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CN111977894A - Domestic sewage treatment system and control method - Google Patents

Domestic sewage treatment system and control method Download PDF

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Publication number
CN111977894A
CN111977894A CN202010776151.1A CN202010776151A CN111977894A CN 111977894 A CN111977894 A CN 111977894A CN 202010776151 A CN202010776151 A CN 202010776151A CN 111977894 A CN111977894 A CN 111977894A
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domestic sewage
tank
treatment
pump
sewage
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王熙俊
涂孝飞
李志成
侯巍
底广辉
张洪江
胡远翔
王竞一
李磊
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Hebei Zhuozhou Jingyuan Thermal Electricity Co ltd
State Grid Corp of China SGCC
North China Electric Power Research Institute Co Ltd
Huadian Electric Power Research Institute Co Ltd
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Hebei Zhuozhou Jingyuan Thermal Electricity Co ltd
State Grid Corp of China SGCC
North China Electric Power Research Institute Co Ltd
Huadian Electric Power Research Institute Co Ltd
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Priority to CN202010776151.1A priority Critical patent/CN111977894A/en
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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
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/50Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
    • 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
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/38Organic compounds containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/302Nitrification and denitrification treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F7/00Aeration of stretches of water

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

Abstract

一种生活污水处理系统及控制方法,所述系统包含缓冲装置、分解装置、回用装置和输出装置;缓冲装置存储接收到的生活污水,并滤除大于预设体积的漂浮物;分解装置对缓存装置滤除处理后的生活污水进行初步沉淀处理后进行水解反应和酸化反应,将有机固体及预定类别的有机物分解为小分子溶解性的有机物污染物;通过膜生物的代谢作用将有机物污染物转化为氨氮,再通过好氧硝化和缺氧反硝化过程去除氨氮;回用装置对分解装置处理后的生活污水进行固液分离处理,获得脱落生物膜和生活污水;将脱落生物膜输入至分解装置进行污泥回用,对生活污水进行消毒处理后输出;输出装置将回用装置输出的生活污水进行活性炭过滤后输出至外部用水机构。

Figure 202010776151

A domestic sewage treatment system and a control method, the system comprises a buffer device, a decomposition device, a reuse device and an output device; the buffer device stores the received domestic sewage, and filters out floating objects larger than a preset volume; The buffer device filters out the treated domestic sewage, performs preliminary precipitation treatment, and then performs hydrolysis reaction and acidification reaction to decompose organic solids and predetermined types of organic matter into small-molecule-soluble organic pollutants; Convert it into ammonia nitrogen, and then remove ammonia nitrogen through aerobic nitrification and anoxic denitrification; the recycling device performs solid-liquid separation treatment on the domestic sewage treated by the decomposition device to obtain exfoliated biofilm and domestic sewage; the exfoliated biofilm is input to decomposition The device reuses the sludge, disinfects the domestic sewage and outputs it; the output device filters the domestic sewage output by the recycling device with activated carbon and outputs it to the external water use mechanism.

Figure 202010776151

Description

生活污水处理系统及控制方法Domestic sewage treatment system and control method

技术领域technical field

本发明涉及环境处理领域,尤指一种生活污水处理系统及控制方法。The invention relates to the field of environmental treatment, in particular to a domestic sewage treatment system and a control method.

背景技术Background technique

工业厂区生活污水主要来自厂房、生产、行政办公楼、浴池、食堂排水及其他附属建筑的卫生间排水。厂区生活污水中主要水质指标:BOD5(100~200mg/L)、SS(150~200mg/L)、COD(200~400mg/L)、NH3-N(30~40mg/L)、pH(6~9)。对照典型生活污水水质指标,产区生活污水各指标处于较低值区间。但是随着国家废水零排放政策进一步贯彻落地,厂区作为一个相对独立的工业生产、生活区域,实现产区内水资源循环、再利用,从而实现污水超低甚至零排放势在必行。厂区生活污水处理后的去向设计为绿化喷洒用水,针对工业产区生活污水特点,进行生活污水深度处理,使得水质指标达到污水回用绿化用水的标准。因此,业内亟需研究开发一种适用于厂区生活污水处理系统,可搭载数据处理日益强大的计算机DCS控制方法完成自动化污水处理,提供一种污水处理系统自动、协调、连续运行控制的系统及方法。The domestic sewage in the industrial plant area mainly comes from the drainage of workshops, production, administrative office buildings, baths, canteens and toilets of other ancillary buildings. Main water quality indicators in the domestic sewage in the factory area: BOD 5 (100-200mg/L), SS (150-200mg/L), COD (200-400mg/L), NH 3 -N (30-40mg/L), pH ( 6 to 9). Compared with the typical domestic sewage water quality indicators, the indicators of domestic sewage in the production area are in the lower range. However, with the further implementation of the national zero-discharge policy of wastewater, the factory, as a relatively independent industrial production and living area, realizes the recycling and reuse of water resources in the production area, so as to achieve ultra-low or even zero discharge of sewage. The destination of the domestic sewage in the factory area after treatment is designed to be water for greening and spraying. According to the characteristics of domestic sewage in industrial production areas, advanced treatment of domestic sewage is carried out, so that the water quality index reaches the standard of green water for sewage reuse. Therefore, it is urgent in the industry to research and develop a domestic sewage treatment system suitable for the factory area, which can be equipped with a computer DCS control method with increasingly powerful data processing to complete automatic sewage treatment, and provide a system and method for automatic, coordinated, and continuous operation control of the sewage treatment system. .

发明内容SUMMARY OF THE INVENTION

本发明目的在于提供一种生活污水处理系统及控制方法,使用该系统及控制方法能够提高生活污水处理效率、降低运行成本。The purpose of the present invention is to provide a domestic sewage treatment system and a control method, and the use of the system and the control method can improve the domestic sewage treatment efficiency and reduce the operation cost.

为达上述目的,本发明所提供的生活污水处理系统,所述系统包含缓冲装置、分解装置、回用装置和输出装置;所述缓冲装置用于存储接收到的生活污水,并滤除所述生活污水中大于预设体积的漂浮物;所述分解装置用于对所述缓存装置滤除处理后的生活污水进行初步沉淀处理,对处理后的生活污水进行水解反应和酸化反应,将生活污水中的有机固体及预定类别的有机物分解为小分子溶解性的有机物污染物;通过膜生物的代谢作用将所述有机物污染物转化为氨氮,再通过好氧硝化和缺氧反硝化过程去除所述氨氮,输出去除所述氨氮后的生活污水;所述回用装置用于对所述分解装置处理后的生活污水进行固液分离处理,获得脱落生物膜和生活污水;将所述脱落生物膜输入至所述分解装置进行污泥回用,对分离处理获得的生活污水进行消毒处理后输出;所述输出装置用于将所述回用装置输出的生活污水进行活性炭过滤后输出至外部用水机构。In order to achieve the above purpose, the domestic sewage treatment system provided by the present invention includes a buffer device, a decomposition device, a reuse device and an output device; the buffer device is used to store the received domestic sewage and filter out the Floating matter larger than a preset volume in the domestic sewage; the decomposition device is used to perform preliminary precipitation treatment on the domestic sewage filtered and treated by the buffer device, perform hydrolysis reaction and acidification reaction on the treated domestic sewage, and decompose the domestic sewage. The organic solids and predetermined types of organic matter in the plant are decomposed into small-molecule-soluble organic pollutants; the organic pollutants are converted into ammonia nitrogen through the metabolism of membrane organisms, and then removed through aerobic nitrification and anoxic denitrification processes. Ammonia nitrogen, output the domestic sewage after the ammonia nitrogen is removed; the reuse device is used to perform solid-liquid separation treatment on the domestic sewage treated by the decomposition device to obtain detached biofilm and domestic sewage; input the detached biofilm The sludge is reused in the decomposition device, and the domestic sewage obtained by the separation treatment is disinfected and then output; the output device is used to filter the domestic sewage output by the recycling device with activated carbon and then output it to an external water use mechanism.

在上述生活污水处理系统中,优选的,所述缓冲装置包含格栅井和调节池;所述格栅井用于滤除所述生活污水中大于预设体积的漂浮物;所述调节池用于存储所述格栅井滤除漂浮物后的所述生活污水,为所述分解装置提供稳定水质和水量。In the above-mentioned domestic sewage treatment system, preferably, the buffer device includes a grid well and a regulating tank; the grid well is used to filter out floating objects larger than a preset volume in the domestic sewage; The domestic sewage after the grid well has been filtered to filter the floating objects is stored to provide stable water quality and quantity for the decomposition device.

