CN105565608B - A kind of sewage disposal system based on data mining - Google Patents

A kind of sewage disposal system based on data mining Download PDF

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CN105565608B
CN105565608B CN201610074036.3A CN201610074036A CN105565608B CN 105565608 B CN105565608 B CN 105565608B CN 201610074036 A CN201610074036 A CN 201610074036A CN 105565608 B CN105565608 B CN 105565608B
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tank
aeration
data
cod
ammonia nitrogen
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CN105565608A (en
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刘忠宝
赵文娟
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North University of China
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • 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
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/06Controlling or monitoring parameters in water treatment pH
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/08Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/14NH3-N
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/18PO4-P
    • 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
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1268Membrane bioreactor systems
    • 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
    • C02F3/28Anaerobic digestion processes

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  • 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)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

本发明基于数据挖掘的污水处理系统;依次包括进水管、调节池、厌气池、曝气池、膜生物反应池、膜组件、污泥池、储水池;进水管中的污水注入调节池中,调节池底部设置有第一潜污泵,膜组件设置在膜生物反应池中,膜生物反应池底部设置有第二潜污泵,膜组件连接抽吸泵,抽吸泵将膜组件过滤后的污水输送到储水池中;其特征在于厌气池的上部被隔板分割,隔板的一侧设置有过滤区,隔板的另一侧通过连接口连通曝气池;曝气池中部设置有上曝气管,曝气池底部设置有下曝气管,下曝气管和上曝气管连接鼓风机;曝气池的上部通过过滤墙连通膜生物反应池;膜生物反应池底部设置有第三潜污泵,膜组件的两侧设置有曝气板。

The sewage treatment system based on data mining in the present invention includes water inlet pipe, regulating tank, anaerobic tank, aeration tank, membrane bioreaction tank, membrane module, sludge tank, and water storage tank in sequence; the sewage in the water inlet pipe is injected into the regulating tank , the first submersible sewage pump is installed at the bottom of the regulating tank, the membrane module is arranged in the membrane bioreaction tank, the second submersible sewage pump is arranged at the bottom of the membrane bioreaction tank, the membrane module is connected to the suction pump, and the suction pump filters the membrane module The sewage is transported to the storage tank; it is characterized in that the upper part of the anaerobic tank is divided by a partition, one side of the partition is provided with a filter area, and the other side of the partition is connected to the aeration tank through a connection port; the middle part of the aeration tank is set There is an upper aeration pipe, and a lower aeration pipe is installed at the bottom of the aeration tank, and the lower aeration pipe and the upper aeration pipe are connected to the blower; the upper part of the aeration tank is connected to the membrane bioreaction tank through the filter wall; the bottom of the membrane bioreaction tank is provided with For the third submersible sewage pump, aeration plates are arranged on both sides of the membrane module.

Description

一种基于数据挖掘的污水处理系统A Sewage Treatment System Based on Data Mining

技术领域technical field

本发明属于节能环保技术领域,具体为一种基于数据挖掘的污水处理系统。The invention belongs to the technical field of energy saving and environmental protection, and specifically relates to a sewage treatment system based on data mining.

