CN206126945U - Permanent water level SBR sewage treatment system of pond formula - Google Patents
Permanent water level SBR sewage treatment system of pond formula Download PDFInfo
- Publication number
- CN206126945U CN206126945U CN201621064651.8U CN201621064651U CN206126945U CN 206126945 U CN206126945 U CN 206126945U CN 201621064651 U CN201621064651 U CN 201621064651U CN 206126945 U CN206126945 U CN 206126945U
- Authority
- CN
- China
- Prior art keywords
- reaction zone
- water
- water level
- water inlet
- sewage treatment
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 99
- 239000010865 sewage Substances 0.000 title claims abstract description 28
- 238000006243 chemical reaction Methods 0.000 claims abstract description 49
- 238000007789 sealing Methods 0.000 claims abstract description 4
- 238000005273 aeration Methods 0.000 claims description 37
- 239000010802 sludge Substances 0.000 claims description 23
- 238000005276 aerator Methods 0.000 claims description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 210000005056 cell body Anatomy 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 210000003437 trachea Anatomy 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 13
- 230000000694 effects Effects 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000004927 clay Substances 0.000 abstract description 2
- 238000012163 sequencing technique Methods 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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
- 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
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The utility model provides a permanent water level SBR sewage treatment system of pond formula, relates to sewage treatment. Be equipped with the sewage treatment pond, three region is constituteed and falld into in the sewage treatment pond by two soft walls of fixing on sewage treatment bottom of the pool portion and both sides wall with sealing method of activity, three region is distinguished for the control area of intaking, reaction zone, play water balance in proper order, it is invariable that three regional water level is distinguished to control area, reaction zone and the play water balance of intaking, the top edge of the soft wall of activity is fixed in at least one cursoryly to be gone up and floats on the horizontal plane, and the surface area of the soft wall of activity is the soft wall of activity 1.5~1.8 times at the surface area in the sewage treatment pond of sewage treatment bottom of the pool portion and both sides wall bearing, and the soft wall of messenger's activity can reduce regional automatic skew to the volume. Can adopt native pond patterns such as low -cost rubble, pure clay, build simply, it is with low costs, reduce the energy consumption, it is unblock, area is little, and the investment economizes, adopt permanent water level to strain the hydrophone, reduced hydraulic losses.
Description
Technical field
This utility model is related to sewage disposal, more particularly to a kind of pool formula perseverance water level SBR sewage disposal systems.
Background technology
Sequencing batch reactor system (sequencing batch reactor, abbreviation SBR methods) is the one of activated sludge process
Kind, for each SBR processing system, operation operation be in time arrange in order, sequence batch, SBR techniques one
In 5 stages of individual complete typical cycle of operation point, it is followed successively by into water, reaction, precipitation, draining and leaves unused, all of operation is all
Complete in a reactor (Peng Yong attains five big advantages [J] of .SBR methods. Chinese water supply and drainage, 1993,9 (2):29-31).
SBR techniques can carry out degraded, denitrogenation dephosphorizing and the solid-liquid separation of Organic substance by adjusting the length of operation period, with place's science and engineering
Skill flow process is simple, floor space is little and the features such as reduced investment, is current town sewage plant construction using one of most technique.
Chinese patent ZL201410232351.5 discloses a kind of denitrogenation dephosphorizing constant water level sequencing batch active sludge method and processes dirty
Water system and its method, sewage flow into three functional areas that the vertical sail of the water being reciprocally moveable is divided into variable volume.The method and its
System is realized permanent water level, continuum micromeehanics in single treatment tank, stirring, aeration, precipitates, strains water and continuous effluent.
The content of the invention
The purpose of this utility model is to provide with effluent quality is good, civil engineering simple, small investment, take up an area little, operation letter
A kind of pool formula perseverance water level SBR sewage disposal systems of the features such as single, easy maintenance.
This utility model is provided with treatment tank, and the treatment tank is fixed on sewage disposal in a sealing fashion by two pieces
Movable soft wall in bottom of pond portion and two side constitutes and is divided into three regions, and three regions are followed successively by into water control zone, instead
Answer area, water outlet equilibrium area, the water inlet control zone, the three region constant levels in reaction zone and water outlet equilibrium area；The activity is soft
The top edge of wall is fixed at least one cursory upper and float on horizontal plane, and the surface area of movable soft wall is movable soft wall in sewage
1.5～1.8 times of the surface area of the treatment tank of processing pond bottom and two side bearing, enable movable soft wall to subtract to volume
Zonule automatic deviation.
The treatment tank can adopt pool Shi Tu ponds for main body, and in the type of falling truncated rectangular pyramids, four the week side of boss wall of main body is equipped with
Antiseepage film, bottom adopt concrete hardening, cell body crown center to be provided with workbench aisle and support crane span structure.Treatment tank also may be used
Secondary Design transformation is carried out using original pond.
The water inlet control zone is provided with continuum micromeehanics mouth, reaction zone water inlet；The reaction zone be provided with reaction zone water inlet pipe,
Reaction zone intake pump, blender, aerator, water decanter, excess sludge sludge pump；The water outlet equilibrium area is provided with reaction zone and goes out
The mouth of a river, continuous effluent mouth.
The reaction zone water inlet in water inlet control zone, reaction zone water inlet Jing pipelines and reaction zone water inlet pipe phase
Even, reaction zone intake pump is provided with the reaction zone water inlet pipe；The import of the excess sludge sludge pump is located in reaction zone, instead
Area's outlet Jing pipelines are answered to be connected with water decanter.
The blender of the reaction zone is Double-curved-surface stirring machine, and blender is vertically arranged in treatment tank, blender top
End is fixed on the support crane span structure merged with workbench aisle.
The aerator can be provided with aerated conduit and at least one rotational flow aeration device.
The aerated conduit can be provided with main aeration tube and at least one aeration tube, and the main aeration tube is located at reaction zone level
On face, centered on main aeration tube, radially structure vertical downwards, props up aeration tube one end and main aeration tube to described aeration tube
It is connected, an aeration tube other end is connected with rotational flow aeration device, and rotational flow aeration device is arranged in water body, the gas that aerator is produced
Body enters rotational flow aeration device by aerated conduit, forms the high gas-liquid mixture fluid of dissolved oxygen amount and diffuses into water body in jet state
In, realize aeration oxygen supply.
The water decanter can be using permanent water-level decanter.
A kind of pool formula perseverance water level SBR sewage disposal systems can also be provided with setting pot, storage basin and decontaminating apparatuss；Institute
The continuum micromeehanics mouth that setting pot outlet Jing pipelines are stated with water inlet control zone is connected, and setting pot water inlet is provided with grid；The storage
Mud sump import Jing excess sludge discharges pipeline is connected with the outlet of excess sludge sludge pump；The water inlet Jing pipes of the decontaminating apparatuss
Road is connected with the continuous effluent mouth of water outlet equilibrium area.
This utility model has following technique effect：
1) treatment tank of the present utility model can adopt the native pond pattern such as rubble, pure clay of low cost, especially
Secondary Design transformation is carried out using the original waste and old pond in small towns, builds simple, low cost.
2) this utility model adopts high-efficiency cyclone aerator, has the characteristics that compared with common aerator：a.
Reduce by 25%～75% energy consumption；B. do not block；C. in jet state, mixing efficiency is high for gas and water mixing；D. single aerator takes
Big (7～the 15m of business area2), aerated conduit is reduced, it is convenient for installation and maintenance.
3) floor space is little, reduced investment, using permanent water-level decanter, reduces hydraulic loss, and energy consumption is low.
Description of the drawings
Structure composition schematic top plan views of the Fig. 1 for this utility model embodiment.
Structure composition cross-sectional schematics of the Fig. 2 for this utility model embodiment.
Specific embodiment
Referring to Fig. 1 and 2, this utility model embodiment is provided with treatment tank, and the treatment tank is by two pieces with sealing
The movable soft wall 1 that mode is fixed on treatment tank bottom and two side constitutes and is divided into three regions, three regions
It is followed successively by into water control zone A, reaction zone B, water outlet equilibrium area C, the water inlet control zone A, reaction zone B and water outlet equilibrium area C tri-
Individual region constant level；The top edge of the movable soft wall 1 is fixed at least one cursory 2 and floats on horizontal plane, activity
The surface area of soft wall 1 is movable soft wall in treatment tank bottom and the surface area of the treatment tank of two side bearing
1.5～1.8 times, movable soft wall 1 is enable to reduce region automatic deviation to volume.
The treatment tank can adopt pool Shi Tu ponds for main body, and in the type of falling truncated rectangular pyramids, four the week side of boss walls are equipped with anti-
Film is oozed, bottom adopts concrete hardening, cell body crown center to be provided with workbench aisle 3 and support crane span structure 4.Treatment tank also may be used
Secondary Design transformation is carried out using original pond.
The water inlet control zone A is provided with continuum micromeehanics mouth 5, reaction zone water inlet 6；The reaction zone B is provided with reaction zone and enters
Water pipe 7, reaction zone intake pump 8, blender 9, aerator, water decanter 11, excess sludge sludge pump 12；The water outlet equilibrium area
C is provided with reaction zone outlet 13, continuous effluent mouth 14.
The reaction zone water inlet 6 in water inlet control zone A, 6 Jing pipelines of reaction zone water inlet and reaction zone water inlet pipe 7
It is connected, in the reaction zone water inlet pipe 7, is provided with reaction zone intake pump 8；The import of the excess sludge sludge pump 12 is located at reaction
In area B, outlet 13 Jing pipelines in reaction zone are connected with water decanter 11.
The blender 9 of the reaction zone B is Double-curved-surface stirring machine, and blender 9 is vertically arranged in treatment tank, blender
9 tops are fixed on the support crane span structure 4 merged with workbench aisle 3.
The aerator can be provided with aerated conduit and at least one rotational flow aeration device 10-2.
The aerated conduit can be provided with main aeration tube 10-1a and at least one aeration tube 10-1b, the main aeration tube 10-
1a on the B horizontal planes of reaction zone, described aeration tube 10-1b radially structure verticals centered on main aeration tube 10-1a
Downwards, prop up aeration tube 10-1b one end to be connected with main aeration tube 10-1a, the aeration tube 10-1b other ends and rotational flow aeration device
10-2 is connected, and rotational flow aeration device 10-2 is arranged in water body, and the gas that aerator 15 is produced enters eddy flow by aerated conduit
Aerator 10-2, forms the high gas-liquid mixture fluid of dissolved oxygen amount and diffuses in water body in jet state, realize aeration oxygen supply.
The water decanter 11 can be using permanent water-level decanter.
A kind of pool formula perseverance water level SBR sewage disposal systems can also be provided with setting pot E, storage basin F and decontaminating apparatuss
G；The setting pot E outlet Jing pipelines are connected with the continuum micromeehanics mouth 5 of water inlet control zone A, and setting pot E water inlets are provided with grid
D；The storage basin F imports Jing excess sludge discharges pipeline is connected with the outlet of excess sludge sludge pump 12；The decontaminating apparatuss G
Water inlet Jing pipelines be connected with the continuous effluent mouth 14 of water outlet equilibrium area C.
Claims (9)
1. a kind of pool formula perseverance water level SBR sewage disposal systems, it is characterised in that be provided with treatment tank, the treatment tank
Three regions, institute are made up of and are divided into the movable soft wall that two pieces are fixed on treatment tank bottom and two side in a sealing fashion
State three regions to be followed successively by into water control zone, reaction zone, water outlet equilibrium area, the water inlet control zone, reaction zone and go out water balance
Three, area region constant level；The top edge of the movable soft wall be fixed on it is at least one cursory upper and float on horizontal plane, it is living
The surface area for moving soft wall is movable soft wall in treatment tank bottom and the surface area of the treatment tank of two side bearing
1.5～1.8 times, movable soft wall is enable to reduce region automatic deviation to volume.
2. a kind of as claimed in claim 1 pool formula perseverance water level SBR sewage disposal systems, it is characterised in that the treatment tank
Pool Shi Tu ponds are adopted for main body, in the type of falling truncated rectangular pyramids, four the week side of boss wall of main body is equipped with antiseepage film, and bottom is hard using concrete
Change, cell body crown center is provided with workbench aisle and supports crane span structure.
3. a kind of as claimed in claim 1 pool formula perseverance water level SBR sewage disposal systems, it is characterised in that the water inlet control zone
It is provided with continuum micromeehanics mouth, reaction zone water inlet；The reaction zone is provided with reaction zone water inlet pipe, reaction zone intake pump, blender, exposure
Device of air, water decanter, excess sludge sludge pump；The water outlet equilibrium area is provided with reaction zone outlet, continuous effluent mouth.
4. a kind of as claimed in claim 1 pool formula perseverance water level SBR sewage disposal systems, it is characterised in that the reaction zone water inlet
In water inlet control zone, reaction zone water inlet Jing pipelines are connected mouth with reaction zone water inlet pipe, are set in the reaction zone water inlet pipe
There is reaction zone intake pump；The import of the excess sludge sludge pump in the reaction zone, reaction zone outlet Jing pipelines with strain water
Device is connected.
5. as claimed in claim 1 a kind of pool formula perseverance water level SBR sewage disposal systems, it is characterised in that the reaction zone is stirred
Machine is mixed for Double-curved-surface stirring machine, blender is vertically arranged in treatment tank, blender top is fixed on and workbench aisle is closed
And support crane span structure on.
6. as claimed in claim 1 a kind of pool formula perseverance water level SBR sewage disposal systems, it is characterised in that the aerator sets
There are aerated conduit and at least one rotational flow aeration device.
7. as claimed in claim 6 a kind of pool formula perseverance water level SBR sewage disposal systems, it is characterised in that the aerated conduit sets
There are main aeration tube and at least one aeration tube, on the horizontal plane of reaction zone, described aeration tube is with main exposure for the main aeration tube
Centered on trachea radially structure vertical downwards, an aeration tube one end is connected with main aeration tube, an aeration tube other end with
Rotational flow aeration device is connected, and rotational flow aeration device is arranged in water body, and the gas that aerator is produced enters eddy flow by aerated conduit
Aerator, forms the high gas-liquid mixture fluid of dissolved oxygen amount and diffuses in water body in jet state, realize aeration oxygen supply.
8. as claimed in claim 1 a kind of pool formula perseverance water level SBR sewage disposal systems, it is characterised in that the water decanter is adopted
Permanent water-level decanter.
9. a kind of a kind of as claimed in claim 1 pool formula perseverance water level SBR sewage disposal systems, it is characterised in that pool formula
Permanent water level SBR sewage disposal systems are additionally provided with setting pot, storage basin and decontaminating apparatuss；The setting pot outlet Jing pipelines with enter
The continuum micromeehanics mouth in water management area is connected, and setting pot water inlet is provided with grid；The storage basin import Jing excess sludge discharge pipes
Road is connected with the outlet of excess sludge sludge pump；The water inlet Jing pipelines of the decontaminating apparatuss and the continuous effluent of water outlet equilibrium area
Mouth is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621064651.8U CN206126945U (en) | 2016-09-20 | 2016-09-20 | Permanent water level SBR sewage treatment system of pond formula |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621064651.8U CN206126945U (en) | 2016-09-20 | 2016-09-20 | Permanent water level SBR sewage treatment system of pond formula |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206126945U true CN206126945U (en) | 2017-04-26 |
Family
ID=58570314
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621064651.8U Expired - Fee Related CN206126945U (en) | 2016-09-20 | 2016-09-20 | Permanent water level SBR sewage treatment system of pond formula |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206126945U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107176758A (en) * | 2017-06-21 | 2017-09-19 | 邬三丽 | A kind of sewage water treatment method of application iQPR water |
| CN108178299A (en) * | 2017-12-12 | 2018-06-19 | 江西齐联环保科技有限公司 | A kind of waste water treatment system and its wastewater treatment method using SBR processing units |
| CN116395846A (en) * | 2023-04-06 | 2023-07-07 | 山东源广环保科技有限公司 | Constant water level combined biological film SBR sewage treatment system |
-
2016
- 2016-09-20 CN CN201621064651.8U patent/CN206126945U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107176758A (en) * | 2017-06-21 | 2017-09-19 | 邬三丽 | A kind of sewage water treatment method of application iQPR water |
| CN108178299A (en) * | 2017-12-12 | 2018-06-19 | 江西齐联环保科技有限公司 | A kind of waste water treatment system and its wastewater treatment method using SBR processing units |
| CN116395846A (en) * | 2023-04-06 | 2023-07-07 | 山东源广环保科技有限公司 | Constant water level combined biological film SBR sewage treatment system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201313860Y (en) | Integrated aeration-sedimentation aerobic reactor | |
| CN101318735B (en) | Sewage water denitrification processing method of artificial rapid infiltration system and application thereof | |
| CN206126945U (en) | Permanent water level SBR sewage treatment system of pond formula | |
| CN103936148A (en) | Constant-effluent variable-load SVBR sewage processing technology | |
| CN102642982A (en) | System integrating sewage treatment with sludge concentration | |
| CN207713494U (en) | Anoxic reacter and sewage disposal device | |
| CN203112657U (en) | Constant-effluent variable-load SVBR (Steady outflow Variable load Biological Reactor) sewage treater | |
| CN102351384B (en) | Livestock and poultry wastewater treatment device | |
| CN204058066U (en) | Permanent water level combination formula biofilm SBR Sewage treatment systems | |
| CN106745747A (en) | Jet-flow aeration biomembrane reaction pond | |
| CN100500593C (en) | Combined type wastewater treatment method and equipment | |
| CN101792212B (en) | Integrated air lift SBR reactor | |
| CN206407974U (en) | Jet-flow aeration biomembrane reaction pond | |
| CN203545784U (en) | Combined type oxidation ditch with external sedimentation basin | |
| CN103420483B (en) | A kind of sequencing batch type waste disposal plant | |
| CN202379803U (en) | Staggered flow type aeration, sediment and filter device | |
| CN101428904B (en) | Gas winding cycle stream stirring system for open type oxygen lack pool | |
| CN2832804Y (en) | Composite sewage treatment equipment | |
| CN208594093U (en) | Villages and small towns decentralized type sewage treatment reactor | |
| CN209010229U (en) | Novel UASB reactor | |
| CN201284273Y (en) | Integrated reverse anoxic / anaerobic / aerobic sewage water denitrification and dephosphorization apparatus | |
| CN202265480U (en) | Livestock wastewater treatment device | |
| CN202519135U (en) | Sewage treatment and sludge concentration integrated system | |
| CN208038127U (en) | A kind of XS-CSFM intelligent and high-efficiencies bioreactor | |
| CN203159330U (en) | Sewage treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170426 |