CN101525204A - Method for treating village sewage and specific device thereof - Google Patents

Method for treating village sewage and specific device thereof Download PDF

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CN101525204A
CN101525204A CN200910082852A CN200910082852A CN101525204A CN 101525204 A CN101525204 A CN 101525204A CN 200910082852 A CN200910082852 A CN 200910082852A CN 200910082852 A CN200910082852 A CN 200910082852A CN 101525204 A CN101525204 A CN 101525204A
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sewage
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CN101525204B (en
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李仰斌
谢崇宝
张国华
籍国东
周游
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Beijing Zhongguan Lvyuan International Consulting Co Ltd
CHINA IRRIGATION AND DRAINAGE DEVELOPMENT CENTER
Peking University
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CHINA IRRIGATION AND DRAINAGE DEVELOPMENT CENTER
Peking University
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Abstract

本发明公开了一种乡村污水处理方法及其专用装置,所述专用装置包括潜污泵及与之相连的多功能折流处理模块,所述多功能折流处理模块顺次包括1-3号池三个厌氧单元、4-5号池两个好氧单元和6号池一个沉淀单元,它们之间通过管道连接;厌氧单元均设有排气孔,好氧单元内均设有悬空的上、下钢丝网,钢丝网之间的隔室内填充填料,下层的钢丝网上设有与曝气机相连的布气孔。所述方法的具体操作步骤详见说明书。本发明所述的方法及专用装置是综合运用沉淀、过滤等物理处理技术和厌氧氧化、好氧氧化等生化处理技术,使污水中的有机物得以降解,无机盐得以固定,氮磷等营养物得以降低,具有水力负荷大并且处理后水质好的优点,特别适合我国的国情需要。

Figure 200910082852

The invention discloses a rural sewage treatment method and its special device. The special device includes a submersible sewage pump and a multifunctional baffle treatment module connected thereto. The multifunctional baffle treatment module sequentially includes No. 1-3 There are three anaerobic units in the pool, two aerobic units in the No. 4-5 pool and one sedimentation unit in the No. 6 pool. They are connected by pipelines; the anaerobic units are equipped with exhaust holes, and the aerobic units are equipped with suspended air vents. The upper and lower steel wire meshes, the compartments between the steel meshes are filled with fillers, and the lower steel meshes are provided with air distribution holes connected with the aerator. The specific operation steps of the method are detailed in the instructions. The method and the special device of the present invention comprehensively use physical treatment technologies such as sedimentation and filtration and biochemical treatment technologies such as anaerobic oxidation and aerobic oxidation, so that organic matter in sewage can be degraded, inorganic salts can be fixed, and nutrients such as nitrogen and phosphorus can be degraded. It can be reduced, has the advantages of large hydraulic load and good water quality after treatment, and is especially suitable for my country's national conditions.

Figure 200910082852

Description

一种乡村污水处理方法及其专用装置 A rural sewage treatment method and its special device

技术领域 technical field

本发明涉及污水处理的装置及方法,特别涉及一种乡村污水处理方法及其专用装置,具体采用多功能折流组合生物滤池处理方式。The invention relates to a sewage treatment device and method, in particular to a rural sewage treatment method and a special device thereof, specifically adopting a multifunctional baffle combined biological filter treatment method.

背景技术 Background technique

长期以来,广大农村地区的生活排水、生活垃圾和农业废弃物任意排放的问题未引起根本重视,人畜粪便、生活垃圾和生活排水等废弃物大部分没有得到处理,随意堆放在道路两旁、田边地头、水塘沟渠或直接排放到河渠等水体中,使“污水乱泼、垃圾乱倒、粪土乱堆、柴草乱跺、畜禽乱跑”、“室内现代化,室外脏乱差”已成为一些农村生态环境的真实写照。据统计,目前我国96%的村庄没有排水渠道和污水处理系统,生产生活污水随意排放,已成为农村水源地潜在的安全隐患、社会主义新农村和谐发展的重要制约因素。未经处理的农村生活污水,一方面,是农村饮用水源地潜在的安全隐患;另一方面,其中含有较多的氮和磷,也是江河湖泊富营养化的重要原因之一。因此,加强农村生活排水收集、处理与资源化设施建设,避免因生活污水直接排放而引起农村水体、土壤和农产品的污染,确保农村水源安全和农民身体健康,既是新农村建设中加强基础设施建设、推进村庄整治工作的一项重要内容,也是当前农村人居环境改善需要解决的最急需、最迫切、最突出的问题,具有重要的现实意义。For a long time, the problem of random discharge of domestic drainage, domestic garbage and agricultural waste in vast rural areas has not attracted fundamental attention. Most of the wastes such as human and animal manure, domestic garbage and domestic drainage have not been treated, and they are randomly piled on both sides of the road and beside the fields. Fields, ponds, ditches or directly discharged into water bodies such as rivers and canals, making "sewage splashing, garbage dumping, excrement piles, firewood stomping, livestock and poultry running around", "indoor modernization, outdoor dirty and messy" have become some A true portrayal of the rural ecological environment. According to statistics, at present, 96% of villages in my country do not have drainage channels and sewage treatment systems, and the random discharge of production and domestic sewage has become a potential safety hazard in rural water sources and an important restrictive factor for the harmonious development of a new socialist countryside. Untreated rural domestic sewage, on the one hand, is a potential safety hazard in rural drinking water sources; on the other hand, it contains more nitrogen and phosphorus, which is also one of the important reasons for the eutrophication of rivers and lakes. Therefore, strengthening the construction of rural domestic drainage collection, treatment and resource utilization facilities, avoiding the pollution of rural water bodies, soil and agricultural products caused by the direct discharge of domestic sewage, and ensuring the safety of rural water sources and the health of farmers are not only the strengthening of infrastructure construction in the construction of new countryside It is an important content to promote village renovation work, and it is also the most urgent, urgent and prominent problem that needs to be solved in the improvement of rural human settlements, and it has important practical significance.

然而,目前我国城市生活污水采用的大规模集中处理方式不适合在广大农村地区推广应用,主要表现为:大规模的集中处理厂需要较大的工程费用来建立复杂的排水管网。在人口密度很低的地区,这项投资将比污水处理厂的总投资高出一个数量级。特别是在农村地区,居住群比较分散,这项费用将更高。此外,管道修复费用也非常昂贵。污水生态处理技术因其工程造价低、运行费用少、基建材料易得、操作简便、处理效果好而受到国内外的普遍重视,包括美、日、英、法、俄等国在内的许多国家都在广泛采用这项技术处理生活排水。我国在“七五”、“八五”、“九五”和“十五”期间,国内的许多科研机构已经开展了大量采用无电力厌氧和生态技术处理小城镇生活排水、小区生活排水和工业排水的试验研究和工程示范,获取了多项不同类型具有自主知识产权的生态处理实用技术。这些单位先后开展了原生介质条件下,人工湿地、毛管浸润和快速渗滤等系列生态技术处理城市生活排水的可行性,获取了系列重要参数,并在嘉兴、沈阳、深圳和盘锦等不同地区进行了工程示范。但是,农村生活排水的特点是分散、量小、远离群居和大水体、水环境容量小及管理水平低,如果将这些技术应用于农村生活排水处理,还存在污染物去除通量低、终年运行不稳定、基质滤料易堵塞、除磷脱氮效率差、运行费用高或浪费土地资源等技术方面的制约瓶颈。However, the large-scale centralized treatment methods currently adopted in my country's urban domestic sewage are not suitable for popularization and application in rural areas. The main performance is that large-scale centralized treatment plants require large engineering costs to establish complex drainage pipe networks. In areas with very low population densities, this investment will be an order of magnitude higher than the total investment in a sewage treatment plant. Especially in rural areas, where the settlements are more dispersed, this cost will be higher. Additionally, plumbing repairs can be very expensive. Sewage ecological treatment technology has been widely valued at home and abroad because of its low engineering cost, low operating cost, easy access to infrastructure materials, simple operation, and good treatment effect. Many countries, including the United States, Japan, Britain, France, Russia, etc. This technology is widely used to treat domestic drainage. During the "Seventh Five-Year Plan", "Eighth Five-Year Plan", "Ninth Five-Year Plan" and "Tenth Five-Year Plan" in our country, many domestic scientific research institutions have carried out a large number of non-electric anaerobic and ecological technologies to treat small town domestic drainage, community domestic drainage and The experimental research and engineering demonstration of industrial drainage have obtained a number of different types of practical technologies for ecological treatment with independent intellectual property rights. These units successively carried out the feasibility of treating urban domestic drainage with a series of ecological technologies such as artificial wetland, capillary infiltration and rapid infiltration under the condition of primary media, obtained a series of important parameters, and carried out research in different areas such as Jiaxing, Shenyang, Shenzhen and Panjin. engineering demonstration. However, rural domestic drainage is characterized by dispersal, small volume, far away from groups and large water bodies, small water environment capacity, and low management level. If these technologies are applied to rural domestic drainage treatment, there are still problems such as low pollutant removal flux and year-round operation. Unstable, easy clogging of matrix filter material, poor phosphorus and nitrogen removal efficiency, high operating costs or waste of land resources and other technical constraints.

