CN108585177A - The perpendicular stream reinforcing formula biological water purification device of one kind and process for purifying water - Google Patents
The perpendicular stream reinforcing formula biological water purification device of one kind and process for purifying water Download PDFInfo
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- CN108585177A CN108585177A CN201810589336.4A CN201810589336A CN108585177A CN 108585177 A CN108585177 A CN 108585177A CN 201810589336 A CN201810589336 A CN 201810589336A CN 108585177 A CN108585177 A CN 108585177A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 165
- 238000000746 purification Methods 0.000 title claims abstract description 111
- 230000003014 reinforcing effect Effects 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims description 15
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 21
- 239000010865 sewage Substances 0.000 claims description 20
- 239000000463 material Substances 0.000 claims description 17
- 239000005995 Aluminium silicate Substances 0.000 claims description 16
- 235000012211 aluminium silicate Nutrition 0.000 claims description 16
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 16
- 239000002245 particle Substances 0.000 claims description 16
- 238000000576 coating method Methods 0.000 claims description 11
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- 238000011049 filling Methods 0.000 claims description 8
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- 238000003306 harvesting Methods 0.000 claims description 6
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- 239000011449 brick Substances 0.000 claims description 5
- 239000008187 granular material Substances 0.000 claims description 5
- 238000007789 sealing Methods 0.000 claims description 5
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- 229920002994 synthetic fiber Polymers 0.000 claims description 5
- 229910001018 Cast iron Inorganic materials 0.000 claims description 4
- 239000012528 membrane Substances 0.000 claims description 4
- 230000005484 gravity Effects 0.000 claims description 3
- 230000008635 plant growth Effects 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 235000020681 well water Nutrition 0.000 claims description 3
- 239000002349 well water Substances 0.000 claims description 3
- 239000012736 aqueous medium Substances 0.000 claims description 2
- 229920003023 plastic Polymers 0.000 claims description 2
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- 238000005276 aerator Methods 0.000 description 11
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- 238000005516 engineering process Methods 0.000 description 7
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- 229920001155 polypropylene Polymers 0.000 description 6
- 239000004800 polyvinyl chloride Substances 0.000 description 6
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- 239000007789 gas Substances 0.000 description 5
- -1 polypropylene Polymers 0.000 description 5
- 239000004698 Polyethylene Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 229920000573 polyethylene Polymers 0.000 description 4
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- 239000000706 filtrate Substances 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 244000001632 Acorus gramineus Species 0.000 description 2
- 235000013073 Acorus gramineus Nutrition 0.000 description 2
- 235000005273 Canna coccinea Nutrition 0.000 description 2
- 240000008555 Canna flaccida Species 0.000 description 2
- 241000721690 Lythrum salicaria Species 0.000 description 2
- 244000246386 Mentha pulegium Species 0.000 description 2
- 235000016257 Mentha pulegium Nutrition 0.000 description 2
- 235000004357 Mentha x piperita Nutrition 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- 235000014676 Phragmites communis Nutrition 0.000 description 2
- 241000746966 Zizania Species 0.000 description 2
- 235000002636 Zizania aquatica Nutrition 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 235000001050 hortel pimenta Nutrition 0.000 description 2
- 230000002906 microbiologic effect Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 244000205574 Acorus calamus Species 0.000 description 1
- 235000000318 Bindesalat Nutrition 0.000 description 1
- 244000106835 Bindesalat Species 0.000 description 1
- 235000011996 Calamus deerratus Nutrition 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 240000008436 Ipomoea aquatica Species 0.000 description 1
- 235000019004 Ipomoea aquatica Nutrition 0.000 description 1
- 241001633663 Iris pseudacorus Species 0.000 description 1
- KRALSLMQBUXNAP-UHFFFAOYSA-N ON=O.ON=O.ON=O.ON=O.ON=O.ON=O.N.N Chemical compound ON=O.ON=O.ON=O.ON=O.ON=O.ON=O.N.N KRALSLMQBUXNAP-UHFFFAOYSA-N 0.000 description 1
- 240000008881 Oenanthe javanica Species 0.000 description 1
- 235000000365 Oenanthe javanica Nutrition 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
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- 238000003487 electrochemical reaction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910001448 ferrous ion Inorganic materials 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000007954 hypoxia Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/32—Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/005—Combined electrochemical biological processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/302—Nitrification and denitrification treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/308—Biological phosphorus removal
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/02—Fluid flow conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/02—Odour removal or prevention of malodour
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Water Supply & Treatment (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Botany (AREA)
- Biotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The present invention proposes a kind of perpendicular stream reinforcing formula biological water purification device, including:Pond body, up-flow well, drop stream well and recycle stream water purification medium;Wherein, pond body both sides are respectively arranged with inlet and outlet;Recycle stream water purification medium is laid in pond body;Up-flow well and drop stream well setting are connected in recycle stream water purification medium, and by advection pipe;Up-flow well and drop stream well are equipped with through-hole;It flows up and is equipped with aeration plate in well, biofilm carrier filler is equipped in drop stream well.The present invention is strengthened by flowing up the perpendicular stream of well and drop stream well, is improved the cycle and mass transfer condition of recycle stream water purification medium, is effectively reduced blocking and short flow problem, saves and take up an area;And by comprehensive functions such as watercourse aeration, microbial degradation, medium adsorption filtrations, greatly improve the bearing load and purifying property of device.The advantages that present invention, which has to save, takes up an area, energy-efficient, easy maintenance, good purification, comprehensive income is high.
