CN212025107U - Artificial wetland system of high-efficient undercurrent - Google Patents

Artificial wetland system of high-efficient undercurrent Download PDF

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CN212025107U
CN212025107U CN202020127767.1U CN202020127767U CN212025107U CN 212025107 U CN212025107 U CN 212025107U CN 202020127767 U CN202020127767 U CN 202020127767U CN 212025107 U CN212025107 U CN 212025107U
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wetland
layer
water
tank
sewage
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秦红科
佟镇
李好波
于田田
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Lingnan Water Group Co ltd
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Abstract

The utility model provides an artificial wetland system of high-efficiency undercurrent, which comprises a multifunctional combined pool and a wetland unit, wherein sewage firstly intercepts suspended matters and floating impurities in the multifunctional combined pool and carries out hydrolytic acidification on a water body; and then filtering and biodegrading in the wetland unit, uniformly distributing water by adopting a drip irrigation system, dredging by adopting a membrane guide system, and purifying the water body.The utility model discloses an artificial wetland system can be adapted to villages and small towns domestic sewage discharge's characteristics, carries out sewage purification, is applicable to the treatment scale and is not higher than 500m3A/d efficient undercurrent artificial wetland treatment system for treating sewage in villages and towns.

Description

一种高效潜流的人工湿地系统An Efficient Underwater Constructed Wetland System

技术领域technical field

本实用新型涉及高效潜流人工湿地的技术领域,具体地说是一种用于村镇污水处理的高效潜流人工湿地系统。The utility model relates to the technical field of high-efficiency subsurface flow artificial wetlands, in particular to a high-efficiency subsurface flow artificial wetland system used for village sewage treatment.

背景技术Background technique

村镇生活污水具有排放源分散、人民环保意识薄弱、设施和经济条件不足、区域差异大、村镇污水时变化大、生化工艺运行困难等特点,对于村镇污水的处理缺乏深入、系统的研究。因此,研发和推广适应我国村镇特点和经济力量的村镇污水处理系统,具有十分重要的理论和应用意义。Domestic sewage in villages and towns has the characteristics of scattered discharge sources, weak people's awareness of environmental protection, insufficient facilities and economic conditions, large regional differences, large changes in villages and towns sewage, and difficult operation of biochemical processes. Therefore, it is of great theoretical and practical significance to develop and popularize the village sewage treatment system that adapts to the characteristics and economic strength of the villages and towns in my country.

人工湿地是20世纪70年代末发展起来的一种污水处理技术,其特点是:出水水质好,具有较强的氮磷处理能力,运行维护方便,管理简单,投资及运行费用低。据有关资料显示,人工湿地投资和运行费用仅占传统二级生化处理技术的10%~50%。比较适合于资金少、能源短缺和技术人才缺乏的中小城镇和乡村、城郊结合处未完善污水管网的小型社区等。Constructed wetland is a sewage treatment technology developed in the late 1970s. Its characteristics are: good effluent quality, strong nitrogen and phosphorus treatment capacity, convenient operation and maintenance, simple management, and low investment and operating costs. According to relevant data, the investment and operating costs of constructed wetlands only account for 10% to 50% of the traditional secondary biochemical treatment technology. It is more suitable for small and medium-sized towns and villages with less capital, energy shortage and lack of technical personnel, and small communities with uncompleted sewage pipe networks at the junction of urban and suburban areas.

人工湿地处理系统是将污水有控制地投放到湿地上,使污水沿一定方向流动,通过土壤、人工介质、植物、微生物的物理、化学、生物共同作用,实现污水净化的一种系统,处理后的水体在终端流出。传统意义上的人工湿地一般是作为生化系统后的深度处理来运行,本次实用新型人工湿地可以独立作为一个高效治理水污染的技术系统,而非仅作为深处理应用技术,使人工湿地技术在我国村镇污水中的应用走向成熟。Constructed wetland treatment system is a system in which sewage is put into wetlands in a controlled manner, so that sewage flows in a certain direction, and through the physical, chemical and biological interaction of soil, artificial media, plants and microorganisms, to achieve sewage purification. The body of water flows out at the terminal. Constructed wetlands in the traditional sense are generally operated as advanced treatment after biochemical systems. The constructed wetland of this utility model can be independently used as a technical system for efficient water pollution control, not just as advanced treatment application technology. The application of sewage in villages and towns in my country is maturing.

人工湿地系统的水流状态是维持系统正常运行、使系统充分发挥净化效果的重要因素,但在发生堵塞后,基质的渗透系数会急剧下降,过水能力也随之降低,大量引入湿地系统的污水直接雍积在湿地表面,长期积水引发恶臭、导致蚊蝇滋生,恶化运行环境;雍水还阻隔氧气向基质层内扩散,进而降低污染物(尤其是有机物和氨氮)的去除效果,使出水指标达不到设计标准,同时缩短了人工湿地的运行寿命。The water flow state of the constructed wetland system is an important factor to maintain the normal operation of the system and enable the system to give full play to the purification effect. However, after the blockage occurs, the permeability coefficient of the matrix will drop sharply, and the water passing capacity will also decrease. A large amount of sewage is introduced into the wetland system. It is directly accumulated on the wetland surface, and the long-term accumulation of water will cause foul odor, lead to the breeding of mosquitoes and flies, and deteriorate the operating environment; Yongshui also blocks the diffusion of oxygen into the matrix layer, thereby reducing the removal effect of pollutants (especially organic matter and ammonia nitrogen), making the effluent water The indicators do not meet the design standards, and at the same time, the operating life of the constructed wetland is shortened.