发明内容 Contents of the invention

本发明的目的是针对上述现有技术的缺陷,提供了一种乡村污水处理方法及其专用装置,该方法及专用装置是综合运用沉淀、过滤等物理处理技术和厌氧氧化、好氧氧化等生化处理技术,使污水中的有机物得以降解,无机盐得以固定,氮磷等营养物得以降低,具有水力负荷大并且处理后水质好的优点,特别适合我国的国情需要。The purpose of the present invention is to address the above-mentioned defects in the prior art, and to provide a rural sewage treatment method and a special device thereof. Biochemical treatment technology degrades organic matter in sewage, fixes inorganic salts, and reduces nutrients such as nitrogen and phosphorus. It has the advantages of large hydraulic load and good water quality after treatment, and is especially suitable for my country's national conditions.

为了实现上述目的本发明采取的技术方案是:一种乡村污水处理专用装置,包括潜污泵及与其相连的多功能折流处理模块,所述多功能折流处理模块按照污水流动方向顺次包括六个池,分别为三个厌氧单元、两个好氧单元和一个沉淀单元,相邻的处理单元通过管道分段连接;其中1号池、2号池及3号池为厌氧单元并且每个单元均设有排气孔,潜污泵连接1号池,3号池内设有三相分布器;4号池和5号池为好氧单元并且池内均设有悬空的上、下钢丝网,上、下钢丝网形成隔室、隔室内填充用于好氧反应的填料,下层的钢丝网上设有布气孔,布气孔通过布气管与曝气机相连;6号池为沉淀单元。所述多功能折流处理模块集化粪池、厌氧处理、好氧处理、生物浮动床、沉淀等功能于一体,污水中的有机物在厌氧和好氧微生物的作用下转化成无害的物质。In order to achieve the above object, the technical solution adopted by the present invention is: a special device for rural sewage treatment, including a submersible sewage pump and a multifunctional baffle treatment module connected to it, and the multifunctional baffle treatment module includes sequentially according to the sewage flow direction There are six pools, which are three anaerobic units, two aerobic units and one sedimentation unit, and the adjacent treatment units are connected by pipeline segments; among them, No. 1 pool, No. 2 pool and No. 3 pool are anaerobic units and Each unit is equipped with an exhaust hole, the submersible sewage pump is connected to No. 1 pool, and a three-phase distributor is installed in No. 3 pool; No. 4 pool and No. 5 pool are aerobic units, and the pools are equipped with suspended upper and lower steel wire mesh , the upper and lower wire meshes form compartments, and the compartments are filled with fillers for aerobic reactions. The lower steel wire mesh is provided with air distribution holes, which are connected to the aerator through air distribution pipes; the No. 6 pool is a sedimentation unit. The multi-functional baffle treatment module integrates the functions of septic tank, anaerobic treatment, aerobic treatment, biological floating bed, sedimentation, etc., and the organic matter in the sewage is converted into harmless substance.

为了对出水水质做深度处理,所述的乡村污水处理专用装置,还包括通过管道与所述多功能折流处理模块出水口相连接的多介质生态渗滤模块,多介质生态渗滤模块为含有多介质滤料层的滤池。多介质生态渗滤模块作为多功能折流处理模块的深度处理单元,能够进一步去除污水中的总氮、总磷、悬浮物和COD(Chemical Oxygen Demand化学需氧量),使得出水水质满足《城镇污水处理厂污染物排放标准》(GB18918-2002)二级标准。In order to perform advanced treatment on the water quality of the effluent, the special device for rural sewage treatment also includes a multi-media ecological infiltration module connected to the outlet of the multi-functional baffle treatment module through a pipeline, and the multi-media ecological infiltration module contains A filter with a multi-media filter layer. As the advanced treatment unit of the multi-functional baffle treatment module, the multi-media ecological infiltration module can further remove total nitrogen, total phosphorus, suspended solids and COD (Chemical Oxygen Demand) in the sewage, so that the effluent quality meets the "urban Discharge Standard of Pollutants for Sewage Treatment Plants (GB18918-2002) Secondary Standard.

所述的乡村污水处理专用装置,多介质生态渗滤模块的上部为曝气材料,具体为大孔网状载体;下部的填料至少由4层组成。每一层填料的底部为透水滤层,顶部为多介质滤料层;其中,每一层顶部的多介质滤料层为多介质滤料和透水滤料交替填充,此即形成“品”字形填充。作为优选,所述多介质滤料层的填充物为多介质滤料,以人工合成的功能陶粒为主,辅以粒径大于2mm的改性沸石,功能陶粒与粒径大于2mm的改性沸石的填充比例范围为体积比1∶10~5∶1。透水滤层的填充物为透水滤料,由粒径为3-40mm的砾石和粒径大于2mm的改性沸石组成,平均粒径为10mm的砾石与粒径大于2mm的改性沸石的填充比例为体积比10∶1~1∶1。In the special device for rural sewage treatment, the upper part of the multi-media ecological infiltration module is an aeration material, specifically a macroporous mesh carrier; the lower part of the filler is composed of at least 4 layers. The bottom of each layer of packing is a water-permeable filter layer, and the top is a multi-media filter material layer; among them, the multi-media filter material layer on the top of each layer is alternately filled with multimedia filter material and water-permeable filter material, which forms the shape of "product" filling. As a preference, the filler of the multi-media filter material layer is a multi-media filter material, which is mainly artificially synthesized functional ceramsite, supplemented by modified zeolite with a particle size greater than 2mm, and functional ceramsite and modified zeolite with a particle size greater than 2mm. The filling ratio range of the non-toxic zeolite is 1:10 to 5:1 by volume. The filler of the permeable filter layer is a permeable filter material, which is composed of gravel with a particle size of 3-40mm and modified zeolite with a particle size larger than 2mm. The filling ratio of gravel with an average particle size of 10mm to modified zeolite with a particle size larger than 2mm The volume ratio is 10:1 to 1:1.

为了延长污水的处理时间,所述单元之间连接的管道为折流管。In order to prolong the treatment time of sewage, the pipes connected between the units are baffle pipes.

为了方便污泥的排出,所述单元靠近底部处设有排泥孔。In order to facilitate the discharge of sludge, the unit is provided with a sludge discharge hole near the bottom.

