CN102701448B - Rural domestic sewage reutilization treatment device - Google Patents
Rural domestic sewage reutilization treatment device Download PDFInfo
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- 239000010865 sewage Substances 0.000 title claims abstract description 66
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 42
- 238000010992 reflux Methods 0.000 claims abstract description 4
- 238000005273 aeration Methods 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 238000012545 processing Methods 0.000 claims description 16
- 239000000463 material Substances 0.000 claims description 10
- 238000004064 recycling Methods 0.000 claims description 7
- 239000010802 sludge Substances 0.000 claims description 7
- 239000011449 brick Substances 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 238000012856 packing Methods 0.000 claims 2
- 230000000630 rising effect Effects 0.000 claims 2
- 241000216843 Ursus arctos horribilis Species 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 16
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 8
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 6
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 6
- 239000011574 phosphorus Substances 0.000 abstract description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 abstract description 4
- 229910052799 carbon Inorganic materials 0.000 abstract description 4
- 239000005416 organic matter Substances 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 58
- 241000196324 Embryophyta Species 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 239000000945 filler Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002054 inoculum Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 235000005273 Canna coccinea Nutrition 0.000 description 1
- 240000008555 Canna flaccida Species 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000001932 seasonal effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
本发明公开了一种农村生活污水资源化处理装置,包括沼气池、格栅预处理单元、地埋式厌氧池、好氧生物滤塔以及潜流人工湿地。沼气池产生的甲烷在厌氧条件下可进行反硝化和硫酸盐还原,利用甲烷作为碳源强化厌氧生化处理,甲烷的增温作用可提高处理效率,塔式生物滤池后设置回流,提高脱氮率。采用本发明可有效去除有机物并高效脱除氮磷,占地面积小,运行成本低,因地制宜,实现了废物资源化利用。
The invention discloses a rural domestic sewage resource treatment device, which comprises a methane pool, a grid pretreatment unit, a buried anaerobic pool, an aerobic biological filter tower and a subsurface artificial wetland. The methane produced by the biogas digester can be denitrified and sulfate reduced under anaerobic conditions. Using methane as a carbon source to strengthen anaerobic biochemical treatment, the temperature increase of methane can improve the treatment efficiency, and the reflux after the tower biofilter can improve Nitrogen removal rate. The invention can effectively remove organic matter and efficiently remove nitrogen and phosphorus, has small footprint, low operating cost, adapts measures to local conditions, and realizes waste resource utilization.
Description
技术领域 technical field
本发明涉环境工程领域,尤其是涉及一种农村生活污水资源化处理装置。 The invention relates to the field of environmental engineering, in particular to a device for treating rural domestic sewage as a resource.
背景技术 Background technique
近年来,随着我国农村的发展和农村人民生活水平的迅速提高,农村生活污水的排放量不断增加,农村生活污水已成为仅次于城市污水的又一严重污染源。与此同时,由于农村污染源分散且面广,污水量少,并且受自然条件限制,农村生活污水具有分散、不易收集等特点,大范围的铺设污水收集管网较为困难,使得农村生活污水不能纳入大型集中污水厂集中进行处理,农村生活污水的无害化处理率很低,只能因地制宜地寻求高效率低能耗的较为适合的污水处理方法及工艺。 In recent years, with the development of my country's rural areas and the rapid improvement of rural people's living standards, the discharge of rural domestic sewage has continued to increase, and rural domestic sewage has become another serious pollution source next to urban sewage. At the same time, due to the scattered and wide-ranging pollution sources in rural areas, the small amount of sewage, and limited by natural conditions, rural domestic sewage is scattered and difficult to collect. It is difficult to lay sewage collection pipes on a large scale, making rural domestic sewage not included Large-scale centralized sewage plants conduct centralized treatment, and the harmless treatment rate of rural domestic sewage is very low. We can only find more suitable sewage treatment methods and processes with high efficiency and low energy consumption according to local conditions.
目前农村生活污水处理常用的工艺主要有生化处理系统(厌氧、缺氧、好氧)和生态处理系统,主要以无动力厌氧生物处理、土地处理、人工湿地工艺为主。这一系列方法存在着停留时间长、冬季处理效果差、废水中氮磷的去除效果不佳等弊端。比如单纯的生化处理系统存在着运行成本高,难以适应农村地区经济状况,而生态处理技术也存在着冬季等季节性处理效果差的情况。因此,现有农村生活污水处理技术不足、氮磷排放过多是导致目前农村生活污水富营养化日趋严重的直接诱因。 At present, the commonly used processes for rural domestic sewage treatment mainly include biochemical treatment systems (anaerobic, anoxic, aerobic) and ecological treatment systems, mainly unpowered anaerobic biological treatment, land treatment, and constructed wetland processes. This series of methods has disadvantages such as long residence time, poor treatment effect in winter, and poor removal effect of nitrogen and phosphorus in wastewater. For example, the simple biochemical treatment system has high operating costs and is difficult to adapt to the economic conditions in rural areas, and the ecological treatment technology also has poor seasonal treatment effects in winter. Therefore, the lack of existing rural domestic sewage treatment technology and excessive nitrogen and phosphorus discharge are the direct causes of the increasingly serious eutrophication of rural domestic sewage.
为了适应农村地区的特点,农村生活污水处理的发展方向是强化厌氧生化处理系统,或采用将曝气充氧与污水提升、混合液回流相结合等方式,同时充分利用生态处理系统,以充分降低运行成本并降低维护管理难度。同时,最新研究表明:在厌氧条件下,甲烷作为碳源进行硝酸盐脱氮以及硫酸盐还原是可行的,并可保持较高的脱氮率。 In order to adapt to the characteristics of rural areas, the development direction of rural domestic sewage treatment is to strengthen the anaerobic biochemical treatment system, or to combine aeration and oxygenation with sewage lifting, mixed liquid return, etc., and make full use of the ecological treatment system to fully Reduce operating costs and reduce the difficulty of maintenance management. At the same time, the latest research shows that under anaerobic conditions, it is feasible to use methane as a carbon source for nitrate denitrification and sulfate reduction, and can maintain a high denitrification rate.
发明内容 Contents of the invention
本发明的目的在于克服现有的不足,解决农村生活污水处理效果差,运行费用高的问题,提供一种高效低耗,治污效率高,环境效益好的农村生活污水资源化处理装置。 The purpose of the present invention is to overcome the existing deficiencies, solve the problems of poor rural domestic sewage treatment effect and high operating costs, and provide a rural domestic sewage resource treatment device with high efficiency, low consumption, high pollution control efficiency and good environmental benefits.
本发明为实现上述目的采用如下技术的方案: The present invention adopts the scheme of following technology for realizing above-mentioned purpose:
一种农村生活污水资源化处理装置,包括沼气池、储气罐、气压调节器、气体循环泵、气体管道、格栅处理单元、地埋式厌氧池、塔式生物滤池、潜流人工湿地、提升泵、流量计、回流泵、污水管道、进水管、曝气装置、生物填料、湿地植物、出水管;所述沼气池与储气罐之间、储气罐与气压调节器之间、气压调节器与气体循环泵之间均通过气体管道连接;所述格栅处理单元和地埋式厌氧池之间、地埋式厌氧池和塔式生物滤池之间、塔式生物滤池和潜流人工湿地之间均通过污水管道连接;所述进水管设于格栅处理单元的前端;所述曝气装置设于地埋式厌氧池内的底部,且曝气装置通过气体管道与气体循环泵连接;所述气压调节器与气体循环泵之间的气体管道上设有气体支管,且该气体支管与地埋式厌氧池相连;所述提升泵设于地埋式厌氧池和塔式生物滤池之间的污水管道上;所述流量计设于塔式生物滤池与潜流人工湿地之间的污水管道上;塔式生物滤池与流量计之间的污水管道上设有污水支管,该污水支管与地埋式厌氧池的底部相连,且回流泵设于污水支管上;所述湿地植物设于潜流人工湿地上,所述出水管设于潜流人工湿地的尾端。 A rural domestic sewage resource treatment device, including a biogas digester, a gas storage tank, a gas pressure regulator, a gas circulation pump, a gas pipeline, a grid treatment unit, a buried anaerobic tank, a tower biofilter, and a subsurface artificial wetland , lifting pump, flow meter, return pump, sewage pipeline, water inlet pipe, aeration device, biological filler, wetland plants, water outlet pipe; between the biogas digester and the gas storage tank, between the gas storage tank and the air pressure regulator, The gas pressure regulator and the gas circulation pump are connected through gas pipelines; between the grid treatment unit and the buried anaerobic tank, between the buried anaerobic tank and the tower biofilter, and between the tower biofilter It is connected with the subsurface constructed wetland through sewage pipes; the water inlet pipe is set at the front end of the grid treatment unit; the aeration device is set at the bottom of the buried anaerobic pool, and the aeration device is connected with the gas The circulation pump is connected; the gas pipeline between the air pressure regulator and the gas circulation pump is provided with a gas branch pipe, and the gas branch pipe is connected with the buried anaerobic tank; the lift pump is located at the buried anaerobic tank and on the sewage pipeline between the tower biofilter; the flow meter is arranged on the sewage pipeline between the tower biofilter and the subsurface flow constructed wetland; on the sewage pipeline between the tower biofilter and the flow meter The sewage branch pipe is connected to the bottom of the buried anaerobic tank, and the return pump is arranged on the sewage branch pipe; the wetland plants are arranged on the subsurface flow artificial wetland, and the outlet pipe is arranged at the end of the subsurface flow artificial wetland.
地埋式厌氧池为全地下式,采用砖砌或混凝土结构,并设有用于清理的人孔。 The buried anaerobic tank is fully underground, adopts brick or concrete structure, and has a manhole for cleaning.
储气罐中的甲烷产自于沼气池,农村往往建有沼气池,可将产生的一部分甲烷储存于气罐中,待使用时通过气压调节器控制流量; The methane in the gas storage tank is produced from a biogas digester. There are often biogas digesters in rural areas, and a part of the methane generated can be stored in the gas tank, and the flow is controlled by a pressure regulator when it is used;
曝气装置曝气的气体为甲烷。地埋式厌氧池利用曝气装置、气体循环泵以及气体管道通过循环甲烷的方式进行曝气。 The aeration gas of the aeration device is methane. The buried anaerobic tank uses an aeration device, a gas circulation pump and a gas pipeline to aerate by circulating methane.
地埋式厌氧池中水力停留时间为20~30小时,其接种污泥来自当地污水处理厂厌氧活性污泥。 The hydraulic retention time in the buried anaerobic tank is 20-30 hours, and the inoculum sludge comes from the anaerobic activated sludge of the local sewage treatment plant.
格栅处理单元为地下式,其进水处安装细格栅,细格栅倾斜角度为40-60度,栅条间隙为20-40毫米。 The grid processing unit is underground, and a fine grid is installed at the water inlet. The inclination angle of the fine grid is 40-60 degrees, and the gap between the grid bars is 20-40 mm.
所述塔式生物滤池内的生物填料为微孔生物滤料,为使污水能与微孔生物滤料发生接触且以一定速率流经微孔生物滤料,同时保持净化效果,堆积密度为600~1200g/cm3,微孔生物滤料的粒径为25~40毫米。 The biological filler in the tower biofilter is a microporous biological filter material. In order to make the sewage contact with the microporous biological filter material and flow through the microporous biological filter material at a certain rate, while maintaining the purification effect, the bulk density is 600~1200g/cm3, the particle size of microporous biological filter material is 25~40 mm.
与现有技术相比,本发明具有以下有益效果: Compared with the prior art, the present invention has the following beneficial effects:
1、 该装置设有沼气池、格栅预处理单元、地埋式厌氧池、好氧生物滤塔、潜流人工湿地,可高效去除农村生活污水中的有机物以及氮磷营养物质。 1. The device is equipped with biogas digesters, grid pretreatment units, buried anaerobic tanks, aerobic biological filter towers, and subsurface constructed wetlands, which can efficiently remove organic matter and nitrogen and phosphorus nutrients in rural domestic sewage.
2、 格栅处理单元以及地埋式厌氧池采用地下式,有利于冬季保温,减轻气温的影响。 2. The grille treatment unit and the buried anaerobic pool adopt the underground type, which is conducive to keeping warm in winter and reducing the impact of temperature.
3、 沼气池产生的甲烷在厌氧条件下可进行反硝化和硫酸盐还原,利用甲烷作为碳源强化厌氧生化处理,并保持较高的脱氮率,因地制宜,实现废物资源化利用。 3. The methane produced by the biogas digester can be denitrified and sulfate reduced under anaerobic conditions. Using methane as a carbon source to strengthen anaerobic biochemical treatment and maintain a high denitrification rate can be adapted to local conditions to realize waste resource utilization.
4、 由于甲烷具有增温作用,可同时提高地埋式厌氧池以及塔式生物滤池的处理效率,效果显著。 4. Because methane has a warming effect, it can simultaneously improve the treatment efficiency of the buried anaerobic tank and the tower biological filter, and the effect is remarkable.
5、 本发明设置滤后混合液回流,可有效提高COD、氨氮以及总氮的去除率,保证出水水质以及系统稳定运行。 5. The invention sets the reflux of the filtered mixed liquid, which can effectively improve the removal rate of COD, ammonia nitrogen and total nitrogen, and ensure the quality of effluent water and the stable operation of the system.
6、 该装置采用自动化控制,操作管理方便,易于维护,只需安排专人定期对格栅出口处的杂物进行清理,定期对水泵、控制系统等进行检查与维护。 6. The device adopts automatic control, which is convenient for operation and management, and easy for maintenance. It only needs to arrange special personnel to regularly clean up the sundries at the grill outlet, and regularly check and maintain the water pump and control system.
附图说明 Description of drawings
图1是本发明农村生活污水资源化处理装置的结构示意图。 Fig. 1 is a schematic structural view of the rural domestic sewage recycling treatment device of the present invention.
图中:1为沼气池、2为储气罐、3为气压调节器、4为气体循环泵、5为气体管道、6为格栅处理单元、7为地埋式厌氧池、8为塔式生物滤池、9为潜流人工湿地、10为提升泵、11为流量计、12为回流泵、13为污水管道、14为进水管、15为曝气装置、16为生物填料、17为湿地植物、18为出水管。 In the figure: 1 is a biogas digester, 2 is a gas storage tank, 3 is a gas pressure regulator, 4 is a gas circulation pump, 5 is a gas pipeline, 6 is a grid processing unit, 7 is an underground anaerobic tank, and 8 is a tower type biological filter, 9 is subsurface constructed wetland, 10 is lift pump, 11 is flow meter, 12 is return pump, 13 is sewage pipe, 14 is water inlet pipe, 15 is aeration device, 16 is biological filler, 17 is wetland Plant, 18 are outlet pipes.
具体实施方式 Detailed ways
下面结合附图对本发明的实施例做进一步的详细描述。 Embodiments of the present invention will be further described in detail below in conjunction with the accompanying drawings.
实施例1Example 1
一种农村生活污水资源化处理装置,包括沼气池1、储气罐2、气压调节器3、气体循环泵4、气体管道5、格栅处理单元6、地埋式厌氧池7、塔式生物滤池8、潜流人工湿地9、提升泵10、流量计11、回流泵12、污水管道13、进水管14、曝气装置15、生物填料16、湿地植物17、出水管18;沼气池1与储气罐2之间、储气罐2与气压调节器3之间、气压调节器3与气体循环泵4之间均通过气体管道连接;格栅处理单元6和地埋式厌氧池7之间、地埋式厌氧池7和塔式生物滤池8之间、塔式生物滤池8和潜流人工湿地9之间均通过污水管道13连接;进水管14设于格栅处理单元6的前端;曝气装置15设于地埋式厌氧池7内的底部,且曝气装置15通过气体管道与气体循环泵4连接;气压调节器3与气体循环泵4之间的气体管道上设有气体支管,且该气体支管与地埋式厌氧池7相连;提升泵10设于地埋式厌氧池7和塔式生物滤池8之间的污水管道上;流量计11设于塔式生物滤池8与潜流人工湿地9之间的污水管道上;塔式生物滤池8与流量计11之间的污水管道上设有污水支管,该污水支管与地埋式厌氧池7的底部相连,且回流泵12设于污水支管上;湿地植物17设于潜流人工湿地9上,出水管18设于潜流人工湿地9的尾端。
A rural domestic sewage resource treatment device, including a biogas digester 1, a gas storage tank 2, an air pressure regulator 3, a gas circulation pump 4, a
地埋式厌氧池7为全地下式,采用砖砌或混凝土结构,并设有用于清理的人孔。
The buried
储气罐2中的甲烷产自于沼气池1,并通过气压调节器3控制流量; The methane in the gas storage tank 2 is produced from the biogas digester 1, and the flow is controlled by the air pressure regulator 3;
曝气装置15曝气的气体为甲烷。地埋式厌氧池7利用曝气装置15、气体循环泵4以及气体管道5通过循环甲烷的方式进行曝气。
The aeration gas of the
地埋式厌氧池7中水力停留时间为20~30小时,其接种污泥来自当地污水处理厂厌氧活性污泥。
The hydraulic retention time in the buried
格栅处理单元6为地下式,其进水处安装细格栅,细格栅倾斜角度为40-60度,栅条间隙为20-40毫米。
The
塔式生物滤池8内的生物填料16为微孔生物滤料,堆积密度为600~1200g/cm3,微孔生物滤料的粒径为25~40毫米。
The
实施例2Example 2
一种农村生活污水资源化处理装置,包括沼气池1、储气罐2、气压调节器3、气体循环泵4、气体管道5、格栅处理单元6、地埋式厌氧池7、塔式生物滤池8、潜流人工湿地9、提升泵10、流量计11、回流泵12、污水管道13、进水管14、曝气装置15、生物填料16、湿地植物17、出水管18;沼气池1与储气罐2之间、储气罐2与气压调节器3之间、气压调节器3与气体循环泵4之间均通过气体管道连接;格栅处理单元6和地埋式厌氧池7之间、地埋式厌氧池7和塔式生物滤池8之间、塔式生物滤池8和潜流人工湿地9之间均通过污水管道13连接;格栅处理单元6的前端设有进水管14;曝气装置15设于地埋式厌氧池7内的底部;且曝气装置15通过气体管道与气体循环泵4连接;气压调节器3与气体循环泵4之间的气体管道上设有气体支管,且该气体支管与地埋式厌氧池7相连;提升泵10设于地埋式厌氧池7和塔式生物滤池8之间的污水管道上;塔式生物滤池8与潜流人工湿地9之间的污水管道上设有流量计11;塔式生物滤池8与流量计11之间的污水管道上设有污水支管,该污水支管与地埋式厌氧池7的底部相连,且污水支管上设有回流泵12;湿地植物17设于潜流人工湿地9上,且潜流人工湿地9的尾端设有出水管18。
A rural domestic sewage resource treatment device, including a biogas digester 1, a gas storage tank 2, an air pressure regulator 3, a gas circulation pump 4, a
地埋式厌氧池7为全地下式,采用砖砌或混凝土结构,并设有用于清理的人孔。
The buried
储气罐2中的甲烷产自于沼气池1,并通过气压调节器3控制流量; The methane in the gas storage tank 2 is produced from the biogas digester 1, and the flow is controlled by the air pressure regulator 3;
地埋式厌氧池7利用曝气装置15、气体循环泵4以及气体管道5通过循环甲烷的方式进行曝气,水力停留时间为24小时,其接种污泥来自当地污水处理厂厌氧活性污泥。
The buried
格栅处理单元6为地下式,其进水处安装细格栅,细格栅倾斜角度为60度,栅条间隙为40毫米。
The
塔式生物滤池8内的生物填料16为微孔生物滤料,堆积密度为1000g/cm3,微孔生物滤料的粒径为40毫米。
The
农村生活污水处理采用本装置。实际工作时,当农村生活污水进水CODcr浓度为350mg/L,NH3-N浓度为32mg/L,TN浓度为59mg/L,TP浓度为3mg/L时,待处理污水从进水管(14)进入,经过格栅处理单元(6)的预处理后进入地埋式厌氧池(7),在厌氧菌作用下分解和去除水中有机物,同时利用甲烷为碳源进行反硝化和硫酸盐还原,通过循环甲烷的方式进行曝气,甲烷的曝气量为2L/h,停留24小时后,通过提升泵(10)污水进入塔式生物滤池(8)进一步去除有机物和氮磷,塔式生物滤池(8)的滤后水通过回流泵(12)回流至地埋式厌氧池(7),回流比为100%,待处理污水氮磷去除率较高、出水较为清澈时,停止回流,让塔式生物滤池(8)的出水进入潜流人工湿地(9)进一步除磷,同时对氮有一定去除,湿地植物(17)为美人蕉,潜流人工湿地(9)采用鹅卵石与高炉炉渣填充,污水最终由潜流人工湿地(9)尾端的出水管(18)流出,经该装置处理过后出水CODcr浓度为33mg/L,去除率为90.6%,NH3-N浓度为4mg/L,去除率为87.5%,TN浓度为9mg/L,去除率为84.7%,TP浓度为0.6mg/L,去除率为80.0%,处理出水达标排放。 This device is used for rural domestic sewage treatment. In actual work, when the concentration of CODcr in the rural domestic sewage is 350mg/L, the concentration of NH 3 -N is 32mg/L, the concentration of TN is 59mg/L, and the concentration of TP is 3mg/L, the sewage to be treated will flow from the water inlet pipe (14 ) into the buried anaerobic tank (7) after being pretreated by the grid treatment unit (6), where organic matter in the water is decomposed and removed under the action of anaerobic bacteria, and at the same time, methane is used as a carbon source for denitrification and sulfate Reduction, aeration is carried out by circulating methane. The aeration rate of methane is 2L/h. After staying for 24 hours, the sewage enters the tower biofilter (8) through the lift pump (10) to further remove organic matter and nitrogen and phosphorus. The tower The filtered water of the type biological filter (8) is returned to the buried anaerobic tank (7) through the return pump (12), and the return ratio is 100%. Stop the backflow, let the effluent from the tower biofilter (8) enter the subsurface constructed wetland (9) for further phosphorus removal, and at the same time remove nitrogen to a certain extent. The wetland plant (17) is canna, and the subsurface constructed wetland (9) uses pebbles and blast furnaces Filled with slag, the sewage finally flows out from the outlet pipe (18) at the end of the subsurface constructed wetland (9). After being treated by this device, the concentration of CODcr in the effluent is 33mg/L, the removal rate is 90.6%, and the concentration of NH 3 -N is 4mg/L. The removal rate is 87.5%, the TN concentration is 9mg/L, the removal rate is 84.7%, the TP concentration is 0.6mg/L, the removal rate is 80.0%, and the treated effluent meets the discharge standard.
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| CN103332788B (en) * | 2013-07-19 | 2015-04-08 | 环境保护部南京环境科学研究所 | Multi-stage anaerobic-aerobic combined nitrogen and phosphorus removing device and method for rural domestic sewage |
| CN103395937B (en) * | 2013-08-06 | 2014-12-10 | 环境保护部南京环境科学研究所 | Processing device and processing method applicable to high-ammonia-nitrogen agricultural wastewater |
| CN104926038B (en) * | 2015-06-17 | 2017-07-14 | 陕西省环境科学研究院 | A kind of biological and ecological composite handling arrangement for rural sewage treatment |
| CN206204102U (en) * | 2016-05-20 | 2017-05-31 | 高节义 | Urban Residential District sanitary sewage disposal zero-emission facility |
| CN106277562A (en) * | 2016-07-27 | 2017-01-04 | 宁海逸航环保科技有限公司 | The technological process of a kind of new village sewage disposal and method |
| WO2020000214A1 (en) * | 2018-06-26 | 2020-01-02 | 江苏宏大环保科技有限公司 | Wastewater recycling treatment apparatus |
| CN110683715A (en) * | 2019-10-30 | 2020-01-14 | 徐州工程学院 | A kind of high-efficiency treatment system for rural domestic sewage recycling |
| CN117902781A (en) * | 2024-03-07 | 2024-04-19 | 广西中冠智合环保技术有限公司 | Ecological water purification system for recycling village domestic sewage |
| CN118619459B (en) * | 2024-07-09 | 2025-06-17 | 中国电建市政建设集团有限公司 | A tailwater enhanced denitrification treatment method based on artificial wetland and artificial wetland system |
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