CN207121522U - A kind of tail water puies forward mark processing system - Google Patents
A kind of tail water puies forward mark processing system Download PDFInfo
- Publication number
- CN207121522U CN207121522U CN201721073790.1U CN201721073790U CN207121522U CN 207121522 U CN207121522 U CN 207121522U CN 201721073790 U CN201721073790 U CN 201721073790U CN 207121522 U CN207121522 U CN 207121522U
- Authority
- CN
- China
- Prior art keywords
- processing system
- puies forward
- mark processing
- tail water
- area
- 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.)
- Active
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model provides a kind of tail water and puies forward mark processing system, including oxidative system and micro-filtration bed system, the oxidative system connect with micro-filtration bed system.The utility model mainly solves the problems such as current city domestic sewage puies forward the high cost of mark reforming technology, high management and water quality increase rate are small, compared with the Ozone activated carbon filter technique of existing use, ozone amount saves 60%, energy-conservation 70%, spoil disposal is washed in non-recoil, without personal management, water quality improves about 2 times, and the discharge water that dispatches from the factory can reach the class standard of surface water 4 or 5.The more common wetland floor space of the utility model reduces about 70%, is saved the area for double-deck build of following sewage plant.
Description
Technical field
It the utility model is related to water conservancy technical field of environment protection equipment, and in particular to a kind of tail water puies forward mark processing system.
Background technology
To control the surface water and the quality of groundwater such as water pollution, protection rivers, lake, canal, channel, reservoir and ocean
Kilter, ensure health, maintaining ecological balance, promote the development of national economy and town and country construction, China specially formulates
Pollution discharge standard.Pollution discharge standard is commonly known as sewage drainage standard, and it is the water according to receiving water body
Matter requirement, combining environmental feature and society, economy, technical conditions, to the water pollutant that is discharged into the waste water of environment and caused
The control standard that injurious factor is made.
At present, the discharge of China's major part city domestic sewage also rests on 1 grade of B discharge standard, proposes mark transformation and compels in eyebrow
Eyelash, but the existing main advanced treating mode for proposing mark transformation or using Ozone activated carbon filter, 1 grade can be realized using the technique
A discharge standard, still, operating cost is very high, extremely difficult if thinking to improve effluent quality again.And China's entirety ecological environment
Very havoc is had been subjected to, natural purifying ability is very weak, even if 1 grade of A discharge standard is not for environment and small
Burden, the formation for black smelly river is also no small contribution.Therefore, draining water quality continue raising will turn into one kind necessarily become
Gesture.
Utility model content
The shortcomings that for above-mentioned prior art, the purpose of this utility model are to provide a kind of energy-conservation, and spoil disposal, nothing are washed in non-recoil
Personal management is needed, the tail water that effluent quality greatly improves puies forward mark processing system so that the discharge water that dispatches from the factory can reach the class of surface water 4
Or 5 class standards, to solve, current city domestic sewage proposes the high cost of mark technique, high management and water quality increase rate is small asks
Topic.
According to one side of the present utility model, there is provided a kind of tail water puies forward mark processing system, including oxidative system and micro-
Filter bed system, the oxidative system connect with micro-filtration bed system.
Preferably, the oxidative system includes the ozone machine and water distributing area being sequentially communicated, pre-oxidation area and sump, institute
Ozone machine is stated to connect with the pre-oxidation area.
Preferably, the micro-filtration bed system is provided with micro-filtration area, anoxic zone and collecting pipe from up to down, the collecting pipe with
Outlet pipe connects.
Preferably, the ozone machine is connected by ozone delivery pipe with the pre-oxidation area.
Preferably, the port that the ozone delivery pipe is placed in pre-oxidation area is provided with ozone diffuser.
Preferably, the ozone delivery pipe is provided with the first valve and the second valve.
Preferably, it is provided with the first downflow weir between the water distributing area and the pre-oxidation area.
Preferably, it is provided with the second downflow weir between the pre-oxidation area and the sump.
Preferably, second pond water inlet pipe is provided with the water distributing area.
Preferably, the pre-oxidation area top is provided with the first discharge pipeline, and bottom is provided with the second discharge pipeline.