为了防止生物反应器堵塞并进一步提高活性污泥脱氮效率,所述填料为大孔状的聚氨酯填料。In order to prevent the blockage of the bioreactor and further improve the denitrification efficiency of the activated sludge, the filler is a macroporous polyurethane filler.

为了分散水流的冲击,进一步沉淀污水中的污泥,伸入所述6号池内的折流管为散水管,散水管的端口为喇叭状。In order to disperse the impact of the water flow and further settle the sludge in the sewage, the baffle pipe extending into the No. 6 pool is a water diversion pipe, and the port of the water diversion pipe is trumpet-shaped.

本发明还包括一方法,是根据所述的乡村污水处理专用装置的乡村污水处理方法,具体包括如下步骤:The present invention also includes a method, which is a rural sewage treatment method according to the special device for rural sewage treatment, which specifically includes the following steps:

步骤A  将污水输送至1号池,并经由1号池厌氧氧化池进行化粪和调节水质处理;Step A Transport the sewage to the No. 1 pool, and carry out septic and water quality treatment through the anaerobic oxidation pool of the No. 1 pool;

步骤B  经1号池处理过的污水通过管道进入2号池厌氧氧化池进行厌氧处理;Step B The sewage treated in No. 1 pool enters the anaerobic oxidation pool of No. 2 pool through the pipeline for anaerobic treatment;

步骤C  经2号池处理过的污水通过管道进入3号池厌氧氧化池,在3号池中三相分布器的作用下将水、污泥、气分离,水经过管道进入4号池,污泥沉淀至池底,气体通过排气口排出;Step C The sewage treated in the No. 2 pool enters the anaerobic oxidation pool of the No. 3 pool through the pipeline, and the water, sludge and gas are separated under the action of the three-phase distributor in the No. 3 pool, and the water enters the No. 4 pool through the pipeline. The sludge settles to the bottom of the tank, and the gas is discharged through the exhaust port;

步骤D  经3号池处理过的污水通过管道进入4号池有氧氧化池,对4号池进行曝气作有氧氧化处理;Step D The sewage treated in the No. 3 pool enters the aerobic oxidation pool of the No. 4 pool through the pipeline, and aerates the No. 4 pool for aerobic oxidation treatment;

步骤E  污水通过管道进入5号池有氧氧化池,重复上述步骤D;Step E The sewage enters the aerobic oxidation pool of No. 5 pool through the pipeline, and repeats the above step D;

步骤F  经5号池处理过的污水后进入6号池沉淀,进一步沉淀污水的悬浮物,最终排出满足标准要求的处理水。Step F The sewage treated in the No. 5 pool enters the No. 6 pool for sedimentation, further sediments the suspended solids of the sewage, and finally discharges the treated water that meets the standard requirements.

所述的方法是集化粪池、厌氧处理、好氧处理、生物浮动床、沉淀等功能于一体,使污水中的有机物在厌氧和好氧微生物的作用下转化成无害的物质。The method integrates the functions of septic tank, anaerobic treatment, aerobic treatment, biological floating bed, sedimentation, etc., so that the organic matters in the sewage can be transformed into harmless substances under the action of anaerobic and aerobic microorganisms.

所述乡村污水处理方法,还包括通过多介质生态渗滤模块的运行过程,具体的是污水经过滤池填料表面的布水管逐级通过由多介质滤料层和透水滤层组成的“品”字形滤料层,进入滤池底部的集水槽后排出。污水经多功能折流处理模块流经多介质生态滤池时,污染物被多介质滤料拦截和吸附在其表面,微生物利用有机物进行生长繁殖,并附着在滤料上形成生物膜。经过一段时间,生物膜成熟,栖息在生物膜上的微生物以流经表明的有机物作为营养,对污水中的有机物进行吸附、分解氧化,从而使流过生态滤池的污水得到净化。The rural sewage treatment method also includes the operation process of the multi-media ecological infiltration module. Specifically, the sewage passes through the water distribution pipes on the surface of the filter tank filler step by step through the "product" composed of a multi-media filter material layer and a water-permeable filter layer. The zigzag filter material layer enters the sump at the bottom of the filter and is discharged. When the sewage flows through the multi-media ecological filter through the multi-functional baffle treatment module, the pollutants are intercepted and adsorbed on the surface of the multi-media filter material, and the microorganisms use the organic matter to grow and reproduce, and attach to the filter material to form a biofilm. After a period of time, the biofilm matures, and the microorganisms inhabiting the biofilm use the organic matter flowing through the surface as nutrients to adsorb, decompose and oxidize the organic matter in the sewage, thereby purifying the sewage flowing through the ecological filter.

所述乡村污水处理方法,其中,所述步骤D及E中的曝气采用间歇曝气方式。采用有利于反硝化脱氮的间歇曝气方式,曝气量仅为普通活性污泥和固定床反应器的1/3~1/5。The rural sewage treatment method, wherein the aeration in the steps D and E adopts intermittent aeration. The intermittent aeration method that is beneficial to denitrification and denitrification is adopted, and the aeration rate is only 1/3 to 1/5 of that of ordinary activated sludge and fixed bed reactors.

本发明的有益效果可概括为以下五个方面:Beneficial effects of the present invention can be summarized as following five aspects:

①相比现有技术,本发明所述乡村污水处理专用装置中的多功能折流处理模块作为多介质生态渗滤模块的预处理装置,具有去除有机物能力强的特点,有效解决了因污水中较高有机物浓度造成多介质生态滤池中生物膜内层厌氧微生物大量繁殖,产生厌氧微分解产物,从而影响出水水质的问题,同时也能有效解决因生物膜过厚,使滤料间孔隙变小,滤池通风情况变差,影响氧的进入,甚至造成滤料堵塞的问题。①Compared with the prior art, the multi-functional baffle treatment module in the rural sewage treatment special device of the present invention is used as a pretreatment device of the multi-media ecological percolation module, which has the characteristics of strong ability to remove organic matter, and effectively solves the problem of sewage caused by The high concentration of organic matter causes a large number of anaerobic microorganisms in the inner layer of the biofilm in the multi-media ecological filter to produce anaerobic micro-decomposition products, thereby affecting the water quality of the effluent. The smaller the pores, the worse the ventilation of the filter, affecting the entry of oxygen, and even causing the problem of filter blockage.

②相比现有技术,本发明所述乡村污水处理专用装置中的多介质生态渗滤模块作为多功能折流处理模块的深度处理单元,能够进一步去除污水中的总氮、总磷、悬浮物和COD,使得出水水质满足《城镇污水处理厂污染物排放标准》(GB18918-2002)二级标准。②Compared with the prior art, the multi-media ecological infiltration module in the special device for rural sewage treatment according to the present invention is used as an advanced treatment unit of the multifunctional baffle treatment module, which can further remove total nitrogen, total phosphorus, and suspended solids in sewage and COD, making the effluent quality meet the secondary standard of the Discharge Standard of Pollutants for Urban Sewage Treatment Plants (GB18918-2002).

③相比现有技术,本发明所述乡村污水处理专用装置中的多功能折流处理模块同时具有化粪池、厌氧悬浮、生物浮动床和沉淀池功能,集厌氧、好氧过程于一体,具有占地面积小、基建投资省,运行费用低(或无),不易堵塞、管理方便,无潜在生态安全隐患,且能够全年运行等特点。③Compared with the prior art, the multifunctional baffle treatment module in the rural sewage treatment special device of the present invention has the functions of septic tank, anaerobic suspension, biological floating bed and sedimentation tank at the same time, integrating anaerobic and aerobic processes into one Integrated, it has the characteristics of small footprint, low infrastructure investment, low (or none) operating costs, not easy to block, convenient management, no potential ecological safety hazards, and can be operated all year round.

④相比现有技术,本发明所述乡村污水处理专用装置中的多介质生态渗滤模块采用“品”字形填料方法,达到既能保证流量又能保证停留时间的平衡点。多介质生态滤池中的多介质滤层是净水介质,透水滤层是水流通道,净水介质和水流通道的功能分异,即可增加污染物的反应时间又可有效防止多介质生态渗滤模块的堵塞。④Compared with the prior art, the multi-media ecological infiltration module in the rural sewage treatment special device of the present invention adopts the "pin"-shaped packing method to achieve a balance point that can ensure both the flow rate and the residence time. The multi-media filter layer in the multi-media ecological filter is the water purification medium, and the permeable filter layer is the water flow channel. The function differentiation of the water purification medium and the water flow channel can increase the reaction time of pollutants and effectively prevent the multi-media ecological seepage. Blockage of the filter module.

⑤相比现有技术,本发明所述乡村污水处理方法是集成了物理处理法、厌氧处理法、活性污泥法和生物膜法等污水处理技术,使污水中的有机物得以降解,无机盐得以固定,氮磷等营养物得以降低,具有水力负荷大并且处理后水质好的优点,特别适合我国的国情需要。5. Compared with the prior art, the rural sewage treatment method of the present invention integrates sewage treatment technologies such as physical treatment method, anaerobic treatment method, activated sludge method and biofilm method, so that the organic matter in the sewage can be degraded, and the inorganic salt It can be fixed, nutrients such as nitrogen and phosphorus can be reduced, and has the advantages of large hydraulic load and good water quality after treatment, which is especially suitable for my country's national conditions.

附图说明 Description of drawings

图1是本发明所述乡村污水处理专用装置的平面布置图;Fig. 1 is the plane layout drawing of the rural sewage treatment special device of the present invention;

图2是图1中沿A-A线的剖视图;Fig. 2 is a sectional view along line A-A in Fig. 1;

图3是图1中沿B-B线的剖视图;Fig. 3 is a sectional view along line B-B in Fig. 1;

图4是图1中沿C-C线的剖视图。Fig. 4 is a sectional view along line C-C in Fig. 1 .

1潜污泵,2污水管,3进水方向,4排气孔,5排气管,6进气管,7曝气机,8出水方向,9多功能折流处理模块出水口,10污泥排放总管,11污泥排放支管,12排泥闸阀,131号池,142号池,153号池,164号池,175号池,186号池,19输水管,20布水管,21多介质生态滤池处理装置出水口,22进水闸阀,23逆止阀,24折流管,25排泥孔,26三相分布器,27钢丝网,28布气管,29聚氨酯填料,30布气孔,31钢丝网支架,32圆锥型铁皮,33散水管托架,34散水管,35集水槽,36透水滤层,37多介质滤层,39曝气材料。1 Submersible sewage pump, 2 Sewage pipe, 3 Water inlet direction, 4 Exhaust hole, 5 Exhaust pipe, 6 Inlet pipe, 7 Aerator, 8 Water outlet direction, 9 Water outlet of multi-functional baffle treatment module, 10 Sludge Discharge main pipe, 11 sludge discharge branch pipe, 12 sludge discharge gate valve, No. 131 pool, No. 142 pool, No. 153 pool, No. 164 pool, No. 175 pool, No. 186 pool, 19 water delivery pipe, 20 water distribution pipe, 21 multi-media ecology Water outlet of filter treatment device, 22 water inlet gate valve, 23 check valve, 24 diversion pipe, 25 mud discharge hole, 26 three-phase distributor, 27 steel wire mesh, 28 air distribution pipe, 29 polyurethane packing, 30 air distribution hole, 31 Steel mesh bracket, 32 conical iron sheet, 33 water distribution pipe bracket, 34 water distribution pipe, 35 water collection tank, 36 permeable filter layer, 37 multi-media filter layer, 39 aeration material.

具体实施方式 Detailed ways

下面结合附图和具体实施例对本发明作进一步说明,但不作为对本发明的限定。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments, but not as a limitation of the present invention.

如图1-4所示,本发明所述乡村污水处理专用装置,作为最佳实施例,其包括多功能折流处理模块和多介质生态渗滤单元。其设计标准负荷:24m3/d;设计最大负荷:48m3/d;出水水质:COD(Chemical Oxygen Demand化学需氧量)≤100mg/L,TSS(悬浮物)≤30mg/L,BOD(Biochemical Oxygen Demand生化需氧量)≤30mg/L,NH3-N(氨氮)≤25(30)mg/L,总磷≤3mg/L,即满足《城镇污水处理厂污染物排放标准》(GB18918-2002)二级标准。As shown in Figures 1-4, the special device for rural sewage treatment according to the present invention, as the best embodiment, includes a multi-functional baffle treatment module and a multi-media ecological percolation unit. Its design standard load: 24m 3 /d; design maximum load: 48m 3 /d; effluent water quality: COD (Chemical Oxygen Demand) ≤ 100mg/L, TSS (suspended solids) ≤ 30mg/L, BOD (Biochemical Oxygen Demand (biochemical oxygen demand) ≤ 30mg/L, NH 3 -N (ammonia nitrogen) ≤ 25(30) mg/L, total phosphorus ≤ 3mg/L, that is, meet the "Urban Sewage Treatment Plant Pollutant Discharge Standard" (GB18918- 2002) secondary standard.

本例中,多功能折流处理模块主体部分为柱形,由6个等大小的池子组成,按照污水流动方向由进水方向3到出水方向8顺次包括1号池13、2号池14、3号池15三个厌氧单元,4号池16、5号池17二个好氧单元和6号池18一个沉淀池单元组成。其整个外轮廓尺寸为长×宽×高:7.15m×2.4m×2.4m。相邻的单元是通过管道分段连接。本例中为了延长污水的处理时间,所述管道采用折流管24。In this example, the main part of the multi-functional baffle treatment module is cylindrical and consists of 6 pools of equal size, including No. 1 pool 13 and No. 2 pool 14 according to the sewage flow direction from the water inlet direction 3 to the water outlet direction 8 1, No. 3 pool 15 three anaerobic units, No. 4 pool 16, No. 5 pool 17 two aerobic units and No. 6 pool 18 a settling tank unit. Its overall outline size is length x width x height: 7.15m x 2.4m x 2.4m. Adjacent units are connected by pipe segments. In this example, in order to prolong the treatment time of sewage, the pipeline adopts a baffle tube 24 .

其中,多功能折流处理模块的工作过程大体分为以下三个阶段。Wherein, the working process of the multifunctional baffle processing module is roughly divided into the following three stages.

第一阶段,厌氧处理:The first stage, anaerobic treatment:

如图1-2所示,潜污泵1通过逆止阀23、进水闸阀22经污水管2连接1号池13,经1号池13的化粪并调节水质后,通过折流管24折流进入2号池14,2号池14为厌氧氧化池,经过2号池14后通过折流管24折流进入3号池15,3号池15为厌氧氧化池。3号池15中三相分布器26具有将水、污泥、气分离的功能,从而减少污泥流失。在3号池15的作用下,水经过折流管24进入4号池16,污泥沉淀至池底,气体通过排气管5经排气孔4排出。上述的厌氧单元使产酸菌和产甲烷菌能够分别生长在各自的适宜环境中,有利于污染物的降解。As shown in Figure 1-2, the submersible sewage pump 1 is connected to No. 1 pool 13 through the check valve 23 and the water inlet valve 22 through the sewage pipe 2. The diversion enters the No. 2 pool 14, and the No. 2 pool 14 is an anaerobic oxidation pool. After passing through the No. 2 pool 14, the diversion enters the No. 3 pool 15 through the baffle tube 24, and the No. 3 pool 15 is an anaerobic oxidation pool. The three-phase distributor 26 in the No. 3 pool 15 has the function of separating water, sludge and gas, thereby reducing sludge loss. Under the action of the No. 3 pool 15, the water enters the No. 4 pool 16 through the baffle pipe 24, the sludge settles to the bottom of the pool, and the gas is discharged through the exhaust pipe 5 through the exhaust hole 4. The above-mentioned anaerobic unit enables acid-producing bacteria and methanogenic bacteria to grow in their respective suitable environments, which is beneficial to the degradation of pollutants.

