CN105859047A - Solar micro-power artificial wet land rural sewage treatment system and use method thereof - Google Patents

Solar micro-power artificial wet land rural sewage treatment system and use method thereof Download PDF

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Publication number
CN105859047A
CN105859047A CN201610370814.3A CN201610370814A CN105859047A CN 105859047 A CN105859047 A CN 105859047A CN 201610370814 A CN201610370814 A CN 201610370814A CN 105859047 A CN105859047 A CN 105859047A
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contact
sewage treatment
oxidation pool
sewage
treatment system
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CN201610370814.3A
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Chinese (zh)
Inventor
申太平
郝海杰
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Sichuan Lijie Environmental Engineering Co Ltd
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Sichuan Lijie Environmental Engineering Co Ltd
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Priority to CN201610370814.3A priority Critical patent/CN105859047A/en
Publication of CN105859047A publication Critical patent/CN105859047A/en
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/009Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/006Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/32Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • 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
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

The invention relates to a solar micro-power artificial wet land rural sewage treatment system and a use method thereof. The system comprises an artificial wet land, a sewage treatment device and a solar photovoltaic control system, wherein a water outlet is arranged at one side of the artificial wet land, dephosphorization plants are planted in a plant layer; the sewage treatment device is arranged under the artificial wet land and superposed with the area of the artificial wet land; and the solar photovoltaic control system is erected and distributed in a spotted state above the artificial wet land for driving the sewage treatment device to operate. The sewage treatment system adopts a three-dimensional layout, i.e. the sewage treatment device is buried under the artificial wet land, and the solar photovoltaic control system is erected and distributed in a spotted state above the artificial wet land, so that the floor area is saved as compared with other techniques. Dephosphorization plants are planted on the artificial wet land, so that while pollution factors such as COD, ammonia nitrogen and SS are well removed by the sewage treatment device, reduction of total phosphorus is ensured by virtue of the dephosphorization effect of the artificial wet land, the dephosphorization rate is above 60%, and the solar photovoltaic control system is adopted for supplying power for the sewage treatment device.

Description

Solar energy micro-power artificial wetland rural sewage treatment system and using method thereof
Technical field
The present invention relates to sewage treatment area, particularly relate to a kind of solar energy micro-power artificial wetland country sewage Processing system and using method thereof.
Background technology
There is operating cost height in rural sewage treatment, the water yield is little, water quality is complicated, distribution disperses, difficult management Feature.Traditional waste water treatment process needs the properly functioning of enough expense support meanss, and expense is in agriculture Village's sewage disposal often exists the problem put in place not in time;And present sewage disposal is to phosphorus ligands requirement Height, and existing sewage disposal technology phosphor-removing effect is by technogenic influence, how inapplicable rural sewage treatment pattern.
Summary of the invention
The invention provides a kind of solar energy micro-power artificial wetland rural sewage treatment system and technique thereof, with Solve above-mentioned technical problem.
In order to achieve the above object, the technical scheme is that and be achieved in that: a kind of solar energy micro power Artificial wetland rural sewage processing system, including: artificial swamp, artificial swamp is followed successively by plant from top to bottom Layer, sandy soils and gravel layer, the side of artificial swamp is provided with outlet, and layer of plants kind is implanted with dephosphorization plant; Sewage-treatment plant, is arranged at below artificial swamp, and the occupation of land with artificial swamp is overlapping, sewage-treatment plant Including the grid pond being sequentially connected with, the first contact-oxidation pool, anoxic pond, the second contact-oxidation pool, sedimentation tank; Grid Chi Chu is provided with water inlet;Lifting device it is provided with between sedimentation tank and artificial swamp;First contact oxygen Change in pond and the second contact-oxidation pool and be provided with aerating system;First contact-oxidation pool, anoxic pond and second Contact-oxidation pool is provided with biomembrane, containing the antibacterial removing BOD, ammonia nitrogen and total phosphorus etc. in biomembrane Bacterium colony;Solar photovoltaic control system, establishes in point-like and is distributed on artificial swamp, be used for driving at sewage The operating of reason device.
Further, the first contact-oxidation pool, anoxic pond and the second contact-oxidation pool are provided with filler, fill out Material is used for loading biomembrane, and filler includes floating type filler and mounted model filler.
Further, the first contact-oxidation pool, anoxic pond and the second contact-oxidation pool are provided with dissolved oxygen meter use In monitoring oxygen content.
Further, water inlet and water outlet are provided with effusion meter, for metering water inlet respectively and water outlet Capacity.
Further, during dephosphorization plant is Caulis Zizaniae caduciflorae, Canna generalis Bailey, cyperus alternifolius and Semen Coicis one or more Combination.
Further, water outlet is provided with pigeon-holed wall, is used for making water outlet uniform.
A kind of using method of above-mentioned solar energy micro-power artificial wetland rural sewage treatment system, including with Lower step:
(1) total Water is that after the sewage of Q crosses grid pond, the sewage of 0.5Q flows directly into the first catalytic oxidation Pond, the sewage of 0.5Q flows directly into anoxic pond;
(2) flow into the sewage of the first contact-oxidation pool to flow into behind 4~the adsorption and oxidation effect of 6 hours and lack Oxygen pond;
(3) sewage flowing into anoxic pond flows into the second catalytic oxidation behind 4~the Denitrification of 6 hours Chi Zhong, flows into the water in the second contact-oxidation pool by after the adsorption and oxidation effect of 6~10 hours 0.8Q~2Q is back in anoxic pond, and remainder flows into sedimentation tank;
(4) flowing into the sewage of sedimentation tank through 4~the precipitation of 6 hours, the mud after precipitation is pressed from sedimentation tank 0.2Q~1.0Q is back to the first contact-oxidation pool, and the upper strata filtrate after precipitation is pumped into manually by lifting device Wetland;
(5) filtrate flowing into artificial swamp is discharged after the dephosphorization function of artificial swamp.
Further, in step (1), the organic loading of the first contact-oxidation pool is 0.3~1.0kgBOD/ (m3 d), gas-water ratio is 2~4:1, and dissolved oxygen content is 2~3mg/L.
Further, in step (2), the organic loading of anoxic pond is 0.1~0.5kgNOx-N/(m3D), Dissolved oxygen content 0.2~0.5mg/L.
Further, in step (3), the organic loading of the second contact-oxidation pool is 0.05~0.3kgBOD/ (m3 d), gas-water ratio is 4~6:1, and dissolved oxygen content is 2~4mg/L.
Compared with prior art, it is an advantage of the current invention that: solar energy micro-power artificial wetland rural area of the present invention Sewage disposal system uses stereoscopic arrangement: is used by sewage-treatment plant and buried is arranged on below artificial swamp, Earth's surface is artificial swamp, does landscape style design, and solar photovoltaic control system is that point-like setting is distributed in artificial Wetland, compares other techniques and saves floor occupying area;Planting dephosphorization plant in artificial swamp, sewage disposal fills Putting and connected by lifting device between artificial swamp, the present invention well removes at use sewage-treatment plant While the pollution factors such as COD, ammonia nitrogen, SS, ensured the abatement of total phosphorus by the dephosphorization function of artificial swamp, Dephosphorizing rate reaches more than 60%, uses solar photovoltaic control system to provide the energy for sewage-treatment plant, adopts Use distinctive technique, decrease the energy consumption that equipment runs, be significantly reduced process operation expense.
Accompanying drawing explanation
In order to be illustrated more clearly that the specific embodiment of the invention or technical scheme of the prior art, below will The accompanying drawing used required in detailed description of the invention or description of the prior art is briefly described, it is clear that Ground, the accompanying drawing in describing below is some embodiments of the present invention, comes for those of ordinary skill in the art Say, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the structural representation of the embodiment of the present invention.
In figure: 1, artificial swamp;11, layer of plants;12, sandy soils;13, gravel layer;2, dirty Water treatment facilities;21, grid pond;22, the first contact-oxidation pool;23, anoxic pond;24, the second contact Oxidation pond;25, sedimentation tank;3, solar photovoltaic control system;4, water inlet;5, outlet;6、 Pigeon-holed wall;7, lifting device.
Detailed description of the invention
Below with reference to accompanying drawing, the technical scheme of various embodiments of the present invention is carried out clear, complete description, aobvious So, described embodiment is only a part of embodiment of the present invention rather than whole embodiments.Base Embodiment in the present invention, those of ordinary skill in the art are institute on the premise of not making creative work The all other embodiments obtained, broadly fall into the scope that the present invention is protected.
Below by specific embodiment and combine accompanying drawing the present invention is described in further detail.
The present invention relates to a kind of solar energy micro-power artificial wetland 1 rural sewage treatment system, including: artificial Wetland 1, artificial swamp 1 is followed successively by layer of plants 11, sandy soils 12 and gravel layer 13, manually from top to bottom The side of wetland 1 is provided with outlet 5, and layer of plants 11 kinds is implanted with dephosphorization plant;Sewage-treatment plant 2, Being arranged at below artificial swamp 1, the occupation of land with artificial swamp 1 is overlapping, and sewage-treatment plant 2 includes successively Grid pond 21, first contact-oxidation pool 22 of connection, anoxic pond the 23, second contact-oxidation pool 24, precipitation Pond 25;Grid Chi21Chu is provided with water inlet 4;It is provided with lifting between sedimentation tank 25 and artificial swamp 1 Device 7;First contact-oxidation pool 22 and the second contact-oxidation pool 24 are provided with aerating system;First Contact-oxidation pool 22 and the second contact-oxidation pool 24 are provided with biomembrane;Anoxic pond 23 is provided with life Thing film;Containing the bacterial clump removing BOD, ammonia nitrogen and total phosphorus etc. in biomembrane;Photovoltaic controls system System 3, establishes in point-like and is distributed on artificial swamp 1, for driving the operating of sewage-treatment plant 2.
Solar energy micro-power artificial wetland 1 rural sewage treatment system of the present invention uses stereoscopic arrangement: by sewage Processing means 2 uses and buried is arranged on below artificial swamp 1, and earth's surface is artificial swamp 1, does landscape style Design, solar photovoltaic control system 3 is erect in point-like and is distributed in artificial swamp 1, compares other technique joint About floor space;In artificial swamp 1, plant dephosphorization plant, sewage-treatment plant 2 and artificial swamp 1 it Between connected by lifting device 7, the present invention use sewage-treatment plant 2 well remove COD, ammonia nitrogen, While the pollution factors such as SS, being ensured the abatement of total phosphorus by the dephosphorization function of artificial swamp 1, dephosphorizing rate reaches To more than 60%, use solar photovoltaic control system 3 to provide the energy for sewage-treatment plant 2, use spy Some technique, decreases the energy consumption that equipment runs, is significantly reduced process operation expense.Micro-on biomembrane Biological bacterium colony, the other biological such as including antibacterial, fungus, prokaryote, obtain biomembrane under aerobic condition main Removing COD, ammonia nitrogen (Nitrification) etc. by adsorption and oxidation, the biomembrane of anoxic pond mainly adapts to lack The biology of oxygen condition, carries out denitrification process, removes total nitrogen.
Enter the sewage of sewage-treatment plant 2, after grid pond 21 obtains filtration, flow into first and connect Touch in oxidation pond 22, flow in anoxic pond 23 after the adsorption and oxidation effect of the first contact-oxidation pool 22, The second contact-oxidation pool 24 is flowed into, through the second contact-oxidation pool after the Denitrification of anoxic pond 23 Flowing into after the adsorption and oxidation effect of 24 in sedimentation tank 25, the filtrate after sedimentation tank 25 precipitates is filled by lifting Putting 7 entrance artificial swamps 1, filtrate is finally discharged after the dephosphorization function of artificial swamp 1, is completed once The process of sewage.
Preferably, the first contact-oxidation pool 22, anoxic pond 23 and the second contact-oxidation pool 24 are provided with fill out Material, filler is loaded with biomembrane, and filler includes floating type filler and mounted model filler.
Floating type filler is the spherical high density polyethylene (HDPE) with porous, and biomembrane is supported in hole;Mounted model Filler by cradle hangs in the first contact-oxidation pool 22, anoxic pond 23 and the second contact-oxidation pool 24, Mounted model filler is polyethylene and polypropylene, and mounted model filler is loaded with hydroformylation silk fiber material, biomembrane It is supported on fibrous material.
Preferably, the first contact-oxidation pool 22, anoxic pond 23 and the second contact-oxidation pool 24 are provided with molten Oxygen instrument is used for monitoring oxygen content.
Arrange dissolved oxygen meter to monitor in the first contact-oxidation pool 22, anoxic pond 23 and the second contact-oxidation pool 24 Oxygen content, makes the adsorption and oxidation effect in the first contact-oxidation pool 22 and the second contact-oxidation pool 24 and lacks Denitrification in oxygen pond 23 is normally carried out, in order to preferably go out the Organic substance in decontaminated water.
Preferably, at water inlet 4 and outlet 5, it is provided with effusion meter, for metering water inlet and water outlet respectively Capacity.
Preferably, one or more the group during dephosphorization plant is Caulis Zizaniae caduciflorae, Canna generalis Bailey, cyperus alternifolius and Semen Coicis Close.
Preferably, at outlet 5, it is provided with pigeon-holed wall 6, is used for making water outlet uniform.
A kind of using method of above-mentioned solar energy micro-power artificial wetland 1 rural sewage treatment system, including Following steps:
(1) total Water is that after the sewage of Q crosses grid pond 21, the sewage of 0.5Q flows directly into the first contact oxygen Changing pond 22, the sewage of 0.5Q flows directly into anoxic pond 23;
(2) flow into the sewage of the first contact-oxidation pool 22 to flow behind 4~the adsorption and oxidation effect of 6 hours Enter anoxic pond 23;
(3) sewage flowing into anoxic pond 23 flows into the second contact behind 4~the Denitrification of 6 hours In oxidation pond 24, the water flowed in the second contact-oxidation pool 24 is made by the adsorption and oxidation through 6~10 hours Being back in anoxic pond 23 with rear 0.8Q~2Q, remainder flows into sedimentation tank 25;
(4) flowing into the sewage of sedimentation tank 25 through 4~the precipitation of 6 hours, the mud after precipitation is from sedimentation tank 25 are back to the first contact-oxidation pool 22 by 0.2Q~1.0Q, and the upper strata filtrate after precipitation passes through lifting device 7 Pump into artificial swamp 1;
(5) filtrate flowing into artificial swamp 1 is discharged after the dephosphorization function of artificial swamp 1.
Preferably, in step (1), the organic loading of the first contact-oxidation pool 22 is 0.3~1.0kgBOD/ (m3 d), gas-water ratio is 2~4:1, and dissolved oxygen content is 2~3mg/L.
Preferably, in step (2), the organic loading of anoxic pond 23 is 0.1~0.5kgNOx-N/(m3D), Dissolved oxygen content is less than 0.5mg/L.
Preferably, in step (3), the organic loading of the second contact-oxidation pool 24 is 0.05~0.3kgBOD/ (m3 d), gas-water ratio is 4~6:1, and dissolved oxygen content is 2~4mg/L.
Show through substantial amounts of experiment, according to the method that operates above to run solar energy micro-power artificial of the present invention Wetland 1 rural sewage treatment system, while well removing the pollution factors such as COD, ammonia nitrogen, SS, phosphorus, Decrease the energy consumption that equipment runs, be significantly reduced process operation expense.
The above, be only presently preferred embodiments of the present invention, not makees the present invention any pro forma Limit, any those skilled in the art, in the range of without departing from technical solution of the present invention, when can profit Make a little change with the technology contents of the disclosure above or be modified to the Equivalent embodiments of equivalent variations, as long as being Without departing from the content of technical solution of the present invention, according to appointing that above example is made by the technical spirit of the present invention What simple modification, equivalent variations and modification, all still fall within the range of technical solution of the present invention.

Claims (10)

1. a solar energy micro-power artificial wetland rural sewage treatment system, it is characterised in that including:
Artificial swamp, described artificial swamp is followed successively by layer of plants, sandy soils and gravel layer from top to bottom, described The side of artificial swamp is provided with outlet, and described layer of plants kind is implanted with dephosphorization plant;
Sewage-treatment plant, is arranged at below described artificial swamp, and the occupation of land with described artificial swamp is overlapping, Described sewage-treatment plant includes the grid pond being sequentially connected with, the first contact-oxidation pool, anoxic pond, second connects Touch oxidation pond, sedimentation tank;Described grid Chi Chu is provided with water inlet;Described sedimentation tank and described artificial swamp Between be provided with lifting device;Described first contact-oxidation pool and described second contact-oxidation pool are provided with Aerating system;Described first contact-oxidation pool, anoxic pond and described second contact-oxidation pool are provided with life Thing film, containing the bacterial clump removing BOD, ammonia nitrogen and total phosphorus etc. in described biomembrane;
Solar photovoltaic control system, establishes in point-like and is distributed on described artificial swamp, is used for driving described The operating of sewage-treatment plant.
2. solar energy micro-power artificial wetland rural sewage treatment system as claimed in claim 1, its feature It is: described first contact-oxidation pool, described anoxic pond and described second contact-oxidation pool are provided with filler, Described filler is used for loading described biomembrane, and described filler includes floating type filler and mounted model filler.
3. solar energy micro-power artificial wetland rural sewage treatment system as claimed in claim 1, its feature It is: described first contact-oxidation pool, described anoxic pond and described second contact-oxidation pool are provided with dissolved oxygen Instrument is used for monitoring oxygen content.
4. solar energy micro-power artificial wetland rural sewage treatment system as claimed in claim 1, its feature It is: described water inlet and described water outlet are provided with effusion meter, for metering water inlet respectively and water outlet Capacity.
5. solar energy micro-power artificial wetland rural sewage treatment system as claimed in claim 1, its feature It is: described dephosphorization plant is one or more the combination in Caulis Zizaniae caduciflorae, Canna generalis Bailey, cyperus alternifolius and Semen Coicis.
6. solar energy micro-power artificial wetland rural sewage treatment system as claimed in claim 1, its feature It is: described water outlet is provided with pigeon-holed wall, is used for making water outlet uniform.
7. the solar energy micro-power artificial wetland rural sewage treatment system as described in claim 1~6 Using method, it is characterised in that comprise the following steps:
(1) total Water is that after the sewage of Q crosses grid pond, the sewage of 0.5Q flows directly into the first catalytic oxidation Pond, the sewage of 0.5Q flows directly into anoxic pond;
(2) flow into the sewage of the first contact-oxidation pool to flow into behind 4~the adsorption and oxidation effect of 6 hours and lack Oxygen pond;
(3) sewage flowing into anoxic pond flows into the second catalytic oxidation behind 4~the Denitrification of 6 hours Chi Zhong, flows into the water in the second contact-oxidation pool by after the adsorption and oxidation effect of 6~10 hours 0.8Q~2Q is back in anoxic pond, and remainder flows into sedimentation tank;
(4) flowing into the sewage of sedimentation tank through 4~the precipitation of 6 hours, the mud after precipitation is pressed from sedimentation tank 0.2Q~1.0Q is back to the first contact-oxidation pool, and the upper strata filtrate after precipitation is pumped into manually by lifting device Wetland;
(5) filtrate flowing into artificial swamp is discharged after the dephosphorization function of artificial swamp.
8. the user of solar energy micro-power artificial wetland rural sewage treatment system as claimed in claim 7 Method, it is characterised in that: in step (1), the organic loading of described first contact-oxidation pool is 0.3~1.0kgBOD/ (m3 d), gas-water ratio is 2~4:1, and dissolved oxygen content is 2~3mg/L.
9. the user of solar energy micro-power artificial wetland rural sewage treatment system as claimed in claim 7 Method, it is characterised in that: in step (2), the organic loading of described anoxic pond is 0.1~0.5kgNOx-N/(m3D), dissolved oxygen content 0.2~0.5mg/L.
10. the use of solar energy micro-power artificial wetland rural sewage treatment system as claimed in claim 7 Method, it is characterised in that: in step (3), the organic loading of described second contact-oxidation pool is 0.05~0.3kgBOD/ (m3 d), gas-water ratio is 4~6:1, and dissolved oxygen content is 2~4mg/L.
CN201610370814.3A 2016-05-30 2016-05-30 Solar micro-power artificial wet land rural sewage treatment system and use method thereof Pending CN105859047A (en)

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CN106745755A (en) * 2017-03-24 2017-05-31 云南中贸环境节能科技投资股份有限公司 A kind of solar energy microkinetic Intelligent life sewage disposal system and sewage water treatment method
WO2018129895A1 (en) * 2017-01-16 2018-07-19 深圳市碧园环保技术有限公司 Treatment system for rural domestic sewage
CN109111050A (en) * 2018-09-29 2019-01-01 湖南新九方科技有限公司 Solar energy microkinetic rural sewage treatment system
CN109111052A (en) * 2018-09-30 2019-01-01 湖南新九方科技有限公司 The polynary rural sewage treatment system of landscape
CN111392967A (en) * 2020-03-25 2020-07-10 上海城投瀛洲生活垃圾处置有限公司 Sewage treatment system of garbage disposal station

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CN204039208U (en) * 2014-04-17 2014-12-24 陈海军 A kind of Sewage treatment systems utilizing sun power and wind energy
CN205821101U (en) * 2016-05-30 2016-12-21 四川利洁环境工程有限公司 Solar energy micro-power artificial wetland rural sewage treatment system

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CN103183410A (en) * 2012-01-01 2013-07-03 周平 Solar aerobiotic/anoxic/aerobiotic biological film lake water body treatment device
CN202482178U (en) * 2012-03-21 2012-10-10 杭州金鸣环境科技有限公司 Solar driven ecological sewage treatment system
CN103241904A (en) * 2013-05-24 2013-08-14 郑州大学 Multi-point water inlet aeration anoxic-aerobic high-efficient nitrogen and phosphorus removal method
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Publication number Priority date Publication date Assignee Title
WO2018129895A1 (en) * 2017-01-16 2018-07-19 深圳市碧园环保技术有限公司 Treatment system for rural domestic sewage
CN106745755A (en) * 2017-03-24 2017-05-31 云南中贸环境节能科技投资股份有限公司 A kind of solar energy microkinetic Intelligent life sewage disposal system and sewage water treatment method
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CN109111052A (en) * 2018-09-30 2019-01-01 湖南新九方科技有限公司 The polynary rural sewage treatment system of landscape
CN111392967A (en) * 2020-03-25 2020-07-10 上海城投瀛洲生活垃圾处置有限公司 Sewage treatment system of garbage disposal station

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