Description
Technical field
The present invention relates to biological water purification fields, more particularly to a kind of perpendicular stream reinforcing formula biological water purification device and process for purifying water.
Background technology
Biological water purification technology is currently used non-point source pollution control technology, have the unique hydrology, physics, chemistry,
The characteristics such as biology can not only form distinctive biocoene habitat, be provided simultaneously with filtering, sedimentation, remove external source pollution
Ability.In recent years, biological water purification technology derives various devices, technique simple, small investment, quick advantage in its method
It is developed rapidly.
Artificial swamp is Typical Representative therein.Artificial wetland process is broadly divided into two type of surface low formula and undercurrent type
Type.The water level of surface low formula artificial swamp is shallower (being generally no greater than 60cm), relies primarily on the absorption purification of wetland plant
Sewage.In relation to studies have shown that surface low formula artificial swamp is because of the simple absorption for relying on plant, clean-up effect is extremely limited,
And organic nitrogen phosphorus can be released into water body again by Litter with the degradation of microorganism.
The water level of underflow type artificial wet land is relatively deep (generally more than 60cm), does not only rely on the absorption of plant, and
By the filtering of filtrate, suction-operated and be attached to filter material surface microbiological deterioration realize sewage purification, to have
It is standby to compare surface low formula artificial wet land system more preferably purifying property.But traditional underflow type artificial wet land is in actual operation still
In the presence of take up a large area, water reoxygenation is poor, short stream, easily stifled etc. knotty problems.
Underflow type artificial wet land system fights for valuable land resource because taking up a large area, with agricultural land.Therefore logical
The purification efficiency for improving unit area wetland is crossed to save its occupation of land, becomes the important side of biological water purification technology and process modification
To.
Because water level is deeper, filtrate gas permeability after longtime running biofilm weakens underflow type artificial wet land system, causes reoxygenation
Scarce capacity, this becomes common recognition already.When water hypoxia, the aerobic decomposition of nitrification and organic matter of microorganism will be by
Inhibit, therefore there is an urgent need for the dissolved oxygen levels of underflow type artificial wet land water body are promoted using cost-effective mode.
Short stream is that it's showing for water time shortening pasts to underflow type artificial wet land the sewage caused by unsmooth flowing in actual operation
As.The shortening of water time is crossed so that wet land system cannot achieve the complete nitrification of ammonia nitrogen, and then limit the further anti-nitre of nitrogen
Change so that the total nitrogen of water body can not be up to standard after processing.In addition, the suspension particulate matter (SS) in sewage easily blocks wetland filter
Material, causes to stop.Therefore the short stream of underflow type artificial wet land and blockage problem are urgently to be resolved hurrily.
In addition, if the plant of underflow type artificial wet land cannot clear up in time after decaying, the cauline leaf and root system of plant will be rotten
It is rotten, organic pollution materials are released, the organic loading of wet land system is further exacerbated by.Therefore the load carrying of wet land system is improved
Power is also a kind of actual needs.
In order to make up traditional underflow type artificial wet land reoxygenation it is poor, easily block, easily it is short stream, the serious deficiency of secondary pollution, this
Invention proposes a kind of novel biological water purification device.
Invention content
To achieve the purpose of the present invention, the present invention proposes a kind of perpendicular stream reinforcing formula biological water purification device, including:Up-flow
Well, drop stream well, advection pipe and recycle stream water purification medium.
