CN106277322A - A kind of environmental water treatment facilities and processing method - Google Patents
A kind of environmental water treatment facilities and processing method Download PDFInfo
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- CN106277322A CN106277322A CN201610777880.2A CN201610777880A CN106277322A CN 106277322 A CN106277322 A CN 106277322A CN 201610777880 A CN201610777880 A CN 201610777880A CN 106277322 A CN106277322 A CN 106277322A
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- sewage
- rod
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- 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
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- 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
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
-
- 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
Abstract
The present invention relates to a kind of environmental water treatment facilities and processing method, including input unit, process pond portion, output unit, desilting portion.Multiple types source of sewage/the waste water sources such as rainwater, engineering sewage, sanitary sewage can be processed by the present invention, there is multinomial desilting, anti-silting measure, in conjunction with measures such as other monitoring, can ensure that processing equipment effectively operates to greatest extent, minimizing is closed down, and improves utilization rate of equipment and installations and improves production efficiency；The load of process at different levels is shared, and integral pressure reduces, and is suitable for long-play, and system stability and life-span all improve；All kinds of parameter can be monitored in real time, sewage disposal overall process is dynamically monitored, it is simple to the dynamic adjustment to processing procedure, comprehensively control sewage disposal process；Realize the unmanned operating of processing equipment, remote control.
Description
Technical field
The present invention relates to sewage-treatment plant and processing method, in particular to Intelligent sewage comprehensive, ecotypic
Processing means and method.
Background technology
In recent years, along with stepping up of mankind's environmental consciousness, the requirement of environmental development is progressively by cognitive and put on day
Journey, sewage disposal increasingly paid attention to, recycled water utilize purposes more and more extensive.The quality requirements of water after treatment more comes
The highest, wherein the content of nitrogen and phosphorus is also taken seriously.
Process to sewage in prior art, is frequently used outfit anaerobism groove, the processing means of aerobic slot, process suitable
At a high speed and fully, thus by go to denitrogenate with phosphorus required for the most undue the eliminating of Organic substance.The Organic substance being dissolved in sewage
The amount of composition changes because the shape of raw sewage is different, and when the amount of organic components is few, the effect of microorganism is also subject to consistent,
The reaction such as denitrogenation is insufficient.Accordingly, it would be desirable to real-time is monitored materials all kinds of in processing procedure, and come according to Monitoring Data
Adjust amount and opportunity, the operational factor etc. of adjustment various kinds of equipment of all kinds of additive, thus realize the optimum control to sewage disposal
System, effectively control and Based Intelligent Control.
Major part in the sewage of preliminary treatment, due in processing environment/pipeline in reason, change factor change, lead
Cause existence mud dynamically, frequently, floccule, plumbing installation can be blocked, cause unnecessary trouble, or need often to enter
Row cleaning, causes frequent the closing down of equipment, production efficiency and equipment loss is had harmful effect.It is therefore desirable in conveying
Corresponding processing equipment is set on pipeline.
Multi-stage treatment units is Modern sewage, the conventional structure of waste water process, but if in multistep treatment, each level divides
Improper, ineffective to the monitoring of each stage, the low usefulness of process can be caused, interfere, get half the result with twice the effort on the contrary.Meanwhile, load is individual
Other processing links is relatively big, causes damage equipment, and system stability is poor, and is difficult to increase and decrease periodic to source of sewage and cannot fit
Should.It is, therefore, desirable to provide a kind of comprehensive sewage disposal solution, what is more important when in the face of different source of sewage,
When different process requirements and processing intent, it is possible to select between multilevel hierarchy, processing meanss the most at different levels are by load
Share, it is also possible to rationally increase and decrease problem in the face of source of sewage, obtain a scheme optimized.
Summary of the invention
The present invention is the comprehensive technical scheme of one proposed to solve above-mentioned series of problems.The present invention proposes
A kind of novelty, the technical scheme of practicality, the present invention is achieved through the following technical solutions:
A kind of environmental water treatment facilities, including: input unit, it is responsible for pending water source introducing is processed pond portion；Process
Pond portion, is responsible for the water source of input is carried out all kinds of process；Output unit, is responsible for the water output that will be disposed；Desilting portion, being responsible for will
Silting transfer or process.
In described a kind of environmental water treatment facilities, processed water source in input unit, process pond portion, output unit, clear
Circulate between silt portion, the intermediate state water source that described water source includes source of sewage and is partly processed or processes completely.
Further, described input unit includes: power source, straight defeated pipeline, buffer unit, passage.Described power source provides
Power, promotes water source to flow.Described straight defeated pipeline is the source of sewage pipeline outside access, is the importation of whole system；
Described buffer unit is for the interim of water source and/or short-term storage.Described passage is for for processing pond by source of sewage importing
The pipe section in portion.
Further, described process pond portion, comprise anaerobic groove some (numbering 1,2,3 ..., m, m more than or equal to 1 are just
Integer), logical oxygen groove some (numbering 1,2,3 ..., n, n are the positive integer more than or equal to 1), oxygen injection device, stirring device, draw
Stream device (backflow is used), and, and/or denitration portion, dephosphorization portion.
Further, described process pond portion also includes: sensor group, power packages, central processing unit portion；Described central authorities
Processor portion includes data monitoring portion, control portion, speed regulation section.
In above-mentioned a kind of environmental water treatment facilities, the power source of described input unit, by straight defeated pipeline and/or caching
In sewage its passage incoming in portion, and then inflow processes pond portion；In processing pond portion, sewage obtains a series of process and returns
Stream.
Described power source accepts the control in control portion, thus realizes the control to sewage/water source input quantity.
Further, two anaerobic grooves in the portion of described process pond and three logical oxygen grooves constitute one and process reaction member.
The described some grooves processing reaction member are set up in parallel, and arrange stirring device, had aquaporin between groove and groove in groove.
Further, one or both of anaerobic groove carries out denitration reaction, arranges film unit inside last logical oxygen groove.
Described stirring device has driver element, and accepts the control in control portion.
The described sensor group processed in the portion of pond, has multiple sensors: acidity-basicity sensor, oxidation-reduction potential pass
Sensor, dissolved oxygen sensor, electric conductivity value sensor, sensor group be any of the above described the two, three or the combination of four, or entirely
Portion.
Oxygen injection device in the portion of described process pond, injects oxygen in logical oxygen groove.
Further, described process pond portion also have for going dephosphorization to arrange: flocculant groove, and flocculant
Syringe.Described flocculant syringe accepts the control of controller.
Described data monitoring portion receives each sensor group and sends the data of coming, and is sent to the process of control portion, through place
Reason, obtains controlling the instruction of oxygen injection device, controls oxygen injection device by controller, and forms control flocculant syringe
Control instruction, control flocculant syringe by controller.
Described drainage device accepts the control of controller, and drainage device connects the film unit in logical oxygen groove and first anaerobic
Groove, the micropopulation formed film unit side is transmitted to anaerobic groove.Described central processing unit portion is passed by oxidation-reduction potential
The data of sensor have judged whether denitrification step.Oxidation-reduction potential sensor real-time drawn in data monitoring portion
Become change curve, be used for monitoring its saturated mode.
Further, in described logical oxygen groove, the side of film unit has outlet tube, and described outlet tube is connected to output
Portion, output unit is provided with passage, and passage node accesses desilting portion, and desilting portion also has interdependent node phase in process pond portion, input unit
Connection, for processing too many levels, the blocking up of multinode, depositing, block.
Further, the water source of described output unit output is through multinomial detection, to external transmission.
Further, described speed regulation section receives the control in control portion, is used for regulating water source, stirring device, oxygen note
Enter the speed of service of various equipment in each water source intermediate links of portion.
In described process pond portion or output unit afterbody also has: reactor group.Described reactor group, exposes including biological
Solid/liquid/gas reactions still, it is provided that light heterotrophic microorganism group, supporting have to bio-aeration reactor provide described in become light heterotrophism
The nutrient substance of micropopulation use and the structure of organic carbon substrate matter, current in formation.Described all kinds of sensing of reactor group
Device, controller connect.
By the step processing sewage of above-mentioned reactor group it is:
(1) nutrient substance used to the light heterotrophic microorganism group that becomes described in the offer of bio-aeration reactor and organic carbon substrate
Matter, current in formation.
(2) light heterotrophic microorganism group is cultivated to change into by this nutrient substance at least some of and organic carbon substrate matter
Light heterotrophic microorganism group, on this, current and the light heterotrophic microorganism group that becomes collectively form the lower current of bio-aeration reactor.
(3) lower current are transferred to defecation tank from bio-aeration reactor, current under concentrating in defecation tank, formed low solid
Content thing and high solids content thing, at least one being exposed in intensity and wavelength by the light heterotrophic microorganism group that becomes described in making be enough to
This light heterotrophic microorganism group that becomes is made to move apart under the light source of light source to make this light heterotrophic microorganism group that becomes light that becomes to carry out this from concentrating
Concentration process, wherein makes this light heterotrophic microorganism group that becomes concentrate to form high solids content thing.
(4) dehydration of high solids content thing is formed concentrated biological to stick with paste；Processing low-solid content thing is to form treated discharge water
Stream.
Further, on the passage of described input unit, or on the passage of output unit, arrange " flowing water barb ".Institute
" flowing water barb " structure stated is:
The oblique riser being combined on base plate including base plate and polylith bevelled junction.Described base plate is rectangular or square, lies low
Placing, two ends or surrounding have fixed structure, and described fixed structure is for embedding flowing water barb or engaging or anchor or riveting
Gu or the mode that pin is solid or screw thread is solid is fixed on the pipelined channel of input unit.Further, above-mentioned fixing is dismountable so that stream
Water barb can be changed.The angle of described oblique riser and base plate can be 15 °, 30 °, 45 °, 120 °, 135 °, one of 150 °.
Tiltedly having the hole not of uniform size of matrix form on riser, the highest ground square hole in position is the biggest, spacing is the biggest, the ground square hole that position is low
The least, spacing is the least, and the surfacing of described oblique riser has adsorption function, can adsorb in water source and specifically pollute
Material, floccule, or magnetisable material.Multiple oblique risers are removable with parallel or nonparallel, equidistant or non-equidistance state
The mode unloaded is fixed on base plate.On base plate, having granular curvilinear plane, this non-burnishing surface can most in water source
Number or specific polluter carries out adsorbing, stops, accumulates.Also there is on described base plate some storage mud grooves.
Replacing as one, described " flowing water barb " structure is:
Including base plate and oblique riser, and the two is set to hollow structure, and some hollows of oblique riser and the hollow of base plate are
Communicating, there is accumulating tank below base plate, it is used for accumulating the polluter accumulated by oblique riser and base plate.The described end
On plate and/or tiltedly riser, multiple hole all can be set, hole can embed drainage screen, or macromolecular material is set, be used for inhaling
Attached pollutant.Base plate and oblique riser arrange groove, for by accumulating tank below base plate of the pollutant drain of coagulation.
Replacing as one, described " flowing water barb " structure is:
Including a cylinder supported, and multiple can dismantling and the place of flexible angle of being connected on cylinder
The reason body of rod, and the accumulating tank of lower section.Described cylinder can be driven by current and cause rolling, it is also possible to be independently arranged power
Source, is turned by the speed set and/or both forward and reverse directions choosing, or is set as fixed.The described process body of rod and cylinders contact
One of the tangent line at place is 10 °, 15 °, 20 °, 25 °, 30 °, 150 °, 160 °.The most permissible as a selection, cylinder and the process body of rod
Being hollow structure, its surface has the hole by sewage, or has the hole filtering sewage, and pollutant are in cylinder interior and lower section
Accumulated, so cleaned.
Selecting as one, the axle center of described cylinder is slightly above channel surface.
A kind of method of the hand-off process body of rod, it is characterised in that: cylinder has roll capability, is fixing when processing.
Assuming that drum surface is provided with 10 process bodies of rod, these process the most numbered 1-10 of the body of rod, and at some shape
Under state, 1-5 is positioned at above channel surface, and 6-10 is positioned at below channel surface.Processing the body of rod is that to have the hollow of absorbability soft
Body, in cylinder, storage has high density liquid, and is connected with the 1-10 process body of rod, and the 1-5 process body of rod is inflated high density
Liquid, and No. 6-10 is not inflated.By as follows for step that the 6-10 process body of rod switches to duty:
Step one: unload liquid.High density liquid in the 1-5 process body of rod is discharged, is discharged to cylinder interior, makes at No. 1-5
The reason body of rod becomes software；
Step 2: inflation cleaning.By the way of repeatedly ventilating, the high density liquid in the 1-5 process body of rod is cleaned out
Come；In cylinder interior, the high density liquid of release in step one is collected the higher density fluid body memory of cylinder；
Step 3: angle rotates.(controller) controls rotary drum 180 °, if changing a part therein, such as 4
The individual process body of rod, then rotate 144 °, if changing 3, then rotates 108 °, if with changing 2, then rotates 72 °.That is
Sum according to the body of rod and distribution, analogize.
Step 4: inflation.By corresponding high density liquid injection device, high density liquid is injected 6-10 process bar
In body.So far, the process body of rod of work is adjusted to the 6-10 process body of rod.
A kind of special stirring device, a bottom and the half-pipe body that sidewall is hollow, bottom half-pipe body according to certain/
Certain rule lays some air-vents, and air-vent communicates with interior hollow section, is a sealed disc below each air-vent,
It it is the moving telescopic portion that moves up and down of a sustainable sealed disc below sealed disc.Sidewall (or the end at U-shaped hollow cell body
Portion) on, it is provided with baroceptor, gas pump, current meter, source of the gas.Source of the gas uses noble gas.The effect in moving telescopic portion is
By moving up and down so that air-vent is opened or sealed, and moving telescopic portion comprises pressure transducer, for by monitoring disk
And the pressure between air-vent edge, judges that whether sealed disc is by vent seal.
Further, above-mentioned stirring device be suitable for large-area, stir uniformly.
Aforesaid stirring device, work process is as follows:
Original state is sealed disc and vent seal state.Source of the gas is controlled to hollow cavity input by controlling device
Noble gas, monitors baroceptor, treats that pressure reaches requirement, then fall moving telescopic portion, Continuous aeration, keep air pressure sensing
Device monitor value interior fluctuation normal range.
Particularly, stirring device can also be integrated with oxygen injection device: adds oxygen or sky in above-mentioned stirring device
Gas input pipe, source of oxygen or air source, a switch, it is achieved oxygen (air) and the switching of noble gas.When needs are passed through
During oxygen, rise moving telescopic portion, close air-vent, close inert gas source input, be switched to source of oxygen, input gas, prison
Survey the numerical value of baroceptor, after requirement to be achieved, fall moving telescopic portion, continue oxygen supply, keep baroceptor monitor value
Fluctuation in normal range.
Described noble gas, in addition to referring to the noble gas that chemical field is conventional, also refers in particular to: at entirety
For each course of reaction of reason system, each chemical composition, do not make the gas that any chemical composition changes.
Described a kind of environmental water treatment facilities, also includes primary treatment device, two stage treatment device.Described primary
Before processing means, two stage treatment device are arranged on input unit, belong to the pretreatment unit processing pond portion on the whole.
Being two stage treatment device after primary treatment device, function is to separate solid-liquid.
Primary treatment device, including greasy dirt isolating construction, the settlement separate structure of solid constituent, solid dirty delivery section.
Described greasy dirt isolating construction, carries out cursory separation to the greasy dirt in sewage；
The settlement separate structure of described solid constituent, carries out settlement separate to solid constituent in sewage；
Gu dirty delivery section, it is respectively connected to primary treatment device and two stage treatment device, by solid therein, floccule, mud
Shape thing is collected and is transferred out.Gu dirty delivery section, the function also having is to make the settlement separate structure sediment of solid constituent isolate
Solid constituent be detained and be allowed to solubilized.
Further, Gu what dirty delivery section and other structures in primary treatment device were to cooperate with or were connected to, connect suitable
Sequence can be: sewage injection unit, cell body, solid dirty delivery section, installs greasy dirt isolating construction, the settlement separate knot of solid constituent in cell body
Structure.Sewage injection unit makes sewage keep standing, and makes greasy dirt cursory separation from sewage.Cell body makes solid portion settle from sewage
Separate.Gu dirty delivery section comprises power section, it can be motor.
The principle of the settlement separate structure of greasy dirt isolating construction, solid constituent is to process the difference in specific gravity of composition in water according to it.
Through process and the transport of solid dirty delivery section, can make to be occurred solubilized by settlement separate solid constituent, thus
In biological treatment device or similar processing means, nitrogen, phosphorus composition can be carried out bioanalysis etc. and remove, and pass through
Solubilized and the supplementary required organic components of solid constituent, by with being applied in combination of other processing meanss, it is possible to have
The removal organic dirt of effect, nitrogen compound, phosphorus compound, it is possible to reduce the burden of aftertreatment device, stablize, obtain efficiently
Recycled water and/or can the clean water of harmless emission.
Sewage after primary treatment device processes flows into two stage treatment device.
Two stage treatment device major function is solid, liquid separation, it is possible to the residual foreign material processed in water are carried out physics
Separate and remove, and the process water eliminating residual foreign material is sent to buffer unit, standby, treat the processing meanss such as biological treatment device
Process further.
Sewage collecting after primary treatment device and two stage treatment device enters buffer unit, for intelligent/comprehensive/
Biotype water treatment facilities processes.
Further, " flowing water falls to hoard setting on the transport water channel of device (buffer unit) in the entrance of two stage treatment device
Spine ".
By above-mentioned one and/or multiple technologies scheme, the present invention can reach following technique effect:
(1) processing method of the intelligent water treatment facilities of a kind of modernization, also has biotype treatment technology, it is possible to right
Multiple types source of sewage/the waste water sources such as rainwater, engineering sewage, sanitary sewage process, and efficiency is high；
(2) a kind of comprehensive technical scheme, what is more important is in the face of particular type or the sewage of concrete composition, or tool
Body processes when requiring, it is possible to selective use some handling processes therein, highly versatile, it is possible to the solution mesh of maximum magnitude
The difficult problem of front sewage disposal and maximum magnitude adapt to current sewage disposal requirement；
(3) all kinds of parameter can be monitored in real time, sewage disposal overall process is dynamically monitored, it is simple to dynamic to processing procedure
Adjust, comprehensively control sewage disposal process；Realize the unmanned operating of processing equipment, remote control；
(4) there is multinomial desilting, anti-silting measure, in conjunction with measures such as other monitoring, it is possible to guarantee processes and sets to greatest extent
Having effect operating, minimizing is closed down, and improves utilization rate of equipment and installations and improves production efficiency；
(5) in the middle of having sewage and processing, water hoards function, it is possible to according to carrying out runoff investigation processing speed and storing up
Long-pending, treat that idle is reprocessed；Can adapt to the change of the sewage quantity of sanitary sewage, plant effuent one day or seasonality, production cycle property
Change (processing equipment or factory load change)；
(6) multi-stage treatment units, Combined Treatment, effectively process all kinds of known contaminant matter, the load of process at different levels is divided
Load, integral pressure reduces, and is suitable for long-play, and system stability and life-span all improve.
Described above is only the general introduction of technical solution of the present invention, in order to better understand the technological means of the present invention,
And can be practiced according to the content of description, below with presently preferred embodiments of the present invention and coordinate accompanying drawing describe in detail as after.
The detailed description of the invention of the present invention is shown in detail in by following example and accompanying drawing thereof.Many places of the present invention are only to the portion making improvement
Divide and be described, and other undeclared parts can realize by the state of the art, that is undeclared part is by existing
There is technology to realize, be not described in detail at this.
Accompanying drawing explanation
Accompanying drawing described herein is used for providing a further understanding of the present invention, constitutes the part of the application, this
Bright schematic description and description is used for explaining the present invention, is not intended that inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the intelligent water treatment facilities structural representation of the present invention；
Fig. 2-1 is the first flowing water barb structural side view of the present invention；
Fig. 2-2 is the second flowing water barb structural side view of the present invention；
Fig. 3 is the third flowing water barb structural side view of the present invention；
Fig. 4 is the stirring device schematic diagram of the present invention；
Wherein, reference: 1-input unit；2-processes pond portion；3-output unit；4-desilting portion.
Detailed description of the invention
With embodiment, the technology implementation process of the present invention is described further below in conjunction with the accompanying drawings.
Embodiment 1:
The present embodiment mainly introduces a kind of intelligent water treatment facilities, and (comprehensive water treatment facilities/ecotype water processes dress
Put) composition, and the concrete composition of this system and associated components thereof, non-specified otherwise part therein uses prior art real
Existing.Specified otherwise includes the related description in posterior embodiment and related art scheme.
As shown in Figure 1, a kind of intelligent water treatment facilities (comprehensive water treatment facilities/ecotype water treatment facilities),
Including:
Input unit, is responsible for pending water source introducing is processed pond portion；
Process pond portion, be responsible for the water source of input is carried out all kinds of process；
Output unit, is responsible for the water output that will be disposed；
Desilting portion, is responsible for silting transfer or processes.
In the described intelligent water treatment facilities of one (comprehensive water treatment facilities/ecotype water treatment facilities), quilt
The water source processed circulates between pond portion, output unit, desilting portion in input unit, process, and described water source includes source of sewage and quilt
The intermediate state water that part processes or processes completely.
Further, described input unit includes: power source, straight defeated pipeline, buffer unit, passage.Power source provides power, promotees
Making water source flow, concrete can be a kind of pump or motor.Described straight defeated pipeline is the source of sewage pipeline outside access, is whole
The importation of individual system；Buffer unit is for the interim of water source and/or short-term storage, to adapt to the time-out of processing equipment, fortune
The situations such as the reduction of line speed, source of sewage is sudden, provisional, periodicity amount is big.Described passage is for for leading source of sewage
Enter to process the pipe section in pond portion, can be designed as open or closed as required, or closing combines with open.Described
Passage in one or more physical units for preliminary treatment are set.
Further, described process pond portion, comprise anaerobic groove some (numbering 1,2,3 ..., m, m more than or equal to 1 are just
Integer), logical oxygen groove some (numbering 1,2,3 ..., n, n are the positive integer more than or equal to 1), oxygen injection device, stirring device, draw
Stream device (backflow is used), and, and/or denitration portion, dephosphorization portion.
Further, described process pond portion also includes: sensor group, power packages, central processing unit portion；Described central authorities
Processor portion includes data monitoring portion, control portion, speed regulation section.
In the above-mentioned intelligent water treatment facilities of one (comprehensive water treatment facilities/ecotype water treatment facilities), defeated
Entering the power source in portion, by the sewage in straight defeated pipeline and/or buffer unit, (sewage here can also be through front end processing device
Processed) in its passage incoming, preliminary treatment may be carried out in the channel, and then inflow processes pond portion；In processing pond portion
Sewage obtains a series of process and backflow.
Described power source accepts the control in control portion, thus realizes the control to sewage/water source input quantity.
Two anaerobic grooves and three logical oxygen grooves in the portion of described process pond constitute one and process reaction member.Above-mentioned process is anti-
The some grooves answering unit are set up in parallel, groove is arranged stirring device (stirring device can use routine, it would however also be possible to employ this
In bright specially designed), there is between groove and groove aquaporin.Selecting as one, one or both of anaerobic groove carries out denitration
Reaction, arranges film unit inside last logical oxygen groove.
Described stirring device has driver element, and accepts the control in control portion.
Process the sensor group in the portion of pond, there is multiple sensors: acidity-basicity sensor, oxidation-reduction potential sensor,
Dissolved oxygen sensor, electric conductivity value sensor etc., sensor group be any of the above described the two, three or the combination of four, or all.
Oxygen injection device in the portion of described process pond, injects oxygen in logical oxygen groove, and oxygen injection device can use routine
, it is also possible to use the specially designed device integrated with stirring device of the present invention.Oxygen injection device, when oxygen supply, is generally accompanied
Along with puddling of stirring device.
Process and pond portion also has for going dephosphorization to arrange: flocculant groove, and flocculant syringe.Described wadding
Solidifying agent syringe accepts the control of controller.
Described data monitoring portion receives each sensor group and sends the data of coming, and is sent to the process of central processing unit portion,
Through processing, obtain controlling the instruction of oxygen injection device, control oxygen injection device by controller, and form control flocculant
The control instruction of syringe, controls flocculant syringe by controller.So that, the injection rate of flocculant with have been injected into
Amount, reaction member is divided into point in data value, processing stage adapt.According to Monitoring Data, each phosphorus concentration suitable
The injection rate of flocculant, based on phosphorus concentration dependency relation data corresponding with the electric conductivity concentration inputted and corresponding with phosphorus concentration
Flocculent agent injection rate data and determine suitable flocculent agent injection rate.Central processing unit portion based on that input and electric conductivity
The phosphorus concentration related data that concentration is corresponding, according to being measured the electric conductivity value transmitted, calculates corresponding with the electric conductivity value measured
Phosphorus concentration.
Described drainage device accepts the control of controller, and drainage device connects the film unit in logical oxygen groove and first anaerobic
Groove, the micropopulation formed film unit side is transmitted to anaerobic groove.Described central processing unit portion is passed by oxidation-reduction potential
The data of sensor have judged whether denitrification step.Oxidation-reduction potential sensor real-time drawn in data monitoring portion
Become change curve, be used for monitoring its saturated mode.
In described logical oxygen groove, the side of film unit has outlet tube, and described outlet tube is connected to output unit, output unit
Being provided with passage, passage node accesses desilting portion, and desilting portion also has interdependent node in process pond portion, input unit to be connected, and is used for
Process too many levels, the blocking up of multinode, deposit, block.
The water source of described output unit output is through multinomial detection, to external transmission, can be to rivers,lakes and seas or other are big
The discharge of natural environment, it is also possible to be to revert to nature water factory, municipal water use factory etc. to reclaim link, or enter other process rings
Joint, further processes, final satisfactory clean water.
Described speed regulation section receives the control in control portion, be used for regulating water source, stirring device, oxygen injection unit etc. each
The speed of service of various equipment in water source intermediate links.
Assembly of the invention realizes remote data transmission and control by means of Radio Transmission Technology and the Internet, it is achieved device
Unmanned operating and dynamic supervision.
Embodiment 2:
The present embodiment realizes on the basis of previous embodiment 1, mainly introduces a kind of pioneering " reactor group ".
Reactor group, it can be arranged in process pond portion, it is also possible to is set to connect output unit, to output unit output
Process water to process further.
Described reactor group, including bio-aeration reactor, it is provided that light heterotrophic microorganism group, and supporting has
The nutrient substance used to the light heterotrophic microorganism group that becomes described in the offer of bio-aeration reactor and the structure of organic carbon substrate matter, shape
Current on one-tenth.
Described reactor group can also be connected with various kinds of sensors, controllers such as PH.
By mainly comprising the following steps of the process sewage of above-mentioned reactor group:
(1) nutrient substance used to the light heterotrophic microorganism group that becomes described in the offer of bio-aeration reactor and organic carbon substrate
Matter, current in formation.
(2) light heterotrophic microorganism group is cultivated to change into by this nutrient substance at least some of and organic carbon substrate matter
Light heterotrophic microorganism group, on this, current and the light heterotrophic microorganism group that becomes collectively form the lower current of bio-aeration reactor.
(3) lower current are transferred to defecation tank from bio-aeration reactor, current under concentrating in defecation tank, formed low solid
Content thing and high solids content thing, at least one being exposed in intensity and wavelength by the light heterotrophic microorganism group that becomes described in making be enough to
This light heterotrophic microorganism group that becomes is made to move apart under the light source of light source to make this light heterotrophic microorganism group that becomes light that becomes to carry out this from concentrating
Concentration process, wherein makes this light heterotrophic microorganism group that becomes concentrate to form high solids content thing.
(4) dehydration of high solids content thing is formed concentrated biological to stick with paste；Processing low-solid content thing is to form treated discharge water
Stream.
Embodiment 3:
The present embodiment realizes on the basis of previous embodiment 1 or 2, mainly introduces a kind of pioneering " flowing water barb ".
On the passage of described input unit, or on the passage of output unit, arrange " flowing water barb ".Described " flowing water
Barb " there is a various structures:
(1) flat.As shown in accompanying drawing 2-1,2-2, mainly include the oblique riser that base plate and polylith bevelled junction are combined on base plate.
Described base plate is in a variety of shapes, first-selected rectangle and square, and typically lie low placement, two ends or surrounding have fixed structure, institute
The fixed structure stated is for embedding flowing water barb or engaging or anchoring or rivet clasp or pin is solid or screw thread is solid mode are fixed to defeated
Enter on the pipelined channel in portion.Further, above-mentioned fixing is dismountable so that flowing water barb can be changed.Described oblique riser with
The angle of base plate can be 15 °, 30 °, 45 °, 120 °, 135 °, any one proper angle between 150 ° etc. 0-180 °.Tiltedly
Having the hole not of uniform size of matrix form on riser, the highest ground square hole in position is the biggest, spacing is the biggest, and the low ground square hole in position is more
Little, spacing is the least, and the surfacing of described oblique riser has adsorption function, can adsorb specific pollutant in water source
Matter, floccule, or magnetisable material etc..Multiple oblique risers are removable with parallel or nonparallel, equidistant or non-equidistance state
The mode unloaded is fixed on base plate.On base plate, having granular curvilinear plane, this non-burnishing surface can most in water source
Number or specific polluter carries out adsorbing, stops, accumulate, thus avoids these materials to conveyance conduit or process pipeline
Other positions carry out blocking, damaging.Also there is on described base plate some storage mud grooves.
Accompanying drawing 2-1,2-2 respectively illustrate oblique riser and form side view during different angles with base plate.
(2) hollow flat.Further, described base plate and oblique riser can be set to hollow structure, some the most vertical
The hollow of plate and the hollow of base plate communicate, and as shown in accompanying drawing 2-2, there is accumulating tank below base plate, and it is logical for accumulating
Cross oblique riser and the polluter of base plate accumulation.
Further, described base plate and/or tiltedly riser all can arrange multiple hole, hole can embed drainage screen,
Or macromolecular material is set, is used for adsorbing pollutant.Base plate and oblique riser arrange groove, for by the pollutant of coagulation
Drain accumulating tank below base plate.
(3) drum type brake.As shown in Figure 3, it is provided that the flowing water barb of a kind of drum type brake.Its primary structure is one and is propped up
The cylinder of support, and the multiple process bodies of rod can dismantled with flexible angle being connected on cylinder, and the storage of lower section
Long-pending groove.Described cylinder can be driven by current cause roll, it is also possible to be independently arranged power source, by set speed and/
Or both forward and reverse directions choosing turns, or it is set as fixed.The described tangent line at the body of rod and cylinders contact that processes is 0-90 °, excellent
Select 10 °, 15 °, 20 °, 25 °, 30 °, 150 °, 160 °.
May each be hollow structure as a selection, cylinder and the process body of rod, its surface has the hole by sewage, or
Person has the hole filtering sewage, and pollutant are accumulated in cylinder interior and lower section, and then cleaned.
Selecting as one, the axle center of described cylinder is slightly above surface in passage figure.As it has been described above, cylinder has rolling
Ability, but can be fixing when processing.Assuming that drum surface is provided with 10 process bodies of rod, these process the body of rod according to suitable
The numbered 1-10 of sequence, and under some state, 1-5 is positioned at (in running order) above channel surface, and 6-10 is positioned at logical
Road lower face (is in off working state).Processing the body of rod is the hollow soft body with absorbability, and in cylinder, storage has highly dense
Degree liquid, and be connected with the 1-10 process body of rod, the 1-5 process body of rod is inflated high density liquid, and No. 6-10 is not filled
Swollen.The step that 6-10 is switched to duty introduced below:
Step one: unload liquid.High density liquid in the 1-5 process body of rod is discharged, is discharged to cylinder interior, makes at No. 1-5
The reason body of rod becomes software；
Step 2: inflation cleaning.By the way of repeatedly ventilating, the high density liquid in the 1-5 process body of rod is cleaned out
Come；In cylinder interior, the high density liquid of release in step one is collected the higher density fluid body memory of cylinder；
Step 3: angle rotates.(controller) controls rotary drum 180 °, if changing a part therein, such as 4
The individual process body of rod, then rotate 144 °, if changing 3, then rotates 108 °, if with changing 2, then rotates 72 °.That is
Sum according to the body of rod and distribution, analogize.
Step 4: inflation.By corresponding high density liquid injection device, high density liquid is injected 6-10 process bar
In body.So far, the process body of rod of work is adjusted to the 6-10 process body of rod.
Above-mentioned steps one to four, need controller, aerating pipe, liquid-filling pipe, motor, brush good fit.
In above-mentioned (1)-(3), all of mode can mutually be used for reference and replace, and is not introducing one by one, this
Field personnel should know other various ways of existence.In above-mentioned (1)-(3), all material all has Anticorrosive Character, especially
It is to be prevented from specific sewage specific composition or the corrosion, erosion of process material.
Embodiment 4:
The present embodiment is implemented on the basis of previous embodiment 1 and/or 2 and/or 3, and it is a kind of special mainly to introduce
Stirring device, changing middle stirring device can synthesize one with oxygen injection unit, saves space and material, and application is the most extensive.
As shown in Figure 4, a kind of special stirring device, a bottom (and sidewall) is the half-pipe body of hollow, half-pipe
Some air-vents (can be that matrix form is uniform), air-vent and interior hollow section is laid according to certain/certain rule bottom body
Communicate, be a sealed disc below each air-vent, be that a sustainable sealed disc moves up and down below sealed disc
Moving telescopic portion.
On the sidewall (or bottom) of U-shaped hollow cell body, it is provided with baroceptor, gas pump, current meter, source of the gas.Gas
Source uses noble gas.
Described moving telescopic portion can be the conventional structures such as jack.The effect in moving telescopic portion be by move down
Dynamic so that air-vent is opened or sealed, and moving telescopic portion comprises pressure transducer, for by monitoring disk and air-vent limit
Pressure between edge, judges that whether sealed disc is by vent seal.
Above-mentioned stirring device be suitable for large-area, stir uniformly, work process is as follows:
Original state is sealed disc and vent seal state.Source of the gas is controlled to hollow cavity input by controlling device
Noble gas, monitors baroceptor, treats that pressure reaches requirement, then fall moving telescopic portion, Continuous aeration, keep air pressure sensing
Device monitor value interior fluctuation normal range.
Particularly, stirring device can also be integrated with oxygen injection device: adds oxygen or sky in above-mentioned stirring device
Gas input pipe, source of oxygen or air source, a switch, it is achieved oxygen (air) and the switching of noble gas.When needs are passed through
During oxygen, rise moving telescopic portion, close air-vent, close inert gas source input, be switched to source of oxygen, input gas, prison
Survey the numerical value of baroceptor, after requirement to be achieved, fall moving telescopic portion, continue oxygen supply, keep baroceptor monitor value
Fluctuation in normal range.Now, not only achieve and puddle effect, aeration can be realized again, kill two birds with one stone, be skillfully constructed, structure letter
Single, effect is notable.
Described noble gas, in addition to referring to the noble gas that chemical field is conventional, also refers in particular to: at entirety
For each course of reaction of reason system, each chemical composition, do not make the gas that any chemical composition changes.Concrete for one
For pending water source and processing method, noble gas is concrete, and grasped by technical staff.
Embodiment 5:
The present embodiment be previous embodiment 1,2,3,4 one of any or any the two, three, the basis of combination of four
Upper enforcement, mainly introduce the specific configuration of a kind of comprehensive sewage-treatment plant.
Also include primary treatment device, two stage treatment device.Described primary treatment device, two stage treatment device are arranged on
Before input unit, belong to the pretreatment unit processing pond portion on the whole.
Being two stage treatment device after primary treatment device, function is to separate solid-liquid.
Primary treatment device, including greasy dirt isolating construction, the settlement separate structure of solid constituent, solid dirty delivery section.
Described greasy dirt isolating construction, carries out cursory separation to the greasy dirt in sewage；
The settlement separate structure of described solid constituent, carries out settlement separate to solid constituent in sewage；
Gu dirty delivery section, it is respectively connected to primary treatment device and two stage treatment device, by solid therein, floccule, mud
Shape thing is collected and is transferred out.Gu dirty delivery section, the function also having is to make the settlement separate structure sediment of solid constituent isolate
Solid constituent be detained and be allowed to solubilized.
Particularly, Gu what dirty delivery section and other structures in primary treatment device were to cooperate with or were connected to, the order of connection
Can be: sewage injection unit, cell body, solid dirty delivery section, cell body is installed greasy dirt isolating construction, the settlement separate knot of solid constituent
Structure.Sewage injection unit makes sewage keep standing, and makes greasy dirt cursory separation from sewage.Cell body makes solid portion settle from sewage
Separate.Gu dirty delivery section comprises power section, it can be motor.
The principle of the settlement separate structure of greasy dirt isolating construction, solid constituent is to process the difference in specific gravity of composition in water according to it.
Through process and the transport of solid dirty delivery section, can make to be occurred solubilized by settlement separate solid constituent, thus
In biological treatment device or similar processing means, nitrogen, phosphorus composition can be carried out bioanalysis etc. and remove, and pass through
Solubilized and the supplementary required organic components of solid constituent, by with being applied in combination of other processing meanss, it is possible to have
The removal organic dirt of effect, nitrogen compound, phosphorus compound, it is possible to reduce the burden of aftertreatment device, stablize, obtain efficiently
Recycled water and/or can the clean water of harmless emission.
Sewage after primary treatment device processes flows into two stage treatment device.
Two stage treatment device major function is solid, liquid separation, it is possible to the residual foreign material processed in water are carried out physics
Separate and remove, and the process water eliminating residual foreign material is sent to hoard device, standby, treat that biological treatment device etc. processes dress
Put process further.
Sewage collecting after primary treatment device and two stage treatment device enters to hoard device (buffer unit), for intelligence
Type/comprehensive/biotype water treatment facilities processes.
Enter at two stage treatment device and hoard setting " flowing water barb " on the transport water channel of device (buffer unit).
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention, for the skill of this area
For art personnel, the present invention can have various modifications and variations.All within the spirit and principles in the present invention, that is made any repaiies
Change, equivalent, improvement etc., should be included within the scope of the present invention.
Claims (7)
1. an environmental water treatment facilities, including: input unit, process pond portion, output unit, desilting portion, it is characterised in that: described
Input unit, be responsible for the introducing of pending water source is processed pond portion；Described process pond portion, is responsible for carrying out the water source of input respectively
Class processes；Described output unit, is responsible for the water output that will be disposed；Described desilting portion, be responsible for by silting transfer or
Process；Processed water source circulates between pond portion, output unit, desilting portion in input unit, process, and described water source includes source of sewage
And the intermediate state water source being partly processed or processing completely.
2. according to a kind of environmental water treatment facilities described in claim 1, it is characterised in that: described input unit includes: dynamic
Power source, straight defeated pipeline, buffer unit, passage；Described power source provides power, promotes water source to flow；Described straight defeated pipeline is
Source of sewage pipeline outside Jie Ruing, is the importation of whole system；Interim and/or short for water source of described buffer unit
Phase stores；Described passage is the pipe section for source of sewage importing processes pond portion；Described process pond portion, including anaerobic groove
Oxygen groove some, logical is some, oxygen injection device, stirring device, drainage device, sensor group, power packages, central processing unit portion；Described
Central processing unit portion include data monitoring portion, control portion, speed regulation section.
3. according to a kind of environmental water treatment facilities described in claim 2, it is characterised in that: in described process pond portion or defeated
Go out portion's afterbody also to have: reactor group；Described reactor group, including bio-aeration reactor, it is provided that light heterotrophism is micro-
Biota, supporting have to bio-aeration reactor provide described in become nutrient substance that light heterotrophic microorganism group uses and organic
The structure of carbon substrate matter, current in formation；Described reactor group various kinds of sensors, controller connect.
4. according to a kind of environmental water treatment facilities described in claim 3, it is characterised in that: at the passage of described input unit
On, or on the passage of output unit, arrange " flowing water barb "；Described " flowing water barb " structure is: include that one is supported
Cylinder, and the multiple process bodies of rod can dismantled with flexible angle being connected on cylinder, and the accumulating tank of lower section；
Described cylinder can be driven by current and cause rolling, it is also possible to be independently arranged power source, by the speed and/or positive and negative set
Direction choosing turns, or is set as fixed；The described angle processing the tangent line at the body of rod and cylinders contact is 10 °, 15 °,
One of 20 °, 25 °, 30 °, 150 °, 160 °；Cylinder and the process body of rod are all hollow structures, and its surface has the hole by sewage,
Or having the hole filtering sewage, pollutant are accumulated in cylinder interior and lower section, and then cleaned.
5. according to a kind of environmental water treatment facilities described in claim 4, it is characterised in that: described process pond portion includes one
Planting and process reaction member, it is made up of the logical oxygen groove of two anaerobic grooves and three；The described some grooves processing reaction member are arranged side by side
Arrange, groove arranges stirring device, there is between groove and groove aquaporin；One or both of anaerobic groove carries out denitration reaction,
Later is led to and is arranged film unit inside oxygen groove；Described stirring device has driver element, and accepts the control in control portion；Described
The sensor group processed in the portion of pond, there is multiple sensors: acidity-basicity sensor, oxidation-reduction potential sensor, dissolved oxygen
Sensor, electric conductivity value sensor；The described oxygen injection device processed in the portion of pond, injects oxygen in logical oxygen groove；Described
Process and pond portion has for going dephosphorization to arrange: flocculant groove, and flocculant syringe；Described flocculant syringe
Accept the control of controller.
6. the method for the environmental water treatment facilities used described in claim 5, it is characterised in that: by described reaction
The step processing sewage of still group is:
(1) nutrient substance used to the light heterotrophic microorganism group that becomes described in the offer of bio-aeration reactor and organic carbon substrate matter,
Current in formation；
(2) light heterotrophic microorganism group is cultivated different so that this nutrient substance at least some of and organic carbon substrate matter are changed into light
Supporting micropopulation, on this, current and the light heterotrophic microorganism group that becomes collectively form the lower current of bio-aeration reactor；
(3) lower current are transferred to defecation tank from bio-aeration reactor, current under concentrating in defecation tank, form low-solid content
Thing and high solids content thing, at least one being exposed in intensity and wavelength by the light heterotrophic microorganism group that becomes described in making be enough to make this
The light heterotrophic microorganism group that becomes moves apart and makes this light heterotrophic microorganism group that becomes light that becomes carry out this concentration from concentrating under the light source of light source
Process, wherein makes this light heterotrophic microorganism group that becomes concentrate to form high solids content thing；
(4) dehydration of high solids content thing is formed concentrated biological to stick with paste；Processing low-solid content thing is to form treated discharge current.
7. the method for the environmental water treatment facilities used described in claim 4 or 5, it is characterised in that: include that one is cut
Changing the method processing the body of rod, cylinder has roll capability, is fixing when processing, when drum surface is provided with 10 process bars
Body, these process the most numbered 1-10 of the body of rod, and under some state, 1-5 is positioned at above channel surface, 6-10
It is positioned at below channel surface；Processing the body of rod is the hollow soft body with absorbability, and in cylinder, storage has high density liquid, and
Being connected with the 1-10 process body of rod, the 1-5 process body of rod is inflated high density liquid, and No. 6-10 is not inflated；By No. 6-10
Processing the body of rod switches to the step of duty as follows:
Step one: unload liquid；High density liquid in the 1-5 process body of rod is discharged, is discharged to cylinder interior, makes 1-5 process bar
Body becomes software；
Step 2: inflation cleaning；By the way of repeatedly ventilating, the high density liquid in the 1-5 process body of rod is cleared；
In cylinder interior, the high density liquid of release in step one is collected the higher density fluid body memory of cylinder；
Step 3: angle rotates；Controlling rotary drum 180 °, if changing a part therein, then rotating 72 ° of respective corners
Degree；Respective angles, according to processing the sum of the body of rod and distribution, calculates；
Step 4: inflation；By corresponding high density liquid injection device, high density liquid is injected the 6-10 process body of rod
In；So far, the process body of rod of work is adjusted to the 6-10 process body of rod.
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| CN201610777880.2A CN106277322B (en) | 2016-08-30 | 2016-08-30 | A kind of ecotype water treatment facilities and processing method |
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| CN201610777880.2A CN106277322B (en) | 2016-08-30 | 2016-08-30 | A kind of ecotype water treatment facilities and processing method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109264870A (en) * | 2018-11-06 | 2019-01-25 | 上海勘测设计研究院有限公司 | Current wetland sewage disposal system |
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|---|---|---|---|---|
| CN2439441Y (en) * | 2000-08-16 | 2001-07-18 | 张鑫珩 | Unit lifting, variable micro-hole and anti-counter turning type aerator |
| CN2468556Y (en) * | 2001-03-23 | 2002-01-02 | 戴之荷 | High density spiral flow flocculation device |
| CN102438443A (en) * | 2009-03-20 | 2012-05-02 | 藻类科学公司 | System and method for treating wastewater via phototactic heterotrophic microorganism growth |
| CN202898160U (en) * | 2011-06-17 | 2013-04-24 | 旭化成化学株式会社 | Sewage treatment device |
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