CN101585637A - High-concentration sewage treatment system for artificial wetland primarily - Google Patents
High-concentration sewage treatment system for artificial wetland primarily Download PDFInfo
- Publication number
- CN101585637A CN101585637A CNA2008101121510A CN200810112151A CN101585637A CN 101585637 A CN101585637 A CN 101585637A CN A2008101121510 A CNA2008101121510 A CN A2008101121510A CN 200810112151 A CN200810112151 A CN 200810112151A CN 101585637 A CN101585637 A CN 101585637A
- Authority
- CN
- China
- Prior art keywords
- artificial swamp
- sewage treatment
- treatment system
- concentration sewage
- pond
- 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.)
- Pending
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000010802 sludge Substances 0.000 claims abstract description 39
- 230000007062 hydrolysis Effects 0.000 claims abstract description 17
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 17
- 238000005276 aerator Methods 0.000 claims abstract description 3
- -1 sand compound Chemical class 0.000 claims description 4
- 239000002893 slag Substances 0.000 claims description 4
- 239000002562 thickening agent Substances 0.000 claims description 4
- 230000014759 maintenance of location Effects 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 241000353135 Psenopsis anomala Species 0.000 claims description 2
- 229910021536 Zeolite Inorganic materials 0.000 claims description 2
- 239000003818 cinder Substances 0.000 claims description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 2
- 239000011159 matrix material Substances 0.000 claims description 2
- 238000005192 partition Methods 0.000 claims description 2
- 239000004576 sand Substances 0.000 claims description 2
- 239000010457 zeolite Substances 0.000 claims description 2
- 238000012258 culturing Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 17
- 230000000694 effects Effects 0.000 abstract description 4
- 238000000746 purification Methods 0.000 abstract description 4
- 239000003344 environmental pollutant Substances 0.000 abstract description 3
- 231100000719 pollutant Toxicity 0.000 abstract description 3
- 238000004062 sedimentation Methods 0.000 abstract 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 1
- 230000003851 biochemical process Effects 0.000 abstract 1
- 229920002521 macromolecule Polymers 0.000 abstract 1
- 229910052760 oxygen Inorganic materials 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 abstract 1
- 150000003384 small molecules Chemical class 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 5
- 241000196324 Embryophyta Species 0.000 description 2
- 235000014676 Phragmites communis Nutrition 0.000 description 2
- 239000003905 agrochemical Substances 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000002203 pretreatment Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241001494508 Arundo donax Species 0.000 description 1
- 241000684239 Canna x generalis Species 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 240000001398 Typha domingensis Species 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000000247 postprecipitation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000000926 separation method 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
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention relates to a high-concentration sewage treatment system for an artificial wetland primarily, which comprises an anoxic hydrolysis pool, an active sludge pool, a secondary sedimentation tank and the artificial wetland, wherein the yielding water of the anoxic hydrolysis pool is connected into the active sludge pool, the yielding water of the active sludge pool is connected into the secondary sedimentation tank, and the yielding water of the secondary sedimentation tank is connected into the artificial wetland; the bottom of the anoxic hydrolysis pool is provided with a sludge-scrapping device, and the bottom of the active sludge pool is provided with an aerator; and the artificial wetland adopts a horizontal baffling structure, and the water outlet is provided with a water storage tank. The high-concentration sewage treatment system has a simple structure and reasonable process, the anoxic hydrolysis pool decomposes macromolecule organic matters into small molecule organic matters which are easy for aerobic biochemical treatment, and the active sludge pool and the secondary sedimentation tank further reduce the pollutants in the water and improve the oxygen content in the water so as to improve the biochemical process in the artificial wetland, thus the high-concentration sewage can be treated efficiently and good purification effect can be obtained. The high-concentration sewage treatment system is adapted to the treatment of high-concentration sewage.
Description
Technical field
The present invention relates to a kind of Sewage treatment systems, particularly a kind of comprehensive sewage treatment system in conjunction with various processing modes based on artificial swamp belongs to field of environment protection.
Background technology
The mankind use precipitation, filtration process as centralized water treatment plant the earliest from Englishman in 1804, the American had invented coagulation, precipitation, filtration, chlorine disinfectant technology in 1884, use the history in existing 120 years till today, though the mankind constantly have new discovery and raising aspect clean water treatment, but the treatment process of domestic water but remains unchanged basically, does not upgrade in essence and breaks through.Yet very big variation has but taken place at the water source of process object: the water source before century-old is because industrial, agriculture undeveloped, and water body is not contaminated.And in decades, development of modern industry, especially chemical engineering industry happen suddenly, industrial wastewater discharge, the loss of agrochemical, agricultural chemicals, the pollution of sanitary sewage etc., serious day by day to the contaminated degree of source water, make the traditional water treatment process be difficult to guarantee fine water.
Artificial marsh sewage treatment system is a kind of sewage disposal technology that grows up the seventies in 20th century, compare with traditional sewage second-level biochemical processing process, have that good purification, processing unit are simple, the during-operation service convenient management, energy consumption is low, system configuration plasticity-strong,, engineering capital construction strong to load variations adaptability and working cost is low, water outlet has certain biological safety, ecological environment benefit significantly, can realize characteristics such as sewage recycling, obtain people's attention just more and more.Its defective is that floor space is big, and is easy to occur problem such as obstruction, is not suitable for the higher sewage disposal of pollution concentration.
Enter the pollution load of artificial swamp for minimizing, improve the subject range of artificial wet land treating system,, can also utilize the natural wetland condition that wetland is transformed for place with good conditionsi, be adapted to the processing of higher concentration sewage, and do not need land occupation resource separately.Reducing concentration of wastewater can realize by pre-treating technology, for example aerobic biochemical, anaerobic biological, mechanical separation, flocculation sediment or the like, for these modes, need to consider the suitable condition of different places, stability of cost, place, maintenance, quantity of wastewater effluent or the like for example, under passable situation, sorting charge is with minimum pre-treatment mode.
The aerobe method is rapider, thorough than anaerobic treatment method to the removal of organic pollution materials, though need to consume more energy, but still be the most frequently used method of sewage disposal.The aerobe method is divided into two kinds of activated sludge process and biomembrance process substantially, and both differences are that the aerobic microbiological form with mud in sewage in the activated sludge process is the suspended state growth, and the embrane method microorganism then anchors on the filler of setting and grows.These two kinds of aerobic processes respectively have relative merits, and long developing history is arranged all, totally it seems, the former is better to the removal effect of organic pollutant, need lower initial cost, but operation is complicated, is used for the occasion than big yield more: and the latter more adapts to the impact load that the variation of water quality, the water yield brings, operate also simpler, thereby be used for the less water yield or micro-polluted water more. processing.Be very rough, in actual engineering, the aerobic process quality relatively be many-sided, comprise technology, economical and factor society etc.
Summary of the invention
For overcoming the above-mentioned defective of prior art, the invention provides a kind of high-concentration sewage treatment system based on artificial swamp, the required floor space of this system is little, can concentration of treatment than higher sewage, and processing costs is relatively low.
Technical scheme of the present invention is: a kind of high-concentration sewage treatment system based on artificial swamp, comprise anaerobic hydrolysis pond, activated sludge tank, second pond and artificial swamp, the water outlet in described anaerobic hydrolysis pond inserts described activated sludge tank, the water outlet of described activated sludge tank inserts described second pond, and the water outlet of described second pond inserts described artificial swamp.
The present invention has adopted the combination of kinds of processes, earlier larger molecular organics is decomposed into the small organic molecule that is easy to aerobic biochemical by the anaerobic hydrolysis pond, because sewage is in the oxygen consumption of the process of catchmenting, this anaerobic hydrolysis is easy to realize and the regulation and control operating parameter, and can not produce peculiar smell overflows, then by described activated sludge tank aerobic biochemical, micromolecular organism further is decomposed into inorganics and water, warp is at the second pond post precipitation, water enters artificial swamp and carries out the various ways biological treatment, owing to before artificial swamp, carried out hydrolysis and aerobic treatment, greatly reduced pollutants in sewage concentration, help improving the hydraulic load of artificial swamp, improve the degree of purification of water outlet.In addition, this system architecture is simple, and is easy to operate, is adapted to the processing of the sewage of higher concentration.
Description of drawings
Fig. 1 is a system architecture synoptic diagram of the present invention.
Embodiment
Referring to Fig. 1, the invention provides a kind of high-concentration sewage treatment system based on artificial swamp, comprise anaerobic hydrolysis pond 2, activated sludge tank 4, second pond 5 and artificial swamp 6, the water outlet in described anaerobic hydrolysis pond inserts described activated sludge tank, the water outlet of described activated sludge tank inserts described second pond, and the water outlet of described second pond inserts described artificial swamp.
Front, described anaerobic hydrolysis pond can be provided with mechanical grille 1, to eliminate foreign material.
Described anaerobic hydrolysis pond bottom can be provided with scrapes mud device 9, is used for mud is scraped in the mud-collecting slot at the bottom of the pond, by the sludge pump that connects mud-collecting slot mud is released.The discharge tube of described sludge pump connects sludge thickener 8, so that the subsequent disposal of mud.
Described activated sludge tank bottom is provided with aerator 3.
The bottom of described second pond is inversed taper platform shape, and sludge outlet connects sludge pump, and the output channel of described sludge pump inserts described sludge thickener.
The sludge outlet of described second pond also is connected described activated sludge tank by pipeline with pump, to the activated sludge tank returned sluge.
The matrix of described artificial swamp can adopt one or more the mixture in sand compound, rubble, zeolite, Wingdale, cinder, slag, blast furnace slag, rubble, haydite, melon seeds sheet and the cobble.
The plant of described artificial swamp can be adopted the suitable plant that is suitable for local environment conditions and sewage disposal needs, for example reed, Canna generalis Bailey, cattail, Rush, giantreed, Caulis Miscanthis floriduli etc.
Described artificial swamp can utilize existing wetland conditions such as existing depression, pool, handles the back through the bottom surface antiseepage and forms, to avoid sewage permeation polluted underground water in the underground water.
Can also culture bivalves in the described artificial swamp, so that removal of pollutants plays the effect that purifies water.
Described artificial swamp adopts the horizontal baffling structure, and its water outlet place is provided with retention basin 7.
Can be provided with level backflow dividing plate or partition wall in the described artificial swamp, reflux, prolong flow path, and form different conversion zones in different zones so that form.
Described retention basin is arranged on the current end of artificial swamp, so that collect through the sewage behind the wetland purification, is provided with submersible pump in the pond, so that water is got, carries out recycle.
After pre-treatment, can significantly improve the hydraulic surface loading that artificial swamp is disposed of sewage, reduce the floor space of artificial swamp, reduce the sewage treatment project investment cost, and the efficient height of this artificial swamp itself, water flow mode is reasonable, also help to reduce floor space, improve treatment effect, for sanitary sewage and other similar combined sewages, through reaching emission standard after the native system processing.
Claims (10)
1. high-concentration sewage treatment system based on artificial swamp, it is characterized in that comprising anaerobic hydrolysis pond, activated sludge tank, second pond and artificial swamp, the water outlet in described anaerobic hydrolysis pond inserts described activated sludge tank, the water outlet of described activated sludge tank inserts described second pond, and the water outlet of described second pond inserts described artificial swamp.
2. the high-concentration sewage treatment system based on artificial swamp as claimed in claim 1 is characterized in that front, described anaerobic hydrolysis pond is provided with mechanical grille.
3. the high-concentration sewage treatment system based on artificial swamp as claimed in claim 2, it is characterized in that described anaerobic hydrolysis pond bottom is provided with scrapes the mud device, and being provided with the sludge pump that the mud in the pool bottom sludge groove can be extracted out, the discharge tube of described sludge pump connects sludge thickener.
4. the high-concentration sewage treatment system based on artificial swamp as claimed in claim 3 is characterized in that described activated sludge tank bottom is provided with aerator.
5. the high-concentration sewage treatment system based on artificial swamp as claimed in claim 4 is characterized in that the bottom of described second pond is inversed taper platform shape, and sludge outlet connects sludge pump, and the output channel of described sludge pump inserts described sludge thickener.
6. the high-concentration sewage treatment system based on artificial swamp as claimed in claim 5 is characterized in that the sludge outlet of described second pond also is connected described activated sludge tank by pipeline with pump.
7. as claim 1,2,3,4,5 or 6 described high-concentration sewage treatment systems based on artificial swamp, the matrix that it is characterized in that the described artificial swamp of described artificial swamp is that any one or several arbitrarily arbitrary proportions in the following material mixes: sand compound, rubble, zeolite, Wingdale, cinder, slag, blast furnace slag, rubble, haydite, melon seeds sheet and cobble.
8. the high-concentration sewage treatment system based on artificial swamp as claimed in claim 7 is characterized in that being provided with in the described artificial swamp level backflow dividing plate or partition wall.
9. the high-concentration sewage treatment system based on artificial swamp as claimed in claim 8 is characterized in that in the described artificial swamp also culturing that bivalves is arranged.
10. the high-concentration sewage treatment system based on artificial swamp as claimed in claim 9 is characterized in that described retention basin is arranged on the current end of artificial swamp, is provided with submersible pump in the pond, and is provided with the water return line that connects the artificial swamp entrance end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008101121510A CN101585637A (en) | 2008-05-20 | 2008-05-20 | High-concentration sewage treatment system for artificial wetland primarily |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008101121510A CN101585637A (en) | 2008-05-20 | 2008-05-20 | High-concentration sewage treatment system for artificial wetland primarily |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101585637A true CN101585637A (en) | 2009-11-25 |
Family
ID=41370095
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2008101121510A Pending CN101585637A (en) | 2008-05-20 | 2008-05-20 | High-concentration sewage treatment system for artificial wetland primarily |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101585637A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101792234A (en) * | 2010-03-22 | 2010-08-04 | 浙江鎏源环保科技有限公司 | System for disposing artificial wetland sewage and disposal method thereof |
| CN101863585A (en) * | 2010-04-29 | 2010-10-20 | 重庆大学 | Physicochemical treatment + artificial wetland combined treatment system for residential sewage treatment |
| CN101759331B (en) * | 2010-01-12 | 2011-07-20 | 西南大学 | System for treating sewage of preposition activated sludge-gallery type artificial wetland and method therefor |
| CN104176886A (en) * | 2014-09-03 | 2014-12-03 | 长兴日月环保机械有限公司 | Micro power MBR sewage treatment device and method |
-
2008
- 2008-05-20 CN CNA2008101121510A patent/CN101585637A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101759331B (en) * | 2010-01-12 | 2011-07-20 | 西南大学 | System for treating sewage of preposition activated sludge-gallery type artificial wetland and method therefor |
| CN101792234A (en) * | 2010-03-22 | 2010-08-04 | 浙江鎏源环保科技有限公司 | System for disposing artificial wetland sewage and disposal method thereof |
| CN101863585A (en) * | 2010-04-29 | 2010-10-20 | 重庆大学 | Physicochemical treatment + artificial wetland combined treatment system for residential sewage treatment |
| CN104176886A (en) * | 2014-09-03 | 2014-12-03 | 长兴日月环保机械有限公司 | Micro power MBR sewage treatment device and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101397178B (en) | Livestock and poultry raising sewage disposal process and disposal system thereof | |
| CN102775025B (en) | Municipal life wastewater treatment system with high efficiency and low energy consumption | |
| Masi et al. | Multi-stage constructed wetland systems for municipal wastewater treatment | |
| CN103880244B (en) | A comprehensive treatment method for livestock and poultry manure and domestic sewage in rural areas | |
| CN106116031A (en) | A kind of efficient treatment process of slaughtering wastewater | |
| CN209507918U (en) | A kind of sewage-treatment plant suitable for sewage disposal of hospital | |
| CN206266394U (en) | Integrated scattered domestic sewage treatment device | |
| El Moussaoui et al. | Simultaneous assessment of purification performances and wastewater byproducts management plans towards a circular economy: Case of Marrakesh WWTP | |
| CN101585581A (en) | Combined type artificial wetland sewage treatment system | |
| CN104478158A (en) | Sewage treatment method | |
| CN101585579A (en) | High-efficiency artificial wetland sewage treatment system | |
| CN101585637A (en) | High-concentration sewage treatment system for artificial wetland primarily | |
| CN208649072U (en) | A kind of sewage disposal system | |
| CN101585641A (en) | Artificial wetland high-efficiency pre-aeration sewage treatment system | |
| CN107827324B (en) | Urban sewage comprehensive treatment system | |
| Awuah et al. | Performance evaluation of the UASB sewage treatment plant at James Town (Mudor), Accra | |
| CN105036819A (en) | Facility for producing earthworm breeding loam by utilizing aquaculture sewage and method | |
| CN201268647Y (en) | Small-sized domestic sewage processing system | |
| CN108033560A (en) | Septic tank up to standard | |
| CN101585646A (en) | Artificial wetland treatment system for high-concentration sewage | |
| CN101585639A (en) | Artificial wetland sewage treatment system adopting rotational flow active sludge method pretreatment | |
| CN101585642A (en) | Sewage treatment systems based on artificial swamp | |
| Chai et al. | Engineering applications on reclaimed water treatment and reuse of hotel's high grade gray water | |
| CN205011586U (en) | Intelligence sewage treatment system of city hospital | |
| CN101585580A (en) | Artificial wetland sewage treatment system adopting hydrolysis pretreatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| DD01 | Delivery of document by public notice |
Addressee: Haisibote (Beijing) Technology Co., Ltd. Document name: Notification of before Expiration of Request of Examination as to Substance |
|
| DD01 | Delivery of document by public notice |
Addressee: Chen Guangliang Document name: Notification that Application Deemed to be Withdrawn |
|
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20091125 |