CN203373197U - Domestic sewage treatment device - Google Patents
Domestic sewage treatment device Download PDFInfo
- Publication number
- CN203373197U CN203373197U CN201320451379.9U CN201320451379U CN203373197U CN 203373197 U CN203373197 U CN 203373197U CN 201320451379 U CN201320451379 U CN 201320451379U CN 203373197 U CN203373197 U CN 203373197U
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- CN
- China
- Prior art keywords
- aerobic reactor
- sewage
- anoxic pond
- enters
- settling tank
- 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
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- 239000010865 sewage Substances 0.000 title claims abstract description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 230000007246 mechanism Effects 0.000 claims abstract description 19
- 238000005273 aeration Methods 0.000 claims abstract description 10
- 239000000945 filler Substances 0.000 claims abstract description 9
- 238000012545 processing Methods 0.000 claims description 12
- 238000013022 venting Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 4
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 11
- 238000004062 sedimentation Methods 0.000 abstract description 5
- 239000010802 sludge Substances 0.000 abstract description 3
- 238000006213 oxygenation reaction Methods 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 229910002651 NO3 Inorganic materials 0.000 description 4
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 210000002249 digestive system Anatomy 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000006396 nitration reaction Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000143060 Americamysis bahia Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000007034 nitrosation reaction Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 150000003673 urethanes Chemical class 0.000 description 1
Images
Classifications
-
- Y02W10/12—
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The utility model provides a domestic sewage treatment device which comprises an anoxic tank, an aerobic reactor and a sedimentation tank, wherein the anoxic tank is communicated with a sewage source through a pipeline; sewage enters the anoxic tank through pump lifting; a water outlet of the anoxic tank is communicated with the aerobic reactor; the sewage treated in the anoxic tank enters the aerobic reactor; a turbulent flow mechanism is arranged in the aerobic reactor; a water outlet of the aerobic reactor is communicated with the sedimentation tank; the sewage treated in the aerobic reactor enters the sedimentation tank and is treated in the sedimentation tank before being discharged; with a corrugated plate arranged in the aerobic reactor, the clear height ratio is raised, the water flow path is increased, a sludge interception effect is realized, and enough time is provided for the sewage to contact and react with the filler on the corrugated plate; moreover, the path of aeration bubbles is increased, so that the oxygenation efficiency is improved, and an energy saving effect is realized.
Description
Technical field
The utility model relates to water technology, relates in particular to the one way of life waste disposal plant.
Background technology
Existing rural domestic sewage treatment facility is mostly very simple and crude, general three compartment septic tanks that adopt are processed, but it mainly bears the physical sedimentation effect, and processing efficiency is very low, poor effect, in water outlet, the concentration of organism and ammonia nitrogen is still very high, after the discharge surface water body, causes the water function serious degradation, the smelly blackening of water body, even fishes and shrimps disappearance, caused serious pollution to the water environment in rural area, seriously restricted the improvement of rural environment and the development of rural economy.The dissimilar underground powerless anaerobic processing device grown up in recent years, although more remarkable to removing the organic pollutant effect, the COD discharge can reach " integrated wastewater discharge standard " one-level or the requirement of secondary limit value substantially.But " integrated wastewater discharge standard " (GB18918-2002) I and II standard code ammonia nitrogen allows emission limit to be respectively 5mg/L (one-level B is 8mg/L) and 25mg/L, because being limited to the design defect of this type of technique and technology, existing treatment technology and facility water outlet NH
3-N is difficult to up to standard, and in the urgent need to researching and developing high-efficient simple domestic sewage in rural areas by using denitride technology or existing apparatus being carried out to biological reinforced processing, this is that current technology for treating domestic sewage in rural area is badly in need of the significant problem solved.
The utility model content
The purpose of this utility model is to provide the one way of life waste disposal plant, realizes the efficient processing to sanitary sewage.
The utility model is that the technical scheme that its technical problem of solution adopts is,
Sewage treatment unit, comprise anoxic pond, aerobic reactor and settling tank, anoxic pond is communicated with source of sewage by pipeline, sewage promotes and enters in anoxic pond through pump, and the water outlet of anoxic pond is communicated with aerobic reactor, and the sewage after processing in anoxic pond enters aerobic reactor, be provided with flow-disturbing mechanism in aerobic reactor, the water outlet of aerobic reactor is communicated with settling tank, and the sewage after processing in aerobic reactor enters settling tank, after being processed by settling tank, discharges;
Particularly, be provided with water entry in aerobic reactor, this water entry extends to bottom from the aerobic reactor top, flow-disturbing mechanism arranges around this water entry, sewage flows out from its bottom from the water entry top enters, and flows through arrival aerobic reactor top after flow-disturbing mechanism, from the aerobic reactor overhead stream to settling tank, aerobic reactor bottom is provided with aeration mechanism, by aeration mechanism, is become better in oxygen reactor and is passed into air;
Flow-disturbing mechanism comprises one group of corrugated plate, and this corrugated plate surface is provided with the urethane filler, and each corrugated plate extends from the aerobic reactor top to its bottom;
Be provided with the reverse screw paddle stirrer in anoxic pond, the anoxic pond top has lid, in this lid, is provided with venting port, and the gas in anoxic pond is discharged from this venting port.
The utility model has the advantage of, be provided with the reverse screw paddle stirrer in the anoxic pond of this device, both can play stirring action, can hold back mud again, improve sludge concentration, sewage flows into aerobic reactor certainly after processing in anoxic pond, corrugated plate vertically is set in aerobic reactor, corrugated plate surface attachment Polyurethane filler, the corrugated plate design had both improved the clear height ratio greatly, increased flow path, play the effect of holding back mud, allow sewage that the filler contact reacts on sufficient time and corrugated plate is arranged, also increased the path of aeration bubble, improved oxygen-transfer efficiency, play energy-conservation effect, sewage flows into settling tank afterwards, the mud of settling tank and Digestive system mixture through pump reflux to anoxic pond, nitrate in water produces anti-nitration reaction in anoxic pond, nitrate is converted to nitrogen, thereby the nitrogen pollutant in removal water.
The accompanying drawing explanation
Fig. 1 is the structural representation of the sewage treatment unit that the utility model proposes.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach purpose with effect is easy to understand, below in conjunction with illustrating and specific embodiment, further set forth the utility model.
As shown in Figure 1, the sewage treatment unit the utility model proposes comprises anoxic pond 1, aerobic reactor 2 and settling tank 3, anoxic pond 1 is communicated with source of sewage by pipeline, sewage promotes and enters in anoxic pond 1 through pump, the water outlet of anoxic pond 1 is communicated with aerobic reactor 2, sewage after processing in anoxic pond 1 enters aerobic reactor 2, be provided with flow-disturbing mechanism in aerobic reactor 2, the water outlet of aerobic reactor 2 is communicated with settling tank 3, sewage after processing in aerobic reactor 2 enters settling tank 3, after being processed by settling tank 3, discharges;
Be provided with water entry 4 in aerobic reactor 2, this water entry 4 extends to bottom from aerobic reactor 2 tops, flow-disturbing mechanism arranges around this water entry 4, sewage flows out from its bottom from water entry 4 tops enter, arrive aerobic reactor 2 tops after flowing through flow-disturbing mechanism, from aerobic reactor 2 overhead stream to settling tank 3, aerobic reactor 2 bottoms are provided with aeration mechanism, by aeration mechanism, are become better in oxygen reactor 2 and are passed into air;
Flow-disturbing mechanism comprises one group of corrugated plate 5, and these corrugated plate 5 surfaces are provided with the urethane filler, and each corrugated plate 5 extends from aerobic reactor 2 tops to its bottom;
Be provided with reverse screw paddle stirrer 6 in anoxic pond 1, anoxic pond 1 top has lid, in this lid, is provided with venting port, and the gas in anoxic pond 1 is discharged from this venting port.
Sewage is after regulating settling tank, promote and enter anoxic pond through pump, the reverse screw paddle stirrer is set in anoxic pond, both can play stirring action, can hold back mud again, improve sludge concentration, sewage flows into aerobic reactor certainly after processing in anoxic pond, corrugated plate vertically is set in aerobic reactor, corrugated plate surface attachment Polyurethane filler, this urethane filler outside surface of single bio-carrier in aeration tank is realized nitrosation reaction, the denitrification of nitrite is realized in inside, physical adsorption is not only arranged, just also have, the gravitation of negative charge, make carrier surface with hydrophilic radicals such as certain cation activity group and hydroxyls, can with sewage in the microorganisms key of negative charge, the secure bond of valency, thereby firmly be fixed on carrier by microorganism and biological enzyme, microorganism after making to survive is not easy at water, under the shearing action of gas, run off, the charge capacity of microorganism is large, volumetric loading is high, thereby make the ammonia nitrogen in sewage, total nitrogen reaches the purpose simultaneously descended, also there is the cutting bubbling ability strong simultaneously, the spatial volume utilization ratio is large, without characteristics such as dead bands.The corrugated plate design had both improved the clear height ratio greatly, had increased flow path, played the effect of holding back mud, allowed sewage that the filler contact reacts on sufficient time and corrugated plate is arranged, and had increased the path of aeration bubble, had improved oxygen-transfer efficiency, played energy-conservation effect.Sewage flows into settling tank afterwards, and the mud of settling tank and Digestive system mixture are through pump reflux to anoxic pond, and the nitrate in water produces anti-nitration reaction in anoxic pond, and nitrate is converted to nitrogen, thereby removes the nitrogen pollutant in water.
Above demonstration and described ultimate principle of the present utility model, principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and specification sheets, describes just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope, the utility model also has various changes and modifications, and these changes and improvements all fall in claimed the utility model scope.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (4)
1. sewage treatment unit, it is characterized in that, comprise anoxic pond, aerobic reactor and settling tank, anoxic pond is communicated with source of sewage by pipeline, and sewage promotes and enters in anoxic pond through pump, the water outlet of anoxic pond is communicated with aerobic reactor, sewage after processing in anoxic pond enters aerobic reactor, is provided with flow-disturbing mechanism in aerobic reactor, and the water outlet of aerobic reactor is communicated with settling tank, sewage after processing in aerobic reactor enters settling tank, after being processed by settling tank, discharges.
2. sewage treatment unit according to claim 1, it is characterized in that, be provided with water entry in aerobic reactor, this water entry extends to bottom from the aerobic reactor top, and flow-disturbing mechanism arranges around this water entry, and sewage flows out from its bottom from the water entry top enters, arrive the aerobic reactor top after flowing through flow-disturbing mechanism, from the aerobic reactor overhead stream to settling tank, aerobic reactor bottom is provided with aeration mechanism, by aeration mechanism, is become better in oxygen reactor and is passed into air.
3. sewage treatment unit according to claim 2, is characterized in that, flow-disturbing mechanism comprises one group of corrugated plate, and this corrugated plate surface is provided with the urethane filler, and each corrugated plate extends from the aerobic reactor top to its bottom.
4. sewage treatment unit according to claim 1, is characterized in that, is provided with the reverse screw paddle stirrer in anoxic pond, and the anoxic pond top has lid, in this lid, is provided with venting port, and the gas in anoxic pond is discharged from this venting port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320451379.9U CN203373197U (en) | 2013-07-25 | 2013-07-25 | Domestic sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320451379.9U CN203373197U (en) | 2013-07-25 | 2013-07-25 | Domestic sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203373197U true CN203373197U (en) | 2014-01-01 |
Family
ID=49835744
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320451379.9U Expired - Fee Related CN203373197U (en) | 2013-07-25 | 2013-07-25 | Domestic sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203373197U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110092548A (en) * | 2019-05-29 | 2019-08-06 | 常州大学 | Tubulose domestic sewage in rural areas wastewater treatment equipment |
-
2013
- 2013-07-25 CN CN201320451379.9U patent/CN203373197U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110092548A (en) * | 2019-05-29 | 2019-08-06 | 常州大学 | Tubulose domestic sewage in rural areas wastewater treatment equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 314100, Zhenhua Road 58, Wei Tong Street, Jiashan County, Jiaxing, Zhejiang Patentee after: ZHEJIANG EIODMEN ENVIRONMENTAL PROTECTION SCIENCE & TECHNOLOGY CO.,LTD. Address before: 314100, Zhenhua Road 58, Wei Tong Street, Jiashan County, Jiaxing, Zhejiang Patentee before: ZHEJIANG AIDIMAN WATER TECHNOLOGY CO.,LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140101 |