CN209940765U - A sewage treatment system with COD detection - Google Patents

A sewage treatment system with COD detection Download PDF

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CN209940765U
CN209940765U CN201920520798.0U CN201920520798U CN209940765U CN 209940765 U CN209940765 U CN 209940765U CN 201920520798 U CN201920520798 U CN 201920520798U CN 209940765 U CN209940765 U CN 209940765U
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outlet
sludge
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郑英
叶小斌
张益凡
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Jiangxi Wattech Environmental Protection Technology Co ltd
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Jiangxi Book Source Technology Co Ltd
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Abstract

本实用新型公开了一种带COD检测的污水处理系统,包括管道依次连接的集水池、第一pH调节池、絮凝反应池、第一沉淀池、纤维球过滤器、厌氧池、兼氧池、好氧池、第二沉淀池、MBR膜过滤池、消毒池和回用水池,集水池与第一pH调节池之间设有油水分离池,油水分离池的上部设有斜网,油水分离池的上部一侧设有排油管,油水分离池的进口侧设有对应斜网出口的收集池,好氧池的出口管路上设有COD检测仪,好氧池的出口管路经过COD检测仪后分为两路,一路与第二沉淀池连接,另一路通过回流管道、回流阀及回流泵回流至厌氧池。本实用新型可以有效减少无效污泥的带入,减轻后续污染处理的负荷;可防止COD指数不达标外排,减少了水体的二次污染。

The utility model discloses a sewage treatment system with COD detection, which comprises a water collecting tank, a first pH adjusting tank, a flocculation reaction tank, a first sedimentation tank, a fiber ball filter, an anaerobic tank and a facultative oxygen tank which are connected in sequence by pipelines , aerobic tank, second sedimentation tank, MBR membrane filter tank, disinfection tank and reuse tank, an oil-water separation tank is arranged between the collection tank and the first pH adjustment tank, the upper part of the oil-water separation tank is provided with an inclined net, and the oil-water separation tank There is an oil discharge pipe on the upper side of the oil-water separation tank, a collection tank corresponding to the outlet of the inclined net is installed on the inlet side of the oil-water separation tank, a COD detector is installed on the outlet pipeline of the aerobic tank, and the outlet pipeline of the aerobic tank passes through the COD detector. It is divided into two paths, one is connected to the second sedimentation tank, and the other is returned to the anaerobic tank through the return pipeline, the return valve and the return pump. The utility model can effectively reduce the introduction of invalid sludge, reduce the load of subsequent pollution treatment; can prevent the COD index from being discharged outside the standard, and reduce the secondary pollution of the water body.

Description

一种带COD检测的污水处理系统A sewage treatment system with COD detection

技术领域technical field

本实用新型涉及污水处理技术领域,具体是一种带COD检测的污水处理系统。The utility model relates to the technical field of sewage treatment, in particular to a sewage treatment system with COD detection.

背景技术Background technique

污水,通常指受一定污染的、来自生活和生产的排出水。污水主要有生活污水、工业污水和初期雨水。污水的主要污染物有病原体污染物、耗氧污染物、植物营养物和有毒污染物等。污水处理: 为使污水达到排水某一水体或再次使用的水质要求对其进行净化的过程。污水处理被广泛应用于建筑、农业,交通、能源、石化、环保、城市景观、医疗、餐饮等各个领域,也越来越多地走进寻常百姓的日常生活。Sewage, usually refers to the effluent from living and production that is polluted to a certain extent. The sewage mainly includes domestic sewage, industrial sewage and initial rainwater. The main pollutants in sewage are pathogen pollutants, oxygen-consuming pollutants, plant nutrients and toxic pollutants. Sewage treatment: The process of purifying sewage in order to make it meet the quality requirements of a water body for drainage or reuse. Sewage treatment is widely used in construction, agriculture, transportation, energy, petrochemical, environmental protection, urban landscape, medical treatment, catering and other fields, and is increasingly entering the daily life of ordinary people.

