CN202658053U - Buried sewage treatment device - Google Patents

Buried sewage treatment device Download PDF

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CN202658053U
CN202658053U CN201220308081.8U CN201220308081U CN202658053U CN 202658053 U CN202658053 U CN 202658053U CN 201220308081 U CN201220308081 U CN 201220308081U CN 202658053 U CN202658053 U CN 202658053U
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tank
pond
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treating device
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朱洪斌
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SUZHOU COOBOS FLUID TECHNOLOGY Co Ltd
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Abstract

本实用新型公开了一种地埋式污水处理装置,包括由调节池、初沉池、厌氧生物滤池、好氧生物接触氧化池,二沉池,砂滤池,消毒池构成;其中,各个构成部分的依次连接顺序为:调节池、初沉池、厌氧生物滤池、好氧生物接触氧化池、二沉池、砂滤池、消毒池。

Figure 201220308081

The utility model discloses an underground sewage treatment device, which comprises a regulating tank, a primary sedimentation tank, an anaerobic biological filter, an aerobic biological contact oxidation tank, a secondary sedimentation tank, a sand filter and a disinfection tank; wherein, The connection sequence of each component is: regulating tank, primary sedimentation tank, anaerobic biological filter, aerobic biological contact oxidation tank, secondary sedimentation tank, sand filter tank, disinfection tank.

Figure 201220308081

Description

一种地埋式污水处理装置An underground sewage treatment device

技术领域 technical field

本实用新型属于污水处理装置领域,具体涉及一种地埋式污水处理装置。 The utility model belongs to the field of sewage treatment devices, in particular to an underground sewage treatment device.

背景技术 Background technique

在城市的发展进程当中,有些城市基础设施建设如污水处理厂往往滞后于城市的建设,在城市污水管网未到达的地区,住宅小区生活污水处理一直是很难解决的问题。据不完全统计,在城市中生活污水的污染物已占水污染物总量的40%~50%。为解决由于我国的城市地下水道污水收集系统尚不完善,污水处理厂覆盖率较低而造成的众多无法接管地区的生活小区的生活污水不经处理就直接排放,造成环境污染较严重的问题。 In the process of urban development, the construction of some urban infrastructure such as sewage treatment plants often lags behind the construction of the city. In areas where the urban sewage pipe network does not reach, domestic sewage treatment in residential quarters has always been a difficult problem to solve. According to incomplete statistics, the pollutants of domestic sewage in cities have accounted for 40% to 50% of the total amount of water pollutants. In order to solve the problem that the sewage collection system of urban underground waterways in our country is not perfect and the coverage rate of sewage treatment plants is low, and the domestic sewage in many living quarters that cannot be taken over is directly discharged without treatment, resulting in serious environmental pollution.

生活污水包括粪便及其冲洗水、厨房炊事用水、洗浴废水等所有的废水。据第五次全国人口普查,中国农村人口约8.88亿,占人口总数的70.1%。随着乡镇、农村的迅速发展和广大农村人民生活水平的迅速提高及生活条件的明显改善,人口居住日趋集中,农村生活污水的排放量不断增加,到2010年,中国村镇污水排放量约270亿t。然而,我国乡镇农村的生活污水处理能力低、处理方式落后,主要的手段是修建标准化粪池,现在采用的沼气化粪池则必须经过后续兼性或好氧滤池处理才能达到国家综合污水排放二级标准。近年来,国内研究者套用城市或工业污水生化处理或物化处理技术,如采用UASB(上流式厌氧污泥床)、SBR(序批式生物反应器)、膜生物反应器和地埋式接触氧化池等都由于投资大、能耗高、运行费用高、管理难度大等原因难以在农村推广应用;而目前研究较多的人工湿地技术及在其基础上发展而来的人工复合生态床等处理技术也存在有机负荷较低、处理效果受季节影响较大和日常维护难的缺点。 Domestic sewage includes feces and its flushing water, kitchen cooking water, bathing waste water and all waste water. According to the fifth national census, China's rural population is about 888 million, accounting for 70.1% of the total population. With the rapid development of towns and villages and the rapid improvement of the living standards of the vast rural people and the obvious improvement of living conditions, the population is increasingly concentrated, and the discharge of rural domestic sewage continues to increase. By 2010, the sewage discharge of Chinese villages and towns will be about 27 billion t. However, the domestic sewage treatment capacity in towns and rural areas in my country is low and the treatment methods are backward. The main means is to build standardized septic tanks. The biogas septic tanks currently used must be treated by subsequent facultative or aerobic filters to achieve national comprehensive sewage discharge. secondary standard. In recent years, domestic researchers have applied biochemical or physicochemical treatment technologies for urban or industrial sewage, such as UASB (upflow anaerobic sludge bed), SBR (sequencing batch bioreactor), membrane bioreactor and buried contactor. Oxidation ponds are difficult to popularize and apply in rural areas due to large investment, high energy consumption, high operating costs, and difficult management; and the artificial wetland technology and the artificial composite ecological bed developed on the basis of more researches. The treatment technology also has the disadvantages of low organic load, high seasonal influence on treatment effect and difficult daily maintenance.

本实用新型公开了一种地埋式污水处理装置,简述了地埋式污水处理装置在工程设计和工程应用中实际情况,分析了有动力地埋式污水处理装置的优缺点,提出了应根据工程实际情况选择污水处理装置的建议。 The utility model discloses a buried sewage treatment device, briefly describes the actual situation of the buried sewage treatment device in engineering design and engineering application, analyzes the advantages and disadvantages of the powered buried sewage treatment device, and puts forward the application According to the actual situation of the project, it is recommended to select the sewage treatment device.

实用新型内容 Utility model content

本实用新型的技术目的在于公开了一种地埋式污水处理装置,该污水处理系统主要采用生物接触氧化法,在好氧条件下利用好氧菌将污水中的有机物分解,由于污水中含有悬浮物、漂浮物进入调节池,采用AS型污水泵把纤维状物质撕裂、切断、输送至生物接触氧化池进行生物处理,通过接触氧化池填料上生物膜的作用,使污水净化;污水与接触氧化池中脱落的生物膜一起流入二次沉淀池进行污水分离。经沉淀池澄清后的污水流入砂滤池进行深度处理后,进入消毒池进行处理,经消毒后,污水已完成各项处理即回用或排放。 The technical purpose of the utility model is to disclose a buried sewage treatment device. The sewage treatment system mainly adopts the biological contact oxidation method, and uses aerobic bacteria to decompose the organic matter in the sewage under aerobic conditions. The waste and floating matter enter the adjustment tank, and the AS-type sewage pump is used to tear, cut off, and transport the fibrous material to the biological contact oxidation tank for biological treatment. Through the action of the biofilm on the filler of the contact oxidation tank, the sewage is purified; the sewage and contact The biofilm shed in the oxidation tank flows into the secondary sedimentation tank together for sewage separation. The sewage clarified by the sedimentation tank flows into the sand filter tank for advanced treatment, and then enters the disinfection tank for treatment. After disinfection, the sewage has completed various treatments and is reused or discharged.

为实现本实用新型实用新型目的,采用如下技术方案: For realizing the utility model utility model purpose, adopt following technical scheme:

1.      一种地埋式污水处理装置,其特征在于包括由调节池、初沉池、厌氧生物滤池、好氧生物接触氧化池,二沉池,砂滤池,消毒池构成;其中,各个构成部分的依次连接顺序为:调节池、初沉池、厌氧生物滤池、好氧生物接触氧化池、二沉池、砂滤池、消毒池。 1. An underground sewage treatment device, characterized in that it consists of a regulating tank, a primary sedimentation tank, an anaerobic biological filter, an aerobic biological contact oxidation tank, a secondary sedimentation tank, a sand filter, and a disinfection tank; wherein, The connection sequence of each component is: regulating tank, primary sedimentation tank, anaerobic biological filter, aerobic biological contact oxidation tank, secondary sedimentation tank, sand filter tank, disinfection tank.

2.      所述的调节池,其主要调节污水的水质、水量,调节容积视来水的不均匀性而定,一般取6-8 h平均水量,池内设有预曝气装置,同时可避免池中污水厌氧发酵。 2. The regulating pool mentioned above mainly regulates the water quality and quantity of sewage, and the regulating volume depends on the inhomogeneity of incoming water. Generally, the average water quantity of 6-8 hours is taken. There is a pre-aeration device in the pond, which can avoid the Anaerobic fermentation of sewage.

3.      所述的初沉池,其为省地一般采用竖流式沉淀池,上升流速0.2-0.4 mm/s,表面负荷为1.2-1.8 m3/m2·h,出水自流到厌氧生物滤池,沉淀的污泥用空气提至污泥池内。 3. The above-mentioned primary sedimentation tank, which is land-saving, generally adopts a vertical flow sedimentation tank, with an ascending flow rate of 0.2-0.4 mm/s, a surface load of 1.2-1.8 m 3 /m 2 ·h, and the effluent flows to anaerobic organisms by itself. filter, and the settled sludge is lifted to the sludge tank by air.

4.      所述的厌氧生物滤池,其长宽高分别为:18 m,3 m,4 m,滤料体积和滤料粒径分别为:50 m3,35 mm,过滤厌氧池中架空一2.5 m厚的生物滤料层,滤料采用大小均匀的陶粒。 4. The anaerobic biological filter, its length, width and height are respectively: 18 m, 3 m, 4 m, and the volume and particle size of the filter material are respectively: 50 m 3 , 35 mm. A 2.5 m thick layer of biological filter material is overhead, and the filter material is made of ceramsite with uniform size.

5.      所述的好氧生物接触氧化池,其采用推流式生物接触氧化法,并配以新型的立体弹性填料,具有一定的柔性和刚性,回弹性能好,材质比水轻,能在水中均匀舒展,对水气作密集性多层次的切割, 提高了溶解氧的传递系数,减少风量,保持立体空间均匀密度,使水气生物膜充分接触,可确保污水处理后各项指标全面达标。 5. The aerobic biological contact oxidation pond adopts the plug-flow biological contact oxidation method and is equipped with a new three-dimensional elastic filler. It has certain flexibility and rigidity, good resilience performance, and the material is lighter than water. Stretch evenly in the water, make intensive multi-level cutting of water vapor, improve the transfer coefficient of dissolved oxygen, reduce air volume, maintain uniform density in three-dimensional space, make water vapor biofilm fully contact, and ensure that all indicators after sewage treatment are fully up to standard .

6.      所述的二沉池,生化后的污水流到二沉池,它为2只竖流式沉淀池并联运行,作用主要是沉淀剥落下来老化的生物膜,二沉池表面负荷为1-1.3 m3/m2·h,上升流速为0.1-0.15 mm/s排泥用空气提至污泥池。 6. In the secondary settling tank, the biochemical sewage flows to the secondary settling tank. It is two vertical flow settling tanks running in parallel. The effect is mainly to precipitate and peel off the aging biofilm. 1.3 m 3 /m 2 ·h, the ascending flow rate is 0.1-0.15 mm/s, and the sludge is lifted to the sludge tank by air.

7.      所述的砂滤池,其采用顺流过滤、逆流反洗(滤料为石英砂,滤料承托层0.4 m,滤料层0.8 m,压脂层0.5 m)。 7. The sand filter described above adopts downstream filtration and countercurrent backwashing (the filter material is quartz sand, the filter material support layer is 0.4 m, the filter material layer is 0.8 m, and the grease layer is 0.5 m).

