CN108569745A - A kind of cyanophycean toxin processing unit and blue-green algae disposing device - Google Patents
A kind of cyanophycean toxin processing unit and blue-green algae disposing device Download PDFInfo
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- CN108569745A CN108569745A CN201810672792.5A CN201810672792A CN108569745A CN 108569745 A CN108569745 A CN 108569745A CN 201810672792 A CN201810672792 A CN 201810672792A CN 108569745 A CN108569745 A CN 108569745A
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- pipe
- reative cell
- column casing
- nozzle
- processing unit
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- 241000192700 Cyanobacteria Species 0.000 title claims abstract description 96
- 239000003053 toxin Substances 0.000 title claims abstract description 83
- 231100000765 toxin Toxicity 0.000 title claims abstract description 83
- 238000012545 processing Methods 0.000 title claims abstract description 75
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 69
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 57
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 19
- 239000001301 oxygen Substances 0.000 claims abstract description 19
- 239000007921 spray Substances 0.000 claims description 31
- 239000010453 quartz Substances 0.000 claims description 15
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 15
- 238000005192 partition Methods 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 11
- 238000003860 storage Methods 0.000 claims description 11
- 230000000694 effects Effects 0.000 abstract description 65
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 112
- 210000004027 cell Anatomy 0.000 description 104
- 210000002421 cell wall Anatomy 0.000 description 23
- 230000008859 change Effects 0.000 description 19
- 230000001105 regulatory effect Effects 0.000 description 10
- 239000007787 solid Substances 0.000 description 10
- 230000001276 controlling effect Effects 0.000 description 9
- 230000008676 import Effects 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- 241000195493 Cryptophyta Species 0.000 description 8
- SRUWWOSWHXIIIA-UKPGNTDSSA-N Cyanoginosin Chemical compound N1C(=O)[C@H](CCCN=C(N)N)NC(=O)[C@@H](C)[C@H](C(O)=O)NC(=O)[C@H](CC(C)C)NC(=O)[C@H](C)NC(=O)C(=C)N(C)C(=O)CC[C@H](C(O)=O)N(C)C(=O)[C@@H](C)[C@@H]1\C=C\C(\C)=C\[C@H](C)[C@@H](O)CC1=CC=CC=C1 SRUWWOSWHXIIIA-UKPGNTDSSA-N 0.000 description 8
- 230000006378 damage Effects 0.000 description 8
- 230000036541 health Effects 0.000 description 8
- 108010067094 microcystin Proteins 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 239000002344 surface layer Substances 0.000 description 8
- 241000192710 Microcystis aeruginosa Species 0.000 description 7
- 238000010521 absorption reaction Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000000739 chaotic effect Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 241000238578 Daphnia Species 0.000 description 4
- 241001465754 Metazoa Species 0.000 description 4
- 230000006837 decompression Effects 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- 150000004676 glycans Chemical class 0.000 description 4
- 230000002045 lasting effect Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000012544 monitoring process Methods 0.000 description 4
- 210000004400 mucous membrane Anatomy 0.000 description 4
- 235000015097 nutrients Nutrition 0.000 description 4
- 229920001282 polysaccharide Polymers 0.000 description 4
- 239000005017 polysaccharide Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000002537 cosmetic Substances 0.000 description 2
- 230000001351 cycling effect Effects 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000002158 endotoxin Substances 0.000 description 2
- 238000012851 eutrophication Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 230000035558 fertility Effects 0.000 description 2
- 210000003495 flagella Anatomy 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 230000003834 intracellular effect Effects 0.000 description 2
- 239000002101 nanobubble Substances 0.000 description 2
- 230000029553 photosynthesis Effects 0.000 description 2
- 238000010672 photosynthesis Methods 0.000 description 2
- 230000000243 photosynthetic effect Effects 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 239000002574 poison Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 230000003252 repetitive effect Effects 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000013022 venting Methods 0.000 description 2
- 241001062009 Indigofera Species 0.000 description 1
- 230000018199 S phase Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 238000001132 ultrasonic dispersion Methods 0.000 description 1