在上述生活污水处理系统中,优选的,所述分解装置包含初沉池、厌氧水解池、一级接触氧化池和二级接触氧化池;所述初沉池与所述缓冲装置相连,用于对所述缓存装置处理后的生活污水进行预曝气和初步沉淀处理;所述厌氧水解池与所述初沉池相连,用于对所述初沉池处理后的生活污水进行水解和酸化反应,将生活污水中的有机固体及预定类别的有机物分解为小分子溶解性有机物;所述一级接触氧化池与所述厌氧水解池相连,所述二级接触氧化池与所述一级接触氧化池相连,所述一级接触氧化池和所述二级接触氧化池用于通过膜生物的代谢作用将所述厌氧水解池处理后的生活污水中的有机污染物转化为氨氮,再通过好氧硝化和缺氧反硝化过程去除所述氨氮。In the above-mentioned domestic sewage treatment system, preferably, the decomposition device includes a primary sedimentation tank, an anaerobic hydrolysis tank, a primary contact oxidation tank, and a secondary contact oxidation tank; the primary sedimentation tank is connected to the buffer device, and uses The anaerobic hydrolysis tank is connected with the primary sedimentation tank, and is used for hydrolysis and preliminary sedimentation of the domestic sewage treated by the primary sedimentation tank. The acidification reaction decomposes the organic solids and predetermined types of organic matter in the domestic sewage into small-molecule dissolved organic matter; the first-stage contact oxidation tank is connected with the anaerobic hydrolysis tank, and the second-stage contact oxidation tank is connected with the first-stage contact oxidation tank. The first-level contact oxidation tank and the second-level contact oxidation tank are used to convert the organic pollutants in the domestic sewage treated by the anaerobic hydrolysis tank into ammonia nitrogen through the metabolism of membrane organisms, The ammonia nitrogen is then removed through aerobic nitrification and anoxic denitrification processes.

在上述生活污水处理系统中,优选的,所述回用装置包含二沉池、消毒池和污泥池;所述二沉池分别与所述二级接触氧化池和所述厌氧水解池相连,用于对所述二级接触氧化池处理后的生活污水进行固液分离处理,获得污泥、脱落生物膜和生活污水;将所述脱落生物膜输入至所述厌氧水解池进行污泥回用;所述消毒池与所述二沉池相连,用于对所述二沉池处理后的生活污水进行消毒处理;所述污泥池分别与所述二沉池和所述初沉池相连,用于存放所述二沉池分离的所述污泥,并将所述污泥沉淀溢出的生活污水输入至所述初沉池。In the above-mentioned domestic sewage treatment system, preferably, the recycling device includes a secondary sedimentation tank, a disinfection tank and a sludge tank; the secondary sedimentation tank is respectively connected with the secondary contact oxidation tank and the anaerobic hydrolysis tank , used for solid-liquid separation treatment of the domestic sewage treated in the secondary contact oxidation tank to obtain sludge, shed biofilm and domestic sewage; input the shed biofilm into the anaerobic hydrolysis tank for sludge treatment Reuse; the disinfection tank is connected with the secondary sedimentation tank, and is used to disinfect the domestic sewage treated by the secondary sedimentation tank; the sludge tank is respectively connected with the secondary sedimentation tank and the primary sedimentation tank connected to each other for storing the sludge separated by the secondary sedimentation tank, and inputting the domestic sewage overflowing from the sludge precipitation to the primary sedimentation tank.

在上述生活污水处理系统中,优选的,所述系统还包含曝气风机,所述曝气风机与所述初沉池、所述一级接触氧化池、所述二级接触氧化池和所述回用装置相连,用于对所述分解装置中生活污水的初步沉淀处理、将所述有机物污染物转化为氨氮和去除所述氨氮阶段的生活污水进行曝风处理;以及,对所述输出装置中进行活性炭过滤的生活污水进行曝风处理。In the above-mentioned domestic sewage treatment system, preferably, the system further comprises an aeration fan, and the aeration fan is connected to the primary sedimentation tank, the primary contact oxidation tank, the secondary contact oxidation tank and the The recycling device is connected to the precipitation treatment of the domestic sewage in the decomposition device, and the organic pollutants are converted into ammonia nitrogen and the domestic sewage in the ammonia nitrogen removal stage is subjected to aeration treatment; and, the output device is used for aeration treatment. The domestic sewage that is filtered by activated carbon is subjected to aeration treatment.

在上述生活污水处理系统中,优选的,所述系统还包含转动机械组,所述转动机械组包含污水提升泵、污泥回流泵、中间水泵和回用水泵;所述污水提升泵用于将所述缓冲装置中存储的生活污水泵入所述分解装置;所述污泥回流泵用于将所述脱落生物膜泵入至所述分解装置进行污泥回用;所述中间水泵用于将所述回用装置中消毒处理后的生活污水泵入至所述输出装置进行活性炭过滤;所述回用水泵用于将所述输出装置中通过活性炭过滤后的生活污水泵入至外部用水机构和/或泵入至所述输出装置中活性炭过滤的设备提供反洗用水。In the above-mentioned domestic sewage treatment system, preferably, the system further includes a rotating mechanical group, and the rotating mechanical group includes a sewage lifting pump, a sludge return pump, an intermediate water pump and a recycling water pump; the sewage lifting pump is used to The domestic sewage stored in the buffer device is pumped into the decomposition device; the sludge return pump is used to pump the shed biofilm into the decomposition device for sludge reuse; the intermediate water pump is used to The sterilized domestic sewage in the recycling device is pumped into the output device for activated carbon filtration; the recycling water pump is used to pump the domestic sewage filtered by the activated carbon in the output device into an external water-use mechanism and / or pumped into the activated carbon filtering equipment in the output device to provide backwash water.

在上述生活污水处理系统中,优选的,所述系统还包含控制装置,所述控制装置包含污水提升泵控制模块、曝气风机控制模块、污泥回流泵控制模块和回用水泵控制模块;所述污水提升泵控制模块用于当所述缓冲装置内存储的生活污水高于第一预定水量时,开启所述污水提升泵向所述分解装置泵入生活污水;当所述缓冲装置内存储的生活污水低于第二预定水量时,关闭所述污水提升泵,停止向所述分解装置泵入生活污水;所述曝气风机控制模块用于根据接收到的控制指令,控制所述曝气风机对所述分解装置中生活污水的初步沉淀处理、将所述有机物污染物转化为氨氮和去除所述氨氮阶段的生活污水进行曝风处理;和/或,对所述输出装置中进行活性炭过滤的生活污水进行曝风处理;所述污泥回流泵控制模块用于在所述污水提升泵运行第一定时间周期后,控制所述污泥回流泵启动运行第二时间周期;以及,当所述污水提升泵停止运行后,停止所述污泥回流泵运行;所述回用水泵控制模块用于根据接收到的控制指令控制所述回用水泵将所述输出装置中通过活性炭过滤后的生活污水泵入至外部用水机构和/或泵入至所述输出装置中活性炭过滤的设备提供反洗用水。In the above-mentioned domestic sewage treatment system, preferably, the system further includes a control device, and the control device includes a sewage lift pump control module, an aeration fan control module, a sludge return pump control module and a reuse water pump control module; The sewage lifting pump control module is used to start the sewage lifting pump to pump domestic sewage into the decomposition device when the domestic sewage stored in the buffer device is higher than the first predetermined water amount; When the domestic sewage is lower than the second predetermined water volume, the sewage lifting pump is turned off, and the domestic sewage is stopped to be pumped into the decomposition device; the aeration fan control module is used to control the aeration fan according to the received control command. Carry out aeration treatment on the preliminary precipitation treatment of domestic sewage in the decomposition device, convert the organic pollutants into ammonia nitrogen and remove the domestic sewage in the ammonia nitrogen stage; and/or, filter the activated carbon in the output device. The domestic sewage is subjected to aeration treatment; the sludge return pump control module is configured to control the sludge return pump to start running for a second time period after the sewage lift pump operates for a first time period; After the sewage lift pump stops running, stop the sludge return pump; the reuse water pump control module is used to control the reuse water pump according to the received control command to filter the domestic sewage filtered by the activated carbon in the output device Backwash water is provided by pumping to an external water use mechanism and/or pumping to an activated carbon filter in the output device.

本发明还提供一种生活污水处理系统的控制方法,所述方法包含:接收生活污水并滤除所述生活污水中大于预设体积的漂浮物;对生活污水进行初步沉淀处理,对处理后的生活污水进行水解反应和酸化反应,将生活污水中的有机固体及预定类别的有机物分解为小分子溶解性的有机物污染物;通过膜生物的代谢作用将所述有机物污染物转化为氨氮,再通过好氧硝化和缺氧反硝化过程去除所述氨氮;对去除所述氨氮后的生活污水进行固液分离处理,获得脱落生物膜和生活污水;将所述脱落生物膜回流复用,对分离处理获得的生活污水进行消毒处理后进行活性炭过滤,获得输出用水;将所述输出用水输出至外部用水机构。The present invention also provides a control method for a domestic sewage treatment system, the method comprising: receiving domestic sewage and filtering out floating objects larger than a preset volume in the domestic sewage; performing preliminary sedimentation treatment on the domestic sewage, and treating the treated sewage The domestic sewage undergoes a hydrolysis reaction and an acidification reaction to decompose the organic solids and predetermined types of organic substances in the domestic sewage into small-molecule-soluble organic pollutants; the organic pollutants are converted into ammonia nitrogen through the metabolism of membrane organisms, and then pass through The ammonia nitrogen is removed by aerobic nitrification and anoxic denitrification; the solid-liquid separation treatment is performed on the domestic sewage after removing the ammonia nitrogen to obtain a detached biofilm and domestic sewage; the detached biofilm is returned for reuse, and the separation treatment is performed The obtained domestic sewage is disinfected and then filtered with activated carbon to obtain output water; the output water is output to an external water use mechanism.

