CN204281506U - The removal device of pollution substance in a kind of domestic sewage in rural areas - Google Patents
The removal device of pollution substance in a kind of domestic sewage in rural areas Download PDFInfo
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- 239000010865 sewage Substances 0.000 title claims abstract description 71
- 239000000126 substance Substances 0.000 title description 4
- 238000005273 aeration Methods 0.000 claims abstract description 35
- 238000006243 chemical reaction Methods 0.000 claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 238000012856 packing Methods 0.000 claims abstract description 25
- 239000003344 environmental pollutant Substances 0.000 claims abstract description 24
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 24
- 231100000719 pollutant Toxicity 0.000 claims abstract description 24
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000011574 phosphorus Substances 0.000 claims abstract description 20
- 238000010521 absorption reaction Methods 0.000 claims abstract description 17
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- 230000001146 hypoxic effect Effects 0.000 claims abstract description 16
- 238000009826 distribution Methods 0.000 claims abstract description 4
- 238000007667 floating Methods 0.000 claims description 17
- 239000000945 filler Substances 0.000 claims description 13
- 238000005276 aerator Methods 0.000 claims description 7
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical class O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 6
- 238000012423 maintenance Methods 0.000 abstract description 8
- 241000196324 Embryophyta Species 0.000 description 36
- 238000000034 method Methods 0.000 description 17
- 239000010802 sludge Substances 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 238000000746 purification Methods 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
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Abstract
本实用新型公开了一种农村生活污水中污染物质的去除装置,包括顺序连通的三格化粪池、滤网、厌氧悬浮填料床反应池、低氧曝气池、竖流沉淀池、人工水生植物床和吸磷池,且三格化粪池、滤网、厌氧悬浮填料床反应池、低氧曝气池、竖流沉淀池并排设置在上部,而人工水生植物床和吸磷池则并排设置在下部,且所述的竖流沉淀池的出水口和人工水生植物床的进水口之间还设置有布水廊道。本实用新型对农村生活污水的处理效率极高,出水水质可以达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级A标准,同时占地面积小,投资省,运行管理维护简单,运行维护费用低。
The utility model discloses a device for removing pollutants in rural domestic sewage. Aquatic plant beds and phosphorus absorption tanks, and three compartment septic tanks, filter screens, anaerobic suspended packing bed reaction tanks, hypoxic aeration tanks, and vertical flow sedimentation tanks are arranged side by side in the upper part, while artificial aquatic plant beds and phosphorus absorption tanks Then they are arranged side by side at the lower part, and a water distribution corridor is also arranged between the water outlet of the vertical flow sedimentation tank and the water inlet of the artificial aquatic plant bed. The utility model has extremely high treatment efficiency for rural domestic sewage, and the effluent water quality can reach the first-class A standard in the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002). At the same time, it occupies a small area, saves investment and runs Simple management and maintenance, low operation and maintenance costs.
Description
技术领域 technical field
本实用新型涉及一种污染物质的去除装置,尤其是涉及一种农村生活污水中碳、氮、磷等污染物质的去除装置,属于污水处理技术领域。 The utility model relates to a device for removing pollutants, in particular to a device for removing pollutants such as carbon, nitrogen and phosphorus in rural domestic sewage, and belongs to the technical field of sewage treatment.
背景技术 Background technique
农村生活污水主要来自居民日常生活过程中(厨卫、洗浴、洗衣等)排放的污水,其中含有大量的油脂、微生物、杂物,具有氮、磷含量高,水质较为稳定、可生化性好的特点,一般人口规模在4000-6000人的农村城镇污水日产生量在500吨左右且污水排放峰谷差值明显。 Rural domestic sewage mainly comes from the sewage discharged during the daily life of residents (kitchen, bathing, laundry, etc.), which contains a large amount of oil, microorganisms, sundries, high nitrogen and phosphorus content, relatively stable water quality, and good biodegradability Features, the general population size of 4000-6000 rural urban sewage production is about 500 tons per day and the difference between the peak and valley of sewage discharge is obvious.
我国共有63.4万个行政村,目前全国农村每年有大量生活污水直接排放,根据2007年的全国第一次污染源普查结果显示,农村的生活污水、生活垃圾、畜禽养殖污染以及不合理施用化肥农药引发的面源污染等已经占到了环境污染的主导地位。农村面源污染主要来源于未经处理的生活污水无序排放,其中含有大量有机物质和微生物如不能得到有效处理将会污染地表水、地下水等造成农村环境整体恶化,因此怎样实现生活污水的无害化处理成了农村环境综合整治的关键。 There are a total of 634,000 administrative villages in my country. At present, a large amount of domestic sewage is directly discharged in the rural areas of the country every year. According to the results of the first national pollution source survey in 2007, rural domestic sewage, domestic garbage, livestock and poultry breeding pollution and unreasonable use of chemical fertilizers and pesticides The non-point source pollution caused by it has already accounted for the dominant position of environmental pollution. Rural non-point source pollution mainly comes from the disorderly discharge of untreated domestic sewage, which contains a large amount of organic matter and microorganisms. If it cannot be effectively treated, it will pollute surface water, groundwater, etc. and cause overall deterioration of the rural environment. Hazardous treatment has become the key to comprehensive improvement of rural environment.
污水处理模式分为两种,集中式污水处理模式和分散式污水处理模式。其中集中式污水处理模式适合于居住集中的城市和乡镇,而分散式污水处理模式则适合于居住较为分散的农村。我国现有分散式污水处理设施大多采用传统的接触氧化、活性污泥、人工湿地(植物)、无动力工艺等。有的仅采用单一曝气方式、能耗偏高;有的采用人工湿地等植物处理法,占地面积大,受气候影响,运行不稳定;有的设备集成度不高,工艺条件不易掌握和控制,处理后出水水质不易稳定,未考虑脱氮除磷。 There are two types of sewage treatment modes, centralized sewage treatment mode and decentralized sewage treatment mode. Among them, the centralized sewage treatment mode is suitable for the cities and towns where the residents are concentrated, while the decentralized sewage treatment mode is suitable for the scattered rural areas. Most of the existing decentralized sewage treatment facilities in my country use traditional contact oxidation, activated sludge, artificial wetland (plant), and non-powered processes. Some only use a single aeration method, and the energy consumption is relatively high; some use artificial wetland and other plant treatment methods, which cover a large area and are affected by the climate, and the operation is unstable; some equipment integration is not high, and the process conditions are not easy to master and Control, the effluent quality is not easy to stabilize after treatment, and nitrogen and phosphorus removal are not considered.
近年来,国内研究人员对生活污水进行了不少研究,现有文献中专利CN 203333445 U公开的一种阶梯式污水渗滤净化系统,在沿污水收集池下方的坡道上设置湿地渗滤净水系统,在每个湿地渗滤净水系统的四周和底部都设置防水隔离层,在每个湿地渗滤净水系统中都设置渗滤净水层,在渗滤净水层的上方覆盖有用于种植湿地植物的表土层,工艺简单、基建费用低、易管护、无污染,对农村生活污水去除效果好,种植的景观植物、药用植物、食用植物具有较高的观赏性和经济价值,很适合于山区农村净化。 In recent years, domestic researchers have conducted a lot of research on domestic sewage. In the existing literature, the patent CN 203333445 U discloses a stepped sewage infiltration purification system. Wetland infiltration water purification is set on the ramp along the bottom of the sewage collection tank. system, a waterproof isolation layer is set around and at the bottom of each wetland infiltration water purification system, and a percolation water purification layer is set in each wetland infiltration water purification system, and the top of the infiltration water purification layer is covered with a The surface soil layer for planting wetland plants has simple process, low infrastructure cost, easy management and maintenance, and no pollution. It has a good effect on removing rural domestic sewage. The planted landscape plants, medicinal plants, and edible plants have high ornamental and economic value. It is very suitable for rural purification in mountainous areas.
专利CN 101948214 A涉及到的一种处理农村生活污水的生态绿地处理工艺,该处理工艺主要由厌氧预处理步骤、人工湿地处理步骤和浅层生态塘好氧生物处理步骤组成,采用厌氧预处理,人工湿地,浅层生态塘组成一个生态绿地处理系统进行农村生活污水处理,具有处理效果好、可原地回用、投资低、系统运行费用低、维护简单、生态效益显著等特点。 Patent CN 101948214 A relates to an ecological green land treatment process for rural domestic sewage. The treatment process is mainly composed of anaerobic pretreatment steps, artificial wetland treatment steps and shallow ecological pond aerobic biological treatment steps. Treatment, artificial wetlands, and shallow ecological ponds form an ecological green land treatment system for rural domestic sewage treatment, which has the characteristics of good treatment effect, in-situ reuse, low investment, low system operating cost, simple maintenance, and remarkable ecological benefits.
