CN205603300U - High -efficiency biological contact oxidation tank - Google Patents
High -efficiency biological contact oxidation tank Download PDFInfo
- Publication number
- CN205603300U CN205603300U CN201620436709.0U CN201620436709U CN205603300U CN 205603300 U CN205603300 U CN 205603300U CN 201620436709 U CN201620436709 U CN 201620436709U CN 205603300 U CN205603300 U CN 205603300U
- Authority
- CN
- China
- Prior art keywords
- aerated conduit
- packing layer
- filler
- fixed
- support
- 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
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 30
- 230000003647 oxidation Effects 0.000 title abstract description 14
- 239000000945 filler Substances 0.000 claims abstract description 24
- 210000005056 cell body Anatomy 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims description 14
- 238000012856 packing Methods 0.000 abstract description 18
- 239000010865 sewage Substances 0.000 abstract description 15
- 230000000694 effects Effects 0.000 abstract description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 7
- 229910052760 oxygen Inorganic materials 0.000 abstract description 7
- 239000001301 oxygen Substances 0.000 abstract description 7
- 238000005273 aeration Methods 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000004804 winding Methods 0.000 abstract description 3
- 230000006641 stabilisation Effects 0.000 abstract description 2
- 238000011105 stabilization Methods 0.000 abstract description 2
- 230000003197 catalytic effect Effects 0.000 abstract 2
- 230000002349 favourable effect Effects 0.000 abstract 1
- 238000009434 installation Methods 0.000 abstract 1
- 238000005276 aerator Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000003466 welding Methods 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
- Biological Treatment Of Waste Water (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The utility model provides fill by the concatenation of a plurality of react unit in a high -efficiency biological contact oxidation tank, cell body. React unit includes support, load board, filler and aerated conduit. Inside the load board was fixed in the support, the aerated conduit was fixed in a load board department, and a plurality of fillers transversely are fixed in inside the support to set up directly over the aerated conduit. The utility model discloses an adopting the horizontal filler that sets up, realizing the face contact treatment effect on the sewage tangent plane, improve biological catalytic oxidation treatment effeciency, and pack when transversely setting up, the fastening at both ends is convenient for realize to reduce the winding between packing, the stabilization effect. Simultaneously, add multilayer aeration equipment in the packing layer, be favorable to improving the dissolved oxygen volume of each packing layer to improve biological catalytic oxidation treatment effeciency. It is further, through splicing less react unit, accomplish laying of bio -contact oxidation tank packing layer and aeration equipment, installation, maintenance convenience.
Description
Technical field
This utility model relates to technical field of sewage, especially a kind of high-performance bio contact-oxidation pool.
Background technology
Bio-contact oxidation has the features such as purification efficiency height, strong adaptability, operational management convenience, but still there is problems in that
The filler vertical setting of many employings of the most existing biological contact oxidation pond, after longtime running, its lower end occurs to loosen and be mutually wound around.But owing to pond is deep and the restriction of the condition such as water quality, wrapping phenomena is difficult to find in time and process, thus affects wastewater treatment efficiency.
Although the specific surface area of the most existing filler is relatively big, but biomembrane the most only covers on fibre bundle surface, and therefore the part that effectively processes of filler is only its exterior surface area.When sewage flows upwards through packing layer in pond in a vertical manner, the filler of vertical setting is actual on sewage tangent plane carries out biological contact oxidization treatment in the way of point cantact, therefore limits its treatment effect.
The most existing pack length is 2.5m ~ 3.5m, and aerator is arranged at the bottom of pond, thus causes filler top dissolved oxygen rate on the low side, reduces the overall treatment efficiency of filler.
Utility model content
This utility model provides a kind of high-performance bio contact-oxidation pool, to solve the problems referred to above.By using the filler of horizontally set, it is achieved the face contact treatment effect on sewage tangent plane, improve biological contact oxidization treatment efficiency, and during filler horizontally set, the fastening at two ends facilitates implementation, thus reduce the winding between filler, stabilized treatment effect.Meanwhile, packing layer is set up multilamellar aerator, be conducive to improving the dissolved oxygen amount of each packing layer, thus improve biological contact oxidization treatment efficiency.Further, by splicing less reaction member, complete the laying of biological contact oxidation pond packing layer and aerator, install, easy to maintenance.
In order to realize the purpose of this utility model, plan employing techniques below:
A kind of high-performance bio contact-oxidation pool, it is characterised in that filled by the splicing of some reaction members in cell body；Described reaction member includes support, load plate, filler and aerated conduit, described load plate is fixed on described internal stent, described aerated conduit is fixed at described load plate, and some described fillers are fastened transversely to described internal stent, and are arranged at the surface of described aerated conduit.
Further, described support uses grid plate.
Further, described load plate and described aerated conduit are no less than 2 groups.
The beneficial effects of the utility model are:
1. by the less reaction member of splicing, complete the laying of biological contact oxidation pond packing layer and aerator, install, easy to maintenance.
2., by using the filler of horizontally set, it is achieved the face contact treatment effect on sewage tangent plane, improve biological contact oxidization treatment efficiency, and during filler horizontally set, the fastening at two ends facilitates implementation, thus reduce the winding between filler, stabilized treatment effect.
3. in packing layer, set up multilamellar aerator, be conducive to improving the dissolved oxygen amount of each packing layer, thus improve biological contact oxidization treatment efficiency.
Accompanying drawing explanation
Fig. 1 shows the structural representation of this utility model reaction member.
Fig. 2 shows the structural representation of an embodiment of the present utility model.
Detailed description of the invention
As depicted in figs. 1 and 2, a kind of high-performance bio contact-oxidation pool, is spliced filling by some reaction members 2 in cell body 1.It is easily installed and safeguards.
Described reaction member 2 includes support 21, load plate 22, filler 23 and aerated conduit 24.
It is internal that described load plate 22 is perpendicularly fixed at described support 21 by the way of welding.Be conducive to improving the structural stability of described reaction member 2.
Some described fillers 23 are fastened transversely to the surface of described aerated conduit 24 by the grid of described support 21.The face contact treatment effect being advantageously implemented on sewage tangent plane, improve biological contact oxidization treatment efficiency, and described aerated conduit 24 is for providing bigger dissolved oxygen amount at filler 23 described above it, be conducive to improving further biological contact oxidization treatment efficiency.
Described aerated conduit 24 is fixed at described load plate 22.Be conducive to avoiding described aerated conduit 24 to fall off.
Described load plate 22 and described aerated conduit 24 are no less than 2 groups.
Described support 21 uses grid plate.It is easy to fixing and positions described filler 23, and beneficially sewage horizontal mobility.Be conducive to increasing aeration area, improve the dissolved oxygen amount in sewage.
In one embodiment, the long 10m of the described cell body 1 of biological contact oxidation pond, wide 5m, deep 5m.The long 2.5m of described reaction member 2, wide 5m, high 5.5m.Splice 4 described reaction members 2, i.e. complete the laying of biological contact oxidation pond.
The assembling of described reaction member 2:
From bottom to top at 0.5m, 1.5m and 2.5m of described support 21, be respectively welded the first load plate 221, second and carry on a shoulder pole plate 222 and the 3rd load plate 223, and aerated conduit 24 described in 3 groups is individually fixed at above-mentioned load plate.
Described filler 23 is fastened transversely to above above-mentioned load plate by the cell structure 3 of described support 21, from bottom to top forms the first packed layer the 41, second packing layer 42 and the 3rd packing layer 43.
The bio-contact oxidation course of reaction of sewage:
Sewage flows into from the bottom of described cell body 1, buffers in described first carries on a shoulder pole plate 221 region below.Then, sewage influxing described first packing layer 41, being fixed on the described aerated conduit 24 at described first load plate 221 provides dissolved oxygen for described first packing layer 41, to improve the organic oxidation Decomposition efficiency in sewage.
Sewage pours in described second packing layer 42 the most successively and described 3rd packing layer 43 carries out oxidation Decomposition process.
Sewage is by, after described 3rd packing layer 43, carrying out water stabilization in no-arbitrary pricing region, described cell body 1 top, then discharge, complete biological contact oxidization treatment.