在上述控制方法中,优选的,所述方法还包含:在生活污水的初步沉淀处理过程中、将所述有机物污染物转化为氨氮和去除所述氨氮过程中对所述生活污水进行曝风处理;以及,在生活污水进行活性炭过滤过程中对所述生活污水进行曝风处理。In the above control method, preferably, the method further comprises: in the process of preliminary precipitation treatment of domestic sewage, converting the organic pollutants into ammonia nitrogen and removing the ammonia nitrogen, performing aeration treatment on the domestic sewage and, performing air aeration treatment on the domestic sewage during the activated carbon filtration process of the domestic sewage.

在上述控制方法中,优选的,所述方法还包含:当所述缓冲装置内存储的生活污水高于第一预定水量时,向所述分解装置泵入生活污水;当所述缓冲装置内存储的生活污水低于第二预定水量时,停止向所述分解装置泵入生活污水。In the above control method, preferably, the method further includes: when the domestic sewage stored in the buffer device is higher than a first predetermined amount of water, pumping domestic sewage into the decomposition device; when the buffer device stores domestic sewage; When the domestic sewage is lower than the second predetermined amount of water, the pumping of domestic sewage into the decomposition device is stopped.

在上述控制方法中,优选的,将所述输出用水输出至外部用水机构还包含:通过所述输出用水为活性炭过滤设备提供反洗用水。In the above control method, preferably, outputting the output water to an external water use mechanism further comprises: providing backwash water for the activated carbon filter device through the output water.

本发明还提供一种电子设备,包括存储器、处理器及存储在存储器上并可在处理器上运行的计算机程序,所述处理器执行所述计算机程序时实现上述方法。The present invention also provides an electronic device, comprising a memory, a processor and a computer program stored in the memory and running on the processor, the processor implementing the above method when the computer program is executed.

本发明还提供一种计算机可读存储介质,所述计算机可读存储介质存储有执行上述方法的计算机程序。The present invention also provides a computer-readable storage medium storing a computer program for executing the above method.

本发明的有益技术效果在于:实现了生活污水处理污水提升、曝气、污泥回流、过滤器运行反洗、净水回用等功能协调、连续、自动运行,提高了生活污水处理效率、降低了运行成本。The beneficial technical effects of the present invention are as follows: the coordinated, continuous and automatic operation of functions such as sewage lifting, aeration, sludge return, filter operation backwashing, and purified water reuse in domestic sewage treatment is realized, the efficiency of domestic sewage treatment is improved, and the running costs.

附图说明Description of drawings

此处所说明的附图用来提供对本发明的进一步理解,构成本申请的一部分,并不构成对本发明的限定。在附图中:The accompanying drawings described herein are used to provide a further understanding of the present invention, and constitute a part of the present application, and do not constitute a limitation to the present invention. In the attached image:

图1为本发明一实施例所提供的生活污水处理系统的原理示意图;1 is a schematic diagram of the principle of a domestic sewage treatment system provided by an embodiment of the present invention;

图2为本发明一实施例所提供的生活污水处理系统的应用结构示意图;2 is a schematic diagram of an application structure of a domestic sewage treatment system provided by an embodiment of the present invention;

图3为本发明一实施例所提供的生活污水处理系统的控制方法的流程示意图;3 is a schematic flowchart of a control method of a domestic sewage treatment system provided by an embodiment of the present invention;

图4为本发明一实施例所提供的曝气风机的工作逻辑流程示意图;4 is a schematic diagram of a working logic flow diagram of an aeration fan provided by an embodiment of the present invention;

图5为本发明一实施例所提供的生活污水提升泵的工作逻辑流程示意图;FIG. 5 is a schematic flowchart of the working logic of the domestic sewage lift pump provided by an embodiment of the present invention;

图6为本发明一实施例所提供的污泥回流泵的工作逻辑流程示意图;FIG. 6 is a schematic flowchart of the working logic of the sludge return pump provided by an embodiment of the present invention;

图7为本发明一实施例所提供的回用水泵的工作逻辑流程示意图;FIG. 7 is a schematic flow chart of the working logic of the reuse water pump provided by an embodiment of the present invention;

图8为本发明一实施例所提供的活性炭过滤器的工作逻辑流程示意图;FIG. 8 is a schematic flowchart of the working logic of an activated carbon filter provided by an embodiment of the present invention;

图9为本发明一实施例所提供的电子设备的结构示意图。FIG. 9 is a schematic structural diagram of an electronic device provided by an embodiment of the present invention.

具体实施方式Detailed ways

以下将结合附图及实施例来详细说明本发明的实施方式,借此对本发明如何应用技术手段来解决技术问题,并达成技术效果的实现过程能充分理解并据以实施。需要说明的是,只要不构成冲突,本发明中的各个实施例及各实施例中的各个特征可以相互结合,所形成的技术方案均在本发明的保护范围之内。The embodiments of the present invention will be described in detail below with reference to the accompanying drawings and examples, so as to fully understand and implement the implementation process of how the present invention applies technical means to solve technical problems and achieve technical effects. It should be noted that, as long as there is no conflict, each embodiment of the present invention and each feature of each embodiment can be combined with each other, and the formed technical solutions all fall within the protection scope of the present invention.

另外,在附图的流程图示出的步骤可以在诸如一组计算机可执行指令的计算机系统中执行,并且,虽然在流程图中示出了逻辑顺序,但是在某些情况下,可以以不同于此处的顺序执行所示出或描述的步骤。Additionally, the steps shown in the flowcharts of the figures may be performed in a computer system, such as a set of computer-executable instructions, and, although shown in a logical order in the flowcharts, in some cases, may be executed differently The steps shown or described are performed in the order shown herein.

请参考图1所示,本发明所提供的一种本发明所提供的生活污水处理系统,所述系统包含缓冲装置、分解装置、回用装置和输出装置;所述缓冲装置用于存储接收到的生活污水,并滤除所述生活污水中大于预设体积的漂浮物;所述分解装置用于对所述缓存装置滤除处理后的生活污水进行初步沉淀处理,对处理后的生活污水进行水解反应和酸化反应,将生活污水中的有机固体及预定类别的有机物分解为小分子溶解性的有机物污染物;通过膜生物的代谢作用将所述有机物污染物转化为氨氮,再通过好氧硝化和缺氧反硝化过程去除所述氨氮,输出去除所述氨氮后的生活污水;所述回用装置用于对所述分解装置处理后的生活污水进行固液分离处理,获得脱落生物膜和生活污水;将所述脱落生物膜输入至所述分解装置进行污泥回用,对分离处理获得的生活污水进行消毒处理后输出;所述输出装置用于将所述回用装置输出的生活污水进行活性炭过滤后输出至外部用水机构。在该实施例中,所述缓冲装置可与生活污水收集结构相连,接收外部输入的生活污水,其后,利用分解装置、回用装置等处理,获得较为干净的生活用水,最后经过输出装置进一步过滤后即可交由外部用水机构使用;期间,各装置之间均采用自动化衔接控制,例如现有技术中的DCS控制系统予以综合调控,其控制逻辑将在后续实施例中详细说明,在此就不再一一详述。Please refer to FIG. 1 , a domestic sewage treatment system provided by the present invention, the system includes a buffer device, a decomposition device, a recycling device and an output device; the buffer device is used for storing received The domestic sewage is filtered out, and the floating objects larger than the preset volume in the domestic sewage are filtered out; the decomposition device is used to perform preliminary precipitation treatment on the domestic sewage filtered and treated by the buffer device, and the treated domestic sewage is used for preliminary precipitation treatment. Hydrolysis reaction and acidification reaction, decompose organic solids and predetermined types of organic substances in domestic sewage into small-molecule-soluble organic pollutants; through the metabolism of membrane organisms, the organic pollutants are converted into ammonia nitrogen, and then through aerobic nitrification and the anoxic denitrification process to remove the ammonia nitrogen, and output the domestic sewage after removing the ammonia nitrogen; the reuse device is used to perform solid-liquid separation treatment on the domestic sewage treated by the decomposition device to obtain detached biofilm and domestic sewage. sewage; inputting the shed biofilm into the decomposition device for sludge reuse, and sterilizing the domestic sewage obtained by separation treatment and outputting; the output device is used to process the domestic sewage output from the recycling device. The activated carbon is filtered and output to the external water use mechanism. In this embodiment, the buffer device can be connected with the domestic sewage collection structure to receive the domestic sewage input from the outside, and then use the decomposition device, the reuse device, etc. to process it to obtain relatively clean domestic water, and finally pass through the output device for further treatment. After filtering, it can be handed over to the external water use agency; during the period, automatic connection control is adopted between each device, for example, the DCS control system in the prior art is comprehensively regulated, and its control logic will be described in detail in the subsequent embodiments, here I won't go into details.

在上述实施例中,所述缓冲装置可包含格栅井和调节池;所述格栅井用于滤除所述生活污水中大于预设体积的漂浮物;所述调节池用于存储所述格栅井滤除漂浮物后的所述生活污水,为所述分解装置提供稳定水质和水量。所述分解装置可包含初沉池、厌氧水解池、一级接触氧化池和二级接触氧化池;所述初沉池与所述缓冲装置相连,用于对所述缓存装置处理后的生活污水进行预曝气和初步沉淀处理;所述厌氧水解池与所述初沉池相连,用于对所述初沉池处理后的生活污水进行水解和酸化反应,将生活污水中的有机固体及预定类别的有机物分解为小分子溶解性有机物;所述一级接触氧化池与所述厌氧水解池相连,所述二级接触氧化池与所述一级接触氧化池相连,所述一级接触氧化池和所述二级接触氧化池用于通过膜生物的代谢作用将所述厌氧水解池处理后的生活污水中的有机污染物转化为氨氮,再通过好氧硝化和缺氧反硝化过程去除所述氨氮。所述回用装置包含二沉池、消毒池和污泥池;所述二沉池分别与所述二级接触氧化池和所述厌氧水解池相连,用于对所述二级接触氧化池处理后的生活污水进行固液分离处理,获得污泥、脱落生物膜和生活污水;将所述脱落生物膜输入至所述厌氧水解池进行污泥回用;所述消毒池与所述二沉池相连,用于对所述二沉池处理后的生活污水进行消毒处理;所述污泥池分别与所述二沉池和所述初沉池相连,用于存放所述二沉池分离的所述污泥,并将所述污泥沉淀溢出的生活污水输入至所述初沉池。In the above embodiment, the buffer device may include a grid well and a regulating pool; the grid well is used to filter out the floating objects larger than a preset volume in the domestic sewage; the regulating pool is used to store the The grid well filters the domestic sewage after the floating matter is filtered, and provides stable water quality and quantity for the decomposition device. The decomposition device may include a primary sedimentation tank, an anaerobic hydrolysis tank, a primary contact oxidation tank, and a secondary contact oxidation tank; the primary sedimentation tank is connected to the buffer device, and is used for life after the buffer device is processed. The sewage is subjected to pre-aeration and preliminary precipitation treatment; the anaerobic hydrolysis tank is connected to the primary sedimentation tank, and is used for hydrolysis and acidification of the domestic sewage treated by the primary sedimentation tank, and the organic solids in the domestic sewage are removed. and predetermined categories of organic matter are decomposed into small molecule dissolved organic matter; the first-stage contact oxidation tank is connected with the anaerobic hydrolysis tank, the second-level contact oxidation tank is connected with the first-level contact oxidation tank, the first-level contact oxidation tank is connected with the first-level contact oxidation tank The contact oxidation tank and the secondary contact oxidation tank are used to convert the organic pollutants in the domestic sewage treated by the anaerobic hydrolysis tank into ammonia nitrogen through the metabolism of membrane organisms, and then through aerobic nitrification and anoxic denitrification The process removes the ammonia nitrogen. The recycling device includes a secondary sedimentation tank, a disinfection tank and a sludge tank; the secondary sedimentation tank is respectively connected with the secondary contact oxidation tank and the anaerobic hydrolysis tank, and is used for the secondary contact oxidation tank. The treated domestic sewage is subjected to solid-liquid separation treatment to obtain sludge, exfoliated biofilm and domestic sewage; the exfoliated biofilm is input into the anaerobic hydrolysis tank for sludge reuse; the disinfection tank and the two The sedimentation tank is connected to the secondary sedimentation tank for disinfection treatment; the sludge tank is connected to the secondary sedimentation tank and the primary sedimentation tank, respectively, and is used to store the secondary sedimentation tank for separation the sludge, and the domestic sewage overflowed by the sludge precipitation is input to the primary sedimentation tank.

综上,在实际工作中,本发明所提供的生活污水处理系统在结构上可包含格栅井、污水调节池、初沉池、厌氧水解池、一级接触氧化池、二级接触氧化池、二沉池、消毒池、污泥池、中间水池、活性炭过滤器、回用水池;工业产区生活污水来水进入格栅井,对水中大颗粒杂物进行截留过滤,出水进入污水调节池。通过污水提升泵将调节池中污水打入初沉池,对其进行初沉及预曝气,初沉池出水由顶部溢流进入厌氧水解池,在厌氧水解池中将大分子有机物转化为小分子物质,减轻后续处理负荷,降解部分COD,出水溢流至一级接触氧化池、二级接触氧化池。接触氧化池采用技术先进的膜生物反应器,利用生物膜的代谢作用使有机污染物首先转化为氨氮,同时通过好氧硝化和缺氧反硝化过程既去除有机物又去除了氨氮。接触氧化池内置弹性立体填料,比表面积大,使单位体积内保持较高的生物量,且活性较高,能高速去除有机污染物,在同一水量水质的条件下,占地面积小。二级接触氧化池的出水进入二沉池进行固液分离,二沉池主要功能是去除接触氧化池出水中带出的脱落生物膜。二沉池污泥通过污泥回流泵将污泥输送至厌氧水解池完成污泥回流,同时二沉池部分污泥落入污泥池,污泥池上部清水溢流回到初沉池,底部污泥定期向外运送。二沉池出水溢流至消毒池进行投氯片消毒。消毒池出水溢流至中间水池。通过中间水泵将中间水池提升进入活性炭过滤器进行过滤,过滤器产水进入回用水池,通过回用水泵进行最终的净水回用。To sum up, in practical work, the domestic sewage treatment system provided by the present invention can structurally include grid wells, sewage conditioning tanks, primary sedimentation tanks, anaerobic hydrolysis tanks, primary contact oxidation tanks, and secondary contact oxidation tanks , secondary sedimentation tank, disinfection tank, sludge tank, intermediate tank, activated carbon filter, reuse tank; domestic sewage from industrial production areas enters the grid well, and the large particles of debris in the water are intercepted and filtered, and the effluent enters the sewage conditioning tank . The sewage in the adjustment tank is pumped into the primary sedimentation tank by the sewage lift pump, and the primary sedimentation and pre-aeration are carried out. It is a small molecular substance, reducing the load of subsequent treatment, degrading part of the COD, and the effluent overflows to the first-level contact oxidation tank and the second-level contact oxidation tank. The contact oxidation tank adopts a technologically advanced membrane bioreactor, which uses the metabolism of the biofilm to convert organic pollutants into ammonia nitrogen first, and at the same time removes both organic matter and ammonia nitrogen through aerobic nitrification and anoxic denitrification. The contact oxidation tank has a built-in elastic three-dimensional filler, which has a large specific surface area, which can maintain a high biomass per unit volume, and has a high activity, which can remove organic pollutants at a high speed. The effluent of the secondary contact oxidation tank enters the secondary sedimentation tank for solid-liquid separation. The main function of the secondary sedimentation tank is to remove the shed biofilm brought out by the effluent of the contact oxidation tank. The sludge in the secondary sedimentation tank is transported to the anaerobic hydrolysis tank through the sludge return pump to complete the sludge return. Bottom sludge is regularly transported outwards. The effluent from the secondary sedimentation tank overflows to the disinfection tank for disinfection by chlorine tablets. The effluent from the disinfection tank overflows to the intermediate pool. The intermediate water tank is lifted into the activated carbon filter by the intermediate water pump for filtration, and the water produced by the filter enters the recycling water tank, and the final purified water is reused by the recycling water pump.

在本发明一实施例中,所述系统还包含转动机械组,所述转动机械组包含污水提升泵、污泥回流泵、中间水泵和回用水泵;所述污水提升泵用于将所述缓冲装置中存储的生活污水泵入所述分解装置;所述污泥回流泵用于将所述脱落生物膜泵入至所述分解装置进行污泥回用;所述中间水泵用于将所述回用装置中消毒处理后的生活污水泵入至所述输出装置进行活性炭过滤;所述回用水泵用于将所述输出装置中通过活性炭过滤后的生活污水泵入至外部用水机构和/或泵入至所述输出装置中活性炭过滤的设备提供反洗用水。再请参考图2所示,上述结构在功能上可分为四部分,具体如下:In an embodiment of the present invention, the system further includes a rotating mechanical group, and the rotating mechanical group includes a sewage lifting pump, a sludge return pump, an intermediate water pump and a recycling water pump; the sewage lifting pump is used for the buffering The domestic sewage stored in the device is pumped into the decomposition device; the sludge return pump is used for pumping the exfoliated biofilm into the decomposition device for sludge reuse; the intermediate water pump is used for the return of the sludge. The domestic sewage after the disinfection treatment in the device is pumped into the output device for activated carbon filtration; the reuse water pump is used to pump the domestic sewage filtered by the activated carbon in the output device into an external water use mechanism and/or pump The activated carbon filtering equipment fed into the output device provides backwash water. Referring to Figure 2 again, the above structure can be functionally divided into four parts, as follows:

一、格栅井、调节池;1. Grill wells, regulating pools;

由于生活污水中含有一定量的大块漂浮物(如手纸、菜根、塑料袋等),因此先用格栅予以拦截下来,以保证后续处理设备的正常运行,格栅设计在调节池的入口。调节池其功能有以下二个方面:一、作为蓄水池进行污水储存;二、水质缓冲,使厌氧-接触氧化处理设备的进水水质和水量稳定。Since domestic sewage contains a certain amount of large floating objects (such as toilet paper, vegetable roots, plastic bags, etc.), it is intercepted by a grille to ensure the normal operation of the subsequent treatment equipment. The grille is designed at the entrance of the adjustment tank. The function of the regulating tank has the following two aspects: first, as a reservoir for sewage storage; second, water quality buffer, so that the water quality and water quantity of the anaerobic-contact oxidation treatment equipment are stable.

二、初沉池、厌氧水解池、一级二级接触氧化池;2. Primary sedimentation tank, anaerobic hydrolysis tank, primary and secondary contact oxidation tank;

初沉池:进行污水预曝气及初步沉淀,同时回收污泥池溢流污水。Primary sedimentation tank: carry out pre-aeration and preliminary sedimentation of sewage, and recycle the overflow sewage of sludge tank at the same time.

厌氧水解池:进行水解、酸化反应,将污水中的有机固体及不易生物降解的有机物分解为小分子溶解性有机物,减轻后续处理负荷,降解部分COD。Anaerobic hydrolysis tank: carry out hydrolysis and acidification reactions, decompose organic solids and non-biodegradable organic substances in sewage into small molecular dissolved organic substances, reduce the subsequent treatment load, and degrade part of COD.

一级、二级接触氧化池:本单元采用技术先进的膜生物反应器,利用生物膜的代谢作用使有机污染物首先转化为氨氮,同时通过好氧硝化和缺氧反硝化过程既去除有机物又去除了氨氮。生物接触氧化池内置弹性立体填料,比表面积大,使单位体积内保持较高的生物量,且活性较高,能高速去除有机污染物,在同一水量水质的条件下,占地面积小。Primary and secondary contact oxidation tanks: This unit adopts advanced membrane bioreactors, which utilize the metabolism of biofilms to first convert organic pollutants into ammonia nitrogen, and at the same time, through aerobic nitrification and anoxic denitrification processes, both organic matter and Ammonia nitrogen is removed. The biological contact oxidation tank has a built-in elastic three-dimensional filler, which has a large specific surface area, which can maintain a high biomass per unit volume, and has a high activity, which can remove organic pollutants at a high speed.

三、二沉池、污泥回流、消毒池、污泥池;3. Secondary sedimentation tank, sludge return, disinfection tank, sludge tank;

二沉池:进行固液分离,二沉池主要功能是去除接触氧化池出水中带出的脱落生物膜。Secondary sedimentation tank: For solid-liquid separation, the main function of the secondary sedimentation tank is to remove the exfoliated biofilm brought out from the effluent of the contact oxidation tank.

污泥回流:将二沉池底部沉积的污泥(脱落生物膜)通过污泥回流泵输送至厌氧水解池进行污泥回用。Sludge return: The sludge deposited at the bottom of the secondary sedimentation tank (falling off biofilm) is transported to the anaerobic hydrolysis tank through the sludge return pump for sludge reuse.

消毒池:人工定期投加氯片,进行消毒。Disinfection pool: Manually add chlorine tablets on a regular basis for disinfection.

污泥池:进行污泥暂时储存,底部污泥定期外运,上部污水溢流回到初沉池。Sludge tank: Temporarily store the sludge, the bottom sludge is regularly shipped out, and the upper sewage overflows back to the primary sedimentation tank.

四、中间水池、活性炭过滤器、回用水池;4. Intermediate pool, activated carbon filter, reuse pool;

中间水池:消毒池出水进入中间水池。Intermediate pool: The water from the disinfection pool enters the intermediate pool.

活性炭过滤器:活性炭过滤器能实现过滤及有机物吸附功能,通过中间水泵将中间水池中水输送至活性炭过滤器进行过滤,降低水中悬浮物及部分有机物。Activated carbon filter: The activated carbon filter can realize the functions of filtration and organic matter adsorption. The water in the intermediate pool is transported to the activated carbon filter through the intermediate water pump for filtration to reduce suspended solids and some organic matter in the water.

回用水池:过滤器出水进入回用水池,通过回用水泵进行净水对外输送回用,同时给过滤器提供反洗用水。Reuse pool: The effluent from the filter enters the recycle pool, and the purified water is transported to the outside for reuse through the reuse pump, and backwash water is provided to the filter at the same time.

在本发明一实施例中,所述系统还包含曝气风机,所述曝气风机与所述初沉池、所述一级接触氧化池、所述二级接触氧化池和所述回用装置相连,用于对所述分解装置中生活污水的初步沉淀处理、将所述有机物污染物转化为氨氮和去除所述氨氮阶段的生活污水进行曝风处理;以及,对所述输出装置中进行活性炭过滤的生活污水进行曝风处理。在本发明另一实施例中,所述系统还包含控制装置,所述控制装置包含污水提升泵控制模块、曝气风机控制模块、污泥回流泵控制模块和回用水泵控制模块;所述污水提升泵控制模块用于当所述缓冲装置内存储的生活污水高于第一预定水量时,开启所述污水提升泵向所述分解装置泵入生活污水;当所述缓冲装置内存储的生活污水低于第二预定水量时,关闭所述污水提升泵,停止向所述分解装置泵入生活污水;所述曝气风机控制模块用于根据接收到的控制指令,控制所述曝气风机对所述分解装置中生活污水的初步沉淀处理、将所述有机物污染物转化为氨氮和去除所述氨氮阶段的生活污水进行曝风处理;和/或,对所述输出装置中进行活性炭过滤的生活污水进行曝风处理;所述污泥回流泵控制模块用于在所述污水提升泵运行第一定时间周期后,控制所述污泥回流泵启动运行第二时间周期;以及,当所述污水提升泵停止运行后,停止所述污泥回流泵运行;所述回用水泵控制模块用于根据接收到的控制指令控制所述回用水泵将所述输出装置中通过活性炭过滤后的生活污水泵入至外部用水机构和/或泵入至所述输出装置中活性炭过滤的设备提供反洗用水。由此,在上述实施例的全过程中,曝气风机定期对初沉池、一级氧化池、二级氧化池进行曝气处理。综上,在实际工作中,所述控制装置可包含五个控制模块,每个模块均有对应的控制逻辑,具体将在后续实施例中详述,在此就不再一一说明。In an embodiment of the present invention, the system further includes an aeration fan, the aeration fan is connected to the primary sedimentation tank, the primary contact oxidation tank, the secondary contact oxidation tank, and the recycling device is connected to the precipitation treatment of the domestic sewage in the decomposition device, the conversion of the organic pollutants into ammonia nitrogen and the aeration treatment of the domestic sewage in the ammonia nitrogen stage; and the activated carbon in the output device. The filtered domestic sewage is subjected to aeration treatment. In another embodiment of the present invention, the system further includes a control device, the control device includes a sewage lift pump control module, an aeration fan control module, a sludge return pump control module and a recycling water pump control module; the sewage The lift pump control module is used to turn on the sewage lift pump to pump domestic sewage to the decomposition device when the domestic sewage stored in the buffer device is higher than a first predetermined amount of water; when the domestic sewage stored in the buffer device is When the water volume is lower than the second predetermined amount, the sewage lifting pump is turned off, and domestic sewage is stopped to be pumped into the decomposition device; the aeration fan control module is used to control the aeration fan to the Preliminary precipitation treatment of domestic sewage in the decomposition device, converting the organic pollutants into ammonia nitrogen and removing the domestic sewage in the ammonia nitrogen stage for aeration treatment; and/or, performing activated carbon filtration in the output device for domestic sewage. performing aeration treatment; the sludge return pump control module is configured to control the sludge return pump to start running for a second time period after the sewage lifting pump operates for a first certain period of time; and, when the sewage lifts After the pump stops running, the operation of the sludge return pump is stopped; the recycling water pump control module is used to control the recycling water pump to pump the domestic sewage filtered by the activated carbon in the output device according to the received control command. Backwash water is supplied to an external water use mechanism and/or to a device that is pumped into the output device for activated carbon filtration. Therefore, in the whole process of the above-mentioned embodiment, the aeration fan regularly aerates the primary sedimentation tank, the primary oxidation tank, and the secondary oxidation tank. To sum up, in actual work, the control device may include five control modules, each of which has a corresponding control logic, which will be described in detail in subsequent embodiments, and will not be described one by one here.

请参考图3所示,本发明还提供一种生活污水处理系统的控制方法,所述方法包含:Please refer to FIG. 3 , the present invention also provides a control method of a domestic sewage treatment system, the method comprising:

S301接收生活污水并滤除所述生活污水中大于预设体积的漂浮物;S301 Receive domestic sewage and filter out floating objects larger than a preset volume in the domestic sewage;

S302对生活污水进行初步沉淀处理,对处理后的生活污水进行水解反应和酸化反应,将生活污水中的有机固体及预定类别的有机物分解为小分子溶解性的有机物污染物;S302 performs preliminary precipitation treatment on the domestic sewage, performs hydrolysis reaction and acidification reaction on the treated domestic sewage, and decomposes organic solids and predetermined types of organic matter in the domestic sewage into small-molecule-soluble organic pollutants;

S303通过膜生物的代谢作用将所述有机物污染物转化为氨氮,再通过好氧硝化和缺氧反硝化过程去除所述氨氮;S303 converts the organic pollutants into ammonia nitrogen through the metabolism of membrane organisms, and then removes the ammonia nitrogen through aerobic nitrification and anoxic denitrification;

S304对去除所述氨氮后的生活污水进行固液分离处理,获得脱落生物膜和生活污水;S304 performs solid-liquid separation treatment on the domestic sewage after the ammonia nitrogen is removed to obtain detached biofilm and domestic sewage;

S305将所述脱落生物膜回流复用,对分离处理获得的生活污水进行消毒处理后进行活性炭过滤,获得输出用水;S305, the detached biofilm is recycled and reused, and the domestic sewage obtained by the separation treatment is disinfected and filtered with activated carbon to obtain output water;

S306将所述输出用水输出至外部用水机构。S306 outputs the output water to an external water use mechanism.

在上述实施例中,所述方法还可包含:在生活污水的初步沉淀处理过程中、将所述有机物污染物转化为氨氮和去除所述氨氮过程中对所述生活污水进行曝风处理;以及,在生活污水进行活性炭过滤过程中对所述生活污水进行曝风处理。具体的可参考图4所示,在曝风处理过程中主要可分为两种模式,即接触氧化处理供气和活性炭过滤器擦洗用气;其中,接触氧化处理供气模式中,生活污水提升泵已运行时(当生活污水提升泵包含多台时,任一生活污水提升泵)启动联锁投入状态下的曝气风机,生活污水提升泵(所有生活污水提升泵)均停时停止联锁投入状态下的曝气风机。In the above-mentioned embodiment, the method may further include: in the process of preliminary precipitation treatment of domestic sewage, during the process of converting the organic pollutants into ammonia nitrogen and removing the ammonia nitrogen, performing aeration treatment on the domestic sewage; and , the domestic sewage is subjected to aeration treatment during the activated carbon filtration process of the domestic sewage. For details, please refer to Figure 4. In the aeration treatment process, it can be divided into two modes, namely contact oxidation treatment gas supply and activated carbon filter scrubbing gas; among them, in the contact oxidation treatment gas supply mode, the domestic sewage is upgraded When the pump is running (when there are multiple domestic sewage lifting pumps, any domestic sewage lifting pump) starts the aeration fan in the interlocking state, and stops the interlocking when the domestic sewage lifting pumps (all domestic sewage lifting pumps) are stopped. The aeration fan in the input state.

在本发明一实施例中,所述方法还包含:当所述缓冲装置内存储的生活污水高于第一预定水量时,向所述分解装置泵入生活污水;当所述缓冲装置内存储的生活污水低于第二预定水量时,停止向所述分解装置泵入生活污水。实际工作中,该流程即为污水提升泵的运行控制逻辑,请参考图5所示,以三台泵设备为例,该污水提升泵的运行基准在于调节池的液位高度,调节池液位高(L≥3.0m)时启动联锁投入状态下的生活污水提升泵,调节池液位低(L≤0.8m)时停止联锁投入状态下的生活污水提升泵。In an embodiment of the present invention, the method further includes: when the domestic sewage stored in the buffer device is higher than a first predetermined amount of water, pumping domestic sewage into the decomposition device; when the domestic sewage stored in the buffer device is higher than a first predetermined amount of water; When the domestic sewage is lower than the second predetermined water volume, the pumping of the domestic sewage into the decomposition device is stopped. In actual work, this process is the operation control logic of the sewage lifting pump. Please refer to Figure 5. Take three pump equipment as an example. When the level is high (L≥3.0m), start the domestic sewage lifting pump in the state of interlocking input, and stop the domestic sewage lifting pump in the state of interlocking input when the liquid level in the regulating tank is low (L≤0.8m).

请参考图6所示,在本发明一实施例中,上述步骤S305在实际工作中的控制逻辑如下:生活污水提升泵已运行(当生活污水提升泵包含多台时,任一生活污水提升泵)时,开始计时,2400S(本领域相关技术人员可根据实际情况选择设置)后,联锁状态下污泥回用泵运行15min,然后停止运行,复位计时时间,如此循环;生活污水提升泵均停(所有生活污水提升泵)时停止联锁投入状态下的污泥回流泵。Referring to FIG. 6 , in an embodiment of the present invention, the control logic of the above step S305 in actual work is as follows: ), start timing, after 2400S (persons skilled in the art can choose and set according to the actual situation), the sludge recycling pump runs for 15min in the interlocking state, then stops running, resets the timing time, and circulates like this; When stopping (all domestic sewage lifting pumps), stop the sludge return pump in the state of interlocking.

在本发明一实施例中,将所述输出用水输出至外部用水机构还包含:通过所述输出用水为活性炭过滤设备提供反洗用水。实际工作中,该处回用水泵的控制逻辑分为两种模式,即对外供水和活性炭过滤器反洗,具体的,请参考图7所示:In an embodiment of the present invention, outputting the output water to an external water use mechanism further includes: providing backwash water for the activated carbon filter device through the output water. In actual work, the control logic of the water pump here is divided into two modes, namely external water supply and activated carbon filter backwashing. For details, please refer to Figure 7:

一、对外供水模式:1. External water supply mode:

液位高(L≥3.5m)时启动联锁投入状态下的回用水泵,液位低(L≤1.5m)时停止联锁投入状态下的回用水泵。When the liquid level is high (L≥3.5m), start the reuse water pump in the state of interlocking input, and stop the reuse water pump in the state of interlocking input when the liquid level is low (L≤1.5m).

二、活性炭过滤器反洗模式:2. Activated carbon filter backwash mode:

根据活性炭过滤器反洗程控步骤执行启动停止。Start and stop according to the activated carbon filter backwash program control steps.

再请参考图8所示,在本发明一实施例中,关于活性炭过滤器的控制逻辑分为运行程控和反洗程控;Please refer to FIG. 8 again, in an embodiment of the present invention, the control logic of the activated carbon filter is divided into operation program control and backwash program control;

活性炭过滤器运行程控:Activated carbon filter operation program control:

1、正洗(开正洗排放阀,正洗排放阀到位后开进水阀,进水阀开到位之后启动被选择状态中间水泵;以上均满足以后,程序开始计时,时间到达设定时间自动进入下一步);1. Positive washing (open the discharge valve of the positive washing, open the water inlet valve after the positive washing discharge valve is in place, and start the intermediate water pump in the selected state after the water inlet valve is in place; after all the above are satisfied, the program starts timing, and the time reaches the set time automatically. to the next step);

2、运行(开出水阀,出水阀开到位之后,关闭正洗排放阀,该步进水阀开、出水阀开、被选择中间水泵均满足后,程序开始计时,程序处于该步骤时,中间水泵根据中间水池液位自动启停,中间水泵停运时,不计时,运行时,计时);2. Operation (open the water outlet valve, after the outlet valve is opened in place, close the front washing discharge valve, after the step water valve is open, the outlet valve is open, and the selected intermediate water pump is satisfied, the program starts timing, when the program is in this step, the middle The water pump automatically starts and stops according to the liquid level of the intermediate pool. When the intermediate water pump is out of operation, it will not count the time, and when it is running, it will count);

3、备用(累积运行时间达到设定时间,停被选择中间水泵,关闭进水阀、出水阀、到位后程序结束运行,并提示运行人员需要进行反洗)3. Standby (the accumulative running time reaches the set time, stop the selected intermediate water pump, close the water inlet valve and the water outlet valve, and the program ends when it is in place, and prompts the operator to perform backwashing)

活性炭过滤器反洗程控:Activated carbon filter backwash program control:

程控面板中增加回用水泵、曝气风机选择功能(被选中回用水泵、曝气风机根据程控步骤自动启停)。活性炭过滤器反洗步骤如下:The program control panel adds the selection function of the reused water pump and aeration fan (the selected reused water pump and aeration fan are automatically started and stopped according to the program control steps). The steps of backwashing the activated carbon filter are as follows:

1、排水:开反洗排放阀,反洗排放阀开到位后,开正洗排放阀,开始计时,时间到自动进入下一步,;1. Drainage: Open the backwash discharge valve. After the backwash discharge valve is opened in place, open the positive wash discharge valve, start timing, and automatically enter the next step when the time is up;

2、气洗:关闭正洗排放阀,启动被选中罗茨风机,开进气阀,开始计时,时间到进入下一步;2. Air wash: close the discharge valve of the front wash, start the selected Roots blower, open the intake valve, start timing, and go to the next step when the time is up;

3、水洗:关进气阀(停风机同时执行),开反洗进水阀,反洗进水阀开到位之后,启动被选中回用水泵;程序开始计时;时间到自动进入下一步;3. Water washing: close the intake valve (execute at the same time when the fan is stopped), open the backwash inlet valve, after the backwash inlet valve is opened in place, start the selected reuse pump; the program starts timing; when the time is up, it will automatically enter the next step;

4、正洗:停被选中回用水泵,泵停止后关系反洗进水阀、关闭反洗排水阀;开正洗排放阀,开进水阀,启动被选中中间水泵,满足后计时,时间到进入自动进入下一步;4. Front washing: stop the selected water pump for reuse. After the pump is stopped, the backwash inlet valve and the backwash drain valve are closed; To enter automatically enter the next step;

5、备用:停中间水泵,关闭正洗排放阀、关进水阀,程序复位累积运行时间。5. Standby: stop the intermediate water pump, close the discharge valve of the positive wash, close the water inlet valve, and the program resets the accumulated running time.

本发明的有益技术效果在于:实现了生活污水处理污水提升、曝气、污泥回流、过滤器运行反洗、净水回用等功能协调、连续、自动运行,提高了生活污水处理效率、降低了运行成本。The beneficial technical effects of the present invention are as follows: the coordinated, continuous and automatic operation of functions such as sewage lifting, aeration, sludge return, filter operation backwashing, and purified water reuse in domestic sewage treatment is realized, the efficiency of domestic sewage treatment is improved, and the running costs.

本发明还提供一种电子设备,包括存储器、处理器及存储在存储器上并可在处理器上运行的计算机程序,所述处理器执行所述计算机程序时实现上述方法。The present invention also provides an electronic device, comprising a memory, a processor and a computer program stored in the memory and running on the processor, the processor implementing the above method when the computer program is executed.

本发明还提供一种计算机可读存储介质,所述计算机可读存储介质存储有执行上述方法的计算机程序。The present invention also provides a computer-readable storage medium storing a computer program for executing the above method.

如图9所示,该电子设备600还可以包括:通信模块110、输入单元120、音频处理单元130、显示器160、电源170。值得注意的是,电子设备600也并不是必须要包括图9中所示的所有部件;此外,电子设备600还可以包括图9中没有示出的部件,可以参考现有技术。As shown in FIG. 9 , the electronic device 600 may further include: a communication module 110 , an input unit 120 , an audio processing unit 130 , a display 160 , and a power supply 170 . It is worth noting that the electronic device 600 does not necessarily include all the components shown in FIG. 9 ; in addition, the electronic device 600 may also include components not shown in FIG. 9 , and reference may be made to the prior art.

如图9所示,中央处理器100有时也称为控制器或操作控件,可以包括微处理器或其他处理器装置和/或逻辑装置,该中央处理器100接收输入并控制电子设备600的各个部件的操作。As shown in FIG. 9 , the central processing unit 100 , also sometimes referred to as a controller or operational control, may include a microprocessor or other processor device and/or logic device, and the central processing unit 100 receives input and controls various aspects of the electronic device 600 component operation.

其中,存储器140,例如可以是缓存器、闪存、硬驱、可移动介质、易失性存储器、非易失性存储器或其它合适装置中的一种或更多种。可储存上述与失败有关的信息,此外还可存储执行有关信息的程序。并且中央处理器100可执行该存储器140存储的该程序,以实现信息存储或处理等。Wherein, the memory 140 may be, for example, one or more of a cache, a flash memory, a hard drive, a removable medium, a volatile memory, a non-volatile memory or other suitable devices. The above-mentioned information related to the failure can be stored, and a program executing the related information can also be stored. And the central processing unit 100 can execute the program stored in the memory 140 to realize information storage or processing.

输入单元120向中央处理器100提供输入。该输入单元120例如为按键或触摸输入装置。电源170用于向电子设备600提供电力。显示器160用于进行图像和文字等显示对象的显示。该显示器例如可为LCD显示器,但并不限于此。The input unit 120 provides input to the central processing unit 100 . The input unit 120 is, for example, a key or a touch input device. The power supply 170 is used to provide power to the electronic device 600 . The display 160 is used for displaying display objects such as images and characters. The display can be, for example, but not limited to, an LCD display.

该存储器140可以是固态存储器,例如,只读存储器(ROM)、随机存取存储器(RAM)、SIM卡等。还可以是这样的存储器,其即使在断电时也保存信息,可被选择性地擦除且设有更多数据,该存储器的示例有时被称为EPROM等。存储器140还可以是某种其它类型的装置。存储器140包括缓冲存储器141(有时被称为缓冲器)。存储器140可以包括应用/功能存储部142,该应用/功能存储部142用于存储应用程序和功能程序或用于通过中央处理器100执行电子设备600的操作的流程。The memory 140 may be solid state memory, eg, read only memory (ROM), random access memory (RAM), SIM card, and the like. There may also be memories that retain information even when powered off, selectively erased and provided with more data, examples of which are sometimes referred to as EPROMs or the like. Memory 140 may also be some other type of device. Memory 140 includes buffer memory 141 (sometimes referred to as a buffer). The memory 140 may include an application/function storage part 142 for storing application programs and function programs or for performing operations of the electronic device 600 through the central processing unit 100 .

存储器140还可以包括数据存储部143,该数据存储部143用于存储数据,例如联系人、数字数据、图片、声音和/或任何其他由电子设备使用的数据。存储器140的驱动程序存储部144可以包括电子设备的用于通信功能和/或用于执行电子设备的其他功能(如消息传送应用、通讯录应用等)的各种驱动程序。The memory 140 may also include a data store 143 for storing data such as contacts, digital data, pictures, sounds and/or any other data used by the electronic device. The driver storage section 144 of the memory 140 may include various drivers of the electronic device for communication functions and/or for executing other functions of the electronic device (eg, a messaging application, a contact book application, etc.).

通信模块110即为经由天线111发送和接收信号的发送机/接收机110。通信模块(发送机/接收机)110耦合到中央处理器100,以提供输入信号和接收输出信号,这可以和常规移动通信终端的情况相同。The communication module 110 is the transmitter/receiver 110 that transmits and receives signals via the antenna 111 . A communication module (transmitter/receiver) 110 is coupled to the central processing unit 100 to provide input signals and receive output signals, as may be the case with conventional mobile communication terminals.

基于不同的通信技术,在同一电子设备中,可以设置有多个通信模块110,如蜂窝网络模块、蓝牙模块和/或无线局域网模块等。通信模块(发送机/接收机)110还经由音频处理器130耦合到扬声器131和麦克风132,以经由扬声器131提供音频输出,并接收来自麦克风132的音频输入,从而实现通常的电信功能。音频处理器130可以包括任何合适的缓冲器、解码器、放大器等。另外,音频处理器130还耦合到中央处理器100,从而使得可以通过麦克风132能够在本机上录音,且使得可以通过扬声器131来播放本机上存储的声音。Based on different communication technologies, multiple communication modules 110 may be provided in the same electronic device, such as a cellular network module, a Bluetooth module, and/or a wireless local area network module. Communication module (transmitter/receiver) 110 is also coupled to speaker 131 and microphone 132 via audio processor 130 to provide audio output via speaker 131 and to receive audio input from microphone 132 for general telecommunication functions. Audio processor 130 may include any suitable buffers, decoders, amplifiers, and the like. In addition, the audio processor 130 is also coupled to the central processing unit 100 so as to enable recording on the local unit through the microphone 132 and to play back the sound stored on the local unit through the speaker 131 .

本领域内的技术人员应明白,本发明的实施例可提供为方法、系统、或计算机程序产品。因此,本发明可采用完全硬件实施例、完全软件实施例、或结合软件和硬件方面的实施例的形式。而且,本发明可采用在一个或多个其中包含有计算机可用程序代码的计算机可用存储介质(包括但不限于磁盘存储器、CD-ROM、光学存储器等)上实施的计算机程序产品的形式。As will be appreciated by one skilled in the art, embodiments of the present invention may be provided as a method, system, or computer program product. Accordingly, the present invention may take the form of an entirely hardware embodiment, an entirely software embodiment, or an embodiment combining software and hardware aspects. Furthermore, the present invention may take the form of a computer program product embodied on one or more computer-usable storage media (including, but not limited to, disk storage, CD-ROM, optical storage, etc.) having computer-usable program code embodied therein.

本发明是参照根据本发明实施例的方法、设备(系统)、和计算机程序产品的流程图和/或方框图来描述的。应理解可由计算机程序指令实现流程图和/或方框图中的每一流程和/或方框、以及流程图和/或方框图中的流程和/或方框的结合。可提供这些计算机程序指令到通用计算机、专用计算机、嵌入式处理机或其他可编程数据处理设备的处理器以产生一个机器,使得通过计算机或其他可编程数据处理设备的处理器执行的指令产生用于实现在流程图一个流程或多个流程和/或方框图一个方框或多个方框中指定的功能的装置。The present invention is described with reference to flowchart illustrations and/or block diagrams of methods, apparatus (systems), and computer program products according to embodiments of the invention. It will be understood that each flow and/or block in the flowchart illustrations and/or block diagrams, and combinations of flows and/or blocks in the flowchart illustrations and/or block diagrams, can be implemented by computer program instructions. These computer program instructions may be provided to the processor of a general purpose computer, special purpose computer, embedded processor or other programmable data processing device to produce a machine such that the instructions executed by the processor of the computer or other programmable data processing device produce Means for implementing the functions specified in a flow or flow of a flowchart and/or a block or blocks of a block diagram.

这些计算机程序指令也可存储在能引导计算机或其他可编程数据处理设备以特定方式工作的计算机可读存储器中,使得存储在该计算机可读存储器中的指令产生包括指令装置的制造品,该指令装置实现在流程图一个流程或多个流程和/或方框图一个方框或多个方框中指定的功能。These computer program instructions may also be stored in a computer-readable memory capable of directing a computer or other programmable data processing apparatus to function in a particular manner, such that the instructions stored in the computer-readable memory result in an article of manufacture comprising instruction means, the instructions The apparatus implements the functions specified in the flow or flows of the flowcharts and/or the block or blocks of the block diagrams.

这些计算机程序指令也可装载到计算机或其他可编程数据处理设备上,使得在计算机或其他可编程设备上执行一系列操作步骤以产生计算机实现的处理,从而在计算机或其他可编程设备上执行的指令提供用于实现在流程图一个流程或多个流程和/或方框图一个方框或多个方框中指定的功能的步骤。These computer program instructions can also be loaded on a computer or other programmable data processing device to cause a series of operational steps to be performed on the computer or other programmable device to produce a computer-implemented process such that The instructions provide steps for implementing the functions specified in the flow or blocks of the flowcharts and/or the block or blocks of the block diagrams.

以上所述的具体实施例,对本发明的目的、技术方案和有益效果进行了进一步详细说明,所应理解的是,以上所述仅为本发明的具体实施例而已,并不用于限定本发明的保护范围,凡在本发明的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The specific embodiments described above further describe the purpose, technical solutions and beneficial effects of the present invention in detail. It should be understood that the above-mentioned specific embodiments are only specific embodiments of the present invention, and are not intended to limit the scope of the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.

Claims (13)

1. A domestic sewage treatment system is characterized by comprising a buffering device, a decomposition device, a recycling device and an output device;
the buffer device is used for storing the received domestic sewage and filtering floating objects larger than a preset volume in the domestic sewage;
the decomposition device is used for carrying out primary precipitation treatment on the domestic sewage filtered and treated by the cache device, carrying out hydrolysis reaction and acidification reaction on the treated domestic sewage, and decomposing organic solids and organic matters of a preset category in the domestic sewage into small-molecule soluble organic pollutant; converting the organic pollutants into ammonia nitrogen through the metabolism of membrane organisms, removing the ammonia nitrogen through aerobic nitrification and anoxic denitrification processes, and outputting the domestic sewage after the ammonia nitrogen is removed;
the recycling device is used for carrying out solid-liquid separation treatment on the domestic sewage treated by the decomposition device to obtain a falling biological film and domestic sewage; inputting the falling biological membrane into the decomposition device for sludge recycling, and outputting the domestic sewage obtained by separation treatment after disinfection treatment;
the output device is used for outputting the domestic sewage output by the recycling device to an external water mechanism after being filtered by active carbon.
2. The domestic sewage treatment system of claim 1 wherein said buffering means comprises a grid well and a conditioning tank;
the grating well is used for filtering floating objects larger than a preset volume in the domestic sewage;
the adjusting tank is used for storing the domestic sewage after the floating objects are filtered by the grille well, and the decomposing device is used for providing stable water quality and water quantity.
3. The domestic sewage treatment system of claim 1 wherein said decomposition means comprises a primary settling tank, an anaerobic hydrolysis tank, a primary contact oxidation tank and a secondary contact oxidation tank;
the primary sedimentation tank is connected with the buffer device and is used for carrying out pre-aeration and primary sedimentation treatment on the domestic sewage treated by the buffer device;
the anaerobic hydrolysis tank is connected with the primary sedimentation tank and is used for carrying out hydrolysis and acidification reactions on the domestic sewage treated by the primary sedimentation tank and decomposing organic solids and organic matters of a preset category in the domestic sewage into micromolecular soluble organic matters;
the first-stage contact oxidation pond with the anaerobic hydrolysis pond links to each other, the second grade contact oxidation pond with the first-stage contact oxidation pond links to each other, the first-stage contact oxidation pond with the second grade contact oxidation pond is used for through the biological metabolism of membrane will organic pollutant in the domestic sewage after the anaerobic hydrolysis pond is handled turns into the ammonia nitrogen, and the rethread aerobic nitrification and oxygen deficiency denitrification process get rid of the ammonia nitrogen.
4. The domestic sewage treatment system of claim 3 wherein said recycling means comprises a secondary sedimentation tank, a disinfection tank and a sludge tank;
the secondary sedimentation tank is respectively connected with the secondary contact oxidation tank and the anaerobic hydrolysis tank and is used for carrying out solid-liquid separation treatment on the domestic sewage treated by the secondary contact oxidation tank to obtain sludge, a falling biological membrane and domestic sewage; inputting the falling biological membrane into the anaerobic hydrolysis tank for sludge recycling;
the disinfection tank is connected with the secondary sedimentation tank and is used for disinfecting the domestic sewage treated by the secondary sedimentation tank;
the sludge tank is respectively connected with the secondary sedimentation tank and the primary sedimentation tank and is used for storing the sludge separated by the secondary sedimentation tank and inputting the domestic sewage overflowed by the sludge sedimentation into the primary sedimentation tank.
5. The domestic sewage treatment system of claim 4, further comprising an aeration fan, wherein said aeration fan is connected to said primary sedimentation tank, said primary contact oxidation tank, said secondary contact oxidation tank and said recycling device, and is used for performing aeration treatment on the domestic sewage in said decomposition device for preliminary sedimentation treatment, converting said organic pollutants into ammonia nitrogen and removing said ammonia nitrogen; and carrying out aeration treatment on the domestic sewage subjected to active carbon filtration in the output device.
6. The domestic sewage treatment system of claim 5, wherein said system further comprises a rotating machinery group, said rotating machinery group comprising a sewage lift pump, a sludge recirculation pump, an intermediate water pump, and a reuse water pump;
the sewage lifting pump is used for pumping the domestic sewage stored in the buffer device into the decomposition device;
the sludge reflux pump is used for pumping the falling biological membrane into the decomposition device for sludge recycling;
the intermediate water pump is used for pumping the domestic sewage after the disinfection treatment in the recycling device to the output device for active carbon filtration;
the recycling water pump is used for pumping the domestic sewage filtered by the activated carbon in the output device to an external water using mechanism and/or pumping the domestic sewage to an activated carbon filtering device in the output device to provide backwashing water.
7. The domestic sewage treatment system of claim 6, wherein said system further comprises a control device comprising a sewage lift pump control module, an aeration blower control module, a sludge return pump control module, and a reuse pump control module;
the sewage lifting pump control module is used for starting the sewage lifting pump to pump domestic sewage into the decomposition device when the domestic sewage stored in the buffer device is higher than a first preset water amount; when the domestic sewage stored in the buffer device is lower than a second preset water amount, the sewage lifting pump is closed, and the domestic sewage is stopped from being pumped into the decomposition device;
the aeration fan control module is used for controlling the aeration fan to carry out preliminary sedimentation treatment on the domestic sewage in the decomposition device and convert the organic pollutants into ammonia nitrogen and carry out aeration treatment on the domestic sewage in the ammonia nitrogen removal stage according to the received control instruction; and/or, the domestic sewage filtered by the active carbon in the output device is subjected to aeration treatment;
the sludge reflux pump control module is used for controlling the sludge reflux pump to start to operate for a second time period after the sewage lifting pump operates for a first certain time period; and stopping the operation of the sludge reflux pump after the operation of the sewage lifting pump is stopped;
the reuse water pump control module is used for controlling the reuse water pump to pump the domestic sewage filtered by the activated carbon in the output device into an external water using mechanism and/or pump the domestic sewage into the output device for providing backwashing water by the activated carbon filtering equipment according to the received control instruction.
8. A control method for a domestic sewage treatment system according to claim 1, wherein said method comprises:
receiving domestic sewage and filtering floating objects larger than a preset volume in the domestic sewage;
carrying out primary precipitation treatment on the domestic sewage, carrying out hydrolysis reaction and acidification reaction on the treated domestic sewage, and decomposing organic solids and organic matters of a predetermined category in the domestic sewage into small-molecule soluble organic pollutant;
converting the organic pollutants into ammonia nitrogen through the metabolism of membrane organisms, and removing the ammonia nitrogen through aerobic nitrification and anoxic denitrification processes;
carrying out solid-liquid separation treatment on the domestic sewage from which the ammonia nitrogen is removed to obtain a falling biological film and domestic sewage;
the falling biological membrane is recycled by refluxing, and the domestic sewage obtained by separation treatment is disinfected and then filtered by activated carbon to obtain output water;
and outputting the output water to an external water mechanism.
9. The control method according to claim 8, characterized in that the method further comprises:
in the primary precipitation treatment process of the domestic sewage, converting the organic pollutants into ammonia nitrogen and carrying out aeration treatment on the domestic sewage in the process of removing the ammonia nitrogen; and carrying out aeration treatment on the domestic sewage in the process of filtering the domestic sewage by using the activated carbon.
10. The control method according to claim 8, characterized in that the method further comprises:
when the domestic sewage stored in the buffer device is higher than a first preset water amount, pumping the domestic sewage into the decomposition device;
and when the domestic sewage stored in the buffer device is lower than a second preset water amount, stopping pumping the domestic sewage into the decomposition device.
11. The control method according to claim 8, wherein the means for outputting the output water to the external water further comprises: and supplying backwashing water for the activated carbon filtering equipment through the output water.
12. An electronic device comprising a memory, a processor and a computer program stored on the memory and executable on the processor, wherein the processor implements the method of any of claims 8 to 11 when executing the computer program.
13. A computer-readable storage medium, characterized in that the computer-readable storage medium stores a computer program for executing the method of any one of claims 8 to 11.
CN202010776151.1A 2020-08-05 2020-08-05 Domestic sewage treatment system and control method Pending CN111977894A (en)

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