- 238000009827 uniform distribution Methods 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
- C02F1/325—Irradiation devices or lamp constructions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/2366—Parts; Accessories
- B01F23/2368—Mixing receptacles, e.g. tanks, vessels or reactors, being completely closed, e.g. hermetically closed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
- B01F23/23761—Aerating, i.e. introducing oxygen containing gas in liquids
- B01F23/237613—Ozone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/712—Feed mechanisms for feeding fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/7179—Feed mechanisms characterised by the means for feeding the components to the mixer using sprayers, nozzles or jets
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/305—Treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/78—Details relating to ozone treatment devices
- C02F2201/782—Ozone generators
-
- 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
- C02F2301/06—Pressure conditions
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Physical Water Treatments (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The present invention relates to a kind of cyanophycean toxin processing units, it includes reative cell and ozone generator, the reative cell is equipped with the water inlet pipe and outlet pipe communicated with the reative cell, ultraviolet radiator is equipped in the reative cell, the ozone generator is equipped with for the ozone ingress pipe of delivery of ozone into the reative cell and the airway for conveying oxygen into the ozone generator.This cyanophycean toxin processing unit is with ultraviolet radiator and ozone treatment cyanophycean toxin, and processing cost is low, energy consumption is low, and processing water is big, and secondary pollution is small, and strong applicability, treatment effect is reliable and stable, and operation and maintenance are simple, technical maturity.The invention further relates to a kind of blue-green algae disposing devices, solve the bad technical problem of cyanobacteria treatment effect in the prior art.
Description
Technical field
The present invention relates to cyanobacteria processing technology fields, more particularly, to a kind of cyanophycean toxin processing unit and cyanobacteria processing dress
It sets.
Background technology
Body eutrophication is increasingly becoming a great environmental problem for influencing the social people's livelihood at present, water quality can be caused to dislike
Change, destroys ecological environment.Wherein cyanobacterial bloom is a characteristic feature of eutrophication water, and algae removal technology exists both at home and abroad at present
When handling cyanobacteria, it will usually its cell wall is smashed, its toxin can not be handled when encountering the cyanobacteria for having toxin, and cyanobacteria
The cell wall rupture of cell can cause the toxin (such as Microcystin) in Cells of Blue-green Algae to flow out, and toxin is dissolved in water, causes water
Body secondary pollution brings hidden danger to health, while after the toxin release in Cells of Blue-green Algae, toxin is dissolved in water, decomposes and accelerates,
It rots to accelerate, proliferation is accelerated, and to generate carcinogen, water body gives out foreign odor, pollutes environment.
Such as ultrasonic dispersion apparatus, it is the cell wall for smashing Cells of Blue-green Algae by ultrasonic in processing cyanobacteria, makes cyanobacteria
The cell wall of cell becomes ghost, and toxicant is free in water, does not adopt an effective measure and eliminates toxin, causes water body
Secondary pollution brings hidden danger to health.In addition the cyanobacteria treatment effect of existing blue-green algae disposing device is bad.
Invention content
The purpose of the present invention is to provide a kind of cyanophycean toxin processing unit, to solve in the prior art not eliminating indigo plant
The technical issues of algae toxin.
The above-mentioned technical problem of the present invention is mainly to be addressed by following technical proposals：A kind of cyanophycean toxin processing
Device, includes reative cell and ozone generator, and the reative cell is equipped with the water inlet pipe communicated with the reative cell and goes out
Water pipe, the reative cell is interior to be equipped with ultraviolet radiator, and the ozone generator is equipped with for being conveyed into the reative cell
The ozone ingress pipe of ozone and for into the ozone generator convey oxygen airway.
