CN205973978U - Town sewage biochemical treatment device - Google Patents
Town sewage biochemical treatment device Download PDFInfo
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- CN205973978U CN205973978U CN201620921759.8U CN201620921759U CN205973978U CN 205973978 U CN205973978 U CN 205973978U CN 201620921759 U CN201620921759 U CN 201620921759U CN 205973978 U CN205973978 U CN 205973978U
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Abstract
The utility model discloses a town sewage biochemical treatment device, including the anaerobism section, the oxygen deficiency section that feed through the in proper order oxygen section of becoming reconciled, be equipped with the water inlet in the anaerobism section, be equipped with the delivery port in good oxygen section, be equipped with fixed filler, combined packing and suspension respectively and pack in the oxygen section is become reconciled to anaerobism section, oxygen deficiency section, become reconciled the bottom of oxygen section in the oxygen deficiency section and be equipped with aeration equipment. The utility model discloses a biochemical treatment device can improve the biodegradability of sewage and carry out the anaerobism with the mixed liquid of backward flow oxygen deficiency section and release the phosphorus reaction, combined packing denitrification is filled to the oxygen deficiency section, and pack nitrifying of the oxidation that can accomplish organic pollutant fast, ammonia nitrogen and inhale reaction such as phosphorus of suspension is filled to good oxygen section, accomplishes biological multiplication simultaneously, controls its dissolved oxygen and can save energy saving in a large number and consume. Load different fillers respectively, the waste water treatment capacity multiplication, the pond appearance obtains make full use of, and the province is taken up an area of to technology, and anti -impact is strong, and the stable performance is maintained simply.
Description
Technical field
This utility model is related to a kind of town sewage biochemical treatment apparatus, belongs to technical field of sewage.
Background technology
At present, with the quickening of urbanization, villages and small towns population is constantly concentrated, and township enterprise develops rapidly, and town sewage discharges
Amount is also continuously increased, and small towns sewage disposal is a dark horse, and domestic routine small towns sewage disposal biochemical process has bio-contact oxidation
Method, SBR and its deformation, land disposal method, ecological pond and some other domestic sewage treatment process, and these biochemical treatments
In technique, the flow process that dirty organic pollutants are degraded is shorter, degradable will need to take larger process space, simultaneously dirty
Nitrogen phosphorus in water is different to the demand of oxygen, the denitrogenation dephosphorizing of sewage to be completed, and process above is difficult to meet and requires, thus processing
Effect is difficult to be guaranteed.
Utility model content
For the deficiencies in the prior art, this utility model be intended to exploitation different from existing biochemical processing process device, will fill out
The anaerobism section filling fixing filler, the anoxia section filling combined stuffing, the aerobic section of filling floating stuffing are combined in the biochemistry of one
Processing meanss, it is good to have a biochemical treatment Effects of Water Quality, takes up an area few, structure is simple, makes a kind of biochemical dress of cheap integrated A AO
Put.
The technical solution of the utility model is to provide a kind of town sewage biochemical treatment apparatus, including detesting of being sequentially communicated
Oxygen section, anoxia section and aerobic section, are provided with water inlet in anaerobism section, are provided with outlet in aerobic section, become reconciled in anaerobism section, anoxia section
It is respectively equipped with fixing filler, combined stuffing and floating stuffing in oxygen section, be provided with aerator in the bottom of anoxia section and aerobic section.
Aerobic section can be a uncovered container.Floating stuffing can make violent unordered fortune under the promotion of bottom aerator
Dynamic, so that every nook and cranny is in aerobic state, be conducive to the carrying out of biochemical treatment.
Further, it is provided between described anaerobism section and anoxia section and detest scarce passage and detest scarce return flow line.Detest lacked water lead to
Road is the passage that anaerobism section flows to anoxia section;Correspondingly, detest the passage that scarce return flow line is that anoxia section is back to anaerobism section.Its
In, passage may each be an opening.
Further, it is provided between described anoxia section and aerobic section and lack passage and become reconciled scarce return flow line.Lacked well water to lead to
Road is the passage that anoxia section flows to aerobic section;Correspondingly, lacking well return flow line is the passage that aerobic section is back to anoxia section.Its
In, passage may each be an opening.
Further, in described anaerobism section, several deflection plates are installed, fixing uniform filling is distributed between deflection plate.
This utility model can also connect offer nitrification settler, including sedimentation tank, described sedimentation tank after aerobic section
Inside it is divided into contraminated zone and settling zone, is provided with aerating system in the bottom of sedimentation tank, be provided with nitrifying sludge in the lower section of aerating system
Return duct and air stripping system.
Fill inclined plate packing in the settling zone of sedimentation tank, carry out biochemical treatment further, and precipitation carries through aerating system
For oxygen nitrification after mud through air stripping system flowback to anaerobism section be anaerobe provide carbon source.
Know-why of the present utility model:After pretreatment, Small Town Wastewater is through entering integrated A AO(Anaerobic-anoxic-good
Oxygen)Biochemical device anaerobism section, arranges multiple little lattice in anaerobism section, each little lattice is provided with deflection plate, is filled with fixation between deflection plate
Filler, sewage advances through the upper and lower baffling of deflection plate after entering anaerobism section, carries out a point reaction by every lattice one by one, has good water
Power fluidised form, in water inlet, hardly degraded organic substance here is hydrolyzed acidifying, improves the biodegradability of sewage;The sewage of anaerobism section tail end
Enter anoxia section in anaerobism section with scarce section section junction one end, it is anti-that the other end then carries out anaerobic phosphorus release for backflow anoxia section mixed liquor
That answers detests scarce return flow line;Sewage enters filling suspension in aerobic section, aerobic section through anoxia section and aerobic section intersection one end and fills out
Material, forms biological floating bed, because suspended biological flotation bed is under the promotion of at the bottom of pond aerator, is thoroughly mixed, touches with sewage
Hit, shear, make the bubble that aerator transmits more tiny, improve coefficient of oxygen utilization, complete the oxidation of organic pollution, ammonia nitrogen
The reaction such as nitrification and suction phosphorus, the other end is then the well scarce return flow line that aerobic section nitrification liquid is back to anoxia section, enters anoxia section,
It is provided with combined stuffing, the nitrification liquid here of backflow carries out denitrification denitrogenation, and its water outlet part is back to anaerobism in anoxia section
Section, substantially reduces the harmful effect that nitrate nitrogen reacts to anaerobic phosphorus release;Enter the sewage of aerobic section, in the effect of floating stuffing
Under, fast breeding, accomplish biological multiplication;Sewage is downward through outlet row after the process of anaerobism section → anoxia section → aerobic section
Procedure.
Aerating system is laid in sedimentation tank central authorities near bottom, by micro supply, accelerates the mud nitrification sinking to the bottom;Conflux
Nitrification mud liquid to bottom of device central authorities is back to preamble by the air stripping system being arranged on below aerator by nitrifying mud liquid
Technique;Source of the gas is respectively aerating system supply and air stripping system supply, individually controls.Air stripping system shares one with aerating system
Feeder, avoids the need for installing power-equipment in the bottom of sedimentation tank;Nitrifying sludge can be flowed back by siphonage and provide
Carbon source, can save power.
The beneficial effects of the utility model:1. one AAO biochemical treatment apparatus form one by unit-modularized for civil engineering structure
The form of body equipment, reduces on-site construction time, shortens construction period.2. anaerobism section baffling hydrolysis acidification, improve sewage
Biodegradability simultaneously carries out anaerobic phosphorus release reaction with backflow anoxia section mixed liquor;Anoxia section fills combined stuffing denitrification denitrogenation, good
Oxygen section filling floating stuffing can be rapidly completed the oxidation of organic pollution, the nitrification of ammonia nitrogen and inhale the reaction such as phosphorus, accomplish to give birth to simultaneously
Thing doubles, and controls its dissolved oxygen can save energy consumption in a large number.3. AAO process unit loads different fillers, sewage treatment capacity respectively
Multiplication, aerobic section(O section)Floating stuffing by comprehensive to sewage and mud contact, collision and shearing, pond holds is fully used, work
Skill takes up an area province, and resistance to impact is strong, stable performance, safeguards simple.4. outlet effect is good, can reach《Urban wastewater treatment firm pollutes
Thing discharge standard》GB18918-2002 primary standard.
Brief description
Fig. 1 represents that Fig. 1 is planar structure schematic diagram of the present utility model;
Fig. 2 is the A-A profile of Fig. 1.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawings and examples.
Embodiment 1
The present embodiment provides a kind of integrated A AO biochemical device, and its structure is including water inlet 1, anaerobism section 2, anoxia
Section 3, aerobic section 4 and outlet 6, are respectively equipped with fixing filler 22, combined stuffing 31 in anaerobism section 2, anoxia section 3 and aerobic section 4
With floating stuffing 41, it is provided with aerator 5 in the bottom of anoxia section 3 and aerobic section 4;It is provided between anaerobism section 2 and anoxia section 3 and detest
Lack aquaporin 23 and detest scarce return flow line 32;Be provided between anoxia section 3 and aerobic section 4 lacked aquaporin 33 become reconciled lack backflow
Passage 42;In anaerobism section 2, several deflection plates 21 are installed, fixing filler 22 is evenly distributed between deflection plate 21.
Certain rural town sewerage treatment plant amount of inlet water 450m3/ d, water concentration:COD >=250mg/L, BOD >=100mg/
L, SS >=120mg/L, TN >=40mg/L, NH3- N >=8mg/L, TP >=2mg/L.
After the biochemical treatment of the present embodiment device and conventional nitrification precipitation, filter tank process, effluent quality:COD <
50mg/L, BOD < 20mg/L, SS < 10mg/L, TN < 5mg/L, NH3- N < 1mg/L, TP < 0.5mg/L.
Claims (5)
1. a kind of town sewage biochemical treatment apparatus, including the anaerobism section being sequentially communicated(2), anoxia section(3)And aerobic section(4),
In anaerobism section(2)It is provided with water inlet(1), in aerobic section(4)It is provided with outlet(6)It is characterised in that in anaerobism section(2), anoxia
Section(3)And aerobic section(4)Inside it is respectively equipped with fixing filler(22), combined stuffing(31)And floating stuffing(41), in anoxia section(3)
And aerobic section(4)Bottom be provided with aerator(5).
2. device as claimed in claim 1 is it is characterised in that described anaerobism section(2)With anoxia section(3)Between be provided with to detest and lacked
Aquaporin(23)With detest scarce return flow line(32).
3. device as claimed in claim 1 is it is characterised in that described anoxia section(3)And aerobic section(4)Between be provided with and lacked
Aquaporin(33)Become reconciled scarce return flow line(42).
4. device as claimed in claim 1 is it is characterised in that described anaerobism section(2)The several deflection plates of interior installation(21), fixing
Filler(22)It is evenly distributed on deflection plate(21)Between.
5. device as claimed in claim 1 is it is characterised in that described biochemical treatment apparatus also include and aerobic section(4)Connection
Nitrification settler, described nitrification settler includes sedimentation tank, is divided into contraminated zone and settling zone, in sedimentation tank in sedimentation tank
Bottom be provided with aerating system, be provided with nitrifying sludge return duct and air stripping system in the lower section of aerating system.
Priority Applications (1)
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CN201620921759.8U CN205973978U (en) | 2016-08-23 | 2016-08-23 | Town sewage biochemical treatment device |
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CN201620921759.8U CN205973978U (en) | 2016-08-23 | 2016-08-23 | Town sewage biochemical treatment device |
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CN205973978U true CN205973978U (en) | 2017-02-22 |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107244737A (en) * | 2017-06-27 | 2017-10-13 | 四川腾颢环保工程有限公司 | Complex biological denitrification and dephosphorization method and device |
CN108483660A (en) * | 2018-06-15 | 2018-09-04 | 王宝贞 | Fixed biofilm ecological treatment system |
CN111777179A (en) * | 2020-06-29 | 2020-10-16 | 北京工业大学 | A/O coupling sulfur autotrophic denitrification enhanced low-carbon-nitrogen-ratio sewage nitrogen and phosphorus removal device and method |
CN112661268A (en) * | 2021-01-05 | 2021-04-16 | 境友环保科技(北京)有限公司 | Novel sewage treatment equipment capable of realizing solid-liquid separation |
-
2016
- 2016-08-23 CN CN201620921759.8U patent/CN205973978U/en active Active
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107244737A (en) * | 2017-06-27 | 2017-10-13 | 四川腾颢环保工程有限公司 | Complex biological denitrification and dephosphorization method and device |
CN108483660A (en) * | 2018-06-15 | 2018-09-04 | 王宝贞 | Fixed biofilm ecological treatment system |
CN111777179A (en) * | 2020-06-29 | 2020-10-16 | 北京工业大学 | A/O coupling sulfur autotrophic denitrification enhanced low-carbon-nitrogen-ratio sewage nitrogen and phosphorus removal device and method |
CN112661268A (en) * | 2021-01-05 | 2021-04-16 | 境友环保科技(北京)有限公司 | Novel sewage treatment equipment capable of realizing solid-liquid separation |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder |
Address after: No. 16, camphor East Road, Yuhua District, Changsha, Hunan Patentee after: POWERCHINA ZHONGNAN ENGINEERING Corp.,Ltd. Patentee after: China Power Construction Environmental Protection Technology Co.,Ltd. Address before: No. 16, camphor East Road, Yuhua District, Changsha, Hunan Patentee before: POWERCHINA ZHONGNAN ENGINEERING Corp.,Ltd. Patentee before: Hunan Zhongnan Water Environmental Protection Technology Co.,Ltd. |
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CP01 | Change in the name or title of a patent holder |