CN108275782B - Integrated three-dimensional wetland sewage treatment effluent TN control device and method - Google Patents

Integrated three-dimensional wetland sewage treatment effluent TN control device and method Download PDF

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CN108275782B
CN108275782B CN201810195478.2A CN201810195478A CN108275782B CN 108275782 B CN108275782 B CN 108275782B CN 201810195478 A CN201810195478 A CN 201810195478A CN 108275782 B CN108275782 B CN 108275782B
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CN108275782A (en
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许明
李明
白永刚
刘伟京
涂勇
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Jiangsu Provincial Academy of Environmental Science
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/32Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/006Regulation methods for biological treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/105Phosphorus compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/16Nitrogen compounds, e.g. ammonia
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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Abstract

The invention provides an integrated three-dimensional wetland sewage treatment effluent TN control device and method, wherein the treatment device comprises a sewage pretreatment area, a horizontal flow wetland sewage purification area, a vertical flow wetland sludge purification area and a vertical flow sewage purification area, wherein the horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area are arranged above the sewage pretreatment area in parallel; the vertical flow sewage purification area is arranged on the side edge and is separated by a concrete structure, the vertical flow sewage purification area is sequentially provided with a rubble layer, a natural vermiculite layer, a river sand layer and a biological filler ball layer from top to bottom, each layer is assembled in a modular manner, and the filling ratio of the biological filler balls in the biological filler ball layer is 20% -65%. The device can reduce the nitrogen content in the sewage and reduce the harm of harmful substances in rural domestic drainage to the surrounding water environment. The method has the advantages of small occupied area, stable treatment effect, convenient operation and management and no secondary pollution, and is suitable for various sewage treatments.

Description

一体化立体湿地污水处理出水TN控制装置及方法Integrated three-dimensional wetland sewage treatment effluent TN control device and method

技术领域Technical field

本发明属于污水处理技术领域,具体涉及一体化立体湿地污水处理出水TN控制装置及方法,可以降低生活污水中氮磷和有机物的含量,从而达到保护水环境的作用,尤其适用于我国农村地区。The invention belongs to the technical field of sewage treatment, and specifically relates to an integrated three-dimensional wetland sewage treatment effluent TN control device and method, which can reduce the content of nitrogen, phosphorus and organic matter in domestic sewage, thereby protecting the water environment, and is especially suitable for rural areas in my country.

背景技术Background technique

我国是农业大国,人口众多,人均水资源占有量约为2200m3,不足世界平均水平的1/4,水资源严重短缺。随着我国经济水平的不断提高,人民生活水平日益提高,由此带来的水环境恶化问题也受到了人们的重视。但人们仅仅关注城市的水环境问题,从而忽视了农村地区的水体污染状况,尤其是农村地区生活污水问题。China is a large agricultural country with a large population. The per capita water resources are about 2200m 3 , which is less than 1/4 of the world average. There is a serious shortage of water resources. With the continuous improvement of my country's economic level and the improvement of people's living standards, the resulting deterioration of the water environment has also attracted people's attention. However, people only focus on the water environment problems in cities, thus ignoring the water pollution conditions in rural areas, especially the domestic sewage problems in rural areas.

农村地区的居民在日常生活中排放出来的厨房污水、清洁污水、厕所洗浴污水等统称为农村生活污水。相比于城市居民的生活污水,由于农村居民的生活方式单一,人均用水量较低,所以农村地区的污水整体排放量远低于城市地区,这就使得我国农村地区的生活污水治理问题没有得到当地政府足够的重视。而且我国农村地区的供水设施过于简陋,自来水也没有全面普及,导致农村生活污水对周边环境造成了严重污染。与此同时,我国农村的村落居住区分布没有规律,这就使得农村地区的生活污水具有较强的分散性与随意性,很难与城市地区一样采用集中式的污水处理方式。而且农村地区的污水水质波动大,一般不含重金属和有毒有害等污染物,仅含有一定量的氮磷元素,同时我国农村生活污水具有较强的生化性,污水的污染浓度相对来说也较低。Kitchen sewage, cleaning sewage, toilet bathing sewage, etc. discharged by residents in rural areas in their daily lives are collectively referred to as rural domestic sewage. Compared with the domestic sewage of urban residents, due to the simple lifestyle of rural residents and low per capita water consumption, the overall sewage discharge in rural areas is much lower than that in urban areas. This makes the problem of domestic sewage treatment in rural areas of my country not addressed. The local government pays enough attention. Moreover, the water supply facilities in rural areas of our country are too crude, and tap water is not fully popularized, resulting in rural domestic sewage causing serious pollution to the surrounding environment. At the same time, the distribution of residential areas in rural areas of our country is irregular, which makes domestic sewage in rural areas highly dispersed and random, making it difficult to use centralized sewage treatment methods like urban areas. Moreover, the quality of sewage in rural areas fluctuates greatly. It generally does not contain heavy metals and toxic and harmful pollutants, and only contains a certain amount of nitrogen and phosphorus. At the same time, domestic sewage in rural areas in my country has strong biochemical properties, and the pollution concentration of sewage is relatively high. Low.

我国农村的面积占据了全国总面积的90%左右,农村生活污水的排放总量占全国生活污水排放总量的20%以上。在我国,农村居民没有环保意识,日常生活污水通常没有经过处理就直接排放到周边的河流或湖泊中,这样不仅造成了农村地区河流、湖泊等水体富营养化严重现象,也使得农村居民生活环境遭到了严重污染,十分不利于农村地区居民的健康生活。The area of rural areas in my country accounts for about 90% of the country's total area, and the total discharge of domestic sewage in rural areas accounts for more than 20% of the total discharge of domestic sewage in the country. In our country, rural residents have no awareness of environmental protection, and daily sewage is usually discharged directly into surrounding rivers or lakes without treatment. This not only causes serious eutrophication of rivers, lakes and other water bodies in rural areas, but also affects the living environment of rural residents. It has been seriously polluted, which is very detrimental to the healthy life of residents in rural areas.

目前,人工湿地已广泛运用于水处理方面,201410150093.6公开了一种复合型人工湿地处理系统,其特点是垂直流人工湿地处理池设置于系统的进水端,潜流人工湿地处理池设置于系统的出水端,该系统还包括一个配水箱,配水箱内设置导流墙,该配水箱位于系统的进水端,其出水口与垂直流人工湿地处理池的进水管连通垂直流人工湿地处理池中的填料由下至上依次为粗粒径填料层、中粒径填料层和细粒径填料层。这种处理系统并未考虑填料堵塞问题,更换填料时基建工程量大,施工较为复杂。201610873243.5公开了一种人工湿地高效净化系统,其特点是由3~5个处理单元组成,每个处理单元由过滤体、植物、有机层、过滤一层、过滤二层、生物层、过滤三层和防渗板构成,过滤体位于处理单元入水口一侧每个处理单元底部设置防渗层,两端设置防渗墙需净化的污水或低污染水通过进水管进入该人工湿地依次经过各个处理单元后被净化,最后通过出水管排入集水池中。这种方法在处理方式单一,在冬季气温较低时,人工湿地运行效率低,处理效果不够稳定。At present, constructed wetlands have been widely used in water treatment. A composite constructed wetland treatment system was disclosed in 201410150093.6. Its characteristic is that the vertical flow constructed wetland treatment tank is set at the water inlet end of the system, and the subsurface flow constructed wetland treatment tank is set at the system. At the water outlet end, the system also includes a water distribution tank with a diversion wall set up inside the water distribution tank. The water distribution tank is located at the water inlet end of the system, and its water outlet is connected to the water inlet pipe of the vertical flow constructed wetland treatment pool in the vertical flow constructed wetland treatment pool. The fillers are coarse-grained filler layer, medium-grained filler layer and fine-grained filler layer from bottom to top. This treatment system does not consider the problem of filler clogging. When replacing the filler, the amount of infrastructure work is large and the construction is complicated. 201610873243.5 discloses a high-efficiency purification system for artificial wetlands, which is characterized by being composed of 3 to 5 processing units. Each processing unit consists of a filter body, plants, organic layer, first filtration layer, second filtration layer, biological layer, and three filtration layers. It is composed of an anti-seepage plate and the filter body is located on the side of the water inlet of the treatment unit. An anti-seepage layer is installed at the bottom of each treatment unit. Anti-seepage walls are installed at both ends. The sewage or low-pollution water that needs to be purified enters the constructed wetland through the water inlet pipe and undergoes various treatments in turn. The unit is then purified and finally discharged into the collection tank through the outlet pipe. This method has a single treatment method. When the temperature is low in winter, the artificial wetland operation efficiency is low and the treatment effect is not stable enough.

