CN202099163U - Combined layering biological filter for sewage treatment - Google Patents

Combined layering biological filter for sewage treatment Download PDF

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CN202099163U
CN202099163U CN2011201716400U CN201120171640U CN202099163U CN 202099163 U CN202099163 U CN 202099163U CN 2011201716400 U CN2011201716400 U CN 2011201716400U CN 201120171640 U CN201120171640 U CN 201120171640U CN 202099163 U CN202099163 U CN 202099163U
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biofilter
sewage treatment
sump
water
layered
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邱江平
李旭东
纪婧
邱卫国
欧文幍
戴一琦
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Shanghai Aung Environmental Protection Development Co Ltd
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Shanghai Jiao Tong University
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Abstract

一种污水处理技术领域的用于污水处理的组合式分层生物滤池,包括:集水池、组合式分层生物滤池、中间池和水平潜流式湿地,其中:集水池、生物滤池、中间池和水平潜流式湿地依次串联连接。本装置利用分层生物滤池对污水中的有机物、悬浮物和氨氮等进行预处理,利用人工湿地对污水中的氮、磷和剩余有机物进一步进行处理、通过物理、化学、生物综合作用达到净化水质的目的。传统的生物滤池工艺单独使用时处理出水能达到二级标准,本装置提供的联合工艺应用实例出水水质各项指标经检测均优于《城镇污水处理厂污染物排放标准》(GB18918-2002)一级B标准,吨水占地面积约3.5m2

A combined layered biofilter for sewage treatment in the technical field of sewage treatment, including: a sump, a combined layered biofilter, an intermediate pool and a horizontal subsurface wetland, wherein: the sump, the biofilter, The intermediate pool and the horizontal subsurface wetland are connected in series in sequence. This device uses layered biofilter to pretreat the organic matter, suspended matter and ammonia nitrogen in the sewage, and uses the artificial wetland to further treat the nitrogen, phosphorus and remaining organic matter in the sewage, and achieve purification through comprehensive physical, chemical and biological effects. water quality purposes. When the traditional biological filter process is used alone, the treated effluent can reach the second-class standard. The combined process application example provided by this device has all the indicators of effluent water quality tested. Class I B standard, the area occupied by a ton of water is about 3.5m 2 .

Description

用于污水处理的组合式分层生物滤池Combined layered biological filter for sewage treatment

技术领域 technical field

本实用新型涉及的是一种污水处理技术领域的装置,具体是一种用于村镇生活污水处理的用于污水处理的组合式分层生物滤池。The utility model relates to a device in the technical field of sewage treatment, in particular to a combined layered biofilter used for sewage treatment in villages and towns.

背景技术 Background technique

村镇生活污水是广大农村地区面源污染的重要来源之一,我国95%以上村庄和90%以上的小集镇都没有完善的污水收集和处理设施,产生的生活污水和部分工业废水,几乎是未经任何处理直接排入水体(河道、池塘、地下水等),造成村镇水体的严重污染,黑臭河道、池塘和富营养化的湖泊已成为普遍现象。Domestic sewage in villages and towns is one of the important sources of non-point source pollution in vast rural areas. More than 95% of villages and more than 90% of small market towns in my country do not have perfect sewage collection and treatment facilities. After any treatment, it is directly discharged into water bodies (rivers, ponds, groundwater, etc.), causing serious pollution of water bodies in villages and towns. Black and smelly rivers, ponds and eutrophic lakes have become a common phenomenon.

村镇生活污水处理有如下几个特点:1)面广、分散,水质、水量波动性大,排水管网很不健全;2)村镇经济力量薄弱,污水处理技术或工艺需投资省、能耗低、运行费用少;3)村镇缺乏污水处理专业人员,处理设施应运行管理简单,维护方便;4)缺乏有针对性的先进适用污水处理技术,在村镇污水处理方面不宜采用较为成熟的城市污水工艺,而一些所谓的生态型工艺往往不能满足处理要求,或缺乏实施的条件(如土地资源)。因此需采用一些工艺简洁、处理效果好,占地省、能耗低、运行管理简便、二次污染少的先进适用技术,并用分散处理模式。Domestic sewage treatment in villages and towns has the following characteristics: 1) Wide area, scattered, large fluctuations in water quality and water volume, and unsound drainage network; 2) The economic strength of villages and towns is weak, and sewage treatment technology or process requires low investment and low energy consumption , low operating costs; 3) There is a lack of sewage treatment professionals in villages and towns, and the treatment facilities should be simple to operate and manage, and easy to maintain; 4) There is a lack of targeted advanced and applicable sewage treatment technologies, and it is not appropriate to adopt more mature urban sewage processes in villages and towns sewage treatment , and some so-called ecological processes often cannot meet the treatment requirements, or lack the conditions for implementation (such as land resources). Therefore, it is necessary to adopt some advanced and applicable technologies with simple process, good treatment effect, low land occupation, low energy consumption, simple operation and management, and less secondary pollution, and use a decentralized treatment mode.

