CN204281519U - A kind of staged sewage complex ecological treatment facility - Google Patents
A kind of staged sewage complex ecological treatment facility Download PDFInfo
- Publication number
- CN204281519U CN204281519U CN201420783961.XU CN201420783961U CN204281519U CN 204281519 U CN204281519 U CN 204281519U CN 201420783961 U CN201420783961 U CN 201420783961U CN 204281519 U CN204281519 U CN 204281519U
- Authority
- CN
- China
- Prior art keywords
- sewage
- feed
- river
- aerating apparatus
- anaerobic device
- 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
Abstract
The utility model relates to a kind of staged sewage complex ecological treatment facility, its anti impulsion load ability is high, operation runs simple, concrete technical scheme is: adopt grid maker, the anaerobic device being provided with multiple cell and aerating apparatus to form stepped sewage treatmentmethod, progressively removed by the foreign material of sewage.Sewage can carry out multiple abatement processes at unit lattice, improves the treatment effect of sewage, and multiple cell can alleviate surging force when sewage enters simultaneously, the anti impulsion load ability of lift technique, improves equipment to the efficiency of sewage disposal.In addition stepped sewage treatmentmethod, contributes to the waste water that device progressively adapts to high density pollution, improves equipment to the processing power of high-concentration waste water.
Description
Technical field
The utility model relates to a kind of sewage disposal device, especially a kind of staged sewage complex ecological treatment facility.
Background technology
Existing sewage disposal generally adopts the traditional methods such as A20, MBR.A20 and AA0 technique is anaerobism, anoxic, aerobic abbreviation; MBR sewage disposal is a kind of usual way of Modern sewage process, and its membrane bioreactor adopted (Membrane Bioreactor is called for short MBR) technology is a kind of new technology that biologic treating technique combines with membrane separation technique.Above treatment process generally comprises following steps: first rigging up and debugging runs, and the sludge treatment then produced in system operation is finally the cleaning of system cloud gray model certain hour artifact film.There is following shortcoming in these treatment processs: anti impulsion load ability is not high, and effluent quality is unstable; Operation operational management is complicated, and at least one professional need be arranged to safeguard; The mud produced is as mishandling easy generation secondary pollution; Cost of investment is many, and floor space is large, the problems such as working cost is relatively high.
Summary of the invention
In order to overcome the deficiencies in the prior art, it is high that the purpose of this utility model is to provide a kind of anti impulsion load ability, and operation runs simple sewage disposal device.
For solving the problem, the technical scheme that the utility model adopts is as follows: a kind of staged sewage complex ecological treatment facility, comprises grid maker, feed-pipe, anaerobic device, aerating apparatus and water collecting basin.
Described feed-pipe is provided with opening for feed and discharge port, described anaerobic device is provided with water-in and the first row mouth of a river, the opening for feed of described feed-pipe is connected with described grid maker, and the discharge port of described feed-pipe is connected with the water-in of described anaerobic device, and described grid maker is connected with slag-drip opening.
Be provided with first module lattice that several are communicated with, linear array in described anaerobic device, described water-in is arranged on first module lattice foremost, and the described first row mouth of a river is arranged on the first module lattice of least significant end.
Described aerating apparatus is arranged on first exit end at the described first row mouth of a river, and be provided with second unit lattice that several are communicated with, linear array in described aerating apparatus, the second unit lattice of described least significant end are provided with the second row mouth of a river; Described water collecting basin is arranged on second exit end at the described second row mouth of a river.
Preferably: the top of described anaerobic device is provided with access hole.
Preferably: described aerating apparatus comprises the reaction tank be made up of described second unit lattice, be filled with the multiporous biological filler of PE material in described reaction tank, described reaction tank is connected with Aeration fan.
Compared to existing technology, the beneficial effects of the utility model are: sewage is through grid maker, foreign material in sewage are removed by grid maker, then sewage enters anaerobic device, solid matter in sewage can be resolved into dissolved matter or part organic matter degradation by the biological material hanging in anaerobic device, thus improves the biochemical treatment of sewage.After anaerobic device regulating water quality, sewage flows into aerating apparatus, excellent micropopulation and nitrifier, phosphorus bacteria is there is in microbial film under aeration state, can degrade or carbon containing, ammonia nitrogen, phosphorus organic pollution materials in planar water, to reach the object purified water, the water after purification flows into water collecting basin.Sewage is through grid maker, anaerobic device and aerating apparatus successively, progressive, forms stepped processing mode.And there is cell in anaerobic device and aerating apparatus, sewage can carry out multiple abatement processes at unit lattice, improve the treatment effect of sewage, multiple cell can alleviate surging force when sewage enters simultaneously, the anti impulsion load ability of lift technique, improves equipment to the efficiency of sewage disposal.In addition stepped sewage treatmentmethod, contributes to the waste water that device progressively adapts to high density pollution, improves equipment to the waste treatment capacity of high density.
Accompanying drawing explanation
Fig. 1 is overall schematic of the present utility model.
In figure, mark is described as follows:
1, anaerobic device; 2, aerating apparatus; 3, feed-pipe; 4, the first row mouth of a river; 5, the second row mouth of a river; 6, slag-drip opening; 7, biological material hanging; 8, biologic packing material; 9, Aeration fan; 10, first module lattice; 11, access hole; 100, siphunculus.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
A kind of staged sewage complex ecological treatment facility as shown in Figure 1, comprises grid maker (not shown), feed-pipe 3, anaerobic device 1, aerating apparatus 2 and water collecting basin (not shown).
Feed-pipe 3 has opening for feed and discharge port, anaerobic device 1 is provided with water-in and the first row mouth of a river, and the opening for feed of feed-pipe 3 is provided with grid maker, and the discharge port of feed-pipe 3 is connected with the water-in of anaerobic device 1, and grid maker is connected with slag-drip opening 6.Foreign material are first removed through grid maker by sewage, and foreign material are discharged from slag-drip opening 6, and then sewage enters anaerobic device 1 via feed-pipe 3.For convenience of maintenance, access hole 11 is set on the top of anaerobic device 1.
First module lattice 10 that several are communicated with, linear array are comprised in anaerobic device 1, the water-in of anaerobic device 1 is arranged on first module lattice foremost, the first row mouth of a river 4 is arranged on the first module lattice 10 of least significant end, and first exit end at the first row mouth of a river 4 arranges aerating apparatus 2.Sewage by biological material hanging 7, the i.e. effect of anaerobion, consumes a part of organism and solid matter in sewage is resolved into dissolved matter or part organic matter degradation, thus improve the biochemical treatment of sewage in anaerobic device 1.First module lattice 10 quantity shown in Fig. 1 is two, sewage enters the first module lattice 10 in left side after anaerobic treatment from feed-pipe 3, owing to constantly there being sewage to enter formation mobility, the first module lattice 10 making sewage enter into right side from siphunculus 100 carry out anaerobic treatment again.
After regulating water quality, sewage flows in aerating apparatus 2 from the first row mouth of a river 4.Comprise second unit lattice that several are communicated with, linear array in aerating apparatus 2, the second unit lattice of least significant end are provided with the second row mouth of a river 5, and water collecting basin is arranged on second exit end at the second row mouth of a river 5.The role of multiple second unit lattice to the process of sewage and first module lattice 10 in aerating apparatus 2 is different, but processing mode is the same, is all utilize multiple second unit lattice to sewage repeatedly decontamination.
Aerating apparatus 2 is mainly used for the organic and denitrogenation dephosphorizing of degraded, meets aerobic microbiological, anaerobe removes carbon source oxygen requirement, i.e. the writing a Chinese character in simplified form of BOD(Biochemical Oxygen Demand) and nitrobacteria by NH
3ammonia-nitrogen content index in-N(waste water) transform NO
xpHB(poly-β-hydroxybutyric acid in molten phosphorus and decomposer in long-pending phosphorus bacteria absorbing environmental in oxygen environment needed for (oxynitride) and dephosphorization) contact environment that fully reacts for the anaerobic environment of self-reproduction and pollution substance and biophase.
Aerating apparatus 2 comprises the reaction tank be made up of described second unit lattice, fills the multiporous biological filler 8 of PE material in reaction tank, improves the utilising efficiency of air and required oxygen-supplying amount.Reaction tank is connected with Aeration fan 9, and Aeration fan 9 maintains the excellent contact environment in reaction tank, ensures the abundant contact reactss of related substances such as organic pollutants, oxygen, microbial film, water.
Multiple complex microorganism group is defined in aerating apparatus 2, high-solubility oxygen and excellent biological flora and organic pollutant contact reacts, for falling of organic pollutant is removed, the absorption of the oxidation of ammonia nitrogen and phosphorus is removed to create and is conformed most, improves the removal efficiency of organic pollutant and ammonia nitrogen, phosphorus.
Aerator in aerating apparatus 2 selects stainless steel to make aerator by oneself, match with biologic packing material 8, have that power efficiency of oxygen supply is high, coefficient of oxygen utilization is high, surface-area is large, easy to be filmed, do not block, voidage greatly, the advantages such as long service life.
Above-mentioned embodiment is only preferred implementation of the present utility model; can not limit the scope of the utility model protection with this, change and the replacement of any unsubstantiality that those skilled in the art does on basis of the present utility model all belong to the utility model scope required for protection.
Claims (3)
1. a staged sewage complex ecological treatment facility, is characterized in that: comprise grid maker, feed-pipe, anaerobic device, aerating apparatus and water collecting basin;
Described feed-pipe is provided with opening for feed and discharge port, described anaerobic device is provided with water-in and the first row mouth of a river, the opening for feed of described feed-pipe is connected with described grid maker, and the discharge port of described feed-pipe is connected with the water-in of described anaerobic device, and described grid maker is connected with slag-drip opening;
Be provided with first module lattice that several are communicated with, linear array in described anaerobic device, described water-in is arranged on first module lattice foremost, and the described first row mouth of a river is arranged on the first module lattice of least significant end;
Described aerating apparatus is arranged on first exit end at the described first row mouth of a river, and be provided with second unit lattice that several are communicated with, linear array in described aerating apparatus, the second unit lattice of described least significant end are provided with the second row mouth of a river;
Described water collecting basin is arranged on second exit end at the described second row mouth of a river.
2. a kind of staged sewage complex ecological treatment facility as claimed in claim 1, is characterized in that: the top of described anaerobic device is provided with access hole.
3. a kind of staged sewage complex ecological treatment facility as claimed in claim 1, it is characterized in that: described aerating apparatus comprises the reaction tank be made up of described second unit lattice, be filled with the multiporous biological filler of PE material in described reaction tank, described reaction tank is connected with Aeration fan.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420783961.XU CN204281519U (en) | 2014-12-12 | 2014-12-12 | A kind of staged sewage complex ecological treatment facility |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420783961.XU CN204281519U (en) | 2014-12-12 | 2014-12-12 | A kind of staged sewage complex ecological treatment facility |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204281519U true CN204281519U (en) | 2015-04-22 |
Family
ID=52864702
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201420783961.XU Expired - Fee Related CN204281519U (en) | 2014-12-12 | 2014-12-12 | A kind of staged sewage complex ecological treatment facility |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN204281519U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107032494A (en) * | 2017-05-18 | 2017-08-11 | 南昌工程学院 | The removal device and minimizing technology of polluter in a kind of domestic sewage in rural areas |
-
2014
- 2014-12-12 CN CN201420783961.XU patent/CN204281519U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107032494A (en) * | 2017-05-18 | 2017-08-11 | 南昌工程学院 | The removal device and minimizing technology of polluter in a kind of domestic sewage in rural areas |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102775025B (en) | Municipal life wastewater treatment system with high efficiency and low energy consumption | |
CN101885538B (en) | Membrane bioreactor process for removing phosphorus without mud discharge | |
CN101817615A (en) | Anaerobic-sequencing batch biofilm reactor-artificial wetland method for treating piggery wastewater | |
CN104118970B (en) | The biochemical processing method of a kind of percolate and device thereof | |
CN110395851B (en) | High-altitude town sewage treatment method based on nitrogen and phosphorus capture and completely autotrophic nitrogen removal | |
CN204824516U (en) | Breed advanced waste treatment system | |
CN205258126U (en) | AAO - MBR integration nitrogen and phosphorus removal sewage treatment device | |
CN201932988U (en) | Anaerobic/aerobic contact oxidation membrane bioreactor | |
CN204079721U (en) | A kind of sewage disposal device adopting pure oxygen aeration and remaining oxygen reuse | |
CN204079699U (en) | A kind of sewage water recycling and processing equipment of continuous lignin-sludge minimizing | |
CN202116373U (en) | Membrane bioreactor suitable for plateau sewage treatment | |
CN201614333U (en) | Decentralized sewage treatment device | |
CN103641268A (en) | Two-stage bioreactor device and technology for treating garbage leachate | |
CN101386446B (en) | Air-lift baffling internal circulation bioreactor and use method thereof | |
CN102936082B (en) | Short-range aeration sewage purifier | |
CN204281519U (en) | A kind of staged sewage complex ecological treatment facility | |
CN208562049U (en) | A kind of three-dimensional rural sewage treatment equipment | |
CN217947891U (en) | Kitchen garbage effluent disposal system | |
CN203269735U (en) | Equipment for treating rubbish leachate by utilizing two-stage bioreactors | |
CN203582653U (en) | Livestock/fowl culture wastewater treatment system | |
CN202322492U (en) | Sewage treatment equipment of immobilized microorganism reactor | |
CN205313331U (en) | Treatment of domestic sewage retrieval and utilization equipment | |
CN204198490U (en) | A kind of assembly type membrane bioreactor | |
CN113087154A (en) | FMNR nano diatom high-efficiency bioreactor | |
CN105523635A (en) | Integrated biological contact device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150422 Termination date: 20151212 |
|
EXPY | Termination of patent right or utility model |