In practical application, can passing through existing blue-green algae disposing device, treated that liquid is passed through reative cell by water inlet pipe
It is interior, then irradiated by ultraviolet radiator, elimination is dissolved in liquid endotoxin, while oxygen is converted into ozone by ozone generator, and will be smelly
Oxygen, which imports, forms micro air bubble, that is, nano bubble in reative cell, generate negative pressure and mixed with liquid, to reach processing cyanobacteria poison
The effect of element, avoids toxin from being dissolved in water, causes secondary pollution of water, hidden danger is brought to health.In addition cyanophycean toxin is handled
Device is with ultraviolet radiator and ozone treatment cyanophycean toxin, and processing cost is low, energy consumption is low, and processing water is big, and secondary pollution is small, fits
Strong with property, treatment effect is reliable and stable, and operation and maintenance are simple, technical maturity.
Wherein, the interface of ozone ingress pipe and reative cell is equipped with two or more, and ozone ingress pipe is through reaction
Room, and stretch into reative cell.Ultraviolet radiator can be the LED lamp of internal battery or external power supply, can be covered with outside it
Transparent watertight set.The setting of transparent watertight set can improve durability when quartz burner directly uses under water, improve cyanobacteria
The service life of toxin processing unit.
Preferably, the reative cell is the cylindrical and described reative cell include one side into the left-hand cylinder body of opening setting and
Right end cap, the right end cap lid is closed can constitute closed container when on the left-hand cylinder body with the left-hand cylinder body.
Wherein, left-hand cylinder body and right end cap are to be detachably connected, and include but not limited to be bolted.Reative cell is cylinder,
Not only material, it is simple in structure, it is easy to process, and reative cell be cylinder, in the unit interval can by the ability bigger of water,
And the tube wall uniform force of reative cell, it is not easy to deform.
Preferably, the ultraviolet radiator includes vitalight lamp and quartz burner, the vitalight lamp is set to institute
It states on the inner wall of reative cell, fixed strut is convexly equipped on the right end cap, the quartz burner is set on the fixed strut.
In addition, fixed strut and right end cap are at coaxial arrangement.Wherein quartz burner is low pressure lamp, and sudden and violent in ultraviolet light
Dew amount is 1000mJ/cm2The effect for handling cyanophycean toxin is best.
Ultraviolet radiator includes vitalight lamp and quartz burner, vitalight lamp be equipped with two or more and it is mutual
It is arranged at interval, and is evenly distributed on the inner wall of reative cell, the axis of vitalight lamp and reative cell is ultraviolet at being vertically arranged
Line fluorescent tube is equipped with two or more and is mutually arranged at interval, and is evenly distributed on fixed strut, quartz burner
Axis is coaxially disposed with reative cell so that can adequately be handled by the liquid of reative cell, avoids omitting, cause water body
Secondary pollution makes it bring hidden danger to health.
Preferably, the airway include with the first airway for communicating on the outside of the reative cell and with
The second airway that the reative cell communicates, second airway is through the side wall of the left-hand cylinder body and close
The right end cap, the ozone ingress pipe through the left-hand cylinder body left end wall and with the right end cap at being oppositely arranged, it is described
Ozone ingress pipe is located at the lower section of second airway.
In practical application, ozone becomes oxygen again after reaction in reative cell and is returned to by the second airway
Ozone generator, then ozone is converted thereof by ozone generator, it continues on through and is sent into reative cell by ozone ingress pipe, processing is blue
Algae toxin.Second airway runs through the left end of left-hand cylinder body through the side wall and close right end cap, ozone ingress pipe of left-hand cylinder body
Wall and with right end cap at being oppositely arranged, ozone ingress pipe is located at the lower section of the second airway, ensure that the second oxygen import
Pipe and ozone ingress pipe and the distance between reative cell and interface difference and difference in height, are conducive to the reflux of oxygen, avoid ozone
It is passed straight back in ozone generator.
In addition, water inlet pipe is equipped with the solenoid valve for regulating and controlling flow rate of liquid in water inlet pipe, outlet pipe is equipped with drain valve.
Water inlet pipe is equipped with the pipeline tachymeter for monitoring flow rate of liquid in water inlet pipe.