目前,针对村镇污水分散式处理,国内外主要采用三大类技术和工艺。一类是借鉴城市污水处理厂二级生化处理的成功经验,将一些传统的城市污水处理厂二级生化处理工艺小型化,应用于村镇分散式污水处理。如SBR、氧化沟、A/O,甚至A2/O,MBR等等。仅从技术的角度来讲,这些技术和工艺都比较成熟,可以满足污水处理的要求。但是,这些技术和工艺通常都比较复杂,需要的设备也比较多。因此,投资相对较大、系统维护管理较为复杂、能耗及运行管理费用高,并且还可能产生一些二次污染问题。这样的处理系统与我国村镇社会经济的实际情况很不适应。其结果是化花了大量投资,建成的污水处理厂(站),因为高昂的运行费用、缺乏正常的维护管理等原因而处于非正常运行或停止运行的状态。At present, for the decentralized treatment of village and town sewage, three major types of technologies and processes are mainly used at home and abroad. One is to learn from the successful experience of secondary biochemical treatment in urban sewage treatment plants, miniaturize some traditional secondary biochemical treatment processes in urban sewage treatment plants, and apply them to decentralized sewage treatment in villages and towns. Such as SBR, oxidation ditch, A/O, even A2/O, MBR and so on. From a technical point of view, these technologies and processes are relatively mature and can meet the requirements of sewage treatment. However, these technologies and processes are usually more complicated and require more equipment. Therefore, the investment is relatively large, the system maintenance and management are more complicated, the energy consumption and operation management costs are high, and some secondary pollution problems may also occur. Such a processing system is very incompatible with the actual social and economic conditions of our country's villages and towns. As a result, a large amount of investment has been spent, and the built sewage treatment plant (station) is in a state of abnormal operation or out of operation due to high operating costs, lack of normal maintenance and management, and other reasons.

第二类是采用一些相对简单的生态化污水处理技术,包括人工湿地、氧化塘、土地处理系统等。这类技术的优点是工艺简单、投资小、低能耗、维护简便、环境友好等,缺点是处理效率较低,通常要在一定的条件下才能取得稳定的处理效果和维持系统的长期正常运行,如较低的水力负荷和有机负荷及较长的HRT,这就要求有较大的可以利用的土地面积。The second category is to adopt some relatively simple ecological sewage treatment technologies, including artificial wetlands, oxidation ponds, and land treatment systems. The advantages of this type of technology are simple process, small investment, low energy consumption, easy maintenance, and environmental friendliness, etc. The disadvantage is that the treatment efficiency is low, and it usually takes certain conditions to achieve stable treatment effects and maintain the long-term normal operation of the system. Such as lower hydraulic load and organic load and longer HRT, which requires a larger land area that can be used.

第三类是厌氧处理技术,以厌氧反应器为主的厌氧处理系统是一种低成本的废水处理技术,同时又能回收利用能源。对于农村生活污水处理来说,可以把人、畜粪便,农作物秸秆、杂草、树叶和农产品加工企业的有机废水等加入到厌氧沼气池内与生活污水同时进行厌氧处理,产生的沼气可以用作浴室和家庭能源。污水厌氧产沼气技术已在我国一些地方得到了有效推广和使用。但是,单独的厌氧污水处理技术还不能使处理出水满足排放要求,必须进行后续处理。The third category is anaerobic treatment technology. The anaerobic treatment system based on anaerobic reactor is a low-cost wastewater treatment technology that can recycle energy at the same time. For rural domestic sewage treatment, human and animal manure, crop stalks, weeds, leaves and organic wastewater from agricultural product processing enterprises can be added to the anaerobic digester for anaerobic treatment at the same time as domestic sewage, and the generated biogas can be used For bathroom and home energy. Sewage anaerobic biogas production technology has been effectively promoted and used in some places in my country. However, the anaerobic sewage treatment technology alone cannot make the treated effluent meet the discharge requirements, and subsequent treatment must be carried out.

此外,发展集预处理、二级处理和深度处理于一体的中小型污水处理一体化装置,是国内外污水分散处理发展的一种趋势,在农村生活污水处理中具有广阔的应用前景。日本研究的一体化装置主要采用厌氧-好氧-二沉池组合工艺,兼具降解有机物和脱氮的功能,其出水BOD5<20mg/L、TN<20mg/L。近年来开发的膜处理技术,可对BOD5和TN进行深度处理。欧洲许多国家开发了以SBR、移动床生物膜反应器、生物转盘和滴滤池技术为主,结合化学除磷的小型污水处理集成装置。但这类一体化装置同样也存在能耗较高、运行管理较复杂等问题,同时其适用范围还有待于进一步拓展。In addition, the development of small and medium-sized sewage treatment integrated devices integrating pretreatment, secondary treatment and advanced treatment is a trend in the development of sewage decentralized treatment at home and abroad, and has broad application prospects in rural domestic sewage treatment. The integrated device studied in Japan mainly adopts the combined process of anaerobic-aerobic-secondary sedimentation tank, which has the functions of degrading organic matter and denitrification, and its effluent BOD5<20mg/L, TN<20mg/L. The membrane treatment technology developed in recent years can carry out advanced treatment of BOD5 and TN. Many countries in Europe have developed small sewage treatment integrated devices based on SBR, moving bed biofilm reactor, biological turntable and trickling filter technology combined with chemical phosphorus removal. However, this type of integrated device also has problems such as high energy consumption and complicated operation and management, and its scope of application needs to be further expanded.

现有技术中用于分散污水处理工艺均能达到城镇污水处理厂污染物排放标准(GB18918-2002)或国家农田灌溉水质标准(GB5084-2005)。但是这些技术或工艺存在以下局限性和不足:In the prior art, the decentralized sewage treatment process can meet the pollutant discharge standard of urban sewage treatment plants (GB18918-2002) or the national farmland irrigation water quality standard (GB5084-2005). However, these technologies or processes have the following limitations and deficiencies:

1.工艺复杂,处理单元过多,增加了建设、施工和管理难度,滤池与厌氧池间的多次回流致使基建和运行管理费用增加。1. The process is complicated and there are too many treatment units, which increases the difficulty of construction, construction and management. The multiple backflows between the filter tank and the anaerobic tank increase the cost of capital construction and operation management.

2.湿地类型多为表面流湿地,虽然易于建设,但卫生条件差,且水力停留时间过长,导致工程占地面积大,在使用推广上易受限制。2. Most of the wetlands are surface flow wetlands. Although they are easy to construct, they have poor sanitary conditions and too long hydraulic retention time, resulting in a large project area, which is easily restricted in use and promotion.

3.蚯蚓生物滤池内投加了大量蚯蚓,由于蚯蚓易受环境因素、污水水质等的影响,需定期对蚯蚓进行补充添加,难于养护。3. A large number of earthworms are added to the earthworm biofilter. Since earthworms are easily affected by environmental factors and sewage water quality, they need to be added regularly, which is difficult to maintain.

实用新型内容 Utility model content

本实用新型针对现有技术存在的上述不足,提供一种用于污水处理的组合式分层生物滤池,利用分层生物滤池对污水中的有机物、悬浮物和氨氮等进行预处理,利用人工湿地对污水中的氮、磷和剩余有机物进一步进行处理、通过物理、化学、生物综合作用达到净化水质的目的。传统的生物滤池工艺单独使用时处理出水能达到二级标准,用传统的人工湿地单独处理生活污水,每处理1m3污水,约需10m2以上土地。而本装置提供的联合工艺应用实例出水水质各项指标经检测均优于《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级B标准,吨水占地面积约3.5m2Aiming at the above-mentioned deficiencies in the prior art, the utility model provides a combined layered biological filter for sewage treatment. The layered biological filter is used to pretreat the organic matter, suspended matter and ammonia nitrogen in the sewage. Constructed wetlands further process nitrogen, phosphorus and remaining organic matter in sewage, and achieve the purpose of purifying water quality through comprehensive physical, chemical and biological effects. When the traditional biofilter process is used alone, the effluent can reach the secondary standard. If the traditional artificial wetland is used to treat domestic sewage alone, more than 10m 2 of land is required for processing 1m 3 of sewage. In the combined process application example provided by this device, all indicators of effluent water quality have been tested to be superior to the first-level B standard of "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002), and the area per ton of water is about 3.5m 2 .

本实用新型是通过以下技术方案实现的,本实用新型包括:依次串联连接的集水池、生物滤池、中间池和水平潜流式湿地。The utility model is realized through the following technical solutions, and the utility model comprises: a sump pond, a biological filter pond, an intermediate pond and a horizontal submerged wetland which are sequentially connected in series.

所述的中间池的下端设有回流口并与集水池相连。The lower end of the intermediate pool is provided with a return port and is connected with the sump.

所述的集水池为两格式钢筋混凝土结构,沿水流方向体积分配比例为2∶1。The sump is a two-form reinforced concrete structure, and the volume distribution ratio along the direction of water flow is 2:1.

所述的集水池内设有格栅、自动液位控制器和潜污泵,其中:格栅位于集水池两格之间的挡墙上,自动液位控制器和潜污泵置于格栅后的水格内。The sump is equipped with a grille, an automatic liquid level controller and a submersible sewage pump, wherein: the grille is located on the retaining wall between the two grids of the sump, and the automatic liquid level controller and the submersible sewage pump are placed on the grille In the water grid behind.

所述的格栅的网格小于10mm,面积大于等于1.0m2The mesh of the grid is less than 10mm, and the area is greater than or equal to 1.0m 2 .

所述的生物滤池由上而下依次包括:布水装置、由第一池体与滤料组成的滤床和排水系统,其中:滤床为分层框架结构,单层高40-50cm,层间间距大于等于50mm。The biological filter comprises from top to bottom: a water distribution device, a filter bed composed of a first pool body and a filter material, and a drainage system, wherein: the filter bed is a layered frame structure, and the height of a single layer is 40-50cm. Interlayer spacing is greater than or equal to 50mm.

所述的滤料为火山岩生物填料、陶粒和除磷填料。The filter material is volcanic rock biological filler, ceramsite and phosphorus removal filler.

所述的中间池包括:第二池体、配水系统和回流管,其中:第二池体的有效水深大于等于2.0m,带有三角堰的配水系统位于第二池体出水端并将水均分为若干份且分别流入湿地以及通过回流管回流至集水池。The intermediate pool includes: a second pool body, a water distribution system and a return pipe, wherein: the effective water depth of the second pool body is greater than or equal to 2.0m, and the water distribution system with a triangular weir is located at the water outlet end of the second pool body and distributes the water evenly It is divided into several parts and flows into the wetland respectively and returns to the sump through the return pipe.

所述的水平潜流式湿地由下而上依次包括:防渗层、填料层、土壤层、耐水植物层和出水布水渠。The horizontal subsurface wetland comprises, from bottom to top, an anti-seepage layer, a filling layer, a soil layer, a water-resistant plant layer, and a water distribution channel.

在人为调控下,由基质-微生物-植物构成的生态系统中物理、化学和生物的综合作用完成对污水氮的反硝化、磷的吸附和剩余有机物的去除等,人工湿地出水通过出水管排出系统。为提高系统的处理效果,中间池部分出水可回流至集水池。Under human control, the comprehensive action of physics, chemistry and biology in the ecosystem composed of substrate-microbe-plant completes the denitrification of sewage nitrogen, adsorption of phosphorus and removal of remaining organic matter, etc., and the effluent of the constructed wetland is discharged from the system through the outlet pipe . In order to improve the treatment effect of the system, part of the effluent from the middle pool can be returned to the sump.

本装置通过以下方式进行工作:生活污水经格栅后进入集水池,由泵自动提升至组合式分层生物滤池,与其中的生物膜进行充分接触,污染物被微生物吸附并降解;滤池出水经沉淀后部分回流至集水池,其余进入人工湿地系统,在填料-土壤-植物共同作用下进一步去除有机物、氮和磷,出水达标准后排入附近水体。The device works in the following way: the domestic sewage enters the sump after passing through the grille, and is automatically lifted by the pump to the combined layered biological filter, where it fully contacts with the biofilm, and the pollutants are absorbed and degraded by microorganisms; the filter Part of the effluent flows back to the sump after sedimentation, and the rest enters the constructed wetland system, where organic matter, nitrogen and phosphorus are further removed under the joint action of filler-soil-plants, and the effluent is discharged into nearby water bodies after reaching the standard.

本装置与现有技术相比,具有以下优点及有益效果:Compared with the prior art, this device has the following advantages and beneficial effects:

(1)采用分层生物滤池和人工湿地进行工艺组合,组合后各单元在发挥自身作用同时,可功能互补,从而提高整体效果。(1) The layered biofilter and artificial wetland are used for process combination. After the combination, each unit can complement each other while playing its own role, thereby improving the overall effect.

(2)分层生物滤池通风条件好,充氧能力强,作为人工湿的前处理,提高了整个工艺对生活污水的抗冲击能力,能有效削减污水中的有机物、悬浮物,并为氨氮的硝化提供了便利,并大幅度降低了后续人工湿地的污染负荷和占地面积(为传统人工湿地的1/3~1/2)。(2) The layered biological filter has good ventilation conditions and strong oxygenation capacity. As a pre-treatment of artificial wet, it improves the impact resistance of the whole process to domestic sewage, and can effectively reduce organic matter and suspended matter in sewage, and generate ammonia nitrogen. The nitrification provides convenience, and greatly reduces the pollution load and floor area of the subsequent constructed wetland (1/3 to 1/2 of the traditional constructed wetland).

(3)潜流湿地采用粒径30~50mm的充气混凝土做为填料,该填料以70%粉煤灰、15%生石灰、10%水泥、3%磷石膏及2%其它为原料,在高温高压下充气压制而成,一方面对磷具有较强的吸附性能,可有效削减污水中总磷含量;另一方面该填料大的比表面积易于微生物挂膜生长,可同时有效去除污水中的有机物和氮磷;第三,采用大粒径填料利于提高系统的过水能力,克服了传统湿地易堵塞的缺点,可长期稳定运行。系统对氮、磷的去除率与现有技术相比有显著提高,总氮去除率为50~60%,总磷的去除率为70~80%,并有着较少的占地面积和基建投资,管理简单。(3) Subsurface flow wetlands use aerated concrete with a particle size of 30-50mm as the filler. The filler is made of 70% fly ash, 15% quicklime, 10% cement, 3% phosphogypsum and 2% others. Inflated and compressed, on the one hand, it has strong adsorption performance on phosphorus, which can effectively reduce the total phosphorus content in sewage; on the other hand, the large specific surface area of the filler is easy for microbial film growth, and can effectively remove organic matter and nitrogen in sewage at the same time Phosphorus; third, the use of large particle size fillers is beneficial to improve the water passing capacity of the system, overcomes the shortcomings of traditional wetlands that are easy to block, and can run stably for a long time. Compared with the existing technology, the removal rate of nitrogen and phosphorus of the system has been significantly improved, the removal rate of total nitrogen is 50-60%, the removal rate of total phosphorus is 70-80%, and it has less land occupation and infrastructure investment , easy to manage.

附图说明 Description of drawings

图1为本装置俯视图;Figure 1 is a top view of the device;

图2为实施例应用示意图;Fig. 2 is the schematic diagram of embodiment application;

图3为滤池剖面图。Figure 3 is a cross-sectional view of the filter.

具体实施方式 Detailed ways

下面对本装置的实施例作详细说明,本实施例在以本装置技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本装置的保护范围不限于下述的实施例。The embodiment of the device is described in detail below. This embodiment is implemented on the premise of the technical solution of the device, and the detailed implementation and specific operation process are provided, but the protection scope of the device is not limited to the following implementation example.

实施例1、上海市松江区泖港镇曹家浜村污水处理工程Example 1. Sewage treatment project in Caojiabang Village, Maogang Town, Songjiang District, Shanghai

工程设计处理规模60m3/d,占地面积250m2,服务人口约900人,收集处理约235户村民的生活污水。The designed treatment scale of the project is 60m 3 /d, covers an area of 250m 2 , serves a population of about 900, and collects and treats domestic sewage from about 235 villagers.

本实施例包括:依次串联连接的集水池1、生物滤池2、中间池3和水平潜流式湿地4,本实例未设回流。This embodiment includes: a sump 1 , a biofilter 2 , an intermediate pool 3 and a horizontal subsurface wetland 4 connected in series in sequence, and no backflow is provided in this example.

所述的中间池3的下端设有回流口5并与集水池1相连。The lower end of the intermediate pool 3 is provided with a return port 5 and is connected with the sump 1 .

所述的集水池1为两格式钢筋混凝土结构,沿水流方向体积分配比例为2∶1。The sump 1 is a reinforced concrete structure with two formats, and the volume distribution ratio along the direction of water flow is 2:1.

所述的集水池1内设有格栅6、自动液位控制器7和潜污泵8,其中:格栅6位于集水池1两格之间的挡墙上,自动液位控制器7和潜污泵8置于格栅6后的水格内。The sump 1 is provided with a grille 6, an automatic liquid level controller 7 and a submersible sewage pump 8, wherein: the grille 6 is located on the retaining wall between the two grids of the sump 1, and the automatic liquid level controller 7 and The submersible sewage pump 8 is placed in the water grid behind the grid 6 .

所述的格栅6的网格小于10mm,面积大于等于1.0m2The mesh of the grid 6 is less than 10mm, and the area is greater than or equal to 1.0m 2 .