In perpendicular stream reinforcing formula biological water purification device proposed by the present invention, the up-flow well and drop stream well are vertically provided at described
In recycle stream water purification medium;The advection pipe is set between up-flow well top and the tops drop Liu Jing, and the two is connected to;The liter
Stream underground portion and drop stream underground portion are equipped with several through-holes;It is equipped with aeration plate in the up-flow well, is set in the drop stream well
There is biofilm carrier filler;The recycle stream water purification medium is laid on the up-flow well and drops the outside of stream well, between dielectric layer
Lay non-woven fabrics;The recycle stream water purification medium top surface can plant wetland plant.
Preferably, the laying height of recycle stream water purification medium exceeds the perpendicular stream reinforcing formula biological water purification device normal water level
5~10cm of line;
Preferably, the shape of up-flow well and drop stream well is cylinder, is made of reinforcing bar concrete placings or the modes such as brick;
Preferably, a diameter of 5~20cm of well is flowed up, the recycle stream water purification medium 10~20cm of top surface is highly exceeded;
Preferably, a diameter of 15~50cm of drop stream well, highly exceeds the recycle stream water purification medium 10~20cm of top surface.
Aeration plate in the up-flow well uses diaphragm microporous aeration disc, is supplied by the air blower being set on wetland ground
Gas, aeration disk diameter are slightly less than the diameter of up-flow well;
Preferably, the carrier filler in drop stream well uses artificial synthetic fiber or plastics, such as:Polyethylene (PE), polypropylene
(PP), reinforced polypropylene (RPP), chliorinated polyvinyl chloride (CPVC) and poly- inclined alkene (PVDF) etc. are made, the filling rate of carrier filler
It is 65%~95%.
The lower part of the up-flow well and drop stream well is equipped with several through-holes, and through-hole diameter is 1~3cm, and quantity is 10~
It 50, is uniformly distributed within the scope of 5~50cm of shaft bottom or more.
Preferably, advection pipe is set between up-flow well top and the tops drop Liu Jing, and the up-flow well and drop stream well are connected
It is logical;
Preferably, the setting height of advection pipe is flushed with the recycle stream water purification medium top surface;
Preferably, advection pipe uses cast iron or PVC material, a diameter of 5~15cm, tube wall sealing.
The recycle stream water purification medium is laid on the outside of the up-flow well and drop stream well, is from top to bottom followed successively by coarse sand
Layer, haydite layer, iron carbon-coating, sintering kaolin particle layer, lay non-woven fabrics between filter material layer between filter material layer;
Preferably, the laying depth of coarse sands layer is 10~30cm, and coarse sand grain size is 0.5~1mm;
Preferably, the laying depth of haydite layer is 20~40cm, and haydite grain size is 5~10mm;
Preferably, the laying depth of iron carbon-coating is 30~50cm, and iron carbon granules diameter is 8~12mm;
Preferably, the laying depth of sintering kaolin particle layer is 40~60cm, and the grain size for being sintered kaolin particle is 40
~80mm.
The coarse sands layer top surface can plant the emergent aquactic plants such as canna, calamus, reed, iris, be 5~20cm childrens when plantation
Seedling, spring plantation, winter harvesting.
Based on purifier, the present invention proposes a kind of perpendicular stream reinforcing formula biological water purification method, including following step simultaneously
Suddenly:
Step 1:Sewage is flow to from water inlet in pond body;
Step 2:Sewage first flows through the root system of plant planted in recycle stream water purification medium top surface, then in gravity
Under flow through multilayer water purification medium from top to bottom;
Step 3:Sewage reaches near up-flow well lower through-hole, is inhaled into via the suction function of up-flow well water lift, and according to
It is promoted to advection pipe by stripping effect, is then transported to drop stream well;Sewage flows through the carrier filler inside drop stream well, therein
Polluter is to be removed by the biological membrane degradation on carrier filler;It is net that the through-hole that last sewage flows underground portion from drop flows back to recycle stream
During water is situated between;
Step 4:Water body the pushing away in wetland entirety flow with purification is repeatedly recycled through recycle stream water purification medium and drop stream well
Wetland effluent mouth is flowed under stream effect and is discharged;
Step 5:It is gathered in after the mature plant growth;
Step 6:After harvesting, the plant is planted again in recycle stream water purification Jie top surface.