背景技术Background technique

按污水来源分类,污水处理一般分为生产污水处理和生活污水处理。生产污水包括工业污水、农业污水以及医疗污水等,而生活污水就是日常生活产生的污水,是指各种形式的无机物和有机物的复杂混合物,包括:①漂浮和悬浮的大小固体颗粒;②胶状和凝胶状扩散物;③纯溶液。按水污的质性来分,水的污染有两类:一类是自然污染;另一类是人为污染。当前对水体危害较大的是人为污染。水污染可根据污染杂质的不同而主要分为化学性污染、物理性污染和生物性污染三大类。污染物主要有:⑴未经处理而排放的工业废水;⑵未经处理而排放的生活污水;⑶大量使用化肥、农药、除草剂的农田污水;⑷堆放在河边的工业废弃物和生活垃圾;⑸水土流失;⑹矿山污水。处理污水的方法很多,一般可归纳为物理法、化学法和生物法等。According to the classification of sewage sources, sewage treatment is generally divided into production sewage treatment and domestic sewage treatment. Production sewage includes industrial sewage, agricultural sewage and medical sewage, etc., while domestic sewage is sewage produced in daily life, which refers to a complex mixture of various forms of inorganic and organic substances, including: ①floating and suspended solid particles of large and small sizes; ②glue Shape and gel-like diffuser; ③ pure solution. According to the nature of water pollution, there are two types of water pollution: one is natural pollution; the other is man-made pollution. At present, the most harmful to water bodies is man-made pollution. Water pollution can be divided into three categories: chemical pollution, physical pollution and biological pollution according to the different impurities. Pollutants mainly include: ⑴ untreated industrial wastewater discharged; ⑵ untreated domestic sewage discharged; ⑶ farmland sewage with extensive use of chemical fertilizers, pesticides, and herbicides; ⑷ industrial waste and domestic garbage piled up by the river ; ⑸ soil erosion; ⑹ mine sewage. There are many ways to treat sewage, which can be generally classified into physical, chemical and biological methods.

膜-生物反应器(Membrane Bio-Reactor,MBR)为膜分离技术与生物处理技术有机结合之新型态废水处理系统。以膜组件取代传统生物处理技术末端二沉池,在生物反应器中保持高活性污泥浓度,提高生物处理有机负荷,从而减少污水处理设施占地面积,并通过保持低污泥负荷减少剩余污泥量。主要利用膜分离设备截留水中的活性污泥与大分子有机物。膜生物反应器系统内活性污泥(MLSS)浓度可提升至8000~10,000mg/L,甚至更高;污泥龄(SRT)可延长至30天以上。膜生物反应器因其有效的截留作用,可保留世代周期较长的微生物,可实现对污水深度净化,同时硝化菌在系统内能充分繁殖,其硝化效果明显,对深度除磷脱氮提供可能。Membrane Bio-Reactor (MBR) is a new type of wastewater treatment system that organically combines membrane separation technology and biological treatment technology. Replace the terminal secondary sedimentation tank of traditional biological treatment technology with membrane modules, maintain a high concentration of activated sludge in the bioreactor, increase the organic load of biological treatment, thereby reducing the footprint of sewage treatment facilities, and reduce the remaining sewage by maintaining low sludge load amount of mud. Mainly use membrane separation equipment to intercept activated sludge and macromolecular organic matter in water. The concentration of activated sludge (MLSS) in the membrane bioreactor system can be increased to 8000~10,000mg/L, or even higher; the sludge age (SRT) can be extended to more than 30 days. Membrane bioreactor can retain microorganisms with a long generation cycle due to its effective interception, and can realize deep purification of sewage. At the same time, nitrifying bacteria can fully reproduce in the system, and its nitrification effect is obvious, providing possibility for deep phosphorus and nitrogen removal .

发明内容Contents of the invention

本发明目的在于克服现有技术中的不足,提供一种基于数据挖掘的污水处理系统。The purpose of the present invention is to overcome the deficiencies in the prior art and provide a sewage treatment system based on data mining.

本发明基于数据挖掘的污水处理系统;依次包括进水管、调节池、厌气池、曝气池、膜生物反应池、膜组件、污泥池、储水池;所述进水管中的污水注入所述调节池中,所述调节池底部设置有第一潜污泵,所述膜组件设置在所述膜生物反应池中,所述膜生物反应池底部设置有第二潜污泵,所述第二潜污泵用于将所述膜生物反应池的污水输送到所述污泥池中,所述膜组件连接抽吸泵,所述抽吸泵将所述膜组件过滤后的污水输送到所述储水池中;所述厌气池的上部被隔板分割,所述隔板的一侧设置有过滤区,所述过滤区内填充物由粒度40目的二氧化硅、粒度20目的无烟煤滤料、粒度10目的麦饭石按重量比7:4:10混合而成;所述第一潜污泵将调节池的污水输送到所述过滤区中,所述隔板的另一侧通过连接口连通所述曝气池;所述曝气池中部设置有上曝气管,所述曝气池底部设置有下曝气管,所述下曝气管和上曝气管连接鼓风机;所述曝气池的上部通过过滤墙连通所述膜生物反应池;所述过滤墙内填充物由粒度30目的纳米矿晶、粒度20目沸石、粒度10目钠基膨润土按重量比5:11:8混合而成;所述膜生物反应池底部设置有第三潜污泵,所述第三潜污泵用于将所述膜生物反应池的污水输送到所述过滤区中,所述膜组件的两侧设置有曝气板。 所述曝气池中设置有COD检测器、氨氮检测器、总磷检测器、pH检测器、SS检测器。所述曝气板的出气方向均朝向膜组件方向,根据时间设定交替出气。The sewage treatment system based on data mining in the present invention includes water inlet pipes, regulating tanks, anaerobic tanks, aeration tanks, membrane bioreaction tanks, membrane modules, sludge tanks, and water storage tanks in sequence; the sewage in the water inlet pipes is injected into the In the adjustment tank, the bottom of the adjustment tank is provided with a first submersible sewage pump, the membrane module is provided in the membrane bioreaction tank, and the bottom of the membrane bioreaction tank is provided with a second submersible sewage pump. The second submersible sewage pump is used to transport the sewage from the membrane bioreactor to the sludge tank, and the membrane module is connected to a suction pump, and the suction pump transports the sewage filtered by the membrane module to the sludge tank. In the water storage tank; the upper part of the anaerobic tank is divided by a partition, and a filter area is provided on one side of the partition, and the filler in the filter area is made of silica with a particle size of 40 and anthracite filter material with a particle size of 20. , 10-mesh medical stone with a particle size of 7:4:10 by weight; the first submersible sewage pump transports the sewage from the regulating tank to the filter area, and the other side of the partition passes through the connection port connected to the aeration tank; the middle part of the aeration tank is provided with an upper aeration pipe, and the bottom of the aeration tank is provided with a lower aeration pipe, and the lower aeration pipe and the upper aeration pipe are connected to a blower; the aeration The upper part of the air pool is connected to the membrane bioreaction tank through the filter wall; the filler in the filter wall is composed of nano-mineral crystals with a particle size of 30 mesh, zeolite with a particle size of 20 mesh, and sodium bentonite with a particle size of 10 mesh in a weight ratio of 5:11:8. formed; the bottom of the membrane bioreactor tank is provided with a third submersible sewage pump, and the third submersible sewage pump is used to transport the sewage from the membrane bioreactor tank to the filter area, and the two membrane modules There is an aeration plate on the side. The aeration tank is provided with a COD detector, an ammonia nitrogen detector, a total phosphorus detector, a pH detector, and an SS detector. The air outlet direction of the aeration plate is all towards the direction of the membrane module, and the air outlet is alternately set according to the time.

特别的,本发明基于数据挖掘的污水处理系统;在距离进水管500米、1000米、1500米、2000米、2500米的污水渠位置,分别设置有COD检测器、氨氮检测器、总磷检测器,COD检测器、氨氮检测器、总磷检测器定时将检测的数据传送给计算机,计算机将五个位置同一时刻收集的COD数据、氨氮数据、总磷数据分别加和后储存为加和COD数据、加和氨氮数据、加和总磷数据;In particular, the sewage treatment system of the present invention is based on data mining; COD detectors, ammonia nitrogen detectors, and total phosphorus detectors are respectively installed at the sewage drains 500 meters, 1,000 meters, 1,500 meters, 2,000 meters, and 2,500 meters away from the water inlet pipe. The COD detector, ammonia nitrogen detector, and total phosphorus detector regularly transmit the detected data to the computer, and the computer adds the COD data, ammonia nitrogen data, and total phosphorus data collected at the same time at five locations and stores them as summed COD data, summed ammonia nitrogen data, summed total phosphorus data;

计算机将储存的前15日的加和COD数据、加和氨氮数据、加和总磷数据,分别通过线性函数y=(x-MinValue)/(MaxValue-MinValue)转换归一化后,进行K-均值聚类划分为五个档级;五个档级分别预先对应设置不同的鼓风机工作强度。同时计算不同档级的:档级X平均COD值、档级X平均氨氮值、档级X平均总磷值,X=1,2,3,4,5;The computer converts and normalizes the stored COD data, ammonia nitrogen data, and total phosphorus data of the first 15 days respectively through the linear function y=(x-MinValue)/(MaxValue-MinValue), and performs K- The mean value clustering is divided into five grades; the five grades correspond to different blower working strengths in advance. At the same time, calculate different grades: grade X average COD value, grade X average ammonia nitrogen value, grade X average total phosphorus value, X=1,2,3,4,5;

将转换归一化处理的实时采集到的数据,实时COD值、实时氨氮值、实时总磷值,按照:Y=(实时COD数据-档级X平均COD值)2+(实时氨氮数据-档级X平均氨氮值)2+(实时总磷数据-档级X平均总磷值)2,X=1,2,3,4,5计算;Y最小时的X档级所对应的鼓风机的工作强度,为下一小时,鼓风机的工作强度。The real-time collected data will be converted and normalized, real-time COD value, real-time ammonia nitrogen value, real-time total phosphorus value, according to: Y=(real-time COD data-level X average COD value) 2 +(real-time ammonia nitrogen data-level level X average ammonia nitrogen value) 2 + (real-time total phosphorus data - level X average total phosphorus value) 2 , X=1,2,3,4,5 calculation; when Y is the smallest, the work of the blower corresponding to the X level Intensity, for the next hour, the working intensity of the blower.

本发明基于数据挖掘的污水处理系统,采用了曝气池、膜生物反应池两个好氧反应池,以及特殊的的曝气系统设置,增强了污水处理系统的处理分解能力;同时,设置有由特殊材料制成的过滤墙进行过滤,在膜组件的两侧曝气板交替出气加大了膜组件摆动,减少了膜组件的污染增强了膜组件的寿命;厌气池上方过滤区的设置增强了厌氧池的分解能力;同时本发明,将污水处理系统上游检测到的历史数据分为不同档级,不同档级分别对应不同的鼓风机的工作强度;根据实时获得的污水处理系统上游数据最接近的档级,该档级对应的鼓风机的工作强度,为未来一段时间鼓风机的工作强度;本控制方法,非常适合有不定期进行污水排放的排放源的污水处理系统的控制;采用该方法能够大大降低,污水处理系统的能耗,提高系统的污水处理能力。The sewage treatment system based on data mining in the present invention adopts two aerobic reaction tanks, the aeration tank and the membrane bioreaction tank, and a special aeration system setting, which enhances the treatment and decomposition ability of the sewage treatment system; at the same time, it is equipped with The filter wall made of special materials is used for filtration, and the aeration plates on both sides of the membrane module alternately discharge air to increase the swing of the membrane module, reduce the pollution of the membrane module and enhance the life of the membrane module; the setting of the filter area above the anaerobic pool The decomposition ability of the anaerobic pool is enhanced; at the same time, the present invention divides the historical data detected upstream of the sewage treatment system into different grades, and different grades correspond to the working intensity of different blowers; according to the upstream data of the sewage treatment system obtained in real time The closest gear, the working intensity of the blower corresponding to this gear, is the working intensity of the blower for a period of time in the future; this control method is very suitable for the control of sewage treatment systems with discharge sources that discharge sewage irregularly; using this method It can greatly reduce the energy consumption of the sewage treatment system and improve the sewage treatment capacity of the system.

附图说明Description of drawings

图1是本发明基于数据挖掘的污水处理系统结构示意图。Fig. 1 is a schematic structural diagram of the sewage treatment system based on data mining in the present invention.

具体实施方式detailed description

下面给出的实施例拟对本发明作进一步说明,但不能理解为是对本发明保护范围的限制,本领域技术人员根据本发明内容对本发明的一些非本质的改进和调整,仍属于本发明的保护范围。The embodiment given below intends to further illustrate the present invention, but can not be interpreted as the restriction to protection scope of the present invention, those skilled in the art still belongs to the protection of the present invention to some non-essential improvements and adjustments of the present invention according to the content of the present invention scope.

实施例如图1所示,基于数据挖掘的污水处理系统;依次包括进水管1、调节池2、厌气池3、曝气池4、膜生物反应池5、膜组件6、污泥池7、储水池8;膜组件6为浸没式设置的中空纤维膜组件;厌气池3添加沧州市中信生物科技有限公司污水处理专用菌种菌B;曝气池4和膜生物反应池5添加沧州市中信生物科技有限公司污水处理专用菌种菌A。The embodiment example is shown in Figure 1, a sewage treatment system based on data mining; sequentially includes a water inlet pipe 1, a regulating tank 2, an anaerobic tank 3, an aeration tank 4, a membrane bioreaction tank 5, a membrane module 6, a sludge tank 7, The water storage tank 8; the membrane module 6 is a submerged hollow fiber membrane module; the anaerobic tank 3 is added with special bacteria B for sewage treatment of Cangzhou Zhongxin Biotechnology Co., Ltd; Special bacteria strain A for sewage treatment of CITIC Biotechnology Co., Ltd.

进水管1中的污水注入调节池2中,调节池2底部设置有第一潜污泵9,膜组件6设置在膜生物反应池5中,膜生物反应池5底部设置有第二潜污泵10,第二潜污泵10用于将膜生物反应池5的污水输送到污泥池7中,膜组件6连接抽吸泵11,抽吸泵11将膜组件6过滤后的污水输送到储水池8中;厌气池3的上部被隔板12分割,隔板12的一侧设置有过滤区13,过滤区13内填充物由粒度40目的二氧化硅、粒度20目的无烟煤滤料、粒度10目的麦饭石按重量比7:4:10混合而成;第一潜污泵9将调节池2的污水输送到过滤区13中,隔板12的另一侧通过连接口14连通曝气池4;曝气池4中部设置有上曝气管15,曝气池4底部设置有下曝气管16,下曝气管15和上曝气管16连接鼓风机17;下曝气管15和上曝气管16均采用微孔曝气方式;The sewage in the water inlet pipe 1 is injected into the regulating tank 2, the bottom of the regulating tank 2 is provided with a first submersible sewage pump 9, the membrane module 6 is provided in the membrane bioreaction tank 5, and the bottom of the membrane bioreaction tank 5 is provided with a second submersible sewage pump 10. The second submersible sewage pump 10 is used to transport the sewage from the membrane bioreactor 5 to the sludge pool 7. The membrane module 6 is connected to the suction pump 11, and the suction pump 11 transports the sewage filtered by the membrane module 6 to the storage tank. In the pool 8; the upper part of the anaerobic pool 3 is divided by a partition 12, and one side of the partition 12 is provided with a filter area 13, and the filler in the filter area 13 is made of silica with a particle size of 40 mesh, anthracite filter material with a particle size of 20 mesh, and a filter material with a particle size of 20 mesh. The 10-mesh medical stone is mixed according to the weight ratio of 7:4:10; the first submersible sewage pump 9 transports the sewage from the regulating tank 2 to the filter area 13, and the other side of the partition 12 is connected to the aeration through the connection port 14 Pond 4; The middle part of the aeration tank 4 is provided with an upper aeration pipe 15, and the bottom of the aeration tank 4 is provided with a lower aeration pipe 16, and the lower aeration pipe 15 and the upper aeration pipe 16 are connected to the blower 17; the lower aeration pipe 15 and The upper aeration pipe 16 adopts the microporous aeration method;

曝气池4的上部通过过滤墙18连通膜生物反应池5;过滤墙18内填充物由粒度30目的纳米矿晶、粒度20目沸石、粒度10目钠基膨润土按重量比5:11:8混合而成;膜生物反应池5底部设置有第三潜污泵19,第三潜污泵19用于将膜生物反应池5的污水输送到过滤区13中,补充厌气池3其中的污泥浓度为15~20g/L;膜组件6的两侧设置有曝气板20。曝气板20采用射流曝气方式,曝气池4中设置有COD检测器、氨氮检测器、总磷检测器、pH检测器、SS检测器。曝气板20的出气方向均朝向膜组件6方向,两个曝气板20根据时间设定为2秒为周期交替出气。曝气池4和膜生物反应池5内保持的污泥浓度MLSS 为10~15g/L,The upper part of the aeration tank 4 is connected to the membrane bioreaction tank 5 through the filter wall 18; the filler in the filter wall 18 is composed of nano-mineral crystals with a particle size of 30 mesh, zeolite with a particle size of 20 mesh, and sodium bentonite with a particle size of 10 mesh in a weight ratio of 5:11:8 mixed; the bottom of the membrane bioreactor 5 is provided with a third submersible sewage pump 19, and the third submersible sewage pump 19 is used to transport the sewage of the membrane bioreactor 5 to the filter area 13 to supplement the sewage in the anaerobic pool 3. The mud concentration is 15~20g/L; the two sides of the membrane module 6 are provided with aeration plates 20 . The aeration plate 20 adopts a jet aeration method, and the aeration tank 4 is provided with COD detectors, ammonia nitrogen detectors, total phosphorus detectors, pH detectors, and SS detectors. The air outlet directions of the aeration plates 20 all face the direction of the membrane module 6, and the two aeration plates 20 are set to alternately output air at a period of 2 seconds according to the time. The sludge concentration MLSS maintained in the aeration tank 4 and the membrane bioreactor 5 is 10~15g/L,

特别的,在距离进水管500米、1000米、1500米、2000米、2500米的污水渠位置,分别设置有COD检测器、氨氮检测器、总磷检测器,COD检测器、氨氮检测器、总磷检测器定时将检测的数据传送给计算机,计算机将五个位置同一时刻收集的COD数据、氨氮数据、总磷数据分别加和后储存为加和COD数据、加和氨氮数据、加和总磷数据;In particular, COD detectors, ammonia nitrogen detectors, total phosphorus detectors, COD detectors, ammonia nitrogen detectors, The total phosphorus detector transmits the detected data to the computer at regular intervals, and the computer sums the COD data, ammonia nitrogen data, and total phosphorus data collected at the same time at five locations and stores them as summed COD data, summed ammonia nitrogen data, and summed total phosphorus data;

每五天,计算机将储存的前15日的加和COD数据、加和氨氮数据、加和总磷数据,分别通过线性函数y=(x-MinValue)/(MaxValue-MinValue)转换归一化后,利用SPSS19.0提供的K-均值聚类算法划分为五个档级;五个档级分别预先对应设置不同的鼓风机工作强度。同时计算不同档级的:档级X平均COD值、档级X平均氨氮值、档级X平均总磷值,X=1,2,3,4,5;Every five days, the computer converts and normalizes the stored COD data, ammonia nitrogen data, and total phosphorus data of the first 15 days respectively through the linear function y=(x-MinValue)/(MaxValue-MinValue) , using the K-means clustering algorithm provided by SPSS19.0 to divide it into five levels; the five levels correspond to different blower working strengths in advance. At the same time, calculate different grades: grade X average COD value, grade X average ammonia nitrogen value, grade X average total phosphorus value, X=1,2,3,4,5;

COD检测器、氨氮检测器、总磷检测器每一小时实时传送实时数据,将转换归一化处理的实时采集到的数据即实时COD值、实时氨氮值、实时总磷值,按照:Y=(实时COD数据-档级X平均COD值)2+(实时氨氮数据-档级X平均氨氮值)2+(实时总磷数据-档级X平均总磷值)2,X=1,2,3,4,5计算;Y最小时的X档级所对应的鼓风机的工作强度,为下一小时,鼓风机的工作强度。COD detectors, ammonia nitrogen detectors, and total phosphorus detectors transmit real-time data in real time every hour, and convert and normalize the real-time collected data, namely real-time COD values, real-time ammonia nitrogen values, and real-time total phosphorus values, according to: Y= (Real-time COD data - grade X average COD value) 2 + (real-time ammonia nitrogen data - grade X average ammonia nitrogen value) 2 + (real-time total phosphorus data - grade X average total phosphorus value) 2 , X=1,2, 3,4,5 calculation; the working intensity of the blower corresponding to the X gear when Y is the smallest is the working intensity of the blower for the next hour.

Claims (1)

  1. A kind of 1. sewage disposal system based on data mining, successively including water inlet pipe, regulating reservoir, pond of being sick of, aeration tank, film life Thing reaction tank, membrane module, sludge-tank, tank;Sewage in the water inlet pipe is injected in the regulating reservoir, the regulating reservoir bottom Portion is provided with the first submersible sewage pump, and the membrane module is arranged in the membrane biological reaction pond, and the membrane biological reaction bottom of pond portion is set The second submersible sewage pump is equipped with, second submersible sewage pump is used for by the sewage transport in the membrane biological reaction pond into the sludge-tank, The membrane module connects suction pump, and the suction pump is by the sewage transport after membrane module filtering into the tank;Its It is characterised by that the top in the lonely pond is split by dividing plate, the side of the dividing plate is provided with filtering area, is filled out in the filtering area Fill thing by the silica of the mesh of granularity 40, the ANTHRACITE FILTER MEDIA of the mesh of granularity 20, the mesh of granularity 10 medical stone by weight 7:4:10 Mix;By the sewage transport of regulating reservoir into the filtering area, the opposite side of the dividing plate passes through first submersible sewage pump Connector connects the aeration tank;Aeration tube is provided with the middle part of the aeration tank, the aeration tank bottom is provided with lower aeration Pipe, the lower aeration tube connect air blower with upper aeration tube;The top of the aeration tank connects the film biology by filtering wall Reaction tank;It is described filtering within the walls filler by the mesh of granularity 30 nanometer ore deposit crystalline substance, the mesh zeolite of granularity 20, the mesh sodium bentonite of granularity 10 By weight 5:11:8 mix;The membrane biological reaction bottom of pond portion is provided with the 3rd submersible sewage pump, and the 3rd submersible sewage pump is used In by the sewage transport in the membrane biological reaction pond, into the filtering area, the both sides of the membrane module are provided with aeration board, institute State and COD detectors, ammonia nitrogen detector, total P detector, pH detectors, SS detectors are provided with aeration tank, intake in distance 500 meters of pipe, 1000 meters, 1500 meters, 2000 meters, 2500 meters of sewer position, it is respectively arranged with COD detectors, ammonia nitrogen detection Device, total P detector, COD detectors, ammonia nitrogen detector, the timing of total P detector send the data of detection to computer, counted COD data that calculation machine collects five position synchronizations, ammonia nitrogen data, total phosphorus data add respectively and after save as plus and COD Data plus and ammonia nitrogen data plus and total phosphorus data;Computer by first 15 days of storage plus and COD data, plus and ammonia nitrogen number According to, plus and total phosphorus data, respectively by linear function conversion normalization after, carry out K- mean clusters be divided into five shelves levels;Five Individual shelves level is correspondingly arranged different air blower working strengths in advance respectively;Calculate different shelves levels simultaneously:The average COD values of shelves level X, The average ammonia nitrogen values of shelves level X, the average total phosphorus values of shelves level X, X=1,2,3,4,5;The number collected in real time of normalized will be changed According to, real-time COD value, real-time ammonia nitrogen value, real-time total phosphorus value, according to:Y=(The real-time average COD values of COD data-shelves level X)2+(In real time The average ammonia nitrogen values of ammonia nitrogen data-shelves level X)2+(The real-time average total phosphorus values of total phosphorus data-shelves level X)2, X=1,2,3,4,5 calculate;Y is most Hour X shelves levels corresponding to air blower working strength, be next hour, the working strength of air blower, the aeration board Towards membrane module direction, alternately outlet is set according to the time for outgassing direction.
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