CN205115214U - Distributed rural domestic sewage integrated process device of modularization MBR - Google Patents

Distributed rural domestic sewage integrated process device of modularization MBR Download PDF

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CN205115214U
CN205115214U CN201520542126.1U CN201520542126U CN205115214U CN 205115214 U CN205115214 U CN 205115214U CN 201520542126 U CN201520542126 U CN 201520542126U CN 205115214 U CN205115214 U CN 205115214U
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tank
mbr
mbr membrane
pool
membrane cisterna
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张心良
陈静
洪祖喜
陈伟
张绍君
季颖
沈婧
张娅萍
滕美珍
徐文倩
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Shanghai Academy of Environmental Sciences
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Abstract

本实用新型涉及一种模块化MBR分散式农村生活污水集成处理装置,所述的处理装置将MBR膜生物反应器与缺氧池采用一体式净化槽的结构,依序包括沉渣池、调节池、一体式净化槽和清水池,各池水位由浮球液位器和电磁阀控制,污水进入沉渣池,经沉渣池沉淀后的污水自流进入调节池,在调节池内匀质、匀量后,泵入一体式净化槽的缺氧池,然后进入MBR膜池,所述的MBR膜池与鼓风机连通作为曝气池,在MBR膜池设置投放除磷剂的加料口,鼓风机对MBR膜池内的污水进行鼓风曝气并对MBR膜生物反应器的膜组件进行冲刷以降低膜污染;曝气后的混合液通过气提管抽提回流至缺氧池,生化反应出水经过膜分离后由自吸泵泵入清水池,污泥经剩余污泥排泥管到沉渣池。

The utility model relates to a modularized MBR decentralized rural domestic sewage integrated treatment device. The treatment device adopts an integrated purification tank structure of an MBR membrane bioreactor and anoxic pool, and sequentially includes a sediment pool, a regulating pool, Integrated purification tank and clear water tank, the water level of each tank is controlled by a float level device and a solenoid valve, the sewage enters the sediment tank, and the sewage after sedimentation in the sediment tank flows into the regulating tank by itself, and after being homogenized and uniform in the regulating tank, the pump Enter the anoxic pool of the integrated purification tank, and then enter the MBR membrane pool. The MBR membrane pool is connected with the blower as an aeration tank. Perform blower aeration and flush the membrane modules of the MBR membrane bioreactor to reduce membrane fouling; the mixed solution after aeration is extracted and returned to the anoxic tank through the air stripping tube, and the biochemical reaction effluent is separated by the membrane and then absorbed by the self-priming The pump is pumped into the clear water tank, and the sludge is sent to the sediment tank through the remaining sludge discharge pipe.

Description

模块化MBR分散式农村生活污水集成处理装置Modular MBR decentralized rural domestic sewage integrated treatment device

技术领域 technical field

本实用新型涉及一种模块化MBR分散式农村生活污水集成处理装置,适用于小型分散式农村生活污水处理、有中水回用要求的小区或度假村,或生态敏感区的生活污水处理等。 The utility model relates to a modular MBR decentralized rural domestic sewage integrated treatment device, which is suitable for small-scale decentralized rural domestic sewage treatment, residential areas or resorts with reclaimed water reuse requirements, or domestic sewage treatment in ecologically sensitive areas.

背景技术 Background technique

现有技术中,有的将抽屉式膜技术应用于农村生活污水处理,有的将生物滤床用于净化槽中实现生活污水的高效处理,也有的采用平推流二段厌氧滤床和全混流好氧生物膜一体化技术用于净化槽中处理生活污水,还有的研发了新型的集成反应器用于农村生活污水的脱氮处理。 In the prior art, some apply drawer-type membrane technology to rural domestic sewage treatment, some use biological filter beds in purification tanks to achieve efficient treatment of domestic sewage, and some use plug-flow two-stage anaerobic filter beds and The fully mixed-flow aerobic biofilm integrated technology is used to treat domestic sewage in the purification tank, and a new type of integrated reactor has been developed for the denitrification treatment of rural domestic sewage.

MBR污水处理技术是生物处理技术与膜分离技术相结合的一种新技术,,是现代污水处理的一种常用方式,其采用膜生物反应器(MembraneBioreactor,简称MBR〕,取代传统工艺中的二沉池,可以高效地进行固液分离,得到可回用的稳定中水。适用范围:住宅小区、办公楼、商场、宾馆、饭店、机关、学校、部队、工厂等生活污水和与之类似的工业有机废水等。 MBR sewage treatment technology is a new technology combining biological treatment technology and membrane separation technology. It is a common way of modern sewage treatment. Sedimentation tanks can efficiently separate solids and liquids to obtain reusable and stable reclaimed water. Scope of application: residential quarters, office buildings, shopping malls, hotels, restaurants, institutions, schools, troops, factories and other domestic sewage and similar Industrial organic wastewater, etc.

A/O生物除磷工艺是由厌氧和好氧两部分反应组成的污水生物处理系统。污水进入厌氧池后,与回流污泥混合。活性污泥中的聚磷菌在这一过程中大量吸收污水中的BOD,并将污泥中的磷以正磷酸盐的形式释放到混合液中。混合液进入好氧池后,有机物被氧化分解,同时,聚磷菌大量吸收混合液中的正磷酸盐。由于聚磷菌在好氧条件下吸收的磷多于厌氧条件下释放的磷,因此污水经过“厌氧-好氧”的交替作用和二沉池的污泥分离达到除磷的目的。一般情况下,TP的去除率可达到85%以上。 The A/O biological phosphorus removal process is a sewage biological treatment system composed of anaerobic and aerobic two-part reactions. After the sewage enters the anaerobic tank, it is mixed with the return sludge. During this process, the phosphorus accumulating bacteria in the activated sludge absorb a large amount of BOD in the sewage and release the phosphorus in the sludge into the mixed solution in the form of orthophosphate. After the mixed solution enters the aerobic tank, the organic matter is oxidized and decomposed, and at the same time, the phosphorus-accumulating bacteria absorb a large amount of orthophosphate in the mixed solution. Since the phosphorus-accumulating bacteria absorb more phosphorus under aerobic conditions than they release under anaerobic conditions, the purpose of phosphorus removal is achieved through the alternating action of "anaerobic-aerobic" and the separation of sludge in the secondary sedimentation tank. In general, the removal rate of TP can reach more than 85%.

另外,有文献报道了青岛流亭国际机场污水处理站采用A/O法与MBR的结合工艺,COD、氨氮去除率稳定,运行费用为每吨水1.90元。文献基于城市污水处理和农村生活污水去除CODCr、BOD5和SS的效益分析,对城市污水处理厂的处理效果和运营成本同时进行了对比分析。 In addition, there are literature reports that Qingdao Liuting International Airport sewage treatment station adopts the combined process of A/O method and MBR, the removal rate of COD and ammonia nitrogen is stable, and the operating cost is 1.90 yuan per ton of water. Based on the benefit analysis of urban sewage treatment and rural domestic sewage removal of COD Cr , BOD 5 and SS, the literature compares and analyzes the treatment effect and operating cost of urban sewage treatment plants at the same time.

如:专利号:201420296372.9涉及污水处理领域,提供了一种分散式模块化生活污水处理装置,包括生物处理模块、过滤模块和设备管路模块以及控制模块;所述生物处理模块为集成式一体化污水处理池,包括接触氧化池、斜管沉淀池、中间水池和消毒池;所述设备管路模块包括毛发收集器、水泵及风机等设备;生活污水经过毛发收集器进入接触氧化池,经过接触氧化池处理后进入斜管沉淀池,经过斜管沉淀池处理后进入中间水池,经过中间水池缓冲后进入过滤模块,经过过滤罐过滤后进入消毒池进行消毒。该分散式模块化生活污水处理装置具有产品集成化高、模块化设计、现场安装方便快捷、占地面积小、运行稳定且成本低、自控程度高、操作简单、维护方便、出水水质好且稳定、可直接回用于冲厕和绿化等优点。 For example: Patent No.: 201420296372.9 relates to the field of sewage treatment and provides a decentralized modular domestic sewage treatment device, including biological treatment modules, filtration modules, equipment pipeline modules and control modules; the biological treatment modules are integrated Sewage treatment ponds, including contact oxidation ponds, inclined tube sedimentation ponds, intermediate pools and disinfection ponds; the equipment pipeline modules include hair collectors, water pumps, fans and other equipment; domestic sewage enters the contact oxidation ponds through the hair collectors, and after contacting After being treated in the oxidation tank, it enters the inclined tube sedimentation tank, after being treated in the inclined tube sedimentation tank, it enters the intermediate pool, after being buffered by the intermediate pool, it enters the filtration module, and after being filtered by the filter tank, it enters the disinfection pool for disinfection. The decentralized modular domestic sewage treatment device has high product integration, modular design, convenient and quick on-site installation, small footprint, stable operation and low cost, high degree of self-control, simple operation, convenient maintenance, good and stable effluent quality , It can be directly reused for toilet flushing and greening.

专利申请号:201310000914.3涉及一种好氧流离与磁絮凝集成污水处理装置与方法,属于污水处理领域。污水处理装置由进水池、好氧池、混合池、絮凝池、沉淀池、在线控制装置、磁分离器组成。该技术采用好氧流离生物处理技术与磁絮凝处理技术连用,实现污水连续流反应器的短程硝化、同步硝化反硝化和磁分离技术的有机结合,能够有效实现生活污水的脱氮除磷和降低有机物含量的目标。该技术在实际应用中具有节能、占地面积小、处理水质好,处理成本低廉等优点。 Patent application number: 201310000914.3 relates to an aerobic flow separation and magnetic flocculation integrated sewage treatment device and method, belonging to the field of sewage treatment. The sewage treatment device consists of an inlet tank, an aerobic tank, a mixing tank, a flocculation tank, a sedimentation tank, an online control device, and a magnetic separator. This technology uses aerobic flow biological treatment technology combined with magnetic flocculation treatment technology to realize the organic combination of short-range nitrification, synchronous nitrification and denitrification and magnetic separation technology of sewage continuous flow reactor, which can effectively realize the denitrification and phosphorus removal of domestic sewage and reduce the target for organic matter content. In practical application, this technology has the advantages of energy saving, small footprint, good water quality and low treatment cost.

实用新型内容 Utility model content

本实用新型目的在于:提供一种模块化MBR分散式农村生活污水集成处理装置,出水能稳定达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级以上的排放要求。 The purpose of the utility model is to provide a modularized MBR decentralized rural domestic sewage integrated treatment device, and the effluent can stably meet the discharge requirements above the first level of the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB18918-2002).

本实用新型目的通过下述方案实现:模块化MBR分散式农村生活污水集成处理装置,采用MBR膜生物反应器,至少包括沉渣池、调节池、设置MBR膜生物反应器的MBR膜池、厌氧池和清水池,其中: The purpose of the utility model is realized by the following scheme: the modularized MBR decentralized rural domestic sewage integrated treatment device adopts an MBR membrane bioreactor, and at least includes a sediment pool, a regulating pool, an MBR membrane pool provided with an MBR membrane bioreactor, an anaerobic pools and clear water pools, of which:

所述的处理装置将MBR膜生物反应器与缺氧池采用一体式净化槽的结构,依序包括沉渣池、调节池、一体式净化槽和清水池,各池水位由浮球液位器和电磁阀控制,污水进入沉渣池,经沉渣池沉淀后的污水自流进入调节池,在调节池内匀质、匀量后,泵入一体式净化槽的缺氧池,然后进入MBR膜池,所述的MBR膜池与鼓风机连通作为曝气池,在MBR膜池设置投放除磷剂的加料口,鼓风机对MBR膜池内的污水进行鼓风曝气并对MBR膜生物反应器的膜组件进行冲刷以降低膜污染;曝气后的混合液通过气提管抽提回流至缺氧池,生化反应出水经过膜分离后由自吸泵泵入清水池,污泥经剩余污泥排泥管到沉渣池。 The treatment device adopts the structure of an integrated purification tank with the MBR membrane bioreactor and the anoxic tank, and includes a sediment tank, a regulating tank, an integrated purification tank and a clear water tank in sequence, and the water level of each pool is controlled by a float level device and a clear water tank. Controlled by the solenoid valve, the sewage enters the sedimentation tank, and the sewage after sedimentation in the sedimentation tank flows into the regulating tank by itself. The MBR membrane tank is connected with the blower as an aeration tank, and the feeding port for phosphorus removal agent is set in the MBR membrane tank, and the blower blows and aerates the sewage in the MBR membrane tank and flushes the membrane components of the MBR membrane bioreactor to Reduce membrane pollution; the mixed liquid after aeration is extracted and returned to the anoxic tank through the air lift tube, the biochemical reaction effluent is pumped into the clear water tank by the self-priming pump after membrane separation, and the sludge is sent to the sediment tank through the remaining sludge sludge discharge pipe .

本实用新型采用A/O-MBR+化学除磷相结合的污水深度处理装置。在A/O系统的好氧池中设置MBR膜组件,生化池内活性污泥浓度高,实现高效的脱氮及有机物去除效果,同时采用化学强化除磷,可确保出水稳定达到国家一级排放标准。 The utility model adopts a sewage advanced treatment device combining A/O-MBR+chemical phosphorus removal. MBR membrane modules are installed in the aerobic pool of the A/O system. The concentration of activated sludge in the biochemical pool is high to achieve efficient denitrification and organic matter removal effects. At the same time, chemically enhanced phosphorus removal is used to ensure that the effluent is stable and meets the national first-level discharge standards. .

在上述方案基础上,所述的一体式净化槽采用地埋式结构,其中, On the basis of the above scheme, the integrated septic tank adopts an underground structure, wherein,

MBR膜池溶解氧控制在2~4mg/L; The dissolved oxygen in the MBR membrane pool is controlled at 2-4mg/L;

缺氧池溶解氧控制在小于0.5mg/L; The dissolved oxygen in the anoxic pool is controlled at less than 0.5mg/L;

曝气池污泥浓度:3000mg/L~6000mg/L; Aeration tank sludge concentration: 3000mg/L~6000mg/L;

所述的自吸泵运行方式为开、停间歇运行方式,如:控制开8分钟,停2分钟,以防止在自吸泵连续出水的情况下发生膜丝堵塞。 The operation mode of the self-priming pump is an intermittent operation mode of on and off, such as: control to open for 8 minutes and stop for 2 minutes, so as to prevent membrane filament clogging when the self-priming pump continuously discharges water.

在上述方案基础上,所述的一体式净化槽由罐体作为外壳,一侧设缺氧池,另一侧设MBR膜池,在所述的缺氧池和MBR膜池之间设有隔板和过水孔,在缺氧池设有进水管;MBR膜池设有膜池出水管,与污泥管、空气管连通。 On the basis of the above scheme, the tank body is used as the shell of the integrated purification tank, an anoxic pool is set on one side, an MBR membrane pool is set on the other side, and a partition is provided between the anoxic pool and the MBR membrane pool And the water hole, the anoxic tank is provided with a water inlet pipe; the MBR membrane tank is provided with a membrane tank outlet pipe, which is connected with the sludge pipe and the air pipe.

所述的一体式净化槽中,在MBR膜池的槽体上设有人孔,用于设置固定膜组件的膜导轨框架。 In the integrated purification tank, a manhole is provided on the tank body of the MBR membrane tank for setting a membrane rail frame for fixing the membrane modules.

在所述的一体式净化槽中设置管网系统,包括: A pipe network system is set in the integrated septic tank, including:

MBR膜池内由伸入膜池污泥管内的空气管,经法兰与罐体外部的连通风机的剩余污泥空气管连接,构成剩余污泥空气管系统; In the MBR membrane tank, the air pipe extending into the sludge pipe of the membrane tank is connected to the remaining sludge air pipe connected to the fan outside the tank through the flange to form the remaining sludge air pipe system;

MBR膜池污泥管连至沉渣池构成剩余污泥排泥系统; The sludge pipe in the MBR membrane tank is connected to the sediment tank to form the excess sludge discharge system;

伸入MBR膜池内的回流管,罐体外部自风机到罐体的回流管构成内回流空气管系统; The return pipe extending into the MBR membrane tank, and the return pipe from the fan to the tank outside the tank form the internal return air pipe system;

自MBR膜池至缺氧池设有内回流水管系统。 There is an internal return water pipe system from the MBR membrane pool to the anoxic pool.

在上述方案基础上,所述的MBR膜池、各电磁阀、鼓风机由自动监控设备控制,所述的自动监控设备至少包括处理器、数据采集模块、显示模块和监控模块,数据采集模块采集各池的水位、各池连接管道的瞬时流量值和累计流量值、耗电量、膜池出水管路上的负压值,数据采集模块将采集的数据输入计算机处理器,在处理器中完成数据比较和计算后,对所述的MBR膜池和各电磁阀、鼓风机进行监控。 On the basis of the above scheme, the described MBR membrane tank, each solenoid valve, and blower are controlled by automatic monitoring equipment, and the described automatic monitoring equipment includes at least a processor, a data acquisition module, a display module and a monitoring module, and the data acquisition module collects each The water level of the pool, the instantaneous flow value and cumulative flow value of the connecting pipes of each pool, the power consumption, the negative pressure value on the outlet pipe of the membrane pool, the data acquisition module will input the collected data into the computer processor, and complete the data comparison in the processor After the calculation and calculation, the MBR membrane tank, each electromagnetic valve and blower are monitored.

为了实现在线集中管理模式,在上述方案基础上,所述的自动监控设备带远程控制的系统接口,与农村生活污水治理综合监控中心和远程监控分中心联网,实现远程监控和农村整体污水的综合治理。可实现污水处理站无人值守,同时可实现政府相关部门等的在线监管,确保项目环境效益和社会效益目标得到切实的落实。 In order to realize the online centralized management mode, on the basis of the above scheme, the automatic monitoring equipment has a remote control system interface, and is connected with the rural domestic sewage treatment comprehensive monitoring center and the remote monitoring sub-center to realize remote monitoring and comprehensive integration of rural overall sewage. governance. Unattended sewage treatment stations can be realized, and online supervision by relevant government departments can be realized to ensure that the environmental and social benefit goals of the project are effectively implemented.

本实用新型提供一种上述装置的模块化MBR分散式农村生活污水集成处理方法,流程为:污水首先进入沉渣池,在沉渣池内去除污水中较大的颗粒物质及部分其它污染物,然后污水自动流入调节池,在调节池内对污水进行匀质匀量后,通过水泵提升后首先进入缺氧池,然后进入MBR膜池,在MBR膜池内通过鼓风曝气,一方面对膜组件进行冲刷以降低膜污染,同时对添加了除磷剂的混合液进行曝气,混合液通过气提回流至缺氧池,生化反应后出水经过膜分离后,通过自吸泵抽吸,出水至清水池或直接排放。 The utility model provides a modularized MBR decentralized rural domestic sewage integrated treatment method of the above-mentioned device. The process is as follows: firstly, the sewage enters the sediment pool, and larger particulate matter and some other pollutants in the sewage are removed in the sediment pool, and then the sewage is automatically It flows into the adjustment tank. After the sewage is homogenized and evenly distributed in the adjustment tank, it is lifted by the water pump and first enters the anoxic tank, and then enters the MBR membrane tank. In the MBR membrane tank, it is aerated by blasting. Reduce membrane fouling, and at the same time, aerate the mixed solution added with phosphorus removal agent, and the mixed solution is returned to the anoxic tank through air stripping. After the biochemical reaction, the effluent water is separated by the membrane and sucked by the self-priming pump, and the effluent is sent to the clean water tank or direct discharge.

本实用新型调节池进水、清水池指标主要指:COD、BOD、氨氮、总氮、总磷、SS、大肠杆菌。 The indicators of the water inlet and the clear water pool of the utility model mainly refer to: COD, BOD, ammonia nitrogen, total nitrogen, total phosphorus, SS, Escherichia coli.

本实用新型优越性在于: The utility model has the advantages of:

设备模块化、成套化。设备为模块化设计,可根据用户实际情况,对设备进行拼装组合,满足不同的处理要求;全套设备在工厂生产加工制作完成,质量可控,并有效缩短现场施工周期; Modularization and complete sets of equipment. The equipment is modular design, which can be assembled and combined according to the actual situation of the user to meet different processing requirements; the complete set of equipment is produced and processed in the factory, the quality is controllable, and the on-site construction period is effectively shortened;

一体式净化槽采用地埋式,对周边环境的臭气、噪音影响小; The integrated purification tank adopts the buried type, which has little impact on the odor and noise of the surrounding environment;

抗冲击符合能力强。对水量、水质波动具有良好的适应能力,通过系统设定的不同运行模式,可及时根据进水水质水量的波动情况,调整设备的运行模式,确保处理站的正常运行和稳定出水,同时大大节约运行能耗,降低运行费用。 Strong impact resistance. It has good adaptability to water volume and water quality fluctuations. Through the different operation modes set by the system, the operation mode of the equipment can be adjusted in time according to the fluctuation of influent water quality and water volume, so as to ensure the normal operation of the treatment station and stable water output, while greatly saving Operating energy consumption, reducing operating costs.

占地面积小。设备全地埋式,地面以上仅为控制室,不影响景观和绿化,占地面积小于1m2/吨水。 Small footprint. The equipment is fully buried, and the above ground is only the control room, which does not affect the landscape and greening, and the occupied area is less than 1m 2 /ton of water.

自动化程度高,运行维护简单。设备实现全自动化运行,处理站实现无人值守,正常情况下仅需每3个月现场设备保养一次;采用独特的抽屉式MBR膜,灵活轻便,非常便于安装和拆卸,污染后可集中专业化清洗。 High degree of automation, simple operation and maintenance. The equipment realizes fully automated operation, and the processing station is unattended. Under normal circumstances, the on-site equipment maintenance is only required every 3 months; the unique drawer-type MBR film is used, which is flexible and light, very easy to install and disassemble, and can be concentrated and specialized after pollution cleaning.

智能远程监控。通过数据采集与监控系统(SCADA),自动监视远距离无人操控的现场运行状态,并在中央管理室以及客户办公室通过互联网进行监管,对所有污水处理站进行集中运行管理,实现企业、政府和用户的实时在线监管。 Intelligent remote monitoring. Through the data acquisition and monitoring system (SCADA), the remote unmanned on-site operation status is automatically monitored, and the central management room and customer offices are supervised through the Internet, and all sewage treatment stations are centrally operated and managed to realize the realization of enterprises, governments and Real-time online monitoring of users.

附图说明 Description of drawings

附图1本实用新型结构框图; Accompanying drawing 1 structural block diagram of the utility model;

附图2本实用新型一体式净化槽俯视图; Accompanying drawing 2 is the top view of the integrated purification tank of the utility model;

附图3为图2的1-1剖视图; Accompanying drawing 3 is 1-1 sectional view of Fig. 2;

附图4为图2的2-2剖视图; Accompanying drawing 4 is 2-2 sectional view of Fig. 2;

附图5为图2的3-3剖视图; Accompanying drawing 5 is the 3-3 sectional view of Fig. 2;

附图6自动监控设备框图; Accompanying drawing 6 automatic monitoring equipment block diagrams;

附图7污水处理站自动化运行框图; Accompanying drawing 7 sewage treatment station automatic operation block diagram;

附图8本实用新型模块化MBR分散式农村生活污水集成处理方法流程图; Accompanying drawing 8 is the flowchart of the utility model modularized MBR decentralized rural domestic sewage integrated treatment method;

附图9农村污水治理综合监控系统构成框架图; Attached Figure 9 is a frame diagram of the comprehensive monitoring system for rural sewage treatment;

附图10具体实施例设备流程图; Accompanying drawing 10 specific embodiment equipment flowchart;

图中标号说明: Explanation of symbols in the figure:

1、1’——沉渣池;2、2’——调节池 1, 1' - sedimentation tank; 2, 2' - regulating tank

3、3’——一体式净化槽; 3, 3'——integrated purification tank;

31、31’——缺氧池;32、32’——MBR膜池; 31, 31' - anoxic pool; 32, 32' - MBR membrane pool;

33——加料部;34——隔板; 33—feeding part; 34—baffle;

35——过水孔; 35——water hole;

4、4’——清水池; 4, 4'—clear water pool;

5——加药管; 5—dosing tube;

6——鼓风机;61——鼓风机一;62——鼓风机二; 6——blower; 61——blower one; 62——blower two;

7——空气管;8——污泥管; 7—air pipe; 8—sludge pipe;

9——污水管。 9 - Sewage pipe.

具体实施方式 detailed description

实施例1 Example 1

如附图1本实用新型结构框图所示,本实用新型模块化MBR分散式农村生活污水集成处理装置,采用MBR膜生物反应器,包括沉渣池1、调节池2、设置MBR膜生物反应器的MBR膜池32、缺氧池31和清水池4,其中:所述的处理装置将设有MBR膜生物反应器的MBR膜池32与缺氧池31采用一体式净化槽3的结构,依序包括沉渣池1、调节池2、一体式净化槽3和清水池4,各池水位由浮球液位器和电磁阀控制,污水进入沉渣池1,经沉渣池1沉淀后的污水自流进入调节池2,在调节池2内匀质、匀量后,泵入一体式净化槽3的缺氧池31、然后进入MBR膜池32,所述的MBR膜池32与鼓风机连通作为曝气池,在MBR膜池32设置投放除磷剂的加料口,经加药管5与加料部33连通,鼓风机6经空气管7对MBR膜池32内的污水进行鼓风曝气并对MBR膜生物反应器的膜组件进行冲刷;曝气后的混合液通过气提管抽提回流至缺氧池31,生化反应出水经过膜分离后由自吸泵泵入清水池4,污泥经气提排泥的污泥管8到沉渣池1。 As shown in the structural block diagram of the utility model in accompanying drawing 1, the utility model modular MBR decentralized rural domestic sewage integrated treatment device adopts an MBR membrane bioreactor, including a sedimentation tank 1, a regulating tank 2, and an MBR membrane bioreactor. MBR membrane pond 32, anoxic pond 31 and clear water pond 4, wherein: described treatment device will be provided with the MBR membrane pond 32 of MBR membrane bioreactor and the anoxic pond 31 adopts the structure of integrated purification tank 3, sequentially Including sedimentation tank 1, regulating tank 2, integrated purification tank 3 and clear water tank 4, the water level of each tank is controlled by float level device and solenoid valve, the sewage enters the sedimentation tank 1, and the sewage after sedimentation in the sedimentation tank 1 flows into the regulating tank by itself Pond 2, after regulating homogeneous, uniform quantity in pond 2, pump into the anoxic pool 31 of integrated purification tank 3, then enter MBR membrane pool 32, described MBR membrane pool 32 is communicated with air blower as aeration tank, The MBR membrane pool 32 is provided with a feeding port for putting in phosphorus removal agent, which is communicated with the feeding part 33 through the dosing pipe 5, and the blower 6 blows and aerates the sewage in the MBR membrane pool 32 through the air pipe 7 and has a biological reaction on the MBR membrane. The membrane module of the device is washed; the mixed liquid after aeration is extracted and returned to the anoxic pool 31 through the air stripping tube, the biochemical reaction effluent is pumped into the clear water pool 4 by the self-priming pump after being separated by the membrane, and the sludge is discharged through the air lift The sludge pipe 8 to the sediment tank 1.

如附图2本实用新型一体式净化槽安装示意图、附图3为图2的1-1剖视图、附图4为图2的2-2剖视图和附图5为图2的3-3剖视图所示,所述的一体式净化槽采用地埋式结构,缺氧池31和MBR膜池32之间设有隔板34和过水孔35,在缺氧池设有进水管;MBR膜池32设置膜池出水管,MBR膜池32与污泥管8、空气管7连通。设备处理规格针对典型农村污水水量特点,分别为:5m3/d,10m3/d,15m3/d,···100m3/d等,实现产品系列化,其中: As shown in accompanying drawing 2, the installation diagram of the integrated purification tank of the utility model, accompanying drawing 3 is a sectional view of 1-1 of FIG. 2 , accompanying drawing 4 is a sectional view of 2-2 of FIG. As shown, the integrated purification tank adopts a buried structure, and a partition plate 34 and a water hole 35 are arranged between the anoxic pool 31 and the MBR membrane pool 32, and a water inlet pipe is provided in the anoxic pool; the MBR membrane pool 32 The outlet pipe of the membrane pool is set, and the MBR membrane pool 32 communicates with the sludge pipe 8 and the air pipe 7 . The equipment treatment specifications are aimed at the characteristics of typical rural sewage water volume, which are: 5m 3 /d, 10m 3 /d, 15m 3 /d, 100m 3 /d, etc., to achieve product serialization, of which:

MBR膜池溶解氧控制在2~4mg/L; The dissolved oxygen in the MBR membrane pool is controlled at 2-4mg/L;

缺氧池溶解氧控制在0.5mg/L以下; The dissolved oxygen in the anoxic pool is controlled below 0.5mg/L;

曝气池污泥浓度:3000mg/L~6000mg/L; Aeration tank sludge concentration: 3000mg/L~6000mg/L;

所述的自吸泵运行方式为开、停间歇运行方式。 The operation mode of the self-priming pump is an intermittent operation mode of on and off.

在MBR膜池32内,二个人孔用于设置膜导轨框架,用于固定膜组件。 In the MBR membrane tank 32, two manholes are used to set the membrane rail frame for fixing the membrane modules.

在所述的一体式净化槽中设置管网系统,包括: A pipe network system is set in the integrated septic tank, including:

MBR膜池内由伸入膜池污泥管内的空气管,经法兰与罐外部的连通风机的剩余污泥空气管连接,构成剩余污泥空气管系统; In the MBR membrane tank, the air pipe extending into the sludge pipe of the membrane tank is connected to the remaining sludge air pipe connected to the fan outside the tank through the flange to form the remaining sludge air pipe system;

MBR膜池污泥管连至沉渣池构成剩余污泥排泥系统; The sludge pipe in the MBR membrane tank is connected to the sediment tank to form the excess sludge discharge system;

伸入膜池内的回流管,罐体外部自风机到罐体的回流管构成内回流空气管系统; The return pipe extending into the membrane tank, and the return pipe from the fan to the tank outside the tank constitute the internal return air pipe system;

自MBR膜池32至缺氧池31设有内回流水管系统。 From the MBR membrane tank 32 to the anoxic tank 31, an internal return water pipe system is provided.

如附图6自动监控设备框图所示,各池的液位、电磁阀、鼓风机、自吸泵由现场PLC站控制,农村污水治理综合监控中心包括显示屏、工程管理器、WEB服务器、数据服务器,通信服务器手机用户可通过通信服务器收到短信或直接查询信息,各服务器通过路由器将各现场PLC站+GPRS通讯控制器+防盗设备的信息和工程师管理器操作指挥信息传递给用户、政府管理部门、运营企业等终端客户,数据采集模块采集各池的水位、各池连接管道间的瞬时流量值和累计流量值、耗电量、膜池出水管路上的负压值、调节池和清水池中的指标值。本实用新型实施例采用PLC控制系统,各设备运行信号及故障信号送至PLC系统,设备发生故障时报警并启动备用设备,在处理器中完成数据比较和计算后,经工程师管理器经路由器与各现场PLC站采用CDMA和/或GPRS通讯。 As shown in the block diagram of the automatic monitoring equipment in Figure 6, the liquid level, solenoid valve, blower, and self-priming pump of each pool are controlled by the on-site PLC station, and the comprehensive monitoring center for rural sewage treatment includes a display screen, a project manager, a WEB server, and a data server , communication server mobile phone users can receive text messages or directly query information through the communication server, and each server transmits the information of each on-site PLC station + GPRS communication controller + anti-theft equipment and the operation command information of the engineer manager to the user and the government management department through the router , operation enterprises and other end customers, the data acquisition module collects the water level of each pool, the instantaneous flow value and cumulative flow value between the connecting pipes of each pool, power consumption, the negative pressure value on the outlet pipe of the membrane pool, the water level in the regulating pool and the clear water pool index value. The embodiment of the utility model adopts the PLC control system, and the operation signals and fault signals of each equipment are sent to the PLC system. When the equipment fails, it will alarm and start the backup equipment. After the data comparison and calculation are completed in the processor, the engineer manager passes through the router and Each on-site PLC station adopts CDMA and/or GPRS communication.

如附图7污水处理站自动化运行框图所示,所述的自动监控设备带远程控制的系统接口,与农村生活污水治理综合监控中心和远程监控分中心联网。在系统中应用依据图7所示的逻辑框图实现数据采集和污水处理站自动化运行。MBR膜池液位、调节池液位和集水井(可选)液位,根据各池的液位信息实现对相应设备的监控,实现在线集中管理,一方面可实现污水处理站无人值守,同时可实现政府相关部门等的在线监管,确保项目环境效益和社会效益目标得到切实的落实。 As shown in the automatic operation block diagram of the sewage treatment station in Figure 7, the automatic monitoring equipment has a remote control system interface and is connected to the integrated monitoring center for rural domestic sewage treatment and the remote monitoring sub-center. In the system, the logic block diagram shown in Figure 7 is used to realize data collection and automatic operation of sewage treatment stations. The liquid level of the MBR membrane pool, the liquid level of the regulating pool and the liquid level of the water collection well (optional) are realized according to the liquid level information of each pool to monitor the corresponding equipment and realize online centralized management. On the one hand, the sewage treatment station can be unattended, At the same time, online supervision by relevant government departments can be realized to ensure that the environmental and social benefits of the project are effectively implemented.

附图8为本实用新型模块化MBR分散式农村生活污水集成处理方法流程图:污水首先进入沉渣池1,在沉渣池1内去除污水中较大的颗粒物质及部分其它污染物,然后污水自动流入调节池2,在调节池2内进行匀质匀量后,通过水泵提升后首先进入一体式净化槽3中的缺氧池,然后进入MBR膜池,在MBR膜池内通过鼓风曝气,一方面对膜组件进行冲刷以降低膜污染,同时对添加了除磷剂的混合液进行曝气,混合液通过气提回流至缺氧池,生化反应后出水,经过膜分离后通过自吸泵抽吸,出水至清水池4或直接排放。污泥经气提排泥管到沉渣池,沉渣池污泥定期用粪车抽吸外运。 Accompanying drawing 8 is the flow chart of the utility model modularized MBR decentralized rural domestic sewage integrated treatment method: the sewage first enters the sedimentation tank 1, removes larger particulate matter and some other pollutants in the sewage in the sedimentation tank 1, and then the sewage is automatically It flows into the regulating tank 2, and after being homogenized in the regulating tank 2, it is lifted by a water pump and first enters the anoxic tank in the integrated purification tank 3, and then enters the MBR membrane tank, where it is aerated by blasting. On the one hand, the membrane module is flushed to reduce membrane fouling, and at the same time, the mixed solution added with phosphorus removal agent is aerated, and the mixed solution is returned to the anoxic tank through air lift. After the biochemical reaction, the water is discharged, and after membrane separation, it passes through the self-priming pump. Suction, the water is discharged to the clear water pool 4 or directly discharged. The sludge is sent to the sedimentation tank through the air lift sludge discharge pipe, and the sludge in the sedimentation tank is regularly sucked and transported by a dung truck.

如图9为农村污水治理综合监控系统构成框架图所示。系针对农村生活处理站的运行管理要求开发设计的集中在线管理系统,具体功能包括:站点分布查询、实时系统监视、报警管理、数据查询、运营报表查询和权限管理等。通过这一在线管理系统,可以通过系统导航栏进行站点快速定位和站点基本信息的查询;通过实时数据一览表可展示所有站点的实时数据;通过实时和历史报警一览表可以实现实时和历史故障查询;通过数据查询可实现对日运行数据、月运行数据和年运行数据的查询;通过运营报表可以实现对设备维护记录、污水水质检测记录、污泥处置记录、药剂管理记录4种报表的查询;权限管理可对系统终端管理人员、现场运行管理人员、各级监管部门、污水处理站建设方授予不同的权限。 Figure 9 is a frame diagram of the comprehensive monitoring system for rural sewage treatment. It is a centralized online management system developed and designed for the operation and management requirements of rural life processing stations. Its specific functions include: site distribution query, real-time system monitoring, alarm management, data query, operation report query and authority management, etc. Through this online management system, you can quickly locate the site and query the basic information of the site through the system navigation bar; display the real-time data of all sites through the real-time data list; realize real-time and historical fault query through the real-time and historical alarm list; Data query can realize the query of daily operation data, monthly operation data and annual operation data; through the operation report, it can realize the query of four types of reports: equipment maintenance records, sewage water quality inspection records, sludge disposal records, and chemical management records; authority management Different authority can be granted to system terminal management personnel, on-site operation management personnel, supervision departments at all levels, and construction parties of sewage treatment stations.

本实用新型对调节池进水和清水池进行水质指标采集,各项指标分别指:COD、BOD、氨氮、总氮、总磷、SS、大肠杆菌。 The utility model collects the water quality indexes of the inlet water of the regulating pool and the clear water pool, and each index respectively refers to: COD, BOD, ammonia nitrogen, total nitrogen, total phosphorus, SS, Escherichia coli.

实施例2 Example 2

附图10为具体实施例设备流程图,日处理量为25m3/d,关键设备及设备参数为: Accompanying drawing 10 is the flow chart of the equipment of the specific embodiment, the daily processing capacity is 25m 3 /d, and the key equipment and equipment parameters are:

一体式净化槽Φ2000×(2800+400×2)地埋式; Integrated purification tank Φ2000×(2800+400×2) buried type;

调节池提升泵2台Q=8.0m3/h,H=7m,N=0.18kW,1用1备; Adjusting pool lift pump 2 sets Q=8.0m 3 /h, H=7m, N=0.18kW, 1 for use and 1 for standby;

膜池自吸泵2台Q=1.5m3/h,H=20m,N=0.37kW,1用1备; Membrane tank self-priming pump 2 sets Q=1.5m 3 /h, H=20m, N=0.37kW, 1 for use and 1 for standby;

鼓风机2台Q=0.225m3/min,转数=430rpm,N=0.37kW,鼓风机一61和鼓风机二62中一用一备; 2 sets of blowers Q=0.225m 3 /min, speed=430rpm, N=0.37kW, blower 1 61 and blower 2 62, one for use and one for standby;

膜组件1组ECONITYCF–C22S,膜框605W×784L×1,120H; Membrane module 1 group ECONITYCF–C22S, membrane frame 605W×784L×1,120H;

污水自De300进水管进入沉渣池1’,在沉渣池1’内去除污水中较大的颗粒物质及部分其它污染物,然后污水自流入调节池2’,在调节池2’内对污水进行匀质匀量后,通过水泵提升经De32管路首先进入一体式净化槽3中的缺氧池31’,然后进入MBR膜池32’,在MBR膜池32’内通过鼓风曝气,一方面对膜组件进行冲刷以降低膜污染,同时对添加了除磷剂的混合液进行曝气,混合液通过气提经De50内回流管回流至缺氧池31’,生化反应后出水,出水经过膜分离后通过自吸泵抽吸至清水井4’。同时,MBR膜池32’内的污泥经De50剩余淤泥管排到沉渣池1’。 The sewage enters the sedimentation tank 1' from the De300 inlet pipe, removes larger particulate matter and some other pollutants in the sewage in the sedimentation tank 1', and then the sewage flows into the adjustment tank 2', where the sewage is homogenized After the quality is uniform, it is lifted by the water pump and first enters the anoxic pool 31' in the integrated purification tank 3 through the De32 pipeline, and then enters the MBR membrane pool 32', and is aerated by blast in the MBR membrane pool 32'. Flush the membrane module to reduce membrane fouling, and at the same time, aerate the mixed solution added with phosphorus removal agent, and the mixed solution is returned to the anoxic pool 31' through the De50 internal return pipe through air lift, and the water is discharged after the biochemical reaction, and the discharged water passes through the membrane After separation, it is sucked to the clean water well 4' by a self-priming pump. At the same time, the sludge in the MBR membrane tank 32' is discharged to the sediment tank 1' through the De50 residual sludge pipe.

根据不同处理出水水质的要求,系统可在MBR膜池投加除磷剂,结合膜组件的特点,将化学除磷与膜分离原理进行优化组合,不但可强化除磷效果,而且与传统的化学除磷相比较,可大大降低化学药剂的投加量,减少运行费用和污泥产量。 According to the requirements of different treatment effluent quality, the system can add dephosphorization agent in the MBR membrane tank, combine the characteristics of membrane modules, and optimize the combination of chemical dephosphorization and membrane separation principle, which can not only strengthen the dephosphorization effect, but also be different from traditional chemical dephosphorization. Compared with phosphorus, it can greatly reduce the dosage of chemical agents, reduce operating costs and sludge production.

采用本实施例设计方案,出水能稳定达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级以上的排放要求。 By adopting the design scheme of this embodiment, the effluent can stably meet the discharge requirements above Class I of the Discharge Standard of Pollutants for Urban Sewage Treatment Plants (GB18918-2002).

技术特点及创新点: Technical features and innovations:

1、采用模块化MBR农村生活污水处理装置采用一体化净化槽,设备整体工厂生产,无渗漏,便于安装,施工周期短,出水能稳定达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级以上的排放要求; 1. The modular MBR rural domestic sewage treatment device adopts an integrated purification tank, and the equipment is produced in a factory as a whole, without leakage, easy to install, short construction period, and the effluent can stably meet the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB18918- 2002) emission requirements above level one;

2、污水处理系统具有高效稳定的脱氮除磷效果,根据排放水体要求,能够稳定达到GB18918-2002一级以上的排放要求; 2. The sewage treatment system has efficient and stable denitrification and phosphorus removal effects, and can stably meet the discharge requirements of GB18918-2002 Class I or above according to the requirements of the discharged water body;

3、系统具有很高的污染物去除率,CODcr去除率≥90%;氨氮去除率≥88%;总磷去除率≥90%;TN去除率为≥65%;SS去除率接近100%。 3. The system has a high pollutant removal rate, CODcr removal rate ≥ 90%; ammonia nitrogen removal rate ≥ 88%; total phosphorus removal rate ≥ 90%; TN removal rate ≥ 65%; SS removal rate close to 100%.

4、系统可全自动化运行,通过网络在线集中管理,污水处理站无人值守,正常情况下,日常维护周期在3个月以上; 4. The system can be fully automated, managed online and centralized through the network, and the sewage treatment station is unattended. Under normal circumstances, the daily maintenance cycle is more than 3 months;

5、系统造价在0.4万元/户以内,用地省,占地面积小于1m2/m3水,根据处理规模和处理要求的不同,吨水运行费用在0.5元~0.7元。与常规有动力处理工艺相比,在造价和运行费用方面具有明显优势; 5. The cost of the system is within 40,000 yuan/household, and the land is saved. The area is less than 1m 2 /m 3 water. According to the different treatment scale and treatment requirements, the operating cost per ton of water is 0.5 to 0.7 yuan. Compared with the conventional dynamic treatment process, it has obvious advantages in terms of construction cost and operating cost;

6、能耗低:单位污水处理费用(电费)0.56元/吨水; 6. Low energy consumption: the unit sewage treatment cost (electricity charge) is 0.56 yuan/ton of water;

7、药耗少:平均每吨污水花费除磷剂费用为0.01元/吨水; 7. Low chemical consumption: the average cost of phosphorus removal agent per ton of sewage is 0.01 yuan/ton of water;

8、系统泥龄长,产泥率低,剩余污泥产泥量少,平均年绝干污泥产量在0.3吨以内。在污泥去向上,可与区域内其它污水处理站统一收集处理,进行污泥堆肥后利用,或者运送至附近污水处理厂。 8. The sludge age of the system is long, the sludge production rate is low, the residual sludge production is small, and the average annual absolute dry sludge production is within 0.3 tons. In terms of sludge removal, it can be collected and treated with other sewage treatment stations in the area, and used after composting sludge, or transported to nearby sewage treatment plants.

检测结果见下表: The test results are shown in the table below:

其中:进水取自调节池;出水取自清水井。 Among them: the influent water is taken from the regulating pool; the effluent water is taken from the clear water well.

Claims (7)

1. modularization MBR distributing domestic sewage in rural areas integrated treating device, adopt MBR membrane bioreactor, at least comprise detritus pool, equalizing tank, the MBR membrane cisterna of MBR membrane bioreactor is set, anaerobic pond and clean water basin, it is characterized in that: MBR membrane bioreactor and anoxic pond are adopted the structure of integral type purification tank by described treatment unit, sequentially comprise detritus pool, equalizing tank, integral type purification tank and clean water basin, connected by pipeline between each pond, each pool water level is by Floating Ball Liquid Level device and solenoid control, sewage enters detritus pool, equalizing tank is entered through the gravity flow of detritus pool oettIed sewage, homogeneous in equalizing tank, after even amount, pump into the anoxic pond of integral type purification tank, then MBR membrane cisterna is entered, described MBR membrane cisterna is communicated with as aeration tank with gas blower, the charging opening throwing in dephosphorization agent is set at MBR membrane cisterna, gas blower carries out blast aeration to the sewage in MBR membrane cisterna and washes away to reduce fouling membrane to the membrane module of MBR membrane bioreactor, mixed solution after aeration is back to anoxic pond by stripping tube extracting, and biochemical reaction water outlet pumps into clean water basin by vacuum primingpump after membrane sepn, mud through excess sludge shore pipe to detritus pool.
2. modularization MBR distributing domestic sewage in rural areas integrated treating device according to claim 1, is characterized in that: described integral type purification tank adopts buried structure, wherein,
MBR membrane cisterna dissolved oxygen controls at 2 ~ 4mg/L;
Dissolved oxygen in anoxic tank controls at below 0.5mg/L;
Aeration tank sludge concentration: 3000mg/L ~ 6000mg/L;
Described vacuum primingpump operation scheme is for opening, stopping intermittent operation mode.
3. modularization MBR distributing domestic sewage in rural areas integrated treating device according to claim 1 and 2, it is characterized in that: described integral type purification tank by tank body as shell, anoxic pond is established in side, opposite side establishes MBR membrane cisterna, between described anoxic pond and MBR membrane cisterna, be provided with dividing plate and water hole, be provided with water inlet pipe in anoxic pond; MBR membrane cisterna is provided with membrane cisterna rising pipe, with sludge pipe, air line.
4. modularization MBR distributing domestic sewage in rural areas integrated treating device according to claim 3, is characterized in that: in described integral type purification tank, the cell body of MBR membrane cisterna is provided with manhole, for arranging the film guide rail frame of fixing membrane module.
5. modularization MBR distributing domestic sewage in rural areas integrated treating device according to claim 3, is characterized in that, arrange pipe network system, comprising in described integral type purification tank:
By the blast main stretched in membrane cisterna sludge pipe in MBR membrane cisterna, be connected through the excess sludge blast main of flange with the connection blower fan of tank body outside, form excess sludge air tube system;
MBR membrane cisterna sludge pipe is connected to detritus pool and forms excess sludge sludge drainage system;
Stretch into the return line in MBR membrane cisterna, tank body is outside forms internal reflux air tube system from blower fan to the return line of tank body;
Internal reflux water pipe system is provided with from MBR membrane cisterna to anoxic pond.
6. modularization MBR distributing domestic sewage in rural areas integrated treating device according to claim 1 and 2, it is characterized in that: the MBR membrane cisterna described in automatic monitoring equipment controls, each magnetic valve, gas blower, this automatic monitoring equipment at least comprises treater, data acquisition module, display module and monitoring module, the water level in each pond of data collecting module collected, the instantaneous delivery value of each pond connecting tube and integrated flow value, current consumption, negative pressure value on MBR membrane cisterna outlet pipeline, the data input reason device that data acquisition module will gather, complete after data compare and calculate within a processor, to described MBR membrane cisterna and each magnetic valve, gas blower is monitored.
7. modularization MBR distributing domestic sewage in rural areas integrated treating device according to claim 6, it is characterized in that: the system interface of described automatic monitoring equipment band Long-distance Control, administer comprehensively monitoring center and remote monitoring branch center with domestic sewage in rural areas and network.
CN201520542126.1U 2015-07-24 2015-07-24 Distributed rural domestic sewage integrated process device of modularization MBR Expired - Fee Related CN205115214U (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105884146A (en) * 2016-06-24 2016-08-24 湖南易净环保科技有限公司 Rural distributed wastewater treatment system
CN107285554A (en) * 2017-06-05 2017-10-24 浙江水利水电学院 A kind of decentralized sewage treatment method
CN107879445A (en) * 2017-12-19 2018-04-06 江苏力鼎环保工程有限公司 A kind of water treatment system for villages and small towns dispersion type domestic wastewater
CN109534593A (en) * 2018-10-26 2019-03-29 深圳市水务规划设计院股份有限公司 A kind of multi-stage aerobic reinforced phosphor-removing APO-M system and technique
CN110028200A (en) * 2019-04-24 2019-07-19 东南大学 A kind of small-sized purification tank mixed liquor regurgitant volume self-checking device and adjusting method
CN111196666A (en) * 2020-01-22 2020-05-26 上海环科淙达水务有限公司 Modularized MBR domestic sewage integrated treatment device and method with improved dosing position
CN111196667A (en) * 2020-01-22 2020-05-26 上海环科淙达水务有限公司 Modularized MBR sewage treatment method based on ecological pool technology
CN113415955A (en) * 2021-07-27 2021-09-21 南京苏城环保科技有限公司 Method for treating sulfur-containing hot spring bath sewage

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105884146A (en) * 2016-06-24 2016-08-24 湖南易净环保科技有限公司 Rural distributed wastewater treatment system
CN105884146B (en) * 2016-06-24 2018-07-24 湖南易净环保科技有限公司 A kind of rural area decentralized type sewage processing system
CN107285554A (en) * 2017-06-05 2017-10-24 浙江水利水电学院 A kind of decentralized sewage treatment method
CN107285554B (en) * 2017-06-05 2020-07-07 浙江水利水电学院 A kind of decentralized sewage treatment method
CN107879445A (en) * 2017-12-19 2018-04-06 江苏力鼎环保工程有限公司 A kind of water treatment system for villages and small towns dispersion type domestic wastewater
CN109534593A (en) * 2018-10-26 2019-03-29 深圳市水务规划设计院股份有限公司 A kind of multi-stage aerobic reinforced phosphor-removing APO-M system and technique
CN110028200A (en) * 2019-04-24 2019-07-19 东南大学 A kind of small-sized purification tank mixed liquor regurgitant volume self-checking device and adjusting method
CN110028200B (en) * 2019-04-24 2021-08-24 东南大学 A kind of small purification tank mixed liquid return flow automatic adjustment device and adjustment method
CN111196666A (en) * 2020-01-22 2020-05-26 上海环科淙达水务有限公司 Modularized MBR domestic sewage integrated treatment device and method with improved dosing position
CN111196667A (en) * 2020-01-22 2020-05-26 上海环科淙达水务有限公司 Modularized MBR sewage treatment method based on ecological pool technology
CN113415955A (en) * 2021-07-27 2021-09-21 南京苏城环保科技有限公司 Method for treating sulfur-containing hot spring bath sewage

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