CN205892991U - Biological ecology water treatment facilities - Google Patents
Biological ecology water treatment facilities Download PDFInfo
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- CN205892991U CN205892991U CN201620630739.5U CN201620630739U CN205892991U CN 205892991 U CN205892991 U CN 205892991U CN 201620630739 U CN201620630739 U CN 201620630739U CN 205892991 U CN205892991 U CN 205892991U
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Abstract
The utility model discloses a biological ecology water treatment facilities, it includes wetland pond and circulating and filtering system, the wetland pond includes microorganism and the aquatic plant of top in the bed of packings body, the bed of packings body, the bed of packings body is equipped with separating net including the matrix layer of the biological contact layer of undercurrent and its top between biological contact layer of undercurrent and the matrix layer, circulating and filtering system includes loop filter pump, inlet tube, outlet pipe and electromagnetic control equipment. Adopt the device, filtration pump hocket in pond no. 1 and pond no. 2 is passed through to sewage treatment's anaerobism and good oxygen process, form the tidal flow, water is when the circulation system inner loop, dirty water particles is filtered on matrix layer 3, dirty water particles thing gathering, biomembrane adsorbed particle thing granulation thing lump, the lump is discharged after filtration system filters with the large granule that gathers formation such as phosphorus fungus, the pollutant that is decomposed into simultaneously soluble component is then got rid of through biomembrane and aquatic plant root system, has good nitrogen and phosphorus removal effect.
Description
Technical field
This utility model is related to biological and ecological engineering field and in particular to a kind of biological and ecological water treatment facilities.
Background technology
Artificial swamp is a kind of half environmental sewage disposal system by engineer, transformation, mainly by (various
Water penetration) soil matrix, (growth in the saturation water and anaerobism substrate) the plant and microorganism (microbial species such as aerobic or anaerobism
Group) three part compositions.At present artificial swamp presses water stream characteristics, can be divided into surface stream undercurrent vertical current constructed wetland, wherein table
Surface current artificial swamp expenditure of construction relatively saves, but floor space is more than undercurrent and vertical current constructed wetland, and winter surface easily freezes,
Summer easily breeds mosquito, and frowziness.The advantage of subsurface wetland is that it takes full advantage of the space of wetland, has played system
Between synergism, and sanitary condition is good, but construction cost is higher.To have floor space more other because of it for vertical current constructed wetland
The advantages of form wetland is little, treatment effeciency is high, whole system can build underground in completely, is widely used.In perpendicular flow artificial
In wetland, sewage from top layer (or from lower floor upwards) vertical penetration downwards, in the warp successively to during dirty (or to upstream)
Cross different dielectric layers, reach the purpose of purification.
But existing undercurrent vertical current constructed wetland be proven and still suffer from following shortcoming: 1) existing artificial swamp skill
Art to total nitrogen ammonia nitrogen phosphorus removal ability limited, in water outlet, nitrogen phosphorus is unstable, easily exceeded；2) pipeline easily blocks.
Content of the invention
The purpose of this utility model is to provide a kind of biological and ecological water treatment facilities, at the sewage carrying out using this device
Reason method is a kind of strengthened denitrification and the sewage water treatment method of reinforced phosphor-removing function, carries especially for water solution phase-change separation system
Technique for pre-treatment.
Carry out in sewage disposal process using biological and ecological water treatment facilities of the present utility model, biologic treating technique adopts
The techniques such as biological method, remove most of Organic substance and part nitrogen phosphorus；Using artificial swamp, go to denitrogenate using soil and plant
Phosphorus.
For achieving the above object, this utility model adopts the following technical scheme that
A kind of biological and ecological water treatment facilities, it includes wetland pond and circulated filter system, and described wetland pond includes filler
Microorganism in bed body, filler bed body and the water plant above filler bed body；Described filler bed body includes undercurrent biology and connects
Contact layer and the hypothalluses above it, are provided with separate mesh between described undercurrent biological layer and hypothalluses.
Described hypothalluses include hypothalluses 1 and hypothalluses 2 from top to bottom successively, and described undercurrent biological layer is from top to bottom
Include hypothalluses 3 successively and the material particle size of 4,4 hypothalluses of hypothalluses increases from top to bottom successively.
Described wetland pond at least includes pond one and 2 two, pond cell body, described circulated filter system include cycle filter pump,
Water inlet pipe, outlet pipe and Electromagnetic Control equipment, described water inlet pipe and outlet pipe are located in pond one and pond two, and described Electromagnetic Control sets
For being located on water inlet pipe and outlet pipe, described outlet pipe is provided with stable-pressure device, the port of export of described cycle filter pump and pond one
Water inlet pipe, the water inlet pipe in pond two be all connected with, the entrance point of cycle filter pump is all connected with the outlet pipe in pond one, the outlet pipe in pond two
Connect；Wherein, the water inlet pipe in pond one or pond two is also connected with sewage water inlet pipe；Described pond one is provided with the breather leading to pond one bottom,
Described pond two is provided with the breather leading to pond two bottom.
Further, described water inlet pipe is located on hypothalluses 3, and outlet pipe is located at hypothalluses 4 bottom, and is staggered.
The material of described hypothalluses 1 is soil, and the material of hypothalluses 2 is small particle material, such as bulky grain sand, hypothalluses 3
Material be elastic filler, soft-filler, light porous filler or the ceramic grain filter being suitable to invade for a long time Sewage Environment, hypothalluses
4 material is big size particle materials, such as rubble.
Described separate mesh (such as: geonet) is located at hypothalluses 3 top, and on separate mesh, current are vertical current, under separate mesh
For mixed flow, between pond one and pond two, current are alternatively formed tidal current.Biofilter and ecological filter are separated and connect by net, raw
Thing filter tank is the microorganism filter tank system that horizontal hand-stuff is formed, and ecological filter is the minisize ecological that longitudinal water plant is formed
System.
The pond number in described wetland pond is 2 multiple, and runs current backwashing system each other.
This utility model adopts above technical scheme, filling filler in biological and ecological cell body, the whole filler of sewage submergence,
In oxygen, sewage and filler three-phase contact process, by ecological pool anoxia and aerobic alternate run, Qian Liu is vertical for Chao Xixunhuan
The composite technology flow process of stream surface stream, is removed together with water plant with the biomembrane of Guo Lvbeng filler and apposition growth thereon
The pollutant such as the float in sewage, Organic substance, ammonia nitrogen, total nitrogen phosphorus, be a kind of filter with anoxia aerobe integrated treatment skill
Art.
1) carry out sewage purification using the miniature biochemical analyzer that biomembrane and the water plant of hand-stuff formation are formed.
2) biological denitrificaion phosphorus technique adopts single ecological pool anoxia and aerobic alternate run, and Qian Liu Chui Zhiliu surface is flowed
Group technology flow process, can effectively remove Organic substance and the ammonia nitrogen in waste water, make water outlet codcr, bod5, ss and nh4+-n
Tn and tp etc. is up to standard.
3) in biofilter, the filtration of particulate matter is mainly completed by filler, and soluble pollutants then pass through biomembrane and water
Plant root system removes.The plant of ecological filter, based on emergent aquactic plant, is substantially a miniature artificial wet land system, belongs to
Ecological engineering measure.Ecological filter is processed with environmental project and unites two into one, and the water after biological treatment passes through interior following in pond
Ring carries out advanced treating.Ecological filter water inlet and recirculated water, through filter pump filtration treatment, are removing larger particulate matter simultaneously, are leading to
Crossing impulsive force cleaning filter layer avoids packing layer to block.
4), before sewage enters biofilter, reduce concentration through pretreatment, with blockage resisting filtrate.Biofilter during interior circulation
Biomembrane on filtrate constantly comes off renewal, and polyP bacteria flows out with circular treatment water, filters through filter pump and suspends and particulate matter.
5) in biological and ecological treatment tank, the release of p typically occurs under anaerobic, and the removal of p is then led to
Often occur under aerobic condition.
6) biological tank adopt two sets of parallel wet land systems, anoxia aerobic rotation make the twice that its dry spell that falls is the water inlet phase
So that system is sufficiently rested;Lay breather, be system underlying substrate conveying air, improve artificial swamp denitrification ability
Outside oxygenation measure (artificial swamp front end Air Exposure).
7) anaerobic-aerobic Combined Treatment, had both overcome Aerobic Process for Treatment energy consumption deficiency in short supply with land area greatly, had overcome again
Anaerobic treatment does not reach the defect of requirement, has that small investment, operating cost be low, good purification, energy environment comprehensive benefit
High the advantages of.
This utility model adopts above technical scheme, and artificial swamp pond is double pond, and anaerobism, anoxia and aerobic process can be handed over
For carrying out, possess preferable plug-flow process, biochemical reaction motive force is big, there is following significant advantage: 1, there is good taking off
Nitrogen phosphor-removing effect, by Controlling operation method, it is possible to achieve anaerobism, anoxia and aerobic process are alternately；2nd, run spirit
Live, according to water quality, the water yield, each operation of technical process can be adjusted；3rd, muddy water separates under preferable resting state and sinks
Form sediment, the separation process time is short, effect is good；4th, operation and maintenance convenient management, processes few and simple using equipment；5th, answer recruitment
Journey means improve system oxygen supply situation, improve system uniformity of water distribution, enhanced sewage treatment effect.
Brief description
With reference to the accompanying drawings and detailed description this utility model is further described:
Fig. 1 is one of schematic diagram of this utility model artificial wet land system；
Fig. 2 is the two of the schematic diagram of this utility model artificial wet land system；
Fig. 3 is the waste water processes schematic diagram of this utility model artificial wet land system.
Specific embodiment
As shown in one of Fig. 1 to 3, biological and ecological water treatment facilities of the present utility model, including wetland pond and circulating filtration
System, described wetland pond includes filler bed body, the microorganism in filler bed body and the water plant above filler bed body；Described
Filler bed body includes undercurrent biological layer and the hypothalluses above it, is provided between described undercurrent biological layer and hypothalluses
Separate mesh.
Described hypothalluses include hypothalluses 1 and hypothalluses 2 from top to bottom successively, and described undercurrent biological layer is from top to bottom
Include hypothalluses 3 successively and the material particle size of 4,4 hypothalluses of hypothalluses increases from top to bottom successively.
As shown in Fig. 2 the wetland pond of the present embodiment includes pond one and 2 two, pond cell body, circulated filter system includes circulating
Filter pump, water inlet pipe, outlet pipe and Electromagnetic Control equipment, described water inlet pipe and outlet pipe are located in pond one and pond two, described electricity
Magnetic control control equipment is located on water inlet pipe and outlet pipe；Outlet pipe is provided with stable-pressure device.The port of export of described cycle filter pump with
The water inlet pipe in pond one, the water inlet pipe in pond two are all connected with, the outlet pipe in the entrance point of cycle filter pump and pond one, the outlet pipe in pond two
It is all connected with；Wherein, the water inlet pipe in pond one or pond two is also connected with sewage water inlet pipe；Described pond one is provided with the ventilation leading to pond one bottom
Pipe, described pond two is provided with the breather leading to pond two bottom.
The sewage water treatment method being carried out using biological and ecological water treatment facilities of the present utility model, the anaerobism of sewage disposal with
And aerobic process pass through filter pump in pond one and pond two alternately, formed tidal current, finally realize qualified discharge, including with
Lower step:
First, sewage disinfection treatment unit: be a kind of principle using precipitation and anaerobe fermentation, to remove fecal sewage
Or float, Organic substance and pathogenic microorganism are the sewage primary treatment facility of main purpose in other sanitary sewages.
Sewage after pretreatment unit, typically to codcr, bod5, ss etc., routinely index has preferable degraded,
50% treatment effect can be up to about, but little to the index treatment effect such as nitrogen, phosphorus.
2nd, regulating reservoir: to enter anaerobism process water before aerobic circulating biological pond (the present embodiment refers to pond one and pond two) enter
Row concentration adjusts, and when influent quality is very poor when 200mg/l (as bod5 >), opens reflux pump, will process water and return
Stream, dilutes raw water, reduces bod5 load.
3rd, anaerobism aerobic circulation processing pool (artificial swamp pond, the i.e. pond one of the present embodiment and pond two):
1) pond one intakes: sewage is delivered in pond one by the water inlet pipe on the hypothalluses 3 in pond one, when the sewage water of Chi Yizhong
Pressure reaches 1-30 rice h2During o post, stop sending water, the water in pond one, under hydraulic pressure effect, moves to surface water flow；
2) pond one sucking filtration: the water in pond one is extracted out by cycle filter pump by the outlet pipe of pond one hypothalluses 4 bottom, then
It is re-fed in pond one by the water inlet pipe on the hypothalluses 3 of pond one, system circulation in formation；
3) pond one water process: the water in pond one in circulated filter system interior circulation, pond one hypothalluses 3 filter sewage granule,
Wastewater particle is assembled, biomembrane adsorption particle thing, forms particulate matter agglomerate, the bulky grain warp of the formation such as agglomerate and polyP bacteria
Filtration system is discharged after filtering, and is broken down into the pollutant of soluble component simultaneously, then pass through biomembrane and water plant root system
Remove；
4) water retention in pond one stops and circulating, standing；
5) water in pond one is pumped to pond two: cycle filter pump pumps the water of Chi Yizhong to pond two, due to water level in pond one
Decline and form negative pressure, pond one breather air inlet exposes oxygen, pond one particulate matter agglomerate of biomembrane absorption under suction function comes off, pond
Two water inlets expose the air that oxygen is discharged in pond, and described water inlet refers to that the water in pond one is pumped to pond two, and pond two is simultaneously using water inlet recoil
Service sink two, meanwhile, the air in pond two is discharged by the breather in pond two；Chi Yishui under gravity, from wetland surface
Internally flow, the pollutant agglomerate in cleaning hypothalluses 1 and hypothalluses 2, so as to depart from substrate, drops to hypothalluses 3 He
Hypothalluses 4；.
6) pond two sucking filtration: the water in pond two is extracted out by cycle filter pump by the outlet pipe of pond two hypothalluses 4 bottom, so
It is re-fed in pond two by the water inlet pipe on the hypothalluses 3 of pond two afterwards, system circulation in formation；
7) pond two water process: the water in pond two in circulated filter system interior circulation, pond two hypothalluses 3 filter sewage granule,
Wastewater particle is assembled, biomembrane adsorption particle thing, forms particulate matter agglomerate, the bulky grain warp of the formation such as agglomerate and polyP bacteria
Filtration system is discharged after filtering, and is broken down into the pollutant of soluble component simultaneously, then pass through biomembrane and water plant root system
Remove；This process, is processed under the anaerobic condition of pond one；
8) water retention in pond two stops and circulating, standing；
9) water in pond two is pumped to pond one: cycle filter pump pumps the water of Chi Erzhong to pond one, due to water level in pond two
Decline and form negative pressure, pond two breather air inlet exposes oxygen, pond two particulate matter agglomerate of biomembrane absorption under suction function comes off, pond
One water inlet exposes the air that oxygen is discharged in pond, and described water inlet refers to that the water in pond two is pumped to pond one, and pond one is simultaneously using water inlet recoil
Service sink one, meanwhile, the air in pond one is discharged by the breather in pond one；Chi Ershui under gravity, from wetland surface
Internally flow, the pollutant agglomerate in cleaning hypothalluses 1 and hypothalluses 2, so as to depart from substrate, drops to hypothalluses 3 He
Hypothalluses 4；
10) repeat step 2) -9), water circular treatment between pond one and pond two, until after water process is up to standard, give off
Go.
The anaerobism of this utility model biological and ecological water treatment facilities aerobic circulation processing pool have the following characteristics that
1) structure: adopt rectangle or square, the ratio of length and width is between 1:2-1:1 more cell body the bottom surface；Pond number
Or total number of divisions is typically no less than 2 multiples.
2) host material
Host material selects: the selection of each layer substrate and filling thickness in artificial swamp, the selection of substrate answer treatment in accordance with local conditions,
Gather materials on the spot, to reduce the cost of artificial swamp, stromal thickness should determine according to concrete water quality and field condition, total substrate bed
Thickness generally 1m about.For the substrate lacking nutrient supply or the excessive substrate being unfavorable for plant fixed growth of hole,
The thick soil of 15 ~ 25cm need to be covered above substrate, as the substrate of plant growing.
Filler: in ecological pool, the filtration of particulate matter is mainly completed by filler, soluble pollutants then pass through biomembrane and water
Plant root system removes.
Bio-filter stuffing is from being suitable to invade for a long time the elastic filler of Sewage Environment, soft-filler, light porous filler
Or ceramic grain filter etc., typically select ceramic grain filter or light porous filler, ceramic grain filter particle diameter is preferably 0.5-30mm, light porous
Packing material size preferably controls in below 45mm, and the water distribution of biofilter must be uniformly.
Biofilter structures are simple, during day-to-day operation, mainly patrol and examine the power-equipments such as water pump and whether filtrate occurs
Clogging, whether ventilation effect is good；It should be noted that antifreeze when water temperature in winter is relatively low, reduce amount of inlet water load simultaneously, with
Ensure treatment effect；
3) vegetation selects wetland water plant mainly to include emergent aquactic plant, submerged plant and floating plant.Different areas
Domain, different growing environment, the wetland plant species of suitable growth is different.Should choose that process performance is good, survival rate is high,
Stain resistance is strong and has necessarily aesthstic and economic worth water plant.As water plant be Herba Typhae, phragmites communiss, Medulla Junci, water
Radix Ophiopogonis etc..
4) hydraulic condition emphasis considers to cause the various influence factors of Wetland clogging, and Wetland clogging mostly occurs in system bed
Body portion, the material that results in blockage is most of to be inorganic matters, and this shows that particulate matter in the sewage precipitation in wetland bed is to make
Become the main cause of Wetland clogging.Additionally, root system of plant and its attachment etc. are also a big inducement of Wetland clogging.
5) biological layer is processed is to process skill by filling filler in pond and a kind of of enhanced water anaerobic treatment effect
Art, in sewage, larger molecular organicses anaerobism in pond is broken down into small organic molecule, can effectively reduce subsequent processing units
Organic pollution load.
Biological layer processes advantage: reduced investment, simple, easy maintenance of constructing；Earthing planting plants above it, with plant
Form artificial swamp.
6) ecological pool Aerobic Process for Treatment, according to waste water processes, can be divided into catalytic oxidation, a sub-contact to aoxidize and many
Secondary catalytic oxidation.Biological tank middle setting intermediate sedimentation pond, for filtering pump circulation water inlet, filtering biological matter, improves cell body saturating
Aqueouss and effluent quality.
Advantage during ecological pool Aerobic Process for Treatment: microbial biomass stably enriches, the strong adaptability to water quality, water yield fluctuation；Operation
Easy；Good to pollutant removal.
The pretreatment facility such as sedimentation tank and filter pump is set in biological tank anaerobism, aerobic circulation processing pool, to prevent from blocking.
Need the aerating system of reasonable Arrangement biological contact oxidation pond in pond, realize uniform aeration.Filler filling will rationally prevent from blocking up
Plug.
Claims (7)
1. a kind of biological and ecological water treatment facilities it is characterised in that: described water treatment facilities includes wetland pond and circulating filtration system
System, described wetland pond includes filler bed body, the microorganism in filler bed body and the water plant above filler bed body；Described fill out
Material bed body includes undercurrent biological layer and the hypothalluses above it, is provided with point between described undercurrent biological layer and hypothalluses
Every using separate mesh with connecting.
2. a kind of biological and ecological water treatment facilities according to claim 1 it is characterised in that: described hypothalluses are from top to bottom
Include hypothalluses 1 and hypothalluses 2 successively, described undercurrent biological layer includes hypothalluses 3 and hypothalluses 4,4 from top to bottom successively
The material particle size of individual hypothalluses increases from top to bottom successively.
