processing steps closely related to the solution of the present invention are shown in the drawings, and the details related to the present invention are omitted. Invent other details that are less relevant.
另外,还需要说明的是,术语“包括”、“包含”或者其任何其他变体意在涵盖非排他性的包含,从而使得包括一系列要素的过程、方法、物品或者设备不仅包括那些要素,而且还包括没有明确列出的其他要素,或者是还包括为这种过程、方法、物品或者设备所固有的要素。Additionally, it should be noted that the terms "comprises," "comprises," or any other variation thereof are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that includes a list of elements includes not only those elements, but also It also includes other elements not expressly listed or that are inherent to the process, method, article or equipment.
请参阅图1至5所示,本发明提供的模块化多级生化-过滤污水处理系统100,上述污水处理系统至少包括一个污水处理区10,每个污水处理区包括依次连通的第一生化区20、第一过滤区30、第二生化区40及第二过滤区50,第一生化区20的一侧与进水口21连接,第二过滤区50的末端与清水区51相连,清水区51的末端设有出水口511,第一生化区20和第二生化区40的底部设置曝气装置60,以便控制上述生化区为缺氧或好氧状态。通过利用上述系统对污水进行多级生化处理和过滤处理,实现了污水生化处理和泥水分离一体化,提高了污水中固体悬浮物的去除效率,并能提高脱氮效果。Referring to Figures 1 to 5, the present invention provides a modular multi-stage biochemical-filtration sewage treatment system 100. The above-mentioned sewage treatment system includes at least one sewage treatment area 10, and each sewage treatment area includes a first biochemical area connected in sequence. 20. The first filtration area 30, the second biochemical area 40 and the second filtration area 50. One side of the first biochemical area 20 is connected to the water inlet 21, and the end of the second filtration area 50 is connected to the clean water area 51. The clean water area 51 A water outlet 511 is provided at the end, and an aeration device 60 is provided at the bottom of the first biochemical zone 20 and the second biochemical zone 40 to control the above-mentioned biochemical zones to be in an anoxic or aerobic state. By using the above system to perform multi-stage biochemical treatment and filtration of sewage, the integration of sewage biochemical treatment and mud and water separation is achieved, which improves the removal efficiency of solid suspended matter in sewage and improves the denitrification effect.
请参阅图1至图4所示,第一生化区20和第二生化区40的底部设置曝气装置60,使第一生化区20为缺氧区,第二生化区40为好氧区,污水在第一生化区20内发生反硝化反应,在第二生化区40发生硝化反应,且污水在第一生化区20和第二生化区40的停留时间为2~6h,确保生化反应的充分进行,同时还可利于污水中的污泥进行沉降。Referring to Figures 1 to 4, an aeration device 60 is provided at the bottom of the first biochemical zone 20 and the second biochemical zone 40, so that the first biochemical zone 20 is an anoxic zone and the second biochemical zone 40 is an aerobic zone. The denitrification reaction of sewage occurs in the first biochemical zone 20, and the nitrification reaction occurs in the second biochemical zone 40, and the residence time of the sewage in the first biochemical zone 20 and the second biochemical zone 40 is 2 to 6 hours, ensuring the sufficient biochemical reaction. It can also facilitate the sedimentation of sludge in sewage.
进一步地,第一过滤区30设置于第一生化区20的末端,第一过滤区30内并排设置若干可拆卸的过滤组件31,过滤组件31的个数为1~20,在该过滤组件31个数下,即可确保过滤效果,同时便于过滤后的水体顺利通过;过滤组件31包括固定骨架311和分别设置于固定骨架311两侧的柔性填料312,固定骨架311为四边形,固定骨架311内设有用于固定柔性填料的固定件,以确保柔性填料312能够稳定固定于固定骨架311上,并能满足污水厂鼓励过程中对过滤组件31的强度要求,每一侧的柔性填料312的厚度为2~5cm,由于过滤区处于缺氧状态,因而柔性填料312上能够生长一定量的反硝化微生物,从而提高反硝化脱氮效果,本实施例中的柔性填料312为聚氨酯海绵,在另一些实施例中也可以为其他材料,只要能够满足过滤时对过滤组件31的强度、过滤阻力及过滤通量的要求即可,此处不以此为限。Further, the first filtration area 30 is disposed at the end of the first biochemical area 20. A number of detachable filter assemblies 31 are arranged side by side in the first filtration area 30. The number of the filter assemblies 31 is 1 to 20. In the filter assemblies 31 The filter assembly 31 includes a fixed frame 311 and flexible fillers 312 respectively provided on both sides of the fixed frame 311. The fixed frame 311 is quadrilateral. There are fixing pieces for fixing the flexible filler to ensure that the flexible filler 312 can be stably fixed on the fixed frame 311 and can meet the strength requirements of the filter assembly 31 during the encouragement process of the sewage plant. The thickness of the flexible filler 312 on each side is 2 ~ 5cm. Since the filter area is in an anoxic state, a certain amount of denitrifying microorganisms can grow on the flexible filler 312, thereby improving the denitrification and denitrification effect. The flexible filler 312 in this embodiment is a polyurethane sponge. In other implementations In this example, other materials can also be used, as long as they can meet the requirements for the strength, filtration resistance and filtration flux of the filter component 31 during filtration, and are not limited to this here.
特别地,过滤组件31可拆卸设置于第一过滤区30,具体地,第一过滤区30内设有若干安装卡槽(图中未示出),过滤组件31的固定骨架311上的相应位置设有可卡设于安装卡槽内的安装块(图中未标号),且安装卡槽的个数不小于安装块的个数,如此设置,可便于对过滤组件31进行安装和拆卸;另外,当第一过滤区30出现堵塞时,可将靠近第一过滤区30的过滤组件31与第二过滤区50末端的过滤组件31进行更换,并将从第一过滤区30上换下的过滤组件31安装至第二过滤区50末端,同时使过滤组件31的过滤面朝外,利用系统内部水力对过滤面进行反洗,也可直接对拆下的过滤组件31离线清洗。通过上述设置,可使经过预处理的污水依次经过每一级生化区和过滤区,交替对污水进行生化和过滤处理,从而使污水中的污染物浓度和活性污泥浓度逐级降低,同时,每次过滤后活性污泥均被截留在过滤区,实 现了污泥和水力的分离,延长污泥泥龄,有助于硝化细菌繁殖,促进生物脱氮。第二过滤区50设置于第二生化区40的末端,其结构和第一过滤区30基本一致,在此不再赘述。需要说明的是,实际应用过程中还可根据污水内的污染物的情况对污水处理区的组成进行调整,当污水中的污染物浓度很低时也可只设置第一生化区20和第一过滤区30,当污水中的污染物浓度很高时,可根据实际需要适应性增加污水处理区。In particular, the filter assembly 31 is detachably disposed in the first filter area 30. Specifically, the first filter area 30 is provided with a number of installation slots (not shown in the figure). The corresponding positions on the fixed frame 311 of the filter assembly 31 are There are installation blocks (not numbered in the figure) that can be stuck in the installation slots, and the number of installation slots is not less than the number of installation blocks. This arrangement can facilitate the installation and removal of the filter assembly 31; in addition, , when the first filter area 30 is clogged, the filter assembly 31 close to the first filter area 30 and the filter assembly 31 at the end of the second filter area 50 can be replaced, and the filter assembly 31 removed from the first filter area 30 can be replaced. The component 31 is installed at the end of the second filter area 50 with the filtering surface of the filtering component 31 facing outward. The filtering surface is backwashed using the hydraulic power inside the system. The removed filtering component 31 can also be directly cleaned offline. Through the above settings, the pretreated sewage can pass through each level of biochemical zone and filtration zone in sequence, and the sewage can be biochemically and filtered alternately, so that the concentration of pollutants and activated sludge concentration in the sewage can be gradually reduced. At the same time, After each filtration, the activated sludge is trapped in the filtration area, which realizes the separation of sludge and hydraulics, prolongs the sludge age, helps nitrifying bacteria reproduce, and promotes biological denitrification. The second filtration area 50 is disposed at the end of the second biochemical area 40, and its structure is basically the same as that of the first filtration area 30, which will not be described again here. It should be noted that in the actual application process, the composition of the sewage treatment area can also be adjusted according to the pollutants in the sewage. When the concentration of pollutants in the sewage is very low, only the first biochemical zone 20 and the first biochemical zone 20 can be set. In the filtering area 30, when the concentration of pollutants in the sewage is very high, the sewage treatment area can be adaptively added according to actual needs.
本发明的工作原理:应用本发明提出的块化多级生化-过滤污水处理系统100进行污水处理时,先通过进水口21将经过预处理的污水引入第一生化区20,由于该区域为缺氧状态,该区域内发生反硝化反应,接着,经过第一生化区20处理的水力经过第一过滤区30,第一过滤区30内的过滤组件31可对水力中的活性污泥进行截留,使淤泥停留在第一生化区20内。然后,经过第一过滤区30过滤的水体进入好氧的第二生化区40进行第二次生化反应,最后经第二过滤区50的过滤作用即得到干净的水体,若此时的水体内仍存在污染物,可通过增设污水处理区进一步对水体进行生化和过滤处理,直至水体内无污染物。本领域技术人员应当理解,增设污水处理池后,应使首个第一生化区20与进水口21连接,最后一个第二过滤区50与清水区51相连。Working principle of the present invention: When applying the modular multi-stage biochemical-filtration sewage treatment system 100 proposed by the present invention for sewage treatment, the pretreated sewage is first introduced into the first biochemical zone 20 through the water inlet 21. Since this area is lacking Oxygen state, denitrification reaction occurs in this area, then, the hydraulic treated by the first biochemical zone 20 passes through the first filtering zone 30, and the filter assembly 31 in the first filtering zone 30 can intercept the activated sludge in the hydraulic, The sludge is allowed to stay in the first biochemical zone 20 . Then, the water filtered by the first filtration zone 30 enters the aerobic second biochemical zone 40 for a second biochemical reaction. Finally, through the filtration of the second filtration zone 50, a clean water body is obtained. If the water body at this time is still If there are pollutants, the water body can be further biochemically and filtered by adding a sewage treatment area until the water body is free of pollutants. Those skilled in the art should understand that after adding a sewage treatment tank, the first first biochemical zone 20 should be connected to the water inlet 21 , and the last second filter zone 50 should be connected to the clean water zone 51 .
综上所述,本发明模块化多级生化-过滤污水处理系统100,上述污水处理系统至少包括一个污水处理区,污水处理区包括依次连通的第一生化区20、第一过滤区30、第二生化区40及第二过滤区50;第一生化区20的一侧与进水口21连接,第二过滤区50的末端与清水区51相连,清水区51的末端设有出水口511,第一生化区20和第二生化区40的底部与曝气装置60连接,污水处理系统能够实现污水生化处理和泥水分离一体化;通过使第一生化区20为缺氧区,第二生化区40为好氧区,可实现多级生化-过滤处理。通过上述方式,有效提升了污水处理效率,并能不设置沉淀池就实现污水生化处理与泥水分离一体化,有效减少了污水处理过程的成本。To sum up, the modular multi-stage biochemical-filtration sewage treatment system 100 of the present invention includes at least one sewage treatment area. The sewage treatment area includes a first biochemical area 20, a first filtration area 30, and a first sewage treatment area connected in sequence. The second biochemical zone 40 and the second filter zone 50; one side of the first biochemical zone 20 is connected to the water inlet 21, the end of the second filter zone 50 is connected to the clean water zone 51, and the end of the clean water zone 51 is provided with a water outlet 511. The bottoms of the first biochemical zone 20 and the second biochemical zone 40 are connected to the aeration device 60, and the sewage treatment system can realize the integration of sewage biochemical treatment and mud water separation; by making the first biochemical zone 20 an anoxic zone, the second biochemical zone 40 It is an aerobic zone and can achieve multi-stage biochemical-filtration treatment. Through the above method, the efficiency of sewage treatment is effectively improved, and the biochemical treatment of sewage and mud water separation can be integrated without setting up a sedimentation tank, effectively reducing the cost of the sewage treatment process.
以上实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发 明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围。The above embodiments are only used to illustrate the technical solutions of the present invention and are not limiting. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be modified or equivalently substituted. without departing from the spirit and scope of the technical solution of the present invention.

Claims (10)

  1. 一种模块化多级生化-过滤污水处理系统,其特征在于,所述污水处理系统至少包括一个污水处理区,所述污水处理区包括依次连通的第一生化区、第一过滤区、第二生化区及第二过滤区;A modular multi-stage biochemical-filtration sewage treatment system, characterized in that the sewage treatment system includes at least one sewage treatment area, and the sewage treatment area includes a first biochemical area, a first filtration area, and a second sewage treatment area that are connected in sequence. Biochemical area and second filtration area;
    所述第一生化区的一侧与进水口连接,所述第二过滤区的末端与清水区相连,所述清水区的末端设有出水口,所述第一生化区和所述第二生化区的底部设置曝气装置,所述污水处理系统能够实现污水生化处理和泥水分离一体化。One side of the first biochemical zone is connected to the water inlet, the end of the second filter zone is connected to the clean water zone, and the end of the clean water zone is provided with a water outlet. The first biochemical zone and the second biochemical zone An aeration device is installed at the bottom of the zone, and the sewage treatment system can integrate sewage biochemical treatment and mud-water separation.
  2. 根据权利要求1所述的模块化多级生化-过滤污水处理系统,其特征在于,所述第一生化区为缺氧区,所述第二生化区为好氧区。The modular multi-stage biochemical-filtration sewage treatment system according to claim 1, wherein the first biochemical zone is an anoxic zone and the second biochemical zone is an aerobic zone.
  3. 根据权利要求1所述的模块化多级生化-过滤污水处理系统,其特征在于,所述污水在所述第一生化区和所述第二生化区的停留时间均为2~6h。The modular multi-stage biochemical-filtration sewage treatment system according to claim 1, characterized in that the residence time of the sewage in the first biochemical zone and the second biochemical zone is 2 to 6 hours.
  4. 根据权利要求1所述的模块化多级生化-过滤污水处理系统,其特征在于,所述第一过滤内并排设置若干可拆卸的过滤组件,所述过滤组件包括固定骨架和分别设置于所述固定骨架两侧的柔性填料。The modular multi-stage biochemical-filtration sewage treatment system according to claim 1, characterized in that, a plurality of detachable filter components are arranged side by side in the first filter, and the filter components include a fixed frame and a fixed frame respectively arranged on the Flexible padding on both sides of the frame.
  5. 根据权利要求4所述的模块化多级生化-过滤污水处理系统,其特征在于,所述柔性填料的厚度为2~5cm。The modular multi-stage biochemical-filtration sewage treatment system according to claim 4, characterized in that the thickness of the flexible filler is 2 to 5 cm.
  6. 根据权利要求4所述的模块化多级生化-过滤污水处理系统,其特征在于,所述过滤组件的个数为1~20。The modular multi-stage biochemical-filtration sewage treatment system according to claim 4, characterized in that the number of the filter components is 1 to 20.
  7. 根据权利要求6所述的模块化多级生化-过滤污水处理系统,其特征在于,所述第一过滤区内设有若干安装卡槽,所述固定骨架上的相应位置设有能够卡设于所述安装卡槽内的安装块。The modular multi-stage biochemical-filtration sewage treatment system according to claim 6, characterized in that a plurality of installation slots are provided in the first filtering area, and corresponding positions on the fixed frame are provided with clamping devices. The installation block in the installation card slot.
  8. 根据权利要求7所述的模块化多级生化-过滤污水处理系统,其特征在于,所述安装卡槽的个数不小于所述安装块的个数。The modular multi-stage biochemical-filtration sewage treatment system according to claim 7, characterized in that the number of the installation slots is not less than the number of the installation blocks.
  9. 根据权利要求4所述的模块化多级生化-过滤污水处理系统,其特征在于,所述固定骨架为四边形,所述固定骨架内设有用于固定所述柔性填料的固定件。The modular multi-stage biochemical-filtration sewage treatment system according to claim 4, wherein the fixed frame is quadrilateral, and a fixing piece for fixing the flexible filler is provided in the fixed frame.
  10. 根据权利要求1所述的模块化多级生化-过滤污水处理系统,其特征在 于,所述第一过滤区和所述第二过滤区为缺氧区。The modular multi-stage biochemical-filtration sewage treatment system according to claim 1, characterized in that the first filtration zone and the second filtration zone are anoxic zones.
PCT/CN2022/121626 2022-07-19 2022-09-27 Modular multi-stage biochemical-filtering sewage treatment system WO2023178966A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202210845739.7 2022-07-19
CN202210845739.7A CN115231704A (en) 2022-07-19 2022-07-19 Modular multistage biochemical-filtering sewage treatment system

Publications (1)

Publication Number Publication Date
WO2023178966A1 true WO2023178966A1 (en) 2023-09-28

Family

ID=83673855

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2022/121626 WO2023178966A1 (en) 2022-07-19 2022-09-27 Modular multi-stage biochemical-filtering sewage treatment system

Country Status (2)

Country Link
CN (1) CN115231704A (en)
WO (1) WO2023178966A1 (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007007557A (en) * 2005-06-30 2007-01-18 Maezawa Ind Inc Waste water treatment apparatus
CN105236577A (en) * 2015-09-23 2016-01-13 南京吉佳新材料科技实业有限公司 Detachable module-type wetland system, and sewage treatment method
CN107162197A (en) * 2017-07-10 2017-09-15 北京科技大学 Three rank O/A decentralized type sewages handle integrated apparatus and method
CN110642476A (en) * 2019-10-30 2020-01-03 重庆郅治环保科技有限公司 Multistage A/O sewage treatment system
CN210683533U (en) * 2019-10-11 2020-06-05 润田环境工程有限公司 Rural domestic sewage treatment integration equipment
CN112624499A (en) * 2020-12-10 2021-04-09 农业农村部环境保护科研监测所 Integrated single-family and household-connected rural domestic sewage treatment method

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2944804A1 (en) * 1978-11-06 1980-05-22 Kureha Chemical Ind Co Ltd Biological sewage treatment - by alternate immersion and raised aeration of biologically active structures
CN107777773A (en) * 2016-08-25 2018-03-09 冯葆如 A kind of batch-type exchange cycles method for activated sludge wastewater treatment
CN107601669A (en) * 2017-11-01 2018-01-19 济宁市孚源环保科技有限公司 A kind of method based on MBBR technique upgrade expanding biochemistry pools
CN211556188U (en) * 2020-03-23 2020-09-22 深圳市金丰盛电子有限公司 Self-locking structure of annular terminal and terminal wire
CN113772805B (en) * 2021-09-17 2023-04-25 海口永祺环保设备技术有限公司 Biological film hanging device for rural sewage treatment tank
CN114031182A (en) * 2021-11-26 2022-02-11 深圳永清水务有限责任公司 Domestication and culture device for halotolerant bacteria in salt-containing wastewater and use method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007007557A (en) * 2005-06-30 2007-01-18 Maezawa Ind Inc Waste water treatment apparatus
CN105236577A (en) * 2015-09-23 2016-01-13 南京吉佳新材料科技实业有限公司 Detachable module-type wetland system, and sewage treatment method
CN107162197A (en) * 2017-07-10 2017-09-15 北京科技大学 Three rank O/A decentralized type sewages handle integrated apparatus and method
CN210683533U (en) * 2019-10-11 2020-06-05 润田环境工程有限公司 Rural domestic sewage treatment integration equipment
CN110642476A (en) * 2019-10-30 2020-01-03 重庆郅治环保科技有限公司 Multistage A/O sewage treatment system
CN112624499A (en) * 2020-12-10 2021-04-09 农业农村部环境保护科研监测所 Integrated single-family and household-connected rural domestic sewage treatment method

Also Published As

Publication number Publication date
CN115231704A (en) 2022-10-25

Similar Documents

Publication Publication Date Title
CN101624252B (en) Efficient treatment process for printing and dyeing waste water
CN200999217Y (en) Composite membrane bioreactor
CN102583747A (en) Device and process for biochemically denitrifying high-ammonia nitrogen tanning wastewater
CN114084998A (en) Rubbish transfer station waste water and domestic sewage cooperative processing system
CN104341076A (en) Continuous biochemical reaction and intermittent static precipitation integrated sewage treatment device
CN103172176A (en) Technology for treating chemical wastewater by immobilized microorganism and zigzag packed bed and equipment thereof
CN202576155U (en) Biochemical denitrification treatment device for high ammonia nitrogen tannery wastewater
US7820048B2 (en) Method and system for treating organically contaminated waste water
CN212025101U (en) MBR integration sewage treatment plant
CN105110556A (en) Integrated denitrification decarbonization biological aerated filter and processing system thereof
CN116693057A (en) Intelligent modularized integrated treatment equipment for domestic sewage in high-speed service area of cold area
WO2023178966A1 (en) Modular multi-stage biochemical-filtering sewage treatment system
CN111606502A (en) Harmless wastewater treatment process and system for livestock and poultry died of diseases
CN218321041U (en) Domestic sewage treatment system of IASBR technology coupling magnetism biochar
KR20080089799A (en) A wastewater transaction system
CN104310587A (en) Denitrification and dephosphorization wastewater treatment system and process
CN113912248A (en) Composite process treatment system suitable for rural domestic sewage
CN213112947U (en) AO is biochemical-MBR integration effluent treatment plant
CN202754840U (en) Biological aerated filters in two-stage serial connection
CN208361984U (en) It is a kind of for being electroplated, board wastewater processing multi-stage aeration biological filter tank
CN101607774A (en) A kind of sewage disposal device and method
CN204752324U (en) Sewage continuous flow AO biochemical reactions and static integrated device that deposits of mud
CN215712488U (en) Composite process treatment system suitable for rural domestic sewage
CN210340633U (en) Novel nitrogen and phosphorus removal integrated equipment
CN216141336U (en) MBR domestic sewage treatment device

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 22933018

Country of ref document: EP

Kind code of ref document: A1