而本发明占地面积小、处理效果稳定、操作管理方便、无二次污染,适用于各类污水处理。The invention occupies a small area, has stable treatment effect, is convenient for operation and management, has no secondary pollution, and is suitable for various types of sewage treatment.

发明内容Contents of the invention

本发明的目的是针对农村生活污水污染控制问题,提供了一体化立体湿地污水处理出水TN控制装置及方法,通过对农村家庭生活污水的处理,减少农村生活污水中氮磷和有机物等有害物质含量以避免造成河流、湖泊等水体的富营养化,保护农村周边的生态环境。The purpose of this invention is to address the problem of rural domestic sewage pollution control and provide an integrated three-dimensional wetland sewage treatment effluent TN control device and method to reduce the content of harmful substances such as nitrogen, phosphorus and organic matter in rural domestic sewage by treating rural household sewage. In order to avoid eutrophication of rivers, lakes and other water bodies, and protect the ecological environment around rural areas.

技术解决方案:为实现上述技术目的,本发明提出一种一体化立体湿地污水处理出水TN控制装置,所述处理装置包括污水预处理区、水平流湿地污水净化区、垂直流湿地污泥净化区和垂直流污水净化区,其中,所述水平流湿地污水净化区和垂直流湿地污泥净化区并列设置于所述污水预处理区的上方,所述水平流湿地污水净化区和垂直流湿地污泥净化区的下方设置有基质层,水平流湿地污水净化区和垂直流湿地污泥净化区的基质层与污水预处理区用混凝土结构隔开;水平流湿地污水净化区是对污水进行初步净化处理,垂直流湿地污泥净化区是对污水中的悬浮物、泥沙等杂质进行干化处理。所述垂直流污水净化区设置于所述水平流湿地污水净化区、垂直流湿地污泥净化区和污水预处理区的侧边并用混凝土结构隔开,所述垂直流污水净化区从上向下依次为碎石层、天然蛭石层、河沙层和生物填料球层,每层均采用模块式组装,根据不同的出水水质要求和不同的温度条件,所述生物填料球层中的生物填料球的填充比可设置为20%~65%。具体地,当气温>12℃时,选择生物填料球区不同的填充比可以达到不同的地表水环境质量标准。在45%的填充比下可以TN达到地表水环境质量Ⅴ类标准;在60%的填充比下TN可以达到地表水环境质量Ⅳ类标准。当气温<12℃时,人工湿地处理效率较低,需要加大填充比来达到所需的水质标准。在填充比小于60%时,TN均达不到地表水环境质量Ⅴ类标准;在60%的填充比下TN可以达到地表水环境质量Ⅴ类标准。最高填充比不得超过65%。Technical solution: In order to achieve the above technical objectives, the present invention proposes an integrated three-dimensional wetland sewage treatment effluent TN control device. The treatment device includes a sewage pretreatment area, a horizontal flow wetland sewage purification area, and a vertical flow wetland sludge purification area. and a vertical flow sewage purification area, wherein the horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area are arranged side by side above the sewage pretreatment area, and the horizontal flow wetland sewage purification area and the vertical flow wetland sewage purification area are arranged side by side above the sewage pretreatment area. There is a matrix layer below the mud purification area. The matrix layer of the horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area is separated from the sewage pretreatment area by a concrete structure; the horizontal flow wetland sewage purification area is for preliminary purification of sewage. For treatment, the vertical flow wetland sludge purification area is used to dry the suspended solids, sediment and other impurities in the sewage. The vertical flow sewage purification area is arranged on the side of the horizontal flow wetland sewage purification area, the vertical flow wetland sludge purification area and the sewage pretreatment area and is separated by a concrete structure. The vertical flow sewage purification area is arranged from top to bottom. There are gravel layer, natural vermiculite layer, river sand layer and biological filler ball layer in sequence. Each layer is assembled in a modular manner. According to different effluent water quality requirements and different temperature conditions, the biological filler in the biological filler ball layer The filling ratio of the ball can be set from 20% to 65%. Specifically, when the temperature is >12°C, different filling ratios of the biofiller ball area can be selected to achieve different surface water environmental quality standards. At a filling ratio of 45%, TN can reach the surface water environmental quality Class V standard; at a filling ratio of 60%, TN can reach the surface water environmental quality Class IV standard. When the temperature is <12°C, the treatment efficiency of constructed wetlands is low, and the filling ratio needs to be increased to achieve the required water quality standards. When the filling ratio is less than 60%, TN cannot meet the surface water environmental quality Class V standard; at a filling ratio of 60%, TN can meet the surface water environmental quality Class V standard. The maximum filling ratio must not exceed 65%.