3. a kind of biological and ecological water treatment facilities according to claim 1 it is characterised in that: described wetland pond at least includes
Pond one and 2 two, pond cell body, described circulated filter system include circulating filtration equipment, water inlet pipe, outlet pipe, pressure stabilizing device and
Electromagnetic Control equipment；
Described water inlet pipe and outlet pipe are located on pond one and the circulated filter system in pond two, and described Electromagnetic Control equipment is located at into water
On pipe and outlet pipe；
The port of export of described circulating filtration equipment is all connected with the water inlet pipe in the water inlet pipe in pond one, pond two, circulating filtration equipment
Entrance point is all connected with the outlet pipe in pond one, the outlet pipe in pond two；Wherein, the water inlet pipe in pond one or pond two is also connected with artificial swamp
System sewage water inlet pipe；
Described pond one is provided with the breather leading to pond one bottom, and described pond two is provided with the breather leading to pond two bottom.
4. a kind of biological and ecological water treatment facilities according to claim 3 it is characterised in that: described outlet pipe is provided with surely
Pressure device, described water inlet pipe is located on hypothalluses 3, and outlet pipe is located at hypothalluses 4 bottom, and is staggered.
5. a kind of biological and ecological water treatment facilities according to claim 2 it is characterised in that: the material of described hypothalluses 1
For soil, the material of hypothalluses 2 is small particle material, and the material of hypothalluses 3 is to be suitable to invade for a long time the elasticity of Sewage Environment to fill out
Material, soft-filler, light porous filler or ceramic grain filter, the material of hypothalluses 4 is big size particle materials.
6. a kind of biological and ecological water treatment facilities according to claim 2 it is characterised in that: described separate mesh is located at substrate
Layer 3 top, on separate mesh, current are vertical current, are mixed flow, between pond one and pond two, current are alternatively formed tide under separate mesh
Stream.
7. a kind of biological and ecological water treatment facilities according to claim 1 it is characterised in that: the pond in described wetland pond
The multiple for 2 for the number, and run current backwashing system each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620630739.5U CN205892991U (en) | 2016-06-23 | 2016-06-23 | Biological ecology water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620630739.5U CN205892991U (en) | 2016-06-23 | 2016-06-23 | Biological ecology water treatment facilities |
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| Publication Number | Publication Date |
|---|---|
| CN205892991U true CN205892991U (en) | 2017-01-18 |
Family
ID=57768891
Family Applications (1)
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| CN201620630739.5U Active CN205892991U (en) | 2016-06-23 | 2016-06-23 | Biological ecology water treatment facilities |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109133494A (en) * | 2018-07-06 | 2019-01-04 | 广州格淋环境保护技术有限公司 | A kind of complex ecological water purification system and its process for purifying water |
| CN113371936A (en) * | 2021-06-16 | 2021-09-10 | 中国水利水电科学研究院 | Improved anti-blocking constructed wetland and use method thereof |
| CN113860503A (en) * | 2020-06-30 | 2021-12-31 | 国河环境研究院(南京)有限公司 | Multifunctional electrochemical coupling ecological floating bed |
| CN115340184A (en) * | 2022-07-25 | 2022-11-15 | 悉地（苏州）勘察设计顾问有限公司 | Anti-blocking type biological detention pond system and working method thereof |
-
2016
- 2016-06-23 CN CN201620630739.5U patent/CN205892991U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109133494A (en) * | 2018-07-06 | 2019-01-04 | 广州格淋环境保护技术有限公司 | A kind of complex ecological water purification system and its process for purifying water |
| CN113860503A (en) * | 2020-06-30 | 2021-12-31 | 国河环境研究院(南京)有限公司 | Multifunctional electrochemical coupling ecological floating bed |
| CN113371936A (en) * | 2021-06-16 | 2021-09-10 | 中国水利水电科学研究院 | Improved anti-blocking constructed wetland and use method thereof |
| CN115340184A (en) * | 2022-07-25 | 2022-11-15 | 悉地（苏州）勘察设计顾问有限公司 | Anti-blocking type biological detention pond system and working method thereof |
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Effective date of registration: 20170104 Address after: South Village David Dehua County of Quanzhou City, Fujian province 350000 Township Patentee after: The Agricultural Ecology Institue of Fujian Academy of Agricultural Sciences Patentee after: Dehua green ecological agriculture and Forestry Co., Ltd. Address before: 350000 Academy of Agricultural Sciences, No. 54 North Road, Gulou District, Fujian, Fuzhou, China Patentee before: Zhang Jinyu Patentee before: Dehua green ecological agriculture and Forestry Co., Ltd. |