CN1420088A - Aerobic bio-membrane sewage treating device - Google Patents
Aerobic bio-membrane sewage treating device Download PDFInfo
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- CN1420088A CN1420088A CN02157780A CN02157780A CN1420088A CN 1420088 A CN1420088 A CN 1420088A CN 02157780 A CN02157780 A CN 02157780A CN 02157780 A CN02157780 A CN 02157780A CN 1420088 A CN1420088 A CN 1420088A
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- rice
- mixing tank
- device case
- oxygenation
- water
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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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- Biological Treatment Of Waste Water (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
An aerobic biomembrane device for treating sewage is composed of a cylindrical or rectangular casing for containing sewage, aerating mixers which are vertically and uniformly fixed to the bottom of said casing, and biologic carrier filler which has biomembrane on its surface and is distributed around each aerating mixer. The compressed air is uniformly distributed to each aerating mixer. When sewage flows through said aerating mixers and filler, the oxygen and organic substances are transferred to said biomembrane to decompose the organic substances by the microbes in biomembrane. Its advantages are high effect, high biomembrane forming speed and low energy consumption.
Description
Technical field:
The present invention relates to a kind of sewage aerobic microbial film treatment unit, be used for city domestic sewage and industrial waste water purifying and handle and reuse, belong to technical field of sewage.
Background technology:
In the prior art, the aerobe membrane treatment appts of a kind of being referred to as " contact oxidation pond " is widely used for the purifying treatment of city dirt sewage alive and trade effluent.The typical construction of this device is: be used for aerator to the water oxygenation be placed in the carrier filler layer that adhered to microbial film below, pressurized air arrives aerator by pipeline, forming bubble flow by it then discharges in water, bubble flow is upward through and arrives the water surface from the bottom of packing layer, in this process, contained oxygen is dissolved in the water in the bubble, reaches the purpose of oxygenation.Dissolved oxygen in the water finishes to organic degraded and removal in the water it by diffusing into biomembranous inside, offer the microorganism of living therein.
In said process, influencing treatment unit, normally to bring into play the most critical key element of effect be the kind of aerator and the mounting arrangements mode in device thereof.At present, the kind of aerator generally adopts two kinds; A kind of is " the pore type aerator " that can produce micro-bubble, another kind is airflow to be cut into " the turbulent flow type aerator " that disperses bubble, their mounting arrangements mode is the interval by 0.4m-0.6m, flatly be placed in apart from the treatment unit bottom surface 0.1m-0.2m that makes progress, and apart from packing layer the 0.2m-0.4m place that faces down.
Facts have proved that there are following problem in such aerator and mounting arrangements mode:
1, bubble flow is violent to the disturbance of packing layer, causes microorganism to adhere to the biofilm difficulty on filler, causes the packing layer mechanical stability poor simultaneously, and intensity fatigue takes place the packing layer support body material easily, causes the packing layer landslide, and treatment unit is damaged;
2, the flow-shape in the packing layer is bad, the resistance to flow of horizontal direction is very big, dead water region exists in a large number, do not reach the mass transfer effect of expection, cause zone, many places biofilm development inhomogeneous, organic matter degradation is removed inefficiency, influence microbial film simultaneously and upgraded the function performance that comes off automatically, cause packing layer to stop up easily, make the further deterioration of the flow-shape in the packing layer, finally cause the disabler of treatment unit.
Because the existence of the problems referred to above makes the processing efficiency in this kind contact oxidation pond be difficult to raising, the increase of maintenance management difficulty.
Summary of the invention;
The objective of the invention is at the deficiencies in the prior art, propose a kind of sewage aerobic microbial film treatment unit of novel texture, can not only improve sewage treating efficiency, and maintenance management is easy.
For realizing such purpose, sewage aerobic microbial film treatment unit provided by the invention, mainly constitute by the device case that can hold water, bio-carrier and oxygenation mixing tank, the oxygenation mixing tank is evenly distributed on the bottom surface of device case in the mode of upright and axle center spacing equalization, its cylindrical shell base and device case bottom surface keep a segment distance, bio-carrier be distributed in the oxygenation mixing tank around.Current upwards flow in the oxygenation mixing tank on one side, dissolving on one side absorbs the airborne oxygen of compression, after flowing out the oxygenation mixing tank, current just in packing layer, begin to flow downward, and oxygen and organism passed to microbial film attached to filling surface, make organism by the microbiological degradation in the microbial film.
Rounded or the rectangle of the transverse shape of device case of the present invention, the degree of depth of water is a 3-5 rice in the device, the height of biologic packing material layer is a 2-4 rice, the bottom surface of packing layer is a 0.3-0.5 rice apart from the distance of device case bottom surface, the transverse shape of oxygenation mixing tank is circle or rectangle, when being circular cross sections, the diameter of oxygenation mixing tank is a 0.15-0.40 rice, when being rectangular cross section, its bond length is a 0.15-0.40 rice, the oxygenation mixing tank is the mode uniform distribution of 1.0-1.6 rice and the bottom surface that is fixed on device case with upright and axle center spacing, its cylindrical shell base is a 0.15-0.4 rice apart from the distance of device case bottom surface, the bio-carrier layer is distributed in around it, and pressurized air is given each oxygenation mixing tank by air line and the uniformly distributing of air volume regulating valve door.
The aerator that is used for to the water oxygenation is the oxygenation mixing tank with jet enhanced feature, it is placed in the centre of the carrier filler layer that has adhered to microbial film, pressurized air arrives oxygenation mixing tank and the ejection of the shower nozzle from oxygenation mixing tank jet enhancing tube by pipeline, air-flow mixes mutually with current in the jet enhancing tube, form gas one liquid two-phase, and the water cycle of packing layer bottom is flowed.In this process, contained oxygen is dissolved in the water in the air-flow, reaches the purpose of oxygenation.Simultaneously, the dissolved oxygen in the water offers the microorganism of living therein by spreading the biomembranous inside that constantly enters into attached on the filler, and it is finished organic degraded and removal in the water, reaches the purpose of purifying treatment sewage.
The oxygenation mixing tank adopts gas one water jet pump principle design, and its mass transfer mode is a foundation with the interface renewal theory.
Facts have proved, the present invention has solved the existing problem in present contact oxidation pond fully, and the current in no current dead angle and the packing layer are laminar flow in the device, so biomembranous formation time is very short, only need 1/5-/10 times in contact oxidation pond, can form in promptly 24 hours, and the growth of dirt thing film is even, the lifeless matter film is grown later or the problem that is difficult to come off and results in blockage.Biomembranous specific surface area is big, very superior to current filtration contact performance, and therefore the current concentration of suspension limpid, that go out in the flowing water in the device is very low.
Biofilm carrier of the present invention and maintenance microbial film have the filler of enough surface-area to adopt the hairbrush shape of polyethylene material or block diamond hole netted (chalina shape) filler of spray silk moulding.
The present invention has advantages such as power consumption is low, microbial film forms soon, treatment effect is good, maintenance management is convenient, is applicable to the various purifying treatment that contain the organism sewage or waste water.
Description of drawings:
Fig. 1 is a structural representation of the present invention.
Fig. 2 is a plan structure synoptic diagram of the present invention.
Among Fig. 1 Fig. 2,1 is aerobe membrane treatment appts housing, and 2 are water inlet, and 3 are the oxygenation mixing tank, and 4 is air line, and 5 is water (flow) direction, and 6 is packing layer, and 7 is water, and 8 is air compressor, and 9 is the air flow rate adjustment valve door, and 10 are water outlet.
Fig. 3 is the structural representation of oxygenation mixing tank of the present invention.
Among Fig. 3,11 are oxygenation mixing tank jet enhancing tube, and arrow 12 indications are the inflation direction, and 13 is the jet splash head, and 14 is gas one liquid two-phase flow direction.
Embodiment:
Below in conjunction with accompanying drawing technical scheme of the present invention is further described.
As shown in the figure, device of the present invention mainly by the device case 1 that can hold water, bio-carrier 6, oxygenation mixing tank 3, air compressor 8 and intake 2, water outlet 10 and air line 4, valve 9 constitute.
Rounded or the rectangle of the transverse shape of device case 1, the degree of depth of water 7 is a 3-5 rice in the device, the height of biologic packing material layer 6 is a 2-4 rice, the bottom surface of packing layer 6 is a 0.3-0.5 rice apart from the distance of device case 1 bottom surface, the transverse shape of oxygenation mixing tank 3 is circle or rectangle, when being circular cross sections, the diameter of oxygenation mixing tank 3 is a 0.15-0.40 rice, when being rectangular cross section, its bond length is a 0.15-0.40 rice, oxygenation mixing tank 3 is the mode uniform distribution of 1.0-1.6 rice and the bottom surface that is fixed on device case 1 with upright and axle center spacing, its cylindrical shell base is a 0.15-0.4 rice apart from the distance of device case 1 bottom surface, bio-carrier layer 6 is distributed in around it, the pressurized air that air compressor 8 provides by air volume regulating valve door 9 and air line 4 uniformly distributings to each oxygenation mixing tank 3.
The aerator that is used for to the water oxygenation is the oxygenation mixing tank 3 with jet enhanced feature, it is placed in the centre of the carrier filler layer 6 that has adhered to microbial film, pressurized air is by the inflation direction 12 arrival oxygenation mixing tanks 3 of pipeline 4 along arrow indication among Fig. 3, and ejection in the shower nozzle 13 from oxygenation mixing tank jet enhancing tube 11, air-flow mixes mutually with current in the jet enhancing tube, form gas one liquid two-phase, and constantly the water of the packing layer bottom direction shown in the arrow 14 in the figure is circulated.In this process, contained oxygen is dissolved in the water in the air-flow, reaches the purpose of oxygenation.Simultaneously, the dissolved oxygen in the water offers the microorganism of living therein by spreading the biomembranous inside that constantly enters into attached on the filler, and it is finished organic degraded and removal in the water, reaches the purpose of purifying treatment sewage.
In the oxygenation process, current constantly are raised the top of packing layer through oxygenation mixing tank 3 by the bottom of packing layer, then flow downward, pass filter material layer, and the circulation up and down that forms current mixes.In such circulation mixing process, the main body of the current inlet end of slave unit gradually flows to exit end, and its flow pattern is horizontal sinusoidal wave formula piston flow.In this process, constantly from current, organism is adsorbed to its surface and carries out metabolism attached to the microbial film of filling surface, it is decomposed into water and carbonic acid gas, the organic concentration in the current is reduced.
Claims (3)
1, a kind of sewage aerobic microbial film treatment unit, it is characterized in that mainly comprising the device case (1) that can hold water, bio-carrier (6) and oxygenation mixing tank (3), rounded or the rectangle of transverse shape of device case (1), the depth of water is 3-5 rice in the device, the height of biologic packing material (6) is a 2-4 rice, the bottom surface of packing layer is a 0.3-0.5 rice apart from the distance of device case (1) bottom surface, the transverse shape of oxygenation mixing tank (3) is circle or rectangle, oxygenation mixing tank (3) is the mode uniform distribution of 1.0-1.6 rice and the bottom surface that is fixed on device case (1) with upright and axle center spacing, its cylindrical shell base is a 0.15-0.4 rice apart from the distance of device case (1) bottom surface, bio-carrier (6) is distributed in around it, and the pressurized air that air compressor (8) provides is given each oxygenation mixing tank (3) by air volume regulating valve door (9) and air line (4) uniformly distributing.
2, as the said sewage aerobic microbial film of claim 1 treatment unit, when the transverse shape that it is characterized in that the oxygenation mixing tank was circular cross sections, its diameter was a 0.15-0.40 rice, and when being rectangular cross section, its bond length is a 0.15-0.40 rice.
3,, it is characterized in that bio-carrier (6) adopts the hairbrush shape of polyethylene material or the block diamond hole gauze packing of spray silk moulding as the said sewage aerobic microbial film of claim 1 treatment unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021577803A CN1226200C (en) | 2002-12-26 | 2002-12-26 | Aerobic bio-membrane sewage treating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021577803A CN1226200C (en) | 2002-12-26 | 2002-12-26 | Aerobic bio-membrane sewage treating device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1420088A true CN1420088A (en) | 2003-05-28 |
| CN1226200C CN1226200C (en) | 2005-11-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021577803A Expired - Fee Related CN1226200C (en) | 2002-12-26 | 2002-12-26 | Aerobic bio-membrane sewage treating device |
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| CN (1) | CN1226200C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100340498C (en) * | 2004-09-11 | 2007-10-03 | 中国石油化工股份有限公司 | Microbial filler and production thereof |
| CN101913732A (en) * | 2010-08-04 | 2010-12-15 | 中国海洋大学 | Sequencing batch type suspended filler biofilm sewage treatment device |
| WO2013169091A1 (en) * | 2012-05-11 | 2013-11-14 | Ronser Bio-Tech Sdn Bhd | Zero discharge treatment system of palm oil mill effluent (pome) |
| CN103508623A (en) * | 2012-06-29 | 2014-01-15 | 中国海洋石油总公司 | Treatment method of coal gasification wastewater |
| CN110437990A (en) * | 2014-04-09 | 2019-11-12 | Nch公司 | Detect the detection system and method for the microorganism growth in fluid and water system |
-
2002
- 2002-12-26 CN CNB021577803A patent/CN1226200C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100340498C (en) * | 2004-09-11 | 2007-10-03 | 中国石油化工股份有限公司 | Microbial filler and production thereof |
| CN101913732A (en) * | 2010-08-04 | 2010-12-15 | 中国海洋大学 | Sequencing batch type suspended filler biofilm sewage treatment device |
| CN101913732B (en) * | 2010-08-04 | 2012-03-21 | 中国海洋大学 | Sequencing batch type suspended filler biofilm sewage treatment device |
| WO2013169091A1 (en) * | 2012-05-11 | 2013-11-14 | Ronser Bio-Tech Sdn Bhd | Zero discharge treatment system of palm oil mill effluent (pome) |
| CN103508623A (en) * | 2012-06-29 | 2014-01-15 | 中国海洋石油总公司 | Treatment method of coal gasification wastewater |
| CN103508623B (en) * | 2012-06-29 | 2015-10-28 | 中国海洋石油总公司 | A kind for the treatment of process of coal gasification waste water |
| CN110437990A (en) * | 2014-04-09 | 2019-11-12 | Nch公司 | Detect the detection system and method for the microorganism growth in fluid and water system |
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| Publication number | Publication date |
|---|---|
| CN1226200C (en) | 2005-11-09 |
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Granted publication date: 20051109 Termination date: 20181226 |