CN2598995Y - Self-controlled rapid biofilm reaction sewage treatment equipment - Google Patents
Self-controlled rapid biofilm reaction sewage treatment equipment Download PDFInfo
- Publication number
- CN2598995Y CN2598995Y CNU032333471U CN03233347U CN2598995Y CN 2598995 Y CN2598995 Y CN 2598995Y CN U032333471 U CNU032333471 U CN U032333471U CN 03233347 U CN03233347 U CN 03233347U CN 2598995 Y CN2598995 Y CN 2598995Y
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- China
- Prior art keywords
- water
- connects
- ultrafiltration membrane
- pump
- aeration
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- 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.)
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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
- 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
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
自控快速生物膜反应污水处理设备，其特征在于：初滤器8、精滤器9顺次连接后连接超滤膜生物反应器10的进水口，超滤膜生物反应器10的底部为曝气管12，曝气管12与进气阀13和曝气泵15连接，超滤膜生物反应器10的内部有超滤组件11，超滤组件11为外压中空纤维超滤膜，两侧为收集管22，收集管22上部连通出水管23，出水管23连接出水泵16，出水泵16的出水口连接中水箱17的进水口，臭氧机18的气体出口连接中水箱17的进水口；臭氧机18，内有臭氧发生器；能有效处理污水，大大减少污水中的有机物、无机物、杀菌、消毒、脱色。
The automatic control rapid biofilm reaction sewage treatment equipment is characterized in that: the primary filter 8 and the fine filter 9 are connected in sequence and then connected to the water inlet of the ultrafiltration membrane bioreactor 10, and the bottom of the ultrafiltration membrane bioreactor 10 is an aeration pipe 12 , the aeration pipe 12 is connected with the air inlet valve 13 and the aeration pump 15, and the ultrafiltration membrane bioreactor 10 has an ultrafiltration module 11 inside, and the ultrafiltration module 11 is an external pressure hollow fiber ultrafiltration membrane, and both sides are collecting pipes 22. The upper part of the collection pipe 22 is connected to the water outlet pipe 23, the water outlet pipe 23 is connected to the water outlet pump 16, the water outlet of the water outlet pump 16 is connected to the water inlet of the middle water tank 17, the gas outlet of the ozone machine 18 is connected to the water inlet of the middle water tank 17; the ozone machine 18 , There is an ozone generator inside; it can effectively treat sewage, greatly reduce organic and inorganic substances in sewage, sterilize, disinfect and decolorize.
Description
Technical field: the utility model relates to waste disposal plant.
Technical background: a main approach that solves the pollution of shortage of water resources and water is water treatment, in numerous lacks of water city is not have water, but water resources severe exacerbation, do not meet service requirements, if can pass through both economically feasibles, reliable again stable method is handled, and makes water satisfy the various requirement of user and environment, and recycle, then water shortage problem will be alleviated significantly.
Summary of the invention:
The purpose of this utility model is to provide a kind of automatic control quick bio film reaction sewage disposal device.
Automatic control quick bio film reaction sewage disposal device of the present utility model, comprise: screen cloth 1, screen cloth 2 are arranged in the water inlet pipe of equalizing tank 6, aeration tube 4 is fixed on the middle and lower part of equalizing tank 6, aeration pump 3 connects aeration tube 4, the water outlet of equalizing tank 6 connects intake pump 7, the bottom sealing and fixing wash water valve 5 of equalizing tank 6;
Primary filter 8, secondary filter 9 connects the water-in that the back connects ultrafiltration membrane bioreactor 10 in turn, the bottom of ultrafiltration membrane bioreactor 10 is an aeration tube 12, aeration tube 12 is connected with aeration pump 15 with intake valve 13, there is ultrafiltration module 11 inside of ultrafiltration membrane bioreactor 10, ultrafiltration module 11 is the external pressure hollow fiber ultrafiltration membrane--be called microbial film again, both sides are collection tube 22, collection tube 22 tops are communicated with rising pipe 23, rising pipe 23 connects water pump 16 and recoil valve 14, the other end of recoil valve 14 connects intake valve 13, the water-in of water tank 17 during the water outlet that goes out water pump 16 connects, the water-in of water tank 17 during the pneumatic outlet of ozone machine 18 connects;
Adorn superfine order grid in the primary filter 8, dress PE film in the secondary filter 9, the filtering membrane of PE film for making through special process by polyethylene and tackiness agent, the aperture is 1～5 μ m.Also can adorn the PP film in the secondary filter 9, the filtering membrane of PP film for making through special process by polypropylene and tackiness agent.Market is on sale.
Principle: the main purpose of screen cloth 1,2 is large particulate matters that pump, valve and other equipment can be blocked or block to removal.
Aeration pump 3, aeration tube 4, wash water valve 5, equalizing tank 6, the effect of intake pump 7, because waste water is not to flow into the sewage disposal unit with fixed flow rate, flow velocity reflects the rule of life of service community over time, in most of demanding party units, daily life, mode of operation can influence wastewater flow and pollution level, because wastewater flow and concentration constantly change, make the waste water operation be difficult to effectively carry out, therefore automatic control quick bio film reaction sewage disposal device must design by Peak Flow Rate, the result causes these facilities excessive under the mean flow rate situation, for the above-mentioned reasons, the purpose of Flow-rate adjustment, reduce water yield fluctuation exactly, make waste water almost enter automatic control quick bio film reaction sewage disposal device of the present utility model, improve service ability with the fixed flow velocity.
The purpose of primary filter 8 is further to remove big particulate matter, and the purpose of secondary filter 9 is to remove most SSC, can remove more than 90%, and attach and remove number of C OD, BOD, bacterium etc., and the colourity of sewage has clear improvement at this.
Ultrafiltration membrane bioreactor 10, comprise: ultrafiltration module 11 is the external pressure hollow fiber ultrafiltration membrane--be called microbial film again, exposed membrane fiber bundle is placed in the activated sludge reactor, make formation negative pressure (about 0.1Mpa) in the hollow-fibre membrane owing to go out the suction function of water pump 16, water enters in the external pressure hollow-fibre membrane in the reactor, after both sides collection tube 22 compiled, via going out water pump 16 water outlets, liquid level and Inlet and outlet water were by automatic controlling system in the ultrafiltration membrane bioreactor 10;
Aeration pump 15 is imported aeration tube 12 after air is imported intake valve 13 again, be used for aeration, aeration directly impacts the membrane fiber of the external pressure hollow fiber ultrafiltration membrane of shake under water, the aqueous vapor two-phase is the cross-flow form and impacts to prevent face deposition affects water flux, go out water tank 17 in water pump 16 cooperations, be used to collect finished product water.When needing recoil aeration tube 12, start recoil valve 14, water enters aeration tube 12 through intake valve 13, cleans.The purpose of recoil is in order to prolong the external pressure hollow fiber ultrafiltration membrane--is called biomembranous work-ing life again, guarantees the stable of water flux.Wash water valve 19, residual sea water pump 20 are used for draining-off sewage; Ozone machine 18, in ozonizer is arranged, it mainly is to remove a large amount of bacterium in the water, further removes colourity, COD, BOD etc.
Advantage and effect: through after the device processes of the present utility model, COD, BOD, turbidity, SS clearance can reach 90%-100%, and following table is a waste water and through water-quality ratio after the device processes of the present utility model,
| COD/ (mg.L) | BOD (mg.L) | SS/ (mg.L) | Turbidity/degree | Colourity/degree | PH | |
| Waste water | 600 | 400 | 700 | 500 | 10 | 5-8 |
| Water outlet | ＜60 | ＜20 | 0 | ＜3 | ＜1 | 7-7.5 |
Description of drawings: Fig. 1: automatic control quick bio film reaction sewage disposal device of the present utility model.
Each several part numbering among the figure: screen cloth 1, screen cloth 2, aeration pump 3, aeration tube 4, wash water valve 5, equalizing tank 6, intake pump 7, primary filter 8, secondary filter 9, ultrafiltration membrane bioreactor 10, ultrafiltration module 11, aeration tube 12, intake valve 13, recoil valve 14, aeration pump 15, go out water pump 16, middle water tank 17, ozone machine 18, wash water valve 19, residual sea water pump 20, collection tube 22, rising pipe 23.
Embodiment: see Fig. 1, automatic control quick bio film reaction sewage disposal device of the present utility model comprises:
Screen cloth 1, screen cloth 2 are arranged in the water inlet pipe of equalizing tank 6, and aeration tube 4 is fixed on the middle and lower part of equalizing tank 6, and aeration pump 3 connects aeration tube 4, and the water outlet of equalizing tank 6 connects intake pump 7, the bottom sealing and fixing wash water valve 5 of equalizing tank 6;
Primary filter 8, secondary filter 9 connects the water-in that the back connects ultrafiltration membrane bioreactor 10 in turn, the bottom of ultrafiltration membrane bioreactor 10 is an aeration tube 12, aeration tube 12 is connected with aeration pump 15 with intake valve 13, there is ultrafiltration module 11 inside of ultrafiltration membrane bioreactor 10, ultrafiltration module 11 is the external pressure hollow fiber ultrafiltration membrane--be called microbial film again, both sides are collection tube 22, collection tube 22 tops are communicated with rising pipe 23, rising pipe 23 connects water pump 16 and recoil valve 14, the other end of recoil valve 14 connects intake valve 13, the water-in of water tank 17 during the water outlet that goes out water pump 16 connects, the water-in of water tank 17 during the pneumatic outlet of ozone machine 18 connects;
Adorn superfine order grid in the primary filter 8, dress PE film in the secondary filter 9, the filtering membrane of PE film for making through special process by polyethylene and tackiness agent, the aperture is 1～5 μ m.Also can adorn the PP film in the secondary filter 9, the filtering membrane of PP film for making through special process by polypropylene and tackiness agent.Market is on sale.
During installation, screen cloth 1, screen cloth 2, aeration pump 3, aeration tube 4, wash water valve 5, equalizing tank 6, intake pump 7 are that the user builds installation in addition.Connect primary filter 8, secondary filter 9, ultrafiltration membrane bioreactor 10, middle water tank 17, ozone machine 18 more in turn.Wherein, ozone machine 18 is outsourcing pieces.Ozone can the oxidation inorganics, organism, can sterilization, and the oxidation capacity of ozone is very strong, and sterilization, sterilization, deodorization, decolouring aspect are had significant effect.
Claims (2)
1, automatic control quick bio film reaction sewage disposal device, it is characterized in that: primary filter (8), secondary filter (9) connects the water-in that the back connects ultrafiltration membrane bioreactor (10) in turn, the bottom of ultrafiltration membrane bioreactor (10) is aeration tube (12), aeration tube (12) is connected with aeration pump (15) with intake valve (13), there is ultrafiltration module (11) inside of ultrafiltration membrane bioreactor (10), ultrafiltration module (11) is the external pressure hollow fiber ultrafiltration membrane, both sides are collection tube (22), collection tube (22) top is communicated with rising pipe (23), rising pipe (23) connects water pump (16) and recoil valve (14), the other end of recoil valve (14) connects intake valve (13), the water-in of water tank (17) during the water outlet that goes out water pump (16) connects, the water-in of water tank (17) during the pneumatic outlet of ozone machine (18) connects.
2, automatic control quick bio film reaction sewage disposal device according to claim 1, it is characterized in that: adorn superfine order grid in the primary filter (8), dress PE film in the secondary filter (9), the filtering membrane of PE film for making through special process by polyethylene and tackiness agent, the aperture is 1～5 μ m; Secondary filter also can be adorned the PP film in (9), the filtering membrane of PP film for being made through special process by polypropylene and tackiness agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU032333471U CN2598995Y (en) | 2003-02-28 | 2003-02-28 | Self-controlled rapid biofilm reaction sewage treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU032333471U CN2598995Y (en) | 2003-02-28 | 2003-02-28 | Self-controlled rapid biofilm reaction sewage treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2598995Y true CN2598995Y (en) | 2004-01-14 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU032333471U Expired - Fee Related CN2598995Y (en) | 2003-02-28 | 2003-02-28 | Self-controlled rapid biofilm reaction sewage treatment equipment |
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| CN (1) | CN2598995Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100340500C (en) * | 2004-05-21 | 2007-10-03 | 叶茂杨 | Middle water reuse process with compound bacteria and membrane bioreactor and apparatus therefor |
| CN100375726C (en) * | 2005-10-27 | 2008-03-19 | 韩春来 | Membrane refinery sewage recycling method and equipment |
| CN102050505A (en) * | 2009-11-03 | 2011-05-11 | Lg电子株式会社 | Immersion type membrane separator device |
| CN101200331B (en) * | 2006-10-12 | 2011-09-28 | 北京碧水源科技股份有限公司 | Method for producing reclaimed water by membrane bioreactor-ozone combination technique |
| CN102642950A (en) * | 2012-05-04 | 2012-08-22 | 郑州大学 | Device utilizing ozone to carry out oxidization decoloration treatment |
| CN102674637A (en) * | 2012-05-30 | 2012-09-19 | 汪硕 | Household sewage treatment equipment |
| CN106007212A (en) * | 2016-07-11 | 2016-10-12 | 佛山杰致信息科技有限公司 | Composite type biological decomposition membrane sewage treating system |
-
2003
- 2003-02-28 CN CNU032333471U patent/CN2598995Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100340500C (en) * | 2004-05-21 | 2007-10-03 | 叶茂杨 | Middle water reuse process with compound bacteria and membrane bioreactor and apparatus therefor |
| CN100375726C (en) * | 2005-10-27 | 2008-03-19 | 韩春来 | Membrane refinery sewage recycling method and equipment |
| CN101200331B (en) * | 2006-10-12 | 2011-09-28 | 北京碧水源科技股份有限公司 | Method for producing reclaimed water by membrane bioreactor-ozone combination technique |
| CN102050505A (en) * | 2009-11-03 | 2011-05-11 | Lg电子株式会社 | Immersion type membrane separator device |
| CN102050505B (en) * | 2009-11-03 | 2015-09-16 | Lg电子株式会社 | Immersion type membrane separator device |
| CN102642950A (en) * | 2012-05-04 | 2012-08-22 | 郑州大学 | Device utilizing ozone to carry out oxidization decoloration treatment |
| CN102642950B (en) * | 2012-05-04 | 2013-08-28 | 郑州大学 | Device utilizing ozone to carry out oxidization decoloration treatment |
| CN102674637A (en) * | 2012-05-30 | 2012-09-19 | 汪硕 | Household sewage treatment equipment |
| CN106007212A (en) * | 2016-07-11 | 2016-10-12 | 佛山杰致信息科技有限公司 | Composite type biological decomposition membrane sewage treating system |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |