CN108328854A - A kind of country sewage integrated equipment for wastewater treatment and processing method - Google Patents

A kind of country sewage integrated equipment for wastewater treatment and processing method Download PDF

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CN108328854A
CN108328854A CN201810031812.0A CN201810031812A CN108328854A CN 108328854 A CN108328854 A CN 108328854A CN 201810031812 A CN201810031812 A CN 201810031812A CN 108328854 A CN108328854 A CN 108328854A
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filter
pipe
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biological filter
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申华楠
陆少鸣
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South China University of Technology SCUT
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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
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • 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
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/302Nitrification and denitrification treatment

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  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
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  • Biological Treatment Of Waste Water (AREA)

Abstract

本发明公开了一种农村污水一体化处理设备及处理方法。该设备主要包括折流式缺氧生物滤池、升流式曝气生物滤池、斜板沉淀池和电控柜;折流式缺氧生物滤池和升流式曝气生物滤池自上而下依次设有上部配水集水区、滤网板、悬浮陶粒滤床、滤床流化缓冲区、布气装置和底部配水集水装置;进水管、回流管、出水管、配气管、反冲洗进水管、反冲洗排水管、曝气混合管、出水管和排泥管安装有电动阀门,电动阀门都与电控柜连接;电控柜还分别连接鼓风机和反冲洗水泵。本发明设备集污水初滤、回流反硝化脱氮、生物降解硝化、混凝沉淀除磷等功能于一体,高效节能,通过网络远程控制实现无人值守,适用于农村污水处理。

The invention discloses an integrated treatment equipment and treatment method for rural sewage. The equipment mainly includes baffled anoxic biological filter, upflow biological aerated filter, inclined plate sedimentation tank and electric control cabinet; baffled anoxic biological filter and upflow biological aerated filter And the bottom is equipped with upper water distribution catchment area, filter screen plate, suspended ceramsite filter bed, filter bed fluidization buffer zone, air distribution device and bottom water distribution and collection device; water inlet pipe, return pipe, outlet pipe, gas distribution pipe, The backwash water inlet pipe, backwash drain pipe, aeration mixing pipe, water outlet pipe and mud discharge pipe are equipped with electric valves, and the electric valves are all connected with the electric control cabinet; the electric control cabinet is also respectively connected with the blower and the backwash water pump. The equipment of the present invention integrates the functions of primary sewage filtration, reflux denitrification and denitrification, biodegradation and nitrification, coagulation and precipitation phosphorus removal, etc., is highly efficient and energy-saving, realizes unattended operation through network remote control, and is suitable for rural sewage treatment.

Description

一种农村污水一体化处理设备及处理方法A kind of rural sewage integrated treatment equipment and treatment method

技术领域technical field

本发明涉及一种污水处理技术领域,具体是涉及一种农村污水一体化处理设备及处理方法。The invention relates to the technical field of sewage treatment, in particular to an integrated treatment equipment and treatment method for rural sewage.

背景技术Background technique

近年来,农村地区的人民生活水平不断提高,用水量逐年加大,同时增加了农村污水的排放量。农村污水的水质与城市生活污水接近,有机物、氮、磷等污染物质浓度较高。由于在农村地区,污水处理规模小,农户居住较为分散,污水收集困难,难以大规模集中处理,适合采用处理小规模生活污水的无人值守一体化污水处理设备。In recent years, people's living standards in rural areas have been continuously improved, water consumption has increased year by year, and at the same time, the discharge of rural sewage has increased. The water quality of rural sewage is close to that of urban domestic sewage, and the concentration of organic matter, nitrogen, phosphorus and other pollutants is relatively high. Because in rural areas, the scale of sewage treatment is small, the farmers live in scattered places, it is difficult to collect sewage, and it is difficult to collect large-scale centralized treatment. It is suitable to use unattended integrated sewage treatment equipment for small-scale domestic sewage.

目前,对农村污水处理工艺的研究趋于多样化,但主要包括利用土壤作为收集和排放载体的自然生态处理系统、利用复杂的生物和物理过程的传统处理系统及小型污水处理装置。自然生态处理系统如人工湿地,占地面积过大,投资费用高,管理复杂,出水效果不尽人意;常用的传统生活污水处理工艺如厌氧‐缺氧‐好氧活性污泥法,活性污泥常常出现异常,或污泥膨胀,或污泥解体,因此需要有人值守,以便及时针对活性污泥异常情况采取应对措施;小型污水处理装置如膜生物反应器虽然实现了结构上的一体化,但装置投资较高,运行电耗较大。At present, research on rural sewage treatment processes tends to be diversified, but mainly includes natural ecological treatment systems using soil as a carrier for collection and discharge, traditional treatment systems using complex biological and physical processes, and small sewage treatment devices. Natural ecological treatment systems such as artificial wetlands occupy too large an area, require high investment costs, complex management, and unsatisfactory effluent results; commonly used traditional domestic sewage treatment processes such as anaerobic-anoxic-aerobic activated sludge process, activated sewage Sludge often has abnormalities, or sludge bulking, or sludge disintegration, so someone needs to be on duty to take timely measures against abnormalities in activated sludge; although small sewage treatment devices such as membrane bioreactors have achieved structural integration, However, the equipment investment is relatively high, and the operating power consumption is relatively large.

因此,针对农村污水特点以及现有技术存在的管理复杂、投资运行费用高、处理效果差的缺点,需要寻求一种可无人值守、投资运行费用低、高效节能的农村污水一体化处理设备。Therefore, in view of the characteristics of rural sewage and the shortcomings of existing technologies such as complex management, high investment and operation costs, and poor treatment effects, it is necessary to seek an integrated rural sewage treatment equipment that can be unattended, low investment and operation costs, and highly efficient and energy-saving.

发明内容Contents of the invention

本发明的目的在于针对现有农村污水处理工艺的不足,提供一种集污水初滤、回流反硝化脱氮、生物降解硝化、混凝沉淀除磷等功能于一体,投资运行费用低、高效节能的农村污水一体化处理设备及处理方法。The purpose of the present invention is to address the shortcomings of the existing rural sewage treatment process, to provide a sewage treatment system that integrates the functions of primary sewage filtration, reflux denitrification denitrification, biodegradation nitrification, coagulation precipitation phosphorus removal, etc., with low investment and operation costs, high efficiency and energy saving Integrated rural sewage treatment equipment and treatment methods.

