CN111450616A - Efficient activated sludge interception type secondary sedimentation tank process system with coupling depth filtering function - Google Patents
Efficient activated sludge interception type secondary sedimentation tank process system with coupling depth filtering function Download PDFInfo
- Publication number
- CN111450616A CN111450616A CN202010264874.3A CN202010264874A CN111450616A CN 111450616 A CN111450616 A CN 111450616A CN 202010264874 A CN202010264874 A CN 202010264874A CN 111450616 A CN111450616 A CN 111450616A
- Authority
- CN
- China
- Prior art keywords
- secondary sedimentation
- sedimentation tank
- tank
- water
- activated sludge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Activated Sludge Processes (AREA)
Abstract
一种具有耦合深度过滤功能的高效活性污泥截留型二沉池工艺系统,将配水系统与具有耦合深度过滤功能的高效活性污泥截留型二沉池相通,具有耦合深度过滤功能的高效活性污泥截留型二沉池包括池体、进水管、布水系统、溢流堰、挡渣板、刮渣板、刮泥板、驱动电机、搅拌装置和耦合式过滤池。该系统具有网补、絮凝沉淀及过滤作用且兼顾泥水分离、化学除磷及深度过滤功能,可明显提升二沉池的泥水分离效果,降低二沉池的水力停留时间及占地,并耦合深度过滤系统,既节省了二次提升能耗,又节省了相应的污水管线。
A high-efficiency activated sludge retention type secondary sedimentation tank process system with coupled depth filtering The mud retention type secondary sedimentation tank includes a tank body, a water inlet pipe, a water distribution system, an overflow weir, a slag baffle, a slag scraper, a mud scraper, a driving motor, a stirring device and a coupled filter tank. The system has the functions of mesh replenishment, flocculation sedimentation and filtration, and takes into account the functions of mud-water separation, chemical phosphorus removal and deep filtration, which can significantly improve the mud-water separation effect of the secondary sedimentation tank, reduce the hydraulic retention time and land occupation of the secondary sedimentation tank, and couple the depth of The filtration system not only saves the energy consumption of the secondary lifting, but also saves the corresponding sewage pipeline.
Description
技术领域technical field
本发明属于污水处理技术领域,特别涉及一种具有耦合深度过滤功能的高效活性污泥截留型二沉池工艺系统。The invention belongs to the technical field of sewage treatment, and in particular relates to a high-efficiency activated sludge retention type secondary sedimentation tank process system with a coupling depth filtration function.
背景技术Background technique
总结我国污水处理厂近十几年来升级改造经验,普遍遇到的最大难题是占地面积受限,现有污水处理厂的建设用地不能满足提标改造的实际需求,严重制约污水处理厂的发展,而二沉池的占地在工艺系统中占10%~20%;其次,我国污水处理厂污水管网以合流制系统为主,雨季时,进水的水量波动导致污水处理厂的进水负荷严重超过设计标准,污水处理厂工艺稳定运行受到严重威胁,其中最为突出的问题之一是二沉池的表面负荷不足。Summarizing the experience of upgrading and transformation of sewage treatment plants in my country in the past ten years, the biggest problem commonly encountered is the limited floor space, and the construction land of the existing sewage treatment plants cannot meet the actual needs of upgrading and transformation, which seriously restricts the development of sewage treatment plants. , and the area of the secondary sedimentation tank accounts for 10% to 20% of the process system; secondly, the sewage pipe network of my country's sewage treatment plants is mainly a confluence system. The load seriously exceeds the design standard, and the stable operation of the sewage treatment plant process is seriously threatened. One of the most prominent problems is the insufficient surface load of the secondary sedimentation tank.
同时发现,大部分污水处理厂的二沉池出水到到后续深度处理的过滤系统,需要二次提升,而二次提升能耗在污水处理能耗中占10%以上的比例,在我国提倡节能降耗、提质增效的目标背景下,这部分能耗的节省也是至关重要的。At the same time, it was found that the effluent from the secondary sedimentation tank of most sewage treatment plants to the filtration system for subsequent advanced treatment requires a second upgrade, and the energy consumption of the second upgrade accounts for more than 10% of the energy consumption of sewage treatment. Energy saving is advocated in my country. Under the background of the goal of reducing consumption and improving quality and efficiency, the saving of this part of energy consumption is also crucial.
在土地资源受限、合流制管网进水水量波动、二级处理污水到深度处理的二次提升能耗等成为城镇污水处理厂提质增效的重要影响因素时,二沉池运行效率的提升是减少占地、应对进水水量波动、节能降耗的一个重要措施,亟需解决。When land resources are limited, the influent water volume of the combined pipe network fluctuates, and the energy consumption for secondary improvement from secondary treatment of sewage to advanced treatment becomes an important factor affecting the quality and efficiency of urban sewage treatment plants, the operation efficiency of the secondary sedimentation tank will increase. Upgrading is an important measure to reduce land occupation, cope with fluctuations in influent water volume, save energy and reduce consumption, and it needs to be solved urgently.
发明内容SUMMARY OF THE INVENTION
本发明目的在于克服传统二沉池运行效率偏低且占地偏大的不足,提供一种具有耦合深度过滤功能的高效活性污泥截留型二沉池工艺系统,该系统具有网补、絮凝沉淀及过滤作用且兼顾泥水分离、化学除磷及深度过滤功能,可明显提升二沉池的泥水分离效果,降低二沉池的水力停留时间及占地,并耦合深度过滤系统,既节省了二次提升能耗,又节省了相应的污水管线。The purpose of the invention is to overcome the shortcomings of low operating efficiency and large footprint of traditional secondary sedimentation tanks, and to provide a high-efficiency activated sludge retention type secondary sedimentation tank process system with coupled depth filtration function. It can significantly improve the mud-water separation effect of the secondary sedimentation tank, reduce the hydraulic retention time and land occupation of the secondary sedimentation tank, and couple the depth filtration system, which not only saves secondary sedimentation Improve energy consumption and save the corresponding sewage pipeline.
如上构思,本发明的技术方案是:一种具有耦合深度过滤功能的高效活性污泥截留型二沉池工艺系统,包括配水系统,其特征在于:配水系统与具有耦合深度过滤功能的高效活性污泥截留型二沉池相通,所述具有耦合深度过滤功能的高效活性污泥截留型二沉池包括池体、进水管、布水系统、溢流堰、挡渣板、刮渣板、刮泥板、驱动电机、搅拌装置和耦合式过滤池,所述进水管垂直安装在在池体的中心处且其顶部安装驱动电机,所述布水系统环绕于进水管,所述搅拌装置安装在池体的内壁上,所述溢流堰设置在池体内部水面且溢流堰外部制有溢流口,所述挡渣板设置在溢流堰的内部,所述刮渣板设置在池体上部水面处,所述刮泥板设置在池体底部,刮渣板和刮泥板均与驱动电机相连,所述耦合式过滤池设置于池体周围且与溢流口相通,其底部制有出水口,所述池体底端制有排泥/污泥回流口,所述配水系统与进水管连通。As conceived above, the technical scheme of the present invention is: a high-efficiency activated sludge retention type secondary sedimentation tank process system with coupled depth filtration function, including a water distribution system, characterized in that: the water distribution system and the coupled depth filtration function High-efficiency activated sludge The sludge retention type secondary sedimentation tank is connected, and the high-efficiency activated sludge retention type secondary sedimentation tank with coupled depth filtration function includes a tank body, a water inlet pipe, a water distribution system, an overflow weir, a slag baffle, a slag scraper, and a sludge scraper. A plate, a driving motor, a stirring device and a coupled filter tank, the water inlet pipe is installed vertically at the center of the tank body and a driving motor is installed on the top thereof, the water distribution system surrounds the water inlet pipe, and the stirring device is installed in the tank On the inner wall of the body, the overflow weir is arranged on the water surface inside the pool body and an overflow port is made outside the overflow weir, the slag baffle plate is arranged inside the overflow weir, and the slag scraper is arranged on the upper part of the pool body At the water surface, the scraper is arranged at the bottom of the pool body, and both the slag scraper and the scraper are connected to the drive motor. The coupled filter pool is arranged around the pool body and communicated with the overflow port. The bottom end of the pool body is provided with a sludge discharge/sludge return port, and the water distribution system is communicated with the water inlet pipe.
所述配水系统外接加药系统。The water distribution system is externally connected with a dosing system.
所述溢流堰为锯齿形结构,且呈环状设置在池体内部水面处。The overflow weir has a zigzag structure and is annularly arranged at the water surface inside the tank body.
本发明的工作原理是:使生物系统泥水混合液进入二沉池的进水管,通过进水管进入二沉池的布水系统,混合液通过布水系统进入二沉池中下部后通过搅拌系统形成的高低密度不同的悬浮活性污泥层的截留和吸附作用,将混合液中的活性污泥快速截留,密度高的活性污泥通过沉淀作用进入二沉池底部污泥斗中,一部分可通过内回流泵回流至生物处理系统,另一部分通过二沉池底部的排泥设备排出池外进入后续污泥处理系统。位于二沉池上部为泥水分离后的上清液,清液重力流入深度过滤系统(耦合式过滤池)进一步去除清液中的悬浮固体物质。The working principle of the invention is as follows: the mud-water mixture of the biological system enters the water inlet pipe of the secondary sedimentation tank, enters the water distribution system of the secondary sedimentation tank through the water inlet pipe, and the mixed liquid enters the middle and lower parts of the secondary sedimentation tank through the water distribution system and is formed by the stirring system. The retention and adsorption of suspended activated sludge layers with different high and low densities quickly intercept the activated sludge in the mixed solution, and the activated sludge with high density enters the sludge hopper at the bottom of the secondary sedimentation tank through sedimentation, and a part of it can pass through. The internal return pump returns to the biological treatment system, and the other part is discharged out of the tank through the sludge discharge equipment at the bottom of the secondary sedimentation tank and enters the subsequent sludge treatment system. Located in the upper part of the secondary sedimentation tank is the supernatant liquid after the separation of mud and water, and the supernatant liquid flows into the depth filtration system (coupled filter tank) by gravity to further remove the suspended solids in the supernatant liquid.
上述工艺系统的水力停留时间为1.5-2.5小时,活性污泥的停留时间控制在10小时以内,可通过回流泵和污泥排泥泵综合控制。本系统还可通过加药系统将混凝剂(如化学除磷药剂)投加进配水系统中,以提高系统的化学除磷效果和活性污泥絮凝效果,使得二沉池在高效泥水分离过程中耦合化学除磷,并通过后续一体式深度过滤系统(耦合式过滤池)进一步去除二沉池清液中的SS和磷酸盐。The hydraulic retention time of the above process system is 1.5-2.5 hours, and the residence time of activated sludge is controlled within 10 hours, which can be controlled comprehensively by the return pump and the sludge discharge pump. The system can also add coagulants (such as chemical phosphorus removal agents) into the water distribution system through the dosing system to improve the chemical phosphorus removal effect and activated sludge flocculation effect of the system, so that the secondary sedimentation tank can be used in the high-efficiency mud-water separation process. Medium-coupled chemical phosphorus removal, and further removal of SS and phosphate in the supernatant of the secondary sedimentation tank through the subsequent integrated depth filtration system (coupled filter tank).
混凝剂与生物系统泥水混合液混合后,有助于悬浮活性污泥层的形成,这样不仅可提升二沉池悬浮污泥层的吸附和絮凝效果,而且同时可去除水中的磷酸盐,将泥水分离和化学除磷功能耦合,提升二沉池的运行效能。After the coagulant is mixed with the sludge-water mixture of the biological system, it is helpful for the formation of the suspended activated sludge layer, which can not only improve the adsorption and flocculation effect of the suspended sludge layer in the secondary sedimentation tank, but also remove the phosphate in the water. The function of mud-water separation and chemical phosphorus removal is coupled to improve the operation efficiency of the secondary sedimentation tank.
本发明具有如下优点和积极效果:The present invention has the following advantages and positive effects:
1、本发明在传统二沉池内部设置搅拌系统,可形成悬浮活性污泥层,较传统二沉池的沉淀泥水分离效果,悬浮活性污泥层可对进入二沉池的生物系统混合液进行网补、吸附、絮凝并最终通过沉淀作用达到快速泥水分离效果。1. In the present invention, a stirring system is set inside the traditional secondary sedimentation tank, which can form a suspended activated sludge layer. Compared with the sedimentation mud-water separation effect of the traditional secondary sedimentation tank, the suspended activated sludge layer can be used for the biological system mixed liquid entering the secondary sedimentation tank. Net replenishment, adsorption, flocculation and finally through precipitation to achieve rapid mud-water separation effect.
2、本发明具有耦合深度过滤功能的高效活性污泥截留型二沉池水力停留时间为1.5~2.5h,较传统二沉池节省了30%以上的池容及占地。2. The hydraulic retention time of the high-efficiency activated sludge retention type secondary sedimentation tank with the function of coupling depth filtration of the present invention is 1.5-2.5 h, which saves more than 30% of the tank capacity and land occupation compared with the traditional secondary sedimentation tank.
3、本发明可通过加药系统将将混凝剂(如除磷药剂)投加进配水系统中,混凝剂与生物系统泥水混合液混合后,有助于悬浮活性污泥层的形成,这样不仅可提升二沉池悬浮污泥层的吸附和絮凝效果,而且同时可去除水中的磷酸盐,将泥水分离和化学除磷功能耦合,提升二沉池的运行效能。3. In the present invention, the coagulant (such as phosphorus removal agent) can be added into the water distribution system through the dosing system. After the coagulant is mixed with the mud-water mixture of the biological system, it is helpful for the formation of the suspended activated sludge layer. This not only improves the adsorption and flocculation effect of the suspended sludge layer in the secondary sedimentation tank, but also removes phosphate in the water, couples the functions of sludge water separation and chemical phosphorus removal, and improves the operational efficiency of the secondary sedimentation tank.
4、本发明将耦合式过滤池设置于池体周围,耦合成一体式深度过滤系统,使二沉池出水直接重力自流入耦合式过滤池,既节省了二次提升能耗,也节省了相应的污水管线等。4. In the present invention, the coupled filter tank is arranged around the tank body and coupled to form an integrated depth filtration system, so that the effluent of the secondary sedimentation tank directly flows into the coupled filter tank by gravity, which not only saves the energy consumption of the secondary lifting, but also saves the corresponding sewage pipelines, etc.
附图说明Description of drawings
图1是耦合深度过滤功能的高效活性污泥截留型二沉池结构侧视图;Figure 1 is a side view of the structure of a high-efficiency activated sludge retention type secondary sedimentation tank coupled with a depth filtration function;
图2是耦合深度过滤功能的高效活性污泥截留型二沉池结构俯视图;Figure 2 is a top view of the structure of a high-efficiency activated sludge retention type secondary sedimentation tank coupled with a depth filtration function;
图3是耦合深度过滤功能的高效活性污泥截留型二沉池工艺流程图。Figure 3 is a process flow diagram of a high-efficiency activated sludge retention type secondary sedimentation tank coupled with a depth filtration function.
图中:1、进水管;2、布水系统;3、溢流堰;4、挡渣板;5、溢流口;6刮渣板;7、刮泥板;8、驱动电机;9、搅拌系统;10、耦合式过滤池;11、出水口;12、排泥/污泥回流口;13、池体;14、配水系统;15、加药系统;16、具有耦合深度过滤功能的高效活性污泥截留型二沉池。In the figure: 1. Water inlet pipe; 2. Water distribution system; 3. Overflow weir; 4. Slag baffle; 5. Overflow port; 6. Slag scraper; 7. Mud scraper; 8. Drive motor; 9. Mixing system; 10. Coupling filter tank; 11. Water outlet; 12. Sludge discharge/sludge return port; 13. Tank body; 14. Water distribution system; 15. Dosing system; 16. High efficiency with coupled depth filtration Activated sludge retention type secondary sedimentation tank.
具体实施方式Detailed ways
如图1、2所示,一种具有耦合深度过滤功能的高效活性污泥截留型二沉池工艺系统,由配水系统、加药系统和具有耦合深度过滤功能的高效活性污泥截留型二沉池组成。As shown in Figures 1 and 2, a high-efficiency activated sludge retention type secondary sedimentation tank process system with coupled depth filtration function consists of a water distribution system, a dosing system and a high-efficiency activated sludge retention type secondary sedimentation tank with coupled depth filtration function. pool composition.
所述具有耦合深度过滤功能的高效活性污泥截留型二沉池包括池体13、进水管1、布水系统2、溢流堰3、挡渣板4、刮渣板6、刮泥板7、驱动电机8、搅拌装置9和耦合式过滤池10。The high-efficiency activated sludge retention type secondary sedimentation tank with coupled depth filtration function includes a
所述进水管1外接配水系统14,所述布水系统2环绕于进水管1,将进水管1的出导流并均匀布入池体13中。The
所述搅拌装置9安装于池体13内壁上,通过搅拌功率的控制使池体13内形成稳定的高效活性污泥层,该污泥层在池深的50-80%左右。The stirring
所述溢流堰3为锯齿形构造,在池体13内部水面处呈环状布置,可以保证出水均匀。The
所述挡渣板4为一半没入水面下的挡板,设置于溢流堰3的内部,用于挡住水面的浮渣。The
所述溢流口5在溢流堰3外部,出水经溢流堰3流入溢流口5,经溢流口5流入耦合式滤池10。The
所述刮渣板6没入水面与驱动电机8相连。The slag scraper 6 is submerged into the water and is connected to the
所述刮泥板7位于池体13底部,紧贴池体13底部并平行,同时与驱动电机8相连。The
所述驱动电机8带动刮渣板6和刮泥板7进行缓慢圆周运动,刮渣板6将水面浮渣撇除,刮泥板7将池底积泥刮至排泥/污泥回流口12进行排泥和回流。The
所述耦合式过滤池10设置于池体13外围,根据实际水力负荷计算后可全部环绕也可部分环绕,耦合式滤池(10)内部可采用多层砂滤或滤布等滤料,由于负荷较低,可采用人工清洗或自动清洗模式。池体出水经溢流口5流入耦合式过滤池10,过滤后经耦合式过滤池10的出水口11流出系统。The coupled
如图3所示:本发明的工作过程是:生物系统泥水混合液进入配水系统14,经配水系统14后进入进水管1,经进水管1和布水系统2进入池体13,之后在池体13内通过搅拌装置9形成的高低密度不同的悬浮活性污泥层,密度高的活性污泥通过沉淀作用进入二沉池底部污泥斗中,一部分通过内回流泵回流至生物处理系统,一部分通过二沉池底部的刮泥板和排泥/污泥回流口12排出池外,进入后续污泥处理系统。加药系统15可将混凝剂(如化学除磷药剂)投加进配水系统14,混凝剂与生物系统泥水混合液混合后,有助于悬浮活性污泥层的形成,这样不仅可提升二沉池悬浮污泥层的吸附和絮凝效果,而且同时可去除水中的磷酸盐,将泥水分离和化学除磷功能耦合,提升二沉池的运行效能。As shown in Figure 3: the working process of the present invention is: the biological system mud-water mixture enters the
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010264874.3A CN111450616A (en) | 2020-04-07 | 2020-04-07 | Efficient activated sludge interception type secondary sedimentation tank process system with coupling depth filtering function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010264874.3A CN111450616A (en) | 2020-04-07 | 2020-04-07 | Efficient activated sludge interception type secondary sedimentation tank process system with coupling depth filtering function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111450616A true CN111450616A (en) | 2020-07-28 |
Family
ID=71674116
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010264874.3A Pending CN111450616A (en) | 2020-04-07 | 2020-04-07 | Efficient activated sludge interception type secondary sedimentation tank process system with coupling depth filtering function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111450616A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022032604A1 (en) * | 2020-08-13 | 2022-02-17 | 苏州迪维勒普信息科技有限公司 | Industrial sewage treatment apparatus |
| WO2022032605A1 (en) * | 2020-08-13 | 2022-02-17 | 苏州迪维勒普信息科技有限公司 | Overflow-type industrial sewage sedimentation apparatus |
| WO2023016088A1 (en) * | 2021-08-13 | 2023-02-16 | 中国市政工程华北设计研究总院有限公司 | Novel low-carbon wastewater deep dephosphorization processing system based on suspension medium layer |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101913703A (en) * | 2010-07-06 | 2010-12-15 | 国家城市给水排水工程技术研究中心 | Primary sludge fermentation pretreatment method and system for improving performances of dephosphorization and denitrification on town sewage |
| CN102350104A (en) * | 2011-07-26 | 2012-02-15 | 华中科技大学 | Chemical-biological flocculation radiation-flow secondary settler |
| CN104276691A (en) * | 2014-09-23 | 2015-01-14 | 同济大学 | Reactive precipitation coupling pool for intensively removing iron and manganese |
| CN106242002A (en) * | 2016-10-20 | 2016-12-21 | 沈阳建筑大学 | A kind of modified model reinforced phosphor-removing device and dephosphorization process |
| CN106552445A (en) * | 2016-11-24 | 2017-04-05 | 北京城市排水集团有限责任公司 | A kind of rectangle Zhou Jinzhou goes out second pond and its using method |
| CN206631259U (en) * | 2017-03-31 | 2017-11-14 | 北京首创清源环境科技有限公司 | A kind of second pond |
| CN212283191U (en) * | 2020-04-07 | 2021-01-05 | 中国市政工程华北设计研究总院有限公司 | Filtering and precipitating coupling novel secondary precipitation tank system based on physicochemical biological synergy |
-
2020
- 2020-04-07 CN CN202010264874.3A patent/CN111450616A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101913703A (en) * | 2010-07-06 | 2010-12-15 | 国家城市给水排水工程技术研究中心 | Primary sludge fermentation pretreatment method and system for improving performances of dephosphorization and denitrification on town sewage |
| CN102350104A (en) * | 2011-07-26 | 2012-02-15 | 华中科技大学 | Chemical-biological flocculation radiation-flow secondary settler |
| CN104276691A (en) * | 2014-09-23 | 2015-01-14 | 同济大学 | Reactive precipitation coupling pool for intensively removing iron and manganese |
| CN106242002A (en) * | 2016-10-20 | 2016-12-21 | 沈阳建筑大学 | A kind of modified model reinforced phosphor-removing device and dephosphorization process |
| CN106552445A (en) * | 2016-11-24 | 2017-04-05 | 北京城市排水集团有限责任公司 | A kind of rectangle Zhou Jinzhou goes out second pond and its using method |
| CN206631259U (en) * | 2017-03-31 | 2017-11-14 | 北京首创清源环境科技有限公司 | A kind of second pond |
| CN212283191U (en) * | 2020-04-07 | 2021-01-05 | 中国市政工程华北设计研究总院有限公司 | Filtering and precipitating coupling novel secondary precipitation tank system based on physicochemical biological synergy |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022032604A1 (en) * | 2020-08-13 | 2022-02-17 | 苏州迪维勒普信息科技有限公司 | Industrial sewage treatment apparatus |
| WO2022032605A1 (en) * | 2020-08-13 | 2022-02-17 | 苏州迪维勒普信息科技有限公司 | Overflow-type industrial sewage sedimentation apparatus |
| WO2023016088A1 (en) * | 2021-08-13 | 2023-02-16 | 中国市政工程华北设计研究总院有限公司 | Novel low-carbon wastewater deep dephosphorization processing system based on suspension medium layer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206927730U (en) | A kind of efficient sedimentation tank | |
| CN201334406Y (en) | Integrated water treatment device for surface water and sewage treatment | |
| CN111450616A (en) | Efficient activated sludge interception type secondary sedimentation tank process system with coupling depth filtering function | |
| CN212283191U (en) | Filtering and precipitating coupling novel secondary precipitation tank system based on physicochemical biological synergy | |
| CN210934074U (en) | A waste water reuse system of a concrete batching plant | |
| CN100366549C (en) | A high-efficiency energy-saving water purification process and device | |
| CN103539280A (en) | Integrated water purification device | |
| CN201999778U (en) | Single-layer pressure integration oil eliminator | |
| CN116282444A (en) | An integrated high turbidity purification device | |
| CN211595371U (en) | A domestic sewage treatment device | |
| CN201292297Y (en) | Integral water purifier | |
| CN218232105U (en) | Electromagnetic interference effluent treatment plant | |
| CN217757087U (en) | Sewage treatment pool | |
| CN207645963U (en) | A kind of integrating device of improved efficient sedimentation tank and sand filter | |
| CN208200478U (en) | A kind of efficient sedimentation tank | |
| CN216549781U (en) | Advanced wastewater treatment tank | |
| CN110436596A (en) | A combined backwash water treatment and reuse system | |
| CN215208965U (en) | Dense medium magnetic coagulation high-efficiency integrated shale gas extraction water purification device | |
| CN215327347U (en) | An integrated water-sand separation equipment for Yellow River water | |
| CN116282523A (en) | Anaerobic Tank Sludge Removal Cooperative Sand Removal System and Method | |
| CN209352686U (en) | A kind of small-scale waste water processing system | |
| CN211035519U (en) | Carwash effluent disposal system | |
| CN209052497U (en) | Three classes water sewage-treatment plant | |
| CN208454686U (en) | A municipal sewage treatment device with short treatment cycle | |
| CN207928849U (en) | A kind of pump pressure Circulated water filter |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200728 |
