CN101323484A - Nesting type multidimensional membrane assembly dynamic membrane bioreactor - Google Patents
Nesting type multidimensional membrane assembly dynamic membrane bioreactor Download PDFInfo
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- CN101323484A CN101323484A CNA2008101386422A CN200810138642A CN101323484A CN 101323484 A CN101323484 A CN 101323484A CN A2008101386422 A CNA2008101386422 A CN A2008101386422A CN 200810138642 A CN200810138642 A CN 200810138642A CN 101323484 A CN101323484 A CN 101323484A
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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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- Activated Sludge Processes (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention provides an embedding type multi-dimensional membrane element dynamic-membrane biological reactor, comprising a bed body, an aeration pipeline and a multi-dimensional membrane element. The internal part of the bed body is divided into an aeration zone and a dynamic membrane biological reaction zone. A water inlet is arranged on one side of the aeration zone of the bed body and the aeration pipeline is arranged at the bottom of the bed body; a sludge draining outlet and a water draining pipe are arranged on one side of the dynamic membrane biological reaction zone; the water draining pipe is connected with a back-washing aeration pipe, at least one group of multi-dimensional membrane element is fixed in the bed body, and each group of multi-dimensional membrane element consists of at least two layers of three-dimensional frames which are embedded mutually, and the size of each layer of three-dimensional frame is enlarged from inside to outside sequentially, and the periphery of each layer of three-dimensional frame is covered by a strainer, and the apertures of the strainers on the three-dimensional frames are enlarged from inside to outside and the clearances are filled with fillings. A duct is arranged in the innermost three-dimensional frame, and the duct of each group of multi-dimensional membrane element is connected with the water draining pipe on the bed body. The invention can effectively avoid jamming; the disposal efficiency is high; the disposed water quality is better and various waste water can be disposed; the running is stable and the service life is long.
Description
Technical field
The present invention relates to be used for the bioreactor of dynamic membrane of sewage disposal, belong to the sewage purification technology field.
Background technology
Membrane bioreactor is the novel water technology that is organically combined by membrane separation technique and bioprocess technology, replace second pond with membrane module, but have that processing efficiency height, effluent quality are good, water outlet direct reuse, occupation area of equipment are little, be convenient to advantages such as automatic control, activated sludge concentration height and excess sludge production are low.
Notification number is that the Chinese patent of CN100384520C discloses a kind of " bioreactor of dynamic membrane of 3 D filter cloth ", and its membrane module is wrapped on the framework by 3 D filter cloth and makes, and the filtering surface along continuous straight runs of membrane module is provided with scarfing.This bioreactor of dynamic membrane can effectively reduce film and stop up, and delays film and pollutes, and the backwashing period of extension reactor and the work-ing life of film base material, increases the stability that reactor moves.But the mould material that adopts is the dry goods material, causes film to pollute (being that film stops up) in operational process easily, and aquifer yield is little, often needs flushing repeatedly, and energy consumption is bigger.
Summary of the invention
The present invention is directed to the deficiency that existing membrane Bio-reactor Technology exists, the nesting type multidimensional membrane assembly dynamic membrane bioreactor that provide big, the difficult obstruction of a kind of unit membrane area, can further improve detergent power, effluent quality is good.
Nesting type multidimensional membrane assembly dynamic membrane bioreactor of the present invention adopts following technical proposals:
Nesting type multidimensional membrane assembly dynamic membrane bioreactor, comprise a body, aerated conduit and multidimensional membrane module, be divided into aeration zone and dynamic film bio reaction zone in the bed body, aeration zone one side of bed body is provided with water-in, the bottom is provided with aerated conduit, be provided with mud discharging mouth and rising pipe in dynamic film bio reaction zone one side, be connected with the back flushing aeration tube on the rising pipe, at least be fixed with one group of multidimensional membrane module in the bed body, every group of multidimensional membrane module is made up of the two-layer at least framework of about suit, each layer framework increases from the inside to the outside successively, the periphery of every layer of framework all is enclosed with filter screen, and the aperture of each layer framework upper filter screen increases successively from the inside to the outside, and all is filled with filler in the slit between the adjacent two layers framework, be provided with conduit in the inner chamber of the inside framework, the conduit in every group of multidimensional membrane module all is connected with rising pipe on the body.
Filler is a hard filler, is a kind of in haydite, gac, charcoal, stone, sand and the concrete body at least.
The past more framework nexine of the volume of filler particles is more little, so that form three-dimensional structure between each layer filler.
Framework is any solid geometry shape.
Multidimensional membrane module among the present invention constitutes with nested form, and the filter screen aperture of each layer framework increases from inside to outside successively, and pollutent is removed in layering.During operation, the water-in of sewage on the bed body flows into, and under aeration condition, microorganism breeds in a large number, thereby forms the large number of biological film on membrane module, improves processing efficiency.When sewage when having overworked biomembranous multidimensional membrane module, the particulate matter of larger aperture is directly stopped at outer space framework, and fine particle and soluble substance nexine by space framework on the dynamic membrane filtering of small-bore, sewage after being purified arrives innermost space framework inner chamber, flows out via the water outlet that is connected to intraluminal catheter in the inside space framework then.Excess sludge is then discharged by mud discharging mouth.
Multidimensional membrane module of the present invention is difficult for stopping up, back flushing easily, and the processing efficiency height, effluent quality is good, but direct reuse has been realized sewage recycling, can handle various wastewater, and is stable, life cycle is long, and is simple in structure, and operation, operation conveniently are easy to realize automatic control.
Description of drawings
Accompanying drawing is a nesting type multidimensional membrane assembly dynamic membrane bioreactor structural representation of the present invention.
Among the figure: 1, bed body, 2, water inlet pipe, 3, water distribution board, 4, the multidimensional membrane module, 5, mud discharging mouth, 6, valve, 7, air compressor, 8, aerated conduit, 9, rising pipe, 10, conduit, 11, filter screen, 12, filler, 13, the back flushing aeration tube, 14, valve, 15, valve, 16, framework.
Embodiment
As shown in drawings, nesting type multidimensional membrane assembly dynamic membrane bioreactor of the present invention mainly comprises a body 1, aerated conduit 8 and multidimensional membrane module 4, be provided with water distribution board 3 in the bed body 1, aeration zone and dynamic film bio reaction zone will be divided in the bed body 1, a side bottom is provided with water inlet pipe 2 in the aeration zone of bed body 1, the bottom is provided with aerated conduit 8, and aerated conduit 8 is connected with air outside compressor 7, and valve 6 is installed on the pipe connecting; Dynamic film bio reaction zone one side bottom at bed body 1 is provided with mud discharging mouth 5, top is provided with rising pipe 9, valve 15 is installed on the rising pipe 9, be connected with back flushing aeration tube 13 between rising pipe 9 and the air compressor 7, valve 14 is installed, to realize back flushing on the back flushing aeration tube 13 to the multidimensional membrane module.On water inlet pipe 2, mud discharging mouth 5 and the rising pipe 9 valve is installed all.Multidimensional membrane module 4 is fixed on the bottom of dynamic film bio reaction zone in the body 1, and the quantity that multidimensional membrane module 4 is set in the bed body 1 determines that according to the size of bed body 1 two groups of multidimensional membrane modules are arranged in the present embodiment.Rising pipe 9 on the bed body 1 is connected with the conduit 10 in every group of multidimensional membrane module.
Multidimensional membrane module 4 is made up of the two-layer at least framework 16 that is three-dimensional arrangement of about suit, multidimensional membrane module in the present embodiment has four layers, each layer framework increases from the inside to the outside successively, all be enclosed with filter screen 11 on each face of the periphery of every layer of framework, the aperture of each layer framework upper filter screen increases successively from the inside to the outside, and all is filled with filler 12 between the adjacent two layers space framework, and the past more nexine volume of filler 12 particles is more little, so that form three-dimensional structure between each layer filler, guarantee effluent characteristics.Be provided with conduit 10 in the inner chamber of innermost layer framework, conduit 10 is connected with the rising pipe of bed on the body 1.Filler 12 is one or more the mixture in the hard fillers such as haydite, gac, charcoal, stone, sand and concrete body.
Framework 16 can be any solid geometry shape, and available stainless steel or the welding of hard aluminium alloy material are made, and filter screen 11 can adopt stainless steel or engineering plastics to make.When the intensity of filter screen 11 was enough, framework 16 also can directly surround with filter screen.
Sewage treatment process of the present invention is:
Sewage is entered in the body 1 by water inlet pipe 2, flows through the aeration zone at aerated conduit 8 places, produces a large amount of microorganisms, enters the dynamic film bio reaction zone via water distribution board 3 then.When aeration, valve-off 14 is opened valve 6, carries out aeration.In the dynamic film bio reaction zone, microorganism forms the large number of biological film on multidimensional membrane module 4, sewage enters inner chamber through the filtration layer by layer of the filter screen in the multidimensional membrane module 4, water quality is purified, wherein bigger particulate matter is dammed by the microbial film on the filter screen of outer wide aperture, fine particulate matter and soluble substance are filtered at inner filter screen, thereby improve decontamination effect improving greatly.Treated sewage is flowed out by the rising pipe on the bed body 19 by multidimensional membrane module 4 lumen catheter 10.Mud is discharged from mud discharging mouth 5.After operation for some time, in the time of need carrying out back flushing to multidimensional membrane module 4, valve-off 6 and valve 15 are opened valve 14, carry out back flushing.
Claims (4)
1. nesting type multidimensional membrane assembly dynamic membrane bioreactor, comprise a body, aerated conduit and multidimensional membrane module, be divided into aeration zone and dynamic film bio reaction zone in the bed body, aeration zone one side of bed body is provided with water-in, the bottom is provided with aerated conduit, be provided with mud discharging mouth and rising pipe in dynamic film bio reaction zone one side, be connected with the back flushing aeration tube on the rising pipe, it is characterized in that: be fixed with one group of multidimensional membrane module at least in the bed body, every group of multidimensional membrane module is made up of the two-layer at least framework of about suit, each layer framework increases from the inside to the outside successively, the periphery of every layer of framework all is enclosed with filter screen, the aperture of each layer framework upper filter screen increases successively from the inside to the outside, and all be filled with filler in the slit between the adjacent two layers framework, be provided with conduit in the inner chamber of the inside framework, the conduit in every group of multidimensional membrane module all is connected with rising pipe on the body.
2. nesting type multidimensional membrane assembly dynamic membrane bioreactor according to claim 1 is characterized in that: described filler is a hard filler, is a kind of in haydite, gac, charcoal, stone, sand and the concrete body at least.
3. nesting type multidimensional membrane assembly dynamic membrane bioreactor according to claim 1 is characterized in that: the past more framework nexine of the volume of described filler particles is more little.
4. nesting type multidimensional membrane assembly dynamic membrane bioreactor according to claim 1 is characterized in that: described framework is any solid geometry shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008101386422A CN101323484A (en) | 2008-07-25 | 2008-07-25 | Nesting type multidimensional membrane assembly dynamic membrane bioreactor |
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| Application Number | Priority Date | Filing Date | Title |
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| CNA2008101386422A CN101323484A (en) | 2008-07-25 | 2008-07-25 | Nesting type multidimensional membrane assembly dynamic membrane bioreactor |
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| CN101323484A true CN101323484A (en) | 2008-12-17 |
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| CNA2008101386422A Pending CN101323484A (en) | 2008-07-25 | 2008-07-25 | Nesting type multidimensional membrane assembly dynamic membrane bioreactor |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101481175B (en) * | 2009-02-17 | 2010-08-25 | 天津市天水环保设计工程有限公司 | V shaped groove type microgrid component capable of continuously on-line updating dynamic membrane and use method thereof |
| CN101481174B (en) * | 2009-02-10 | 2010-12-29 | 天津市天水环保设计工程有限公司 | V shaped groove type microgrid component capable of continuously on-line updating dynamic membrane and use method thereof |
| CN101554545B (en) * | 2009-04-14 | 2011-04-20 | 天津市天水环保设计工程有限公司 | Micro-net component with continuous mobile line-shaped backwash and distributed with shock absorption and application method thereof |
| CN102381754A (en) * | 2011-09-29 | 2012-03-21 | 同济大学 | Micro-net separating biological membrane process reinforced activated sludge method for removing ammonia nitrogen |
| CN103964635A (en) * | 2014-04-28 | 2014-08-06 | 中国建筑东北设计研究院有限公司 | Metal double-layered membrane bioreactor for sewage treating |
| CN104355401A (en) * | 2014-10-27 | 2015-02-18 | 浙江开创环保科技有限公司 | Integral composite membrane bioreactor device |
| CN104773815A (en) * | 2015-03-23 | 2015-07-15 | 厦门大学 | Method utilizing active carbon to control MBR membrane pollution |
| CN105152479A (en) * | 2015-09-09 | 2015-12-16 | 大连海事大学 | Modified granular active carbon coupled membrane bioreactor (MBR) and heavy metal containing wastewater treatment method |
-
2008
- 2008-07-25 CN CNA2008101386422A patent/CN101323484A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101481174B (en) * | 2009-02-10 | 2010-12-29 | 天津市天水环保设计工程有限公司 | V shaped groove type microgrid component capable of continuously on-line updating dynamic membrane and use method thereof |
| CN101481175B (en) * | 2009-02-17 | 2010-08-25 | 天津市天水环保设计工程有限公司 | V shaped groove type microgrid component capable of continuously on-line updating dynamic membrane and use method thereof |
| CN101554545B (en) * | 2009-04-14 | 2011-04-20 | 天津市天水环保设计工程有限公司 | Micro-net component with continuous mobile line-shaped backwash and distributed with shock absorption and application method thereof |
| CN102381754A (en) * | 2011-09-29 | 2012-03-21 | 同济大学 | Micro-net separating biological membrane process reinforced activated sludge method for removing ammonia nitrogen |
| CN103964635A (en) * | 2014-04-28 | 2014-08-06 | 中国建筑东北设计研究院有限公司 | Metal double-layered membrane bioreactor for sewage treating |
| CN103964635B (en) * | 2014-04-28 | 2015-10-28 | 中国建筑东北设计研究院有限公司 | A kind of metal bi membrane bioreactor of disposing of sewage |
| CN104355401A (en) * | 2014-10-27 | 2015-02-18 | 浙江开创环保科技有限公司 | Integral composite membrane bioreactor device |
| CN104773815A (en) * | 2015-03-23 | 2015-07-15 | 厦门大学 | Method utilizing active carbon to control MBR membrane pollution |
| CN105152479A (en) * | 2015-09-09 | 2015-12-16 | 大连海事大学 | Modified granular active carbon coupled membrane bioreactor (MBR) and heavy metal containing wastewater treatment method |
| CN105152479B (en) * | 2015-09-09 | 2017-12-08 | 大连海事大学 | Modified particles activated carbon couples membrane bioreactor and heavy metal-containing wastewater treatment method |
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Open date: 20081217 |