CN201817328U - Aeration biological filter with hollow porous fiber filler and flow baffle plate - Google Patents
Aeration biological filter with hollow porous fiber filler and flow baffle plate Download PDFInfo
- Publication number
- CN201817328U CN201817328U CN2010205706742U CN201020570674U CN201817328U CN 201817328 U CN201817328 U CN 201817328U CN 2010205706742 U CN2010205706742 U CN 2010205706742U CN 201020570674 U CN201020570674 U CN 201020570674U CN 201817328 U CN201817328 U CN 201817328U
- Authority
- CN
- China
- Prior art keywords
- biological aerated
- aerated filter
- height
- baffle
- filter
- 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.)
- Expired - Fee Related
Links
- 239000000945 filler Substances 0.000 title claims abstract description 20
- 239000000835 fiber Substances 0.000 title claims abstract description 8
- 238000005273 aeration Methods 0.000 title description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 9
- 239000001301 oxygen Substances 0.000 abstract description 9
- 229910052760 oxygen Inorganic materials 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 4
- 238000011001 backwashing Methods 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 abstract description 3
- 238000012546 transfer Methods 0.000 abstract description 3
- 239000010802 sludge Substances 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 abstract description 2
- 239000012528 membrane Substances 0.000 description 9
- 239000012510 hollow fiber Substances 0.000 description 8
- 244000005700 microbiome Species 0.000 description 6
- 238000012856 packing Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 230000001788 irregular Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000011152 fibreglass Substances 0.000 description 1
- -1 gravel Substances 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- 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
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
一种中空多孔纤维填料折流曝气生物滤池,曝气生物滤池的一侧开有进水口,另一侧开有出水口,曝气生物滤池的底端分别固定连有若干块折流板ⅰ,折流板ⅰ的高度为曝气生物滤池的池壁高度的4/5,折流板ⅰ之间在曝气生物滤池的顶端分别固定连有折流板ⅱ,折流板ⅱ的高度为曝气生物滤池池壁高度的4/5,曝气生物滤池内放置有填料。本实用新型的技术效果是:提高了单位空间内的污泥浓度,该发明采用无泡供氧,氧的传质效率也大大提高,能够处理高浓度有机废水。另外,滤料在水中呈流态状,不易堵塞,可减少反冲洗频率,节约能源,减少占地面积。
A hollow porous fiber filled baffle biological aerated filter, one side of the biological aerated filter is opened with a water inlet, the other side is opened with a water outlet, and the bottom of the biological aerated filter is fixedly connected with several folding Baffle i, the height of baffle i is 4/5 of the height of the pool wall of the biological aerated filter, and between the baffle i, there are respectively fixed baffles ii and baffles at the top of the biological aerated filter. The height of plate ii is 4/5 of the height of the wall of the biological aerated filter, and fillers are placed in the biological aerated filter. The technical effect of the utility model is that the sludge concentration in a unit space is increased, the invention adopts non-bubble oxygen supply, the mass transfer efficiency of oxygen is also greatly improved, and high-concentration organic wastewater can be treated. In addition, the filter material is in a fluid state in the water and is not easy to be blocked, which can reduce the frequency of backwashing, save energy, and reduce the occupied area.
Description
技术领域technical field
本实用新型涉及一种曝气生物滤池,尤其涉及一种中空多孔纤维填料折流曝气生物滤池。The utility model relates to an aerated biological filter, in particular to a hollow porous fiber filler deflection aerated biological filter.
背景技术Background technique
曝气生物滤池是集生物氧化和截留悬浮固体于一体,节省了后续二次沉淀池,在保证处理效果的前提下使处理工艺简化,此外,曝气生物滤池工艺有机物容积负荷高、水力负荷大、水力停留时间短、所需基建投资少、能耗及运行成本低、同时该工艺出水水质高。滤料是曝气生物滤池的关键部分,对曝气生物滤池的功效有直接的影响,同时也影响到曝气生物滤池的结构形式和成本。由于制作加工和价格原因,国内目前采用的接触填料主要有玻璃钢或塑料蜂窝填料、立体波状填料、软性纤维填料、半软性填料以及不规则粒状滤料(砂、碎石、矿渣、焦炭、无烟煤)等。玻璃钢或塑料填料表面光滑,生物膜附着力差,易老化,且在实际使用中往往容易产生不同程度填料的堵塞;软性填料中的水流流态不理想,易被微生物膜粘结在一起,产生结球现象,使其有效表面积大为减小,进而在结球的内部产生厌氧现象,影响处理效果。不规则粒状填料水流阻力大,易于引起滤池堵塞。近年来我国也开展了应用片状陶粒处理水源的微污染研究,片状陶粒属不规则粒状填料,尽管挂膜性能良好,但存在水流阻力大、孔隙率小、容易堵塞、强度差、易破碎、不耐冲刷等缺陷,限制了它仅能应用于水源水的微污染处理,而不适合污水处理。正是由于这些传统的接触填料存在一定的缺陷,限制了曝气生物滤池在我国污水处理中的应用,因此选用一种好的滤池滤料非常关键。The biological aerated filter integrates biological oxidation and interception of suspended solids, saves the subsequent secondary sedimentation tank, and simplifies the treatment process under the premise of ensuring the treatment effect. Large load, short hydraulic retention time, less infrastructure investment required, low energy consumption and operating costs, and high quality effluent from the process. The filter material is a key part of the biological aerated filter, which has a direct impact on the efficacy of the biological aerated filter, and also affects the structure and cost of the biological aerated filter. Due to production, processing and price reasons, the contact fillers currently used in China mainly include glass fiber reinforced plastic or plastic honeycomb fillers, three-dimensional corrugated fillers, soft fiber fillers, semi-soft fillers, and irregular granular filter materials (sand, gravel, slag, coke, anthracite), etc. The surface of FRP or plastic packing is smooth, the adhesion of biofilm is poor, and it is easy to age, and in actual use, it is easy to cause plugging of packing to varying degrees; the flow of water in soft packing is not ideal, and it is easy to be bonded together by microbial film. The phenomenon of balling occurs, which greatly reduces the effective surface area, and then produces anaerobic phenomenon inside the ball, which affects the treatment effect. Irregular granular packing has high resistance to water flow, which is easy to cause filter blockage. In recent years, my country has also carried out micro-pollution research on the application of flaky ceramsite to treat water sources. Flake ceramsite is an irregular granular filler. Although the film-hanging performance is good, it has large water flow resistance, small porosity, easy clogging, poor strength, Defects such as fragility and intolerance to erosion limit it to be used only for micro-pollution treatment of source water, not for sewage treatment. It is precisely because these traditional contact packings have certain defects that limit the application of biological aerated filters in sewage treatment in my country, so it is very important to choose a good filter material.
发明内容Contents of the invention
本实用新型的目的在于提供了一种中空多孔纤维填料折流曝气生物滤池,采用中空多孔纤维为填料,在中空纤维内部进行曝气,并在滤池内设置折流板,克服曝气生物滤池填料易堵塞、需频繁反冲洗的缺点,提高氧气传质效率,增加水流程和水处理时间。该曝气生物滤池结构简单,在满足微生物对氧需求的同时节约空间和能源,可同时高效去除COD和氮,提高出水水质。The purpose of this utility model is to provide a hollow porous fiber filler baffle biological aerated filter, which uses hollow porous fiber as filler, aerates inside the hollow fiber, and sets baffles in the filter to overcome the aeration The shortcomings of biofilter fillers are easy to block and require frequent backwashing, which improves oxygen mass transfer efficiency and increases water flow and water treatment time. The biological aerated filter has a simple structure, can meet the oxygen demand of microorganisms while saving space and energy, can efficiently remove COD and nitrogen at the same time, and improve the quality of effluent water.
本实用新型是这样来实现的,它包括曝气生物滤池、进水口、出水口、折流板ⅰ、折流板ⅱ、填料,其特征是曝气生物滤池的一侧开有进水口,另一侧开有出水口,曝气生物滤池的底端分别固定连有若干块折流板ⅰ,折流板ⅰ的高度为曝气生物滤池的池壁高度的4/5,折流板ⅰ之间在曝气生物滤池的顶端分别固定连有折流板ⅱ,折流板ⅱ的高度为曝气生物滤池池壁高度的4/5,曝气生物滤池内放置有填料。The utility model is realized in such a way that it includes a biological aerated filter, a water inlet, a water outlet, a baffle i, a baffle ii, and fillers, and is characterized in that a water inlet is opened on one side of the biological aerated filter , there is a water outlet on the other side, and several baffles i are fixedly connected to the bottom of the biological aerated filter. The height of the baffles i is 4/5 of the height of the wall of the biological aerated filter. The top of the biological aerated filter between the baffles i is fixedly connected with the baffle ii, and the height of the baffle ii is 4/5 of the height of the wall of the biological aerated filter. filler.
本实用新型的技术效果是:水流以上下的方式流动,增加水流程和水处理时间,同时垂直于中空纤维膜,利于微生物的截留。此外,中空纤维膜的比表面积特别大,提高了单位空间内的污泥浓度,该发明采用无泡供氧,氧的传质效率也大大提高,能够处理高浓度有机废水。另外,滤料在水中呈流态状,不易堵塞,可减少反冲洗频率,节约能源,减少占地面积。The technical effect of the utility model is: the water flows in an up and down manner, increases the water flow and water treatment time, and at the same time is perpendicular to the hollow fiber membrane, which is beneficial to the interception of microorganisms. In addition, the specific surface area of the hollow fiber membrane is particularly large, which increases the sludge concentration in a unit space. The invention uses non-bubble oxygen supply, and the oxygen mass transfer efficiency is also greatly improved, which can treat high-concentration organic wastewater. In addition, the filter material is in a fluid state in the water and is not easy to be blocked, which can reduce the frequency of backwashing, save energy, and reduce the occupied area.
附图说明Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
图2为本实用新型填料的结构示意图。Fig. 2 is a structural schematic diagram of the filler of the present invention.
在图中,1、曝气生物滤池 2、进水口 3、出水口 4、折流板ⅰ 5、折流板ⅱ 6、填料。In the figure, 1. Biological aerated filter 2. Water inlet 3. Water outlet 4. Baffle ⅰ 5. Baffle ⅱ 6. Packing.
具体实施方式Detailed ways
如图1、图2所示,本实用新型是这样来实现的,曝气生物滤池1的一侧开有进水口2,另一侧开有出水口3,曝气生物滤池1的底端分别固定连有若干块折流板ⅰ4,折流板ⅰ4的高度为曝气生物滤池1的池壁高度的4/5,折流板ⅰ4之间在曝气生物滤池1的顶端分别固定连有折流板ⅱ5,折流板ⅱ5的高度为曝气生物滤池1池壁高度的4/5,曝气生物滤池1内放置有填料6。反应器运行时,污水由进水口2流入,空气或纯氧通过空气管进入中空纤维的内腔,通过膜扩散供氧,污水通过折流板ⅰ4均匀布水,水流以一定的角度流过折流板间的疏水性中空微孔纤维束填料6,微生物附着在中空纤维膜表面,氧扩散通过膜后,直接被附着在膜外壁的微生物利用。滤料在水中呈流态状,不易堵塞。在整个运行过程中,水流整体成推流状态,以一定角度流过中空纤维膜,利于微生物的截留。同时,被中空纤维膜截留住的微生物由于与中空纤维膜直接接触,会得到充足的氧。此外,微生物生长所需的营养物质也因污水的进入不断得到供应。经一定时间运行后,可适当对滤料进行反冲洗。As shown in Figure 1 and Figure 2, the utility model is realized in this way, one side of the biological aerated filter 1 is provided with a water inlet 2, and the other side is provided with a water outlet 3, and the bottom of the biological aerated filter 1 A number of baffles i4 are fixedly connected to the ends respectively, and the height of the baffles i4 is 4/5 of the height of the pool wall of the biological aerated filter 1, and the tops of the biological aerated filter 1 between the baffles i4 are respectively The baffle plate ⅱ5 is fixedly connected, and the height of the baffle plate ⅱ5 is 4/5 of the height of the wall of the biological aerated filter tank 1, and the
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010205706742U CN201817328U (en) | 2010-10-21 | 2010-10-21 | Aeration biological filter with hollow porous fiber filler and flow baffle plate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010205706742U CN201817328U (en) | 2010-10-21 | 2010-10-21 | Aeration biological filter with hollow porous fiber filler and flow baffle plate |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201817328U true CN201817328U (en) | 2011-05-04 |
Family
ID=43915291
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010205706742U Expired - Fee Related CN201817328U (en) | 2010-10-21 | 2010-10-21 | Aeration biological filter with hollow porous fiber filler and flow baffle plate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201817328U (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105399279A (en) * | 2015-12-17 | 2016-03-16 | 宜兴市东方水设备有限公司 | Ship sanitary sewage multilevel processing biochemical box |
CN106587334A (en) * | 2016-12-30 | 2017-04-26 | 南京悠谷知识产权服务有限公司 | Self-cleaning biotrickling filter and application thereof to emulsion waste water treatment |
CN107459152A (en) * | 2017-09-30 | 2017-12-12 | 邱学尧 | A kind of bio-contact oxidation filtering settling pond |
CN107792935A (en) * | 2017-11-27 | 2018-03-13 | 江苏宜裕环保科技有限公司 | A kind of deflector type removes ammonia denitrogenation BAF |
CN111620446A (en) * | 2020-06-05 | 2020-09-04 | 北京赛富威环境工程技术有限公司 | Treatment method of high-concentration phenol-containing industrial wastewater |
-
2010
- 2010-10-21 CN CN2010205706742U patent/CN201817328U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105399279A (en) * | 2015-12-17 | 2016-03-16 | 宜兴市东方水设备有限公司 | Ship sanitary sewage multilevel processing biochemical box |
CN106587334A (en) * | 2016-12-30 | 2017-04-26 | 南京悠谷知识产权服务有限公司 | Self-cleaning biotrickling filter and application thereof to emulsion waste water treatment |
CN106587334B (en) * | 2016-12-30 | 2020-04-07 | 南京悠谷知识产权服务有限公司 | Self-cleaning biological trickling filter and application thereof in emulsion wastewater treatment |
CN107459152A (en) * | 2017-09-30 | 2017-12-12 | 邱学尧 | A kind of bio-contact oxidation filtering settling pond |
CN107792935A (en) * | 2017-11-27 | 2018-03-13 | 江苏宜裕环保科技有限公司 | A kind of deflector type removes ammonia denitrogenation BAF |
CN111620446A (en) * | 2020-06-05 | 2020-09-04 | 北京赛富威环境工程技术有限公司 | Treatment method of high-concentration phenol-containing industrial wastewater |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103880193B (en) | Build the method for vertical current constructed wetland processing breeding wastewater based on waterworks sludge | |
CN201534813U (en) | Composite filler biofilter | |
CN201834804U (en) | Biological aeration filter | |
CN203866157U (en) | Integrated baffle type anaerobic/anoxic/aerobic membrane filtration high-concentration organic wastewater treatment device | |
CN102092896B (en) | A kind of dual-membrane type bio-reactor | |
CN201817328U (en) | Aeration biological filter with hollow porous fiber filler and flow baffle plate | |
CN201634500U (en) | A biological aerated filter | |
CN204162570U (en) | A kind of light electrolysis/aerobic/anaerobic/membrane filtration treatment unit | |
CN201932988U (en) | Anaerobic/aerobic contact oxidation membrane bioreactor | |
CN102249480A (en) | System and operating method for treating rubbish leachate and urban household sewage in combined way | |
CN101704575B (en) | Energy-saving and aerating filling device and integrated oxidization and sedimentation basin having same | |
CN201598221U (en) | Biological filter - ceramic membrane bioreactor device | |
CN101434435B (en) | Method and apparatus for using aerating biological filter in advanced treatment of dyeing waste water | |
CN205241449U (en) | Water ecological remediation system | |
CN206562380U (en) | A kind of unpowered sewage complex biological processing integrated apparatus | |
CN201890824U (en) | Advanced purification combination device for polluted surface water | |
CN205061690U (en) | Anaerobism - good oxygen integrative sewage treatment device | |
CN103304098A (en) | Volcanic filler-based sewage treatment system of biological aerated filter | |
CN204281406U (en) | A kind of membrane bioreactor based on fouling membrane in-situ control | |
CN101786722B (en) | Soft and hard double-bed double-filler anaerobic filter | |
CN107162313A (en) | A kind of integral type river course high-efficiency water purifying treatment device | |
CN205575883U (en) | Domestic sewage treatment device | |
CN203382614U (en) | Treatment device for landfill leachate | |
CN206188490U (en) | Handle high concentration organic waste water's device | |
CN105174626A (en) | Constructed wetland coupled biological reaction tank purification water-gas system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110504 Termination date: 20121021 |