Claims (3)
1. a high-performance bio contact-oxidation pool, it is characterised in that filled by some reaction members (2) splicing in cell body (1)；Described reaction member (2) includes support (21), load plate (22), filler (23) and aerated conduit (24), it is internal that described load plate (22) is fixed on described support (21), described aerated conduit (24) is fixed on described load plate (22) place, it is internal that some described fillers (23) are fastened transversely to described support (21), and is arranged at the surface of described aerated conduit (24).
A kind of high-performance bio contact-oxidation pool the most according to claim 1, it is characterised in that described support (21) uses grid plate.
A kind of high-performance bio contact-oxidation pool the most according to claim 1, it is characterised in that described load plate (22) and described aerated conduit (24) are no less than 2 groups.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620436709.0U CN205603300U (en) | 2016-05-16 | 2016-05-16 | High -efficiency biological contact oxidation tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620436709.0U CN205603300U (en) | 2016-05-16 | 2016-05-16 | High -efficiency biological contact oxidation tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205603300U true CN205603300U (en) | 2016-09-28 |
Family
ID=56967590
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620436709.0U Expired - Fee Related CN205603300U (en) | 2016-05-16 | 2016-05-16 | High -efficiency biological contact oxidation tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205603300U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115124200A (en) * | 2022-07-28 | 2022-09-30 | 厚成科技（南通）有限公司 | Wastewater treatment device and wastewater treatment system with same |
-
2016
- 2016-05-16 CN CN201620436709.0U patent/CN205603300U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115124200A (en) * | 2022-07-28 | 2022-09-30 | 厚成科技（南通）有限公司 | Wastewater treatment device and wastewater treatment system with same |
| CN115124200B (en) * | 2022-07-28 | 2023-12-05 | 厚成科技（南通）有限公司 | Wastewater treatment device and wastewater treatment system with same |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205603300U (en) | High -efficiency biological contact oxidation tank | |
| CN204675884U (en) | A kind of sewage disposal filler framework | |
| CN204529440U (en) | Immersion hanging filler erecting device and comprise the contact-oxidation pool of this device | |
| CN104261560A (en) | River course sewage purification system | |
| CN201801410U (en) | Water treatment packing binding device | |
| JP2019034722A (en) | Independently supported water surface solar power generation system for discrete type operation and maintenance channel and its installation method | |
| CN203333370U (en) | Circulation type bio-contact oxidation integrated reactor allowing membranes to be formed easily | |
| CN204626618U (en) | A kind of cover plate for sewage pool structure | |
| CN214936374U (en) | Limiting module system for water treatment | |
| CN109835979A (en) | Filler, sewage-treatment plant and sewage water treatment method | |
| CN216129381U (en) | Magic cube formula biomembrane filler module | |
| CN215627075U (en) | Light energy biotransformation ecological regulation and control device | |
| CN210736318U (en) | Rapid denitrification pool upgrading and reforming module for non-stop construction | |
| CN211770584U (en) | Filler module of integrated aeration system | |
| CN201809226U (en) | Biofilm belt purification device for riverway water quality treatment | |
| CN212198717U (en) | Ecological floating bed module and ecological floating bed for water quality purification | |
| CN103304024A (en) | Easy membrane formation type circulating bio-contact oxidation integrated reactor | |
| CN202346840U (en) | Hanging device of belt-shaped microorganism fillers in water bodies | |
| CN203683206U (en) | Bracket for carriers in biological contact oxidation tank | |
| CN213977134U (en) | Biochemical pool applying biomass carbon film frame | |
| CN110451640B (en) | Rapid standard lifting and reconstruction module of denitrification tank for non-stop construction and construction process thereof | |
| CN217808916U (en) | Floated ecological bed | |
| CN216584640U (en) | Ecological floating raft and solar aeration integrated device for water environment treatment | |
| CN210620401U (en) | Filler for sewage treatment and frame structure thereof | |
| CN212129226U (en) | Pin-connected panel utility tunnel |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: No. 90 Longshan Street, Youxian Economic Experimental Zone, Mianyang City, Sichuan Province, 621000 Patentee after: Sichuan Sequoia Ridge Environmental Protection Technology Co.,Ltd. Address before: 621900 Long-term Nano Building No. 64 Mianshan Road, Mianyang City, Sichuan Province Patentee before: RED WOOD SCIENCE & TECHNOLOGY Co.,Ltd. |
|
| 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: 20160928 |