CN201648104U - A sleeve filter device for sewage reuse - Google Patents
A sleeve filter device for sewage reuse Download PDFInfo
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- CN201648104U CN201648104U CN2010200468729U CN201020046872U CN201648104U CN 201648104 U CN201648104 U CN 201648104U CN 2010200468729 U CN2010200468729 U CN 2010200468729U CN 201020046872 U CN201020046872 U CN 201020046872U CN 201648104 U CN201648104 U CN 201648104U
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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
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
一种用于污水回用的套筒过滤装置涉及污水处理及回用领域。本实用新型公开了一种污水回用装置。其主体是一个套筒型滤池。套筒中心区域为上向流的曝气生物滤池或粗滤料深床滤池。套筒外部环状空间上下分层,为并联运行的慢滤池。该装置充分利用了曝气生物滤池的外部空间,有效避免了慢滤池占地面积大的缺点,利用快滤池去除浊度和有机物并为慢滤池提供低浊度进水,利用慢滤池进一步去除浊度,并去除色度和臭味等。本装置可用于污水二级处理出水的深度处理,以生产高品质再生水。
A sleeve filter device for sewage reuse relates to the field of sewage treatment and reuse. The utility model discloses a sewage recycling device. Its main body is a sleeve type filter. The central area of the sleeve is an upflow biological aerated filter or a deep bed filter with coarse filter material. The outer annular space of the sleeve is layered up and down, which is a slow filter running in parallel. The device makes full use of the external space of the biological aerated filter, effectively avoids the disadvantage of a large area occupied by the slow filter, uses the fast filter to remove turbidity and organic matter and provides low turbidity inflow water for the slow filter The filter further removes turbidity, and removes color and odor, etc. The device can be used for advanced treatment of secondary sewage treatment effluent to produce high-quality reclaimed water.
Description
技术领域technical field
本实用新型涉及污水处理及回用领域,是用于污水回用或污水深度处理的一种装置。The utility model relates to the field of sewage treatment and reuse, and is a device for sewage reuse or advanced treatment of sewage.
背景技术Background technique
污水回用是解决我国水资源短缺的有效途径。为此,我国诸多城市纷纷兴建污水回用工程,很多城市的小区和大型公共建筑也安装了中水回用装置。然而当前市场上的污水回用装置存在诸多不足之处。如以澄清过滤为原理的装置虽然处理成本较低,但出水水质较差;以膜技术为核心的装置虽然出水浊度低,水质优良,但投资和运行费用较高;以人工湿地为核心单元的装置虽然运行费用低,但占地面积过大;以活性炭吸附为主的装置虽然能有效去除色度和臭味,但投资和运行费用较高。为此迫切需要开发高效低耗、占地面积小的污水回用装置。Sewage reuse is an effective way to solve the shortage of water resources in my country. For this reason, many cities in our country have built sewage reuse projects one after another, and reclaimed water reuse devices have also been installed in residential areas and large public buildings in many cities. However, there are many deficiencies in the sewage reuse devices currently on the market. For example, although the treatment cost of the device based on clarification and filtration is low, the quality of the effluent is poor; the device based on membrane technology has low turbidity and good water quality, but the investment and operation costs are high; the core unit is the artificial wetland. Although the operating cost of the device is low, the floor area is too large; although the device based on activated carbon adsorption can effectively remove color and odor, the investment and operating cost are relatively high. For this reason, it is urgent to develop a sewage recycling device with high efficiency, low consumption and small footprint.
实用新型内容Utility model content
本实用新型提供了一种污水回用组合装置。该装置用于污水二级处理出水的深度处理,具有出水水质好、占地面积小和运行费用低的优点。The utility model provides a combined device for recycling sewage. The device is used for advanced treatment of effluent from secondary sewage treatment, and has the advantages of good effluent quality, small floor space and low operating cost.
一种污水再生处理及回用装置,其特征在于,包括两个套在一起的同心柱,内柱为曝气生物滤池;外柱与内柱围成的环状空间被至少分割为上下两个并联运行的慢滤池;利用曝气生物滤池的围护结构将曝气生物滤池和慢滤池在空间上分开;曝气生物滤池出水管、曝气生物滤池反冲洗排水管和慢滤池进水管合用一根管道;A sewage regeneration treatment and reuse device, characterized in that it includes two concentric columns nested together, the inner column is a biological aerated filter; the annular space surrounded by the outer column and the inner column is at least divided into upper and lower two Two slow filter tanks running in parallel; the biological aerated filter tank and the slow filter tank are separated in space by the enclosure structure of the biological aerated filter tank; the outlet pipe of the biological aerated filter tank and the backwash drain pipe of the biological aerated filter tank Share a pipe with the slow filter inlet pipe;
该管道上设有至少三个阀门;其中两个阀门分别设置在慢滤池进水处,一个阀门设置在管道末端作为排水用。通过管道上阀门的切换实现三种管道功能。The pipeline is provided with at least three valves; two of the valves are respectively arranged at the water inlet of the slow filter tank, and one valve is arranged at the end of the pipeline for drainage. Three pipeline functions are realized by switching the valve on the pipeline.
本实用新型采用的技术方案是:The technical scheme that the utility model adopts is:
(1)在工艺上采用曝气生物滤池和慢滤池组合的方式。曝气生物滤池不仅具有过滤功能,可去除水中悬浮颗粒,降低水的浊度,而且具有生物作用,可降解溶解性有机物和硝化氨氮。慢滤具备良好的出水水质,不仅能够降低水的浊度,而且对色度、臭味以及细菌病毒等具有良好的去除效果。且慢滤的运行费用低廉,管理简单。(1) In terms of technology, the combination of biological aerated filter and slow filter is adopted. Biological aerated filter not only has filtering function, can remove suspended particles in water, reduce water turbidity, but also has biological function, can degrade dissolved organic matter and nitrified ammonia nitrogen. Slow filtration has good effluent quality, not only can reduce the turbidity of water, but also has a good removal effect on color, odor, bacteria and viruses. Moreover, the operation cost of the slow filter is low, and the management is simple.
当进水有机物浓度较低时,也可停止曝气,将曝气生物滤池按照普通快滤池运行。When the concentration of organic matter in the influent is low, the aeration can also be stopped, and the biological aerated filter can be operated as a normal fast filter.
(2)在形状上,曝气生物滤池属于“瘦高”型,而慢滤池属于“矮胖”型。为了充分利用空间和减少占地面积,将曝气生物滤池和慢滤池在空间上组合在一起,做成一个竖直摆放的套筒形状。即中心小套筒作为曝气生物滤池,外筒与中心小套筒围成的环状空间作为慢滤池。曝气生物滤池位于慢滤池中心位置。利用曝气生物滤池的围护结构将二者在空间上分开。根据曝气生物滤池的高度,可将套筒的环状空间分成上下多层,作为并联运行的慢滤池。具体设计时应根据水质情况,确定曝气生物滤池和慢滤池的设计参数,然后确定慢滤层数,套筒中心区域(曝气生物滤池)和外部环状区域(慢滤池)的面积。(2) In terms of shape, the biological aerated filter belongs to the "thin and tall" type, while the slow filter belongs to the "short and fat" type. In order to make full use of the space and reduce the occupied area, the biological aerated filter and the slow filter are spatially combined to form a vertical sleeve shape. That is, the central small sleeve serves as the biological aerated filter, and the annular space surrounded by the outer cylinder and the central small sleeve serves as the slow filter. The biological aerated filter is located in the center of the slow filter. The enclosure structure of the biological aerated filter is used to separate the two in space. According to the height of the biological aerated filter, the annular space of the sleeve can be divided into upper and lower layers, as a slow filter running in parallel. In the specific design, the design parameters of the biological aerated filter and the slow filter should be determined according to the water quality, and then the number of slow filter layers, the central area of the sleeve (biological aerated filter) and the outer annular area (slow filter) should be determined. area.
(3)为了布置紧凑、节约管材,曝气生物滤池出水管、曝气生物滤池反冲洗排水管和慢滤池进水管合用一根管道。通过管道上阀门的切换实现三种管道功能。(3) In order to arrange compactly and save pipe materials, the outlet pipe of the biological aerated filter, the backwash drain pipe of the biological aerated filter and the inlet pipe of the slow filter share one pipe. Three pipeline functions are realized by switching the valve on the pipeline.
污水二级处理出水作为本实用新型装置的进水。水自套筒中心空间的底部(曝气生物滤池底部)进入,上向流动至套筒中心空间顶部(曝气生物滤池顶部),然后经过分流装置进入套筒环状区域的上下各层(慢滤池)。水经过慢滤后进入集水装置,然后进入清水箱做消毒等下一步处理。曝气生物滤池反冲洗采用上向流操作方式。反冲洗时,装置停止进水,反冲洗排水经分流装置排出。慢滤需要刮砂时,装置停止进水,将慢滤池放空,然后人工刮砂。The secondary treatment effluent of sewage is used as the water inflow of the device of the utility model. Water enters from the bottom of the central space of the sleeve (the bottom of the biological aerated filter), flows upward to the top of the central space of the sleeve (the top of the biological aerated filter), and then enters the upper and lower layers of the annular area of the sleeve through the diversion device (slow filter). The water enters the water collection device after being slowly filtered, and then enters the clean water tank for disinfection and other next steps. The backwashing of the biological aerated filter adopts the upward flow operation mode. When backwashing, the device stops water intake, and the backwashing water is discharged through the diversion device. When the slow filter needs sand scraping, the device stops water intake, empty the slow filter, and then manually scrape the sand.
该技术方案充分利用了两种过滤方式的优点。曝气生物滤池滤速快,能有效去除水中悬浮物、化学需氧量(COD)、生化需氧量(BOD)、浊度和氨氮等污染物质,且为慢滤池提供低浊度进水,避免了慢滤池堵塞。慢滤池对色度和臭味有良好的去除效果。二者组合后出水水质可达到甚至优于城镇污水处理厂污染物排放标准(GB 18918-2002)中的一级A标准和城市污水再生利用城市杂用水水质(GB/T 18920-2002)标准。该水可用于冲厕、道路清扫、消防、城市绿化、车辆冲洗、建筑施工的非饮用水及景观环境用水等。The technical scheme fully utilizes the advantages of the two filtering methods. The biological aerated filter has a fast filtration rate, which can effectively remove suspended solids, chemical oxygen demand (COD), biochemical oxygen demand (BOD), turbidity and ammonia nitrogen and other pollutants in the water, and provide low turbidity for the slow filter. water, avoiding the clogging of the slow filter. The slow filter has a good removal effect on color and odor. After the combination of the two, the effluent water quality can reach or even exceed the first-class A standard in the pollutant discharge standard for urban sewage treatment plants (GB 18918-2002) and the urban miscellaneous water quality for urban sewage recycling (GB/T 18920-2002) standard. The water can be used for toilet flushing, road cleaning, fire protection, urban greening, vehicle washing, non-drinking water for building construction and water for landscape environment, etc.
套筒式结构避免了曝气生物滤池和慢滤池的缺点。曝气生物滤池占地面积不大,但池体较高,一般在4m以上。慢滤池占地面积较大,但高度有限,可不超过2m。因此将二者做成套筒型结构,与单独放置两个滤池相比,极大节约了占地面积和空间。The sleeve structure avoids the disadvantages of biological aerated filter and slow filter. The biological aerated filter covers a small area, but the pool body is relatively high, generally above 4m. The slow filter covers a large area, but its height is limited, which may not exceed 2m. Therefore, the two are made into a sleeve-shaped structure, which greatly saves the occupied area and space compared with placing two filter tanks separately.
附图说明:Description of drawings:
图1是本实用新型的结构剖视图。Fig. 1 is a structural sectional view of the utility model.
具体实施方式Detailed ways
本实用新型装置的主体结构由两个套在一起的同心柱组成,内柱为曝气生物滤池1。外柱与内柱围成的环状空间被分割为上下两个并联运行的慢滤池。柱的截面可以为但不局限于圆形或者矩形。The main structure of the device of the utility model is composed of two concentric columns nested together, and the inner column is a biological aerated filter tank 1 . The annular space surrounded by the outer column and the inner column is divided into two upper and lower slow filter tanks running in parallel. The cross-section of the columns can be, but not limited to, circular or rectangular.
利用曝气生物滤池的围护结构将曝气生物滤池和慢滤池在空间上分开;曝气生物滤池出水管、曝气生物滤池反冲洗排水管和慢滤池进水管合用一根管道;即图中的分流管18。The enclosure structure of the biological aerated filter is used to separate the biological aerated filter and the slow filter in space; the outlet pipe of the biological aerated filter, the backwash drain pipe of the biological aerated filter and the inlet pipe of the slow filter are combined root pipeline; that is, the
该管道上设有至少三个阀门;其中两个阀门分别设置在慢滤池进水处,一个阀门设置在管道末端作为排水用。通过管道上阀门的切换实现三种管道功能。The pipeline is provided with at least three valves; two of the valves are respectively arranged at the water inlet of the slow filter tank, and one valve is arranged at the end of the pipeline for drainage. Three pipeline functions are realized by switching the valve on the pipeline.
曝气生物滤池1从下至上由连接有进水管11和进气管12的混合室13、多孔板14、承托层15、滤层16、连接有分流管18的清水区17组成。分流管上设置阀门I 48、阀门II 46和阀门III45。另外进水管11配备进水阀IV42和反冲洗进水阀V41;进气管12上设有进气阀VI44。The biological aerated filter 1 is composed of a
慢滤池I 2和慢滤II池3的组成相同。以慢滤池I 2为例,从上至下由储水区21、砂层22、承托层23和集水管24组成。其中集水管24上配备阀门VIII47。Slow filter I 2 and slow filter II
本实用新型装置运行方式如下;The utility model device mode of operation is as follows;
过滤时,打开进水阀IV42,关闭反冲洗进水阀V 41,水通过进水管11进入混合室13。同时,打开进气阀VI44,空气经进气管12进入混合室13。水和气在混合室13混合后通过多孔板14进入承托层15,然后进入滤层16,再到清水区17,最后进入分流管18。此时分流管上阀门III45关闭,阀门I 48和阀门II 46打开。水通过阀门I 48进入慢滤池I 2,通过阀门II 46进入慢滤II池3。When filtering, open the water inlet valve IV42, close the backwash water inlet valve V41, and water enters the
曝气生物滤池1反冲洗时,关闭进水阀IV42,打开反冲洗进水阀V41,打开进气阀VI44。同时关闭分流管上阀门I 48和阀门II46,打开阀门III45,将反冲洗废水排出。When BAF 1 backwashes, close water inlet valve IV42, open backwash water inlet valve V41, and open air inlet valve VI44. At the same time, close the valve I48 and the valve II46 on the shunt pipe, open the valve III45, and discharge the backwash waste water.
两个慢滤池为并联运行。以慢滤池I 2为例,过滤时来自曝气生物滤池1的水通过阀门I 48首先进入储水区21,然后缓慢流过砂层22,进入位于承托层23内部的集水管24,最后通过阀门VIII47排出。Two slow filters run in parallel. Taking the slow filter I 2 as an example, the water from the biological aerated filter 1 first enters the
慢滤池需要刮砂时,关闭曝气生物滤池1的进水阀IV42、进气阀VI44和反冲洗进水阀V 41。然后打开阀门VIII47将慢滤池I 2放空,将慢滤池I 2内砂层22的表面刮掉即可。When the slow filter needs to scrape sand, close the inlet valve IV42, inlet valve VI44 and backwash inlet valve V41 of biological aerated filter 1. Then open valve VIII47 to empty the slow filter tank I 2, and scrape off the surface of the
本实用新型装置用于污水深度处理,可用于污水二级处理后的出水的再生处理。二级出水经过该装置后经过消毒即可用于冲厕、道路清扫、消防、城市绿化、车辆冲洗、建筑施工等城市杂用或景观水补水。The device of the utility model is used for advanced treatment of sewage, and can be used for regeneration treatment of effluent after secondary treatment of sewage. After passing through the device, the secondary effluent can be used for toilet flushing, road cleaning, fire protection, urban greening, vehicle washing, building construction and other urban miscellaneous purposes or landscape water replenishment after disinfection.
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| CN2010200468729U CN201648104U (en) | 2010-01-15 | 2010-01-15 | A sleeve filter device for sewage reuse |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102765803A (en) * | 2012-07-02 | 2012-11-07 | 北京工业大学 | Shallow layer stacking and slow filtering device and process method thereof |
| CN102897916A (en) * | 2012-10-25 | 2013-01-30 | 宁夏宝塔石化集团有限公司 | Biological two-stage aeration filter pool and water distribution and air distribution method of pool body |
| CN107055754A (en) * | 2017-01-24 | 2017-08-18 | 河海大学 | A kind of circulation Zero-valent Iron biofilter of intensive treatment domestic sewage in rural areas |
| CN108017141A (en) * | 2017-11-29 | 2018-05-11 | 湖北大学 | A kind of slow draining treament system of biology |
-
2010
- 2010-01-15 CN CN2010200468729U patent/CN201648104U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102765803A (en) * | 2012-07-02 | 2012-11-07 | 北京工业大学 | Shallow layer stacking and slow filtering device and process method thereof |
| CN102765803B (en) * | 2012-07-02 | 2013-10-16 | 北京工业大学 | Shallow layer stacking and slow filtering process method |
| CN102897916A (en) * | 2012-10-25 | 2013-01-30 | 宁夏宝塔石化集团有限公司 | Biological two-stage aeration filter pool and water distribution and air distribution method of pool body |
| CN102897916B (en) * | 2012-10-25 | 2014-02-26 | 宁夏宝塔石化集团有限公司 | Biological two-stage aeration filter pool and water distribution and air distribution method of pool body |
| CN107055754A (en) * | 2017-01-24 | 2017-08-18 | 河海大学 | A kind of circulation Zero-valent Iron biofilter of intensive treatment domestic sewage in rural areas |
| CN108017141A (en) * | 2017-11-29 | 2018-05-11 | 湖北大学 | A kind of slow draining treament system of biology |
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