Preferably, elevator pump is installed, the elevator pump is connected by water distributor with micro-filtration area in the sump.
Preferably, the water distributor is provided with electromagnetic flowmeter, for measuring water flow.
Preferably, the water distributor is provided with the 3rd valve.
Preferably, the ozone machine is connected by tube aerator with anoxic zone.
Preferably, one end that the tube aerator connects with ozone machine is placed between the first valve and the second valve.
Preferably, spiral nozzle is provided with the micro-filtration area.
Preferably, water plant is provided with the micro-filtration area.
Preferably, the collecting pipe is provided with peep hole.
Compared with prior art, the utility model tail water carries mark processing system, including oxidative system and micro-filtration bed system, institute
Oxidative system is stated to connect with micro-filtration bed system.Sewage plant is difficult to continue to pollute in biodegradable tail water by the utility model first
Thing, into small molecule, then enters back into micro-filtration bed system, pollutant is micro- by oxidative system Oxidative demage after sprinkling is aerated
Filter bed internal system can be handled with deep biochemical, faster the carbon filter residence time be about 40 times.The utility model mainly solves
The problems such as city domestic sewage puies forward the high cost of mark reforming technology at present, high management and water quality increase rate are small, with existing use
Ozone activated carbon filter technique compare, ozone amount save 60%, energy-conservation 70%, spoil disposal is washed in non-recoil, without personal management, water quality
About 2 times are improved, the discharge water that dispatches from the factory can reach the class standard of surface water 4 or 5.The more common wetland floor space of the utility model is reduced
About 70%, saved the area for double-deck build of following sewage plant.
Brief description of the drawings
Fig. 1 is that the tail water of an embodiment puies forward mark processing system schematic front view;
Fig. 2 is that the tail water of an embodiment puies forward mark processing system schematic top plan view;
1- ozone machines;The valves of 2- first;The valves of 3- second;4- second pond water inlet pipes;5- ozone tracheaes;6- water distributing areas;7-
Pre-oxidize area;The downflow weirs of 8- first;9- ozone diffusers;The discharge pipelines of 10- first;The discharge pipelines of 11- second;12- sumps;13-
First downflow weir;14- elevator pumps;15- water distributors;The valves of 16- the 3rd;17- electromagnetic flowmeters;18- tube aerators;19- is lacked
Oxygen area;20- micro-filtrations area;21- collecting pipes;22- spiral nozzles;23- peep holes;24- outlet pipes;25- water plants;26- ozone
Delivery pipe.
Embodiment
In order that creation characteristic of the present utility model, technological means and reached purpose are readily apparent from understanding, below in conjunction with tool
The utility model is expanded on further in body embodiment.
A kind of tail water provided by the utility model carries mark processing system, including oxidative system and micro-filtration bed system, the oxygen
Change system connects with micro-filtration bed system.Sewage plant is difficult to continue pollutant oxidation in biodegradable tail water and broken by the utility model
Badly into small molecule, then enter back into micro-filtration bed system after sprinkling is aerated and carry out deep biochemical processing, solve current city life
The problems such as sewage living puies forward the high cost of mark reforming technology, high management and water quality increase rate are small.
As illustrated, the utility model oxidative system includes ozone machine 1 and the water distributing area 6 being sequentially communicated, pre-oxidation area 7
With sump 12, the ozone machine 1 connects with the pre-oxidation area 7.
Preferably, the utility model ozone machine 1 is connected by ozone delivery pipe 26 with the pre-oxidation area 7.The ozone
The port that delivery pipe 26 is placed in pre-oxidation area 7 is provided with ozone diffuser 9.The ozone delivery pipe 26 is provided with the first valve 2
With the second valve 3.
Preferably, second pond water inlet pipe 4, the water distributing area 6 and the pre-oxidation area are provided with the utility model water distributing area 6
The first downflow weir 8 is provided between 7, the pre-oxidation top of area 7 is provided with the first discharge pipeline 10, and bottom is provided with the second discharge pipeline 11.