厌氧单元内放置带有厌氧菌的颗粒污泥,对污水中的有机物进行厌氧氧化。厌氧生物处理法是利用兼性厌氧菌和专性厌氧菌将污水中大分子有机物降解为低分子化合物,进而转化为甲烷、二氧化碳的有机污水处理方法,分为酸性消化和碱性消化两个阶段。在酸性消化阶段。由产酸菌分泌的外酶作用,使大分子有机物变成简单的有机酸和醇类、醛类氨、二氧化碳等;在碱性消化阶段,酸性消化的代谢产物在甲烷细菌作用下进一步分解成甲烷、二氧化碳等构成的生物气体。这种处理方法主要用于对高浓度的有机废水和粪便污水等处理。Granular sludge with anaerobic bacteria is placed in the anaerobic unit to anaerobically oxidize the organic matter in the sewage. Anaerobic biological treatment is an organic sewage treatment method that uses facultative anaerobic bacteria and obligate anaerobic bacteria to degrade macromolecular organic matter in sewage into low molecular compounds, and then converts them into methane and carbon dioxide. It is divided into acid digestion and alkaline digestion. two stages. during acidic digestion. The exoenzymes secreted by acid-producing bacteria turn macromolecular organic matter into simple organic acids and alcohols, aldehydes ammonia, carbon dioxide, etc.; in the alkaline digestion stage, the metabolites of acidic digestion are further decomposed into Biogases composed of methane and carbon dioxide. This treatment method is mainly used for the treatment of high-concentration organic wastewater and fecal sewage.

第二阶段,好氧处理:The second stage, aerobic treatment:

如图1-2所示,污水经过3号池15后通过折流管24折流顺次进入4号池16及5号池17,这两个有氧氧化池。好氧单元有利于脱碳菌和脱氮菌分别生长在各自适宜的环境中,有利于有机物和氨氮的去除。好氧单元设计为生物浮动床,参见图2,具体是在4号池16和5号池17内分别设置悬空的上、下钢丝网27,并在上、下钢丝网27形成的隔室内填充用于好氧反应的填料。钢丝网27由钢丝网支架31支撑。为了防止生物反应器堵塞并进一步提高活性污泥脱氮效率,所述填料为大孔状的聚氨酯填料29,这样既解决了固定床生物反应器的堵塞问题,又解决了活性污泥脱氮效率差、容积负荷低和产泥量大等问题。4号池16和5号池17下层的钢丝网27上设有布气孔30,布气孔30通过布气管28及进气管6与曝气机7相连。本例中采用鼓风曝气机给气。好氧单元(4号池16和5号)采用有利于反硝化脱氮的间歇曝气方式,曝气量仅为普通活性污泥和固定床反应器的1/3~1/5。其中微生物所需氧由鼓风曝气供给,填料表面附着的生物膜生长至一定厚度后,填料壁的微生物会因缺氧而进行厌氧代谢,产生的气体及曝气形成的冲刷作用会造成生物膜的脱落,并促进新生物膜的生长,此时,脱落的生物膜将随出水流出池外。As shown in Figure 1-2, the sewage passes through the No. 3 pool 15 and then enters No. 4 pool 16 and No. 5 pool 17 through the baffle pipe 24, these two aerobic oxidation pools. The aerobic unit is conducive to the growth of decarburizing bacteria and denitrifying bacteria in their respective suitable environments, and is conducive to the removal of organic matter and ammonia nitrogen. The aerobic unit is designed as a biological floating bed, as shown in Figure 2. Specifically, the upper and lower wire meshes 27 suspended in the air are respectively set in the No. 4 pool 16 and the No. 5 pool 17, and the compartments formed by the upper and lower wire meshes 27 are filled. Fillers for aerobic reactions. The wire mesh 27 is supported by a wire mesh support 31 . In order to prevent the blockage of the bioreactor and further improve the denitrification efficiency of the activated sludge, the filler is a macroporous polyurethane filler 29, which not only solves the problem of the blockage of the fixed bed bioreactor, but also improves the denitrification efficiency of the activated sludge. Poor, low volume load and large mud production. No. 4 pool 16 and No. 5 pool 17 lower steel wire mesh 27 are provided with air distribution hole 30, and air distribution hole 30 is connected with aerator 7 through air distribution pipe 28 and air intake pipe 6. In this example, a blower aerator is used for air supply. The aerobic unit (No. 4 pool No. 16 and No. 5) adopts the intermittent aeration method that is beneficial to denitrification and denitrification, and the aeration rate is only 1/3 to 1/5 of that of ordinary activated sludge and fixed-bed reactors. Among them, the oxygen required by microorganisms is supplied by blast aeration. After the biofilm attached to the surface of the filler grows to a certain thickness, the microorganisms on the filler wall will perform anaerobic metabolism due to lack of oxygen, and the gas produced and the scouring effect formed by aeration will cause The biofilm falls off and promotes the growth of new biofilm. At this time, the shed biofilm will flow out of the pool with the effluent.

好氧单元具有以下特点:1)由于填料比表面积大,池内充氧条件良好,池内单位容积的生物固体量较高,因此,生物接触氧化池具有较高的容积负荷;2)由于池内生物固体量多,水流完全混合,故对水质水量的骤变有较强的适应能力;3)剩余污泥量少,不存在污泥膨胀问题,运行管理简便。The aerobic unit has the following characteristics: 1) Due to the large specific surface area of the filler, the oxygenation conditions in the pool are good, and the amount of biosolids per unit volume in the pool is relatively high, so the biological contact oxidation tank has a high volume load; 2) Due to the biosolids in the pool 3) The amount of residual sludge is small, there is no problem of sludge bulking, and the operation and management are simple.

第三阶段,沉淀池处理:The third stage, sedimentation tank treatment:

为了有利于水的复氧和悬浮物沉淀,以减少悬浮物对后续处理单元的冲击,伸入所述6号池18内的折流管24为散水管34,散水管34的端口呈喇叭状。散水管34是由圆锥型铁皮32制成,通过散水管托架33安装在6号池18内。从5号池17有氧氧化池排出的水,通过沉淀分配给6号池18中的喇叭型散水管34,分散水流的水力冲击,进一步沉淀污水中的污泥。从6号池18的多功能折流处理模块出水口9中排出的出水水质:COD≤150mg/L,悬浮物≤80mg/L,BOD≤60mg/L,满足《农田灌溉水质量标准》(GB5084-2005)要求。In order to facilitate the reoxygenation of water and the precipitation of suspended solids, to reduce the impact of suspended solids on the subsequent processing unit, the baffle tube 24 extending into the No. 6 pool 18 is a diffuser tube 34, and the port of the diffuser tube 34 is trumpet-shaped. . The water spreading pipe 34 is made of a conical iron sheet 32, and is installed in No. 6 pool 18 by a water spreading pipe bracket 33. The water discharged from the aerobic oxidation tank of the No. 5 pool 17 is distributed to the trumpet-shaped water distribution pipe 34 in the No. 6 pool 18 through sedimentation to disperse the hydraulic impact of the water flow and further precipitate the sludge in the sewage. The quality of the effluent water discharged from the outlet 9 of the multifunctional baffle treatment module of No. 6 pool 18: COD≤150mg/L, suspended solids≤80mg/L, BOD≤60mg/L, meeting the "Farmland Irrigation Water Quality Standard" (GB5084 -2005) requirements.

