CN201372233Y - Unpowered Integrated Constructed Wetland Sewage Treatment System - Google Patents
Unpowered Integrated Constructed Wetland Sewage Treatment System Download PDFInfo
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- CN201372233Y CN201372233Y CN200920114602U CN200920114602U CN201372233Y CN 201372233 Y CN201372233 Y CN 201372233Y CN 200920114602 U CN200920114602 U CN 200920114602U CN 200920114602 U CN200920114602 U CN 200920114602U CN 201372233 Y CN201372233 Y CN 201372233Y
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Abstract
本实用新型公开了一种无动力一体化人工湿地污水处理系统。其特征在于垂直流污水生态净化槽分为上下两个分区,经前处理的生活污水经过水泵提升或依靠自然液位高差进入布水系统,预处理后的污水通过交叉布水管网均匀分布于垂直潜流式生态净化槽硝化区域上,依次垂直渗入硝化区域和反硝化区域的人工基质层,布水系统对生态净化槽实行间歇布水,并在上层硝化区域底部和内部设有无动力布气系统,对硝化区域实现连续复氧,上层硝化区域出水直接进入下层反硝化区域,下层反硝化区域内设有集水出水系统,集水口设于反硝化区域下方,出水口设于反硝化区域上方,使出水在反硝化区域内保持一定水位。本实用新型能够实现湿地无动力自然复氧,占地面积小,硝化反硝化一体化高效脱氮。
The utility model discloses an unpowered integrated artificial wetland sewage treatment system. It is characterized in that the vertical flow sewage ecological purification tank is divided into upper and lower partitions. The pre-treated domestic sewage is lifted by the pump or enters the water distribution system relying on the natural liquid level difference. The pretreated sewage is evenly distributed in the water distribution system through the cross water distribution network On the nitrification area of the vertical submerged ecological purification tank, it infiltrates vertically into the artificial matrix layer of the nitrification area and the denitrification area in turn. The water distribution system implements intermittent water distribution for the ecological purification tank, and a non-powered air distribution system is installed at the bottom and inside of the upper nitrification area. The system realizes continuous reoxygenation of the nitrification area, the water from the upper nitrification area directly enters the lower denitrification area, and the lower denitrification area is equipped with a water collection and discharge system. The water collection port is located below the denitrification area, and the water outlet is located above the denitrification area. , so that the effluent maintains a certain water level in the denitrification area. The utility model can realize unpowered natural reoxygenation of the wetland, occupies a small area, and integrates nitrification and denitrification with high-efficiency denitrification.
Description
技术领域 technical field
本实用新型涉及环境保护技术领域,尤其涉及污水处理生态工程技术。The utility model relates to the technical field of environmental protection, in particular to ecological engineering technology for sewage treatment.
背景技术 Background technique
人工湿地污水处理技术是20世纪70年代兴起的一种污水处理生态工程新技术,具有投资少、能耗低、管理方便、无二次污染等优点,正在逐渐被应用于广大农村和中小城镇生活污水处理领域。Constructed wetland sewage treatment technology is a new ecological engineering technology for sewage treatment that emerged in the 1970s. It has the advantages of low investment, low energy consumption, convenient management, and no secondary pollution. It is gradually being used in rural areas and small and medium-sized cities and towns. Sewage treatment field.