其中,所述污水预处理区为一调节池,所述调节池内设置有污泥泵、污水泵和空气泵,其中,杂质沉淀在调节池底部由污泥泵抽到上部的垂直流湿地污泥净化区,在防止垂直流污水净化区堵塞的同时可以资源化。调节池中的污水由污水泵抽吸到水平流湿地污水净化区,再经过垂直流污水净化区进行处理;空气泵通过管道对河沙层和生物填料球层进行充氧曝气。Wherein, the sewage pretreatment area is a regulating tank, and a sludge pump, a sewage pump and an air pump are provided in the regulating tank. The impurities deposited at the bottom of the regulating tank are pumped to the upper vertical flow wetland sludge by the sludge pump. The purification area prevents clogging of the vertical flow sewage purification area and can utilize resources at the same time. The sewage in the regulating tank is pumped by the sewage pump to the horizontal flow wetland sewage purification area, and then processed through the vertical flow sewage purification area; the air pump oxygenates the river sand layer and the biological filler ball layer through the pipeline.

优选地,所述污水预处理区、水平流湿地污水净化区、垂直流湿地污泥净化区和垂直流污水净化区的体积比为(0.9~1.08):(0.48~0.675):(0.06~0.15):1。Preferably, the volume ratio of the sewage pretreatment area, horizontal flow wetland sewage purification area, vertical flow wetland sludge purification area and vertical flow sewage purification area is (0.9~1.08): (0.48~0.675): (0.06~0.15 ):1.

所述一体化立体湿地污水处理装置的尺寸设计为3m×4m×4m、4m×5m×4m、5m×6m×4m中的任意一种。The size of the integrated three-dimensional wetland sewage treatment device is designed to be any one of 3m×4m×4m, 4m×5m×4m, or 5m×6m×4m.

所述水平流湿地污水净化区与垂直流湿地污泥净化区之间用塑料隔板分隔开,水平流湿地污水净化区与垂直流湿地污泥净化区均种植有水生植物。The horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area are separated by plastic partitions, and aquatic plants are planted in both the horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area.

所述碎石层、天然蛭石层、河沙层和生物填料球层分别用钢丝滤网分隔开,碎石层、天然蛭石层、河沙层和生物填料球层的体积比为(0.4~1):(0.6~1):(0.8~1):(1.2~2)。The gravel layer, natural vermiculite layer, river sand layer and biological filler ball layer are separated by steel wire mesh respectively. The volume ratio of the gravel layer, natural vermiculite layer, river sand layer and biological filler ball layer is ( 0.4~1): (0.6~1): (0.8~1): (1.2~2).

所述河沙层和生物填料球层通过空气泵进行曝气充氧,曝气强度1.5~2.0m3/m2·h。The river sand layer and biological filler ball layer are aerated and oxygenated through an air pump, with an aeration intensity of 1.5 to 2.0 m 3 /m 2 ·h.

所述水平流湿地污水净化区和垂直流湿地污泥净化区的基质层为煤渣,基质深度设计为10~30cm,所述水生植物为茭白或水芹。优选地,水生植物的种植密度为每平方米16株以上。优选地,煤渣的粒径4~6mm、比表面积0.25~0.35m2/g。The substrate layer of the horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area is cinder, the depth of the substrate is designed to be 10-30 cm, and the aquatic plants are wild rice or cress. Preferably, the planting density of aquatic plants is more than 16 plants per square meter. Preferably, the coal slag has a particle size of 4 to 6 mm and a specific surface area of 0.25 to 0.35 m 2 /g.

所述碎石层的粒径为5~10mm;所述天然蛭石层的粒径为2~5mm,比表面积为400~600m2/g、孔容为0.2~0.4cm2/g;所述河沙层的粒径为2~4mm;所述生物填料球层为聚乙烯或聚丙烯塑料制成表面凸起的球形填料球,其表面积为800~2500m2/m3,密度为2~4kg/m3,直径为0.04~0.06m。本发明进一步提出了上述一体化立体湿地污水处理装置进行污水处理的方法,包括如下步骤:The particle size of the gravel layer is 5-10mm; the particle size of the natural vermiculite layer is 2-5mm, the specific surface area is 400-600m2 /g, and the pore volume is 0.2-0.4cm2 /g; The particle size of the river sand layer is 2 to 4 mm; the biological filler ball layer is a spherical filler ball with a raised surface made of polyethylene or polypropylene plastic, with a surface area of 800 to 2500 m 2 /m 3 and a density of 2 to 4 kg /m 3 , diameter is 0.04~0.06m. The present invention further proposes the above-mentioned integrated three-dimensional wetland sewage treatment device for sewage treatment method, which includes the following steps:

首先污水先全部排进调节池,在调节池内污水进行调节初沉,杂质沉淀在底部由污泥泵抽到上部的垂直流湿地污泥净化区;调节池中的污水由污水泵抽吸到水平流湿地污水净化区,依次经过垂直分段净化区中的碎石层、天然蛭石层、河沙层和生物填料层得到净化处理;当在气温<12℃时,大部分植物枯死,微生物活性降低,人工湿地处理效率较低,可加大生物填料球层的填充比来提高其净化效果。First, all the sewage is discharged into the regulating tank. The sewage is adjusted and initially settled in the regulating tank. The impurities settle at the bottom and are pumped to the upper vertical flow wetland sludge purification area by the sludge pump. The sewage in the regulating tank is pumped to the horizontal by the sewage pump. The wetland sewage purification area is purified through the gravel layer, natural vermiculite layer, river sand layer and biological filler layer in the vertical segmented purification area in sequence; when the temperature is <12°C, most plants die and microbial activity Reduced, the treatment efficiency of constructed wetlands is low, and the filling ratio of the biological filler ball layer can be increased to improve its purification effect.

本发明的一体化湿地污水处理装置设置在农村家庭庭院内,生活污水先排进调节池,再由泵分别抽到微型人工湿地2个分区,污水经过水平流湿地污水净化区,再依次经过垂直流污水净化区中的碎石、天然蛭石、河沙和生物净化球得到净化处理。当在冬季气温较低时,人工湿地处理效率较低,可将污水直接抽到垂直流污水净化区进行净化处理。在净化装置运行一段时间后垂直流污水净化区的填料可方便地通过一侧的可开式的门进行更换和处理。从而达到装置长期有效处理污水的效果。The integrated wetland sewage treatment device of the present invention is installed in a rural family courtyard. Domestic sewage is first discharged into the regulating tank, and then pumped to the two subdivisions of the micro-constructed wetland by pumps. The sewage passes through the horizontal flow wetland sewage purification area, and then passes through the vertical flow in turn. The gravel, natural vermiculite, river sand and biological purification balls in the sewage purification area are purified. When the temperature is low in winter, the treatment efficiency of constructed wetlands is low, and sewage can be pumped directly to the vertical flow sewage purification area for purification treatment. After the purification device has been running for a period of time, the filler in the vertical flow sewage purification area can be easily replaced and processed through the openable door on one side. In this way, the device can effectively treat sewage for a long time.

本发明的优点:Advantages of the invention:

(1)本发明采用紧凑一体化立体式结构,与传统的人工湿地相比占地面积减少40%以上,投资成本减少20%以上,具有占地面积小、投资省、运行管理以及维护方便的优点;(1) This invention adopts a compact integrated three-dimensional structure, which reduces the floor area by more than 40% and the investment cost by more than 20% compared with traditional artificial wetlands. It has the advantages of small floor space, low investment, convenient operation management and maintenance. advantage;

(2)本发明一体化立体人工湿地装置中垂直流污水净化区滤料可更换,且采用了煤渣,与传统人工湿地相比,降低运行成本30%以上,较适用于各种污水;(2) The filter material in the vertical flow sewage purification area of the integrated three-dimensional artificial wetland device of the present invention is replaceable and uses cinder. Compared with traditional artificial wetlands, the operating cost is reduced by more than 30%, and it is more suitable for various kinds of sewage;

(3)本发明一体化立体人工湿地装置采用不同分区的逐级处理,SS去除率90%以上,氮、磷去除率80%以上,污泥也得到100%削减,不产生二次污染。合理空间布局延缓湿地堵塞,提高滤料挂膜效果和微生物降解作用。当气温<12℃时,可通过调控填充比,强化处理效果,提高出水TN稳定性。(3) The integrated three-dimensional artificial wetland device of the present invention adopts step-by-step treatment in different zones. The SS removal rate is more than 90%, the nitrogen and phosphorus removal rate is more than 80%, and the sludge is also reduced by 100%, without causing secondary pollution. Reasonable spatial layout delays wetland clogging and improves the film-hanging effect and microbial degradation of filter materials. When the temperature is <12°C, the filling ratio can be adjusted to enhance the treatment effect and improve the stability of effluent TN.

附图说明Description of drawings

图1一体化立体湿地污水处理装置框架剖视图。Figure 1 is a cross-sectional view of the frame of the integrated three-dimensional wetland sewage treatment device.

图2一体化立体湿地污水处理装置俯视图。Figure 2 Top view of the integrated three-dimensional wetland sewage treatment device.

其中,1是混凝土框架,2是塑料隔板,3是细密度钢丝滤网,4是水生植物,5是污泥泵,6是清水泵,7是空气泵,8是微型人工湿地基质。Among them, 1 is a concrete frame, 2 is a plastic partition, 3 is a fine-density steel wire filter, 4 is aquatic plants, 5 is a sludge pump, 6 is a clean water pump, 7 is an air pump, and 8 is a micro-constructed wetland matrix.

具体实施方式Detailed ways

实施例1:下面根据附图所示对本发明进行进一步详细描述:Embodiment 1: The present invention will be described in further detail below according to the accompanying drawings:

对照图1,用混凝土1、塑料隔板2、钢丝滤网3构建成一体化湿地污水处理装置,装置尺寸为3m×4m×4m。装置设计为4个分区,一是污水预处理区,二是水平流湿地污水净化区,三是垂直流湿地污泥净化区,四是垂直流污水净化区,4个分区的体积比设置为1:0.6:0.15:1。水平流湿地污水净化区与垂直流湿地污泥净化区之间用塑料隔板分隔开,两个湿地都种植有水生植物4,基质8设计均为对氮磷吸附效果明显的煤渣(粒径4~6mm、比表面积0.25~0.35m2/g),基质深度设计为25cm,水生植物4选择茭白、水芹等经济植物,种植密度为每平方米18株。利用水生植物根部吸收氮,达到初步去除效果。垂直流污水净化区用细密度(孔径值0.8±0.02mm)的钢丝滤网(3)分隔成4层,从上向下依次是碎石层、天然蛭石层、河沙层和生物填料球层,4个填料层的体积比为0.5:0.7:0.9:1.4,每层填料均采用模块式组装,方便定期更换装置内填料。生活污水先排进调节池,再由泵分别抽到微型人工湿地2个分区,污水经过水平流湿地污水净化区,再依次经过垂直流污水净化区中的碎石、天然蛭石、河沙和生物净化球得到净化处理。Referring to Figure 1, an integrated wetland sewage treatment device is constructed using concrete 1, plastic partitions 2, and steel wire filters 3. The device size is 3m×4m×4m. The device is designed into four partitions, one is the sewage pretreatment area, the second is the horizontal flow wetland sewage purification area, the third is the vertical flow wetland sludge purification area, and the fourth is the vertical flow sewage purification area. The volume ratio of the four partitions is set to 1 :0.6:0.15:1. The horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area are separated by plastic partitions. Both wetlands are planted with aquatic plants 4, and the substrate 8 is designed to be cinder (particle size) with obvious nitrogen and phosphorus adsorption effect. 4 ~ 6mm, specific surface area 0.25 ~ 0.35m 2 /g), the substrate depth is designed to be 25cm, aquatic plants 4 choose economic plants such as wild rice and cress, and the planting density is 18 plants per square meter. Use the roots of aquatic plants to absorb nitrogen to achieve the initial removal effect. The vertical flow sewage purification area is divided into 4 layers with a fine-density (pore diameter 0.8±0.02mm) steel wire filter (3). From top to bottom, there are gravel layer, natural vermiculite layer, river sand layer and biological filler balls. The volume ratio of the four packing layers is 0.5:0.7:0.9:1.4. Each layer of packing is modularly assembled to facilitate regular replacement of the packing in the device. Domestic sewage is first discharged into the regulating tank, and then pumped to the two sub-regions of the micro-constructed wetland. The sewage passes through the horizontal flow wetland sewage purification area, and then passes through the gravel, natural vermiculite, river sand and water in the vertical flow sewage purification area. The biological purification ball is purified.

一体化立体湿地污水处理装置进水水质特征值为TN:10~25mg/L,NH4 +-N:11~20mg/L,NO3 --N:0.5~3mg/L,SS:100~200mg/L。通过不同分区的逐级处理,最终氮去除率80%以上,污泥也得到100%削减,SS去除率90%以上。而且本发明采用紧凑一体化立体式结构,与传统的人工湿地相比占地面积减少40%以上,投资成本减少20%以上。The characteristic values of the inlet water quality of the integrated three-dimensional wetland sewage treatment device are TN: 10~25mg/L, NH 4 + -N: 11~20mg/L, NO 3 - -N: 0.5~3mg/L, SS: 100~200mg /L. Through step-by-step treatment in different zones, the final nitrogen removal rate is more than 80%, the sludge is also reduced by 100%, and the SS removal rate is more than 90%. Moreover, the present invention adopts a compact integrated three-dimensional structure, which reduces the floor space by more than 40% and the investment cost by more than 20% compared with traditional artificial wetlands.

图1中箭头表示水流方向,生活污水先排进调节池,再由泵分别抽到微型人工湿地2个分区,污水流经清水湿地处理区,再依次经过垂直分段净化区中的碎石层、天然蛭石层、河沙层和生物填料球层得到净化处理。在气温>12℃时,选择生物填料球区不同的填充比可以达到不同地表水环境质量标准。当出水水质要求较高时,在45%的填充比下可以TN达到地表水环境质量Ⅴ类标准;在60%的填充比下TN可以达到地表水环境质量Ⅳ类标准。(地表水环境质量标准GB3838-2002,地表水环境质量Ⅴ类标准:TN≤2.0mg/L;地表水环境质量Ⅳ类标准:TN≤1.5mg/L)具体实施方案效果如表1所示。The arrow in Figure 1 indicates the direction of water flow. Domestic sewage is first discharged into the regulating tank, and then pumped to the two sub-regions of the micro-constructed wetland by pumps. The sewage flows through the clear water wetland treatment area, and then passes through the gravel layer in the vertical segmented purification area. , natural vermiculite layer, river sand layer and biological filler ball layer are purified. When the temperature is >12°C, choosing different filling ratios in the biofiller ball area can achieve different surface water environmental quality standards. When the effluent quality requirements are high, TN can reach the surface water environmental quality Class V standard at a filling ratio of 45%; TN can reach the surface water environmental quality Class IV standard at a filling ratio of 60%. (Surface water environmental quality standard GB3838-2002, surface water environmental quality Class V standard: TN ≤ 2.0 mg/L; surface water environmental quality Class IV standard: TN ≤ 1.5 mg/L) The specific implementation plan effects are shown in Table 1.

表1在生物填料球层不同填充比下污水通过各段净化区的处理效果:Table 1 The treatment effect of sewage passing through each purification zone under different filling ratios of the biological filler ball layer:

实施例2:本实施例与实施1不同的是:当气温<12℃时,人工湿地处理效率较低,需要加大填充比来达到所需的水质标准。在填充比小于60%时,TN均达不到地表水环境质量Ⅴ类标准;在60%的填充比下TN可以达到地表水环境质量Ⅴ类标准。具体实施方案效果如表1所示。Example 2: The difference between this example and Example 1 is that when the temperature is <12°C, the artificial wetland treatment efficiency is low, and the filling ratio needs to be increased to meet the required water quality standards. When the filling ratio is less than 60%, TN cannot meet the surface water environmental quality Class V standard; at a filling ratio of 60%, TN can meet the surface water environmental quality Class V standard. The specific implementation effects are shown in Table 1.

Claims (5)

1. The integrated three-dimensional wetland sewage treatment effluent TN control device is characterized by comprising a sewage pretreatment area, a horizontal flow wetland sewage purification area, a vertical flow wetland sludge purification area and a vertical flow sewage purification area, wherein the horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area are arranged above the sewage pretreatment area in parallel, a matrix layer is arranged below the horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area, and the matrix layer of the horizontal flow wetland sewage purification area and the vertical flow wetland sludge purification area is separated from the sewage pretreatment area by a concrete structure; the vertical flow sewage purification zone is arranged at the side edges of the horizontal flow wetland sewage purification zone, the vertical flow wetland sludge purification zone and the sewage pretreatment zone and is separated by a concrete structure, the vertical flow sewage purification zone is sequentially provided with a rubble layer, a natural vermiculite layer, a river sand layer and a biological filler ball layer from top to bottom, each layer is assembled by adopting a module, the filling ratio of the biological filler balls in the biological filler ball layer is 20% -65%, aquatic plants are planted in the horizontal flow wetland sewage purification zone and the vertical flow wetland sludge purification zone, the substrate layers of the horizontal flow wetland sewage purification zone and the vertical flow wetland sludge purification zone are coal cinder, the substrate depth is designed to be 10-30 cm, the aquatic plant is cane shoots or cress, the sewage pretreatment area is an adjusting tank, a sludge pump, a sewage pump and an air pump are arranged in the adjusting tank, the air pump is used for oxygenating and aerating a river sand layer and a biological filling ball layer through a pipeline, the river sand layer and the biological filling ball layer are aerated and oxygenated through the air pump, the aeration strength is 1.5-2.0 m < 3 >/m < 2 >. H, the size of the integrated three-dimensional wetland sewage treatment effluent TN control device is designed to be any one of 3m < 4 >, 4m < 5 > m < 4 > and 5m < 6 > m < 4 > m, and the volume ratio of the sewage pretreatment area, the horizontal flow wetland sewage purification area, the vertical flow wetland sludge purification area and the vertical flow sewage purification area is 0.9-1.08): (0.48-0.675): (0.06-0.15): 1, the volume ratio of the crushed stone layer, the natural vermiculite layer, the river sand layer and the biological filling ball layer is (0.4-1): (0.6-1): (0.8-1): (1.2-2), wherein the particle size of the crushed stone layer is 5-10 mm; the particle size of the natural vermiculite layer is 2-5 mm, the specific surface area is 400-600 m < 2 >/g, and the pore volume is 0.2-0.4 cm < 2 >/g; the particle size of the river sand layer is 2-4 mm; the bio-filler ball layer is a spherical filler ball with a raised surface, which is made of polyethylene or polypropylene plastic, the surface area of the bio-filler ball layer is 800-2500 m < 2 >/m < 3 >, the density of the bio-filler ball layer is 2-4 kg/m < 3 >, and the diameter of the bio-filler ball layer is 0.04-0.06 m.
2. The integrated stereoscopic wetland sewage treatment effluent TN control device according to claim 1, wherein the impurities are precipitated at the bottom of the regulating tank and pumped by the sludge pump to the upper vertical flow wetland sludge purification zone; sewage in the regulating tank is pumped into a horizontal flow wetland sewage purification area by a sewage pump and then is treated by a vertical flow sewage purification area.
3. The integrated stereoscopic wetland sewage treatment effluent TN control device according to claim 1, wherein the horizontal flow wetland sewage purification zone and the vertical flow wetland sludge purification zone are separated by a plastic partition.
4. The integrated three-dimensional wetland sewage treatment effluent TN control device of claim 1, wherein the crushed stone layer, the natural vermiculite layer, the river sand layer and the biological filler ball layer are separated by a steel wire filter screen, respectively.
5. A method for sewage treatment by using the integrated three-dimensional wetland sewage treatment effluent TN control device as claimed in claim 1, comprising the steps of:
firstly, sewage is completely discharged into an adjusting tank, sewage in the adjusting tank is adjusted and primarily settled, and impurities are settled at the bottom and pumped into a vertical flow wetland sludge purification area at the upper part by a sludge pump; sewage in the regulating tank is pumped into a sewage purification area of the horizontal flow wetland by a sewage pump, and sequentially passes through a crushed stone layer, a natural vermiculite layer, a river sand layer and a biological filler layer in the vertical section purification area to be purified; when the temperature is less than 12 ℃, the filling ratio of the bio-filler ball layer is increased to improve the purifying effect.
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