如图1-2所示,为了方便污泥的排出,每个处理单元靠近底部处设有排泥孔25,排泥孔25通过排泥闸阀12连接污泥排放支管11最终由污泥排放总管10排出。As shown in Figure 1-2, in order to facilitate the discharge of sludge, each treatment unit is provided with a sludge discharge hole 25 near the bottom, and the sludge discharge hole 25 is connected to the sludge discharge branch pipe 11 through the sludge discharge gate valve 12, and finally the sludge discharge main pipe 10 discharge.

多介质生态渗滤模块的渗滤阶段:The percolation stage of the multi-media ecological percolation module:

如图3-4所示,多介质生态渗滤模块外轮廓尺寸长×宽×高为1.8m×2.4m×2.1m,模块的上部为曝气材料39,具体为大孔网状载体,高度为0.6m;模块下部的填料由8层组成,高度为1.2m。每一层填料高度为0.15m,其中底部为透水滤层36,高度为0.05m;顶部为多介质滤料层37,高度为0.1m。每一层中顶部的多介质滤料层37为多介质滤料和透水滤料交替填充,其中,多介质滤料的填充宽度为0.3m,透水滤料的填充宽度为0.1m。上述填充方法即为“品”字形填充方法,如图3所示。本例中,多介质滤料层37的填充物为多介质滤料,以人工合成的功能陶粒为主,辅以粒径大于2mm的改性沸石,功能陶粒与粒径大于2mm的改性沸石的填充比例体积比为1∶1。透水滤层36的填充物为透水滤料,由平均粒径为10mm的砾石和粒径大于2mm的改性沸石组成,平均粒径为10mm砾石与粒径大于2mm的改性沸石的填充比例为体积比4∶1。As shown in Figure 3-4, the dimensions of the outer contour of the multi-media ecological infiltration module are 1.8m×2.4m×2.1m in length×width×height. is 0.6m; the filler at the lower part of the module is composed of 8 layers, and the height is 1.2m. The height of each layer of packing is 0.15m, wherein the bottom is a permeable filter layer 36 with a height of 0.05m; the top is a multi-media filter material layer 37 with a height of 0.1m. The multi-media filter material layer 37 on the top of each layer is alternately filled with multimedia filter material and water-permeable filter material, wherein the filling width of the multimedia filter material is 0.3m, and the filling width of the water-permeable filter material is 0.1m. The above filling method is the filling method of the character "pin", as shown in Figure 3. In this example, the filler of the multi-media filter material layer 37 is a multi-media filter material, which is mainly artificially synthesized functional ceramsite, supplemented by modified zeolite with a particle size greater than 2mm. The filling proportion volume ratio of the active zeolite is 1:1. The filler of the water-permeable filter layer 36 is a water-permeable filter material, which is composed of gravel with an average particle size of 10 mm and modified zeolite with a particle size greater than 2 mm. The volume ratio is 4:1.

多介质生态渗滤单元外轮廓主体部分为柱形,滤池内的填料按“品”字形填充多层直至滤池上表面。多介质滤料层以人工合成的功能陶粒为主,辅以改性沸石;透水滤层36由砾石和改性沸石组成。滤料顶层表面有六根布水管20组成的布水系统,并将布水管20置于曝气材料39内部以充分曝气和防止布水管20上的出水孔堵塞。布水管20与输水管19相连,污水经输水管19进入多介质滤层37,通过滤池填料表面的布水管20被均匀的分布在填料顶层,污水逐级通过由多介质滤料层37和透水滤层36组成的“品”字形滤料层,部分会渗入净水介质,无法渗入净水介质的水流和透过净水介质的水流,再通过水流通道导入下一层净水介质,直至达到最后一级净水介质。滤料层的底部是钢丝网构成的支撑结构,污水经过滤层后进入集水槽35,再通过多介质生态滤池处理装置出水口21排入池外。The main part of the outer contour of the multi-media ecological infiltration unit is cylindrical, and the filler in the filter tank is filled with multiple layers in the shape of "product" until the upper surface of the filter tank. The multi-media filter material layer is mainly composed of artificially synthesized functional ceramsite, supplemented by modified zeolite; the water-permeable filter layer 36 is composed of gravel and modified zeolite. There is a water distribution system composed of six water distribution pipes 20 on the surface of the filter material top layer, and the water distribution pipes 20 are placed inside the aeration material 39 to fully aerate and prevent the outlet holes on the water distribution pipes 20 from clogging. The water distribution pipe 20 is connected with the water delivery pipe 19, and the sewage enters the multi-media filter layer 37 through the water delivery pipe 19, and the water distribution pipe 20 passing through the surface of the filter tank packing is evenly distributed on the top layer of the packing, and the sewage passes through the multi-media filter material layer 37 and The "product"-shaped filter material layer formed by the water-permeable filter layer 36 will partially penetrate into the water purification medium, and the water flow that cannot penetrate into the water purification medium and the water flow through the water purification medium will be introduced into the next layer of water purification medium through the water flow channel until Reach the last level of water purification medium. The bottom of the filter material layer is a supporting structure made of steel wire mesh. The sewage enters the sump 35 after passing through the filter layer, and then is discharged out of the pool through the water outlet 21 of the multi-media ecological filter treatment device.

滤料层的主要材料:灰渣、砾石、沸石、多介质滤料、大孔网状载体。The main materials of the filter layer: ash, gravel, zeolite, multi-media filter material, macroporous mesh carrier.

(1)灰渣:煤灰渣,原料易得,经济,具有多孔结构,对氮磷具有一定吸附能力,同时其微孔能够形成毛细水,使水能够提升到一定高度;(1) Ash slag: Coal ash slag, the raw material is easy to get, economical, has a porous structure, has a certain adsorption capacity for nitrogen and phosphorus, and its micropores can form capillary water, so that the water can be raised to a certain height;

(2)砾石,普通砾石,原料易得,经济,主要是为微生物提供挂膜的介质,固定微生物的作用;(2) Gravel, ordinary gravel, the raw material is easy to get, economical, mainly to provide the medium for the microbes to hang the film, and to fix the microbes;

(3)沸石,沸石有很多种,原料易得,我们用的是斜发沸石,沸石对磷和氨氮都有一定吸附能力,可以起到深度除磷脱氮的作用;(3) Zeolite, there are many kinds of zeolites, and the raw materials are easy to get. We use clinoptilolite, which has a certain adsorption capacity for phosphorus and ammonia nitrogen, and can play a role in deep phosphorus and nitrogen removal;

(4)多介质滤料,为人工合成的功能陶粒,功能高效,具有吸附氮磷、固定微生物和电解有机物的作用;(4) The multi-media filter material is artificially synthesized functional ceramsite, which has high efficiency and has the functions of adsorbing nitrogen and phosphorus, immobilizing microorganisms and electrolyzing organic matter;

(5)大孔网状载体,为聚氨酯微生物固定化材料,孔隙率大,生物负荷高,其作用为固定化高效降解有机物和脱氮的微生物。(5) The macroporous network carrier is a polyurethane microorganism immobilization material with large porosity and high bioburden, and its function is to immobilize microorganisms that efficiently degrade organic matter and denitrify.

本发明所述的乡村污水处理方法,具体包括如下步骤:Village sewage treatment method of the present invention specifically comprises the following steps:

步骤A通过潜污泵1将污水输送至1号池13,并经由1号池13厌氧氧化池进行化粪和调节水质处理;In step A, the sewage is transported to the No. 1 pool 13 through the submersible sewage pump 1, and the septic and water quality treatment is performed through the anaerobic oxidation pool of the No. 1 pool 13;

步骤B经1号池13处理过的污水通过折流管24进入2号池14厌氧氧化池进行厌氧处理,其中折流管24的作用是延长污水的路径,增加污水的停留时间;In step B, the sewage treated in No. 1 pool 13 enters the anaerobic oxidation tank of No. 2 pool 14 through the baffle tube 24 for anaerobic treatment, wherein the role of the baffle tube 24 is to extend the path of the sewage and increase the residence time of the sewage;

步骤C经2号池14处理过的污水通过折流管24折流进入3号池15厌氧氧化池,在3号池15中三相分布器26的作用下将水、污泥、气分离,水经过折流管24进入4号池16,污泥沉淀至池底,气体通过排气口排出;In step C, the sewage treated in the No. 2 pool 14 is deflected through the baffle pipe 24 and enters the anaerobic oxidation pool of the No. 3 pool 15, and the water, sludge and gas are separated under the action of the three-phase distributor 26 in the No. 3 pool 15 , the water enters the No. 4 pool 16 through the baffle pipe 24, the sludge settles to the bottom of the pool, and the gas is discharged through the exhaust port;

步骤D经3号池15处理过的污水通过折流管24折流进入4号池16有氧氧化池,对4号池16进行曝气作有氧氧化处理;In step D, the sewage treated in the No. 3 pool 15 is deflected through the baffle pipe 24 and enters the No. 4 pool 16 aerobic oxidation pool, and the No. 4 pool 16 is aerated for aerobic oxidation treatment;

步骤E污水通过折流管24折流进入5号池17有氧氧化池,重复上述步骤D;In step E, the sewage enters the aerobic oxidation pool No. 5 pool 17 through the deflection pipe 24, and repeats the above step D;

步骤F经5号池17处理过的污水后进入6号池18沉淀,进一步沉淀污水的悬浮物,最终排出满足标准要求的处理水。In step F, the sewage treated in the No. 5 pool 17 enters the No. 6 pool 18 for sedimentation, further sediments the suspended solids of the sewage, and finally discharges the treated water meeting the standard requirements.

上述方法是集化粪池、厌氧处理、好氧处理、生物浮动床、沉淀等功能于一体,使污水中的有机物在厌氧和好氧微生物的作用下转化成无害的物质。The above method integrates the functions of septic tank, anaerobic treatment, aerobic treatment, biological floating bed, sedimentation, etc., so that the organic matter in the sewage is converted into harmless substances under the action of anaerobic and aerobic microorganisms.

所述乡村污水处理方法,还包括通过多介质生态渗滤模块的运行过程,具体的是污水经过滤池填料表面的布水管20逐级通过由多介质滤料层和透水滤层36组成的“品”字形滤料层,进入滤池底部的集水槽35后排出。污水经多功能折流处理模块流经多介质生态滤池时,污染物被多介质滤料拦截和吸附在其表面,微生物利用有机物进行生长繁殖,并附着在滤料上形成生物膜。经过一段时间,生物膜成熟,栖息在生物膜上的微生物以流经表明的有机物作为营养,对污水中的有机物进行吸附、分解氧化,从而使流过生态滤池的污水得到净化。The rural sewage treatment method also includes the operation process of the multi-media ecological infiltration module. Specifically, the sewage passes through the water distribution pipe 20 on the surface of the filler in the filter tank step by step through the "multi-media filter material layer and the permeable filter layer 36. Product " font filter material layer, discharge after entering the sump 35 at the bottom of the filter tank. When the sewage flows through the multi-media ecological filter through the multi-functional baffle treatment module, the pollutants are intercepted and adsorbed on the surface of the multi-media filter material, and the microorganisms use the organic matter to grow and reproduce, and attach to the filter material to form a biofilm. After a period of time, the biofilm matures, and the microorganisms inhabiting the biofilm use the organic matter flowing through the surface as nutrients to adsorb, decompose and oxidize the organic matter in the sewage, thereby purifying the sewage flowing through the ecological filter.

所述乡村污水处理方法,其中,所述步骤D及E中的曝气采用间歇曝气方式。采用有利于反硝化脱氮的间歇曝气方式,曝气量仅为普通活性污泥和固定床反应器的1/3~1/5。The rural sewage treatment method, wherein the aeration in the steps D and E adopts intermittent aeration. The intermittent aeration method that is beneficial to denitrification and denitrification is adopted, and the aeration rate is only 1/3 to 1/5 of that of ordinary activated sludge and fixed bed reactors.

因此,本发明所述一种乡村污水处理方法及其专用装置,是综合运用沉淀、过滤等物理处理技术和厌氧氧化、好氧氧化等生化处理技术,使污水中的有机物得以降解,无机盐得以固定,氮磷等营养物得以降低,具有水力负荷大并且处理后水质好的优点,特别适合我国的国情需要。Therefore, a kind of rural sewage treatment method and its special device described in the present invention are comprehensively using physical treatment technologies such as sedimentation and filtration and biochemical treatment technologies such as anaerobic oxidation and aerobic oxidation to degrade organic matter in sewage, and inorganic salts It can be fixed, nutrients such as nitrogen and phosphorus can be reduced, and has the advantages of large hydraulic load and good water quality after treatment, which is especially suitable for my country's national conditions.

以上所述的实施例,只是本发明较优选的具体实施方式的一种,本领域的技术人员在本发明技术方案范围内进行的通常变化和替换都应包含在本发明的保护范围内。The embodiments described above are only one of the more preferred specific implementations of the present invention, and the usual changes and replacements performed by those skilled in the art within the scope of the technical solutions of the present invention should be included in the protection scope of the present invention.

Claims (10)

1.一种乡村污水处理专用装置,包括潜污泵和与其相连的多功能折流处理模块,其特征在于:所述多功能折流处理模块按照污水流动方向顺次包括六个池,分别为三个厌氧单元、两个好氧单元和一个沉淀单元,相邻的处理单元通过管道分段连接;其中1号池、2号池及3号池为厌氧单元并且每个单元均设有排气孔,潜污泵连接1号池,3号池内设有三相分布器;4号池和5号池为好氧单元并且池内均设有悬空的上、下钢丝网,上、下钢丝网形成隔室、隔室内填充用于好氧反应的填料,下层的钢丝网上设有布气孔,布气孔通过布气管与曝气机相连;6号池为沉淀单元。1. A special device for rural sewage treatment, comprising a submersible sewage pump and a multifunctional baffle treatment module connected to it, characterized in that: the multifunctional baffle treatment module includes six pools in sequence according to the sewage flow direction, respectively Three anaerobic units, two aerobic units and one sedimentation unit, adjacent processing units are connected by pipeline segments; among them, No. 1 pool, No. 2 pool and No. 3 pool are anaerobic units and each unit has The vent hole and the submersible sewage pump are connected to No. 1 pool, and there is a three-phase distributor in No. 3 pool; No. 4 and No. 5 pools are aerobic units, and the pools are equipped with suspended upper and lower steel wire meshes. A compartment is formed, and the compartment is filled with fillers for aerobic reaction. The steel wire mesh on the lower layer is provided with air distribution holes, and the air distribution holes are connected to the aerator through the air distribution pipe; the No. 6 pool is a sedimentation unit. 2.根据权利要求1所述的乡村污水处理专用装置,其特征在于:还包括通过管道与所述多功能折流处理模块出水口相连接的多介质生态渗滤模块,多介质生态渗滤模块为含有多介质滤料层的滤池。2. The special device for rural sewage treatment according to claim 1, characterized in that: it also includes a multi-media ecological infiltration module connected to the outlet of the multi-functional baffle treatment module through a pipeline, and the multi-media ecological infiltration module It is a filter tank containing a multi-media filter material layer. 3.根据权利要求2所述的乡村污水处理专用装置,其特征在于:所述多介质生态渗滤模块的上部为曝气材料,为大孔网状载体;下部的填料至少由4层组成;每一层填料的底部为透水滤层,顶部为多介质滤料层;多介质滤料层为多介质滤料和透水滤料交替填充,形成“品”字形填充;多介质滤料层以人工合成的功能陶粒为主、辅以改性沸石,透水滤层由砾石和改性沸石组成。3. The special device for rural sewage treatment according to claim 2, characterized in that: the upper part of the multi-media ecological infiltration module is an aeration material, which is a large-pore mesh carrier; the lower part of the filler is composed of at least 4 layers; The bottom of each layer of packing is a water-permeable filter layer, and the top is a multi-media filter material layer; the multi-media filter material layer is alternately filled with multi-media filter material and water-permeable filter material to form a "product"-shaped filling; the multi-media filter material layer is filled with artificial The synthesized functional ceramsite is mainly supplemented with modified zeolite, and the permeable filter layer is composed of gravel and modified zeolite. 4.根据权利要求1所述的乡村污水处理专用装置,其特征在于:所述单元之间连接的管道为折流管。4. The special device for rural sewage treatment according to claim 1, characterized in that: the pipes connected between the units are baffle pipes. 5.根据权利要求1所述的乡村污水处理专用装置,其特征在于:所述单元靠近底部处设有排泥孔。5. The special device for rural sewage treatment according to claim 1, characterized in that: the unit is provided with a mud discharge hole near the bottom. 6.根据权利要求1所述的乡村污水处理专用装置,其特征在于:所述填料为大孔状的聚氨酯填料。6. The special device for rural sewage treatment according to claim 1, characterized in that: the filler is macroporous polyurethane filler. 7.根据权利要求1-6任一权利要求所述的乡村污水处理专用装置,其特征在于:伸入所述6号池内的折流管为散水管,散水管的端口为喇叭状。7. The special device for rural sewage treatment according to any one of claims 1-6, characterized in that: the baffle pipe extending into the No. 6 pool is a diffuser pipe, and the port of the diffuser pipe is trumpet-shaped. 8.根据权利要求1所述的乡村污水处理专用装置的乡村污水处理方法,包括如下步骤:8. The rural sewage treatment method of the rural sewage treatment special device according to claim 1, comprising the steps of: 步骤A将污水输送至1号池,并经由1号池厌氧氧化池进行化粪和调节水质处理;In step A, the sewage is transported to the No. 1 pool, and the septic treatment and water quality adjustment are carried out through the anaerobic oxidation pool of the No. 1 pool; 步骤B经1号池处理过的污水通过管道进入2号池厌氧氧化池进行厌氧处理;In step B, the sewage treated in the No. 1 pool enters the No. 2 pool anaerobic oxidation pool through the pipeline for anaerobic treatment; 步骤C经2号池处理过的污水通过管道进入3号池厌氧氧化池,在3号池中三相分布器的作用下将水、污泥、气分离,水经过管道进入4号池,污泥沉淀至池底,气体通过排气口排出;In step C, the sewage treated in the No. 2 pool enters the anaerobic oxidation pool of the No. 3 pool through the pipeline, and the water, sludge and gas are separated under the action of the three-phase distributor in the No. 3 pool, and the water enters the No. 4 pool through the pipeline. The sludge settles to the bottom of the tank, and the gas is discharged through the exhaust port; 步骤D经3号池处理过的污水通过管道进入4号池有氧氧化池,对4号池进行曝气作有氧氧化处理;In step D, the sewage treated in the No. 3 pool enters the No. 4 pool aerobic oxidation pool through the pipeline, and the No. 4 pool is aerated for aerobic oxidation treatment; 步骤E污水通过管道进入5号池有氧氧化池,重复上述步骤D;In step E, the sewage enters the aerobic oxidation pool of No. 5 pool through the pipeline, and repeats the above step D; 步骤F经5号池处理过的污水后进入6号池沉淀,进一步沉淀污水的悬浮物,最终排出满足标准要求的处理水。In step F, the sewage treated in the No. 5 pool enters the No. 6 pool for sedimentation, further sediments the suspended solids of the sewage, and finally discharges the treated water that meets the standard requirements. 9.根据权利要求8所述乡村污水处理方法,其特征在于:还包括通过多介质生态渗滤模块的运行过程,具体的是污水经过滤池填料表面的布水管逐级通过由多介质滤料层和透水滤层组成的“品”字形滤料层,进入滤池底部的集水槽后排出。9. The rural sewage treatment method according to claim 8, characterized in that: it also includes the operation process of the multi-media ecological infiltration module, specifically, the sewage passes through the water distribution pipes on the surface of the filler in the filter tank step by step through the multi-media filter material The "product"-shaped filter material layer composed of the filter layer and the permeable filter layer enters the sump at the bottom of the filter and is discharged. 10.根据权利要求8或9所述乡村污水处理方法,其特征在于:所述步骤D及E中的曝气采用间歇曝气方式。10. The rural sewage treatment method according to claim 8 or 9, characterized in that: the aeration in the steps D and E adopts an intermittent aeration method.
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CN112723556A (en) * 2020-12-02 2021-04-30 湖北汇农生物科技有限公司 Method for building microorganism sewage treatment device
CN115286109A (en) * 2022-09-30 2022-11-04 四川省生态环境科学研究院 High and cold rural sewage treatment device and treatment method
EP3919447B1 (en) * 2020-06-03 2025-03-19 Beijing KeRuiAo Biological Technology Co., Ltd. Automatic sewage treatment system

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CN102120669A (en) * 2009-12-22 2011-07-13 隆润新技术发展有限公司 Application of high solution bacteria efficient microbiological technology and anaerobic baffled reactor-oxic baffled reactor technology in coking wastewater treatment
CN102120670A (en) * 2009-12-22 2011-07-13 隆润新技术发展有限公司 H.S.B (High Solution Bacteria) high-efficiency microorganism technology and application of ABR+OBR (Anaerobic Baffled Reactor+Oxic Baffled Reactor) process in excrement treatment
CN102358659A (en) * 2011-07-28 2012-02-22 农业部规划设计研究院 Rural domestic sewage composite filter tank treatment system and technology therefor
CN103588355A (en) * 2013-10-15 2014-02-19 常州思宇环保材料科技有限公司 Device for removing high-concentration ammonia nitrogen in waste water
CN104147820A (en) * 2014-01-10 2014-11-19 广东金明环保科技有限公司 Filtering device on water treatment integrated equipment
CN104150579A (en) * 2014-01-10 2014-11-19 广东金明环保科技有限公司 Biological treatment device used on water treatment integrated equipment
CN105502656A (en) * 2015-11-30 2016-04-20 北京大学 Two-section type reinforced denitrification multistage soil percolation system
CN105502656B (en) * 2015-11-30 2019-04-02 北京大学 A two-stage enhanced denitrification multistage soil infiltration system
CN106145317A (en) * 2016-08-24 2016-11-23 中国科学院、水利部成都山地灾害与环境研究所 A kind of Multifunction oxidation pond for rural domestic sewage treatment
CN111099730A (en) * 2020-02-10 2020-05-05 东莞市诚盈环保科技有限公司 Unpowered and micro-power rural sewage integrated treatment equipment
EP3919447B1 (en) * 2020-06-03 2025-03-19 Beijing KeRuiAo Biological Technology Co., Ltd. Automatic sewage treatment system
CN112723556A (en) * 2020-12-02 2021-04-30 湖北汇农生物科技有限公司 Method for building microorganism sewage treatment device
CN115286109A (en) * 2022-09-30 2022-11-04 四川省生态环境科学研究院 High and cold rural sewage treatment device and treatment method

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