In implementation, sewage plant secondary clarifier effluent is collected into water distributing area 6 by second pond water inlet pipe 4, then is overflow by first
The uniform water distribution of weir 8 is flowed to pre-oxidizing in area 7, and ozone machine 1 generates ozone and hardly possible is dropped into pre-oxidation area 7 by ozone diffuser 9
The organic matter of solution carries out pre-oxidation again and destroys its strand, and tail gas carries warp float first row mud pipe on most of particulate matter(
That is air supporting)10 discharge pre-oxidation areas 7, heavy solids outside the second discharge pipeline 11 then by arranging.
Preferably, it is provided with the second downflow weir 13 between the utility model pre-oxidation area 7 and the sump 12.It is described to catchment
Elevator pump 14 is installed, the elevator pump 14 is connected by water distributor 15 with micro-filtration bed system in well 12.In implementation, through pre-oxidation
The water that area 7 pre-oxidizes passes through in the uniform water distribution of the second downflow weir 13 to sump 12, the elevator pump 14 being installed in sump 12
Water cloth will be pre-oxidized into micro-filtration bed system by water distributor 15.
Preferably, the utility model water distributor 15 is provided with electromagnetic flowmeter 17, is particularly used in measurement water flow.Institute
State and the 3rd valve 16 is additionally provided with water distributor 15.
Preferably, the utility model micro-filtration bed system is provided with micro-filtration area 20, anoxic zone 19 and collecting pipe 21 from up to down,
The collecting pipe 21 is connected with outlet pipe 24, by treated tail water qualified discharge.
Preferably, the utility model ozone machine 1 is connected by tube aerator 18 with anoxic zone 19.The tube aerator
18 one end connected with ozone machine 1 are placed between the first valve 2 and the second valve 3.
In implementation, the utility model periodically can be passed through ozone gas by tube aerator 18 to anoxic zone 19, for product
Tire out the regular oxidation processes of the organic matter for being difficult to degrade around medium material, effectively avoid the blockage problem in micro-filtration area 20.This practicality
By setting re-oxidation equipment inside new micro-filtration area 20 so that sewage plant tail water contaminant removal efficiency reaches 40-50%.
Preferably, spiral nozzle 22 is provided with the utility model micro-filtration area 20, medium bacterium is it also avoid in addition to efficiently oxygen-enriched
The blockage problem of group.
Preferably, it is provided with water plant 25 in the micro-filtration area 20.The utility model micro-filtration area 20 is by multi-level multimedium
And water plant 25 forms ecological balance body, have and re-digest and denitrification function.
An efficient branch of the utility model micro-filtration bed system as ecological wetland, there is unique structure construction, lead to
Cross and the micro-filtration area 20 containing water plant, anoxic zone 19 and collecting pipe 21 are set from up to down, can be different from conventional fast
Fast carbon filter and common wetland, form the phytomicroorganism ecological balance of uniqueness, pollutant can be with deep biochemical inside it at
Reason, faster the carbon filter residence time be about 40 times.The utility model rationally alleviates the micro- life of winter low temperature using biological heat energy
The problem of thing poor activity.
Preferably, the utility model collecting pipe 21 is provided with peep hole 23, to facilitate observation water quality situation.
It is as follows that the utility model tail water puies forward mark processing system operation principle:Sewage plant secondary clarifier effluent is intake by second pond
Pipe 4 is collected into water distributing area 6, then by the uniform water distribution of the first downflow weir 8 to pre-oxidizing in area 7, by the first valve 2 and the second valve
Door 3 is opened, and ozone machine 1 generates ozone to be had by the ozone diffuser 9 of ozone delivery pipe 26 into pre-oxidation area 7 to difficult degradation
Machine thing carries out pre-oxidation again and destroys its strand, and tail gas carries warp float first row mud pipe on most of particulate matter(Namely air supporting)
10 discharge pre-oxidation ponds, heavy solids outside the second discharge pipeline 11 then by arranging, and the 3rd valve 16 is open-minded, and pre-oxidation water is boosted
The water distribution of pump 14 to micro-filtration area 20, micro-filtration area 20 forms ecological balance body by multi-level multimedium and water plant 25, has again
Digestion and denitrification function, efficient oxygen-enriched spiral nozzle 22 is employed in micro-filtration area 20 during water distribution, is also avoided in addition to efficiently oxygen-enriched
The blockage problem of medium cenobium body.Meanwhile the utility model is connected with tube aerator 18 in anoxic zone 19 and is periodically passed through ozone
Gas, for being accumulated in the regular oxidation processes of organic matter for being difficult to degrade around medium material, effectively avoid the blocking in micro-filtration area 20
Problem, treated tail water are sent to the qualified discharge of outlet pipe 24 by collecting pipe 21.