本发明设备处理流程是“折流式缺氧生物滤池→升流式曝气生物滤池→斜板沉淀池”。折流式缺氧生物滤池被三块竖直挡板分隔成上下折返的污水通道,分为三级,第一级缺氧生物滤池优选采用粒径¢12~16mm页岩陶粒,第二级缺氧生物滤池优选采用粒径¢8~12mm页岩陶粒,第三级缺氧生物滤池优选采用粒径¢4~8mm页岩陶粒,滤料粒径逐步减小,在滤床中可以较好截滤悬浮物,同时可以避免严重的滤料堵塞,实现初滤预处理,保护后续生物滤池正常运行;在滤料表面生长反硝化生物膜,利用污水中的碳源将硝酸盐转化为氮气释放完成生物脱氮,三级缺氧生物滤池可分别生长多种不同优势菌种的生物膜,降解有机物效果好。升流式曝气生物滤池主要作用是在滤料表面生长硝化生物膜,将污水中的氨氮和有机氮氧化为硝酸盐,滤料表面也生长异养生物膜,进一步降解有机物,此外在其出水渠投加絮凝剂完成混凝。斜板沉淀池将混凝后的污水进行沉淀,去除磷、悬浮物和残存有机物。本发明还可通过网络远程控制,实现无人值守,该特点也特别适用于农村污水处理。The processing flow of the equipment of the present invention is "baffle type anoxic biological filter → upflow type aerated biological filter → inclined plate sedimentation tank". The baffle type anoxic biological filter is separated by three vertical baffles into an up and down return sewage channel, which is divided into three stages. The first stage anoxic biological filter is preferably made of shale ceramsite with a particle size of ¢12-16mm. Shale ceramsite with a particle size of ¢8-12mm is preferred for the secondary anoxic biofilter, and shale ceramsite with a particle size of ¢4-8mm is preferred for the third-stage anoxic biological filter. The particle size of the filter material decreases gradually. Suspended solids can be better intercepted in the filter bed, and serious clogging of the filter material can be avoided at the same time, and the pretreatment of the initial filtration can be realized to protect the normal operation of the subsequent biological filter; a denitrification biofilm can be grown on the surface of the filter material to utilize the carbon source in the sewage The nitrate is converted into nitrogen and released to complete biological denitrification. The three-stage anoxic biological filter can grow biofilms of various dominant bacterial species, and the effect of degrading organic matter is good. The main function of the upflow biological aerated filter is to grow nitrification biofilm on the surface of the filter material, oxidize the ammonia nitrogen and organic nitrogen in the sewage into nitrate, and also grow a heterotrophic biofilm on the surface of the filter material to further degrade organic matter. Add flocculant to the outlet channel to complete the coagulation. The inclined plate sedimentation tank will settle the coagulated sewage to remove phosphorus, suspended solids and residual organic matter. The invention can also be remotely controlled through the network to realize unattended operation, and this feature is also especially suitable for rural sewage treatment.

本发明的目的通过如下技术方案实现:The purpose of the present invention is achieved through the following technical solutions:

一种农村污水一体化处理设备,其特征在于,主要包括折流式缺氧生物滤池、升流式曝气生物滤池、斜板沉淀池和电控柜;所述折流式缺氧生物滤池被三块竖直挡板分隔成上下折返的第一级缺氧生物滤池、第二级缺氧生物滤池和第三级缺氧生物滤池;第一级缺氧生物滤池、第二级缺氧生物滤池、第三级缺氧生物滤池和升流式曝气生物滤池自上而下依次设有上部配水集水区、滤网板、悬浮陶粒滤床、滤床流化缓冲区、布气装置和底部配水集水装置;第一级缺氧生物滤池上部配水集水区与进水管相连通,底部配水集水装置与第二级缺氧生物滤池的底部配水集水装置连通,第二级缺氧生物滤池上部配水集水区和第三级缺氧生物滤池的上部配水集水区连接,第三级缺氧生物滤池的底部配水集水装置与升流式曝气生物滤池底部配水集水装置相连通;An integrated treatment equipment for rural sewage, characterized in that it mainly includes a baffled anoxic biological filter, an upflow biological aerated filter, an inclined plate sedimentation tank and an electric control cabinet; the baffled anoxic biological The filter is separated by three vertical baffles into the first-stage anoxic biological filter, the second-stage anoxic biological filter and the third-stage anoxic biological filter; the first-stage anoxic biological filter, The second-stage anoxic biological filter, the third-stage anoxic biological filter and the upflow biological aerated filter are equipped with upper water distribution catchment area, filter plate, suspended ceramsite filter bed, filter Bed fluidized buffer zone, air distribution device and bottom water distribution and collection device; the upper water distribution and collection area of the first-stage anoxic biological filter is connected to the water inlet pipe, and the bottom water distribution and collection device is connected to the second-stage anoxic biological filter. The bottom water distribution and collection device is connected, the upper water distribution catchment area of the second-stage anoxic biological filter is connected with the upper water distribution catchment area of the third-stage anoxic biological filter, and the bottom water distribution and collection area of the third-stage anoxic biological filter The device is connected with the water distribution and collection device at the bottom of the upflow biological aerated filter;

所述升流式曝气生物滤池上部配水集水区通过回流管与第一级缺氧生物滤池上部配水集水区相连通,回流管与配气管连接,回流管上设有气提装置,升流式曝气生物滤池上部配水集水区一侧设有集水渠,集水渠内部设有曝气混合管和反冲洗水泵,曝气混合管与配气管连接,反冲洗水泵通过反冲洗进水管分别与第一级缺氧生物滤池、第二级缺氧生物滤池、第三级缺氧生物滤池的上部配水集水区相连接;折流式缺氧生物滤池和升流式曝气生物滤池底部布气装置通过配气管与鼓风机连接,底部配水集水装置与反冲洗排水管连接;The upper water distribution catchment area of the upflow biological aerated filter is connected with the upper water distribution catchment area of the first-stage anoxic biological filter through the return pipe, the return pipe is connected with the gas distribution pipe, and the return pipe is provided with an air lift device , There is a collection channel on one side of the upper water distribution catchment area of the upflow biological aerated filter tank, and an aeration mixing pipe and a backwash water pump are installed inside the water collection canal. The aeration mixing pipe is connected to the air distribution pipe, and the backwash water pump passes The water inlet pipes are respectively connected to the upper water distribution catchment area of the first-stage anoxic biological filter, the second-stage anoxic biological filter, and the third-stage anoxic biological filter; the baffle-type anoxic biological filter and the upflow The air distribution device at the bottom of the biological aerated filter is connected to the blower through the air distribution pipe, and the water distribution and collection device at the bottom is connected to the backwash drainage pipe;

所述斜板沉淀池自上而下依次设有上部配水集水区、沉淀区和污泥斗,沉淀区设有斜板和中心管;所述斜板沉淀池的中心管与升流式曝气生物滤池的集水渠相连通,斜板沉淀池的上部配水集水区与出水管连接,底部污泥斗与排泥管连接;The inclined plate sedimentation tank is provided with an upper water distribution catchment area, a sedimentation area and a sludge hopper in sequence from top to bottom, and the sedimentation area is provided with an inclined plate and a central pipe; the central pipe of the inclined plate sedimentation tank is connected with the upflow type The water collection channel of the gas biological filter is connected, the upper water distribution catchment area of the inclined plate sedimentation tank is connected with the outlet pipe, and the bottom sludge bucket is connected with the sludge discharge pipe;

所述进水管、回流管、出水管、配气管、反冲洗进水管、反冲洗排水管、曝气混合管、出水管和排泥管安装有电动阀门,所述电动阀门都与电控柜连接;电控柜还分别连接鼓风机和反冲洗水泵。The water inlet pipe, return pipe, water outlet pipe, gas distribution pipe, backwash water inlet pipe, backwash drain pipe, aeration mixing pipe, water outlet pipe and mud discharge pipe are equipped with electric valves, and the electric valves are all connected to the electric control cabinet ; The electric control cabinet is also connected to the air blower and the backwash water pump respectively.

为进一步实现本发明目的,优选地,所述第一级缺氧生物滤池滤料采用粒径为¢12~16mm页岩陶粒;所述第二级缺氧生物滤池滤料采用粒径为¢8~12mm页岩陶粒;所述第三级缺氧生物滤池滤料采用粒径为¢4~8mm页岩陶粒。In order to further realize the purpose of the present invention, preferably, the filter material of the first-stage anoxic biological filter adopts shale ceramsite with a particle diameter of ¢12~16mm; the filter material of the second-stage anoxic biological filter adopts a particle diameter of Shale ceramsite is ¢8~12mm; the filter material of the third stage anoxic biological filter adopts shale ceramsite with particle size ¢4~8mm.

优选地,所述升流式曝气生物滤池滤料采用粒径为¢4~8mm页岩陶粒。Preferably, the filter material of the upflow biological aerated filter adopts shale ceramsite with a particle size of ¢4-8mm.

优选地,不同粒径的页岩陶粒水浸润颗粒密度为0.95±0.5g/cm3,与滤网板相互作用在水中成悬浮状态。Preferably, the shale ceramsite water-wetting particles with different particle sizes have a particle density of 0.95±0.5g/cm 3 , and interact with the screen plate to form a suspended state in water.

优选地,所述悬浮陶粒滤床的高度为1~2m,所述滤床流化缓冲区的高度为0.3~0.5m。Preferably, the height of the suspended ceramsite filter bed is 1-2m, and the height of the fluidized buffer zone of the filter bed is 0.3-0.5m.

优选地,电控柜通过网络与后台连接。Preferably, the electric control cabinet is connected to the background through the network.

优选地,所述电控柜设在斜板沉淀池的外侧。Preferably, the electric control cabinet is arranged outside the inclined plate sedimentation tank.

优选地,所述斜板沉淀池的一侧设有门。Preferably, a door is provided on one side of the inclined plate sedimentation tank.

应用所述设备的农村污水一体化处理方法:污水进入折流式缺氧生物滤池,上下折返依次通过第一级缺氧生物滤池、第二级缺氧生物滤池和第三级缺氧生物滤池,去除有机物和大颗粒悬浮物;第三级缺氧生物滤池出水从底部配水集水装置向上均匀配水进入升流式曝气生物滤池;压缩空气经布气装置进入升流式曝气生物滤池进行曝气,硝化氨氮和降解污水中残存有机物;升流式曝气生物滤池的升流出水到达上部配水集水区;升流式曝气生物滤池配水集水区的一部分出水回流到第一级缺氧生物滤池配水集水区,与原污水混合,进行反硝化脱氮,另一部分出水进入集水渠,压缩空气经曝气混合管将出水曝气,与投加的药剂充分混合进行混凝;经过混凝后的出水进入斜板沉淀池沉淀区进行沉淀,进一步去除磷、悬浮物和有机物,升流出水通过沉淀区斜板进入集水配水区后汇集至出水管出水,沉淀到污泥斗中污泥通过污泥管排出。The integrated rural sewage treatment method using the above-mentioned equipment: the sewage enters the baffle type anoxic biological filter, and turns up and down to pass through the first-stage anoxic biological filter, the second-stage anoxic biological filter and the third-stage anoxic biological filter. The biological filter removes organic matter and large suspended solids; the effluent of the third-stage anoxic biological filter is evenly distributed upwards from the bottom water distribution and collection device into the upflow biological aerated filter; the compressed air enters the upflow type through the air distribution device The biological aerated filter is aerated to nitrify ammonia nitrogen and degrade the residual organic matter in the sewage; the upflow effluent of the upflow biological aerated filter reaches the upper water distribution catchment area; the upflow biological aerated filter water distribution catchment area A part of the effluent flows back to the first-stage anoxic biological filter water distribution catchment area, where it is mixed with raw sewage for denitrification and denitrification, and the other part of the effluent enters the water collection channel, and the compressed air aerates the effluent through the aeration mixing tube, and is mixed with the dosing The medicaments are fully mixed for coagulation; the effluent after coagulation enters the sedimentation area of the inclined plate sedimentation tank for precipitation, and further removes phosphorus, suspended solids and organic matter. The water comes out of the water pipe and settles into the sludge hopper. The sludge is discharged through the sludge pipe.

生物滤池以生物膜净化污水,不存在污泥膨胀和污泥解体等现象,利于实现无人值守。由于农村生活污水处理相对而言对总氮要求较高,适合采用前置反硝化生物滤池和硝化曝气生物滤池两级串联回流组合工艺。传统的固定床生物滤池,过滤水头损失过大,而且要求进水悬浮物平均粒径不宜超过2mm,进水悬浮物浓度也不宜超过60mg/L,本发明采用流化床生物滤池,同时前置反硝化生物滤池采用不同粒径的页岩陶粒,截滤悬浮物。The biofilter purifies sewage with biofilm, and there is no phenomenon of sludge bulking and sludge disintegration, which is conducive to realizing unattended operation. Since the treatment of domestic sewage in rural areas has relatively high requirements for total nitrogen, it is suitable to adopt the two-stage serial reflux combination process of pre-denitrification biological filter and nitrification aerated biological filter. In the traditional fixed bed biological filter, the loss of filtration head is too large, and the average particle size of suspended solids in the influent should not exceed 2mm, and the concentration of suspended solids in the influent should not exceed 60 mg/L. The present invention adopts a fluidized bed biological filter, and at the same time The pre-denitrification biological filter uses shale ceramsite with different particle sizes to intercept and filter suspended solids.

本发明与现有技术相比,具有如下优点和有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:

(1)采用同类生物滤池折流串联,具有预处理功能,共用曝气和气水反冲洗系统,同时采用气提回流,高度集成一体化,投资运行费用经济。(1) The same kind of biological filter is used in baffle series, with pretreatment function, shared aeration and air-water backwashing system, and adopts air lift backflow at the same time, highly integrated and economical in investment and operation costs.

(2)采用不同粒径页岩陶粒滤料,同时预留滤床流化缓冲区,正常运行滤料为流化状态,不宜板结,反冲洗周期长,滤料使用寿命长,运行维护成本低。(2) Shale ceramsite filter materials with different particle sizes are used, and the fluidized buffer zone of the filter bed is reserved at the same time. The filter material is in a fluidized state during normal operation, and it is not suitable for compaction. The backwash cycle is long, the service life of the filter material is long, and the operation and maintenance costs are low. Low.

(3)本发明集污水初滤、回流反硝化脱氮、生物降解硝化、混凝沉淀除磷等功能于一体,生物膜活性强,更新条件好,稳定可靠,高效节能。(3) The present invention integrates the functions of sewage primary filtration, reflux denitrification and denitrification, biodegradation and nitrification, coagulation and precipitation phosphorus removal, etc., and has strong biofilm activity, good renewal conditions, stability, reliability, high efficiency and energy saving.

(4)本发明自动化管理简单可靠,电控柜可控制鼓风机、排泥泵、潜水泵和各个管道电动阀门的开关,使该设备按程序正常运行,也可通过网络远程控制电控柜可实现无人值守,适用于农村污水处理。(4) The automatic management of the present invention is simple and reliable, and the electric control cabinet can control the switch of blower, mud pump, submersible pump and electric valves of each pipeline, so that the equipment can operate normally according to the program, and the electric control cabinet can also be remotely controlled through the network. Unattended, suitable for rural sewage treatment.

附图说明Description of drawings

图1是本发明农村污水一体化处理设备的结构示意图。Fig. 1 is a structural schematic diagram of the rural sewage integrated treatment equipment of the present invention.

图2是图1的俯视图。FIG. 2 is a top view of FIG. 1 .

图中示出:折流式缺氧生物滤池1、第一级缺氧生物滤池1‐1、第二级缺氧生物滤池1‐2、第三级缺氧生物滤池1‐3、升流式曝气生物滤池2、集水渠2‐1、斜板沉淀池3、沉淀区3‐1、斜板3‐2、中心管3‐3、污泥斗3‐4、上部配水集水区4、滤网板5、悬浮陶粒滤床6、滤床流化缓冲区7、布气装置8、底部集水布气装置9、进水管10、回流管11、气提装置11‐1、配气管12、反冲洗进水管13、反冲洗排水管14、曝气混合管15、出水管16、排泥管17、反冲洗水泵18、鼓风机19、电控柜20、门21、电动阀门22。The figure shows: baffle type anoxic biological filter 1, first-stage anoxic biological filter 1-1, second-stage anoxic biological filter 1-2, third-stage anoxic biological filter 1-3 , upflow biological aerated filter 2, catchment channel 2-1, inclined plate sedimentation tank 3, sedimentation area 3-1, inclined plate 3-2, central pipe 3-3, sludge hopper 3-4, upper water distribution Water collection area 4, filter screen plate 5, suspended ceramsite filter bed 6, filter bed fluidization buffer zone 7, air distribution device 8, bottom water collection and air distribution device 9, water inlet pipe 10, return pipe 11, air lift device 11 ‐1. Air distribution pipe 12, backwash water inlet pipe 13, backwash drain pipe 14, aeration mixing pipe 15, water outlet pipe 16, mud discharge pipe 17, backwash water pump 18, blower 19, electric control cabinet 20, door 21, Electric valve 22.

具体实施方式Detailed ways

为更好理解本发明,下面结合附图对本发明作进一步说明,但本发明的实施方式不限于此。In order to better understand the present invention, the present invention will be further described below in conjunction with the accompanying drawings, but the embodiments of the present invention are not limited thereto.

如图1和图2所示,一种农村污水一体化处理设备,主要包括折流式缺氧生物滤池1,升流式曝气生物滤池2,斜板沉淀池3和电控柜20;折流式缺氧生物滤池1和升流式曝气生物滤池2自上而下依次设有上部配水集水区4、滤网板5、悬浮陶粒滤床6、滤床流化缓冲区7、布气装置8和底部配水集水装置9;斜板沉淀池3自上而下依次设有上部配水集水区4、沉淀区3‐1和污泥斗3‐4,沉淀区3‐1设有斜板3‐2和中心管3‐3;折流式缺氧生物滤池1、升流式曝气生物滤池2和斜板沉淀池3依次连通。As shown in Figure 1 and Figure 2, an integrated rural sewage treatment equipment mainly includes a baffle type anoxic biological filter 1, an upflow type aerated biological filter 2, an inclined plate sedimentation tank 3 and an electric control cabinet 20 ; The baffle type anoxic biological filter 1 and the upflow type biological aerated filter 2 are provided with the upper water distribution catchment area 4, the filter plate 5, the suspended ceramsite filter bed 6, and the fluidized filter bed in sequence from top to bottom Buffer zone 7, air distribution device 8 and bottom water distribution and collection device 9; inclined plate sedimentation tank 3 is provided with upper water distribution and catchment area 4, sedimentation area 3-1 and sludge bucket 3-4 from top to bottom, and sedimentation area 3-1 is provided with inclined plate 3-2 and central pipe 3-3; baffled anoxic biological filter 1, upflow biological aerated filter 2 and inclined plate sedimentation tank 3 are connected in sequence.

折流式缺氧生物滤池1被三块竖直挡板分隔成上下折返的第一级缺氧生物滤池1‐1、第二级缺氧生物滤池1‐2和第三级缺氧生物滤池1‐3,第一级缺氧生物滤池1‐1上部配水集水区4与进水管10相连通,底部配水集水装置9与第二级缺氧生物滤池1‐2的底部配水集水装置9连通,第二级缺氧生物滤池1‐2上部配水集水区4和第三级缺氧生物滤池1‐3的上部配水集水区4连接,第三级缺氧生物滤池1‐3的底部配水集水装置9与升流式曝气生物滤池2底部配水集水装置9相连通。升流式曝气生物滤池2上部配水集水区4通过回流管11与第一级缺氧生物滤池1‐1上部配水集水区4相连通,回流管11与配气管12连接,回流管11上设有气提装置11‐1,升流式曝气生物滤池2出水由于重力作用流入回流管11,通过气提装置11‐1与压缩空气作用将升流式曝气生物滤池2的部分出水导向第一级缺氧生物滤池1‐1上部配水集水区4,升流式曝气生物滤池2上部配水集水区4一侧设有集水渠2‐1,集水渠2‐1内部设有曝气混合管15和反冲洗水泵18,曝气混合管15与配气管12连接,反冲洗水泵18通过反冲洗进水管13分别与第一级缺氧生物滤池1‐1、第二级缺氧生物滤池1‐2、第三级缺氧生物滤池1‐3的上部配水集水区4相连接。折流式缺氧生物滤池1和升流式曝气生物滤池2底部布气装置8通过配气管12与鼓风机19连接,底部配水集水装置9与反冲洗排水管14连接。斜板沉淀池3的中心管3‐3与升流式曝气生物滤池2的集水渠2‐1相连通,斜板沉淀池3的上部配水集水区4与出水管16连接,底部污泥斗3‐4则与排泥管17连接。The baffle type anoxic biological filter 1 is separated by three vertical baffles into the first-stage anoxic biological filter 1-1, the second-stage anoxic biological filter 1-2 and the third-stage anoxic Biofilter 1-3, the upper water distribution catchment area 4 of the first-stage anoxic biological filter 1-1 is connected to the water inlet pipe 10, and the bottom water distribution and collection device 9 is connected to the second-stage anoxic biological filter 1-2 The bottom water distribution and collection device 9 is connected, the upper water distribution catchment area 4 of the second-stage anoxic biological filter 1-2 is connected with the upper water distribution catchment area 4 of the third-stage anoxic biological filter 1-3, and the third-stage anoxic biological filter 1-3 is connected. The water distribution and collection device 9 at the bottom of the oxygen biological filter 1-3 communicates with the water distribution and collection device 9 at the bottom of the upflow biological aerated filter 2. The upper water distribution catchment area 4 of the upflow biological aerated filter 2 is connected with the upper water distribution catchment area 4 of the first-stage anoxic biological filter 1-1 through the return pipe 11, and the return pipe 11 is connected with the gas distribution pipe 12, and the return flow An air lift device 11-1 is provided on the pipe 11, and the effluent of the upflow biological aerated filter 2 flows into the return pipe 11 due to the action of gravity, and the upflow biological aerated filter is discharged through the action of the air lift device 11-1 and compressed air. Part of the effluent of 2 is directed to the upper water distribution catchment area 4 of the first-stage anoxic biological filter 1-1, and the upper water distribution catchment area 4 of the upflow biological aerated filter tank 2 is equipped with a water collection channel 2-1 on one side, and the water collection channel 2-1 There is an aeration mixing pipe 15 and a backwashing water pump 18 inside, the aeration mixing pipe 15 is connected to the gas distribution pipe 12, and the backwashing water pump 18 is respectively connected to the first-stage anoxic biological filter 1-1 through the backwashing water inlet pipe 13 1. The upper water distribution catchment area 4 of the second-stage anoxic biological filter 1-2 and the third-stage anoxic biological filter 1-3 are connected. The bottom air distribution device 8 of the baffle type anoxic biological filter 1 and the upflow biological aerated filter 2 is connected to the blower 19 through the air distribution pipe 12 , and the bottom water distribution and collection device 9 is connected to the backwash drain pipe 14 . The central pipe 3-3 of the inclined plate sedimentation tank 3 is connected with the catchment channel 2-1 of the upflow biological aerated filter 2, the upper water distribution catchment area 4 of the inclined plate sedimentation tank 3 is connected with the outlet pipe 16, and the bottom sewage The mud bucket 3‐4 is connected with the mud discharge pipe 17.

第一级缺氧生物滤池1‐1滤料采用粒径为¢12~16mm页岩陶粒,第二级缺氧生物滤池1‐2滤料采用粒径为¢8~12mm页岩陶粒,第三级缺氧生物滤池1‐3滤料采用粒径为¢4~8mm页岩陶粒,升流式曝气生物滤池2滤料采用粒径为¢4~8mm页岩陶粒,上述不同粒径的页岩陶粒水浸润颗粒密度都为0.95±0.5g/cm3,与滤网板5相互作用在水中成悬浮状态,悬浮陶粒滤床6高度为1~2m,滤床流化缓冲区7高度为0.3~0.5m。正常运行时悬浮陶粒滤床6的滤料成膨胀流化状态。进水管10、回流管11、配气管12、反冲洗进水管13、反冲洗排水管14、曝气混合管15、出水管16和排泥管17上都安装有电动阀门22,电动阀门22都与电控柜20连接;电控柜20还分别连接鼓风机19和反冲洗水泵18;电控柜20可控制鼓风机19、反冲洗水泵18和各个管道上的电动阀门22的开关,使该设备按程序正常运行,电控柜20设在斜板沉淀池3外侧,控制反冲洗水泵18、鼓风机19和各个管道电动阀门22的开关,使该设备正常运行。电控柜20包括整套电气设备、手动按钮和触摸屏控制和信号发射接收器;电控柜20通过网络与后台连接,后台通过网络远程控制电控柜20,可以通过网络远程操作,实现设备按程序正常运行,无人值守。该农村污水一体化处理设备为密闭箱体结构,斜板沉淀池3的一侧设有门21。可通过设备门21进入设备内部操作维修相关装置,平时,门21为关闭锁住状态,避免他人进入设备内部。The first-stage anoxic biological filter 1-1 filter material uses shale ceramsite with a particle size of ¢12-16mm, and the second-stage anoxic biological filter 1-2 filter material uses a particle size of ¢8-12mm shale ceramics shale ceramsite with a particle size of ¢4-8mm for the filter material of the third anoxic biological filter 1‐3, and shale ceramsite with a particle size of ¢4~8mm for the filter material of the upflow biological aerated filter 2 The above-mentioned shale ceramsite water infiltration particle density of different particle sizes is 0.95±0.5g/cm 3 , interacts with the filter screen plate 5 to form a suspended state in the water, and the height of the suspended ceramsite filter bed 6 is 1-2m. The height of the fluidized buffer zone 7 of the filter bed is 0.3-0.5m. During normal operation, the filter material of the suspended ceramsite filter bed 6 is in an expanded fluidized state. Water inlet pipe 10, return pipe 11, gas distribution pipe 12, backwash water inlet pipe 13, backwash drain pipe 14, aeration mixing pipe 15, water outlet pipe 16 and mud discharge pipe 17 are all equipped with electric valve 22, and electric valve 22 all It is connected with the electric control cabinet 20; the electric control cabinet 20 is also connected with the air blower 19 and the backwash water pump 18 respectively; The program runs normally, and the electric control cabinet 20 is arranged on the outside of the inclined plate sedimentation tank 3 to control the switch of the backwash water pump 18, the blower 19 and the electric valves 22 of each pipeline to make the equipment run normally. The electric control cabinet 20 includes a complete set of electrical equipment, manual buttons and touch screen control and signal transmitter receivers; the electric control cabinet 20 is connected to the background through the network, and the background remotely controls the electric control cabinet 20 through the network, and can be operated remotely through the network to realize the equipment according to the program Normal operation, unattended. The rural sewage integrated treatment equipment has a closed box structure, and a door 21 is provided on one side of the inclined plate sedimentation tank 3 . The device interior can be accessed through the device door 21 to operate and maintain related devices. Normally, the door 21 is closed and locked to prevent others from entering the device.

应用农村污水一体化处理设备的农村污水一体化处理方法:污水进入折流式缺氧生物滤池1,上下折返依次通过第一级缺氧生物滤池1‐1、第二级缺氧生物滤池1‐2、第三级缺氧生物滤池1‐3,去除有机物和大颗粒悬浮物;第三级缺氧生物滤池1‐3出水从底部配水集水装置9向上均匀配水进入升流式曝气生物滤池2悬浮陶粒滤床6,压缩空气经曝气生物滤池2布气装置8进入悬浮陶粒滤床2进行曝气,硝化氨氮和降解污水中残存有机物,升流出水到达上部配水集水区4;升流式曝气生物滤池2配水集水区4的一部分出水回流到第一级缺氧生物滤池1‐1配水集水区4,与原污水混合,进行反硝化脱氮,另一部分出水则进入集水渠2‐1,压缩空气经曝气混合管15将出水曝气,从而与投加的药剂充分混合进行混凝;经过混凝后的出水进入斜板沉淀池3沉淀区3‐1进行沉淀,从而进一步去除磷、悬浮物和有机物,升流出水通过斜板3‐2进入集水配水区4后汇集至出水管16出水,沉淀到污泥斗3‐4中污泥通过污泥管17排出。Integrated rural sewage treatment method using integrated rural sewage treatment equipment: sewage enters the baffled anoxic biofilter 1, and turns up and down to pass through the first-stage anoxic biofilter 1-1, the second-stage anoxic biofilter Pool 1-2 and third-stage anoxic biofilter 1-3 remove organic matter and large suspended solids; the effluent from third-stage anoxic biofilter 1-3 distributes water upward evenly from the bottom water distribution and collection device 9 and enters the upflow Type biological aerated filter 2 suspended ceramsite filter bed 6, compressed air enters the suspended ceramsite filter bed 2 through the biological aerated filter 2 air distribution device 8 for aeration, nitrifies ammonia nitrogen and degrades the residual organic matter in the sewage, and raises the effluent Reach the upper water distribution catchment area 4; part of the effluent from the upflow biological aerated filter 2 water distribution catchment area 4 returns to the first-stage anoxic biological filter 1-1 water distribution catchment area 4, mixes with raw sewage, and carries out Denitrification and denitrification, the other part of the effluent enters the water collection channel 2-1, and the compressed air passes through the aeration mixing tube 15 to aerate the effluent, so as to fully mix with the dosed chemical for coagulation; the coagulated effluent enters the inclined plate Sedimentation tank 3 Sedimentation area 3-1 conducts sedimentation to further remove phosphorus, suspended solids and organic matter, and the rising effluent enters the water collection and distribution area 4 through the sloping plate 3-2, and then collects to the outlet pipe 16 to discharge the water, and settles to the sludge hopper 3 The sludge in -4 is discharged through the sludge pipe 17.

折流式缺氧生物滤池1运行间隔一段时间需要进行反冲洗恢复其过滤水头,采用气水联合反冲洗。当对第一级缺氧生物滤池1‐1进行反冲洗时,设备停止投加絮凝剂五分钟后停止进水,打开第一级缺氧生物滤池1‐1底部配气管12的电动阀门22,压缩空气经配气管12流向第一级缺氧生物滤池1‐1底部布气装置8,对滤池进行均匀曝气增加悬浮陶粒滤床6流化膨胀程度,脱落生物膜和杂质沉入底部,曝气五分钟后打开反冲洗水泵18将出水渠2‐1较干净的水通过反冲洗进水管14打入第一级缺氧生物滤池1‐1配水集水区4,流入悬浮陶粒滤床6进行气水联合清洗,同时打开底部将含有杂质的污水排出池外,十分钟后关闭反冲洗水泵18并停止曝气和排水,恢复进水和加药,从而完成对第一级缺氧生物滤池1‐1的反冲洗。第二级缺氧生物滤池1‐2和第三级缺氧生物滤池1‐3采用相同方法进行反冲洗。升流式曝气生物滤池2的悬浮陶粒滤床6一直处于曝气流化状态,不需要进行反冲洗。The baffle type anoxic biological filter 1 needs to be backwashed to restore its filtration head after a period of time between operations, and air-water combined backwashing is used. When backwashing the first-stage anoxic biological filter 1-1, the equipment stops adding flocculant for five minutes and then stops water intake, and opens the electric valve of the gas distribution pipe 12 at the bottom of the first-stage anoxic biological filter 1-1 22. The compressed air flows through the air distribution pipe 12 to the air distribution device 8 at the bottom of the first-stage anoxic biological filter 1-1, and evenly aerates the filter to increase the fluidization expansion degree of the suspended ceramsite filter bed 6, and shed biofilm and impurities Sink to the bottom, open the backwash water pump 18 after five minutes of aeration, and pump the clean water from the outlet channel 2-1 through the backwash inlet pipe 14 into the first-stage anoxic biological filter 1-1 water distribution catchment area 4, and flow into The suspended ceramsite filter bed 6 is combined with air and water for cleaning, and at the same time, the bottom is opened to discharge the sewage containing impurities out of the pool. After ten minutes, the backwashing water pump 18 is turned off and the aeration and drainage are stopped, and the water intake and dosing are resumed, thereby completing the second stage. Backwashing of primary anoxic biofilter 1‐1. The second-stage anoxic biofilter 1-2 and the third-stage anoxic biofilter 1-3 are backwashed in the same way. The suspended ceramsite filter bed 6 of the upflow biological aerated filter 2 is always in the state of aeration and fluidization, and no backwashing is required.

本发明采用同类生物滤池折流串联,具有预处理功能,共用曝气和气水反冲洗系统,同时采用气提回流,高度集成一体化,投资运行费用经济。The invention adopts similar biological filters to be baffled and connected in series, has a pretreatment function, shares aeration and air-water backwashing systems, and adopts air-lifting and reflux at the same time, is highly integrated, and has economical investment and operation costs.

本发明采用不同粒径页岩陶粒滤料,同时预留滤床流化缓冲区,正常运行滤料为流化状态,不宜板结,反冲洗周期长,滤料使用寿命长,运行维护成本低。The present invention uses shale ceramsite filter materials with different particle sizes, and reserves a fluidized buffer zone for the filter bed. The filter material is in a fluidized state during normal operation, and is not suitable for compaction. The backwash cycle is long, the service life of the filter material is long, and the operation and maintenance cost is low. .

本发明集污水初滤、回流反硝化脱氮、生物降解硝化、混凝沉淀除磷等功能于一体,生物膜活性强,更新条件好,稳定可靠,高效节能。The invention integrates the functions of primary sewage filtration, reflux denitrification and denitrification, biodegradation and nitrification, coagulation and precipitation phosphorus removal, etc., and has strong biofilm activity, good renewal conditions, stability and reliability, and high efficiency and energy saving.

本发明自动化管理简单可靠,电控柜可控制鼓风机、排泥泵、潜水泵和各个管道电动阀门的开关,使该设备按程序正常运行,也可通过网络远程控制电控柜可实现无人值守,适用于农村污水处理。The automatic management of the present invention is simple and reliable, and the electric control cabinet can control the switch of blower, mud pump, submersible pump and electric valves of each pipeline, so that the equipment can operate normally according to the program, and the electric control cabinet can be remotely controlled through the network to realize unattended operation , suitable for rural sewage treatment.

Claims (9)