人工湿地普遍占地面积大、水力负荷低、冬季运行效果差,本次实用新型所开发的专利技术主要是解决人工湿地占地面积大、调节能力差、易堵塞、冬季湿地的运行效果差等问题。Constructed wetlands generally cover a large area, with low hydraulic load and poor operation in winter. The patented technology developed in this utility model mainly solves the problem of large area of constructed wetlands, poor adjustment ability, easy blockage, and poor operation effect of wetlands in winter. question.

针对以上困难,我们在对传统人工湿地的深入研究基础上,根据污水成分组成的特点,开发出适用于处理规模不高于500m3/d的村镇污水处理的高效潜流人工湿地处理系统。In response to the above difficulties, based on in-depth research on traditional constructed wetlands, we have developed a high-efficiency subsurface-flow constructed wetland treatment system suitable for the treatment of villages and towns with a scale of not more than 500m 3 /d according to the characteristics of the composition of sewage.

实用新型内容Utility model content

本实用新型的目的是为了解决上述问题,提供一种能够适应村镇居民污水处理特点的高效潜流人工湿地系统。The purpose of the present utility model is to solve the above problems, and provide a high-efficiency subsurface-flow constructed wetland system that can adapt to the characteristics of sewage treatment of villagers and towns.

为了实现上述目的,本实用新型采用的技术方案如下:In order to achieve the above purpose, the technical scheme adopted by the present utility model is as follows:

一种高效潜流的人工湿地系统,包括多功能组合池和湿地单元,污水先在所述多功能组合池中截留悬浮物和漂浮物杂质,对水体进行水解酸化;再在湿地单元中过滤、生物降解,采用滴灌系统进行均匀布水,导膜系统排淤,进行水体净化。A high-efficiency subsurface constructed wetland system includes a multifunctional combined pool and a wetland unit. The sewage first intercepts suspended solids and floating impurities in the multifunctional combined pool, and hydrolyzes and acidifies the water body; Degradation, the drip irrigation system is used to distribute water evenly, and the membrane guide system is used to discharge silt and purify the water body.

进一步,所述多功能组合池分为上下两层结构,上层结构为两格的格栅池,一格为机械格栅,一格为人工格栅,截留悬浮物和漂浮物杂质;下层结构为水解酸化调节池,上层格栅池出水通过池内折流板重力自流到水解酸化池底部,通过池内的酸性细菌进行水解,在多功能组合池内2/3处设有提升泵抽取污水。Further, the multifunctional combined pool is divided into upper and lower two-layer structures, the upper layer structure is a grid pool with two grids, one grid is a mechanical grid, and the other grid is an artificial grid, which retains suspended matter and floating matter impurities; the lower layer structure is In the hydrolysis and acidification adjustment tank, the effluent from the upper grille tank flows to the bottom of the hydrolysis and acidification tank by gravity through the baffle plate in the tank, and is hydrolyzed by the acidic bacteria in the tank. There is a lift pump in 2/3 of the multi-functional combined tank to extract sewage.

进一步,在所述水解酸化调节池内设置立体弹性组合填料,对搅动的废水进行水力切割,填料材质为聚丙烯和/或聚乙烯。Further, a three-dimensional elastic composite filler is arranged in the hydrolysis and acidification adjustment tank, and the agitated waste water is hydraulically cut, and the filler material is polypropylene and/or polyethylene.

进一步,在所述多功能组合池的底部设有多个漏斗状收集器,将收集的污泥定期排出。Further, a plurality of funnel-shaped collectors are arranged at the bottom of the multifunctional combined tank to discharge the collected sludge regularly.

进一步,在多功能组合池和湿地单元之间设有吸力自清洗网式过滤器,包括过滤器本体、粗滤网、细滤室、冲洗阀和冲洗控制器,经过吸力自清洗网式过滤器的污水,先通过粗滤网、细滤网两级过滤,截留大于100μm的污染物在滤网上,出水进入湿地单元,当滤网上内外压差大于预设值时,控制器打开冲洗阀,通利用压差的变化吸入反冲洗水冲洗滤网污物,通过冲洗阀排出。Further, a suction self-cleaning mesh filter is arranged between the multi-functional combined pool and the wetland unit, including the filter body, the coarse filter, the fine filter chamber, the flush valve and the flush controller. After the suction self-cleaning mesh filter The sewage is first filtered through the coarse filter screen and the fine filter screen, and the pollutants larger than 100 μm are retained on the filter screen, and the effluent enters the wetland unit. The backwash water is sucked in to wash the filter screen dirt by the change of pressure difference, and it is discharged through the flush valve.

进一步,所述湿地单元由下至上依次铺设聚乙烯土工布层、第一粗砂层、第一砾石层、钢丝网层、第二砾石层、第二粗砂层、种植土层。Further, a polyethylene geotextile layer, a first coarse sand layer, a first gravel layer, a steel mesh layer, a second gravel layer, a second coarse sand layer, and a planting soil layer are sequentially laid in the wetland unit from bottom to top.

进一步,所述聚乙烯土工布层以厚度为0.5mm的聚乙烯塑料膜铺设,在两边衬垫密度为500g/m2的土工布;所述第一粗砂层的厚度为100mm,所述第一砾石层的厚度为500mm,砾石粒径为φ100~150mm;所述钢丝网层的孔径为10*10mm,钢丝直径为0.6mm;所述第二砾石层厚底为200mm,砾石粒径为φ10-15mm;所述第二粗砂层的厚度为200mm;所述种植土层的厚度为200mm,种植土层种植水生植物。Further, the polyethylene geotextile layer is laid with a polyethylene plastic film with a thickness of 0.5mm, and a geotextile with a density of 500g/m2 is lined on both sides; the thickness of the first coarse sand layer is 100mm, and the first The thickness of the gravel layer is 500mm, and the particle size of the gravel is φ100-150mm; the diameter of the wire mesh layer is 10*10mm, and the diameter of the steel wire is 0.6mm; the thickness of the second gravel layer is 200mm, and the particle size of the gravel is φ10-15mm ; The thickness of the second coarse sand layer is 200mm; the thickness of the planting soil layer is 200mm, and the planting soil layer is used for planting aquatic plants.

进一步,所述人工湿地系统由若干个湿地单元顺序连接。Further, the constructed wetland system is sequentially connected by several wetland units.

进一步,所述湿地单元的滴灌系统铺设在所述第二砾石层,由一支布水主管进入湿地单元,由两根布水支管平行铺设在湿地单元内,布水支管采用贴片式滴灌带,所述贴片式滴灌带包括依次连通的贴片、紊流通道、过滤窗。Further, the drip irrigation system of the wetland unit is laid on the second gravel layer, a water distribution main pipe enters the wetland unit, and two water distribution branch pipes are laid in parallel in the wetland unit, and the water distribution branch pipes use a patch type drip irrigation belt. The patch-type drip irrigation tape includes patches, turbulent channels, and filter windows that are connected in sequence.

进一步,所述湿地单元的导膜系统为丰字集水管铺设在所述第一砾石层,集水孔的孔径采用为φ20mm,并列排列的集水管的间距150mm。Further, the guide membrane system of the wetland unit is that the Fengzi water collection pipes are laid on the first gravel layer, the diameter of the water collection holes is φ20mm, and the spacing between the parallel water collection pipes is 150mm.

进一步,所述人工湿地系统用于村镇生活污水的净化处理。Further, the constructed wetland system is used for the purification treatment of domestic sewage in villages and towns.

一种污水处理方法,将生活污水流入所述多功能组合池,机械格栅或人工格栅根据清捞需要间隔工作,提升泵以3小时为间隔将组合池中的污水抽净一次;A sewage treatment method, the domestic sewage is flowed into the multifunctional combined pool, the mechanical grille or the artificial grille works at intervals according to the needs of scouring, and the lifting pump cleans the sewage in the combined pool once every 3 hours;

湿地单元的使用数量根据液位高度的需求选定,夏季节选择高液位运行,液位到达种植土层上的植物,春秋季节选择中液位运行,液位到达第二粗砂层,冬季节选择低液位运行,液位到达第二砾石层;The number of wetland units used is selected according to the requirements of the liquid level height. In summer, high liquid level operation is selected, and the liquid level reaches the plants on the planting soil layer. In spring and autumn, medium liquid level operation is selected, and the liquid level reaches the second coarse sand layer. In winter Select low liquid level operation in section, and the liquid level reaches the second gravel layer;

在湿地单元运行初期,开启集水管出水阀门,污水各层吸附的积累物通过集水管排出;In the initial stage of operation of the wetland unit, open the outlet valve of the water collection pipe, and the accumulated materials adsorbed by each layer of sewage are discharged through the water collection pipe;

在湿地单元运行后期,关闭集水管出水阀门,污水在湿地单元中水力停留时间为24h,各层老化的生物膜脱落进入水中,瞬间开启集水管出水阀门,老化的生物膜脱落进入导膜系统,排出人工湿地系统。In the late stage of operation of the wetland unit, close the outlet valve of the water collection pipe, the hydraulic retention time of sewage in the wetland unit is 24 hours, the aging biofilm of each layer falls off into the water, and the outlet valve of the water collection pipe is opened instantly, and the aging biofilm falls off and enters the guiding membrane system. Discharge from the constructed wetland system.

采用上述技术方案,本实用新型具有如下有益效果:Adopting the above-mentioned technical scheme, the utility model has the following beneficial effects:

第一、本实用新型的人工湿地系统能够适应于村镇生活污水排放的特点,进行污水净化处理,适用于处理规模不高于500m3/d的村镇污水处理的高效潜流人工湿地处理系统。First, the constructed wetland system of the present utility model can adapt to the characteristics of domestic sewage discharge in villages and towns for sewage purification treatment, and is suitable for a high-efficiency subsurface flow constructed wetland treatment system for village sewage treatment with a treatment scale of not more than 500 m 3 /d.

第二、本实用新型的多功能组合池:能够调节水质水量的瞬时变化;提高废水可生化性,将大分子有机物转化为小分子;池体的计设灵活性较高,可根据来水水质需求组合,改造成其他功能池。Second, the multifunctional combined pool of the present utility model can adjust the instantaneous change of water quality and quantity; improve the biodegradability of wastewater, and convert macromolecular organic matter into small molecules; the design flexibility of the pool body is high, and the water quality can be adjusted according to the quality of the incoming water. Requirement combination, transformed into other functional pools.

第三、本实用新型的湿地单元能够灵活调节湿地单元的使用数量,并且湿地单元占地面积小,水力负荷高,能够适应冬季越冬的环境问题,有效防止湿地堵塞情况,保持湿地水通畅,净化能力强。Third, the wetland unit of the present invention can flexibly adjust the number of wetland units used, and the wetland unit occupies a small area and has a high hydraulic load, which can adapt to the environmental problems of overwintering in winter, effectively prevent the blockage of the wetland, keep the wetland water unobstructed, and purify the wetland. strong ability.

第四、本专利采用滴灌系统进行均匀布水,提高湿地的处理效率,保证湿地投放的污染负荷一致,防止短路流和死水区的发生,减缓湿地的堵塞。导膜系统能够定期将湿地运行过程中产生的沉淀物、截留物以及剥落的生物膜排出湿地单元,保证湿地中水流畅通。Fourth, this patent uses a drip irrigation system to distribute water evenly, improve the efficiency of wetland treatment, ensure that the pollution load placed on the wetland is consistent, prevent the occurrence of short-circuit flow and dead water area, and slow down the blockage of the wetland. The guiding membrane system can regularly discharge the sediment, retentate and peeling biofilm produced during the operation of the wetland to the wetland unit to ensure the smooth flow of water in the wetland.

附图说明Description of drawings

图1是本实用新型的人工湿地系统的结构示意图;Fig. 1 is the structural representation of the artificial wetland system of the present invention;

图2是本实用新型的湿地单元的滴灌系统和导膜系统的结构示意图;2 is a schematic structural diagram of the drip irrigation system and the film guiding system of the wetland unit of the present invention;

图3是本实用新型的湿地单元的铺设结构示意图;3 is a schematic diagram of the laying structure of the wetland unit of the present invention;

图4是本实用新型的滴灌带的结构示意图。4 is a schematic structural diagram of the drip irrigation belt of the present invention.

其中,1、多功能组合池,2、吸力自清洗网式过滤器,3、湿地单元,4、格栅池,5、水解酸化调节池,6、滴灌系统,61、贴片,62、紊流通道,63、过滤窗,7、导膜系统Among them, 1. Multifunctional combined pool, 2. Suction self-cleaning mesh filter, 3. Wetland unit, 4. Grille pool, 5. Hydrolysis and acidification adjustment pool, 6. Drip irrigation system, 61. Patch, 62. Turbulence Flow channel, 63, filter window, 7, film guide system

为了使本实用新型的目的、技术方案及优点更加清楚明白,下面结合附图及实施例,对本实用新型进行进一步详细说明。应当理解,此处所描述的结构图及具体实施例仅用以解释本实用新型,并不用于限定本实用新型。In order to make the purpose, technical solutions and advantages of the present utility model more clearly understood, the present utility model will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the structural diagrams and specific embodiments described herein are only used to explain the present invention, and are not intended to limit the present invention.

具体实施方式Detailed ways

实施例1Example 1

如图1所示,一种高效潜流的人工湿地系统,包括多功能组合池1和湿地单元3,污水先在多功能组合池中截留悬浮物和漂浮物杂质,对水体进行水解酸化;再在湿地单元中过滤、生物降解,采用滴灌系统6进行均匀布水,导膜系统7排淤,进行水体净化。As shown in Figure 1, a high-efficiency subsurface constructed wetland system includes a multi-functional combined pool 1 and a wetland unit 3. The sewage first intercepts suspended solids and floating impurities in the multi-functional combined pool, and hydrolyzes and acidifies the water body; The wetland unit is filtered and biodegraded, the drip irrigation system 6 is used to distribute water evenly, and the membrane guide system 7 is used to discharge silt and purify the water body.

多功能组合池分为上下两层结构,上层结构为两格的格栅池4,一格为机械格栅,一格为人工格栅,截留悬浮物和漂浮物杂质;下层结构为水解酸化调节池5,上层格栅池出水通过池内折流板重力自流到水解酸化池底部,使得整个池子处于完全混合状态,控制水解酸化池的停留时间和上升流速,使反应处于酸化阶段,水解反应依靠酸化细菌的胞外酶进行完成,在多功能组合池内2/3处设有提升泵抽取污水。The multi-functional combined pool is divided into upper and lower two-layer structures. The upper structure is a grid pool 4 with two grids. One grid is a mechanical grid and the other is an artificial grid, which retains suspended solids and floating impurities. The lower layer structure is hydrolysis and acidification adjustment. Pool 5, the effluent from the upper grid pool flows to the bottom of the hydrolysis and acidification pool by gravity through the baffles in the pool, so that the whole pool is in a state of complete mixing, and the residence time and rising flow rate of the hydrolysis and acidification pool are controlled, so that the reaction is in the acidification stage, and the hydrolysis reaction relies on acidification. The extracellular enzymes of bacteria are completed, and 2/3 of the multi-functional combined pool is equipped with a lift pump to extract sewage.

在水解酸化调节池内设置立体弹性组合填料,对搅动的废水进行水力切割,填料材质为聚丙烯和/或聚乙烯。对搅动的废水进行水力切割,延长水力停留时间,使悬浮状态的污泥与水充分混合。为水解酸化菌的生长提供有利条件。组合填料通过角钢焊接的外框架固定在水解酸化调节池内,填料固定在距池底1m位置处。A three-dimensional elastic composite filler is arranged in the hydrolysis and acidification adjustment tank, and the agitated waste water is hydraulically cut, and the filler material is polypropylene and/or polyethylene. The agitated wastewater is hydraulically cut to prolong the hydraulic retention time, so that the suspended sludge can be fully mixed with water. Provide favorable conditions for the growth of hydrolytic acidification bacteria. The combined filler is fixed in the hydrolysis and acidification adjustment tank through the outer frame welded by angle steel, and the filler is fixed at a position 1m away from the bottom of the tank.

优选地,在多功能组合池的底部还设有多个漏斗状收集器,将收集的污泥定期排出。Preferably, a plurality of funnel-shaped collectors are also arranged at the bottom of the multifunctional combined tank to discharge the collected sludge regularly.

在多功能组合池和湿地单元之间设有吸力自清洗网式过滤器2,包括过滤器本体、粗滤网、细滤室、冲洗阀和冲洗控制器,经过吸力自清洗网式过滤器的污水,先通过粗滤网、细滤网两级过滤,截留大于100μm的污染物在滤网上,出水进入湿地单元,当滤网上内外压差大于预设值时,控制器打开冲洗阀,通利用压差的变化吸入反冲洗水冲洗滤网污物,通过冲洗阀排出。A suction self-cleaning mesh filter 2 is arranged between the multi-functional combined pool and the wetland unit, including a filter body, a coarse filter, a fine filter chamber, a flush valve and a flush controller. After the suction self-cleaning mesh filter The sewage is first filtered through the coarse filter screen and the fine filter screen, and the pollutants larger than 100μm are retained on the filter screen, and the effluent enters the wetland unit. When the pressure difference between the inside and outside of the filter screen is greater than the preset value, the controller opens the flushing valve, and the flow through the The change of pressure difference sucks in backwash water to wash the filter screen dirt and discharges it through the flush valve.

水流进入吸力自清洗网式过滤器后,首先通过粗滤网,然后进入细过滤室,由细滤网将大于100um污染物截留下来,出水即为净水,该过滤器的使用减小人工湿地的堵塞,延缓人工湿地填料的更换周期。After the water flow enters the suction self-cleaning mesh filter, it first passes through the coarse filter screen, and then enters the fine filter chamber. The fine filter screen intercepts pollutants larger than 100um, and the effluent is purified water. The use of this filter reduces the use of constructed wetlands. The blockage of the constructed wetland will delay the replacement cycle of the constructed wetland filler.

污物聚集在细滤网上,使滤网内表面和外表面形成压力差。当压差达到预设值时,便启动自清洗循环。压差传感器将信号传至控制器触动其打开冲洗阀,这样液压马达室内、污物收集器及吸嘴内的压力降至与大气相通。引起吸嘴相对的细滤网内面(污水)和细滤网外面(净水)之间的压力差,产生一股吸力强劲的反冲洗水将吸嘴相对的滤网上的污物清洗干净,由冲洗阀排出。Dirt collects on the fine screen, creating a pressure difference between the inner and outer surfaces of the screen. When the differential pressure reaches the preset value, the self-cleaning cycle starts. The differential pressure sensor transmits the signal to the controller to trigger it to open the flush valve, so that the pressure in the hydraulic motor chamber, the dirt collector and the suction nozzle is reduced to be open to the atmosphere. Causes the pressure difference between the inner surface of the fine filter screen (sewage) opposite the suction nozzle and the outside of the fine filter screen (clean water), and generates a strong suction backwash water to clean the dirt on the filter screen opposite the suction nozzle. Flush valve drains.

反冲洗水经过液压马达时带动污物收集器转动,这样吸嘴就将整个滤网上的污物吸走清洗干净。当滤网冲洗干净,控制器关闭冲洗阀,设备自动恢复到全滤状态。整个反冲洗过程只需几秒钟,而且期间主流不间断,也无须更换滤芯。冲洗用水只占主流1%。When the backwash water passes through the hydraulic motor, it drives the dirt collector to rotate, so that the suction nozzle can suck up and clean the dirt on the entire filter screen. When the filter screen is cleaned, the controller closes the flush valve, and the equipment automatically returns to the full filter state. The entire backwashing process takes only a few seconds, and the main flow is uninterrupted during this period, and there is no need to replace the filter element. The flushing water is only 1% of the mainstream.

实施例2Example 2

如图2、3所示,湿地单元由下至上依次铺设聚乙烯土工布层、第一粗砂层、第一砾石层、钢丝网层、第二砾石层、第二粗砂层、种植土层。As shown in Figures 2 and 3, polyethylene geotextile layer, first coarse sand layer, first gravel layer, steel mesh layer, second gravel layer, second coarse sand layer, and planting soil layer are laid in the wetland unit from bottom to top. .

其中,聚乙烯土工布层以厚度为0.5mm的聚乙烯塑料膜铺设,在两边衬垫密度为500g/m2的土工布;所述第一粗砂层的厚度为100mm,所述第一砾石层的厚度为500mm,砾石粒径为φ100~150mm;所述钢丝网层的孔径为10*10mm,钢丝直径为0.6mm;所述第二砾石层厚底为200mm,砾石粒径为φ10-15mm;所述第二粗砂层的厚度为200mm;所述种植土层的厚度为200mm,种植土层种植水生植物。Wherein, the polyethylene geotextile layer is laid with polyethylene plastic film with a thickness of 0.5mm, and a geotextile with a density of 500g/m2 is lined on both sides; the thickness of the first coarse sand layer is 100mm, and the first gravel layer is The thickness of the second gravel layer is 500mm, and the particle size of the gravel is φ100-150mm; the diameter of the steel mesh layer is 10*10mm, and the diameter of the steel wire is 0.6mm; the thickness of the second gravel layer is 200mm, and the particle size of the gravel is φ10-15mm; The thickness of the second coarse sand layer is 200mm; the thickness of the planting soil layer is 200mm, and the planting soil layer is used for planting aquatic plants.

人工湿地系统由若干个湿地单元顺序连接,传统意义上潜流垂直流人工湿地的水力停留时间为3~5d,本实用新型的湿地单元水力停留时间为1d,大大的减小占地面积,极大的提高水力负荷。The constructed wetland system is sequentially connected by a number of wetland units. In the traditional sense, the hydraulic retention time of the submerged vertical flow constructed wetland is 3-5d. The hydraulic retention time of the wetland unit of the present invention is 1d, which greatly reduces the floor space and greatly increase the hydraulic load.

湿地单元的滴灌系统铺设在第二砾石层,由一支布水主管进入湿地单元,由两根布水支管平行铺设在湿地单元内,布水支管采用贴片式滴灌带,贴片式滴灌带包括依次连通的贴片61、紊流通道62、过滤窗63。The drip irrigation system of the wetland unit is laid on the second gravel layer. A water distribution main pipe enters the wetland unit, and two water distribution branch pipes are laid in parallel in the wetland unit. The water distribution branch pipes use a patch type drip irrigation belt. It includes patches 61 , turbulent channels 62 , and filter windows 63 that are connected in sequence.

滴灌带中水先流经贴片,在流经紊流通道后进入过滤窗后经滴头出水。滴头流道为紊流流道,如图4所示,水从一个稳定状态到另一个稳定状态滴水均匀,能够实现灌水均匀,同时滴头带有过滤窗,抗堵性能好。不同作物不同土壤更换滴头模具就可以得到,不同滴水性能的滴灌带,易于实现精细化精准灌溉。滴灌带是利用塑料管道将水通过直径约10mm毛管上的孔口或滴头送到作物根部进行局部灌溉。贴片式滴灌带是把扁平形状的滴头镶在管带内壁上的一体化滴灌带,贴片式滴灌带的滴水孔选用机械打孔方法完结,配有残渣收回体系,打孔速度快,无残留渣屑。滴头、管道整体性强。The water in the drip irrigation belt first flows through the patch, and after flowing through the turbulent channel, it enters the filter window and then exits through the dripper. The dripper flow channel is a turbulent flow channel, as shown in Figure 4, the water drips uniformly from one stable state to another stable state, which can achieve uniform irrigation, and the dripper has a filter window, which has good anti-blocking performance. Different crops and different soils can be obtained by replacing the dripper mold. Drip irrigation belts with different dripping properties are easy to achieve refined and precise irrigation. Drip irrigation belts use plastic pipes to send water to the roots of crops through orifices or drippers on capillary tubes with a diameter of about 10mm for local irrigation. The patch type drip irrigation belt is an integrated drip irrigation belt with a flat-shaped dripper embedded on the inner wall of the pipe belt. The drip hole of the patch type drip irrigation belt is completed by a mechanical punching method. No residue residue. Dripper, pipeline integrity is strong.

同时,在滴灌带铺设时可以人为的将滴头出水口向上,通水后水中含有的杂质比重大于水,杂质会沉在滴灌带底部,在滴灌带清洗时将杂质从滴灌带尾部排出因此不会造成滴头堵塞。不但能够保证系统运行的可靠性,而且可以简化过滤装置结构,降低水质处理所需的高昂费用。At the same time, when the drip irrigation belt is laid, the water outlet of the dripper can be artificially turned upward. After the water is passed through, the proportion of impurities contained in the water is greater than that of the water, and the impurities will sink at the bottom of the drip irrigation belt. Can cause the dripper to clog. It can not only ensure the reliability of the system operation, but also simplify the structure of the filter device and reduce the high cost of water quality treatment.

湿地单元的导膜系统为丰字集水管铺设在第一砾石层,集水孔的孔径采用为φ20,并列排列的集水管的间距150mm,导膜系统排淤,进行水体净化。The guiding membrane system of the wetland unit is a Fengzi water collection pipe laid on the first gravel layer. The diameter of the water collection hole is φ20, and the distance between the water collection pipes arranged in parallel is 150mm. The guiding film system discharges silt for water purification.

人工湿地系统用于村镇生活污水的净化处理。鉴于村镇及城郊结合处居民用水的不均匀性,设置多功能组合池用于调节污水量,且根据居民用水时间的特点分析,主要用水时间集中在早、中、晚3个时间点,在上午6:00~8:00和下午的17:00~20:00流量最大,最大时间点的用水时长普遍不超过3h,本次多功能组合池设计调节时间为3h,及时缓解用水高峰时刻污水的收集,组合池内设置提升泵,在用水高峰时刻来临前能及时清空调节池内污水。The constructed wetland system is used for the purification and treatment of domestic sewage in villages and towns. In view of the non-uniformity of residents' water use at the junction of villages and towns and suburban areas, a multi-functional combined pool is set up to adjust the amount of sewage. From 6:00 to 8:00 and from 17:00 to 20:00 in the afternoon, the flow rate is the largest, and the water consumption time at the maximum time point generally does not exceed 3 hours. The design adjustment time of this multi-functional combined pool is 3 hours, so as to timely alleviate the pollution of sewage during peak water consumption. Collection, a lift pump is installed in the combined tank, and the sewage in the adjustment tank can be emptied in time before the peak time of water consumption.

本实用新型的人工湿地系统的进水为经吸力自清洗网式过滤器后的出水,水质参数pH为6-7.2,DO为0.01-0.05,TSS为45-62mg/L,CODcr为124-200mg/L,BOD5为66-96mg/L,TN为65-75mg/L,NH4-N为30.5-45mg/L,TP为4.8-5.3mg/L。The inlet water of the constructed wetland system of the utility model is the outlet water after the suction self-cleaning mesh filter, the water quality parameters are pH 6-7.2, DO is 0.01-0.05, TSS is 45-62mg/L, and CODcr is 124-200mg /L, BOD5 is 66-96mg/L, TN is 65-75mg/L, NH4-N is 30.5-45mg/L, TP is 4.8-5.3mg/L.

在系统运行过程中,采用连续进水方式,在湿地单元中运行超过12个月,出水pH和DO的效果分别为:6.9-7.2,3.9-4.9mg/L。其中TSS去除率为50-70%,CODcr去除率为52.3-72.5%,BOD5去除率51-70.4%,TN去除率26.3-43.9%,NH4-N去除率56.4-85.4%,TP去除率85-94.8%。During the operation of the system, the continuous water inflow method was adopted, and the wetland unit was operated for more than 12 months. The effects of effluent pH and DO were 6.9-7.2 and 3.9-4.9 mg/L, respectively. Among them, TSS removal rate is 50-70%, CODcr removal rate is 52.3-72.5%, BOD5 removal rate is 51-70.4%, TN removal rate is 26.3-43.9%, NH4-N removal rate is 56.4-85.4%, TP removal rate is 85- 94.8%.

实施例3Example 3

在人工湿地的运行初期,填料中的细微粘土粒子与许多淤积的SS共同组成致密不透水层,胞外聚合物不断凝聚和吸附不同粒径的悬浮或胶体状态的底物,进而形成大粒径絮团状的累积物,造成有机物和无机物共同积累,堵塞填料孔隙,需及时导出老化脱落的生物膜系统,定期把集水池中出水管将湿地运行过程中产生的沉淀物、截留物以及剥落的生物膜排出湿地单元,保证湿地中水流畅通。导膜装置启用时,关闭人工湿地集水池内出水管上阀门,使湿地内填料处于满水浸润状态,采用水力浸润时间24h,使填料上老化的生物膜更易脱落进入水中,之后瞬时打开阀门,在人工湿地内有压水流状态的冲击下,使老化的生物膜脱落进入导膜系统即集水系统中,导入集水池内,排出人工湿地系统。In the early stage of the operation of the constructed wetland, the fine clay particles in the filler and many deposited SS together form a dense and impermeable layer, and the extracellular polymer continuously coagulates and adsorbs the suspended or colloidal substrates of different particle sizes, thereby forming a large particle size. The floc-like accumulation causes the co-accumulation of organic matter and inorganic matter, which blocks the pores of the filler. It is necessary to export the aging and falling off biofilm system in time. The biofilm is discharged from the wetland unit to ensure the smooth flow of water in the wetland. When the membrane guide device is activated, close the valve on the outlet pipe in the water collection tank of the constructed wetland, so that the filler in the wetland is in a state of full water infiltration, and the hydraulic infiltration time is 24h, so that the aging biofilm on the filler is more likely to fall off into the water, and then open the valve instantly, Under the impact of the pressurized water flow in the constructed wetland, the aging biofilm falls off into the guiding membrane system, that is, the water collection system, and is introduced into the water collection tank and discharged from the constructed wetland system.

本实用新型提供了一种利用人工湿地系统的污水处理方法:将生活污水流入所述多功能组合池,机械格栅或人工格栅根据清捞需要间隔工作,提升泵以3小时为间隔将组合池中的污水抽净一次;The utility model provides a sewage treatment method using a constructed wetland system: the domestic sewage is flowed into the multifunctional combined pool, the mechanical grille or the artificial grille works at intervals according to the needs of cleaning, and the lifting pump is combined at an interval of 3 hours. The sewage in the pool is pumped once;

湿地单元的使用数量根据液位高度的需求选定,夏季节选择高液位运行,液位到达种植土层上的植物,春秋季节选择中液位运行,液位到达第二粗砂层,冬季节选择低液位运行,液位到达第二砾石层;The number of wetland units used is selected according to the requirements of the liquid level height. In summer, high liquid level operation is selected, and the liquid level reaches the plants on the planting soil layer. In spring and autumn, medium liquid level operation is selected, and the liquid level reaches the second coarse sand layer. In winter Select low liquid level operation in section, and the liquid level reaches the second gravel layer;

在湿地单元运行初期,开启集水管出水阀门,污水各层吸附的积累物通过集水管排出;In the initial stage of operation of the wetland unit, open the outlet valve of the water collection pipe, and the accumulated materials adsorbed by each layer of sewage are discharged through the water collection pipe;

在湿地单元运行后期,关闭集水管出水阀门,污水在湿地单元中水力停留时间为24h,各层老化的生物膜脱落进入水中,瞬间开启集水管出水阀门,老化的生物膜脱落进入导膜系统,排出人工湿地系统。In the late stage of operation of the wetland unit, close the outlet valve of the water collection pipe, the hydraulic retention time of sewage in the wetland unit is 24 hours, the aging biofilm of each layer falls off into the water, and the outlet valve of the water collection pipe is opened instantly, and the aging biofilm falls off and enters the guiding membrane system. Discharge from the constructed wetland system.

该高效潜流人工湿地系统的进水为辽宁市某郊区市政污水,水质参数pH为7.2-8.0,DO为0.03-0.13。采用上述方法进行污水处理。The influent of this high-efficiency subsurface constructed wetland system is municipal sewage in a suburb of Liaoning City, with water quality parameters of pH 7.2-8.0 and DO of 0.03-0.13. Sewage treatment is carried out using the above method.

在高效潜流人工湿地系统运行超过12个月,出水pH和DO的效果分别为:6.9-7.2,3.9-4.9mg/L。其中TSS去除率为85-92.2%,CODcr去除率为86.7-94.6%,BOD5去除率83.2-90.3%,TN去除率35%,NH4-N去除率78.6-86.2%,TP去除率85-95%。In the high-efficiency subsurface constructed wetland system running for more than 12 months, the effects of effluent pH and DO are: 6.9-7.2, 3.9-4.9mg/L. Among them, the removal rate of TSS is 85-92.2%, the removal rate of CODcr is 86.7-94.6%, the removal rate of BOD5 is 83.2-90.3%, the removal rate of TN is 35%, the removal rate of NH4-N is 78.6-86.2%, and the removal rate of TP is 85-95%. .

以上所述实施例仅表达了本实用新型的实施方式,其描述较为具体和详细,但并不能因此而理解为对本实用新型专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本实用新型构思的前提下,还可以做出若干变形和改进,这些都属于本实用新型的保护范围。因此,本实用新型专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only represent the embodiments of the present invention, and the descriptions thereof are specific and detailed, but should not be construed as limiting the scope of the present invention. It should be pointed out that for those of ordinary skill in the art, some modifications and improvements can be made without departing from the concept of the present invention, which all belong to the protection scope of the present invention. Therefore, the protection scope of the patent for this utility model shall be subject to the appended claims.

Claims (11)

1. An artificial wetland system with high-efficiency subsurface flow comprises a multifunctional combined pool and wetland units, and is characterized in that sewage firstly intercepts suspended matters and floating impurities in the multifunctional combined pool and carries out hydrolytic acidification on a water body; and then filtering and biodegrading in the wetland unit, uniformly distributing water by adopting a drip irrigation system, dredging by adopting a membrane guide system, and purifying the water body.
2. The constructed wetland system of claim 1, wherein the multifunctional combined tank is divided into an upper layer structure and a lower layer structure, the upper layer structure is a two-lattice grating tank, one lattice is a mechanical grating, the other lattice is an artificial grating, and suspended matters and floating impurities are intercepted; the lower structure is a hydrolysis acidification adjusting tank, the effluent of the upper grid tank flows to the bottom of the hydrolysis acidification tank through the gravity of a baffle plate in the tank, the effluent is hydrolyzed through acidic bacteria in the tank, and a lifting pump is arranged at 2/3 of the position in the multifunctional combined tank to pump sewage.
3. The constructed wetland system of claim 2, wherein a three-dimensional elastic combined filler is arranged in the hydrolysis acidification adjusting tank to perform hydraulic cutting on the stirred wastewater, and the filler is made of polypropylene and/or polyethylene.
4. The constructed wetland system of claim 2, wherein a plurality of funnel-shaped collectors are provided at the bottom of the multipurpose composite tank, and the collected sludge is periodically discharged.
5. The constructed wetland system of claim 2, wherein a suction self-cleaning screen filter is disposed between the multifunctional assembled tank and the wetland unit, and comprises a filter body, a coarse filter screen, a fine filter chamber, a flushing valve and a flushing controller, wherein the sewage passing through the suction self-cleaning screen filter is firstly filtered by the coarse filter screen and the fine filter screen in two stages, the pollutants larger than 100 μm are trapped on the filter screen, the effluent enters the wetland unit, and when the pressure difference between the inside and the outside on the filter screen is larger than a preset value, the controller opens the flushing valve, so that the sewage is flushed by the backwashing water through the filter screen and is discharged through the flushing valve.
6. The constructed wetland system of claim 1, wherein the wetland unit is sequentially paved with a polyethylene geotextile layer, a first coarse sand layer, a first gravel layer, a steel wire mesh layer, a second gravel layer, a second coarse sand layer and a planting soil layer from bottom to top.
7. The constructed wetland system of claim 6, wherein the polyethylene geotextile layer is laid with a polyethylene plastic film having a thickness of 0.5mm and a liner density of 500g/m on both sides2The geotextile of (1); the thickness of the first coarse sand layer is 100mm, the thickness of the first gravel layer is 500mm, and the particle diameter of gravel is phi 100-150 mm; the aperture of the steel wire mesh layer is 10 x 10mm, and the diameter of the steel wire is 0.6 mm; the thickness of the second gravel layer is 200mm, and the particle size of the gravel is phi 10-15 mm; the thickness of the second coarse sand layer is 200 mm; the thickness of planting the soil layer is 200mm, plants aquatic plants in the soil layer.
8. The constructed wetland system of claim 6, wherein the constructed wetland system is composed of a plurality of wetland units which are connected in sequence.
9. The constructed wetland system of claim 8, wherein the drip irrigation system of the wetland unit is laid on the second gravel layer, enters the wetland unit from a main water distribution pipe, and is laid in the wetland unit in parallel from two branch water distribution pipes, the branch water distribution pipes are patch-type drip irrigation belts, and each patch-type drip irrigation belt comprises a patch, a turbulent flow channel and a filter window which are sequentially communicated.
10. The constructed wetland system of claim 9, wherein the membrane guide system of the wetland unit is a Chinese character feng water collecting pipe laid on the first gravel layer, the aperture of the water collecting hole is phi 20mm, and the distance between the water collecting pipes arranged in parallel is 150 mm.
11. The constructed wetland system of any one of claims 1 to 10, wherein the constructed wetland system is used for purifying domestic sewage in villages and towns.
CN202020127767.1U 2020-01-20 2020-01-20 Artificial wetland system of high-efficient undercurrent Expired - Fee Related CN212025107U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111115980A (en) * 2020-01-20 2020-05-08 岭南水务集团有限公司 A high-efficiency underflow constructed wetland system and its sewage treatment method
CN115466004A (en) * 2022-06-22 2022-12-13 苏州市苏水实业发展有限公司 Water works waste water filter equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111115980A (en) * 2020-01-20 2020-05-08 岭南水务集团有限公司 A high-efficiency underflow constructed wetland system and its sewage treatment method
CN115466004A (en) * 2022-06-22 2022-12-13 苏州市苏水实业发展有限公司 Water works waste water filter equipment

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