To sum up, compared with the Ozone activated carbon filter technique of existing use, the utility model ozone amount saves 60%, energy-conservation
70%, spoil disposal is washed in non-recoil, and without personal management, water quality improves about 2 times, and the discharge water that dispatches from the factory can reach the category of surface water 4 or 5
It is accurate.The more common wetland floor space of the utility model reduces about 70%, is saved the area for double-deck build of following sewage plant.This practicality
It is new rationally using biological heat energy to alleviate winter low temperature microbial activity difference the problems such as, be that sewage plant is afforested technique construction and carried entirely
For technological reserve.
For ease of description, the utility model is described with water working media, it should be noted that using other liquid or
The material of other forms reaches as working media administers purpose, also in scope of protection of the utility model.
The advantages of general principle of the present utility model, principal character and the utility model has been shown and described above.One's own profession
The technical staff of industry is it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, the utility model can also on the premise of the spirit and scope of the utility model is not departed from
There are various changes and modifications, these changes and improvements are both fallen within claimed the scope of the utility model.The utility model will
Protection domain is asked to be defined by appended claims and its equivalent.
Claims (18)
1. a kind of tail water puies forward mark processing system, it is characterised in that including oxidative system and micro-filtration bed system, the oxidative system and
Micro-filtration bed system connects.
2. tail water according to claim 1 puies forward mark processing system, it is characterised in that the oxidative system include ozone machine with
And water distributing area, pre-oxidation area and the sump being sequentially communicated, the ozone machine connect with the pre-oxidation area.
3. tail water according to claim 2 puies forward mark processing system, it is characterised in that the micro-filtration bed system is set from up to down
There are micro-filtration area, anoxic zone and collecting pipe, the collecting pipe is connected with outlet pipe.
4. the tail water according to Claims 2 or 3 puies forward mark processing system, it is characterised in that the ozone machine is defeated by ozone
Pipe is sent to be connected with the pre-oxidation area.
5. tail water according to claim 4 puies forward mark processing system, it is characterised in that the ozone delivery pipe is placed in pre-oxidation
Port in area is provided with ozone diffuser.
6. tail water according to claim 5 puies forward mark processing system, it is characterised in that the ozone delivery pipe is provided with first
Valve and the second valve.
7. the tail water according to Claims 2 or 3 puies forward mark processing system, it is characterised in that the water distributing area and the pre- oxygen
Change is provided with the first downflow weir between area.
8. tail water according to claim 7 puies forward mark processing system, it is characterised in that the pre-oxidation area and the sump
Between be provided with the second downflow weir.
9. the tail water according to Claims 2 or 3 puies forward mark processing system, it is characterised in that it is heavy that two are provided with the water distributing area
Pond water inlet pipe.
10. the tail water according to Claims 2 or 3 puies forward mark processing system, it is characterised in that the pre-oxidation area top is provided with
First discharge pipeline, bottom are provided with the second discharge pipeline.
11. tail water according to claim 3 puies forward mark processing system, it is characterised in that lifting is provided with the sump
Pump, the elevator pump are connected by water distributor with micro-filtration area.
12. tail water according to claim 11 puies forward mark processing system, it is characterised in that the water distributor is provided with electromagnetic current
Gauge, for measuring water flow.
13. tail water according to claim 12 puies forward mark processing system, it is characterised in that the water distributor is provided with the 3rd valve
Door.
14. tail water according to claim 3 puies forward mark processing system, it is characterised in that the ozone machine is aerated by tubular type
Device connects with anoxic zone.
15. tail water according to claim 14 puies forward mark processing system, it is characterised in that the tube aerator and ozone machine
One end of connection is placed between the first valve and the second valve.
16. tail water according to claim 3 puies forward mark processing system, it is characterised in that spiral is provided with the micro-filtration area and is sprayed
Head.
17. tail water according to claim 3 puies forward mark processing system, it is characterised in that aquatic plant is provided with the micro-filtration area
Thing.
18. tail water according to claim 3 puies forward mark processing system, it is characterised in that the collecting pipe is provided with peep hole.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721073790.1U CN207121522U (en) | 2017-08-25 | 2017-08-25 | A kind of tail water puies forward mark processing system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721073790.1U CN207121522U (en) | 2017-08-25 | 2017-08-25 | A kind of tail water puies forward mark processing system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207121522U true CN207121522U (en) | 2018-03-20 |
Family
ID=61611187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721073790.1U Active CN207121522U (en) | 2017-08-25 | 2017-08-25 | A kind of tail water puies forward mark processing system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207121522U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112794549A (en) * | 2019-11-14 | 2021-05-14 | 北京远浪潮生态建设有限公司 | High-load anti-blocking type light ultra-high-porosity plant filter bed process technology and method |
CN113620540A (en) * | 2021-09-06 | 2021-11-09 | 深圳市万科物业服务有限公司 | Sewage treatment plant tail water treatment circulation system |
-
2017
- 2017-08-25 CN CN201721073790.1U patent/CN207121522U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112794549A (en) * | 2019-11-14 | 2021-05-14 | 北京远浪潮生态建设有限公司 | High-load anti-blocking type light ultra-high-porosity plant filter bed process technology and method |
CN113620540A (en) * | 2021-09-06 | 2021-11-09 | 深圳市万科物业服务有限公司 | Sewage treatment plant tail water treatment circulation system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102001785B (en) | Compound biological film integrated reactor for treatment of domestic sewage and application method | |
CN205590508U (en) | Integrate sewage treatment system | |
CN103508640B (en) | Device for wastewater treatment and sludge reduction and stabilization and wastewater treatment method thereof | |
CN102161554A (en) | Anaerobic hydrolysis-acidification and anoxic-aerobic process-sequencing batch reactor (AO-SBR) integrated sewage treatment reaction tank | |
CN104710018A (en) | Submerged device and method for rapid multiplication culture by jetting and backflow for anaerobic ammonia oxidizing bacteria multi-phase mixed culture | |
CN112897835A (en) | Preparation device and domestication method for domesticating anaerobic digestion sludge into Feammox functional sludge | |
CN207121522U (en) | A kind of tail water puies forward mark processing system | |
CN106517524B (en) | Device and method for treating town sewage by micro-aeration baffling wetland filter tank | |
CN105668947A (en) | Sewage purification filter system | |
CN111138046A (en) | Rear denitrification and denitrification filter device based on depth upgrading and treatment process thereof | |
CN207986978U (en) | A kind of synchronous nitration and denitrification sewage-treatment plant | |
CN105645699A (en) | Sewage purification treatment device | |
CN104528922A (en) | Upward flow type biological aerated filter | |
CN106336011A (en) | Method for treating sewage plant tail water by utilizing continuous backwash denitrification deep bed filter | |
CN104591409B (en) | Method for treating pig farm wastewater by using micro-aerobic biological treatment device for low-C/N-ratio manure dry-collection pig farm wastewater | |
CN201395543Y (en) | Aeration Sedimentation Sewage Treatment Plant | |
CN207973640U (en) | A kind of buried under earth type sewage integrated treatment unit | |
CN205933394U (en) | In put that oxygen nitrifies, both ends anoxic denitrification denitrification device | |
CN108862571A (en) | A kind of integral bio Air Exposure equipment | |
CN201825822U (en) | Ozone-BAF integrated reaction equipment used for wastewater treatment | |
CN206448357U (en) | A kind of environment protection public lavatory | |
CN205258129U (en) | Low discharge sewage degree of depth nitrogen and phosphorus removal device | |
CN205347127U (en) | A2O -MBR integrative sewage treatment device | |
CN212894345U (en) | Sewage treatment plant of plant | |
CN211946685U (en) | Rear denitrification filter device based on depth upgrading |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |