CN201010585Y - Intermittent Constructed Wetland Sewage Treatment Reactor - Google Patents
Intermittent Constructed Wetland Sewage Treatment Reactor Download PDFInfo
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- CN201010585Y CN201010585Y CNU2007201235762U CN200720123576U CN201010585Y CN 201010585 Y CN201010585 Y CN 201010585Y CN U2007201235762 U CNU2007201235762 U CN U2007201235762U CN 200720123576 U CN200720123576 U CN 200720123576U CN 201010585 Y CN201010585 Y CN 201010585Y
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- 239000010865 sewage Substances 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000000945 filler Substances 0.000 claims abstract description 17
- 238000009423 ventilation Methods 0.000 claims abstract description 15
- 239000011159 matrix material Substances 0.000 claims description 7
- 238000012856 packing Methods 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 238000000354 decomposition reaction Methods 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 239000010802 sludge Substances 0.000 abstract 1
- 239000000758 substrate Substances 0.000 abstract 1
- 230000000630 rising effect Effects 0.000 description 7
- 241000196324 Embryophyta Species 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000002787 reinforcement Effects 0.000 description 2
- 238000007596 consolidation process Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- -1 vent-pipe Substances 0.000 description 1
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Classifications
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- 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
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- Biological Treatment Of Waste Water (AREA)
Abstract
本实用新型请求保护一种间歇式人工湿地污水处理反应器，反应器包括有池体、填料、进水管、出水管及通风管等。池体内充填基质填料，并设置通风管，填料上种植植物。反应器每个运行周期包括进水-反应-出水和排空闲置四个阶段，序批式运行，周期重复循环。进水管从上部接入，在反应阶段通过通风管的设置强化了系统底部的复氧，有利于硝化效能的提高。反应完成后由底部出水管排出；随后湿地进入排空闲置阶段，在排空闲置期，反应器完成强化复氧作用，促进了系统硝化效能提高，并有利于污泥的氧化分解，改善反应器的堵塞。本实用新型具有处理效能高、脱氮效果好、不易堵塞、占地少、无能耗、投资及运行费低等优点。
The utility model claims an intermittent artificial wetland sewage treatment reactor, which includes a pool body, fillers, water inlet pipes, water outlet pipes, ventilation pipes and the like. The body of the pool is filled with substrate filler, and a ventilation pipe is arranged, and plants are planted on the filler. Each operation cycle of the reactor includes four stages of water inflow-reaction-water outflow and idling, sequence batch operation, cycle repeating cycle. The water inlet pipe is connected from the upper part, and the reoxygenation at the bottom of the system is strengthened through the setting of the ventilation pipe during the reaction stage, which is beneficial to the improvement of nitrification efficiency. After the reaction is completed, it is discharged from the outlet pipe at the bottom; then the wetland enters the idling stage. During the idling stage, the reactor completes the enhanced reoxygenation, which promotes the improvement of the nitrification efficiency of the system, and is conducive to the oxidation and decomposition of sludge, improving the reactor. of the jam. The utility model has the advantages of high treatment efficiency, good denitrification effect, not easy to block, less land occupation, no energy consumption, low investment and operation costs, and the like.
Description
Technical field:
The utility model belongs to sewage disposal, environmental protection technical field, is specifically related to a kind of wetland sewage disposal technology.
Background technology:
Do not see report at present both at home and abroad as yet relevant for the intermission type artificial marsh Sewage treatment systems.Existing artificial marsh sewage treating method mainly contains forms such as surface current, underground undercurrent and vertical current, is Continuous Flow; In practical engineering application, exist usefulness low, take up an area of big, particularly since in the system DO concentration low, make that nitrated usefulness is low and influence denitrification efficiency; And there are problems such as water distribution system complexity and water distribution be inhomogeneous.
Summary of the invention:
The utility model is at the deficiency that exists in the existing artificial swamp sewage disposal, a kind of intermission type artificial marsh sewage-treating reactor has been proposed, improve treatment efficiency, reduce and take up an area of, solve the uniformity of water distribution problem, and can improve the silting problem of wet land system, the stability of wet land system is improved.
The technical solution of the utility model is as follows:
The intermission type artificial marsh sewage-treating reactor comprises pond body, filler, vent-pipe, water inlet pipe and rising pipe etc.Fill matrix fill in the body of pond, plant plant on the filler, water inlet pipe is arranged at body top, pond, rising pipe is arranged at the bottom, be distributed with vent-pipe in the matrix fill of pond body, vent-pipe can be provided with many groups, and every group is interconnected by ventilation standpipe and horizontal vent-pipe and to form, the ventilation standpipe stretches out the water surface, and horizontal vent-pipe is distributed in the filler.
This reactor adopts the sequence batch (operation, and each cycle of operation comprises: water inlet-reaction-water outlet and the emptying four-stage that leaves unused, per stage according to the order of sequence batch mode move the cycle recirculation.Inlet and outlet water intermittently, the treating processes in each stage is as follows:
Water inlet: sewage is flow to the pond body through water inlet pipe from body top, pond;
Reaction: microorganism and the abundant contact reacts of plant in sewage and the pond body on the filler, simultaneously by air through the vent-pipe input, the reoxygenation of consolidation system bottom;
Water outlet: after reaction was finished, sewage was discharged by the rising pipe of pond body bottom;
Emptying is idle: make the system of emptying sewage enter the emptying lay-up period, rely on the reinforcement reoxygenation effect of the air that atmospheric natural reaeration and vent-pipe feed to recover microbic activity after, enter the next cycle circulation again.
Above-mentioned intermission type artificial marsh sewage-treating reactor compared with prior art has following characteristics:
1. strengthen the natural reaeration ability, reactor for treatment usefulness height, the denitrogenation ability is strong.
Reactor adopts the sequence batch (operation, has strengthened the reoxygenation of system bottom by the setting (utilizing internal-external temperature difference) of vent-pipe in step of reaction; Simultaneously, at the emptying lay-up period, because the sewage emptying, the natural reaeration ability of reactor improves greatly, has improved the activity of nitrifier, helps the raising of system's denitrification efficiency.
2. improved the obstruction of reactor.
Emptying lay-up period at reactor has made up sufficient aerobic environment to the microorganism on the filler, can promote the oxygenolysis of mud self, prevents the obstruction of reactor.
3. simplified water distribution system, water distribution is even.
Because reactor is pressed periodic running, water intake mode is the Inlet and outlet water at intermittence, does not have the water distribution uniformity problem, need not to be provided with complicated water distribution pipe system, and water outlet is discharged from the wet land system bottom by rising pipe and gate valve, need not to be provided with the complicated water collection system that goes out.
4. take up an area of less, invest low, the convenient management of working cost.
This reactor has been strengthened the reoxygenation usefulness of system, and the treatment efficiency of reactor is improved greatly, and it is dark to increase the pond, helps reducing taking up an area of, and reduces construction investment; Reactor does not have the energy consumption operation, and working cost is low; Convenient management.
Description of drawings
Fig. 1 is the structural representation of this reactor.
Embodiment:
Referring to Fig. 1, this reactor includes pond body 2, filler 3, ventilation standpipe 4, horizontal vent-pipe 5, water inlet pipe 1 and rising pipe 6 and flowing water Valve 7 etc.Pond body 2 adopts the rectangle form pool body, fills filler 3 in the body of pond, establishes ventilation standpipe 4 and horizontal vent-pipe 5 in the filler 3, and ventilation standpipe 4 stretches out the water surface, and horizontal vent-pipe 5 is distributed in the filler.Body top, pond is connected water inlet pipe 1 and rising pipe 6 respectively with the bottom.Sewage enters the pond body by water inlet pipe 1, after microorganism on sewage and the filler and the plant 8 abundant contact reactss, opens the valve 7 on the rising pipe 6, and sewage is discharged by run by gravity.The wet land system of emptying sewage enters the emptying lay-up period, rely on the reinforcement reoxygenation effect of atmospheric natural reaeration and ventilation standpipe 4 and horizontal vent-pipe 5 after, enter next cycle circulation again.
Main technical details:
Flooding time: 1h;
Reaction times: 24～48h;
Emptying lay-up period: 6～12h;
The water outlet time: 1h;
Structural parameter:
Intermission type artificial marsh size: V=L * B * H;
Intermission type artificial marsh useful volume: V
ψ=HRT * Q (ψ-matrix pores rate, Q-flow);
Matrix fill type: gravel etc.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201235762U CN201010585Y (en) | 2007-02-12 | 2007-02-12 | Intermittent Constructed Wetland Sewage Treatment Reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201235762U CN201010585Y (en) | 2007-02-12 | 2007-02-12 | Intermittent Constructed Wetland Sewage Treatment Reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201010585Y true CN201010585Y (en) | 2008-01-23 |
Family
ID=39045526
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201235762U Expired - Fee Related CN201010585Y (en) | 2007-02-12 | 2007-02-12 | Intermittent Constructed Wetland Sewage Treatment Reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201010585Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102139957A (en) * | 2011-02-23 | 2011-08-03 | 山东大学 | Operation mode capable of efficiently and intensively denitrifying on vertical flow constructed wetland |
| CN102633366A (en) * | 2012-05-03 | 2012-08-15 | 重庆大学 | Mountainous urban artificial wetland sewage treatment system capable of controlling methane emission |
| CN102765810A (en) * | 2012-07-16 | 2012-11-07 | 中山大学 | Method for improving pollution cleaning capability of constructed wetland |
| CN103214100A (en) * | 2013-05-21 | 2013-07-24 | 重庆大学 | Artificial wetland reclaimed water treatment system running in sequencing batch manner |
| CN104045155A (en) * | 2014-06-20 | 2014-09-17 | 哈尔滨工业大学深圳研究生院 | Landscape ecology type decentralization sewage treatment process and device |
-
2007
- 2007-02-12 CN CNU2007201235762U patent/CN201010585Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102139957A (en) * | 2011-02-23 | 2011-08-03 | 山东大学 | Operation mode capable of efficiently and intensively denitrifying on vertical flow constructed wetland |
| CN102139957B (en) * | 2011-02-23 | 2012-11-07 | 山东大学 | Operation mode capable of efficiently and intensively denitrifying on vertical flow constructed wetland |
| CN102633366A (en) * | 2012-05-03 | 2012-08-15 | 重庆大学 | Mountainous urban artificial wetland sewage treatment system capable of controlling methane emission |
| CN102765810A (en) * | 2012-07-16 | 2012-11-07 | 中山大学 | Method for improving pollution cleaning capability of constructed wetland |
| CN103214100A (en) * | 2013-05-21 | 2013-07-24 | 重庆大学 | Artificial wetland reclaimed water treatment system running in sequencing batch manner |
| CN104045155A (en) * | 2014-06-20 | 2014-09-17 | 哈尔滨工业大学深圳研究生院 | Landscape ecology type decentralization sewage treatment process and device |
| CN104045155B (en) * | 2014-06-20 | 2016-06-15 | 哈尔滨工业大学深圳研究生院 | A kind of scenery molding decentralized type sewage processes technique |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080123 Termination date: 20100212 |