Innovation and gain effect of the present invention compared with existing the relevant technologies be:
1. the present invention introduces up-flow well and drop stream well in underflow type artificial wet land, enhances the vertical of water body in wetland and follow
Ring, laterally exchange and vertical filtration compensate for undercurrent type people so as to improve the hydraulics and mass transfer characteristic of wet land system
The shortcomings that work wetland water body cycle exchanges deficiency, easily short stream;
2. the aeration facility of up-flow well improves the dissolved oxygen of water body in wet land system, be conducive to aerobic degradation water body
In organic matter and ammonia nitrogen (nitrification), prevent black and odorous water, to while improving purifying property improvement wet land system ring
Border condition and landscape effect;
3. drop stream well have the function of enriched microorganism, and the biomembrane formed on carrier filler have it is " aerobic-simultaneous
The microenvironment of oxygen-anaerobism ", to realize more work(of the microorganism to organic matter, ammonia nitrogen, nitrate nitrogen, sulfide, phosphate etc. in sewage
Energy, high-efficient purification;
4. the vertical cycle of water body is exchanged with lateral in recycle stream water purification medium couples wetland, the contact area with water body
With vertical filtration be improved significantly, filtering, absorption, ion exchange and the electrochemical reaction efficiency of filtrate are substantially promoted
Into;
5. introducing iron carbon material in recycle stream water purification medium, the denitrogenation (nitre of water body is enhanced by electro-catalysis reduction
State nitrogen and nitrite nitrogen nitrogen are reduced to nitrogen) and dephosphorization (dissolubility orthophosphates forms insoluble with ferrous ion and hydroxyl
Complex compound) effect, so as to improve the denitrogenation dephosphorizing performance of traditional biological purifier;
6. the setting for flowing up well and drop stream well in recycle stream water purification medium increases wetland while strengthened purification performance
The dischargeable capacity of system to have the bearing load of bigger compared with underflow type artificial wet land, therefore can effectively save occupation of land;
7. the carrier filler in drop stream well can retain the suspended particulate substance in water body, can pass through after one period runs
Cleaning, the mode for replacing carrier filler remove the suspended particulate substance of its retention, to reduce the risk of wet land system blocking, and are
Maintenance is safeguarded and is provided convenience;
8. the aeration facility in perpendicular stream reinforcing formula biological water purification device proposed by the present invention had both realized the perpendicular of wet land system
It is exchanged to water circulation with lateral, and realizes wetland water body reoxygenation and the supply of aerobic microbiological oxygen consumption, one can be mostly used, and efficiently save
Energy;Further it is proposed that perpendicular stream strengthen formula biological water purification device on can plant economic crops, water purification simultaneously obtain economy
Income.
9. the air-flow from air blower has warming effect in winter, it is insufficient scarce to make up traditional wetland winter purifying property
It falls into.
To sum up, perpendicular stream reinforcing formula biological water purification device and its process for purifying water proposed by the present invention have to save and take up an area, efficiently
It is energy saving, the advantages that easy maintenance, good purification, comprehensive income is high.
Description of the drawings
Fig. 1 is the elevation of the perpendicular stream reinforcing formula biological water purification device of the present invention.
Fig. 2 is the plan view of the perpendicular stream reinforcing formula biological water purification device of the present invention.
Fig. 3 is the flow-shape figure of the perpendicular stream reinforcing formula biological water purification device of the present invention.
Specific implementation mode
In conjunction with following specific examples and attached drawing, the invention will be described in further detail.Implement process, the item of the present invention
Part, experimental method etc. are among the general principles and common general knowledge in the art in addition to the following content specially referred to, the present invention
Content is not particularly limited.
In Fig. 1-Fig. 3,1- water inlets;2- drop stream wells;3- biofilm carrier fillers;4- flows up well;5- aerators;6- is flat
Flow tube;7- wetland plants;8- is sintered kaolin particle layer;9- iron carbon-coatings;10- haydite layers;11- coarse sands layers;12- pond bodies;13- without
Woven fabric;14- normal water level lines;15- water outlets.
Embodiment 1:
Perpendicular stream in the present embodiment strengthens formula biological water purification device, and as shown in Fig. 1~2, up-flow well 4 and drop stream well 2 are vertical
It is arranged in recycle stream water purification medium;Advection pipe 6 is set between 2 top of up-flow 4 top of well and drop stream well, and the two is connected to;
Up-flow 4 lower part of well and 2 lower part of drop stream well are equipped with several through-holes;It flows up and is equipped with aerator 5 in well 4, life is equipped in drop stream well 2
Object membrane carrier filler 3;Recycle stream water purification medium 8~13 is laid on the outside of up-flow well 4 and drop stream well 2, is laid between filter material layer
Non-woven fabrics 13;Recycle stream water purification medium top surface can plant wetland plant 7.
The pond body size of perpendicular stream reinforcing formula biological water purification device is:10 × 5 × 1.1m, pond body 12 are laid with using antiseepage film.
Water inlet 1 is arranged at away from bottom of pond 90cm, and water outlet 15 is arranged at away from bottom of pond 5cm, and water inlet 1 and water outlet 15 are all made of directly
The pvc pipe of diameter 110cm is made.
The laying height of recycle stream water purification medium 8~13 flows reinforcing formula biological water purification device normal water level line 14 about beyond perpendicular
10cm;The shape for flowing up well 4 and drop stream well 2 is cylinder, is made of reinforcing bar concrete placings mode;Flow up a diameter of of well 4
10cm highly exceeds 8~13 top surface 10cm of recycle stream water purification medium;A diameter of 30cm of drop stream well 2, it is net highly to exceed recycle stream
8~13 top surface 10cm of aqueous medium;
The aerator 5 flowed up in well 4 uses diaphragm microporous aeration disc, is supplied by the air blower being set on wetland ground
Gas, 5 a diameter of 8cm of aerator;The tolerance of air blower is 0.75m3/ s, the promotion water flow for flowing up well are 0.05m3/m;Drop
Carrier filler 3 in stream well 4 is made of polyethylene (PE) fibrous material, and the filling rate of carrier filler is 75%.
The lower part of up-flow well 4 and drop stream well 2 is equipped with several through-holes, through-hole diameter 1cm, and quantity is 20, is uniformly divided
It is distributed within the scope of 5~40cm of shaft bottom or more.Advection pipe 6 is set between 2 top of up-flow 4 top of well and drop stream well, and will flow up well 4
It is connected to drop stream well 2.The setting height of advection pipe 6 is flushed with recycle stream water purification medium top surface, a diameter of using PVC material
5cm, tube wall sealing;
Recycle stream water purification medium 8~13 is laid on the outside of up-flow well and drop stream well, is from top to bottom followed successively by coarse sands layer
11, haydite layer 10, iron carbon-coating 9, sintering kaolin particle layer 8 lay non-woven fabrics 13 between filter material layer between filter material layer;Coarse sands layer
11 laying depth is 10cm, and coarse sand grain size is 0.5~1mm;The laying depth of haydite layer 10 be 20cm, haydite grain size be 5~
8mm;The laying depth of iron carbon-coating 9 is 30cm, and iron carbon granules diameter is 8~12mm;The laying depth of sintering kaolin particle layer 8 is
40cm, the grain size for being sintered kaolin particle are 40~60mm.
Canna, wild rice stem and oenanthe stolonifera 7 are planted in 11 top surface of coarse sands layer, and when plantation is 5~10cm seedling, spring plantation, autumn
Season gathers in.
The process for purifying water that perpendicular stream in above-described embodiment strengthens formula biological water purification device includes the following steps:
Step 1:Sewage is flow to from water inlet in wetland;
Step 2:Sewage first flows through the root system of plant planted in recycle stream water purification medium top surface, then in gravity
Under flow through recycle stream water purification medium from top to bottom;
Step 3:Sewage reaches near up-flow well lower through-hole, is inhaled into via the suction function of up-flow well water lift, and according to
It is promoted to advection pipe by stripping effect, is then transported to drop stream well;Sewage flows through the carrier filler inside drop stream well, therein
Polluter is to be removed by the biological membrane degradation on carrier filler;Last sewage flows back to filter material layer from the through-hole in drop stream underground portion;
Step 4:Water body the pushing away in wetland entirety flow with purification is repeatedly recycled through recycle stream water purification medium and drop stream well
Wetland effluent mouth is flowed under stream effect and is discharged.
Step 5:It is gathered in after mature plant growth;
Step 6:After harvesting, in recycle stream water purification medium top surface again serike.