所述的生物滤池2由上而下依次包括:布水装置9、由第一池体10与滤料11组成的滤床12和排水系统13,其中:滤床12为分层框架结构,单层高40-50cm,层间间距大于等于50mm。The biological filter 2 includes from top to bottom: a water distribution device 9, a filter bed 12 composed of a first pool body 10 and a filter material 11, and a drainage system 13, wherein: the filter bed 12 is a layered frame structure, The height of a single layer is 40-50cm, and the distance between layers is greater than or equal to 50mm.

所述的滤料11为火山岩生物填料、陶粒和除磷填料。The filter material 11 is volcanic rock biological filler, ceramsite and phosphorus removal filler.

所述的中间池3包括:配水系统14、回流管15和第二池体16,其中:第二池体16的有效水深大于等于2.0m,带有三角堰的配水系统14位于第二池体16出水端并将水均分为若干份且分别流入湿地以及通过回流管15回流至集水池1。The intermediate pool 3 includes: a water distribution system 14, a return pipe 15 and a second pool body 16, wherein: the effective water depth of the second pool body 16 is greater than or equal to 2.0m, and the water distribution system 14 with a triangular weir is located in the second pool body 16 the water outlet and divide the water into several parts and flow into the wetland respectively and return to the sump 1 through the return pipe 15 .

所述的水平潜流式湿地4由下而上依次包括:防渗层17、填料层18、土壤层19、耐水植物层20、进水布水渠21和出水渠22。The horizontal subsurface flow wetland 4 includes, from bottom to top, an anti-seepage layer 17 , a filler layer 18 , a soil layer 19 , a water-resistant plant layer 20 , an inlet distribution channel 21 and an outlet channel 22 .

集水池1有效容积为15m3,有效水深1.0m。滤池分为6层,水力负荷为4m3/m3.d,滤池采用火山岩、陶粒及除磷滤料11复合滤料11。中间池3有效容积为7.5m3,水力停留时间为3h。人工湿地有效面积180m2,水力负荷为0.33m3/m2.d,填料层18厚0.6m,采用充气混凝土,土壤层19厚30cm,上植黑麦草。工程于2007年10月底建成并投运行,至今已稳定运行3年半。工程运行完全自动化,管理简单,不需专人值守,只需定期检查。运行费用以为主,吨水运行费用不超过0.1元。The pool 1 has an effective volume of 15m 3 and an effective water depth of 1.0m. The filter tank is divided into 6 layers, and the hydraulic load is 4m 3 /m 3 .d. The filter tank uses volcanic rock, ceramsite and phosphorus removal filter material 11 composite filter material 11. The effective volume of the middle pool 3 is 7.5m 3 , and the hydraulic retention time is 3h. The effective area of the constructed wetland is 180m 2 , the hydraulic load is 0.33m 3 /m 2 .d, the filler layer 18 is 0.6m thick, aerated concrete is used, the soil layer 19 is 30cm thick, and ryegrass is planted on top. The project was completed and put into operation at the end of October 2007, and has been in stable operation for three and a half years. The project operation is fully automated, the management is simple, no special personnel are required to be on duty, and only regular inspections are required. The operating cost is mainly, and the operating cost per ton of water does not exceed 0.1 yuan.

曹家浜生活污水处理工程氨氮、总氮和总磷平均去除率为75%,65%,70%;出水浓度分别在60mg/L,8mg/L和0.8mg/L以下,出水达到了《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级B标准。The average removal rate of ammonia nitrogen, total nitrogen and total phosphorus in Caojiabang domestic sewage treatment project is 75%, 65% and 70%; the effluent concentration is below 60mg/L, 8mg/L and 0.8mg/L respectively, and the effluent has reached the "urban Discharge Standard of Pollutants for Sewage Treatment Plants (GB 18918-2002) Level B Standard.

实施例2:上海市浦东新区航头镇牌楼村污水处理示范工程Example 2: Sewage Treatment Demonstration Project in Pailou Village, Hangtou Town, Pudong New Area, Shanghai

工程设计处理规模60m3/d,占地面积210m2,电耗0.1kWh/m3,服务牌楼村350名村民和现代生态农庄1座。The project design treatment scale is 60m 3 /d, covers an area of 210m 2 , and consumes 0.1kWh/m 3 power, serving 350 villagers in Pailou Village and one modern ecological farm.

本实施例包括:集水池1、组合式分层生物滤池2、中间池3和水平潜流式湿地4,其中:集水池1、生物滤池2、中间池3和水平潜流式湿地4依次串联连接,中间池3的末端设有回流口并与集水池1相连。集水池有效容积为20m3,有效水深1.0m。滤池分为6层,水力负荷为4m3/m3.d,采用火山岩、陶粒及除磷滤料复合滤料。中间池有效容积为7.5m3,水力停留时间为3h。人工湿地有效面积150m2,水力负荷为0.4m3/m2.d,填料层厚0.8m,采用充气混凝土,土壤层厚30cm,上植草皮和灌木。2009年5月底正式投入运行。组合工艺投入运行后,系统处理后,每年可削减COD 21.18t,氨氮1.24t,总磷0.22t。出水COD、氨氮、总磷均能满足《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级B标准。This embodiment includes: a sump 1, a combined layered biofilter 2, an intermediate pool 3 and a horizontal submerged wetland 4, wherein: the sump 1, the biofilter 2, the intermediate pool 3 and the horizontal submerged wetland 4 are connected in series in sequence The end of the middle pool 3 is provided with a return port and is connected with the sump 1. The effective volume of the sump is 20m 3 , and the effective water depth is 1.0m. The filter tank is divided into 6 layers, the hydraulic load is 4m 3 /m 3 .d, and the composite filter material of volcanic rock, ceramsite and phosphorus removal filter material is used. The effective volume of the middle pool is 7.5m 3 , and the hydraulic retention time is 3h. The effective area of the constructed wetland is 150m 2 , the hydraulic load is 0.4m 3 /m 2 .d, the thickness of the filler layer is 0.8m, aerated concrete is used, the soil layer is 30cm thick, and turf and shrubs are planted on it. It was officially put into operation at the end of May 2009. After the combined process is put into operation and treated by the system, COD can be reduced by 21.18t, ammonia nitrogen by 1.24t, and total phosphorus by 0.22t every year. The effluent COD, ammonia nitrogen, and total phosphorus can all meet the first-level B standard of the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002).

实施例3:上海市崇明县港沿镇污水处理示范工程Example 3: Sewage Treatment Demonstration Project in Gangyan Town, Chongming County, Shanghai

崇明县港沿镇集镇区生活污水收集处理工程设计污水收集和处理规模为500m3/d,服务人口4380人,总占地面积1300m2,南北长130m,东西宽宽约10~11.5m。The domestic sewage collection and treatment project in Jizhen District, Gangyan Town, Chongming County has a designed sewage collection and treatment scale of 500m 3 /d, serving a population of 4,380 people, a total area of 1,300m 2 , a length of 130m from north to south, and a width of 10-11.5m from east to west.

本实施例包括:集水池1、组合式分层生物滤池2、中间池3和水平潜流式湿地4,其中:集水池1、生物滤池2、中间池3和水平潜流式湿地4依次串联连接,本实例未设回流。集水池有效容积为120m3,有效水深1.0m。滤池占地面积100m2,滤床分为7层,水力负荷为4m3/m3.d,采用火山岩、陶粒及除磷滤料复合滤料。中间池有效容积为62.5m3,水力停留时间为3h。人工湿地有效面积1100m2,水力负荷为0.45m3/m2.d,填料层厚0.8m,采用充气混凝土,土壤层厚30cm,上植黑麦草。工程于2009年10月正式投入运行。吨水运行费用不超过0.15元。This embodiment includes: a sump 1, a combined layered biofilter 2, an intermediate pool 3 and a horizontal submerged wetland 4, wherein: the sump 1, the biofilter 2, the intermediate pool 3 and the horizontal submerged wetland 4 are connected in series in sequence connection, this example does not set backflow. The effective volume of the sump is 120m 3 , and the effective water depth is 1.0m. The filter covers an area of 100m 2 , the filter bed is divided into 7 layers, the hydraulic load is 4m 3 /m 3 .d, and the composite filter material of volcanic rock, ceramsite and phosphorus removal filter material is used. The effective volume of the middle pool is 62.5m 3 , and the hydraulic retention time is 3h. The effective area of the constructed wetland is 1100m 2 , the hydraulic load is 0.45m 3 /m 2 .d, the filler layer is 0.8m thick, aerated concrete is used, the soil layer is 30cm thick, and ryegrass is planted on top. The project was officially put into operation in October 2009. The operating cost per ton of water is not more than 0.15 yuan.

经组合工艺处理后,COD、氨氮、总磷出水浓度分别小于56mg/L,12mg/L,0.9mg/L,均达到了《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级B标准。After combined process treatment, the effluent concentrations of COD, ammonia nitrogen, and total phosphorus are less than 56mg/L, 12mg/L, and 0.9mg/L respectively, all of which have reached the first level of the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002) B standard.

Claims (9)

1.一种用于污水处理的组合式分层生物滤池,其特征在于,包括依次串联连接的集水池、生物滤池、中间池和水平潜流式湿地。1. A combined layered biofilter for sewage treatment, characterized in that it comprises a sump, a biofilter, an intermediate pond and a horizontal underflow wetland connected in series in succession. 2.根据权利要求1所述的用于污水处理的组合式分层生物滤池,其特征是,所述的中间池的下端设有回流口并与集水池相连。2. The combined layered biofilter for sewage treatment according to claim 1, characterized in that, the lower end of the intermediate pool is provided with a return port and is connected to the sump. 3.根据权利要求1所述的用于污水处理的组合式分层生物滤池,其特征是,所述的集水池为两格式钢筋混凝土结构,沿水流方向体积分配比例为2∶1。3. The combined layered biofilter for sewage treatment according to claim 1, characterized in that the sump is a two-frame reinforced concrete structure, and the volume distribution ratio along the water flow direction is 2:1. 4.根据权利要求1或2或3所述的用于污水处理的组合式分层生物滤池,其特征是,所述的集水池内设有格栅、自动液位控制器和潜污泵,其中:格栅位于集水池两格之间的挡墙上,自动液位控制器和潜污泵置于格栅后的水格内。4. The combined layered biofilter for sewage treatment according to claim 1, 2 or 3, characterized in that a grid, an automatic liquid level controller and a submersible sewage pump are arranged in the sump , wherein: the grid is located on the retaining wall between the two grids of the sump, and the automatic liquid level controller and submersible sewage pump are placed in the water grid behind the grid. 5.根据权利要求4所述的用于污水处理的组合式分层生物滤池,其特征是,所述的格栅的网格小于10mm,面积大于等于1.0m25 . The combined layered biofilter for sewage treatment according to claim 4 , wherein the mesh of the grid is less than 10 mm, and the area is greater than or equal to 1.0 m 2 . 6.根据权利要求4所述的用于污水处理的组合式分层生物滤池,其特征是,所述的生物滤池由上而下依次包括:布水装置、由第一池体与滤料组成的滤床和排水系统,其中:滤床为分层框架结构,单层高40-50cm,层间间距大于等于50mm。6. The combined layered biofilter for sewage treatment according to claim 4, wherein the biofilter comprises from top to bottom: a water distribution device, a first pool body and a filter The filter bed and drainage system are composed of materials, wherein: the filter bed is a layered frame structure, the height of a single layer is 40-50cm, and the distance between layers is greater than or equal to 50mm. 7.根据权利要求6所述的用于污水处理的组合式分层生物滤池,其特征是,所述的滤料为火山岩生物填料、陶粒和除磷填料。7. The combined layered biofilter for sewage treatment according to claim 6, wherein the filter material is volcanic rock biological filler, ceramsite and phosphorus removal filler. 8.根据权利要求1所述的用于污水处理的组合式分层生物滤池,其特征是,所述的中间池包括:第二池体、配水系统和回流管,其中:第二池体的有效水深大于等于2.0m,带有三角堰的配水系统位于第二池体出水端并将水均分为若干份且分别流入湿地以及通过回流管回流至集水池。8. The combined layered biofilter for sewage treatment according to claim 1, characterized in that, the intermediate pool comprises: a second pool body, a water distribution system and a return pipe, wherein: the second pool body The effective water depth is greater than or equal to 2.0m. The water distribution system with a triangular weir is located at the water outlet of the second pool and divides the water into several parts, which flow into the wetland and return to the sump through the return pipe. 9.根据权利要求1或2所述的用于污水处理的组合式分层生物滤池,其特征是,所述的水平潜流式湿地由下而上依次包括:防渗层、填料层、土壤层、耐水植物层和出水布水渠。9. The combined layered biofilter for sewage treatment according to claim 1 or 2, characterized in that the horizontal subsurface wetland sequentially comprises from bottom to top: anti-seepage layer, filler layer, soil layer, water-resistant plant layer and outlet cloth canal.
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CN103043867A (en) * 2013-01-09 2013-04-17 王洪臣 Low-energy self-circulation treatment method for rural sewage
CN103058358A (en) * 2013-01-29 2013-04-24 上海交通大学 Biological filter capable of improving sewage interception capacity of down-flow biological filter
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CN105314797A (en) * 2015-11-23 2016-02-10 上海应用技术学院 Bacterial earthworm filter for synchronous treatment of sewage and sludge and application thereof
CN105399275A (en) * 2015-11-27 2016-03-16 中铁五局集团建筑工程有限责任公司 Wastewater treatment method
CN106336087A (en) * 2016-11-03 2017-01-18 湖北省农业科学院植保土肥研究所 Integrated household biological filter tower for treating rural domestic wastewater
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