CN201530770U - A deep water combined biochemical treatment facility - Google Patents
A deep water combined biochemical treatment facility Download PDFInfo
- Publication number
- CN201530770U CN201530770U CN2009202037537U CN200920203753U CN201530770U CN 201530770 U CN201530770 U CN 201530770U CN 2009202037537 U CN2009202037537 U CN 2009202037537U CN 200920203753 U CN200920203753 U CN 200920203753U CN 201530770 U CN201530770 U CN 201530770U
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- water
- biochemical
- deep
- treatment facility
- reactor
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 56
- 239000010865 sewage Substances 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 10
- 238000004062 sedimentation Methods 0.000 claims abstract description 6
- 238000005192 partition Methods 0.000 claims abstract 2
- 238000005273 aeration Methods 0.000 claims description 13
- 238000001179 sorption measurement Methods 0.000 claims description 3
- 238000005352 clarification Methods 0.000 claims 1
- 238000004140 cleaning Methods 0.000 abstract description 10
- 230000003851 biochemical process Effects 0.000 abstract 1
- 238000009434 installation Methods 0.000 abstract 1
- 230000011218 segmentation Effects 0.000 description 7
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 description 1
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Classifications
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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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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
本实用新型涉及污水处理的技术领域，尤其涉及一种深水组合生化处理设施。本实用新型包括池体、沉淀池及生化反应器，其主要是在较深的污水池体中，将通常分散设置的厌氧生化反应器A，好氧生化反应器O，沉淀池S，曝气生物滤池组合在一起，分别由导流隔板将其分开；池体的一面设有进水管，另一面设有排水管，底部设有排泥管。通过提高水深，将常规生化工艺设施组合为一体化设施。该一体化设施水深6-12m均可，组合的工艺设施或有适当改造。因此具有占地少，级间提升少，管道少的特点，具有节地、节能、节约投资的优点效果。另外，由于设置了自净曝气生物滤池，使其具有二级生化，还可以提高出水质量的优点。
The utility model relates to the technical field of sewage treatment, in particular to a deep-water combined biochemical treatment facility. The utility model includes a pool body, a sedimentation tank and a biochemical reactor. It is mainly in a deep sewage pool body, anaerobic biochemical reactor A, aerobic biochemical reactor O, sedimentation tank S, and exposure The gas biofilters are combined together and separated by diversion partitions; one side of the pool body is provided with a water inlet pipe, the other side is provided with a drain pipe, and the bottom is provided with a mud discharge pipe. By increasing the water depth, the conventional biochemical process facilities are combined into an integrated facility. The water depth of the integrated facility can be 6-12m, and the combined process facilities may be properly modified. Therefore, it has the characteristics of less land occupation, less inter-stage promotion, and fewer pipelines, and has the advantages of land saving, energy saving, and investment saving. In addition, due to the installation of the self-cleaning biological aerated filter, it has the advantages of secondary biochemistry and can also improve the quality of the effluent.
Description
Technical field
The utility model relates to technical field of sewage treatment, relates in particular to a kind of deep water combination biochemical treatment facility.
Background technology
" biochemistry " is the biological treatment that is used for sewage disposal, is made up of series of process equipment and structures.Present employed processing unit and structures have " anaerobic biochemical reactor " A, " aerobic biochemical reactor " O and " settling tank " S or the like usually.Its every kind processing unit and structures all have different classification, different shapes, form different process combination as A/O/S, A/A/O/S, A/O/S/O/S etc., wherein A can be divided into anaerobism, anoxic again, UASB EGSB IC or the like, the waterpower elevation is bigger, 10-20m; O can be divided into mud method, embrane method aeration and BAF or the like again, and water level elevation is generally lower, 4-6m.These combined result have following shortcoming: long flow path, and floor space is huge, and loss of waterpower elevation or lifting are frequent, the energy consumption height.
The utility model content
The problem that the utility model exists at prior art, purpose provide a kind of deep water combination biochemical treatment facility.This facility has darker effective water level than the routine biochemistry aeration tank, has to take up an area of fewly, and inter-stage promotes few, the characteristics that pipeline is few, be save land, energy-conservation, the combined facility of saving investment.
The utility model is realized by the following technical solutions:
A kind of deep water combination biochemical treatment facility, it comprises pond body, settling tank and biochemical reactor, it mainly is in darker sewage lagoon body, with the anaerobic biochemical reactor A that disperses usually to be provided with, aerobic biochemical reactor O, settling tank S, BAF is combined, and by diaphragm it is separated respectively; The one side of pond body is provided with water inlet pipe, and another side is provided with water shoot, and the bottom of pond body is provided with shore pipe.
Traverse baffle by at least more than one in the described anaerobic biochemical reactor A is divided into plurality of sections.
The water level of described pond body 1 is 6～12m, and each section water level is suitable.
Be provided with diaphragm in the described deep water aerobic biochemical reactor O, adopt the air-lift unit aeration mode.
Described settling tank S is the underlying upflowing, adapts to the big depth of water, is provided with swash plate in the settling tank S.
Described BAF can be located on the settling section of settling tank S top.
Described anaerobic biochemical reactor A can also use anoxic reacter, or two anaerobic biochemical reactor A repeat to be provided with or two anoxic reacters repeat to be provided with and the adsorption precipitation pond replaces.
The utility model is by improving the depth of water, with being combined into one of routine biochemistry process facility facility.This integrated facility depth of water 6-12m all can, the process facility of combination or appropriate reconstruction is arranged.Therefore have and take up an area of fewly, inter-stage promotes few, the characteristics that pipeline is few, have save land, energy-conservation, the advantageous effect of saving investment.In addition, the utility model makes it have secondary biochemical owing to be provided with the self-cleaning BAF, can also improve the advantage of effluent characteristics.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the another example structure synoptic diagram of the utility model.
Among the figure; Anaerobic biochemical reactor A, aerobic biochemical reactor O, settling tank S, self-cleaning BAF SBAF, pond body 1, water inlet pipe 2, water shoot 3, aerated conduit 4, aerated conduit 41, aerated conduit 42, shore pipe 5, diaphragm 6, traverse baffle 7,8,9.
Below embodiment of the present utility model is described in detail in conjunction with the accompanying drawings, but not limit by embodiment.
Embodiment
Embodiment 1
As shown in Figure 1, Fig. 1 is a structural representation of the present utility model.
The utility model is a kind of deep water combination biochemical treatment facility, and it is in darker sewage lagoon body 1, with the anaerobic biochemical reactor A that disperses to be provided with, aerobic biochemical reactor O, settling tank S, BAF is combined together, and by diaphragm 6 it is split up into several segmentations respectively.Specifically be successively it to be divided into anaerobic biochemical reactor A by dividing plate 10 and dividing plate 11, aerobic biochemical reactor O, three segmentations of settling tank S; The one side of pond body 1 is provided with water inlet pipe 2, and another side is provided with water shoot 3, and body 1 bottom in pond is provided with one or more shore pipes 5; Anaerobic biochemical reactor A can be divided into multistage with traverse baffle 7,8,9; Aerobic biochemical reactor O adopt to promote aeration mode, in be provided with diaphragm 6, monolateral lifting aeration mode forms vertical water circulation, regulates to adapt to deep water, saves energy.Settling tank S can adopt upward flow settling tank structure, also can establish swash plate.The water level of described pond body 1 is to be advisable between the 6-12m, anaerobic biochemical reactor A wherein, and aerobic biochemical reactor O, three segmentation water levels of settling tank S are equal substantially.
During concrete enforcement, the utility model by reducing anaerobic biochemical reactor A section height, drops in the 12m its water level for adopting multistage anaerobic reactor; Improve aerobic biochemical reactor O section water level depth and anaerobic biochemical reactor A section coupling; Adopt upflowing settling tank S, make its water level and aerobic biochemical reactor O section coupling.Settling tank S can be the underlying upflowing, adapts to the big depth of water.By above measure, biochemical flow process is unified in the integrated rectangle reaction tank body 1 of a basic water level such as grade.
Sewage enters first segmentation anaerobic biochemical reactor A from water inlet pipe 2, and the traverse baffle 7,8,9 of flowing through successively that flows automatically enters among next segmentation aerobic biochemical reactor O, and aerobic biochemical reactor O section air-lift unit aeration is saved the energy; And provide aeration wind through aerated conduit 4, again through settling tank S, by upward flow sewage through suspended layer upwards through swash plate S1 secondary sedimentation, discharge pond bodies 1 via the water shoot 3 of settling tank S section at last, surplus mud is discharged by shore pipe 5.Pass through anaerobic biochemical reactor A, aerobic biochemical reactor O, settling tank S therebetween ... Deng biochemical reaction, reach processing intent.
During concrete enforcement, can also be set the stages such as mud backflow, nitrification liquid backflow or effluent recycling according to arts demand, working method is with conventional way unanimity.
As shown in Figure 2, Fig. 2 is the another example structure synoptic diagram of the utility model.
The utility model can also be set up self-cleaning BAF SBAF by settling section above described settling tank S when implementing.
Described BAF SBAF can utilize the big depth of water, places on the settling tank settling section.Self-cleaning BAF SBAF employing subregion is rotated to isolate and is promoted aeration, forms vertical circulating water flow, and aeration carries mud simultaneously to the underlying settling tank, makes the filter tank self-cleaning.
Adopt in this embodiment underlying settling tank S with on put self-cleaning BAF SBAF combination, its water level and biochemical section are mated.Sewage enters first segmentation anaerobic biochemical reactor A from water inlet pipe 2, the gravity flow baffling 7,8,9 of flowing through successively enters among next segmentation aerobic biochemical reactor O, and provide aeration wind through aerated conduit 4, again through settling tank S, make progress through self-cleaning BAF SBAF through suspended layer by upward flow sewage, discharge pond body 1 via the water shoot 3 of settling tank S section at last, reach processing intent at last.Self-cleaning BAF SBAF is two sections biochemistry, supply aeration wind alternate turns aeration by aerated conduit 41 and the aerated conduit 42 that is provided with in the pond, produce vertical circulation in the filter tank, providing microorganism simultaneously with oxygen, carry and be sunken under the biological sludge in the underlying settling tank, surplus mud is discharged by shore pipe 5.
Embodiment 3
A kind of deep water combination biochemical treatment facility described in the utility model, wherein said anaerobic biochemical reactor A, aerobic biochemical reactor O, settling tank S and self-cleaning BAF pond SBAF, permutation and combination setting arbitrarily under the reasonable depth of water.Anaerobic biochemical reactor A as described is anoxic reacter also, or two anaerobic biochemical reactor A repeat to be provided with or two anoxic reacters repeat to be provided with, other technologies also capable of being combined are as multiple array modes such as adsorption precipitation also capable of being combined ponds before the anaerobic biochemical reactor A section.
Other is with embodiment 1 or 2.
Embodiment 4
The water level of described pond described in the utility model body 1 is between 6～12m, select for use during enforcement 6m, 7m, 8m, 9m, 10m, 11m, 12m all can, each section water level quite gets final product.
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202037537U CN201530770U (en) | 2009-09-29 | 2009-09-29 | A deep water combined biochemical treatment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202037537U CN201530770U (en) | 2009-09-29 | 2009-09-29 | A deep water combined biochemical treatment facility |
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| CN201530770U true CN201530770U (en) | 2010-07-21 |
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| CN2009202037537U Expired - Fee Related CN201530770U (en) | 2009-09-29 | 2009-09-29 | A deep water combined biochemical treatment facility |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102153200A (en) * | 2011-03-02 | 2011-08-17 | 深圳市华伦天成科技开发有限公司 | Mobile integrated organic wastewater treatment device |
| CN102320689A (en) * | 2011-08-05 | 2012-01-18 | 北京城市排水集团有限责任公司 | Continuous flow granular sludge reactor and running method |
| CN103922548A (en) * | 2014-05-04 | 2014-07-16 | 北京航空航天大学 | Biological reaction device for culturing high-oil microalgae by using wastewater |
| CN105198083A (en) * | 2015-09-16 | 2015-12-30 | 北京首创清源环境科技有限公司 | Integrated sewage treatment device and method |
| CN105481201A (en) * | 2016-01-26 | 2016-04-13 | 甘肃金桥水科技（集团）股份有限公司 | Integrated sewage treatment and reuse device |
| CN106145557A (en) * | 2016-08-29 | 2016-11-23 | 武汉东川自来水科技开发有限公司 | A kind of integration switching aeration waste water processing system and processing method |
| CN106242057A (en) * | 2016-09-06 | 2016-12-21 | 山东文远建材科技股份有限公司 | Bioreactor for sewage disposal |
| CN106810003A (en) * | 2015-11-27 | 2017-06-09 | 江苏启创环境科技有限公司 | Integrated sewage treating apparatus |
| CN108101203A (en) * | 2017-12-21 | 2018-06-01 | 武汉森泰环保股份有限公司 | A kind of reaction precipitation integral deep water aeration tower and its treatment process |
| CN112275021A (en) * | 2020-10-15 | 2021-01-29 | 费斯托教学股份有限公司 | Sand filtering simulation equipment |
-
2009
- 2009-09-29 CN CN2009202037537U patent/CN201530770U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102153200A (en) * | 2011-03-02 | 2011-08-17 | 深圳市华伦天成科技开发有限公司 | Mobile integrated organic wastewater treatment device |
| CN102320689A (en) * | 2011-08-05 | 2012-01-18 | 北京城市排水集团有限责任公司 | Continuous flow granular sludge reactor and running method |
| CN102320689B (en) * | 2011-08-05 | 2013-02-13 | 北京城市排水集团有限责任公司 | Continuous flow granular sludge reactor and running method |
| CN103922548A (en) * | 2014-05-04 | 2014-07-16 | 北京航空航天大学 | Biological reaction device for culturing high-oil microalgae by using wastewater |
| CN105198083A (en) * | 2015-09-16 | 2015-12-30 | 北京首创清源环境科技有限公司 | Integrated sewage treatment device and method |
| CN106810003A (en) * | 2015-11-27 | 2017-06-09 | 江苏启创环境科技有限公司 | Integrated sewage treating apparatus |
| CN105481201A (en) * | 2016-01-26 | 2016-04-13 | 甘肃金桥水科技（集团）股份有限公司 | Integrated sewage treatment and reuse device |
| CN106145557A (en) * | 2016-08-29 | 2016-11-23 | 武汉东川自来水科技开发有限公司 | A kind of integration switching aeration waste water processing system and processing method |
| CN106242057A (en) * | 2016-09-06 | 2016-12-21 | 山东文远建材科技股份有限公司 | Bioreactor for sewage disposal |
| CN108101203A (en) * | 2017-12-21 | 2018-06-01 | 武汉森泰环保股份有限公司 | A kind of reaction precipitation integral deep water aeration tower and its treatment process |
| CN112275021A (en) * | 2020-10-15 | 2021-01-29 | 费斯托教学股份有限公司 | Sand filtering simulation equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100721 Termination date: 20140929 |
|
| EXPY | Termination of patent right or utility model |