CN102020393B - Composite artificial wetland denitrifying and dephosphorizing device for surface flow-vertical underflow-two level surface flow - Google Patents
Composite artificial wetland denitrifying and dephosphorizing device for surface flow-vertical underflow-two level surface flow Download PDFInfo
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- CN102020393B CN102020393B CN2009101765349A CN200910176534A CN102020393B CN 102020393 B CN102020393 B CN 102020393B CN 2009101765349 A CN2009101765349 A CN 2009101765349A CN 200910176534 A CN200910176534 A CN 200910176534A CN 102020393 B CN102020393 B CN 102020393B
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Abstract
The invention relates to a composite artificial wetland denitrifying and dephosphorizing device for surface flow-vertical underflow-two level surface flow, which mainly comprises a plastic water distribution bucket, a peristaltic pump, a wetland unit (made of plastic and organic glass), a water inlet tube, a water outlet tube, a valve, stuffing filling and sampling columns and the like, wherein a water distribution device pumps distributed water into the wetland through the peristaltic pump; the outflow water is discharged into a municipal administration water drainage tube network through the water outlet tube; the wetland unit is filled with zeolite which has different grain diameters and thicknesses is used as an adsorption layer; pollutants move and transform under the action of the zeolite and microorganisms when the pollutants flow through a zeolite stuffing layer; the contents of carbon, nitrogen and phosphorus in the inflow water, the outflow water and the water of each processing unit are periodically detected; the stuffing filling and sampling columns are arranged in test grids so as to realize the layering sampling of stuffing, wherein each test grid can be provided with a plurality of sampling columns); and the absorption effect of the stuffing with different depths can be analyzed.
Description
Affiliated technical field
The present invention relates to a kind of surface current-vertical subsurface flow-two-stage surface current combined artificial wetland waste disposal plant, be used to study the removal effect of the composite constructed wetland system of filling different-grain diameter zeolite carbon, nitrogen and phosphorus.
Background technology
Artificial swamp can be divided into 2 types by sewage mobile mode difference in wetland bed: surface current artificial wetland (Surface FlowWetland; SFW) and drowned flow artificial wet land (Subsurface Flow Wetland; SSFW); Current wetland according to water (flow) direction be divided into vertical subsurface flow wetland (Vertical Flow Wetland, VFW) and horizontal drowned flow artificial wet land (Horezental Flow Wetland, HFW).With the drowned flow artificial wet land of homalographic the removal effect of pollutent is better than the surface current artificial wetland usually.Artificial swamp matrix can and provide effect such as attachment point to remove nitrogen, phosphorus in the sewage effectively through absorption for mikrobe.
Summary of the invention
The objective of the invention is: (1) makes full use of surface current-vertical subsurface flow-two-stage surface current combined artificial wetland and handles the major part removal of bed completion to oxygen consumption organic and suspended substance; (2) in artificial swamp, adopt the matrix of high nitrogen adsorptive power, to reach the clearance of higher nitrogen: its clearance situation to phosphorus is investigated in (3) when reaching the requiring of nitrogen removal efficiency.
Primary member of the present invention is filled sampling column by water dispensing apparatus, artificial swamp unit and filler and is formed.Water dispensing apparatus is made up of storage pencil, water distributing pipe, sewage preparation and storing unit, stirring rod and peristaltic pump, and former water gets into artificial swamp through peristaltic pump.Artificial swamp is by being made up of four unit, and artificial wetland effluent is discharged by water shoot, and overall draining is by bottom discharge management and control system.It is the right cylinder of glass reinforced plastic material that filler is filled sampling column; Upper opening, bottom and post jamb are beaten Φ 5mm aperture (evenly densely arranged), and sampling column is put into the test lattice before the test lattice are filled filler; Filler with test lattice filling the same terms; When the device run duration, then can extract sampling column out sampling to filler stratified sampling in the test lattice if need.Regularly collected specimens is analyzed the analysis of filling adsorption analytic properties, filler reproducing characteristic, microbiological property etc.
The beneficial effect of this practical patent of invention is; Can under static conditions, study the real-time absorption situation of zeolite to water pollutant; Characterize also can realize the stratified sampling of filler to the removal and the interdiction capability of nitrogen and phosphorus, can analyze the adsorption effect of different depths filler.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the present invention is further specified.
Fig. 1 is a setting drawing of the present invention.
1. storage pencils in the picture in picture, 2. water distributing pipe, 3. sewage preparation and storing unit; 4. stirring rod, 5. peristaltic pump 6. contains the thick 1~2cm small particle size zeolite layer unit one of 35cm; 7. contain the big particle diameter zeolite layer of 2 thick~4cm of 70cm unit two, 8. contain the big particle diameter zeolite layer of 2 thick~4cm of 35cm unit three, 9. contain the thick 1~2cm small particle size zeolite layer unit four of 35cm; 10. sampling apparatus, 11. water shoots.
Embodiment
In Fig. 1, the medicament of carbon containing, nitrogen and the phosphorus of accurate weighing is placed storage pencil (1), the water in the water distributing pipe (2) is introduced in clean the sewage preparation and storing unit (3); Stir with stirring rod (4); Water is drawn into through peristaltic pump (5) in the processing unit one of 1~2cm small particle size zeolite layer (6), and opening is arranged at (6) bottom, and current flow into the processing unit two of the big particle diameter zeolite layer of 2~4cm (7) from the bottom; Opening is arranged at the top; Current flow into the processing unit three of 2~4cm small particle size zeolite layer (8) from the top, and opening is arranged at the bottom of (8), and current flow into 1~2cm small particle size zeolite layer (9) processing unit four from this; Sampling apparatus (10) is used for carrying out in the filler collection with different layers regularly the analysis of filling adsorption analytic properties, filler reproducing characteristic, microbiological property etc.The water quality situation of each treatment unit of periodic monitoring and the correlation properties of filler and mikrobe.
Claims (3)
1. surface current-vertical subsurface flow-two-stage surface current combined artificial wetland denitrification dephosphorization apparatus, the wetland unit of making by plastics water distribution bucket (3), peristaltic pump (5), plastics and synthetic glass (6,7; 8,9) and water inlet pipe and water outlet pipe, valve form, it is characterized in that: be divided into four processing units; Unit one (6) is the zeolite of 2~4cm particle diameter with the matrix of unit four (9), and unit two (7) is the zeolite of 1~2cm particle diameter with unit three (8), unit one (6); Unit three (8) and unit four (9) are surface current, and unit two (7) is a vertical subsurface flow, adopt upstream and downstream alternate flow mode; It is the right cylinder of glass reinforced plastic material that filler is filled sampling column, and upper opening, bottom and post jamb are beaten Φ 5mm aperture; Densely arranged with evenly, sampling column is put into the test lattice before the test lattice are filled filler, with the filler of test lattice filling the same terms; When the device run duration, if need then extract sampling column out sampling to filler stratified sampling in the test lattice.
2. surface current-vertical subsurface flow according to claim 1-two-stage surface current combined artificial wetland denitrification dephosphorization apparatus; It is characterized in that: combined artificial wetland is handled bed bed height degree 100cm; The employing synthetic glass is a material; The zeolite layer height 35cm of unit one (6), unit three (8), unit four (9), the zeolite layer height of unit two (7) is 75cm.
3. surface current-vertical subsurface flow according to claim 1-two-stage surface current combined artificial wetland denitrification dephosphorization apparatus; It is characterized in that: former water gets into artificial swamp through peristaltic pump (5) water inlet back; Water outlet enters the municipal drainage pipe network through rising pipe, and is every at a distance from 10 days, stops into water 2 days; From the draining of bottom discharge pipe, let the oxygenation of filler nature regenerate.
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CN2009101765349A CN102020393B (en) | 2009-09-22 | 2009-09-22 | Composite artificial wetland denitrifying and dephosphorizing device for surface flow-vertical underflow-two level surface flow |
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CN2009101765349A CN102020393B (en) | 2009-09-22 | 2009-09-22 | Composite artificial wetland denitrifying and dephosphorizing device for surface flow-vertical underflow-two level surface flow |
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CN102020393A CN102020393A (en) | 2011-04-20 |
CN102020393B true CN102020393B (en) | 2012-04-18 |
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Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN103755032B (en) * | 2014-01-13 | 2015-12-30 | 东北师范大学 | Combined artificial marsh sewage treatment system |
CN103992011B (en) * | 2014-06-03 | 2015-05-13 | 上海市农业科学院 | Pollutant sedimentation promoting purifying device for farmland drain outlet |
CN109970204A (en) * | 2019-03-15 | 2019-07-05 | 生态环境部南京环境科学研究所 | A kind of artificial swamp-biomass power generation association system |
CN109835987B (en) * | 2019-03-28 | 2022-05-24 | 生态环境部南京环境科学研究所 | Surface flow-vertical subsurface flow constructed wetland treatment process |
CN110078299A (en) * | 2019-04-15 | 2019-08-02 | 河海大学 | A kind of artificial swamp sewage reutilization device and method |
CN111689653B (en) * | 2020-06-29 | 2022-11-04 | 中国科学院生态环境研究中心 | Biological-ecological integrated sewage treatment device and treatment method |
CN113415893B (en) * | 2021-06-28 | 2023-06-02 | 陕西地建土地工程技术研究院有限责任公司 | Multifunctional wetland simulation system and method for purifying polluted water body |
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US6277274B1 (en) * | 1999-04-16 | 2001-08-21 | Larry Steven Coffman | Method and apparatus for treating stormwater runoff |
CN1887747A (en) * | 2006-07-12 | 2007-01-03 | 浙江师范大学 | Sewage treating artificial wet land method |
CN201065357Y (en) * | 2007-06-08 | 2008-05-28 | 山东大学 | Vertical surface flow composite artificial wet land |
CN101381186A (en) * | 2008-10-23 | 2009-03-11 | 江苏省环境科学研究院 | Multi-stage ecological purification technique of drinking water resource |
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- 2009-09-22 CN CN2009101765349A patent/CN102020393B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6277274B1 (en) * | 1999-04-16 | 2001-08-21 | Larry Steven Coffman | Method and apparatus for treating stormwater runoff |
CN1887747A (en) * | 2006-07-12 | 2007-01-03 | 浙江师范大学 | Sewage treating artificial wet land method |
CN201065357Y (en) * | 2007-06-08 | 2008-05-28 | 山东大学 | Vertical surface flow composite artificial wet land |
CN101381186A (en) * | 2008-10-23 | 2009-03-11 | 江苏省环境科学研究院 | Multi-stage ecological purification technique of drinking water resource |
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