CN201999792U - Internal circulation moving bed bioreactor - Google Patents
Internal circulation moving bed bioreactor Download PDFInfo
- Publication number
- CN201999792U CN201999792U CN2011200006508U CN201120000650U CN201999792U CN 201999792 U CN201999792 U CN 201999792U CN 2011200006508 U CN2011200006508 U CN 2011200006508U CN 201120000650 U CN201120000650 U CN 201120000650U CN 201999792 U CN201999792 U CN 201999792U
- Authority
- CN
- China
- Prior art keywords
- carrier
- zone
- water
- aerobic zone
- moving bed
- 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 - Lifetime
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 239000000969 carrier Substances 0.000 claims abstract description 47
- 238000010992 reflux Methods 0.000 claims description 15
- 239000007921 spray Substances 0.000 claims description 5
- 239000010865 sewage Substances 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 6
- 238000005516 engineering process Methods 0.000 abstract description 5
- 244000005700 microbiome Species 0.000 abstract description 4
- 238000005273 aeration Methods 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 6
- 229910052698 phosphorus Inorganic materials 0.000 description 6
- 239000011574 phosphorus Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 3
- 230000004059 degradation Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 241000565118 Cordylophora caspia Species 0.000 description 2
- 206010061529 Polyp Diseases 0.000 description 2
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound [N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 description 2
- 230000003851 biochemical process Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 230000000813 microbial Effects 0.000 description 2
- 238000006396 nitration reaction Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- AHEWZZJEDQVLOP-UHFFFAOYSA-N Bromobimane Chemical compound BrCC1=C(C)C(=O)N2N1C(C)=C(C)C2=O AHEWZZJEDQVLOP-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 244000052616 bacterial pathogens Species 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000002906 microbiologic Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000000630 rising Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
The utility model discloses an internal circulation moving bed bioreactor, which aims to solve the problems of low denitrification and dephosphorization efficiencies and the like of the conventional moving bed technology. The bioreactor comprises an anaerobic zone, an aerobic zone and a settling zone which are independent of one another, wherein water flow flows into the bioreactor from the anaerobic zone; an annular water distribution device, a special carrier promotion and distribution device, a carrier backflow opening, a carrier and a water inlet overflow weir are arranged in the anaerobic zone; an aeration device and a dive stirrer are arranged at the bottom of the aerobic zone; a carrier recycling device and a spraying faucet are arranged at the tail end of the aerobic zone to separate the carrier from the water flow; a water outlet overflow weir and a water collection tank are arranged at the tail end of the aerobic zone; and the settling zone is arranged in the form that the same wall is shared by the settling zone and the aerobic zone. Due to the adoption of the structure, the bioreactor has the characteristics of high efficiency and the like, saves energy, is easy and convenient to operate and maintain and is particularly suitable for sewage treatment plants in small towns. A moving bed can provide a more appropriate growing environment for microorganisms, so that a denitrification function is intensified and a dephosphorization function is increased while the bioreactor has the advantages of the conventional moving bed bioreactor, and the popularization and application of the process of the bioreactor are further facilitated.
Description
Technical field
The utility model relates to a kind of moving-bed bioreactor, relates in particular to a kind of internal circulation moving bed bio-reactor of high-efficient denitrification and dephosphorization.
Background technology
The municipal sewage plant not only needs to have the function of removing organic pollutant, but also need have the function of denitrogenation dephosphorizing.In many sewage water treatment methods, biochemical process since have power consumption less, advantage such as secondary pollution is light, working cost is low, be most widely used.A kind of especially biochemical process efficiently of MBBR sewage treatment process.Moving-bed bioreactor belongs to the biomembrance process water technology, the density and the water of the microbe carrier that it adopts are approaching, under the situation of aeration or stirring, move with current, collision between producing mutually, prolong the mass transfer route, improved mass transfer effect, make the microbial film that is attached on the carrier have thin, the active high characteristics of rete simultaneously, organism had very strong absorption degradation ability, and can effectively remove ammonia nitrogen in the sewage, but traditional moving-bed bioreactor dephosphorization scarce capacity.In recent years, samll cities and towns' sewage disposal is flourish, emerges multiple integrated water technology.But because traditional moving-bed bioreactor, the deficiency aspect denitrification denitrogenation, dephosphorization has limited its popularization.
The utility model content
In order to overcome above-mentioned defective, the purpose of this utility model is to provide that a kind of denitrogenation dephosphorizing function is strong, the internal circulation moving bed bio-reactor of compact construction.
In order to achieve the above object, internal circulation moving bed bio-reactor of the present utility model comprises reactor body, and described reactor body inside is provided with anaerobic zone, aerobic zone and settling region; Be filled with a certain amount of carrier in described anaerobic zone, the aerobic zone; Described anaerobic zone is disposed with annular water distributor from bottom to top, is provided with the water inlet overflow weir that carrier promotes distribution device and is communicated with aerobic zone; Described annular water distributor connects water-in; Be provided with submersible agitator and aerating apparatus in the aerobic zone; Be communicated with between described aerobic zone and the settling region; Described settling region is provided with water outlet; Described anaerobic zone bottom is provided with the carrier refluxing opening, and eaves is provided with flow deflector in the described carrier refluxing opening connection carrier retrieving arrangement, described carrier refluxing opening.
Wherein, the tail end of described aerobic zone is provided with outlet, and described outlet is communicated with the water outlet overflow weir, and the outlet of described water outlet overflow weir connects water leg, and described water leg is through being communicated with described settling region communicating pipe.
Described carrier-recovering device lower end links to each other with eaves on the refluxing opening, and is tilted at an angle, and its upper end is higher than the water surface.The spray water tap is set near the upper end of this carrier-recovering device.
Above-mentioned structure, pending sewage enters anaerobic zone 1 by annular water distributor 4, be provided with the device 5 that is used to promote and distributes carrier in the anaerobic zone 1, be provided with carrier refluxing opening 6 in the bottom of anaerobic zone 1, be provided with carrier and water inlet overflow weir 7 at the top of anaerobic zone 1, the carrier 15 that is back to anaerobic zone 1 enters aerobic zone 2 with water inlet by overflow weir 7.Aerobic zone 2 bottoms are provided with aerating apparatus 8 and submersible agitator 9 along water (flow) direction, at the tail end of aerobic zone 2 carrier-recovering device 11 and spray water tap 10 are set, and are used for carrier of separating 15 and mud mixture, and are provided with water outlet overflow weir 13 and water leg 12.Water leg 12 is connected by communicating pipe 14 with the settling region, and mud mixture enters the settling region through communicating pipe 14.Settling region 3 adopts the arrangement form that is total to wall with aerobic zone 2, to reducing the construction costs.
Because moving-bed bioreactor has characteristics such as efficient, energy-conservation, that operation and maintenance are easy, be particularly suitable for sewage work of samll cities and towns and use.This moving-bed can provide the growing environment that is more suitable for for microorganism, makes it when possessing traditional moving-bed bioreactor advantage, and intensified anti-nitrated function and increase phosphorus removal functional more help applying of this technology.
Description of drawings
Fig. 1 is the structural representation of the utility model specific embodiment.
Fig. 2 be among Fig. 1 along A-A to the sectional structure synoptic diagram.
Fig. 3 be among Fig. 1 along B-B to the sectional structure synoptic diagram.
Description of drawings: anaerobic zone 1, aerobic zone 2, settling region 3, annular water distributor 4, dedicated carrier promotes and partitioning device 5, carrier refluxing opening 6, carrier and water inlet overflow weir 7, aerating apparatus 8, submersible agitator 9, spray water tap 10, carrier-recovering device 11, water leg 12, water outlet overflow weir 13, communicating pipe 14, carrier 15.
Embodiment
Below in conjunction with drawings and Examples the utility model is described in further detail.
As Figure 1-3, internal circulation moving bed bio-reactor of the present utility model comprises anaerobic zone 1, aerobic zone 2, settling region 3, and anaerobic zone 1, aerobic zone 2 are filled carrier 15.Anaerobic zone 1 is provided with annular water distributor 4 and dedicated carrier promotes and assigned unit 5, and this device is furnished with 1 grade or multistage lifting impeller.Anaerobic zone 1 bottom is provided with carrier refluxing opening 6, and opening length is the 1/4-1/2 of anaerobic zone girth, and width is 0.5m-2m, and eaves is provided with flow deflector in the carrier refluxing opening 6.Anaerobic zone 1 top is provided with carrier and water inlet overflow weir 7, and weir length is the 1/2-1 of anaerobic zone girth.