1.一种农村污水一体化处理设备,其特征在于,主要包括折流式缺氧生物滤池、升流式曝气生物滤池、斜板沉淀池和电控柜;所述折流式缺氧生物滤池被三块竖直挡板分隔成上下折返的第一级缺氧生物滤池、第二级缺氧生物滤池和第三级缺氧生物滤池;第一级缺氧生物滤池、第二级缺氧生物滤池、第三级缺氧生物滤池和升流式曝气生物滤池自上而下依次设有上部配水集水区、滤网板、悬浮陶粒滤床、滤床流化缓冲区、布气装置和底部配水集水装置;第一级缺氧生物滤池上部配水集水区与进水管相连通,底部配水集水装置与第二级缺氧生物滤池的底部配水集水装置连通,第二级缺氧生物滤池上部配水集水区和第三级缺氧生物滤池的上部配水集水区连接,第三级缺氧生物滤池的底部配水集水装置与升流式曝气生物滤池底部配水集水装置相连通;1. A rural sewage integrated treatment equipment is characterized in that it mainly includes a baffle type anoxic biological filter, an upflow type biological aerated filter, an inclined plate sedimentation tank and an electric control cabinet; The oxygen biofilter is separated by three vertical baffles into the first-stage anoxic biofilter, the second-stage anoxic biofilter and the third-stage anoxic biofilter; the first-stage anoxic biofilter Pool, the second-stage anoxic biological filter, the third-stage anoxic biological filter and the upflow biological aerated filter are provided with the upper water distribution catchment area, filter plate, and suspended ceramsite filter bed in sequence from top to bottom. , filter bed fluidization buffer zone, air distribution device and bottom water distribution and collection device; the upper water distribution and collection area of the first-stage anoxic biological filter is connected to the water inlet pipe, and the bottom water distribution and collection device is connected to the second-stage anoxic biological filter The bottom water distribution and collection device of the pool is connected, the upper water distribution catchment area of the second-stage anoxic biological filter is connected with the upper water distribution catchment area of the third-stage anoxic biological filter, and the bottom water distribution of the third-stage anoxic biological filter The water collecting device is connected with the water distribution and collecting device at the bottom of the upflow biological aerated filter; 所述升流式曝气生物滤池上部配水集水区通过回流管与第一级缺氧生物滤池上部配水集水区相连通,回流管与配气管连接,回流管上设有气提装置,升流式曝气生物滤池上部配水集水区一侧设有集水渠,集水渠内部设有曝气混合管和反冲洗水泵,曝气混合管与配气管连接,反冲洗水泵通过反冲洗进水管分别与第一级缺氧生物滤池、第二级缺氧生物滤池、第三级缺氧生物滤池的上部配水集水区相连接;折流式缺氧生物滤池和升流式曝气生物滤池底部布气装置通过配气管与鼓风机连接,底部配水集水装置与反冲洗排水管连接;The upper water distribution catchment area of the upflow biological aerated filter is connected with the upper water distribution catchment area of the first-stage anoxic biological filter through the return pipe, the return pipe is connected with the gas distribution pipe, and the return pipe is provided with an air lift device , There is a collection channel on one side of the upper water distribution catchment area of the upflow biological aerated filter tank, and an aeration mixing pipe and a backwash water pump are installed inside the water collection canal. The aeration mixing pipe is connected to the air distribution pipe, and the backwash water pump passes The water inlet pipes are respectively connected to the upper water distribution catchment area of the first-stage anoxic biological filter, the second-stage anoxic biological filter, and the third-stage anoxic biological filter; the baffle-type anoxic biological filter and the upflow The air distribution device at the bottom of the biological aerated filter is connected to the blower through the air distribution pipe, and the water distribution and collection device at the bottom is connected to the backwash drainage pipe; 所述斜板沉淀池自上而下依次设有上部配水集水区、沉淀区和污泥斗,沉淀区设有斜板和中心管;所述斜板沉淀池的中心管与升流式曝气生物滤池的集水渠相连通,斜板沉淀池的上部配水集水区与出水管连接,底部污泥斗与排泥管连接;The inclined plate sedimentation tank is provided with an upper water distribution catchment area, a sedimentation area and a sludge hopper in sequence from top to bottom, and the sedimentation area is provided with an inclined plate and a central pipe; the central pipe of the inclined plate sedimentation tank is connected with the upflow type The water collection channel of the gas biological filter is connected, the upper water distribution catchment area of the inclined plate sedimentation tank is connected with the outlet pipe, and the bottom sludge bucket is connected with the sludge discharge pipe; 所述进水管、回流管、出水管、配气管、反冲洗进水管、反冲洗排水管、曝气混合管、出水管和排泥管安装有电动阀门,所述电动阀门都与电控柜连接;电控柜还分别连接鼓风机和反冲洗水泵。The water inlet pipe, return pipe, water outlet pipe, gas distribution pipe, backwash water inlet pipe, backwash drain pipe, aeration mixing pipe, water outlet pipe and mud discharge pipe are equipped with electric valves, and the electric valves are all connected to the electric control cabinet ; The electric control cabinet is also connected to the air blower and the backwash water pump respectively. 2.根据权利要求1所述农村污水一体化处理设备,其特征在于,所述第一级缺氧生物滤池滤料采用粒径为¢12~16mm页岩陶粒;所述第二级缺氧生物滤池滤料采用粒径为¢8~12mm页岩陶粒;所述第三级缺氧生物滤池滤料采用粒径为¢4~8mm页岩陶粒。2. The rural sewage integrated treatment equipment according to claim 1, characterized in that, the filter material of the first-stage anoxic biological filter adopts shale ceramsite with a particle size of ¢12-16mm; The filter material of the oxygen biological filter uses shale ceramsite with a particle size of ¢8-12 mm; the filter material of the third-stage anoxic biological filter uses shale ceramsite with a particle size of ¢4-8 mm. 3.根据权利要求1所述农村污水一体化处理设备,其特征在于,所述升流式曝气生物滤池滤料采用粒径为¢4~8mm页岩陶粒。3. The rural sewage integrated treatment equipment according to claim 1, characterized in that the filter material of the upflow biological aerated filter adopts shale ceramsite with a particle size of ¢4-8mm. 4.根据权利要求2或3所述农村污水一体化处理设备,其特征在于,不同粒径的页岩陶粒水浸润颗粒密度为0.95±0.5g/cm3,与滤网板相互作用在水中成悬浮状态。4. The rural sewage integrated treatment equipment according to claim 2 or 3, characterized in that the shale ceramsite water infiltration particle density of different particle sizes is 0.95±0.5g/cm 3 , and interacts with the filter screen plate in water into a suspended state. 5.根据权利要求1所述农村污水一体化处理设备,其特征在于,所述悬浮陶粒滤床的高度为1~2m,所述滤床流化缓冲区的高度为0.3~0.5m。5. The rural sewage integrated treatment equipment according to claim 1, characterized in that the height of the suspended ceramsite filter bed is 1-2m, and the height of the fluidized buffer zone of the filter bed is 0.3-0.5m. 6.根据权利要求1所述农村污水一体化处理设备,其特征在于,电控柜通过网络与后台连接。6. The rural sewage integrated treatment equipment according to claim 1, characterized in that the electric control cabinet is connected to the background through the network. 7.根据权利要求1所述农村污水一体化处理设备,其特征在于,所述电控柜设在斜板沉淀池的外侧。7. The rural sewage integrated treatment equipment according to claim 1, characterized in that, the electric control cabinet is arranged outside the inclined plate sedimentation tank. 8.根据权利要求1所述农村污水一体化处理设备,其特征在于,所述斜板沉淀池的一侧设有门。8. The rural sewage integrated treatment equipment according to claim 1, wherein a door is provided on one side of the inclined plate sedimentation tank. 9.应用权利要求1所述设备的农村污水一体化处理方法,其特征在于,污水进入折流式缺氧生物滤池,上下折返依次通过第一级缺氧生物滤池、第二级缺氧生物滤池和第三级缺氧生物滤池,去除有机物和大颗粒悬浮物;第三级缺氧生物滤池出水从底部配水集水装置向上均匀配水进入升流式曝气生物滤池;压缩空气经布气装置进入升流式曝气生物滤池进行曝气,硝化氨氮和降解污水中残存有机物;升流式曝气生物滤池的升流出水到达上部配水集水区;升流式曝气生物滤池配水集水区的一部分出水回流到第一级缺氧生物滤池配水集水区,与原污水混合,进行反硝化脱氮,另一部分出水进入集水渠,压缩空气经曝气混合管将出水曝气,与投加的药剂充分混合进行混凝;经过混凝后的出水进入斜板沉淀池沉淀区进行沉淀,进一步去除磷、悬浮物和有机物,升流出水通过沉淀区斜板进入集水配水区后汇集至出水管出水,沉淀到污泥斗中污泥通过污泥管排出。9. The rural sewage integrated treatment method using the equipment described in claim 1 is characterized in that, the sewage enters the baffle type anoxic biological filter, and turns up and down to pass through the first-level anoxic biological filter and the second-level anoxic biological filter successively. The biological filter and the third-stage anoxic biological filter remove organic matter and large suspended particles; the effluent of the third-stage anoxic biological filter is evenly distributed upward from the bottom water distribution and collection device into the upflow biological aerated filter; compression The air enters the upflow biological aerated filter through the air distribution device for aeration, nitrifies ammonia nitrogen and degrades the residual organic matter in the sewage; the upflow effluent of the upflow biological aerated filter reaches the upper water distribution catchment area; the upflow aeration Part of the effluent from the distribution catchment area of the aerobic biological filter flows back to the distribution catchment area of the first-stage anoxic biological filter, where it is mixed with the raw sewage for denitrification and denitrification, and the other part of the effluent enters the catchment channel, and the compressed air is aerated and mixed The tube aerates the effluent and fully mixes it with the dosing agent for coagulation; the coagulated effluent enters the sedimentation zone of the inclined plate sedimentation tank for sedimentation, further removes phosphorus, suspended solids and organic matter, and the effluent passes through the inclined plate of the sedimentation zone After entering the water collection and distribution area, it is collected to the outlet pipe to discharge the water, and the sludge is deposited in the sludge hopper and discharged through the sludge pipe.
CN201810031812.0A 2018-01-12 2018-01-12 A kind of country sewage integrated equipment for wastewater treatment and processing method Pending CN108328854A (en)

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