




技术领域technical field
本实用新型涉及废/污水处理净化技术领域,尤其涉及新农村山丘区民居生活污水净化回用系统。The utility model relates to the technical field of waste/sewage treatment and purification, in particular to a system for purifying and reusing domestic sewage in new rural hilly areas.
背景技术Background technique
中国水资源缺乏和水污染严重地制约着我国总体经济的健康持续发展,基础设施滞后和管理水平低下抑制了农村地区居民生活质量的改善和提高,国家正在加大力度扶持新农村水改项目,农村地区的水环境治理应成为我国环境综合治理的重要组成部分。The lack of water resources and water pollution in China are seriously restricting the healthy and sustainable development of my country's overall economy. The lagging infrastructure and low management level have inhibited the improvement and improvement of the quality of life of residents in rural areas. The state is stepping up efforts to support new rural water reform projects. Water environment management in rural areas should become an important part of my country's comprehensive environmental management.
广大农村大量存在以动植物为原料生产产品( 包括畜禽渔养殖业及所需饲料)排放的生产废( 污) 水,以及人类活动产生的生活污水。这些污水不经处理就排放,会对环境造成污染。In the vast rural areas, there are a lot of production waste (sewage) water discharged from the production of products (including livestock, poultry, aquaculture and required feed) using animals and plants as raw materials, as well as domestic sewage generated by human activities. These sewage are discharged without treatment, which will pollute the environment.
实用新型内容Utility model content
本实用新型旨在提供新农村山丘区民居生活污水净化回用系统,可对新农村山丘区民居生活污水进行净化。The utility model aims to provide a system for purifying and reusing the domestic sewage of the dwellings in the hilly areas of the new countryside, which can purify the domestic sewage of the dwellings in the hilly areas of the new countryside.
为达到上述目的,本实用新型采用的生态技术,方案如下:In order to achieve the above object, the ecological technology adopted by the present utility model, the scheme is as follows:
新农村山丘区民居生活污水净化回用系统,包括依次连通的除渣栅网槽、沉砂调节水解酸化池、多级厌氧池、湿地或土地、污泥沉淀池、过滤池和回用水池;The domestic sewage purification and reuse system in the hilly area of new rural areas, including the sequentially connected slag removal grid tank, sand settling adjustment hydrolysis acidification tank, multi-stage anaerobic tank, wetland or land, sludge sedimentation tank, filter tank and reuse pool;
多级厌氧池产生的沼气通入气水分离装置,所述气水分离装置的排水口连通沉砂调节水解酸化池,气水分离装置的排气口连通脱硫装置,脱硫装置的排气口连接储气罐。The biogas generated by the multi-stage anaerobic tank is passed into the gas-water separation device, the water outlet of the gas-water separation device is connected to the sand settling adjustment hydrolysis acidification tank, the exhaust port of the gas-water separation device is connected to the desulfurization device, and the exhaust port of the desulfurization device is connected. Connect the air tank.
进一步的,所述污泥沉淀池底部设污泥泵,污泥泵出口连接排污管,排污管连接污泥浓缩池,所述污泥浓缩池的出液口与沉砂调节水解酸化池连通。Further, a sludge pump is provided at the bottom of the sludge settling tank, the outlet of the sludge pump is connected to a sewage pipe, and the sewage pipe is connected to a sludge thickening tank, and the liquid outlet of the sludge thickening tank is communicated with the sand settling adjustment, hydrolysis and acidification tank.
进一步的,污泥沉淀池内设有斜管区。Further, an inclined pipe area is arranged in the sludge sedimentation tank.
优选地,所述多级厌氧池为两级厌氧池。Preferably, the multi-stage anaerobic pond is a two-stage anaerobic pond.
或者,所述多级厌氧池为三级厌氧池。Alternatively, the multi-stage anaerobic tank is a three-stage anaerobic tank.
进一步优选地,所述三级厌氧池分别为:第一级厌氧复合污泥床高效厌氧池、第二级下流式固定生物膜高效厌氧池、第三级上流式厌氧过滤高效厌氧池。Further preferably, the three-level anaerobic tanks are respectively: the first-level anaerobic composite sludge bed high-efficiency anaerobic tank, the second-level down-flow fixed biofilm high-efficiency anaerobic tank, and the third-level up-flow anaerobic filtration high-efficiency tank. Anaerobic pool.
进一步的,厌氧池间设调压池。Further, a pressure regulating tank is set between the anaerobic tanks.
进一步的,沉砂调节水解酸化池底部设布水器,布水器上方置多孔填料,多孔填料为塑泡多孔填料、或弹性填料、或BF填料。Further, a water distributor is arranged at the bottom of the sand settling adjustment hydrolysis and acidification tank, and a porous filler is arranged above the water distributor, and the porous filler is a plastic foam porous filler, or an elastic filler, or a BF filler.
进一步的,过滤池与回用水池间设取样井。Further, a sampling well is set between the filter tank and the reuse tank.
其中,回用水池中安装回用水泵。Among them, the recycling water pump is installed in the recycling pool.
与现有技术相比,本实用新型具有以下显著效果:Compared with the prior art, the utility model has the following remarkable effects:
1,本实用新型采用生态技术高效厌氧与湿地或土地辅助联合处理,高效厌氧为主,湿地或土地辅助,互补联营,再经沉淀过滤后排出,净化效果好,可确保生活污水处理净化达到排放标准;1. The utility model adopts ecological technology for high-efficiency anaerobic and wetland or land-assisted joint treatment, high-efficiency anaerobic treatment is mainly, wetland or land-assisted, complementary joint operation, and then discharged after precipitation and filtration, the purification effect is good, and the purification of domestic sewage can be ensured. meet emission standards;
2,本实用新型采用厌氧处理为主,低能耗、低投资、低运行费用、管理简单;产生的污泥很少,仅是好氧的1/6-1/10,矿化度高、易脱水,处理的装置小、相应处理费用亦少;2. The utility model mainly adopts anaerobic treatment, low energy consumption, low investment, low operating cost and simple management; the produced sludge is very little, only 1/6-1/10 of aerobic, high salinity, It is easy to dehydrate, the treatment device is small, and the corresponding treatment cost is also low;
3,厌氧处理为主,使净化处理大多在密闭状况下进行,运行控制和嗅味控制容易;厌氧需营养物少;因其污泥浓度高,能承受较大的负荷和水质变化,容积负荷一般达5-10kgCOD/m3.d,高可达50kg COD/m3.d;污泥可长期贮存、保持活性,故季节性间歇运行亦正常;3. Anaerobic treatment is the main method, so that purification treatment is mostly carried out in a closed state, and operation control and odor control are easy; anaerobic needs less nutrients; because of its high sludge concentration, it can withstand large loads and water quality changes. The volume load is generally 5-10kgCOD/m3.d, up to 50kg COD/m3.d; the sludge can be stored for a long time and maintain its activity, so the seasonal intermittent operation is also normal;
4,产生的污泥和沼气,可作肥料、饲铒料,化工原料;出水可回用作清洁、冷却、农灌用水,或存储作消防用水、生态塘养鱼用水,具有一定的经济效益。4. The generated sludge and biogas can be used as fertilizer, erbium feed, and chemical raw materials; the effluent can be reused as water for cleaning, cooling, agricultural irrigation, or stored as water for firefighting and fish farming in ecological ponds, which has certain economic benefits. .
附图说明Description of drawings
图1是本实用新型的结构示意图;Fig. 1 is the structural representation of the present utility model;
图2是三级厌氧池的原理图;Figure 2 is a schematic diagram of a three-stage anaerobic tank;
图3是沉砂调节水解酸化池的平面图;Fig. 3 is a plan view of a sand settling regulating hydrolysis acidification tank;
图4是人工湿地的剖面图;Figure 4 is a sectional view of a constructed wetland;
图5是人工湿地的布水器的平面图。Fig. 5 is a plan view of a water distributor of a constructed wetland.
具体实施方式Detailed ways
为了使本实用新型的目的、生态技术方案及优点更加清楚明白,以下结合附图,对本实用新型进行进一步详细说明。In order to make the objectives, ecological technical solutions and advantages of the present utility model clearer, the present utility model will be further described in detail below with reference to the accompanying drawings.
实施例一Example 1
如图1所示,本实用新型公开的新农村山丘区民居生活污水净化回用系统,包括污泥浓缩池13以及依次连通的除渣栅网槽1、沉砂调节水解酸化池2、多级厌氧池、湿地10、污泥沉淀池6、过滤池7、回用水池9。As shown in FIG. 1, the utility model discloses a system for purifying and reusing domestic sewage in the new rural hilly area, including a
为了减少土地使用面积,节约土建成本,本实用新型进行部分池体合建。沉砂调节水解酸化池2为集除渣沉砂、均化/水解酸化与PH调节改性功能于一体的联槽池。且为了发挥厌氧水解酸化过程高效功能,该池设布水器于底部的活性污泥中;活性污泥上方置填料,填料为塑泡多孔填料、或弹性填料、或BF填料。沉砂调节水解酸化池2使处理进水水质均匀、水量相对稳定,而且可提高后续生化处理池降解污染物质的比率。In order to reduce the land use area and save the civil construction cost, the utility model carries out the joint construction of some pools. The sand settling adjustment hydrolysis and
如图3所示,在沉砂调节水解酸化池2入口设除渣栅网槽101,除渣栅网槽101内设置人工或机械格栅和10-20目不锈钢丝网实现除渣。格栅设置两道,一道间隙为10mm,另一道间隙为5mm,污水流经格栅可去除粗大渣物以免堵塞后续处理设施、设备,利于影响处理效果。为节省成本,可采用人工定期清渣。沉砂调节水解酸化池2紧连除渣栅网槽101设置。As shown in Figure 3, a slag
如图1所示,本实施方式中包括两级厌氧池;分别为第一级厌氧池3和第二级厌氧池4。As shown in FIG. 1 , this embodiment includes two-stage anaerobic tanks; the first-level anaerobic tank 3 and the second-level anaerobic tank 4 are respectively.
如图2所示,在另一个实施方式中,多级厌氧池为三级厌氧池。三级厌氧池分别为:第一级厌氧复合污泥床高效厌氧池、第二级下流式固定生物膜高效厌氧池、第三级上流式厌氧过滤高效厌氧池。As shown in Figure 2, in another embodiment, the multi-stage anaerobic pond is a three-stage anaerobic pond. The three-level anaerobic tanks are: the first-level anaerobic composite sludge bed high-efficiency anaerobic tank, the second-level down-flow fixed biofilm high-efficiency anaerobic tank, and the third-level up-flow anaerobic filtration high-efficiency anaerobic tank.
第一级厌氧复合污泥床高效厌氧池为上流式厌氧污泥床反应器的活性污泥床和厌氧过滤器、降流式厌氧过滤器滤料生物膜床组合,配上仿生布水器,组成的“UASB+AF”反应器,简称第一级UASB+AF。该反应器下部1.0m为活性污泥床、床底安装接前池来水的仿生布水器,其上为1.0—3.0m滤(填)料生物膜床。以上尺寸为本实施方式提供的参考,具体尺寸应视水量、池有效水深确定。The first-stage anaerobic composite sludge bed high-efficiency anaerobic tank is a combination of activated sludge bed and anaerobic filter, and down-flow anaerobic filter filter material biofilm bed of the up-flow anaerobic sludge bed reactor. The bionic water distributor consists of a "UASB+AF" reactor, referred to as the first-stage UASB+AF. The lower 1.0m of the reactor is an activated sludge bed, the bottom of the bed is installed with a bionic water distributor connected to the incoming water from the forepond, and a 1.0-3.0m filter (packing) biofilm bed is installed above it. The above dimensions are provided for reference in this embodiment, and the specific dimensions should be determined according to the amount of water and the effective water depth of the pool.
污泥床底部的布水器,使污水从下往上让活性污泥消化,并让具充分活性的污泥床在代谢中使颗粒污泥富集驯化而繁殖。The water distributor at the bottom of the sludge bed makes the sewage digest the activated sludge from bottom to top, and allows the fully activated sludge bed to enrich and domesticate the granular sludge during metabolism.
厌氧过滤器、降流式厌氧过滤器,其核心是滤(填)料生物膜床,废水无论以升流、降流方式通过之,均系其起关键作用,其不耗能且产沼气CH4,进入正常运行后管理简单。The core of anaerobic filter and downflow anaerobic filter is the filter (packing) biofilm bed. Whether the wastewater passes through it in the way of upflow or downflow, it plays a key role, and it does not consume energy and produce Biogas CH4 is easy to manage after entering normal operation.
第二级高效厌氧池为下流式固定生物膜高效厌氧池,简称第二级DSFF厌氧池;第三级高效厌氧池为上流式厌氧过滤高效厌氧池,简称第三级AF厌氧池。厌氧池内安富集厌氧颗粒污泥,可使单位容积负荷、污染物降除率大大提高,可减少池容,缩小占地面积,降低投资、运行成本。The second-level high-efficiency anaerobic tank is a downflow fixed biofilm high-efficiency anaerobic tank, referred to as the second-level DSFF anaerobic tank; the third-level high-efficiency anaerobic tank is an up-flow anaerobic filtration high-efficiency anaerobic tank, referred to as the third-level AF. Anaerobic pool. The anaerobic granular sludge is safely enriched in the anaerobic tank, which can greatly improve the unit volume load and pollutant removal rate, reduce the tank capacity, reduce the floor space, and reduce investment and operating costs.
多级厌氧池产生的沼气通入气水分离装置16,气水分离装置16的排水口连通除渣栅网槽1,气水分离装置16的排气口连通脱硫装置17,脱硫装置17的排气口连接储气罐19。产生的沼气可燃用。The biogas generated by the multi-stage anaerobic tank is passed into the gas-
湿地10即湿地生态系统,是湿地植物、栖息于湿地的动物、微生物及其环境组成的统一整体。湿地具有多种功能: 保护生物多样性,调节径流,改善水质。湿地生态系统属于水域生态系统,其生物群落由水生和陆生种类组成,物质循环、能量流动和物种迁移与演变活跃,具有较高的生态多样性、物种多样性和生物生产力。我国湿地广泛分布于高原平川、丘陵等地域,这些地域可以利用天然的湿地来进行净化。湿地表面种植水生植物,污水沿一定方向流动的过程中,在植物及微生物的物理和生物的作用下,污水中污染物质通过植物吸收、微生物吸附降解来实现对污水的高效净化,污水中有机污染物和杂质在植物、土壤的吸附吸收作用下基本上被去除。
污泥沉淀池6内设有斜管区61,湿地10的出水通过管道引流到斜管区61下方。污泥沉淀池6底部设污泥泵62,污泥泵62出口连接排污管,排污管连接污泥浓缩池13,污泥浓缩池13的出液口与沉砂调节水解酸化池2连通。The
污泥沉淀池6的上清液自流进入过滤池7,经过滤池7过滤后,流入进入回用水池9,回用水池9中安装回用水泵91,回用水泵91用于将回用水池9中的水抽出作清洁、冷却、农灌用水,或存储作消防用水、生态塘养鱼用水等。过滤池7与回用水池9间设取样井8,方便采样。The supernatant of the
本实用新型的原理如下:The principle of the present utility model is as follows:
生活污水进入除渣栅网槽1,污水通过格栅网后,其粗大、可沉固体及漂浮物被拦截;自流进入沉砂调节水解酸化池2,沉砂调节水解酸化池2对污水进行泥沙沉淀、水质水量调节,而且大分子有机物水解酸化转化为小分子有机物,被分解成稳定的沉渣;The domestic sewage enters the slag
沉砂调节水解酸化池2出水自流进入第一级UASB+AF厌氧池池底区的布水器,布水器将污水分布予高活性厌氧污泥床和厌氧复合床反应区,从而对污水中的高浓度有机物进行处理,处理后的污水流入调压池,再依次经第二级DSFF厌氧池、调压池和第三级AF厌氧池处理;在三级厌氧池内厌氧菌的作用下分解污水中的大部分有机物;处理后的污水流至湿地10,在湿地生态系统的作用下,去除污水中残存的部分有机物;The effluent from sand settling adjustment hydrolysis and
经过前段微生物处理后的水排入污泥沉淀池6,经污泥沉淀池6沉淀后的清水自流进入过滤池7,去除污水中残存的有机物;过滤池7过滤后的水进入回用水池9中进行蓄水。厌氧池和污泥沉淀池6的污泥排入污泥浓缩池13内,污泥浓缩池13内的清液引入沉砂调节水解酸化池2内继续进行微生物处理,污泥浓缩池13内的固体则人工外运处置。The water after the previous microbial treatment is discharged into the
下面介绍使用本实用新型的使用方法:The following introduces the use method of the present utility model:
生活污水经设格栅间隙从10㎜到5㎜两道除渣、再经10-20目的不锈钢丝网过滤,砂粒入槽,然后进入沉砂调节水解酸化池2;The domestic sewage is slag-removed in two steps from 10 mm to 5 mm by setting the grid gap, and then filtered by a 10-20 mesh stainless steel wire mesh, and the sand particles enter the tank, and then enter the sand settling adjustment hydrolysis and
沉砂调节水解酸化池2,让生物质有机废水经2.5-5.0h的水解酸化后,COD、BOD、SS分别被去除40%、30%、80%左右后进入后处理,应用时应充分利用该阶段的此效果,对后期厌氧处理十分有利。将其与水处理的集水、均化调节和厌氧池的调压间组合一体,可实现多工艺、功能集成、缩小反应器,节约投资、运行、管理费用。Settling sand adjusts hydrolysis and
三级厌氧池总池容按常温运行为:V=Q×1.5×a,a=3-10;当BOD≤200㎎/L时,a取3;当BOD≥200㎎/L时,a取3以上。The total tank capacity of the three-stage anaerobic tank runs at room temperature as: V=Q×1.5×a, a=3-10; when BOD≤200㎎/L, a is 3; when BOD≥200㎎/L, a Take 3 or more.
经水解、三级厌氧处理后,生活污水中的生物质有机废水已大多达灌溉水要求、甚至更佳,后接湿地10和过滤处理可达标排放或回用。要求出水达地表水GBIV可采用本实用新型。After hydrolysis and tertiary anaerobic treatment, the biomass organic wastewater in the domestic sewage has reached the requirements of irrigation water, or even better, followed by
实际应用中,应具体因地制宜对出水或根据需要回用作清洁、冷却、农灌用水,或存储作消防用水、生态塘养鱼用水等。In practical applications, the effluent should be specifically adapted to local conditions or reused as needed for cleaning, cooling, agricultural irrigation, or stored as water for firefighting, water for fish farming in ecological ponds, etc.
各池产生污泥以视运行1年至多不超2年见出水浑浊,采用污泥泵管抽吸外运其它需处作菌种、或农林果蔬肥、或运垃圾场处理。在实际运用中应采取接种、培养、驯化污泥,便能较快启动、正常运行。Sludge produced by each pool may be turbid after 1 year of operation and no more than 2 years, and the sludge pump pipe is used to pump out other bacteria that need to be transported, or agricultural, forestry, fruit and vegetable fertilizer, or transport to the garbage dump for disposal. In practical application, inoculation, cultivation and domestication of sludge should be adopted, so that it can start up and operate normally.
实施例二
本实施例与实施例一的区别在于:如图4、5所示,本实施例中湿地10为人工湿地。人工湿地包括从下往上设置的素土夯实层101、100mm厚C15垫层102、SBS防水层103、200mm厚C20砼底板104、600mm厚,φ50~φ100mm湿地专用填料105、土工布106、200mm厚湿地植物专用种植土1010。每层的厚度根据实际需要可合理设置。湿地专用填料105可选择卵石、碎石、河沙等;可种植旱伞草、莎草、再力花、黑藻、大漂等湿地植物。如图4、5所示,湿地专用填料105内有布水器108,布水器108的主管连通入水沟109,水沟109接前厌氧池来水。布水器108的支管110上间隔5cm切割宽5mm、深4cm溢水口,溢水口外包土工布封头。The difference between this embodiment and the first embodiment is that, as shown in FIGS. 4 and 5 , the
本实用新型的原理如下:The principle of the present utility model is as follows:
生活污水进入除渣栅网槽1,污水通过格栅网后,其粗大、可沉固体及漂浮物被拦截;自流进入沉砂调节水解酸化池2,沉砂调节水解酸化池2对污水进行泥沙沉淀、水质水量调节,而且大分子有机物水解酸化转化为小分子有机物,被分解成稳定的沉渣;The domestic sewage enters the slag
沉砂调节水解酸化池2出水自流进入第一级UASB+AF厌氧池池底区的布水器,布水器将污水分布予高活性厌氧污泥床和厌氧复合床反应区,从而对污水中的高浓度有机物进行处理,处理后的污水流入调压池,再依次经第二级DSFF厌氧池、调压池和第三级AF厌氧池处理;在三级厌氧池内厌氧菌的作用下分解污水中的大部分有机物;处理后的污水流至人工湿地;The effluent from sand settling adjustment hydrolysis and
人工湿地通过模拟和强化自然湿地功能,将污水有控制地投配到湿地填料,湿地表面种植水生植物,污水沿一定方向流动的过程中,在填料、植物及微生物的物理、化学和生物的三重作用下,污水中污染物质通过填料过滤、植物吸收、微生物吸附降解来实现对污水的高效净化,污水中有机污染物和杂质在植物、土壤的吸附吸收作用下基本上在该段被去除,出水可直接用于农灌;By simulating and strengthening the functions of natural wetlands, constructed wetlands distribute sewage to wetland fillers in a controlled manner, and aquatic plants are planted on the wetland surface. During the process of sewage flowing in a certain direction, the physical, chemical and biological effects of fillers, plants and microorganisms occur. Under the action, the pollutants in the sewage are efficiently purified by the filler filtration, plant absorption, and microbial adsorption and degradation. The organic pollutants and impurities in the sewage are basically removed in this section under the adsorption and absorption of plants and soil. Can be directly used for agricultural irrigation;
人工湿地出水进入污泥沉淀池6,经污泥沉淀池6沉淀后的清水自流进入过滤池7,去除污水中残存的有机物;过滤池7过滤后的水进入回用水池9中进行蓄水。The effluent from the constructed wetland enters the
在另一个实施方式中,采用土地替换湿地。In another embodiment, land is used to replace wetlands.
本实用新型将物理与生化组合在一起,二者优势互补,同时将髙效厌氧与湿地或土地相结合,污染物去除率高,出水质好;其耗能低、产气量好,产生沼气作燃料,实现产能增效,减少污染。The utility model combines physics and biochemistry, and the advantages of the two complement each other. At the same time, the high-efficiency anaerobicity is combined with the wetland or the land. It can be used as fuel to increase production capacity and reduce pollution.
本实用新型,还可有其它多种实施方式,在不背离本实用新型精神及其实质的情况下,熟悉本领域的技术人员可根据本实用新型作出各种相应的改变和变形。The present utility model can also have other various embodiments, and those skilled in the art can make various corresponding changes and deformations according to the present utility model without departing from the spirit and essence of the present utility model.
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922456700.2UCN211644987U (en) | 2019-12-30 | 2019-12-30 | New rural hilly area resident house domestic sewage purifies recycling system |
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922456700.2UCN211644987U (en) | 2019-12-30 | 2019-12-30 | New rural hilly area resident house domestic sewage purifies recycling system |
| Publication Number | Publication Date |
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| CN211644987Utrue CN211644987U (en) | 2020-10-09 |
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922456700.2UExpired - Fee RelatedCN211644987U (en) | 2019-12-30 | 2019-12-30 | New rural hilly area resident house domestic sewage purifies recycling system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114349261A (en)* | 2021-12-03 | 2022-04-15 | 中国建筑科学研究院有限公司 | Distributed courtyard ecological sewage and wastewater treatment system |
| CN118164646A (en)* | 2024-04-26 | 2024-06-11 | 广东中太环保科技有限公司 | Segment-channel type unpowered sewage treatment system |
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114349261A (en)* | 2021-12-03 | 2022-04-15 | 中国建筑科学研究院有限公司 | Distributed courtyard ecological sewage and wastewater treatment system |
| CN118164646A (en)* | 2024-04-26 | 2024-06-11 | 广东中太环保科技有限公司 | Segment-channel type unpowered sewage treatment system |
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| CF01 | Termination of patent right due to non-payment of annual fee | Granted publication date:20201009 |