人工湿地是人工建造的、可控制的和工程化的湿地系统,一般由池体、人工填料基质、布水系统、集水系统和生长在人工基质上的植物组成,是一个独特的基质-植物-微生物生态系统。人工湿地生态系统水质净化的基本原理是:在一定的填料上种植特定的植物,将污水投加到人工建造的类似于沼泽的湿地上,当污水流过人工湿地时,经砂石、土壤过滤,植物根际的多种微生物活动,使得水质得到净化。根据实验和大量的工程实践证明,人工生态滤床能够很好地去除BOD、TSS、N、P,而且对病原细菌、难降解有机化合物以及金属离子的去除效果也十分有效。人工湿地对环境和经济的综合作用主要体现在以下几个方面:弥补或减少因农业和城市发展对天然湿地造成的影响;构建水生系统,产生食物和纤维;调蓄雨水径流和防洪;进行污水处理,改善水质。Constructed wetlands are artificially constructed, controllable and engineered wetland systems, generally composed of pools, artificial filler substrates, water distribution systems, water collection systems and plants growing on artificial substrates. It is a unique substrate-plant - Microbial ecosystems. The basic principle of water quality purification in the constructed wetland ecosystem is: plant specific plants on certain fillers, add sewage to the artificially constructed wetland similar to a swamp, and when the sewage flows through the constructed wetland, it is filtered through sand, gravel and soil , A variety of microbial activities in the plant rhizosphere make the water quality purified. According to experiments and a large number of engineering practices, artificial ecological filter beds can remove BOD, TSS, N, and P well, and are also very effective in removing pathogenic bacteria, refractory organic compounds, and metal ions. The comprehensive effects of constructed wetlands on the environment and economy are mainly reflected in the following aspects: making up for or reducing the impact of agricultural and urban development on natural wetlands; building aquatic systems to produce food and fiber; regulating stormwater runoff and flood control; treatment to improve water quality.
潜流式垂直流人工湿地是人工湿地的一种类型,主要特点在于:布水系统平铺在上部基质中,将污水均布在基质水平断面后,污水均匀向下流动,流动过程中使污水得到净化;在湿地底部基质中铺设集水系统,收集处理后均布在水平断面的出水经汇集后排出。潜流式垂直流人工湿地充分利用了湿地空间,充分发挥了系统间的协同作用,污水处理后可去除大部分有机质并进行较充分硝化作用,已逐渐成为人工湿地技术发展的主流方向。但是传统的潜流式垂直流人工湿地对污水的反硝化效果不好,不能达到高效脱氮除磷的目的,由于处理过程中不能充分复氧,对污水进行的好氧脱有机物的效果也不甚理想。鉴于上述缺陷,研究人员发明了大量技术改进潜流式垂直流人工湿地,以增加污染物的处理效率。如中国专利CN 1263688C《生活污水垂直流-水平流复合人工湿地脱氮除磷方法》,披露了一种垂直流人工湿地在前,水平流人工湿地在后的串联式复合人工湿地处理工艺。在水平流湿地前人为补充未处理污水为碳源增加水平流人工湿地的反硝化作用效果。但垂直流湿地不能充分复氧,影响了硝化作用和好氧氧化的处理效果,两湿地串联占地面积大、造价高、实用性差。中国专利CN 1325397C《序批式潜流人工湿地污水处理工艺》,披露了一种利用机械自动化方式控制电磁阀对湿地间歇排水出水以实现阶段性复氧。其在一定程度上增加了垂直潜流式人工湿地的复氧效果,但其需外加动力控制系统,增加了投资,另外对于污水的反硝化脱氮无显著的促进作用。The submerged vertical flow constructed wetland is a type of constructed wetland. The main features are: the water distribution system is laid flat in the upper matrix, and the sewage is evenly distributed on the horizontal section of the matrix. The sewage flows downward evenly, and the sewage is obtained during the flow process. Purification: A water collection system is laid in the bottom matrix of the wetland, and the effluent that is evenly distributed in the horizontal section after collection and treatment is collected and discharged. Submerged vertical flow constructed wetlands make full use of the wetland space and give full play to the synergy between systems. After sewage treatment, most of the organic matter can be removed and nitrification can be carried out more fully. It has gradually become the mainstream direction of the development of constructed wetland technology. However, the traditional submerged vertical flow constructed wetland has a poor denitrification effect on sewage, and cannot achieve the purpose of efficient nitrogen and phosphorus removal. Due to insufficient reoxygenation during the treatment process, the effect of aerobic deorganization on sewage is not very good. ideal. In view of the above defects, researchers have invented a large number of technologies to improve subsurface vertical flow constructed wetlands to increase the efficiency of pollutant treatment. For example, the Chinese patent CN 1263688C "Method for Removing Nitrogen and Phosphorus by Vertical Flow-Horizontal Flow Composite Constructed Wetland of Domestic Sewage" discloses a tandem composite constructed wetland treatment process in which the vertical flow constructed wetland is in front and the horizontal flow constructed wetland is followed. Artificially supplementing untreated sewage as a carbon source in front of the horizontal flow wetland increases the denitrification effect of the horizontal flow constructed wetland. However, the vertical flow wetland cannot fully reoxygenate, which affects the treatment effect of nitrification and aerobic oxidation. The connection of two wetlands occupies a large area, high cost, and poor practicability. Chinese patent CN 1325397C "Sequence Batch Submerged Flow Constructed Wetland Sewage Treatment Process" discloses a method of using mechanical automation to control solenoid valves to intermittently drain water from wetlands to achieve staged reoxygenation. It increases the reoxygenation effect of the vertical underflow constructed wetland to a certain extent, but it requires an additional power control system, which increases investment, and has no significant promotion effect on denitrification and denitrification of sewage.
发明内容 Contents of the invention
本实用新型旨在提供一种能够实现湿地无动力自然复氧,占地面积小,硝化反硝化一体化高效脱氮的无动力一体化人工湿地污水处理系统。The utility model aims to provide a non-powered integrated constructed wetland sewage treatment system capable of realizing unpowered natural reoxygenation of wetlands, occupying a small area, and integrating nitrification and denitrification with high-efficiency nitrogen removal.
本实用新型解决上述技术问题所采用的技术方案为:一种无动力一体化人工湿地污水处理系统,包括由硝化区域和反硝化区域两部分组成的垂直流污水生态净化槽、填充槽内的基质、污水预处理系统、布水系统、集水系统、布气系统、排污系统和生长在基质上的植物,其特征在于:The technical scheme adopted by the utility model to solve the above-mentioned technical problems is: a non-powered integrated artificial wetland sewage treatment system, including a vertical flow sewage ecological purification tank composed of two parts, a nitrification area and a denitrification area, and a substrate in the filling tank , sewage pretreatment system, water distribution system, water collection system, air distribution system, sewage system and plants growing on the substrate, characterized in that:
所述的垂直流污水生态净化槽分为上下两个分区:硝化区域和反硝化区域,硝化区域在上,反硝化区域在下,所述人工基质分别填充在硝化区域和反硝化区域中;The vertically flowing sewage ecological purification tank is divided into upper and lower areas: a nitrification area and a denitrification area, the nitrification area is on the top, and the denitrification area is on the bottom, and the artificial matrix is filled in the nitrification area and the denitrification area respectively;
所述的污水预处理系统为利用格栅、三格式沉淀池、厌氧池中的一种或几种前处理工艺对不同污染负荷的污水进行前处理,经前处理的生活污水经过水泵提升或依靠自然液位高差进入布水系统;预处理后的污水通过交叉布水管网均匀分布于垂直潜流式生态净化槽硝化区域上,依次垂直渗入硝化区域和反硝化区域的人工基质层;布水系统对生态净化槽实行间歇布水,并在上层硝化区域底部和内部设有无动力布气系统,对硝化区域实现连续复氧,使污水在上层硝化区域内进行高效的好氧作用和硝化作用;上层硝化区域出水直接进入下层反硝化区域,在此区域内进行兼氧作用和反硝化作用;下层反硝化区域内设有集水出水系统,集水口设于反硝化区域下方,出水口设于反硝化区域上方,使出水在反硝化区域内保持一定水位。The sewage pretreatment system uses one or several pretreatment processes in the grid, three-format sedimentation tank, and anaerobic tank to pretreat sewage with different pollution loads, and the pretreated domestic sewage is lifted by a water pump or Rely on the natural liquid level height difference to enter the water distribution system; the pretreated sewage is evenly distributed on the nitrification area of the vertical submerged ecological purification tank through the cross water distribution pipe network, and then vertically penetrates into the artificial matrix layer of the nitrification area and denitrification area; water distribution The system implements intermittent water distribution for the ecological purification tank, and a non-powered air distribution system is installed at the bottom and inside of the upper nitrification area to realize continuous reoxygenation of the nitrification area, so that the sewage can perform efficient aerobic and nitrification in the upper nitrification area The effluent from the upper nitrification area directly enters the lower denitrification area, where facultative oxygenation and denitrification are carried out; the lower denitrification area is equipped with a water collection and discharge system, the water collection port is located below the denitrification area, and the water outlet is located at Above the denitrification area, keep the effluent at a certain level in the denitrification area.
在垂直流污水生态净化槽内,污水通过与基质、微生物和植物根系的作用,实现物理净化、生物净化作用,达到降低污水的SS、BOD、COD、细菌和高效脱氮除磷的目的。In the vertical flow sewage ecological purification tank, the sewage realizes physical purification and biological purification through the interaction with the substrate, microorganisms and plant roots, and achieves the purpose of reducing SS, BOD, COD, bacteria and efficient nitrogen and phosphorus removal of sewage.
作为优选,所述布水系统为设置在上层污水硝化区域基质表层下5-10cm的布水管网,该布水管网包含有进水阀门、进水口、布水主管和多个与该布水主管连接的布水分支,布水主管和布水分支呈垂直“王”字分布或交叉“王”字分布,布水分支上开有布水小孔。Preferably, the water distribution system is a water distribution pipe network arranged 5-10 cm below the substrate surface in the upper sewage nitrification area, and the water distribution pipe network includes a water inlet valve, a water inlet, a water distribution main pipe and a plurality of water distribution main pipes The connected water distribution branch, the water distribution main pipe and the water distribution branch are distributed vertically or cross the word "Wang", and there are small water distribution holes on the water distribution branch.
作为优选,所述集水系统为设置在下层反硝化区域的集水管网,该集水管网包含有集水口、垂直集水分支、水平集水分支、与垂直集水分支和水平集水分支连接的集水主管、出水口和出水阀门;集水主管和水平集水分支呈垂直“王”字分布或交叉“王”字分布,垂直集水分支与水平集水分支和集水主管之间呈空间垂直分布,中间管路相通;集水口设在垂直集水分支末端,为圆形管路截面上开有的数个集水小孔组成,集水口距离整个池体底部的距离不大于反硝化区域总高度的1/3;水平集水分支、集水主管和集水口位于同一水平高度,它们的水平位置为下层反硝化槽体顶端介于距反硝化槽体顶端2/3高度之间。Preferably, the water collection system is a water collection pipe network arranged in the lower denitrification area, and the water collection pipe network includes a water collection port, a vertical water collection branch, a horizontal water collection branch, and a connection with the vertical water collection branch and the horizontal water collection branch The main water collecting main, water outlet and water outlet valve; the main water collecting main and the horizontal water collecting branches are distributed in the shape of vertical "king" or cross "king", and the vertical water collecting branch and the horizontal water collecting branch and the water collecting main are in the form of The space is vertically distributed, and the middle pipes are connected; the water collection port is set at the end of the vertical water collection branch, which is composed of several small water collection holes on the circular pipe section, and the distance between the water collection port and the bottom of the entire pool is not greater than the denitrification 1/3 of the total height of the area; the horizontal water collection branch, the water collection main pipe and the water collection outlet are located at the same level, and their horizontal position is between the top of the lower denitrification tank and the height between 2/3 of the top of the denitrification tank.
作为优选,所述布气系统为分布在上层一组或多组管身开满小孔的布气管网;每组布气管网由水平布气管、与水平布气管垂直相连的数个垂直布气分支组成;所述垂直布气分支一端连接位于上层硝化区域底部到距离上层硝化区域底部2/3高度之间的水平布气分支,另一端竖直伸出池体基质顶部,与外部空气相连通,垂直布气分支顶端高于基质层表面3-10cm,并设有防尘帽,防止大颗粒物质进入管体堵塞布气管。As a preference, the air distribution system is distributed on the upper layer with one or more sets of air distribution pipe networks filled with small holes; each group of air distribution pipe network consists of horizontal air distribution pipes and several vertical air distribution pipes vertically connected Composed of branches; one end of the vertical air distribution branch is connected to the horizontal air distribution branch between the bottom of the upper nitrification area and 2/3 of the height from the bottom of the upper nitrification area, and the other end vertically protrudes from the top of the pool body matrix to communicate with the outside air , the top of the vertical air distribution branch is 3-10cm higher than the surface of the matrix layer, and a dust cap is provided to prevent large particles from entering the pipe body and blocking the air distribution pipe.
作为优选,所述的垂直流污水生态净化槽反硝化区域底部可呈中间低凹状,低凹最低处设有排水管,排水管表面布满排水小孔,排水管一端封闭,另一端伸出槽外作为排污口,排污口设排污阀门,正常工作时排污阀门关闭,槽体冲洗时排污阀门开启。As a preference, the bottom of the denitrification area of the vertically flowing sewage ecological purification tank can be concave in the middle, the lowest part of the depression is provided with a drainage pipe, the surface of the drainage pipe is covered with small drainage holes, one end of the drainage pipe is closed, and the other end protrudes out of the groove The outside is used as the sewage outlet, and the sewage outlet is equipped with a sewage valve. During normal operation, the sewage valve is closed, and the sewage valve is opened when the tank is flushed.
作为优选,上层硝化区域内部人工基质从下到上的结构分层及材料厚度如下:排水层,采用粒径8-16mm砾石,厚度10-35cm;过渡层,采用粒径4-8mm砾石,厚度8-15cm;生化处理过渡层,采用特殊级配0.2-6mm无泥粗砂,厚度50-60cm;表层采用粒径8-16mm砾石,厚度4-8cm;所述垂直流污水生态净化槽上部种植的植物选自芦苇、芦竹、香蒲、美人蕉、风车草、再力草、香根草、玫瑰、月季、万寿菊等中的一种或多种;As a preference, the structure layering and material thickness of the artificial matrix from bottom to top in the upper nitrification area are as follows: the drainage layer adopts gravel with a particle size of 8-16mm and a thickness of 10-35cm; the transition layer adopts gravel with a particle size of 4-8mm and a thickness of 10-35cm. 8-15cm; biochemical treatment transition layer, using special graded 0.2-6mm mud-free coarse sand, thickness 50-60cm; surface layer adopts gravel with particle size 8-16mm, thickness 4-8cm; the upper part of the vertical flow sewage ecological purification tank is planted The plants are selected from one or more of reeds, reed bamboos, cattails, cannas, windmill grass, zaili grass, vetiver, roses, roses, marigolds, etc.;
所述下层反硝化区域内部基质从下到上的结构分层及材料厚度如下:防渗层,采用0.5mm以上PE膜双面土工布或厚度为1-5cm的天然粘土防渗层;过渡层,采用粒径5-10mm砾石,厚度10-20cm;生化处理过渡层,采用煤渣基质层0.2-6mm,厚度50-60cm。The structural layering and material thickness of the inner matrix of the lower denitrification area from bottom to top are as follows: anti-seepage layer, using PE film double-sided geotextile with a thickness of 0.5mm or more or natural clay anti-seepage layer with a thickness of 1-5cm; transition layer , using gravel with a particle size of 5-10mm and a thickness of 10-20cm; the biochemical treatment transition layer uses a cinder matrix layer of 0.2-6mm and a thickness of 50-60cm.
作为优选,所述上层硝化区域四周侧壁可呈一定坡度,坡度范围0-10%;所述下层反硝化区域四周侧壁可呈一定坡度,坡度范围0-5%。As a preference, the sidewalls around the upper nitrification zone may present a certain slope, with a slope range of 0-10%; the sidewalls around the lower denitrification zone may present a certain slope, with a slope range of 0-5%.
本实用新型具有以下有益效果:The utility model has the following beneficial effects:
硝化与反硝化一体化,采用除磷滤渣,高效脱氮除磷;结构简单、占地面积小,节约土地资源,进、出水落差小,污水不需回流,场地不受限制,处理规模不受限制;间歇式进水,上层好氧、下层兼氧巧妙设计,实现自然无动力复氧促进氧化、硝化等反应的进行,提高污染物好氧处理效率;种芦苇,芦竹等湿地植物,抗酸碱,可去除污染负荷大的污染物。Nitrification and denitrification are integrated, phosphorus removal and filter residue are used, and nitrogen and phosphorus are removed efficiently; the structure is simple, the floor area is small, and land resources are saved. Restrictions; intermittent water inflow, aerobic upper layer and aerobic lower layer are ingeniously designed to realize natural unpowered reoxygenation to promote oxidation, nitrification and other reactions, and improve the efficiency of aerobic treatment of pollutants; plant wetland plants such as reeds and reeds, and resist Acid-base, can remove pollutants with heavy pollution load.
本实用新型涉及的人工湿地污水处理系统具有结构简单、安装容易、布水均匀、水位调节自由方便、不耗电、成本低,可以用于多种类型污水处理,例如生活污水、垃圾渗滤液、农业污水、石油化工废水、城市暴雨地表径流以及湖泊河流污染控制等。选择合适的植物品种还有美化周边环境的作用。The artificial wetland sewage treatment system involved in the utility model has the advantages of simple structure, easy installation, uniform water distribution, free and convenient water level adjustment, no power consumption, and low cost, and can be used for various types of sewage treatment, such as domestic sewage, garbage leachate, Agricultural sewage, petrochemical wastewater, urban rainstorm surface runoff and pollution control of lakes and rivers, etc. Choosing the right plant species can also beautify the surrounding environment.
附图说明 Description of drawings
图1为本实用新型的一种实施例结构示意图;Fig. 1 is a kind of embodiment structural representation of the utility model;
图2为图1布水管网的一种结构示意图;Fig. 2 is a kind of structural representation of Fig. 1 water distribution pipeline network;
图3为图1布水管网的另一种结构示意图;Fig. 3 is another schematic diagram of the structure of the water distribution pipe network in Fig. 1;
图4为图1排水管网的结构俯视图;Fig. 4 is the top view of the structure of the drainage network in Fig. 1;
图5为布水分支剖视图。Fig. 5 is a sectional view of the water distribution branch.
图中:1-预处理池,2-水泵,3-进水阀门,4、湿地植物,5-布水管网,6-池体硝化区域,7-防尘帽,8-垂直布气分支,9-水平布气管,10-布气小孔,11-出水阀门,12-出水口,13-垂直集水分支,14-排污口,15-排污阀门,16-排水小孔,17-排水管,18-集水口,19-池体反硝化区域,20-进水口,21-布水主管,22-布水分支,23-布水小孔,24-水平集水分支,25-集水主管In the figure: 1-pretreatment tank, 2-water pump, 3-water inlet valve, 4, wetland plants, 5-water distribution pipe network, 6-pool body nitrification area, 7-dust cap, 8-vertical gas distribution branch, 9-Horizontal air distribution pipe, 10-Air distribution small hole, 11-Water outlet valve, 12-Water outlet, 13-Vertical water collection branch, 14-Sewage outlet, 15-Drainage valve, 16-Drainage hole, 17-Drainage pipe , 18-Water collection port, 19-Pond denitrification area, 20-Water inlet, 21-Water distribution supervisor, 22-Water distribution branch, 23-Water distribution small hole, 24-Horizontal water collection branch, 25-Water collection supervisor
具体实施方式 Detailed ways
下面通过实施案例,并结合附图,对本实用新型的技术方案作进一步具体说明。The technical solution of the present utility model is further specifically described below through implementation examples and in conjunction with the accompanying drawings.
在本实施例中,预处理通常在三格式沉淀池中完成,污泥将定期清理。对于浓度较高的污水,可在滤床前端加建厌氧池。良好的预沉淀处理是人工生态滤床长期有效运行的保证,同时也能起到调节污水水量和水质的作用。经过预处理的污水,由间歇式污水泵提升,按照设定的控制参数,均匀分配到垂直流污水生态净化槽上层硝化区域人工基质的表面。In this example, pretreatment is usually done in a three-format sedimentation tank, and the sludge will be cleaned periodically. For sewage with higher concentration, an anaerobic pool can be built at the front end of the filter bed. Good pre-sedimentation treatment is the guarantee for the long-term effective operation of the artificial ecological filter bed, and it can also play a role in regulating the amount and quality of sewage water. The pretreated sewage is lifted by the intermittent sewage pump and evenly distributed to the surface of the artificial substrate in the upper nitrification area of the vertical flow sewage ecological purification tank according to the set control parameters.
本实用新型的主体污水处理区域-垂直流污水生态净化槽,它被分隔为相连通的上、下两个区域,上层硝化区域四周侧壁呈5%坡度,下底与下层反硝化区域上部连通,下层反硝化区域为长方体池体;上层硝化区域池内填充人工基质作为污水过滤床和微生物好氧氧化及硝化床,下层反硝化区域填充的人工基质作为污水过滤床和微生物兼氧氧化及反硝化床。上层硝化区域填设的基质由下到上分别为:厚度10-35cm,粒径8-16mm的砾石层;厚度8-15cm,粒径4-8mm的砾石层;厚度50-60cm,粒径0.2-6mm的无泥粗砂层;厚度4-8cm,粒径8-16mm砾石表层。生态净化床表层种植的湿地植物为芦苇和芦竹。The main sewage treatment area of the utility model - the vertical flow sewage ecological purification tank is divided into two connected upper and lower areas. The side walls around the upper nitrification area have a slope of 5%, and the lower bottom is connected to the upper part of the lower denitrification area. , the lower denitrification area is a cuboid pool body; the upper nitrification area pool is filled with artificial substrate as a sewage filter bed and microbial aerobic oxidation and nitrification bed, and the artificial substrate filled in the lower denitrification area is used as a sewage filter bed and microbial facultative oxidation and denitrification bed. The matrix filled in the upper nitrification area from bottom to top is: gravel layer with a thickness of 10-35cm and a particle size of 8-16mm; a gravel layer with a thickness of 8-15cm and a particle size of 4-8mm; a thickness of 50-60cm and a particle size of 0.2 -6mm mud-free coarse sand layer; thickness 4-8cm, particle size 8-16mm gravel surface. The wetland plants planted on the surface of the ecological purification bed are reeds and reed bamboos.
经预处理的污水通过水泵2提升,经进水阀门3进入交叉布水管网5的布水主管21和布水分支22,最终通过布水分支22上的布水小孔23进入池体基质层。布水分支22与布水主管21在同一水平面上,与其垂直相连呈“王”字型(如图2所示)或交叉“王”字型(如图3所示),布水分支22末端封闭,管体每隔10-20cm均匀开有布水小孔23,该布水小孔左右对称,且都位于管体的水平中心线以下。The pretreated sewage is lifted by the water pump 2, enters the water distribution
无动力布气系统由3-5组布气管网组成,它们均匀埋设在上层硝化池内部。每一组布气管网都由相连通的水平布气分支和垂直布气分支8组成,其中靠近池体外壁的垂直布气分支可沿池体坡度适当倾斜,管体上开有无数布气小孔10,其中垂直布气分支8上端伸出池体外的部分均加盖防尘帽。此无动力布气系统能够使池体基质自然富氧且富氧充分均匀,满足微生物好养反应的需要,另外从上层硝化区域流入下层反硝化区域的污水也可在流动过程在无动力布气系统的作用下增加溶解氧,使下层污水处理区域形成兼氧环境,提高污水的氧化效率。The unpowered gas distribution system consists of 3-5 groups of gas distribution pipe networks, which are evenly buried inside the upper nitrification tank. Each group of air distribution pipe network is composed of connected horizontal air distribution branches and vertical air distribution branches 8. Among them, the vertical air distribution branches close to the outer wall of the pool can be properly inclined along the slope of the pool body, and there are countless air distribution holes on the pipe body. The hole 10, wherein the upper end of the vertical air distribution branch 8 extends out of the pool body is covered with a dustproof cap. This unpowered air distribution system can make the pool matrix naturally rich in oxygen and fully uniform in oxygen, which meets the needs of microbial nutrient reactions. In addition, the sewage flowing from the upper nitrification area into the lower denitrification area can also distribute air without power during the flow process. Under the action of the system, dissolved oxygen is increased to form a facultative oxygen environment in the lower sewage treatment area and improve the oxidation efficiency of sewage.
经上层硝化区域处理后的污水直接渗入下层反硝化处理区域,该区域内填设的基质由下到上依次为厚度10-20cm,粒径5-10mm的砾石;厚度50-60cm,粒径0.2-6mm的煤渣基质层。该池体内铺设有潜入式集水管网,具有如下特点:垂直集水分支13与水平集水分支24和集水主管25之间呈空间垂直分布,中间管路相通;集水口设在垂直集水分支13末端,为圆形管路截面上开有的数个集水小孔组成,集水口距离整个池体底部的距离不大于反硝化区域总高度的1/3;水平集水分支24、集水主管25和集水口位于同一水平高度,它们的水平位置为下层反硝化槽体顶端介于距反硝化槽体顶端2/3高度之间。上层硝化区域污水进入下层反硝化区域后继续垂直下渗,至反硝化区域底部,由于集水管网出水口设在反硝化槽体上部,经反硝化区域处理至池体底部的出水虽然在池体底部进入集水口,但并不能即刻出水,污水在底部向上聚积,待垂直集水分支的出水水位达到出水口高度后方可由出水口出水。潜入式集水管网的作用是使污水在下层反硝化床中停留时间增长,营造兼氧环境,使有机物和总氮的降解更加充分。The sewage treated in the upper nitrification area directly infiltrates into the lower denitrification treatment area. The matrix filled in this area is gravel with a thickness of 10-20cm and a particle size of 5-10mm from bottom to top; a thickness of 50-60cm and a particle size of 0.2 -6mm cinder matrix layer. The pool body is laid with a submerged water collection pipe network, which has the following characteristics: the space between the vertical water collection branch 13 and the horizontal water collection branch 24 and the water collection main pipe 25 is vertically distributed, and the middle pipes are connected; the water collection port is located in the vertical water collection The end of the branch 13 is composed of several small water collection holes on the circular pipeline section. The distance between the water collection port and the bottom of the entire pool body is not greater than 1/3 of the total height of the denitrification area; the horizontal water collection branch 24, the collection The water main pipe 25 and the water collecting port are located at the same level, and their horizontal positions are between the top of the lower denitrification tank body and the height between 2/3 of the top of the denitrification tank body. The sewage from the upper nitrification area enters the lower denitrification area and continues to infiltrate vertically until it reaches the bottom of the denitrification area. Since the outlet of the water collection pipe network is located at the upper part of the denitrification tank, the water that is treated in the denitrification area to the bottom of the pool is in the pool body. The bottom enters the water collection port, but the water cannot be discharged immediately. The sewage accumulates upwards at the bottom, and the water can only be discharged from the water outlet after the water outlet level of the vertical water collection branch reaches the height of the water outlet. The role of the submerged water collection pipe network is to increase the residence time of sewage in the lower denitrification bed, create a facultative oxygen environment, and make the degradation of organic matter and total nitrogen more sufficient.
如图1所示,本实施例底部设有排污管,排污管的管身开有大量排污小孔,通过排污口14与外界相连,排污口前设有排污阀门15。本人工湿地污水处理系统正常运行时排污阀门关闭。当滤床基质层发生堵塞或需要清理时,将排污阀门打开,向上部布水管网中通滤池冲洗水,冲洗后的污水通过排污管排出滤池外,达到系统维护的目的。As shown in Figure 1, the bottom of the present embodiment is provided with a sewage pipe, and the pipe body of the sewage pipe has a large number of small sewage holes, which are connected to the outside world through the sewage outlet 14, and a sewage valve 15 is provided in front of the sewage outlet. When the constructed wetland sewage treatment system is in normal operation, the sewage valve is closed. When the matrix layer of the filter bed is clogged or needs to be cleaned, the sewage valve is opened to flush water from the filter pool to the upper water distribution pipe network, and the flushed sewage is discharged out of the filter pool through the sewage pipe to achieve the purpose of system maintenance.
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CN102418327A (en) * | 2011-10-10 | 2012-04-18 | 浙江大学 | Agricultural drain denitrifying phosphorus uptake simulation device |
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CN105668799A (en) * | 2016-01-07 | 2016-06-15 | 张军 | Facility for treating pollutants in rainwater runoff |
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