专利CN 202226754 U涉及到的一体式农村污水处理系统,由污水收集池、生物处理系统、污泥池构成,所述污水收集池通过输送水泵与生物处理系统联通,生物处理系统包括缺氧池、厌氧池、好氧池、二沉池,污泥池置于缺氧池和厌氧池边上并通过气提装置与二沉池连接。该工艺具有技术性能稳定、处理效果好、投资省、占地少、操作简单、管理方便、使用寿命长、维护方便等优点,是专门根据农村生活污水的水质特点所设计的成套处理装置。 The integrated rural sewage treatment system involved in the patent CN 202226754 U is composed of a sewage collection pool, a biological treatment system, and a sludge pool. The sewage collection pool is connected to the biological treatment system through a delivery pump. Anaerobic tank, aerobic tank, secondary sedimentation tank, and sludge tank are placed beside the anoxic tank and anaerobic tank and connected with the secondary sedimentation tank through an air lift device. The process has the advantages of stable technical performance, good treatment effect, low investment, less land occupation, simple operation, convenient management, long service life and convenient maintenance. It is a complete treatment device specially designed according to the water quality characteristics of rural domestic sewage.
专利CN 202744423 U所描述的一体化生物接触氧化装置,其属于环境工程技术领域,该实用新型生物接触氧化法兼有活性污泥法的特点,出水水质好且稳定,生物接触氧化法容积负荷高,处理时间短且无污泥膨胀问题。 The integrated biological contact oxidation device described in the patent CN 202744423 U belongs to the field of environmental engineering technology. The utility model biological contact oxidation method has the characteristics of the activated sludge method, the effluent quality is good and stable, and the volume load of the biological contact oxidation method is high. , short processing time and no sludge bulking problem.
上述农村生活污水处理的工艺基本都具备了技术性能稳定、处理效果好、投资省、占地少、操作简单、管理方便、使用寿命长、维护方便等要求,但出水水质都只能达到国家一级标准。 The above-mentioned rural domestic sewage treatment processes basically meet the requirements of stable technical performance, good treatment effect, low investment, less land occupation, simple operation, convenient management, long service life, and convenient maintenance, etc., but the effluent quality can only meet the national standard level standard.
实用新型内容 Utility model content
本实用新型所要解决的技术问题是,提供一种生活污水处理后能够达到《城镇污水处理厂污染物排放标准》(GB18918-2002)中的一级A标准的农村生活污水中污染物质的去除装置。 The technical problem to be solved by the utility model is to provide a device for removing pollutants in rural domestic sewage that can reach the first-class A standard in the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB18918-2002) after domestic sewage treatment .
为解决上述技术问题,本实用新型采用的技术方案为: In order to solve the problems of the technologies described above, the technical solution adopted in the utility model is:
一种农村生活污水中污染物质的去除装置,其特征在于,包括顺序连通的三格化粪池、滤网、厌氧悬浮填料床反应池、低氧曝气池、竖流沉淀池、人工水生植物床和吸磷池,且三格化粪池、滤网、厌氧悬浮填料床反应池、低氧曝气池、竖流沉淀池并排设置在上部,而人工水生植物床和吸磷池则并排设置在下部,且所述的竖流沉淀池的出水口和人工水生植物床的进水口之间还设置有布水廊道。 A device for removing pollutants in rural domestic sewage, characterized in that it includes sequentially connected three-compartment septic tanks, filter screens, anaerobic suspension packed bed reaction tanks, hypoxic aeration tanks, vertical flow sedimentation tanks, artificial aquatic Plant beds and phosphorus absorption tanks, and three septic tanks, filter screens, anaerobic suspended packing bed reaction tanks, hypoxic aeration tanks, and vertical flow sedimentation tanks are arranged side by side on the upper part, while artificial aquatic plant beds and phosphorus absorption tanks are arranged side by side. They are arranged side by side at the lower part, and a water distribution corridor is also arranged between the water outlet of the vertical flow sedimentation tank and the water inlet of the artificial aquatic plant bed.
进一步,所述的厌氧悬浮填料床反应池的中部设置有折流挡板,所述的折流挡板的开口设置在厌氧悬浮填料床反应池的底部,而所述的厌氧悬浮填料床反应池进水口和出水口均设置在上部,整体形成厌氧悬浮填料床反应池的上流式结构。 Further, the middle part of the anaerobic suspended packing bed reaction tank is provided with a baffle, and the opening of the baffle is set at the bottom of the anaerobic suspended packing bed reaction tank, and the anaerobic suspended packing Both the water inlet and the water outlet of the bed reaction tank are arranged at the upper part, forming an upflow structure of the anaerobic suspended packing bed reaction tank as a whole.
且,所述的厌氧悬浮填料床反应池中的悬浮填料为多孔球形填料。 Moreover, the suspended filler in the anaerobic suspended filler bed reaction tank is a porous spherical filler.
而所述的低氧曝气池中的曝气装置为射流曝气器。且所述的射流曝气器的曝气方式为间歇式曝气。 The aeration device in the hypoxic aeration tank is a jet aerator. And the aeration mode of the jet aerator is intermittent aeration.
更进一步,所述的人工水生植物床包括木条浮岛框架、植物浮床和水生植物,所述的植物浮床架设在木条浮岛框架上,而所述的水生植物则设置在植物浮床上。且所述的植物浮床的材料为聚苯乙烯和塑料的混合物。 Further, the artificial aquatic plant bed includes a wooden floating island frame, a plant floating bed and aquatic plants, the plant floating bed is erected on the wooden floating island frame, and the aquatic plants are arranged on the plant floating bed. And the material of the plant floating bed is a mixture of polystyrene and plastic.
此外,所述的吸磷池中的填料为改性沸石。 In addition, the filler in the phosphorus absorption pool is modified zeolite.
利用上述的农村生活污水中污染物质的去除装置进行农村生活污水中污染物质的去除方法,其特征在于,包括以下步骤: The method for removing pollutants in rural domestic sewage using the above-mentioned device for removing pollutants in rural domestic sewage is characterized in that it includes the following steps:
(1)将生活污水收集后首先排入三格化粪池,生活污水经三格化粪池处理后经滤网拦截大的悬浮颗粒污染物,然后进入厌氧悬浮填料床反应池进行预处理; (1) After the domestic sewage is collected, it is first discharged into the three-compartment septic tank. After the domestic sewage is treated in the three-compartment septic tank, the large suspended particle pollutants are intercepted by the filter screen, and then enters the anaerobic suspended packing bed reaction tank for pretreatment ;
(2)利用厌氧悬浮填料床反应池中附着在悬浮填料上的厌氧菌的代谢功能,将生活污水中的有机物降解,厌氧悬浮填料床水力停留时间为5-6h; (2) Utilize the metabolic function of anaerobic bacteria attached to the suspended packing in the anaerobic suspended packing bed reaction tank to degrade the organic matter in domestic sewage, and the hydraulic retention time of the anaerobic suspended packing bed is 5-6h;
(3)厌氧悬浮填料床反应池出水后进入低氧曝气池进行生化反应,进一步去除污水中的有机物,低氧曝气池的曝气装置为射流曝气器,且采取间歇式曝气方式,低氧曝气池的水力停留时间为2-3h; (3) The water from the anaerobic suspended packed bed reaction tank enters the low-oxygen aeration tank for biochemical reaction to further remove organic matter in the sewage. The aeration device of the low-oxygen aeration tank is a jet aerator, and intermittent aeration is adopted method, the hydraulic retention time of the hypoxic aeration tank is 2-3h;
(4)低氧曝气池出水后进入竖流式沉淀池去除悬浮污泥,然后进入人工水生植物床,利用水生植物根系的吸收作用进一步降低污水中N、P指标; (4) After effluent from the hypoxic aeration tank enters the vertical flow sedimentation tank to remove suspended sludge, then enters the artificial aquatic plant bed, and further reduces the N and P indicators in the sewage by using the absorption of the roots of the aquatic plants;
(5)人工水生植物床的出水进入吸磷池,吸磷池采用改性沸石作为填料,吸附污水中残余磷,经过吸磷池的出水达到国标一级A标准后排入周围水体,其中所述的国标一级A标准为《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级A标准。 (5) The effluent from the artificial aquatic plant bed enters the phosphorus absorption pool. The phosphorus absorption pool uses modified zeolite as filler to absorb residual phosphorus in the sewage. The first-class A standard of the national standard is the first-class A standard in the "Pollutant Discharge Standard for Urban Sewage Treatment Plants" (GB 18918-2002).
本实用新型的有益效果为:本实用新型所述的厌氧悬浮填料床反应池可以将污水中难生物降解物质转变为易生物降解物质,有效提高了农村生活污水处理效率;而低氧曝气池不需要连续曝气,降低了装置长期运转所需费用;且利用人工水生植物床进一步净化污水中的N、P的指标;此外,本实用新型对农村生活污水的处理效率极高,出水水质可以达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级A标准,同时占地面积小,投资省,运行管理维护简单,运行维护费用低。 The beneficial effects of the utility model are: the anaerobic suspension packing bed reaction pool described in the utility model can convert the refractory biodegradable substances in the sewage into easily biodegradable substances, effectively improving the efficiency of rural domestic sewage treatment; and the low-oxygen aeration The pool does not require continuous aeration, which reduces the cost required for long-term operation of the device; and the artificial aquatic plant bed is used to further purify the N and P indicators in the sewage; in addition, the utility model has a very high treatment efficiency for rural domestic sewage, and the effluent water quality It can meet the first-class A standard in the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002), and at the same time occupies a small area, saves investment, simple operation management and maintenance, and low operation and maintenance costs.
附图说明 Description of drawings
图1为本实用新型一实施例的工艺流程图; Fig. 1 is the process flow chart of an embodiment of the utility model;
图2为本实用新型一实施例的平面布置图。 Fig. 2 is a plane layout diagram of an embodiment of the utility model.
图中主要附图标记含义为: The meanings of the main reference signs in the figure are:
1、三格化粪池 2、滤网 3、厌氧悬浮填料床反应池 4、低氧曝气池 1. Three-compartment septic tank 2. Filter screen 3. Anaerobic suspended packing bed reaction tank 4. Hypoxic aeration tank
5、竖流沉淀池 6、人工水生植物床 7、吸磷池。 5. Vertical flow sedimentation tank 6. Artificial aquatic plant bed 7. Phosphorus absorption pool.
具体实施方式 Detailed ways
下面结合附图和具体实施例详细说明本实用新型。 Below in conjunction with accompanying drawing and specific embodiment describe the utility model in detail.
图1为本实用新型一实施例的工艺流程图;图2为本实用新型一实施例的平面布置图。 Fig. 1 is a process flow diagram of an embodiment of the utility model; Fig. 2 is a plane layout diagram of an embodiment of the utility model.
如图1和图2所示:农村生活污水中污染物质的去除装置,包括顺序连通的三格化粪池1、滤网2、厌氧悬浮填料床反应池3、低氧曝气池4、竖流沉淀池5、人工水生植物床6和吸磷池7,且三格化粪池1、滤网2、厌氧悬浮填料床反应池3、低氧曝气池4、竖流沉淀池5并排设置在上部,而人工水生植物床6和吸磷池7则并排设置在下部,且所述的竖流沉淀池5的出水口和人工水生植物床6的进水口之间还设置有布水廊道。 As shown in Figure 1 and Figure 2: the removal device of pollutants in rural domestic sewage, including three-compartment septic tank 1, filter screen 2, anaerobic suspended packing bed reaction tank 3, low-oxygen aeration tank 4, Vertical flow sedimentation tank 5, artificial aquatic plant bed 6 and phosphorus absorption tank 7, and three-compartment septic tank 1, filter screen 2, anaerobic suspension packing bed reaction tank 3, hypoxic aeration tank 4, vertical flow sedimentation tank 5 Arranged side by side at the upper part, while the artificial aquatic plant bed 6 and the phosphorus absorption pool 7 are arranged side by side at the lower part, and a water distribution system is also arranged between the water outlet of the vertical flow sedimentation tank 5 and the water inlet of the artificial aquatic plant bed 6. corridor.
且,在本实施方式中,厌氧悬浮填料床反应池3的中部设置有折流挡板,所述的折流挡板的开口设置在厌氧悬浮填料床反应池3的底部,而所述的厌氧悬浮填料床反应池3进水口和出水口均设置在上部,整体形成厌氧悬浮填料床反应池3的上流式结构,且所述的厌氧悬浮填料床反应池3中的悬浮填料为多孔球形填料。 And, in this embodiment, the middle part of anaerobic suspended packed bed reaction tank 3 is provided with baffle plate, and the opening of described baffle plate is arranged on the bottom of anaerobic suspended packed bed reaction tank 3, and the described The water inlet and outlet of the anaerobic suspended packed bed reaction tank 3 are all arranged on the upper part, forming an upflow structure of the anaerobic suspended packed bed reaction tank 3 as a whole, and the suspended filler in the anaerobic suspended packed bed reaction tank 3 For porous spherical filler.
而所述的低氧曝气池4中的曝气装置为射流曝气器,且所述的射流曝气器的曝气方式为间歇式曝气。 The aeration device in the hypoxic aeration tank 4 is a jet aerator, and the aeration mode of the jet aerator is intermittent aeration.
此外,所述的人工水生植物床6包括木条浮岛框架、植物浮床和水生植物,所述的植物浮床架设在木条浮岛框架上,而所述的水生植物则设置在植物浮床上,且所述的植物浮床的材料为聚苯乙烯和塑料的混合物。 In addition, the artificial aquatic plant bed 6 includes a wooden floating island frame, a plant floating bed and aquatic plants, the plant floating bed is erected on the wooden floating island frame, and the aquatic plants are arranged on the plant floating bed, And the material of the plant floating bed is a mixture of polystyrene and plastic.
而所述的吸磷池中的填料为改性沸石。 And the filler in the phosphorus absorption pool is modified zeolite.
实施例1:Example 1:
采用上述的农村生活污水中污染物质的去除装置处理某村庄产生的生活污水,生活污水的产生量为50吨/日,要求处理达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级A标准后再排入周围水体。 The above-mentioned device for removing pollutants in rural domestic sewage is used to treat domestic sewage produced in a certain village. The production of domestic sewage is 50 tons per day, and the treatment is required to meet the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002) It is discharged into the surrounding water body after meeting the first-level A standard.
生活污水首先进入三格化粪池1,生活污水经三级化粪池1处理后经过滤网2拦截大的悬浮颗粒污染物,然后进入厌氧悬浮填料床反应池3进行预处理; The domestic sewage first enters the three-compartment septic tank 1, and the domestic sewage is treated by the three-stage septic tank 1, and then passes through the filter screen 2 to intercept large suspended particle pollutants, and then enters the anaerobic suspended packing bed reaction tank 3 for pretreatment;
厌氧悬浮填料床反应池3采用上流式结构,悬浮填料采用多孔球型填料,厌氧悬浮填料床水力停留时间控制在5h; The anaerobic suspended packing bed reaction tank 3 adopts an upflow structure, the suspended packing adopts porous spherical packing, and the hydraulic retention time of the anaerobic suspended packing bed is controlled at 5 hours;
厌氧悬浮填料床反应池3出水进入低氧曝气池4进行生化反应,进一步去除污水中的有机物,低氧曝气池4采取间歇式曝气方式,曝气装置采用射流曝气器,低氧曝气池的水力停留时间为3h; The effluent from the anaerobic suspended packed bed reaction tank 3 enters the hypoxic aeration tank 4 for biochemical reaction to further remove organic matter in the sewage. The hydraulic retention time of the oxygen aeration tank is 3h;
低氧曝气池4出水进入竖流式沉淀池5去除悬浮污泥,然后进入人工水生植物床6,利用植物根系的吸收作用进一步降低污水中N、P指标; The effluent from the hypoxic aeration tank 4 enters the vertical flow sedimentation tank 5 to remove suspended sludge, and then enters the artificial aquatic plant bed 6 to further reduce the N and P indicators in the sewage by the absorption of the plant root system;
人工水生植物床6出水进入吸磷池7,吸磷池7采用改性沸石作为填料,吸附污水中残余磷,吸磷池7的出水达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级A标准后排入周围水体。 The effluent from the artificial aquatic plant bed 6 enters the phosphorus-absorbing pool 7, which uses modified zeolite as a filler to absorb residual phosphorus in the sewage. 2002) and discharged into the surrounding water body.
实施例2:Example 2:
某村庄生活污水的产生量为150吨/日,生活污水首先进入三格化粪池1,生活污水经三格化粪池1处理后经过滤网2拦截大的悬浮颗粒污染物,然后进入厌氧悬浮填料床反应池3进行预处理; The production of domestic sewage in a certain village is 150 tons per day. The domestic sewage first enters the three-compartment septic tank 1, and after being treated in the three-compartment septic tank 1, the domestic sewage passes through the filter screen 2 to intercept large suspended particle pollutants, and then enters the exhaust Oxygen suspended packed bed reaction tank 3 is pretreated;
厌氧悬浮填料床反应池3采用上流式结构,悬浮填料采用多孔球型填料,厌氧悬浮填料床水力停留时间控制为5.5h; The anaerobic suspended packing bed reaction tank 3 adopts an upflow structure, the suspended packing adopts porous spherical packing, and the hydraulic retention time of the anaerobic suspended packing bed is controlled to 5.5h;
厌氧悬浮填料床反应池3出水进入低氧曝气池4进行生化反应,进一步去除污水中的有机物,低氧曝气池4采取间歇式曝气方式,曝气装置采用射流曝气器,低氧曝气池4的水力停留时间为2.5h; The effluent from the anaerobic suspended packed bed reaction tank 3 enters the hypoxic aeration tank 4 for biochemical reaction to further remove organic matter in the sewage. The hydraulic retention time of oxygen aeration tank 4 is 2.5h;
低氧曝气池4出水进入竖流式沉淀池5去除悬浮污泥,然后进入人工水生植物床6,利用植物根系的吸收作用进一步降低污水中N、P指标; The effluent from the hypoxic aeration tank 4 enters the vertical flow sedimentation tank 5 to remove suspended sludge, and then enters the artificial aquatic plant bed 6 to further reduce the N and P indicators in the sewage by the absorption of the plant root system;
人工水生植物床6出水进入吸磷池7,吸磷池7采用改性沸石作为填料,吸附污水中残余磷,吸磷池7的出水达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级A标准。 The effluent from the artificial aquatic plant bed 6 enters the phosphorus-absorbing pool 7, which uses modified zeolite as a filler to absorb residual phosphorus in the sewage. 2002) in the Class A standard.
本实用新型按照上述实施例进行了说明应当理解,上述实施例不以任何形式限定本实用新型,凡采用等同替换或等效变换方式所获得的技术方案,均落在本实用新型的保护范围之内。 The utility model has been described according to the above-mentioned embodiments. It should be understood that the above-mentioned embodiments do not limit the present utility model in any form, and all technical solutions obtained by adopting equivalent replacement or equivalent transformation methods all fall within the protection scope of the present utility model. Inside.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104355490A (en) * | 2014-11-06 | 2015-02-18 | 台州学院 | Device and method for removing pollutants in rural domestic sewage |
CN105585210A (en) * | 2015-12-23 | 2016-05-18 | 常熟理工学院 | Novel technology for treating aquaculture wastewater of fungus-aquatic plant symbiotic system |
CN110282815A (en) * | 2019-06-11 | 2019-09-27 | 芜湖浩睿环保科技有限公司 | A kind of rural sewage ecological processing system and technique coupling modern cultivation technique |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104355490A (en) * | 2014-11-06 | 2015-02-18 | 台州学院 | Device and method for removing pollutants in rural domestic sewage |
CN104355490B (en) * | 2014-11-06 | 2016-01-06 | 台州学院 | The removal device of pollution substance and minimizing technology in a kind of domestic sewage in rural areas |
CN105585210A (en) * | 2015-12-23 | 2016-05-18 | 常熟理工学院 | Novel technology for treating aquaculture wastewater of fungus-aquatic plant symbiotic system |
CN110282815A (en) * | 2019-06-11 | 2019-09-27 | 芜湖浩睿环保科技有限公司 | A kind of rural sewage ecological processing system and technique coupling modern cultivation technique |
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