8.      所述的消毒池,砂滤池出水进入消毒池后,水中含有大量微生物及细菌等,消毒采用固体氯片接触溶解的消毒方式,也有采用二氧化氯发生器消毒的,消毒时间为30 min,若是处理医院污水可增加至1-1.5 h。 8. In the disinfection tank mentioned above, after the water from the sand filter enters the disinfection tank, the water contains a large number of microorganisms and bacteria, etc., and the disinfection method adopts the disinfection method of contacting and dissolving solid chlorine tablets, and some chlorine dioxide generators are used for disinfection, and the disinfection time is 30 min, it can be increased to 1-1.5 h if treating hospital sewage.

附图说明 Description of drawings

图1 本实用新型地埋式污水处理装置流程示意图; Fig. 1 Schematic flow chart of the buried sewage treatment device of the utility model;

图1中污水进水管1,格栅2,调节池3,初沉池4,厌氧池5,泵提升6,风机7,好氧生物接触氧化池8,二沉池9,砂滤池10,消毒池11,排放池12。 In Figure 1, sewage inlet pipe 1, grille 2, regulating tank 3, primary sedimentation tank 4, anaerobic tank 5, pump lift 6, fan 7, aerobic biological contact oxidation tank 8, secondary sedimentation tank 9, sand filter tank 10 , disinfection pool 11, discharge pool 12.

具体实施方式 Detailed ways

结合图1,通过实施例对本实用新型作进一步的说明。 In conjunction with Fig. 1, the utility model is further described through embodiments.

实施例 Example

    本实用新型所述的地埋式污水处理装置,其连接顺序依次为:污水进水管1,格栅2,调节池3,初沉池4,厌氧池5,泵提升6,好氧生物接触氧化池8,二沉池9,砂滤池10,消毒池11,排放池12。风机7连接在好氧生物接触氧化池8上曝气。 The buried sewage treatment device described in the utility model, its connection sequence is as follows: sewage inlet pipe 1, grid 2, regulating tank 3, primary sedimentation tank 4, anaerobic tank 5, pump lifting 6, aerobic biological contact Oxidation pond 8, secondary sedimentation pond 9, sand filter pond 10, disinfection pond 11, discharge pond 12. The fan 7 is connected to the aerobic biological contact oxidation tank 8 for aeration.

经格栅2初步过滤的生活污水进入调节池3,由于污水流量的不均性,调节池在工艺设计过程中采用了一池多用,不仅调节池起调节水质、水量的作用,而且还能拦截漂浮物及明油的功能,更有效地提高污水处理的生化性。 The domestic sewage preliminarily filtered by the grid 2 enters the regulating pool 3. Due to the unevenness of the sewage flow, the regulating pool adopts a multi-purpose pool in the process design process. The regulating pool not only plays the role of regulating water quality and water quantity, but also intercepts The function of floating matter and clear oil can more effectively improve the biochemical properties of sewage treatment.

经调节池3处理后的污水,进入到初沉池4,然后再进入两个相互串联着的厌氧池5,过滤厌氧池中架空一2.5 m厚的生物滤料层,滤料采用大小均匀的陶粒。在滤料选用上,前一滤池选用粒径为45-50 mm的陶粒,后一滤池选用的粒径为35-40mm。为了预防滤料堵塞的危险,采用三个预防措施:(1)在进入过滤厌氧池的入口处,加一道细密的栅格,同时在入口处加检修孔,随时清除堵塞物;(2)填料分层设置,每层填料厚0.5~1.0 m,层间留0.25~0.4 m的间隙,以防止堵塞,达到重新整流的目的;(3)把滤料层做成可以转动上部留有一定空隙的滤料层,用一转轴把滤料层架空。正常工作时,滤料层两端用钢丝悬挂,避免失稳倾斜。当滤料层堵塞时,则利用钢丝绳转动滤料层,把滤料层翻转过来,使紧密的滤料颗粒发生相对移动,变得疏松。也同时进行反冲洗,达到清除堵塞的目的。 The sewage treated by the regulating tank 3 enters the primary sedimentation tank 4, and then enters two anaerobic tanks 5 connected in series, and a 2.5 m thick biological filter material layer is suspended in the anaerobic tank, and the filter material adopts a size Uniform ceramsite. In terms of filter material selection, the former filter uses ceramsite with a particle size of 45-50 mm, and the latter filter uses a particle size of 35-40 mm. In order to prevent the risk of filter clogging, three preventive measures are adopted: (1) Add a fine grid at the entrance of the filter anaerobic tank, and add a maintenance hole at the entrance to remove the blockage at any time; (2) The packing is arranged in layers, each layer of packing is 0.5-1.0 m thick, and a gap of 0.25-0.4 m is left between layers to prevent clogging and achieve the purpose of rectification; (3) Make the filter material layer so that it can rotate and leave a certain gap in the upper part The filter material layer is elevated with a rotating shaft. During normal operation, the two ends of the filter material layer are suspended by steel wires to avoid instability and tilt. When the filter material layer is clogged, use the wire rope to rotate the filter material layer and turn the filter material layer over so that the compact filter material particles move relatively and become loose. Backwashing is also carried out at the same time to achieve the purpose of clearing the blockage.

经厌氧池5处理过的污水进入好氧生物接触氧化池8,接触氧化池分为三级,总停留时间4~5 h,污水进入接触氧化池后,在好氧条件下,污水中的有机物通过附着在填料上的微生物的代谢作用,转化成稳定物质,同时,好氧菌生长老化后从填料表面剥落进入污水。填料为新颖弹性填料,容易结膜,填料比表面积可达400 m2/m3,气水比为12:1左右。 The sewage treated in the anaerobic tank 5 enters the aerobic biological contact oxidation tank 8. The contact oxidation tank is divided into three stages, and the total residence time is 4 to 5 h. After the sewage enters the contact oxidation tank, under aerobic conditions, the Organic matter is converted into stable substances through the metabolism of microorganisms attached to the filler. At the same time, aerobic bacteria grow and age and peel off from the filler surface into the sewage. The filler is a novel elastic filler, which is easy to form a film. The specific surface area of the filler can reach 400 m 2 /m 3 , and the air-water ratio is about 12:1.

生化后的污水流到二沉池9,它为2只竖流式沉淀池并联运行,作用主要是沉淀剥落下来老化的生物膜,二沉池表面负荷为1-1.3 m3/m2·h,上升流速为0.1-0.15 mm/s排泥用空气提至污泥池。 The biochemical sewage flows to the secondary sedimentation tank 9, which is a parallel operation of two vertical flow sedimentation tanks. The main function is to precipitate and peel off the aging biofilm. The surface load of the secondary sedimentation tank is 1-1.3 m 3 /m 2 ·h , the rising flow rate is 0.1-0.15 mm/s, and the sludge is lifted to the sludge tank by air.

砂滤池10采用的是顺流过滤、逆流反洗,砂滤池出水进入消毒池后,水中含有大量微生物及细菌等,消毒采用固体氯片接触溶解的消毒方式,也有采用二氧化氯发生器消毒的,消毒时间为30 min,若是处理医院污水可增加至1-1.5 h。 The sand filter 10 adopts downstream filtration and countercurrent backwashing. After the effluent from the sand filter enters the disinfection tank, the water contains a large number of microorganisms and bacteria. The disinfection method adopts the disinfection method of solid chlorine tablets contacting and dissolving, and some chlorine dioxide generators are also used. For disinfection, the disinfection time is 30 minutes, and it can be increased to 1-1.5 hours for hospital sewage.

此装置的工艺特点: The technological characteristics of this device:

(1)采用先进的A/O 法(厌氧+好氧)处理工艺; (1) Adopt advanced A/O method (anaerobic + aerobic) treatment process;

(2)污泥产量少,无需污泥处理设备; (2) Less sludge output, no need for sludge treatment equipment;

(3)有机污染物去除率高,出水水质稳定,抗冲击负荷能力强; (3) The removal rate of organic pollutants is high, the effluent water quality is stable, and the impact load resistance is strong;

(4)脱氮除磷,出水可入天然水体; (4) Nitrogen and phosphorus are removed, and the effluent can enter natural water bodies;

(5)埋于地下,占地少,也可设于地上; (5) Buried underground, occupying less land, it can also be located on the ground;

(6)多个单元联,成为大规模污水处理场; (6) Multiple units are connected to become a large-scale sewage treatment plant;

(7)运行费用低; (7) Low operating cost;

(8)一次性投资少(比传统工艺节省50%以上); (8) Less one-time investment (saving more than 50% compared with traditional crafts);

(9)安装简易,管理方便; (9) Easy installation and convenient management;

(10)地埋式净化槽一般不承受过车荷载,有高荷载时采用加强结构。 (10) The buried septic tank generally does not bear the passing load, and a reinforced structure is used when there is a high load.

Claims (7)

1. a flush-with-ground type sewage treating device is characterized in that comprising by equalizing tank, preliminary sedimentation tank, anaerobic biofilter, aerobic bio-contact oxidation pond, second pond, and sand filter, sterilization pool consists of; Wherein, the successively order of connection of each component part is: equalizing tank, preliminary sedimentation tank, anaerobic biofilter, aerobic bio-contact oxidation pond, second pond, sand filter, sterilization pool.
2. flush-with-ground type sewage treating device according to claim 1 is characterized in that described equalizing tank gets the average water yield of 6-8 h, is provided with preaerator in the pond.
3. flush-with-ground type sewage treating device according to claim 1 is characterized in that described preliminary sedimentation tank adopts vertical sedimentation basin, and upflow velocity 0.2-0.4 mm/s, surface load are 1.2-1.8 m 3/ m 2H, water outlet flows automatically to anaerobic biofilter, and the mud of precipitation is carried to sludge sump with air.
4. flush-with-ground type sewage treating device according to claim 1 is characterized in that the length and width height of described anaerobic biofilter is respectively: 18 m, and 3 m, 4 m, filtrate volume and particle diameter of filter medium are respectively: 50 m 3, 35 mm filter the built on stilts thick biological filter bed of material of one 2.5 m in the anaerobic pond, and filtrate adopts haydite of uniform size.
5. flush-with-ground type sewage treating device according to claim 1 is characterized in that described aerobic bio-contact oxidation pond employing pulling flow type biological contact oxidation process, and is equipped with 3 D elastic filler.
6. flush-with-ground type sewage treating device according to claim 1 is characterized in that described second pond is 2 vertical sedimentation basin parallel runnings, and its surface load is 1-1.3 m 3/ m 2H, upflow velocity are that 0.1-0.15 mm/s spoil disposal is carried to sludge sump with air.
7. flush-with-ground type sewage treating device according to claim 1, the filtrate that it is characterized in that described sand filter is quartz sand, filtrate supporting layer 0.4 m, filter material layer 0.8 m, packed resin layer 0.5 m.
CN201220308081.8U 2012-06-28 2012-06-28 Buried sewage treatment device Expired - Fee Related CN202658053U (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102718365A (en) * 2012-06-28 2012-10-10 苏州科博思流体科技有限公司 Buried sewage treatment device
CN103936224A (en) * 2014-03-20 2014-07-23 宁波创蓝环境科技有限公司 Intelligent sewage treatment equipment and its treatment method
CN104649511A (en) * 2014-12-23 2015-05-27 安徽省天虹绿洲环保科技有限公司 Rural domestic wastewater treatment process

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102718365A (en) * 2012-06-28 2012-10-10 苏州科博思流体科技有限公司 Buried sewage treatment device
CN103936224A (en) * 2014-03-20 2014-07-23 宁波创蓝环境科技有限公司 Intelligent sewage treatment equipment and its treatment method
CN103936224B (en) * 2014-03-20 2015-07-15 宁波创蓝环境科技有限公司 Intelligent sewage treatment equipment and its treatment method
CN104649511A (en) * 2014-12-23 2015-05-27 安徽省天虹绿洲环保科技有限公司 Rural domestic wastewater treatment process

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