CN203144173U - Baffling anaerobic reactor - Google Patents
Baffling anaerobic reactor Download PDFInfo
- Publication number
- CN203144173U CN203144173U CN2013200613849U CN201320061384U CN203144173U CN 203144173 U CN203144173 U CN 203144173U CN 2013200613849 U CN2013200613849 U CN 2013200613849U CN 201320061384 U CN201320061384 U CN 201320061384U CN 203144173 U CN203144173 U CN 203144173U
- Authority
- CN
- China
- Prior art keywords
- reaction chamber
- opening
- anaerobic reactor
- injector
- sewage
- 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
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model provides a baffling anaerobic reactor. The baffling anaerobic reactor comprises a mixing pond, reaction chambers and a sewage discharging device, wherein the reaction chambers comprise a first reaction chamber, a second reaction chamber and a third reaction chamber; an opening at one end of the first reaction chamber is upward and is positioned in the second reaction chamber, and a three-phase separator is arranged above the opening; an injector is arranged at an opening of the other end of the first reaction chamber and is connected with the mixing pond by a pipeline, and the connecting pipeline is provided with an injection pump; an opening at one end of the second reaction chamber is downward, the other end of the second reaction chamber is fixed on a top plate of the third reaction chamber, and a top cover for sealing is arranged above the opening at the other end of the second reaction chamber and is communicated with a methane collecting and purifying system; and a ring-shaped water collector is arranged under a top plate of the third reaction chamber and is communicated with the mixing pond and the sewage discharging device. The baffling anaerobic reactor provided by the utility model has the advantages that the structure is simple, the cost is low, and the methane production is high; and filtered residues can be recycled, so that the additional value generated by sewage treatment is improved.
Description
Technical field
The utility model relates to sewage disposal device, specifically a kind of deflector anaerobic reactor.
Background technology
Upflow anaerobic sludge blanket reactor (UASB, Up-flow Anaerobic Sludge Bed/Blanket) is that present industry is for the treatment of two kinds of anaerobe methods of comparatively using always of wastewater/sewage with expanded granular sludge bed (EGSB, Expanded Granular Sludge Bed).All need floor space big in these two kinds for the treatment of processs, and constitute complicated treatment facility, not only the acquisition cost of equipment, operation expense are high, and equipment construction difficulty height; The biogas that produces when simultaneously, handling wastewater/sewage, filter residue etc. are difficult to effectively be recycled.
The utility model content
In view of the deficiencies in the prior art and defective, the utility model provides a kind of deflector anaerobic reactor.
In order to achieve the above object, the utility model has adopted following technical scheme:
A kind of deflector anaerobic reactor comprises: preparing pool, reaction chamber and sewage discharger;
Described reaction chamber comprises from inside to outside sheathed successively first reaction chamber, second reaction chamber and the 3rd reaction chamber;
The opening of this first reaction chamber, one end is positioned at this second reaction chamber up, and the opening of this end top is provided with triphase separator; The opening part of this first reaction chamber the other end is provided with injector, and this injector is fixed on the base plate of the 3rd reaction chamber, and this injector is connected with this preparing pool by pipeline, and its connecting pipeline is provided with squirt pump;
The opening of this second reaction chamber, one end is positioned at the position of the 3rd reaction chamber bottom down, and the other end is fixed on the top board of the 3rd reaction chamber, is provided with top seal above the opening of this end, and this top cover is provided with pipeline and is communicated with the collecting methane purification system;
The top board below of the 3rd reaction chamber is provided with annular water collector, and this annular water collector is communicated with this preparing pool and this sewage discharger.
As optimal technical scheme of the present utility model: described first reaction chamber is " loudspeaker " shape, and in the openings at two ends, wherein the end that opening diameter is little arranges this injector.
As optimal technical scheme of the present utility model: described sewage discharger comprises the hopper that is connected with this annular water collector and is located at song sieve and the reception basin of this hopper below successively.
As optimal technical scheme of the present utility model: the connecting pipeline of described injector and this preparing pool is provided with valve.
As optimal technical scheme of the present utility model: the height≤7m of described the 3rd reaction chamber.
Compared with prior art, the utility model constantly changes the flow direction of sewage by three reaction chambers, forms the internal recycle effect, makes sewage obtain sufficient oxidation, accelerates the processing efficiency of sewage; Simultaneously, the biogas that sewage is included fully discharges, and increases the output of biogas, and finishes the recycling of filter residue, and three phase separation is preferable, improve the value added that sewage disposal produces, and this device structure is simple, structure height is little, reduces the difficulty of construction of equipment, reduces equipment cost.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
See also Fig. 1, the deflector anaerobic reactor shown in the figure comprises: preparing pool 101, reaction chamber and sewage discharger.
Described reaction chamber comprises from inside to outside sheathed successively first reaction chamber 103, second reaction chamber 104 and the 3rd reaction chamber 105.
The opening of these first reaction chamber, 103 1 ends (with respect to the 3rd reaction chamber 105) up is positioned at this second reaction chamber 104, and near the top board 110 of the 3rd reaction chamber 105, and the opening of this end top is provided with triphase separator 111; The opening part of these first reaction chamber, 103 the other ends is provided with injector 106, this injector 106 is fixed on the base plate 109 of the 3rd reaction chamber 105, and this injector 106 is connected with this preparing pool 101 by pipeline, and its connecting pipeline is provided with squirt pump 107 and valve 112.
The opening of these second reaction chamber, 104 1 ends (with respect to the 3rd reaction chamber 105) down is positioned at the position of the 3rd reaction chamber 105 bottoms (near the base plate 109 of the 3rd reaction chamber 105, but not forming sealing with this base plate 109 is connected), the other end of this second reaction chamber 104 is fixed on the top board 110 of the 3rd reaction chamber 105, be provided with top cover 113 sealings above the opening of this end, this top cover 113 is provided with pipeline and is communicated with the collecting methane purification system.
More excellent, described first reaction chamber 103 is " loudspeaker " shape, and in the openings at two ends, wherein the end that opening diameter is little arranges this injector 106, to reach the effect of jet entrainment mud internal recycle.
More excellent, for reducing difficulty of construction and equipment investment cost, the height≤7m of described the 3rd reaction chamber 105.
Wastewater/sewage (processing of this wastewater/sewage anaerobic hydrolysis acidifying denitrification) in the preparing pool 101, pumped to injector 106 by squirt pump 107, injector 106 is drawn the mud 108 that is deposited on the 3rd reaction chamber 105 bottoms, and pump to the inner chamber of first reaction chamber 103 together with the wastewater/sewage mixed solution, mixed the wastewater/sewage of mud from the opening outflow of first reaction chamber, 103 the other ends, handle through triphase separator 111, impurity in the wastewater/sewage is separated and is back to anoxic denitrification pond (not shown), sewage changes the flow direction, flow into second reaction chamber 104, and the biogas that wastewater/sewage includes is isolated and is entered top cover 113, and connects the collecting methane purification system recycle on top cover 113.The wastewater/sewage that flows into second reaction chamber 104 changes again and flows into the 3rd reaction chamber 105 through down opening of second reaction chamber time, finishes the separation of solid-liquid phase secondary; Then, flow into the hopper 114 of sewage discharger through annular water collector 102, after Via sieve 115 filters, flow into reception basin 116, reception basin 116 can be connected with other treatment facility, finishes other treatment process.Bent sieve 115 filters the filter residue that produces and can be used as the organic fertilizer recycling.
The above is preferred embodiment of the present utility model only, is not to limit practical range of the present utility model; Every equivalence of doing according to the utility model changes and revises, and is all covered by the scope of the utility model claims.
Claims (5)
1. a deflector anaerobic reactor is characterized in that, comprising: preparing pool, reaction chamber and sewage discharger;
Described reaction chamber comprises from inside to outside sheathed successively first reaction chamber, second reaction chamber and the 3rd reaction chamber;
The opening of this first reaction chamber, one end is positioned at this second reaction chamber up, and the opening of this end top is provided with triphase separator; The opening part of this first reaction chamber the other end is provided with injector, and this injector is fixed on the base plate of the 3rd reaction chamber, and this injector is connected with this preparing pool by pipeline, and its connecting pipeline is provided with squirt pump;
The opening of this second reaction chamber, one end is positioned at the position of the 3rd reaction chamber bottom down, and the other end is fixed on the top board of the 3rd reaction chamber, is provided with top seal above the opening of this end, and this top cover is provided with pipeline and is communicated with the collecting methane purification system;
The top board below of the 3rd reaction chamber is provided with annular water collector, and this annular water collector is communicated with this preparing pool and this sewage discharger.
2. deflector anaerobic reactor according to claim 1, it is characterized in that: described first reaction chamber is " loudspeaker " shape, and in the openings at two ends, wherein the end that opening diameter is little arranges this injector.
3. deflector anaerobic reactor according to claim 1 is characterized in that: described sewage discharger comprises the hopper that is connected with this annular water collector and is located at song sieve and the reception basin of this hopper below successively.
4. deflector anaerobic reactor according to claim 1, it is characterized in that: the connecting pipeline of described injector and this preparing pool is provided with valve.
5. deflector anaerobic reactor according to claim 1 is characterized in that: the height≤7m of described the 3rd reaction chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200613849U CN203144173U (en) | 2013-02-01 | 2013-02-01 | Baffling anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200613849U CN203144173U (en) | 2013-02-01 | 2013-02-01 | Baffling anaerobic reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203144173U true CN203144173U (en) | 2013-08-21 |
Family
ID=48971717
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013200613849U Expired - Fee Related CN203144173U (en) | 2013-02-01 | 2013-02-01 | Baffling anaerobic reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203144173U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103756896A (en) * | 2013-12-23 | 2014-04-30 | 陈际平 | Vertical baffling composite anaerobic digester |
| CN107311303A (en) * | 2017-08-28 | 2017-11-03 | 山东许中华环保科技有限公司 | Pulling flow type anaerobic reactor |
| CN107364958A (en) * | 2017-08-28 | 2017-11-21 | 山东许中华环保科技有限公司 | Plug-flow, which declines, exposes aerobic reactor |
-
2013
- 2013-02-01 CN CN2013200613849U patent/CN203144173U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103756896A (en) * | 2013-12-23 | 2014-04-30 | 陈际平 | Vertical baffling composite anaerobic digester |
| CN107311303A (en) * | 2017-08-28 | 2017-11-03 | 山东许中华环保科技有限公司 | Pulling flow type anaerobic reactor |
| CN107364958A (en) * | 2017-08-28 | 2017-11-21 | 山东许中华环保科技有限公司 | Plug-flow, which declines, exposes aerobic reactor |
| CN107364958B (en) * | 2017-08-28 | 2020-06-05 | 山东许中华环保科技有限公司 | Plug-flow type micro-aeration aerobic reactor |
| CN107311303B (en) * | 2017-08-28 | 2020-06-05 | 山东许中华环保科技有限公司 | Plug-flow anaerobic reactor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202499762U (en) | Anaerobic-aerobic integration bioreactor | |
| US20220119746A1 (en) | Anaerobic digestion device based on self-sustained air flotation | |
| CN203144173U (en) | Baffling anaerobic reactor | |
| CN100475716C (en) | Anaerobic bioreacto | |
| CN103288207B (en) | Integrated secondary-fermentation anaerobic digestion tank | |
| CN103880178B (en) | Multistage gas stripping and separating integrated anaerobic treatment device | |
| CN100436342C (en) | Rotary multi-cut-piece anaerobic biological reactor | |
| CN203319762U (en) | Self-circulation anaerobic reactor | |
| CN209778852U (en) | Urban road sewer methane separation and collection device | |
| CN202139226U (en) | Methane anaerobic reactor | |
| CN109574431B (en) | Utilize integrated device of primary sludge preparation organic carbon source | |
| CN203568940U (en) | Pulping sewage recycling system | |
| CN201737771U (en) | High-concentration waste water anaerobic treatment apparatus | |
| CN205367877U (en) | A anaerobic reactor for high concentration sewage treatment | |
| CN202265570U (en) | Negative pressure separator | |
| CN203159323U (en) | Efficient anaerobic reactor | |
| CN105036448A (en) | Biological waste water treatment system | |
| CN201258287Y (en) | Combined sludge bed anaerobic reactor | |
| CN205035213U (en) | Biological wastewater processing system | |
| CN201049910Y (en) | Rotary multi-section anaerobic bioreactor | |
| CN204474492U (en) | Polyester waste water treatment system | |
| CN205170491U (en) | UASB (Upflow anaerobic sludge blanket) reactor | |
| CN203440213U (en) | Filtering layer reactor and wastewater treatment device | |
| CN103043793A (en) | Internally and externally controllable double-circulation efficient anaerobic reactor | |
| CN204699447U (en) | A kind of coking waste liquid circulation crystallization apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20151209 Address after: 519070 Guangdong city in Zhuhai Province before the Shan Dai Road No. 66 building Dudley Patentee after: Zhuhai Delai Environmental Protection Engineering Co. Ltd. Address before: 519070 No. 66, Dai Shan Road, Zhuhai, Guangdong Patentee before: Zhuhai Delai Environmental Science and Technology Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130821 Termination date: 20180201 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |