CN1657440A - Four-segment type sewage treatment system for dispersed residences - Google Patents

Four-segment type sewage treatment system for dispersed residences Download PDF

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CN1657440A
CN1657440A CN2005100380976A CN200510038097A CN1657440A CN 1657440 A CN1657440 A CN 1657440A CN 2005100380976 A CN2005100380976 A CN 2005100380976A CN 200510038097 A CN200510038097 A CN 200510038097A CN 1657440 A CN1657440 A CN 1657440A
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layer
treatment system
sewage treatment
segment type
pond
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CN1305780C (en
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刘华良
王联红
王晓蓉
任洪强
朱文斌
蒋佳良
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Nanjing University
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Nanjing University
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

A 4-segment sewage treating system for the dispersed residences is composed of anaerobic pool, aerobic percolation ditch, anoxic pool and underflow nunja. The process for treating said life sewage includes such steps as treating in anaerobic pool, by-passing, flowing in anoxic pool directly for part of the sewage and via aerobic percolation ditch for rest, anotix treating, and flowing in the underflow nunja.

Description

A kind of four-segment type sewage treatment system for dispersed residences
One, technical field
The present invention relates to a kind of domestic sewage processing method, a kind of four-segment type sewage treatment system for dispersed residences of saying so more specifically.
Two, background technology
Along with constant development of economy, the urbanization process in rural area is accelerated, and living standards of the people improve, and make the quantity of sanitary sewage and concentration all improve greatly, and then cause the villages and small towns water body to be subjected to eutrophication pollution, shows as the pasture and water overgrowing, and water body is smelly.Develop faster with town development that TAI HU AREA is an example, a large amount of unprocessed remittance of small town sewage Taihu Lake have caused Taihu Lake to be subjected to eutrophication pollution, and the pollution that imports Taihu Lake according to statistics has 63.89% from the Taihu Lake basin town domestic sewage.In the vast samll cities and towns of China, residential building often distributes according to physical features, water body, relatively disperses, and sewage is easily collecting not.Therefore, develop the technology of waste water control that is suitable for resident family of dispersive samll cities and towns and become the task of top priority.In addition, along with developing rapidly of tourism, a large amount of villages of having a holiday, the sanatorium's five equilibrium residence district of living scattered also needs domestic sewage processing method simple, on-the-spot disposal.
Activated sludge process is traditional secondary sanitary sewage disposal technology, is widely adopted in the whole world.This method nitric efficiency is undesirable, has only 10~20%.Developed the denitrification denitrogenation Activated Sludge Process with denitrification functions on this basis, as Wuhrmann technology, its flow process is Aerobic Pond---anoxic pond---settling tank.Mainly carry out oxidation, ammonia nitrogen nitrated of carbonaceous organic material in the aerobic reaction pond, the effect in hypoxia response pond is a denitrification denitrogenation.This technology has two shortcomings, and the one, because denitrification process lacks carbon source, the 2nd, sewage enters the first step of system and just carries out aerobic reaction, and for satisfying organic removal, energy consumption is just high.Need power consumption if be used for peasant household of the samll cities and towns aerobic processes that to also have a shortcoming be Aerobic Pond.
The soil is handled as a kind of sewage water treatment method, and its investment working cost is low, is applicable to the samll cities and towns that land resources is abundant beyond doubt, and tourist district, sanatorium's five equilibrium are lived scattered geographic.Artificial swamp belongs to polluted water land and handles category, in recent years, research and application in China increase year by year, municipal effluent soil processing and utilizing design manual (Gao Zhengmin etc., China Standard Press, 1991) some relevant application and designs are disclosed, wherein be widely used underground hollow billet filtration system as a kind of polluted water land treatment system in Japanese rural.And adopt artificial swamp or underground hollow billet filtration system, its nitric efficiency can only reach about 60% (Wu Xiaolei, environmental science, 1995 merely; 16 (3): 83-86).
A kind of domestic sewage processing system (patent No.: 00133498.0) disclose a kind of domestic sewage processing system, organize a performance by biopurification oxidation pond and cross flow purification tank, water reservoir and to constitute, biopurification oxidation pond top is provided with the plant purification water layer, is purifying serike on the water layer.This patent is mainly used in the processing of a small amount of sanitary sewage of concentrating, and the design relative complex need expend certain energy.
Three, summary of the invention
1, the technical problem that will solve
Shortcoming at Wuhrmann technology: the one, because denitrification process lacks carbon source, the 2nd, sewage enters the first step of system and just carries out aerobic reaction, and for satisfying organic removal, energy consumption is just high; The aerobic processes that is used for peasant household of samll cities and towns Aerobic Pond needs power consumption.The invention provides a kind of four-segment type sewage treatment system for dispersed residences, Wuhrmann technology, underground hollow billet filtration system and artificial swamp three are mixed together, the sewage on-the-spot disposal system in a kind of suitable scattered settlement district has been proposed, can so that invest less, operation no energy consumption and treatment effect is good.
2, technical scheme
The present invention improves Wuhrmann technology, promptly (1) thus the load that anaerobic pond reduces aerobic section is set before whole flow process; (2) anaerobic pond goes out a moisture flow part and directly enters anoxic pond and provide carbon source for denitrification process; (3) improving traditional underground hollow billet filtration system is aerobic type diafiltration ditch, replaces the Aerobic Pond in the Wuhrmann technology, thereby has realized aerobic processes with the soil processing mode.The artificial swamp of connecting again after improved Wuhrmann technology at last improves the anti-shock loading of system, guarantees the quality of system's water outlet.Its technical scheme is as follows:
A kind of four-segment type sewage treatment system for dispersed residences, comprise anaerobic pond and anoxic pond, sanitary sewage is shunted after by anaerobic pond, a part enters anoxic pond by the processing of fine oxygen filtration channel, remaining directly enters anoxic pond, sewage after handling by anoxic pond enters current wetland, can directly enter water body by the water outlet of current wetland.
Indoor kitchen waste water, fecal sewage and bath wastewater etc. all sanitary sewage enter anaerobic pond by pipeline, stop more than 1 day at anaerobic pond.Anaerobic pond has various ways: comprise that two grid septic tanks, three-grid septic tank, water outlet are provided with the common fecaluria storage pool of simple and easy grid.Anaerobic pond volume and service number, water consumption and dwell time of sewage are relevant per capita.At anaerobic pond, sewage is through the anaerobically fermenting effect, and organism is wherein tentatively decomposed, and has reduced pollutant load.For general residential district, anaerobic pond exists, and need not invest construction.
Anaerobic pond sewage goes out the moisture two-way, wherein one the tunnel enters fine oxygen filtration channel.Sewage passes through the distribution again of gravel bed in fine oxygen filtration channel, disposing under the soil wicking action to unsaturation diafiltration all around, physics detention, soil by soil absorb a series of effects such as absorption, microbiological degradation utilization and plant absorbing, the oxidized removal of partial organic substances in the sewage, ammonia nitrogen is converted into nitre nitrogen, the phosphoric acid salt major part is formed chemical precipitation then by slag absorption and removes, and small part is by plant absorbing.Sewage flows into water shoot by gravity on the one hand through after the soil filtration, enters atmosphere on the other hand through evapotranspiring.Fine oxygen filtration channel is the key facility of native system.The fine oxygen filtration channel water inlet is from anaerobic pond, and water outlet enters anoxic pond.
Fine oxygen filtration channel (seeing Fig. 2, Fig. 3) gradient 0.5~2%, base plane is del, and the width that catchments is 0.8~1.2 meter, highly is 0.8~1.2 meter (not comprising frozen soil layer thickness), and length is relevant with the processing water yield, and its load is 70~150 liters/Mi Tian.The fine oxygen filtration channel transversal profile is made up of impervious barrier, layer of displacement (unsaturated zone of holding concurrently), filter layer, cloth tank layer, greening layer five part from lower to upper:
A) impervious barrier: be made of polyvinyl chloride film or malthoid etc., be layered on the ground and the side of diafiltration ditch, its effect is to prevent that sewage is to both sides and underground leakage.
B) layer of displacement (hold concurrently ventilate to sudden and violent gas-bearing formation): by diameter is that the gravel (cobble) of 20~40mm is formed.Water after the diafiltration ditch is handled flows into anoxic pond through water outlet pipeline (left side pipeline among the figure) in the stone hole.Air enters from the water outlet pipeline, through stone hole and water body reverse flow, discharges through the pipeline natural ventilation of vertical ground from the opposite side of diafiltration ditch.
C) filter layer: by 15~25% slags, 3~10% peat (or sawdust, rice husk) and the higher ventilation soil of local mixing with soil composition void ratio." sealing coat " established in filter layer and layer of displacement junction, is made of the non-woven fabrics of porous, falls to filling out people's gravel bed to prevent upper layer of soil, destroys the normal draining of layer of displacement.
D) cloth tank layer: the cloth tank is located at how much middle parts of whole diafiltration ditch.Top opening, section takes the shape of the letter U.The water distribution well width is the 25-35% of diafiltration ditch width, dark 80~120mm.Fill out the gravel that diameter is 10~25mm in the cloth tank, the non-woven fabrics and the upper layer of soil of cobble upper berth porous separate.After cesspool sewage enters the cloth tank, distribute, upwards gently be seeped in the soil on every side then through non-woven fabrics in the gravel porous nickel.Cloth tank material can adopt precast concrete or PVC.
E) greening layer: can plant vegetables or lawn, its effect is absorbed nitrogen phosphorus, increases the ability of evapotranspiring, stops rainwater to cause depletion, beautify the environment.Greening laminar surface 10-20cm above ground level, and the centre is higher than the edge, purpose one is to reduce rainwater to infiltrate, the 2nd, increase surface-area, thereby improve the ability of evapotranspiring, improve the make progress potential energy of unsaturation infiltration of sewage.
In order to improve denitrification functions, connect anoxic pond at the fine oxygen filtration channel back segment.Anoxic pond is fluid-tight concrete sump, and in order to keep the anaerobic environment of pool inner water body, anoxic pond top will cover with concrete slab, and cover plate should stay aperture to be used for the discharge of denitrification nitrogen simultaneously.Anoxic pond water inlet comprises two portions, the water outlet of first fine oxygen filtration channel, and it two is in order to the anaerobic pond water outlet of carbon source to be provided, this part water outlet accounts for 10~30% of total water outlet.Sewage is after this stops 5~7 hours, and overflow enters next unit.The anoxic pond useful volume is that 20~25% of anaerobic pond volume is good.
Current wetland is meant artificial marsh sewage treatment system, and its composition is lower floor's lay particle rubble, upper strata mulching soil, kind of plant on soil, microflora that this is actually a kind of soil of uniqueness---plant---.Form one deck microbial film on rubble, soil particle surface, the microorganism on the microbial film participates in each process of sewage purification.This system combines the characteristics of biomembrance process and natural purification, and the detergent power of microorganism and plant is combined, and becomes an efficient purifying system.The wetland groove generally is strip, and long-width ratio is greater than 3, and it is relevant with wetland groove useful volume that the wetland groove is handled the water yield.Constitute by four parts from down to up:
A) impervious barrier: the wetland trench bottom needs the antiseepage polyethylene film.
B) metalling: about 30cm is thick, ballast grain sizes: 4~50mm.
C) pedosphere: about 20cm is thick.
D) layer of plants: must plant specified plant (it is strong to require root system to secrete the oxygen ability, and plant absorbing nitrogen phosphorus ability is strong) on the pedosphere as cattail, reed, Rush, wild rice stem, calamus, Wildcelery Herb etc.
3, beneficial effect
Process native system treated water body effluent quality reaches the B standard (standard that the highest grade) of GB 18918-2002 urban wastewater treatment firm pollutant emission standard primary standard, and promptly COD, ammonia nitrogen, total nitrogen, total phosphorus are respectively less than 50mg/L, 8mg/L, 15mg/L, 0.5mg/L.Water outlet can enter sealing or semiclosed waters such as GB3838 surface water III class function waters, GB3097 seawater two class function waters He Hu, storehouse.Solved the sanitary sewage disposal problem in scattered settlement district.This Sewage treatment systems has following significant advantage: (1) sewage on-the-spot disposal, need not collect, and reduce capital cost; (2) treating processes does not have power consumption, need not special messenger's maintenance and keeps an eye on, and does not have working cost; (3) effluent quality is good, and conventional water-quality guideline reaches the B standard of GB 18918-2002 urban wastewater treatment firm pollutant emission standard primary standard; (4) not only COD, ammonia nitrogen, total phosphorus removal effect are good, and denitrification denitrogenation makes total nitrogen remove efficient to improve greatly; (5) underground water is not polluted.Native system can harvested vegetable when carrying out sewage disposal, beautifies living environment, and peasant household easily accepts popularization.
Four, description of drawings
Fig. 1 is a process flow sheet of the present invention;
Fig. 2 is the fine oxygen filtration channel drawing in side sectional elevation;
Fig. 3 is the fine oxygen filtration channel longitudinal diagram;
Fig. 4 is the plot plan of embodiment 1;
Fig. 5 is the plot plan of embodiment 3.
Five, embodiment
Further specify the present invention by the following examples
Embodiment 1
Certain peasant household an of family of five has built the four-part form domestic sewage processing system.The system design ability of disposing of sewage is 1 ton/day, service population 5 people.Total system is distributed in the house back, and sewage adopts from stream mode, and power need not be provided.All at first to enter volume be first section anaerobic pond of 1 cubic metre to sanitary sewages, and the COD of anaerobic pond water outlet, ammonia nitrogen, total nitrogen, total phosphorus concentration are respectively 95~250mg/L, 20~50mg/L, 31~62mg/L, 2~5mg/L.Anaerobic pond water outlet 80% enters second section fine oxygen filtration channel (fine oxygen filtration channel length is 5 meters, surface plantation wild rice stem), enters the 3rd section anoxic pond after treatment, and other 20% of anaerobic pond water outlet directly enters the 3rd section anoxic pond carbon source is provided.The 3rd section anoxic pond water outlet enters the 4th section artificial swamp (long 5 meters, wide 1 meter, wetland plant is a Wildcelery Herb).The 4th section wetland effluent COD, ammonia nitrogen, total nitrogen, total phosphorus concentration are respectively 23~30mg/L, 2.2~3.4mg/L, 3.0~5.5mg/L, 0.02~0.09mg/L, have reached GB18918-2002 urban wastewater treatment firm pollutant emission standard primary standard B standard.
The fine oxygen filtration channel gradient 1%, base plane is del, and being beneficial to the width that catchments is 1 meter, highly is 1 meter (not comprising frozen soil layer thickness), 5 meters of length, its load is 100 liters/Mi Tian.The fine oxygen filtration channel transverse section is made up of impervious barrier 1, layer of displacement (unsaturated zone of holding concurrently) 2, filter layer 3, cloth tank layer 4, greening layer 5 five part from lower to upper:
1) impervious barrier 1: be made of polyvinyl chloride film, be layered on the ground and the side of diafiltration ditch, its effect is to prevent that sewage is to both sides and underground leakage.
2) layer of displacement (hold concurrently ventilate to sudden and violent gas-bearing formation) 2: by diameter is that the gravel (cobble) of 20~40mm is formed.Water after the diafiltration ditch is handled flows into anoxic pond through water outlet pipeline (left side pipeline among the figure) in the stone hole.Air enters from the water outlet pipeline, through stone hole and water body reverse flow, discharges through the pipeline natural ventilation of vertical ground from the opposite side of diafiltration ditch.
3) filter layer 3: by 15~25% slags, 3~10% peat (or sawdust, rice husk) and the higher ventilation soil of local mixing with soil composition void ratio." sealing coat " established in filter layer and layer of displacement junction, is made of the non-woven fabrics 6 of porous, falls to filling out people's gravel bed to prevent upper layer of soil, destroys the normal draining of layer of displacement.
4) cloth tank layer 4: the cloth tank is located at how much middle parts of whole diafiltration ditch.Top opening, section takes the shape of the letter U.The water distribution well width is the 25-35% of diafiltration ditch width, dark 80~120mm.Fill out the gravel that diameter is 10~25mm in the cloth tank, the non-woven fabrics 6 and the upper layer of soil of cobble upper berth porous separate.After cesspool sewage enters the cloth tank, distribute, upwards gently be seeped in the soil on every side then through non-woven fabrics 6 in the gravel porous nickel.Cloth tank material adopts PVC.
5) the greening layer 5: plant wild rice stem, its effect is that absorbed nitrogen phosphorus, root system are secreted oxygen, beautified the environment.Greening laminar surface 10-20cm above ground level, and the centre is higher than the edge.
Embodiment 2
The four-part form domestic sewage processing system has been built for the engineering staff in certain construction site.Total system is distributed in next door, la vie ouvriere district, building site, and sewage adopts from stream mode, and power need not be provided.The system design service population is 30 people, and handling the water yield is 4 tons/day.All sanitary sewage at first enters first section anaerobic pond three-grid septic tank that volume is 4 sides (according to " the brick septic tank standard collective drawings of flat-top " of Jiangsu Province's engineering construction standard design station publication), and the COD of anaerobic pond water outlet, ammonia nitrogen, total nitrogen, total phosphorus concentration are respectively 120~290mg/L, 28~50mg/L, 35~56mg/L, 2.5~4.5mg/L.Anaerobic pond water outlet 85% enters second section fine oxygen filtration channel, and (fine oxygen filtration channel composes in parallel by 3 sections, 10 meters of every segment lengths, total length is 30 meters, there is the lawn on the surface), enter the 3rd section anoxic pond after treatment, other 15% of anaerobic pond water outlet directly enters the 3rd section anoxic pond.The 3rd section anoxic pond water outlet enters the 4th section artificial swamp (wetland is by long 10 meters, and wide 3 meters, wetland plant is a reed).COD, ammonia nitrogen, total nitrogen, total phosphorus concentration are respectively 25~32mg/L, 3.2~4.8mg/L, 5.0~7.8mg/L, 0.07~0.15mg/L in the 4th section wetland effluent, have reached GB 18918-2002 urban wastewater treatment firm pollutant emission standard primary standard B standard.
Embodiment 3
Certain resident house, four families thing is linked to be a row, and four family residents unite and built the four-part form domestic sewage processing system.The system design ability of disposing of sewage is 3 tons/day, service population 20 people.Total system is distributed in the courtyard of front, house, moves towards parallel with the house, and sewage is flow automatically by east westerly according to the gradient, need not power.This system had both administered sewage, had afforested garden again.The treatment system floor plan is seen Fig. 4.
First three family resident's water outlet is respectively through entering the fine oxygen filtration channel of their front, house after the pre-treatment of septic tank anaerobism, flow into the anoxic pond of front, house, the 4th family after the percolation treatment again, the 4th family resident's sewage without the diafiltration ditch, provides carbon source but directly enter anoxic pond for first three family fine oxygen filtration channel water outlet after pre-treatment.The anoxic pond water outlet enters artificial swamp.COD, ammonia nitrogen, total nitrogen, the total phosphorus mean concns of four family resident's anaerobic pond water outlets are respectively 180mg/L, 35.5mg/L, 47.3mg/L, 4.2mg/L.Water outlet COD, ammonia nitrogen, total nitrogen, total phosphorus mean concns are respectively 23mg/L, 1.2mg/L, 1.8mg/L, 0.12mg/L after the system handles.Not only reached GB 18918-2002 urban wastewater treatment firm pollutant emission standard primary standard B standard, " miscellaneous domestic water quality standard " that also reached promulgated by the ministries or commissions of the Central Government of nation-building (CJ25.1-89).
Embodiment 4
Essential structure is with embodiment 1, anaerobic pond water outlet 70% enters second section fine oxygen filtration channel, and (fine oxygen filtration channel length is 5 meters, surface plantation green vegetables), enter the 3rd section anoxic pond after treatment, other 30% of anaerobic pond water outlet directly enters the 3rd section anoxic pond carbon source is provided.The 3rd section anoxic pond water outlet enters the 4th section artificial swamp (long 5 meters, wide 1 meter, wetland plant is a Wildcelery Herb).The 4th section wetland effluent COD, ammonia nitrogen, total nitrogen, total phosphorus concentration are respectively 23~30mg/L, 2.2~3.4mg/L, 3.0~5.5mg/L, 0.02~0.09mg/L, have reached GB 18918-2002 urban wastewater treatment firm pollutant emission standard primary standard B standard.
The fine oxygen filtration channel gradient 0.5%, base plane is del, and being beneficial to the width that catchments is 1.2 meters, highly is 1.2 meters (not comprising frozen soil layer thickness), 6 meters of length, its load is 120 liters/Mi Tian.The fine oxygen filtration channel transverse section is made up of impervious barrier 1, layer of displacement (unsaturated zone of holding concurrently) 2, filter layer 3, cloth tank layer 4, greening layer 5 five part from lower to upper:
1) impervious barrier 1: be made of malthoid, be layered on the ground and the side of diafiltration ditch, its effect is to prevent that sewage is to both sides and underground leakage.
2) layer of displacement (hold concurrently ventilate to sudden and violent gas-bearing formation) 2: by diameter is that the gravel (cobble) of 20~40mm is formed.Water after the diafiltration ditch is handled flows into anoxic pond through water outlet pipeline (left side pipeline among the figure) in the stone hole.Air enters from the water outlet pipeline, through stone hole and water body reverse flow, discharges through the pipeline natural ventilation of vertical ground from the opposite side of diafiltration ditch.
3) filter layer 3: by 15~25% slags, 3~10% peat (or sawdust, rice husk) and the higher ventilation soil of local mixing with soil composition void ratio." sealing coat " established in filter layer and layer of displacement junction, is made of the non-woven fabrics 6 of porous, falls to filling out people's gravel bed to prevent upper layer of soil, destroys the normal draining of layer of displacement.
4) cloth tank layer 4: the cloth tank is located at how much middle parts of whole diafiltration ditch.Top opening, section takes the shape of the letter U.The water distribution well width is the 25-35% of diafiltration ditch width, dark 80~120mm.Fill out the gravel that diameter is 10~25mm in the cloth tank, the non-woven fabrics 6 and the upper layer of soil of cobble upper berth porous separate.After cesspool sewage enters the cloth tank, distribute, upwards gently be seeped in the soil on every side then through non-woven fabrics 6 in the gravel porous nickel.Cloth tank material adopts PVC.
5) greening layer: plant green vegetables, its effect is that absorbed nitrogen phosphorus, root system are secreted oxygen, beautified the environment.Greening laminar surface 10-20cm above ground level, and the centre is higher than the edge.
Embodiment 5
Essential structure is identical with embodiment 4 with setting, and just the design variable of fine oxygen filtration channel is different with it, the fine oxygen filtration channel gradient 2%, base plane is del, and being beneficial to the width that catchments is 0.8 meter, highly is 0.8 meter (not comprising frozen soil layer thickness), length is 7 meters, and its load is 70 liters/Mi Tian.The fine oxygen filtration channel transversal profile is made up of impervious barrier 1, layer of displacement (unsaturated zone of holding concurrently) 2, filter layer 3, cloth tank layer 4, greening layer 5 five part from lower to upper.

Claims (7)

1. four-segment type sewage treatment system for dispersed residences, comprise anaerobic pond and anoxic pond, it is characterized in that shunting after sanitary sewage is by anaerobic pond, a part enters anoxic pond by the processing of fine oxygen filtration channel, remaining directly enters anoxic pond, sewage after handling by anoxic pond enters current wetland, can directly enter water body by the water outlet of current wetland.
2. a kind of four-segment type sewage treatment system for dispersed residences according to claim 1 is characterized in that fine oxygen filtration channel is made up of impervious barrier, layer of displacement, filter layer, cloth tank layer, greening layer five part from lower to upper.
3. a kind of four-segment type sewage treatment system for dispersed residences according to claim 2, it is characterized in that it is characterized in that the gradient of fine oxygen filtration channel is 0.5~2%, base plane is del, the width that catchments is 0.8~1.2 meter, highly is 0.8~1.2 meter.
4. according to claim 2 or 3 described a kind of four-segment type sewage treatment system for dispersed residences, it is characterized in that cloth tank layer can be distributed in the centre of filter layer.
5. according to claim 1 or 2 or 3 described a kind of four-segment type sewage treatment system for dispersed residences, it is characterized in that the water outlet that is directly entered anoxic pond by anaerobic pond accounts for 10~30% of the total water outlet of anaerobic pond.
6. according to claim 1 or 2 or 3 described a kind of four-segment type sewage treatment system for dispersed residences, it is characterized in that anoxic pond top is concrete slab, leaves venting hole on the plate.
7. according to the described a kind of four-segment type sewage treatment system for dispersed residences of claim 1 to 3, it is characterized in that current wetland is made of impervious barrier, metalling, pedosphere, layer of plants four parts from down to up.
CNB2005100380976A 2005-03-11 2005-03-11 Four-segment type sewage treatment system for dispersed residences Expired - Fee Related CN1305780C (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101475284B (en) * 2008-12-24 2011-06-15 江苏百纳环境工程有限公司 Domestic sewage treatment process and apparatus
CN101439917B (en) * 2008-12-10 2011-08-10 中国矿业大学 Anaerobic adsorption dephosphorization and denitrification process
CN102398991A (en) * 2010-09-16 2012-04-04 天津城市建设学院 Undercurrent type garden filter tank sewage treatment system
CN103030247A (en) * 2011-10-09 2013-04-10 中国环境科学研究院 Method for treating sewage by organism-soil infiltration and device for realizing method
CN108640274A (en) * 2018-04-09 2018-10-12 中国航天员科研训练中心 A kind of waste water circulation utilized device of integrated plant culture

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BR0214176A (en) * 2001-11-14 2004-08-31 Dharma Living Systems Inc System and method for advanced tailings treatment and marketing method
CN1312056C (en) * 2003-09-04 2007-04-25 沈阳环境科学研究院 Polluted water ecological treatment composite process

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101439917B (en) * 2008-12-10 2011-08-10 中国矿业大学 Anaerobic adsorption dephosphorization and denitrification process
CN101475284B (en) * 2008-12-24 2011-06-15 江苏百纳环境工程有限公司 Domestic sewage treatment process and apparatus
CN102398991A (en) * 2010-09-16 2012-04-04 天津城市建设学院 Undercurrent type garden filter tank sewage treatment system
CN103030247A (en) * 2011-10-09 2013-04-10 中国环境科学研究院 Method for treating sewage by organism-soil infiltration and device for realizing method
CN103030247B (en) * 2011-10-09 2014-05-14 中国环境科学研究院 Method for treating sewage by organism-soil infiltration and device for realizing method
CN108640274A (en) * 2018-04-09 2018-10-12 中国航天员科研训练中心 A kind of waste water circulation utilized device of integrated plant culture

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