对于目前的污水处理来说,存在如下问题:1、处理污水的效率较低,并且处理效果不够理想,2、经处理后排放的污水存在COD不达标就外排的情况,3、在处理过程中,压滤机产生的废水容易导致二次污染,从而对环境造成了较大的污染,也更无法实现对工业用水的循环再利用,因此,为了提高处理效果及对现有技术进一步改进,实现处理后的污水的再利用,需要设计出一种带COD检测的污水处理系统。For the current sewage treatment, there are the following problems: 1. The efficiency of sewage treatment is low, and the treatment effect is not ideal; 2. The COD discharged after treatment does not meet the standard and is discharged outside; 3. During the treatment process The waste water produced by the filter press is easy to cause secondary pollution, which causes greater pollution to the environment and makes it impossible to realize the recycling and reuse of industrial water. Therefore, in order to improve the treatment effect and further improve the existing technology, To realize the reuse of treated sewage, it is necessary to design a sewage treatment system with COD detection.

实用新型内容Utility model content

本实用新型所解决的技术问题在于提供一种带COD检测的污水处理系统,以解决上述背景技术中的缺点。The technical problem solved by the present invention is to provide a sewage treatment system with COD detection, so as to solve the shortcomings of the above-mentioned background technology.

本实用新型所解决的技术问题采用以下技术方案来实现:The technical problem solved by the utility model adopts the following technical solutions to realize:

一种带COD检测的污水处理系统,包括集水池、第一pH调节池、絮凝反应池、第一沉淀池、纤维球过滤器、厌氧池、兼氧池、好氧池、第二沉淀池 、MBR膜过滤池、消毒池和回用水池,集水池与第一pH调节池之间设有油水分离池,油水分离池的上部设有斜网,油水分离池的上部一侧设有排油管,油水分离池的进口侧设有对应斜网出口的收集池,油水分离池的出口通过泵与第一pH调节池进口连接,油水分离池与第一pH调节池连接的管道上设有第一加药混合器,第一pH调节池的出口与絮凝反应池的进口连接,第一pH调节池与絮凝反应池连接的管道上设有第二加药混合器,絮凝反应池的出口与第一沉淀池的进口连接,第一沉淀池的出口经进液泵及进液阀与纤维球过滤器的进水口连接,纤维球过滤器的出水口经排液阀与厌氧池的进口连接,厌氧池的出口与兼氧池的进口连接,兼氧池的出口与好氧池,好氧池内设有曝气管,曝气管道与鼓风机连接,好氧池的出口与第二沉淀池进口连接,第二沉淀池的出口与MBR膜过滤池的进口连接,MBR膜过滤池内设有平板膜过滤器,MBR膜过滤池的出口经消毒池与回用水池连接,消毒池内设有紫外线杀菌灯,所述好氧池的出口管路上设有COD检测仪,好氧池的出口管路经过COD检测仪后分为两路,一路与第二沉淀池连接,另一路通过回流管道、回流阀及回流泵回流至厌氧池。A sewage treatment system with COD detection, comprising a collection tank, a first pH adjustment tank, a flocculation reaction tank, a first sedimentation tank, a fiber ball filter, an anaerobic tank, a facultative aerobic tank, an aerobic tank, and a second sedimentation tank , MBR membrane filter tank, disinfection tank and reuse tank, an oil-water separation tank is arranged between the collecting tank and the first pH adjustment tank, the upper part of the oil-water separation tank is provided with an inclined mesh, and the upper side of the oil-water separation tank is provided with an oil drain pipe. The inlet side of the oil-water separation tank is provided with a collection tank corresponding to the outlet of the inclined mesh. The outlet of the oil-water separation tank is connected to the inlet of the first pH adjustment tank through a pump. A chemical mixer, the outlet of the first pH adjustment tank is connected with the inlet of the flocculation reaction tank, the pipeline connecting the first pH adjustment tank and the flocculation reaction tank is provided with a second drug addition mixer, and the outlet of the flocculation reaction tank is connected with the first sedimentation tank The inlet of the tank is connected, the outlet of the first sedimentation tank is connected with the water inlet of the fiber ball filter through the liquid inlet pump and the liquid inlet valve, and the water outlet of the fiber ball filter is connected with the inlet of the anaerobic tank through the drain valve. The outlet of the pool is connected with the inlet of the facultative oxygen pool, the outlet of the facultative oxygen pool is connected with the aerobic pool, the aeration pipe is arranged in the aerobic pool, the aeration pipe is connected with the blower, the outlet of the aerobic pool is connected with the inlet of the second sedimentation tank, The outlet of the second sedimentation tank is connected to the inlet of the MBR membrane filter tank. The MBR membrane filter tank is equipped with a flat membrane filter. The outlet of the MBR membrane filter tank is connected to the reuse tank through the disinfection tank. The disinfection tank is equipped with ultraviolet germicidal lamps. The outlet pipeline of the aerobic tank is provided with a COD detector. The outlet pipeline of the aerobic tank is divided into two channels after passing through the COD detector. back to the anaerobic tank.

进一步,还包括污泥处理系统,污泥处理系统包括压滤机、污泥池、污泥泵和污泥总管,第一pH调节池的排污口、絮凝反应池的排污口、第一沉淀池的排污口、第二沉淀池的排污口以及MBR膜过滤池的排污口分别通过污泥支管及排污阀与污泥总管连接,污泥总管的出口经污泥泵与污泥池的入口连接,污泥池的出口经泵泵送至压滤机。Further, it also includes a sludge treatment system. The sludge treatment system includes a filter press, a sludge tank, a sludge pump and a sludge main pipe, the sewage outlet of the first pH adjustment tank, the sewage outlet of the flocculation reaction tank, and the first sedimentation tank. The sewage outlet of the second sedimentation tank and the sewage outlet of the MBR membrane filter tank are respectively connected with the sludge main pipe through the sludge branch pipe and the sewage valve, and the outlet of the sludge main pipe is connected with the inlet of the sludge tank through the sludge pump. The outlet of the sludge tank is pumped to the filter press by the pump.

进一步,压滤机的滤液出口经管道与污泥池的入口连接。Further, the filtrate outlet of the filter press is connected to the inlet of the sludge tank through a pipeline.

进一步,污泥池的上清液通过管道与集水池连接。Further, the supernatant of the sludge tank is connected to the sump through a pipeline.

本实用新型有益效果在于:The beneficial effects of the utility model are:

1、通过设置斜网可起到初步拦截的作用,减少无效污泥的带入,1. By setting the inclined net, it can play the role of preliminary interception and reduce the introduction of invalid sludge.

2、通过设置油水分离池可将油污排除,减轻后续污染处理的负荷;2. By setting the oil-water separation tank, the oil pollution can be removed and the load of subsequent pollution treatment can be reduced;

3、在好氧池的出口管路上设置了COD检测仪及回流管道,可防止COD指数不达标外排,3. A COD detector and a return pipeline are set on the outlet pipeline of the aerobic tank to prevent the COD index from being discharged outside the standard.

4、第一pH调节池、絮凝反应池、第一沉淀池、第二沉淀池以及MBR膜过滤池的污泥经压滤机压滤后,滤液返回污泥池,污泥池的上清液通过管道返回集水池,滤饼外运,减少了水体的二次污染。4. After the sludge in the first pH adjustment tank, the flocculation reaction tank, the first sedimentation tank, the second sedimentation tank and the MBR membrane filter tank is filtered by the filter press, the filtrate is returned to the sludge tank, and the supernatant of the sludge tank The filter cake is returned to the sump through the pipeline, and the filter cake is transported out, which reduces the secondary pollution of the water body.

附图说明Description of drawings

图1是本实用新型较佳实施例的结构示意图;Fig. 1 is the structural representation of the preferred embodiment of the present utility model;

图中,集水池1,斜网2,收集池3,油水分离池4,排油管41,第一pH调节池5,絮凝反应池6,第一沉淀池7,纤维球过滤器8,COD检测仪9,厌氧池10,兼氧池11,好氧池12,第二沉淀池13,MBR膜过滤池14,消毒池15,回用水池16,压滤机17,污泥池18,鼓风机19,污水泵100,泵101,污泥泵102,进液泵103,回流泵104,平板膜过滤器140,第一加药混合器200,第二加药混合器201,排污阀300,进液阀301,回流阀302,出液阀303,回流管道400,污泥总管500。In the figure, the collection tank 1, the inclined net 2, the collection tank 3, the oil-water separation tank 4, the oil discharge pipe 41, the first pH adjustment tank 5, the flocculation reaction tank 6, the first sedimentation tank 7, the fiber ball filter 8, the COD detection Instrument 9, anaerobic tank 10, facultative oxygen tank 11, aerobic tank 12, second sedimentation tank 13, MBR membrane filter tank 14, disinfection tank 15, reuse tank 16, filter press 17, sludge tank 18, blower 19. Sewage pump 100, pump 101, sludge pump 102, feed pump 103, return pump 104, flat membrane filter 140, first dosing mixer 200, second dosing mixer 201, blowdown valve 300, feed Liquid valve 301 , return valve 302 , liquid outlet valve 303 , return pipe 400 , sludge main pipe 500 .

具体实施方式Detailed ways

为了使本实用新型实现的技术手段、创作特征、达成目的与功效易于明白了解,下面结合具体图示,进一步阐述本实用新型。In order to make it easy to understand the technical means, creation features, achievement goals and effects realized by the present invention, the present invention will be further described below with reference to the specific figures.

实施例1,参见图1所示的一种带COD检测的污水处理系统,包括集水池1、第一pH调节池5、絮凝反应池6、第一沉淀池7、纤维球过滤器8、厌氧池10、兼氧池11、好氧池12、第二沉淀池13 、MBR膜过滤池14、消毒池15和回用水池16,集水池1与第一pH调节池5之间设有油水分离池4,油水分离池4的上部设有斜网2,油水分离池4的上部一侧设有排油管41,油水分离池4的进口侧设有对应斜网2出口的收集池3,油水分离池4的出口通过泵101与第一pH调节池5进口连接,油水分离池4与第一pH调节池5连接的管道上设有第一加药混合器200,第一pH调节池5的出口与絮凝反应池6的进口连接,第一pH调节池5与絮凝反应池6连接的管道上设有第二加药混合器201,絮凝反应池6的出口与第一沉淀池7的进口连接,第一沉淀池7的出口经进液泵103及进液阀301与纤维球过滤器8的进水口连接,纤维球过滤器8的出水口经排液阀303与厌氧池10的进口连接,厌氧池10的出口与兼氧池11的进口连接,兼氧池11的出口与好氧池12,好氧池12内设有曝气管,曝气管道与鼓风机19连接,好氧池12的出口与第二沉淀池13进口连接,第二沉淀池13的出口与MBR膜过滤池14的进口连接,MBR膜过滤池14内设有平板膜过滤器140,MBR膜过滤池14的出口经消毒池15与回用水池16连接,消毒池15内设有紫外线杀菌灯,所述好氧池12的出口管路上设有COD检测仪9,好氧池12的出口管路经过COD检测仪9后分为两路,一路与第二沉淀池13连接,另一路通过回流管道400、回流阀302及回流泵104回流至厌氧池10。Embodiment 1, referring to a sewage treatment system with COD detection shown in FIG. 1, including a water collection tank 1, a first pH adjustment tank 5, a flocculation reaction tank 6, a first sedimentation tank 7, a fiber ball filter 8, a Oxygen tank 10, facultative oxygen tank 11, aerobic tank 12, second sedimentation tank 13, MBR membrane filter tank 14, disinfection tank 15 and reuse tank 16, there is oil and water between the water collection tank 1 and the first pH adjustment tank 5 Separation pool 4, the upper part of the oil-water separation pool 4 is provided with an inclined net 2, the upper side of the oil-water separation pool 4 is provided with an oil discharge pipe 41, and the inlet side of the oil-water separation pool 4 is provided with a collection pool 3 corresponding to the outlet of the inclined net 2, and the oil-water separation pool 4 is provided with a collection pool 3 corresponding to the outlet of the inclined net 2. The outlet of the separation tank 4 is connected to the inlet of the first pH adjustment tank 5 through the pump 101. The pipeline connecting the oil-water separation tank 4 and the first pH adjustment tank 5 is provided with a first dosing mixer 200. The outlet is connected to the inlet of the flocculation reaction tank 6, the pipeline connecting the first pH adjustment tank 5 and the flocculation reaction tank 6 is provided with a second dosing mixer 201, and the outlet of the flocculation reaction tank 6 is connected to the inlet of the first sedimentation tank 7 , the outlet of the first sedimentation tank 7 is connected with the water inlet of the fiber ball filter 8 through the liquid inlet pump 103 and the liquid inlet valve 301, and the water outlet of the fiber ball filter 8 is connected with the inlet of the anaerobic tank 10 through the drain valve 303. , the outlet of the anaerobic tank 10 is connected with the inlet of the anaerobic tank 11, the outlet of the anaerobic tank 11 is connected with the aerobic tank 12, the aeration pipe is provided in the aerobic tank 12, the aeration pipe is connected with the blower 19, and the aerobic tank The outlet of 12 is connected with the inlet of the second sedimentation tank 13, the outlet of the second sedimentation tank 13 is connected with the inlet of the MBR membrane filter tank 14, the MBR membrane filter tank 14 is provided with a flat membrane filter 140, and the outlet of the MBR membrane filter tank 14 The disinfection tank 15 is connected to the reuse water tank 16, and the disinfection tank 15 is provided with an ultraviolet germicidal lamp. The outlet pipeline of the aerobic tank 12 is provided with a COD detector 9, and the outlet pipeline of the aerobic tank 12 passes through the COD detector. After 9, it is divided into two paths, one is connected to the second sedimentation tank 13, and the other is returned to the anaerobic tank 10 through the return pipeline 400, the return valve 302 and the return pump 104.

进一步,还包括污泥处理系统,污泥处理系统包括压滤机17、污泥池18、污泥泵102和污泥总管500,第一pH调节池5的排污口、絮凝反应池6的排污口、第一沉淀池7的排污口、第二沉淀池13的排污口以及MBR膜过滤池14的排污口分别通过污泥支管及排污阀300与污泥总管500连接,污泥总管500的出口经污泥泵102与污泥池18的入口连接,污泥池18的出口经泵泵送至压滤机17。Further, it also includes a sludge treatment system. The sludge treatment system includes a filter press 17, a sludge tank 18, a sludge pump 102, a sludge main pipe 500, a sewage outlet of the first pH adjustment tank 5, and a sewage discharge of the flocculation reaction tank 6. The sewage outlet, the sewage outlet of the first sedimentation tank 7, the sewage outlet of the second sedimentation tank 13 and the sewage outlet of the MBR membrane filter tank 14 are respectively connected with the sludge main pipe 500 through the sludge branch pipe and the sewage valve 300, and the outlet of the sludge main pipe 500 The sludge pump 102 is connected to the inlet of the sludge tank 18, and the outlet of the sludge tank 18 is pumped to the filter press 17 through the pump.

进一步,压滤机17的滤液出口经管道与污泥池18的入口连接。Further, the filtrate outlet of the filter press 17 is connected to the inlet of the sludge tank 18 through a pipeline.

进一步,污泥池18的上清液通过管道与集水池1连接。Further, the supernatant of the sludge tank 18 is connected to the sump 1 through a pipeline.

本实用新型污水处理过程如下:The sewage treatment process of the present utility model is as follows:

污水通过格栅后自流流入集水池1,污水通过污水泵100提至斜网2上端的水槽并由水槽横向分布流到斜网上,斜网过滤出的较大物体滑入收集池3收集,从而起到初步拦截的作用,污水则透过斜网2的网孔落入油水分离池3,油水分离池将油和水进一步分离,油污则通过排油管41排至油污收集桶进行收集,污水则通过泵101进入第一pH调节池5可在第一加药混合器200内加药混合后进入第一pH调节池5,起到调节pH值的作用,污水进入絮凝反应池6,可在第二加药混合器201内添加混凝剂(PAC、PAM)在混凝剂(PAC、PAM)的作用下,使污水中的胶体和细微悬浮物凝聚成絮凝体,予以分离,然后污水进入第一沉淀池7沉淀,沉淀后的上清液进入纤维球过滤器8,以去除污水中的悬浮物;纤维球过滤器8过滤后的污水依次进入厌氧池10、兼氧池11、好氧池12 在此期间进行生化反应能有效脱氮,破坏有机物结构,达到降低COD的目的,为了防止COD指数不达标外排,在好氧池12的出口管路上设置了COD检测仪9,当COD检测仪9检测合格后可将污水进一步导入第二沉淀池13,如不合格可通过回流管道400、回流阀302及回流泵104回流至厌氧池10,第二沉淀池13的上清液进入MBR膜过滤池14过滤,平板膜过滤器140可以有效拦截及过滤难降解的有机物及杂质,起到进一步净化水质的目的,经过MBR膜过滤池14水经过消毒池15,在紫外线杀菌灯的作用下杀灭细菌,之后流入回用水池16待用,各阶段产生的污泥均可通过污泥支管及排污阀300与污泥总管500连接,经压滤机压滤后,滤液返回污泥池18,污泥池18的上清液通过管道返回集水池1,滤饼外运,可有效减少水体的二次污染。After passing through the grille, the sewage flows into the collecting tank 1, and the sewage is lifted to the water tank at the upper end of the inclined net 2 through the sewage pump 100, and then flows laterally to the inclined net from the water tank. Playing the role of preliminary interception, the sewage falls into the oil-water separation tank 3 through the mesh of the inclined net 2, the oil-water separation tank further separates the oil and water, and the oil is discharged to the oil-stain collection bucket through the oil discharge pipe 41 for collection, and the sewage is collected. Entering the first pH adjustment tank 5 through the pump 101 can enter the first pH adjustment tank 5 after dosing and mixing in the first dosing mixer 200, which plays the role of adjusting the pH value. The sewage enters the flocculation reaction tank 6. Coagulants (PAC, PAM) are added in the second dosing mixer 201. Under the action of the coagulants (PAC, PAM), the colloids and fine suspended solids in the sewage are agglomerated into flocs, which are separated, and then the sewage enters the first A sedimentation tank 7 sediments, and the precipitation supernatant enters the fiber ball filter 8 to remove suspended solids in the sewage; the sewage filtered by the fiber ball filter 8 enters the anaerobic tank 10, the facultative tank 11, the aerobic tank During this period, the biochemical reaction of the tank 12 can effectively denitrify, destroy the structure of organic matter, and achieve the purpose of reducing COD. After the detector 9 passes the test, the sewage can be further introduced into the second sedimentation tank 13. If it is unqualified, it can be returned to the anaerobic tank 10 through the return pipe 400, the return valve 302 and the return pump 104, and the supernatant of the second sedimentation tank 13 enters. The MBR membrane filter tank 14 is filtered, and the flat membrane filter 140 can effectively intercept and filter the refractory organic matter and impurities, and further purify the water quality. The water passes through the MBR membrane filter tank 14 and passes through the disinfection tank 15. The filtrate can be connected to the sludge main pipe 500 through the sludge branch pipe and the sewage valve 300. After being filtered by the filter press, the filtrate is returned to the sludge tank. 18. The supernatant of the sludge tank 18 is returned to the collection tank 1 through the pipeline, and the filter cake is transported out, which can effectively reduce the secondary pollution of the water body.

以上显示和描述了本实用新型的基本原理和主要特征和本实用新型的优点。本行业的技术人员应该了解,本实用新型不受上述实施例的限制,上述实施例和说明书中描述的只是说明本实用新型的原理,在不脱离本实用新型精神和范围的前提下,本实用新型还会有各种变化和改进,这些变化和改进都落入要求保护的本实用新型范围内。本实用新型要求保护范围由所附的权利要求书及其等效物界定。The basic principles and main features of the present invention and the advantages of the present invention are shown and described above. It should be understood by those skilled in the art that the present invention is not limited by the above-mentioned embodiments. The above-mentioned embodiments and descriptions only illustrate the principle of the present invention. Without departing from the spirit and scope of the present invention, the present invention There will also be various changes and improvements in the new model, which all fall within the scope of the claimed invention. The claimed scope of the present invention is defined by the appended claims and their equivalents.

Claims (4)

1. The utility model provides a take sewage treatment system of COD detection, including catch basin (1), first pH equalizing basin (5), flocculation reaction pond (6), first sedimentation tank (7), fibre ball filter (8), anaerobism pond (10), facultative tank (11), good oxygen pond (12), second sedimentation tank (13), MBR membrane filtration pond (14), disinfection pond (15) and reuse water pond (16), a serial communication port, be equipped with oil water separating tank (4) between catch basin (1) and first pH equalizing basin (5), the upper portion of oil water separating tank (4) is equipped with inclined wire netting (2), upper portion one side of oil water separating tank (4) is equipped with oil drain pipe (41), the import side of oil water separating tank (4) is equipped with collection pond (3) that correspond inclined wire netting (2) export, the export of oil water separating tank (4) is through pump (101) and first pH equalizing basin (5) access connection, be equipped with first blender on the pipeline that oil water separating tank (4) and first pH equalizing basin (5) are connected (200) The outlet of the first pH adjusting tank (5) is connected with the inlet of the flocculation reaction tank (6), a second medicine adding mixer (201) is arranged on a pipeline connecting the first pH adjusting tank (5) and the flocculation reaction tank (6), the outlet of the flocculation reaction tank (6) is connected with the inlet of the first sedimentation tank (7), the outlet of the first sedimentation tank (7) is connected with the water inlet of the fiber ball filter (8) through a liquid inlet pump (103) and a liquid inlet valve (301), the water outlet of the fiber ball filter (8) is connected with the inlet of the anaerobic tank (10) through a liquid outlet valve (303), the outlet of the anaerobic tank (10) is connected with the inlet of the facultative tank (11), the outlet of the facultative tank (11) is connected with the aerobic tank (12), an aeration pipe is arranged in the aerobic tank (12), the aeration pipe is connected with an air blower (19), the outlet of the aerobic tank (12) is connected with the inlet of the second sedimentation tank (13), the export of second sedimentation tank (13) and the access connection of MBR membrane filtration pond (14), be equipped with dull and stereotyped membrane filter (140) in MBR membrane filtration pond (14), the export of MBR membrane filtration pond (14) is connected with reuse pond (16) through disinfection pond (15), is equipped with sterilamp in disinfection pond (15), be equipped with COD detector (9) on the outlet pipeline of good oxygen pond (12), the outlet pipe way of good oxygen pond (12) is divided into two the tunnel after COD detector (9), is connected with second sedimentation tank (13) all the way, and another way is through backflow pipeline (400), reflux valve (302) and backwash pump (104) backward flow to anaerobism pond (10).
2. The sewage treatment system with the COD detection function according to claim 1, further comprising a sludge treatment system, wherein the sludge treatment system comprises a filter press (17), a sludge tank (18), a sludge pump (102) and a sludge main pipe (500), a sewage discharge port of the first pH adjusting tank (5), a sewage discharge port of the flocculation reaction tank (6), a sewage discharge port of the first sedimentation tank (7), a sewage discharge port of the second sedimentation tank (13) and a sewage discharge port of the MBR membrane filtration tank (14) are respectively connected with the sludge main pipe (500) through sludge branch pipes and a sewage discharge valve (300), an outlet of the sludge main pipe (500) is connected with an inlet of the sludge tank (18) through the sludge pump (102), and an outlet of the sludge tank (18) is pumped to the filter press (17) through the pump.
3. The sewage treatment system with COD detection according to claim 2, wherein the filtrate outlet of the filter press (17) is connected with the inlet of the sludge tank (18) through a pipeline.
4. The sewage treatment system with COD detection according to claim 2, wherein the supernatant of the sludge tank (18) is connected with the water collecting tank (1) through a pipeline.
CN201920520798.0U 2019-04-17 2019-04-17 A sewage treatment system with COD detection Active CN209940765U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115818867A (en) * 2022-11-18 2023-03-21 王兵雷 Sewage treatment process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115818867A (en) * 2022-11-18 2023-03-21 王兵雷 Sewage treatment process

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