Embodiment 2:
Perpendicular stream reinforcing formula biological water purification device, essential structure and process for purifying water are the same as embodiment 1, specific implementation mode
For:
The pond body size of perpendicular stream reinforcing formula biological water purification device is:8 × 6 × 1.6m, pond body 12 are laid with using antiseepage film.Into
The mouth of a river 1 is arranged at away from bottom of pond 90cm, and water outlet 15 is arranged at away from bottom of pond 150cm, and water outlet 15 is arranged away from bottom of pond 10cm
The pvc pipe that place, water inlet 1 and water outlet 15 are all made of diameter 200cm is made.
The laying height of recycle stream water purification medium 8~13 flows reinforcing formula biological water purification device normal water level line 14 about beyond perpendicular
15cm;The shape for flowing up well 4 and drop stream well 2 is cylinder, is made of brick mode;A diameter of 20cm of well 4 is flowed up, it is high
Degree exceeds 8~13 top surface 15cm of recycle stream water purification medium;A diameter of 35cm of drop stream well 2, highly exceeds recycle stream water purification medium 8
~13 top surface 15cm;
The aerator 5 flowed up in well 4 uses diaphragm microporous aeration disc, is supplied by the air blower being set on wetland ground
Gas, 5 a diameter of 16cm of aerator;The tolerance of air blower is 0.95m3/ s, the promotion water flow for flowing up well are 0.1m3/m;Drop
Carrier filler 3 in stream well 4 is made of chliorinated polyvinyl chloride (CPVC) fibrous material, and the filling rate of carrier filler is 80%.
The lower part of up-flow well 4 and drop stream well 2 is equipped with several through-holes, through-hole diameter 2cm, and quantity is 40, is uniformly divided
It is distributed within the scope of 5~50cm of shaft bottom or more.Advection pipe 6 is set between 2 top of up-flow 4 top of well and drop stream well, and will flow up well 4
It is connected to drop stream well 2.The setting height of advection pipe 6 is flushed with recycle stream water purification medium top surface, a diameter of using cast iron quality
10cm, tube wall sealing;
Recycle stream water purification medium 8~13 is laid on the outside of up-flow well and drop stream well, is from top to bottom followed successively by coarse sands layer
11, haydite layer 10, iron carbon-coating 9, sintering kaolin particle layer 8 lay non-woven fabrics 13 between filter material layer between filter material layer;Coarse sands layer
11 laying depth is 20cm, and coarse sand grain size is 0.5~1mm;The laying depth of haydite layer 10 be 30cm, haydite grain size be 5~
8mm;The laying depth of iron carbon-coating 9 is 50cm, and iron carbon granules diameter is 8~12mm;The laying depth of sintering kaolin particle layer 8 is
50cm, the grain size for being sintered kaolin particle are 60~80mm.
Iris, water spinach and romaine lettuce 7 are planted in 11 top surface of coarse sands layer, and when plantation is 5~10cm seedling and seed, and spring plants
Kind, autumn harvesting.
Embodiment 3:
Perpendicular stream reinforcing formula biological water purification device, essential structure and process for purifying water are the same as embodiment 1, specific implementation mode
For:
The pond body size of perpendicular stream reinforcing formula biological water purification device is:12 × 8 × 2m, pond body 12 are laid with using antiseepage film.Into
The mouth of a river 1 is arranged at away from bottom of pond 160cm, and water outlet 15 is arranged at away from bottom of pond 5cm, and water inlet 1 and water outlet 15 are all made of directly
The pvc pipe of diameter 200cm is made.
The laying height of recycle stream water purification medium 8~13 flows reinforcing formula biological water purification device normal water level line 14 about beyond perpendicular
20cm;The shape for flowing up well 4 and drop stream well 2 is cylinder, is made of brick mode;A diameter of 15cm of well 4 is flowed up, it is high
Degree exceeds 8~13 top surface 20cm of recycle stream water purification medium;A diameter of 50cm of drop stream well 2, highly exceeds recycle stream water purification medium 8
~13 top surface 15cm;
The aerator 5 flowed up in well 4 uses diaphragm microporous aeration disc, is supplied by the air blower being set on wetland ground
Gas, 5 a diameter of 12cm of aerator;The tolerance of air blower is 1.2m3/ s, the promotion water flow for flowing up well are 0.13m3/m;Drop
Carrier filler 3 in stream well 4 is made of chliorinated polyvinyl chloride (CPVC) synthetic fibers, and the filling rate of carrier filler is 90%.
The lower part of up-flow well 4 and drop stream well 2 is equipped with several through-holes, through-hole diameter 2cm, and quantity is 50, is uniformly divided
It is distributed within the scope of 5~50cm of shaft bottom or more.Advection pipe 6 is set between 2 top of up-flow 4 top of well and drop stream well, and will flow up well 4
It is connected to drop stream well 2.The setting height of advection pipe 6 is flushed with recycle stream water purification medium top surface, a diameter of using cast iron quality
8cm, tube wall sealing;
Recycle stream water purification medium 8~13 is laid on the outside of up-flow well and drop stream well, is from top to bottom followed successively by coarse sands layer
11, haydite layer 10, iron carbon-coating 9, sintering kaolin particle layer 8 lay non-woven fabrics 13 between filter material layer between filter material layer;Coarse sands layer
11 laying depth is 20cm, and coarse sand grain size is 0.5~1mm;The laying depth of haydite layer 10 be 40cm, haydite grain size be 5~
8mm;The laying depth of iron carbon-coating 9 is 40cm, and iron carbon granules diameter is 8~12mm;The laying depth of sintering kaolin particle layer 8 is
80cm, the grain size for being sintered kaolin particle are 60~80mm.
Reed, wild rice stem and yellow flag 7 are planted in 11 top surface of coarse sands layer, and when plantation is 10~15cm seedling, spring plantation, autumn
Harvesting.
Embodiment 4:
The present embodiment is substantially the same manner as Example 1, the difference is that:
The pond body size of perpendicular stream reinforcing formula biological water purification device is:6 × 5 × 1m, water inlet 1 are arranged away from bottom of pond 85cm
Place, water outlet 15 are arranged at away from bottom of pond 5cm, and the pvc pipe that water inlet 1 and water outlet 15 are all made of diameter 7.5cm is made.
The laying height of recycle stream water purification medium 8~13 flows reinforcing formula biological water purification device normal water level line 14 about beyond perpendicular
8cm;Up-flow well 4 and drop stream well 2 are made of brick mode;A diameter of 8cm of well 4 is flowed up, highly exceeds recycle stream water purification and is situated between
8~13 top surface 10cm of matter;A diameter of 25cm of drop stream well 2, highly exceeds 8~13 top surface 10cm of recycle stream water purification medium;
Flow up 5 a diameter of 6cm of aerator in well 4;The tolerance of air blower is 0.5m3/ s flows up the promotion flow of well
Flow is 0.02m3/m;Carrier filler 3 in drop stream well 4 is made of polypropylene (PP) synthetic fibers, the filling of carrier filler
Rate is 80%.
The setting height of advection pipe 6 is flushed with recycle stream water purification medium top surface, using PVC material, a diameter of 7.5cm;
Lythrum salicaria, grass-leaved sweetflag and peppermint 7 are planted in 11 top surface of coarse sands layer, and when plantation is 5~8cm seedling.
Embodiment 5:
The present embodiment is substantially the same manner as Example 1, the difference is that:
Aerator 5 in up-flow well 4 is made of boring aeration pipe coiling;The tolerance of air blower is 0.65m3/ s rises
The promotion water flow for flowing well is 0.03m3/m;Carrier filler 3 in drop stream well 4 is using poly- inclined alkene (PVDF) synthetic fibers system
At the filling rate of carrier filler is 85%.
Lythrum salicaria, grass-leaved sweetflag and peppermint 7 are planted in 11 top surface of coarse sands layer, and when plantation is 5~8cm seedling.
Embodiment 6:
The present embodiment is substantially the same manner as Example 1, the difference is that:
Aerator 5 in up-flow well 4 is made of the husky head of aeration, sand a diameter of 5cm;The tolerance of air blower is
1.3m3/ s, the promotion water flow for flowing up well are 0.15m3/m;Carrier filler 3 in drop stream well 4 is closed using reinforced polypropylene RPP
It is made at fiber, the filling rate of carrier filler is 90%.
The protection content of the present invention is not limited to above example.Without departing from the spirit and scope of the invention, originally
Field technology personnel it is conceivable that variation and advantage be all included in the present invention, and with appended claims be protect
Protect range.
Claims (9)
1. the perpendicular stream reinforcing formula biological water purification device of one kind, which is characterized in that including:Pond body, up-flow well, drop stream well and recycle stream are net
Aqueous medium;Wherein,
The pond body both sides are respectively arranged with inlet and outlet;
The recycle stream water purification medium is laid in the pond body;
The up-flow well and drop stream well setting are connected in the recycle stream water purification medium, and by advection pipe;
The up-flow well and drop stream well are equipped with through-hole;
It is equipped with aeration plate in the up-flow well, biofilm carrier filler is equipped in the drop stream well.
2. perpendicular stream reinforcing formula biological water purification device as described in claim 1, which is characterized in that the up-flow well and drop stream
Well is vertically arranged in the recycle stream water purification medium, and its spacing is 1~5m, and each up-flow well with 4 drops
Stream well is connected to by the advection pipe.
3. perpendicular stream reinforcing formula biological water purification device as described in claim 1, which is characterized in that the up-flow well and drop stream
The shape of well is cylinder, is made of reinforcing bar concrete placings or the modes such as brick;A diameter of 5~20cm of the up-flow well,
Height exceeds the recycle stream water purification medium 5~20cm of top surface;A diameter of 20~60cm of the drop stream well, highly exceeds described
Recycle stream water purification medium 5~20cm of top surface.
4. perpendicular stream reinforcing formula biological water purification device as described in claim 1, which is characterized in that the up-flow well and drop stream
The lower part of well is equipped with through-hole, and the through-hole diameter is 1~3cm, and quantity is 10~60, be uniformly distributed in shaft bottom or more 5~
Within the scope of 50cm;Aeration plate in the up-flow well using diaphragm microporous aeration disc or micropore aeration pipe coiling or is aerated husky head,
By the air blower gas supply being set on wetland ground, the aeration disk diameter is slightly less than the diameter of the up-flow well;The drop
Carrier filler in stream well is made of artificial synthetic fiber or plastics, and the filling rate of carrier filler is 65%~95%.
5. perpendicular stream reinforcing formula biological water purification device as described in claim 1, which is characterized in that the advection pipe is set to up-flow
Between well top and the tops drop Liu Jing, the setting height of the advection pipe is flushed with the recycle stream water purification medium top surface;It is described flat
Flow tube uses cast iron or PVC material, a diameter of 5~15cm, tube wall sealing.
6. stream reinforcing formula biological water purification device as described in claim 1 perpendicular, which is characterized in that the recycle stream water purification medium by
It is followed successively by coarse sands layer, haydite layer, iron carbon-coating, sintering kaolin particle layer under above, non-woven fabrics is laid between each layer;The cycle
The laying height for flowing water purification medium exceeds 5~10cm of the perpendicular stream reinforcing formula biological water purification device normal water level line;The coarse sand
Layer top surface can plant wetland plant.
7. perpendicular stream reinforcing formula biological water purification device as claimed in claim 6, it is characterised in that:The laying depth of the coarse sands layer
For 10~30cm, coarse sand grain size is 0.5~1mm;The laying depth of the haydite layer be 20~40cm, haydite grain size be 5~
10mm;The laying depth of the iron carbon-coating is 30~50cm, and iron carbon granules diameter is 8~12mm;The sintering kaolin particle layer
Laying depth is 40~60cm, and the grain size for being sintered kaolin particle is 40~80mm.
8. the perpendicular stream reinforcing formula biological water purification method of one kind, which is characterized in that strengthen formula using the perpendicular stream as described in claim 1-7
Biological water purification device, includes the following steps:
Step 1:Sewage is flow to from water inlet in pond body;
Step 2:Sewage first flows through the root system of plant planted in recycle stream water purification medium top surface, then under the effect of gravity certainly
Multilayer water purification medium is flowed through under above;
Step 3:Sewage reaches near up-flow well lower through-hole, is inhaled into via the suction function of up-flow well water lift, and rely on vapour
The effect of carrying is promoted to advection pipe, is then transported to drop stream well;Sewage flows through the carrier filler inside drop stream well, pollution therein
Substance is to be removed by the biological membrane degradation on carrier filler;Last sewage flows back to recycle stream water purification from the through-hole in drop stream underground portion and is situated between
In matter;
Step 4:The plug-flow repeatedly recycled with the water body of purification in wetland entirety flow through recycle stream water purification medium and drop stream well is made
Wetland effluent mouth is flowed under and is discharged.
9. perpendicular stream reinforcing formula biological water purification method as claimed in claim 8, which is characterized in that further comprise the steps:
Step 5:It is gathered in after the mature plant growth;
Step 6:After harvesting, the plant is planted again in the recycle stream water purification medium top surface.
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