Aerobic zone 2 long-width ratios are 1: 1-3: 1, and the bottom is provided with aerating apparatus 8, and oxygen and hybrid power are provided.Aerobic zone 2 head ends link to each other with anaerobic zone 1 overflow weir 7, and tail end and anaerobic zone 1 carrier refluxing opening 6 join.Aerobic zone 2 goes out head piece and is located at this district's tail end, and mud mixture enters water leg 12 by overflow weir 13, enters settling region 3 through communicating pipe 14.Perforated plastic plate or fabric are installed as the carrier-recovering device 11 that separates water outlet and carrier to the zone between the refluxing opening 6 near aerobic zone 2 overflow weirs 13 head end places, carrier-recovering device 11 is in tilted layout, the upper end exceeds aerobic zone 2 liquid levels, the lower end links to each other with eaves on the refluxing opening 6, spray water tap 10 being set, utilize the pressure water of its ejection to disperse the carrier of building up in carrier-recovering device 11 head ends 15 near carrier-recovering device 11 upper ends.Can or submersible agitator 9 be set according to the practical situation setting in the aerobic zone 2.Settling region 3 adopts the rectangular sedimentation tank form, and settling region 3 one sides and aerobic zone 2 be wall altogether.
In the present embodiment, carrier 15 is filled in reactor anaerobic zone 1 and aerobic zone 2, and cyclic motion therein, the microorganism that carrier 15 surface attachment are a large amount of.Anaerobic zone 1 play intensified anti-nitrated with release the effect of phosphorus, aerobic zone 2 plays the effect of degradation of organic substances, nitrated, part denitrification, dephosphorization, carrier of separating 15 and current, settling region 3 plays the effect that separates excess sludge and water outlet.
Working process is as follows: sewage mixes with the carrier 15 that flows into from anaerobic zone 1 bottom through specific equipment 5 liftings from anaerobic zone 1 annular water distributor 4 inflow reactors, and the microbial film adsorb organic compound carries out anti-nitration reaction.Along with the rising of current and the lifting of 5 pairs of carriers 15 of specific equipment, oxygen in the anaerobic zone 1 and nitric nitrogen also reduce along with the increase of height, produce absolute anaerobic environment in the anaerobic zone 1, and microorganism is efficiently released phosphorus.After sewage and carrier rise to anaerobic zone 1 top, under the help of distribution device 5, flow into aerobic zone 2.Be provided with densely arranged aerating apparatus 8 in the aerobic zone 2, for the microbiological deterioration organism provides sufficient oxygen, and quicken carrier 15 and current mix the consequently content of organism, ammonia nitrogen, phosphorus decline in the sewage, the part anti-nitration reaction takes place, carrier 15 surface biological film fast updating.After current and carrier 15 entered the carrier-recovering device 11 of aerobic zone 2 tail ends, carrier 15 descended, and current rise, carrier 15 is back to anaerobic zone 1 bottom, current are dispensed to settling region 3 through overflow weir 13, thereby realize mud-water separation, and excess sludge and water outlet enter the subsequent disposal unit respectively.The material of described carrier-recovering device 11 is perforated plastic plate or fabric.
Above-mentioned structure, compared with prior art, internal circulation moving bed bio-reactor has the following advantages:
The tradition moving-bed bioreactor is higher than general activated sludge process to organic removal efficient, but its shortcoming is that the denitrogenation dephosphorizing effect is relatively poor, and especially dephosphorization aspect often need just can make sewage disposal up to standard by physico-chemical process.Internal circulation moving bed bio-reactor is when keeping traditional moving-bed bioreactor efficient degradation organism characteristics, for polyP bacteria has been created the growing environment that aerobic and absolute anaerobism alternates, help polyP bacteria growth, release phosphorus and poly-phosphorus, the dephosphorization ability of reactor is obviously improved, and the denitrifying capacity of reactor is strengthened.
Internal circulation moving bed bio-reactor is provided with partition wall between aerobic zone and anaerobic zone, obviously reduced oxygen and shifted the destruction of anaerobic zone anaerobic environment and the oxygen loss of aerobic zone, has improved the working efficiency of aerobic zone and anaerobic zone simultaneously, reduces reactor volume.
Internal circulation moving bed bio-reactor is integrated in anaerobic zone, aerobic zone, settling region among the same device, reduces floor space, reduces laid down cost, and simplifies flow process, reduces hydraulic loss, can save running cost.
The utility model is not limited to above-mentioned embodiment, no matter do any variation on its shape or structure, every to utilize above-mentioned internal circulation moving bed bio-reactor all be a kind of distortion of the present utility model, all should think and drop within the utility model protection domain.
Claims (3)
1. an internal circulation moving bed bio-reactor comprises reactor body, it is characterized in that, described reactor body inside is provided with anaerobic zone, aerobic zone and settling region; Fill carrier in described anaerobic zone, the aerobic zone; Described anaerobic zone is disposed with annular water distributor from bottom to top, carrier promotes distribution device and reaches the water inlet overflow weir that is communicated with aerobic zone; Described annular water distributor connects water-in; Be provided with submersible agitator and aerating apparatus in the aerobic zone; Wall and being communicated with altogether between described aerobic zone and the settling region; Described settling region is provided with water outlet; Described anaerobic zone bottom is provided with the carrier refluxing opening, and eaves is provided with flow deflector in the described carrier refluxing opening connection carrier retrieving arrangement, described carrier refluxing opening.
2. internal circulation moving bed bio-reactor as claimed in claim 1, it is characterized in that the tail end of described aerobic zone is provided with outlet, described outlet is communicated with the water outlet overflow weir, the outlet of described water outlet overflow weir connects water leg, and described water leg is through being communicated with described settling region communicating pipe.
3. internal circulation moving bed bio-reactor as claimed in claim 1 or 2 is characterized in that, described carrier-recovering device lower end links to each other with eaves on the refluxing opening, and is tilted at an angle, and its upper end is higher than the water surface.The spray water tap is set near the upper end of this carrier-recovering device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200006508U CN201999792U (en) | 2011-01-04 | 2011-01-04 | Internal circulation moving bed bioreactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200006508U CN201999792U (en) | 2011-01-04 | 2011-01-04 | Internal circulation moving bed bioreactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201999792U true CN201999792U (en) | 2011-10-05 |
Family
ID=44702538
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200006508U Expired - Lifetime CN201999792U (en) | 2011-01-04 | 2011-01-04 | Internal circulation moving bed bioreactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201999792U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2555893C2 (en) * | 2013-11-15 | 2015-07-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Московский государственный строительный университет" (ФГБОУ ВПО "МГСУ") | Method of deep biological purification of sewage waters from organic compounds and ammonium salt nitrogen |
| NO336908B1 (en) * | 2014-05-28 | 2015-11-23 | Hias Iks | Method for biological water purification of wastewater in a continuous process, as well as reactor for continuous biological water purification of wastewater. |
| CN105110458A (en) * | 2015-10-09 | 2015-12-02 | 大连宇都环境工程技术有限公司 | Dredging type wastewater treatment filler circulation system |
| CN105110459A (en) * | 2015-10-09 | 2015-12-02 | 大连宇都环境技术材料有限公司 | Filler intercepting and dredging system for sewage treatment |
| CN105110456A (en) * | 2015-10-09 | 2015-12-02 | 大连宇都环境技术材料有限公司 | Filler intercepting and dredging system with low energy consumption |
| CN105152312A (en) * | 2015-10-09 | 2015-12-16 | 大连宇都环境技术材料有限公司 | Filler interception and drainage system |
-
2011
- 2011-01-04 CN CN2011200006508U patent/CN201999792U/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2555893C2 (en) * | 2013-11-15 | 2015-07-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Московский государственный строительный университет" (ФГБОУ ВПО "МГСУ") | Method of deep biological purification of sewage waters from organic compounds and ammonium salt nitrogen |
| NO336908B1 (en) * | 2014-05-28 | 2015-11-23 | Hias Iks | Method for biological water purification of wastewater in a continuous process, as well as reactor for continuous biological water purification of wastewater. |
| NO20140660A1 (en) * | 2014-05-28 | 2015-11-23 | Hias Iks | Method for biological water treatment of wastewater in a continuous process, as well as reactor for continuous biological water treatment of wastewater. |
| US10280099B2 (en) | 2014-05-28 | 2019-05-07 | Hias How2O As | Method for biological purification of waste water |
| CN105110458A (en) * | 2015-10-09 | 2015-12-02 | 大连宇都环境工程技术有限公司 | Dredging type wastewater treatment filler circulation system |
| CN105110459A (en) * | 2015-10-09 | 2015-12-02 | 大连宇都环境技术材料有限公司 | Filler intercepting and dredging system for sewage treatment |
| CN105110456A (en) * | 2015-10-09 | 2015-12-02 | 大连宇都环境技术材料有限公司 | Filler intercepting and dredging system with low energy consumption |
| CN105152312A (en) * | 2015-10-09 | 2015-12-16 | 大连宇都环境技术材料有限公司 | Filler interception and drainage system |
| CN105110456B (en) * | 2015-10-09 | 2017-07-11 | 大连宇都环境技术材料有限公司 | Low energy consumption filler is intercepted and persuasion system |
| CN105110459B (en) * | 2015-10-09 | 2017-08-08 | 大连宇都环境技术材料有限公司 | Filling for sewage treatment is intercepted and persuasion system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100473616C (en) | Overlay sewage biochemical reactor | |
| CN202089869U (en) | High-efficient composite reaction device for anaerobic organism | |
| CN201999792U (en) | Internal circulation moving bed bioreactor | |
| CN102838205B (en) | External continuous flow aerobic granular sludge membrane bioreactor | |
| CN102701521A (en) | Low-energy-consumption low-carbon-emission economical energy-saving urban sewage treatment method | |
| CN101633531A (en) | Sewage treatment reactor for alternately operating intermittent flow and continuous flow | |
| CN209872514U (en) | Composite ecological reactor based on A2O | |
| CN103708618A (en) | Micro-power municipal sewage treatment equipment and process | |
| CN101468846B (en) | Sectional inlet and drop oxygenation and contact oxidation integrated sewage treating apparatus and method | |
| CN206512058U (en) | A kind of efficient villages and small towns waste water treating and reutilizing device | |
| CN111559837A (en) | Landfill leachate biochemical treatment system and process | |
| CN201313853Y (en) | Biofilm reaction equipment for wastewater treatment | |
| CN102951731B (en) | Airlift oxidation ditch type membrane bioreactor | |
| CN202400904U (en) | Denitrification-dephosphorization water purifier | |
| CN209890441U (en) | Integrated MBBR sewage treatment equipment | |
| CN202186922U (en) | Air-lift type internal recycle de-nitrogenizing and phosphorus-removing bioreactor | |
| CN204298147U (en) | The multistage SND nitrogen rejection facility of a kind of integral type | |
| CN101386446B (en) | Air-lift baffling internal circulation bioreactor and use method thereof | |
| CN100500593C (en) | Combined type wastewater treatment method and equipment | |
| CN203238141U (en) | Sewage biological treatment membrane filtration system | |
| CN2832804Y (en) | Composite sewage treatment equipment | |
| CN202358992U (en) | Sewage treatment device | |
| CN201495154U (en) | Biological wastewater treatment system combining biological fluidized bed with biological filter bed | |
| CN201614333U (en) | Decentralized sewage treatment device | |
| CN101538085A (en) | Structure of spiral-flow aeration sedimentation sewage treatment tank and using method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200925 Address after: 243000 No. 699 West Hunan Road, Anhui, Ma'anshan Patentee after: HUATIAN ENGINEERING & TECHNOLOGY CORPORATION, MCC Patentee after: HUATIAN NANJING ENGINEERING & TECHNOLOGY CORPORATION, MCC Address before: 243005 No. 25, Hunan Road, Anhui, Ma'anshan Patentee before: HUATIAN ENGINEERING & TECHNOLOGY CORPORATION, MCC |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20111005 |
|
| CX01 | Expiry of patent term |