Since cyanophycean toxin processing unit can be used cooperatively with other cyanobacteria processing equipments, but pass through at other cyanobacterias
Managing equipment, treated that fluid flow is larger, and flow velocity is very fast, and cyanophycean toxin processing unit needs a more slow flow velocity,
To ensure the abundant irradiation time of ultraviolet light, toxin can be completely eliminated, therefore cyanophycean toxin processing unit is by being arranged electricity
Magnet valve, to reach slowing effect, keeps its treatment effect more preferable for regulating and controlling flow rate of liquid and flow in water inlet pipe.And outlet pipe
On drain valve setting, the switch of outlet pipe can be controlled, to adapt to actual liquid processing procedure, for example, close outlet pipe
To lengthen the cyanophycean toxin processing time of ultraviolet light, or opens outlet pipe and handled with the cyanophycean toxin for accelerating ultraviolet light.Pipeline
The setting of tachymeter for monitoring flow rate of liquid in water inlet pipe in real time, and is converted into electric signal and feeds back to set on water inlet
Solenoid valve on pipe, the flow velocity for liquid in pipe of being intake by solenoid valve adjust automatically, avoids flow rate of liquid in water inlet pipe too fast so that
The abundant irradiation time of ultraviolet light is insufficient, and treatment effect is bad.
The present invention also aims to provide a kind of blue-green algae disposing device, to solve cyanobacteria treatment effect in the prior art
Bad technical problem.
The above-mentioned technical problem of the present invention is mainly to be addressed by following technical proposals：A kind of cyanobacteria processing dress
It sets, including pressurization sinuous flow mixing apparatus and above-mentioned cyanophycean toxin processing unit, the pressurization sinuous flow mixing apparatus includes two
Closed column casing, force (forcing) pump and the pipette on the force (forcing) pump and outlet tube are held, is equipped with and institute in the column casing
The hollow pipe that column casing inner cavity communicates is stated, the hollow pipe is equipped with can carry out the nozzle that spray is poured to the column casing inner surface, institute
The column casing one end stated is connected with the outlet tube, is equipped with efferent duct on an opposite end, and the efferent duct passes through with the water inlet pipe
Connecting tube connects.
The present invention connects pressurization sinuous flow mixing apparatus with cyanophycean toxin processing unit by connecting tube, is used cooperatively, first
First cyanobacteria is handled using sinuous flow, then cyanophycean toxin is effectively treated so that cyanobacteria treatment effect is more preferable, and treatment effect is stablized
Reliably.
Wherein, it can also be the nozzle being convexly equipped on hollow pipe that nozzle, which can be through-hole,.Hollow pipe is communicated with column casing inner cavity,
I.e. hollow pipe is equipped with opening, and column liquid within the cartridge can be entered by opening in hollow pipe.Opening can be through-hole or hollow
Tube end is arranged at opening.
In actual treatment liquid, liquid to be processed is entered into force (forcing) pump pressurization through pipette, then send by outlet tube
Enter in column casing；Liquid through being overpressurized flows in column casing, and carrying out spray to column casing inner surface via nozzle again by hollow pipe pours
Form sinuous flow.It is internal that there is certain impact force to be formed by impact less than injection again with the sinuous flow that the liquid of pressurization is formed
Power is poured when processed liquid carries out spray by nozzle to column casing inner surface, generates certain collision, processed liquid dispersion
Come, but convergence form new sinuous flow, continue through hollow pipe again via nozzle to column casing inner surface carry out spray pour to be formed it is new
Sinuous flow, repetitive cycling flowing can be to a certain degree to generate a steady, lasting impact force to processed liquid
Upper segregating population cell, thus first using pressurization sinuous flow mixing apparatus both can it is steady by sinuous flow, constantly by groups such as cyanobacterias
Body cell becomes the individual cells of dispersion, can effectively control the water quality disaster of the groups such as cyanobacterial bloom outburst.And produced by sinuous flow
Impact force it is more steady, continue, can be small to the impact of the cell wall of Cells of Blue-green Algae and continue, can protect to a certain extent
The integrality for demonstrate,proving the cell wall of Cells of Blue-green Algae avoids its internal toxin outflow.
In addition, Microcystis aeruginosa, is the group's eucaryotic cell structure surrounded by polysaccharide mucous membrane, and there is gas vesica inside it.
Therefore Microcystis aeruginosa avoids the ability of the animal predation of planktonic organism, photosynthetic ability, carbonate absorption compared with other algae
Ability, fertility is more outstanding, and the present apparatus can destroy its polysaccharide mucous membrane, can be by planktonic organisms such as daphnias
It is edible, while destroying it and administering the gas vesica of surface layer movement, Microcystis aeruginosa surface layer emersion and bottom movement are avoided, to eliminate
The photosynthesis and carbon dioxide absorption function of its surface layer emersion.The bottom nutrients uptake ability after bottom movement is eliminated, into
And eliminate the nutrients uptake ability for moving horizontally ability for blowing stream after being moved based on surface layer.
Preferably, the water inlet pipe is located at the lower section of the efferent duct, there are two the cyanophycean toxin processing unit is set
Or it is more than two, and the adjacent cyanophycean toxin processing unit is connected by the water inlet pipe with the outlet pipe, Ge Gesuo
State cyanophycean toxin processing unit at etc. high settings.
Water inlet pipe is located at the lower section of efferent duct, i.e. pressurization sinuous flow mixing apparatus and cyanophycean toxin processing unit has centainly
Difference in height, and the sinuous flow mixing apparatus that pressurizes is higher than cyanophycean toxin processing unit so that cyanobacteria treatment effect is more preferable.Again by multiple
Contour cyanophycean toxin processing unit, it is ensured that comprehensive removing of cyanophycean toxin avoids omitting, causes secondary pollution of water, makes
It brings hidden danger to health.
Preferably, the column casing is divided into left chamber and right chamber, the left side by the column casing by partition panel
Chamber is connected with the outlet tube, and the right chamber is communicated with the efferent duct, and one end of the hollow pipe is arranged at opening,
The other end is at silent setting, and the hollow pipe is through the partition panel and the open end of the hollow pipe and left chamber's phase
Logical, the lower section of the left chamber is equipped with discharge pipe, and discharge tube valve is equipped on the discharge pipe, and the efferent duct is equipped with
Export tube valve.
Left chamber is as the first reative cell at this time, and right chamber is as the second reative cell, by the way that column casing is divided into two phases
The reative cell of connection had both fully comprehensively broken up group's cell in processed liquid, and can also reinforce breaing up effect.It is hollow
One end of pipe is arranged at opening, and the other end is at silent setting, open end and left chamber of the hollow pipe through partition panel and hollow pipe
It communicating, the closed end of hollow pipe is located at right chamber, then the liquid of left chamber is entered by the open end of hollow pipe in hollow pipe, by
In hollow pipe the another other end at silent setting, then hollow liquid in pipe can only be sprayed by nozzle and be poured on column casing inner surface,
It increases spray and pours dynamics, can reinforce breaing up effect.
It is equipped with discharge pipe in the lower section of left chamber, due to the effect of centrifugal force, some solids with constant weight will
It is detached from sinuous flow, is discharged from discharge pipe, the solid that can be tentatively filtered in processed liquid, for waste material to be tentatively discharged,
To reach certain clean-up effect.Wherein, discharge pipe is normally closed.The setting for exporting tube valve, tube valve being discharged, can control
It switchs to efferent duct and discharge pipe processed, to adapt to actual liquid processing procedure.Pressure-regulating valve can also be set on efferent duct, from
And control the flow velocity for the liquid for flowing into cyanophycean toxin processing unit.
Preferably, the nozzle is set in the right chamber, the nozzle is equipped with two or more, and described
At being uniformly distributed on the outer wall of the hollow pipe, spray can be carried out to the column casing inner surface by being covered with outside the nozzle pours nozzle
Mixing pipeline, be equipped with the inlet pipe through the column casing outer wall on the mixing pipeline, described inlet pipe one end with it is described mixed
It is communicated with pipeline, the other end leads on the outside of the column casing.
In practical application, air on the outside of column casing can be entered by inlet pipe in column casing due to the pressure difference inside and outside column casing.Quilt
The liquid of processing carries out spray to column casing inner surface by nozzle and pours, and is located at outside nozzle due to mixing pipeline, processed liquid
It can briefly rest on and mix in pipeline, air is sent by inlet pipe mix pipeline at this time, due to the effect of pressure, air wink
Between uniformly mixed with processed liquid.Air, which enters mixing pipeline, simultaneously can form bubble, and self-assembling formation negative pressure, cause column
Pressure change in cylinder.Therefore can by regulate and control air importing, change column casing in pressure value, cause pressurize or depressurize
Effect, to promote the treatment effect of cyanobacteria.The importing for regulating and controlling air, can be arranged solenoid valve on inlet pipe, or can be from
Air in regulation and control storeroom, which enters to mix pipeline and can form the size of bubble, starts with, for example, change the flow velocity of air, change into
The internal diameter of pipe changes the measures such as the pressure value size for storing indoor pressure value, or change force (forcing) pump.Wherein sent out through experiment
Existing, in the importing using regulation and control air, when causing effect of easing stress, the present invention is best to the treatment effect of cyanobacteria.This is because blue
The characteristic of algae itself, it is fragile in the occasion of negative pressure.
Nozzle is equipped with two or more, nozzle spray can be made to pour the sinuous flow to be formed more chaotic, to promote the present invention
Treatment effect；Nozzle is set in right chamber, is mixed pipeline and is located at outside nozzle, then sinuous flow is formed in right chamber, right chamber
It can be by set on the inlet pipe mixed on pipeline, regulating and controlling the importing of air to regulate and control the pressure change of right chamber, to cause to add
Pressure or the effect of decompression, to promote the treatment effect of the present invention.
Wherein, nozzle is at least provided with 8, and at being uniformly distributed on the outer wall of hollow pipe, to ensure to be sprayed in right chamber
Mouth vertically left and right four direction to the inner surface of column casing carry out spray pour, enable the sinuous flow in left chamber and right chamber more chaotic and
Full of column casing so that the more abundant group's cell comprehensively broken up in processed liquid of the present invention.
Furthermore it is possible to which the length that left chamber is arranged is less than the length of right chamber, left chamber is as the first reative cell at this time, just
Step is filtered the solid in processed liquid, can import gas with air storage chamber and mix.Right chamber as the second reative cell,
Sinuous flow is formed by the lasting guiding flow of 16 nozzles, fully comprehensively breaks up group's cell in processed liquid.
Preferably, further including left end cap, the left end cap is arranged the left end in the left chamber and can make the left chamber
Room is convexly equipped at least two deflectors being arranged at interval with the column casing inner wall at closed setting on the left end cap, described
Deflector is distributed using the axis of the left end cap as front at circumference array, wherein a deflector setting it is described go out
The lower section of liquid pipe and towards the outlet tube at being obliquely installed, described deflector one end is fixedly connected with the left end cap, one end
It offsets with the partition panel.
Wherein, left end cap is to be detachably connected with left chamber, includes but not limited to be bolted.The indoor hollow pipe of left chamber
On can be equipped with nozzle nozzle can not also be set, in the case where being not provided with nozzle, liquid to be treated can lead in left chamber
It crosses deflector and realizes drainage.Angle of inclination, that is, deflector of deflector and the axis angulation of outlet tube 10 ° to 75 ° it
Between, wherein 30 ° to 45 ° effects are more preferable.
It in practical application, is imported from the processed liquid that force (forcing) pump sucks from outlet tube, processed liquid is first beaten
It is arranged on the deflector at outlet tube nozzle, then liquid is flowed along column casing inner wall, is beaten on next deflector, is continued
Flowed along column casing inner wall, processed liquid circulation flows so that pressure generates continuous variation, then again by hollow pipe into
Enter right chamber.Deflector be arranged the lower section of outlet tube and towards outlet tube at being obliquely installed, i.e., in the nozzle place of outlet tube
Negative pressure is formed, contributes to the flowing of processed liquid, and Cells of Blue-green Algae is made to rupture.Deflector is using the axis of left end cap as front
It is distributed at circumference array so that the angle of inclination of deflector constantly changes, and helps to change the pressure value in column casing, causes to pressurize
Or the effect of decompression, while increasing the point of impingement of cyanobacteria, so that Cells of Blue-green Algae is ruptured, to promote the treatment effect of the present invention.
Deflector one end is fixedly connected with left end cap, and one end offsets with partition panel, reduces the flowing of processed liquid
Path so that processed liquid can only be flowed along column casing inner wall, i.e., all producing continuous pressure by deflector drainage becomes
Change, to promote the treatment effect of the present invention.
Preferably, further including snorkel and air storage chamber, the snorkel runs through the outer wall of the left chamber, and one end is leaned on
The nozzle of the nearly outlet tube, the other end are connected with the air storage chamber.
The indoor air of gas storage enters left chamber by snorkel can also form negative pressure so that Cells of Blue-green Algae is fragile, and logical
Close to the nozzle of outlet tube, i.e. the liquid distance that the air and outlet tube of snorkel importing import is closer, can quilt for tracheae one end
It imported on deflector, not only facilitates the mixing of air and liquid to be treated body, improve the dissolved oxygen value of liquid to be treated body, and
The variation that can aggravate pressure value contributes to the processing to liquid of the present invention.
It is convexly equipped on the outer wall of hollow pipe preferably, mixing pipeline, and mixes pipeline with nozzle into coaxial arrangement.
Mix pipeline be convexly equipped on the outer wall of hollow pipe, it is simple in structure, convenient for manufacture, can also extend storeroom liquid or
The reaction time of person's gas and liquid to be treated body keeps its treatment effect more preferable.Pipeline and nozzle are mixed into coaxial arrangement, that is, works as liquid
Body can be uniformly filled in when being ejected from nozzle to be mixed in pipeline so that the liquid or gas that inlet pipe is imported can be with
The reaction of liquid to be treated body is uniform, keeps its treatment effect more preferable.The height value for mixing pipeline can also be enabled to be more than the height of nozzle
Value, thus, mix pipeline when sinuous flow to column casing inner surface will be full of while spray is poured by nozzle.Wherein, it sprays
Can protruding for mouth is arranged in hollow pipe outer wall, can also be concordant with hollow pipe outer wall.
Preferably, the nozzle is convexly equipped on the outer wall of hollow pipe, and the internal diameter of nozzle along nozzle axis successively
Taper off setting, and the nozzle is on the outer wall of hollow pipe at being uniformly distributed.
Nozzle is convexly equipped on the outer wall of hollow pipe, and the internal diameter of nozzle tapers off setting, i.e. nozzle successively along the axis of nozzle
Section can be convex half cone-shaped or oppositely arranged T shapes.Nozzle is the interior table along the axis direction of nozzle to column casing
Face carries out spray and pours, and tapers off successively setting since its internal diameter pours direction along spray, then makes the circulation passage in nozzle interior gradual
Narrow, can give processed liquid certain impact force, its spray is made to pour dynamics bigger, is formed by sinuous flow with more impact
Power, so that the present invention more effectively breaks up group's cell.
Preferably, the hollow pipe and column casing, at coaxial arrangement, the axis of the nozzle is set with hollow pipe at vertical
It sets.
Hollow pipe and column casing at coaxial arrangement, the axis of nozzle with hollow pipe at being vertically arranged so that processed
Liquid is that vertical spray is poured on column casing inner surface by nozzle, so that reaction of the processed liquid by column casing inner surface
Force direction is identical as its flow direction, to the impact force maximum for making it be subject to, the present invention is enabled faster can more fully to break up
Group's cell.
Preferably, the axis of the outlet tube, efferent duct and discharge pipe is with column casing at being vertically arranged.
Outlet tube with column casing at being vertically arranged, then so that by outlet tube entering column casing after processed liquid is pressurized
When, circulating direction is identical as the direction of outlet tube, and the inner wall of processed liquid and outlet tube is avoided to generate unnecessary collision
And the pressure that venting is certain, to cause the waste of resource, but also the liquid handling effect of the present invention is bad.Efferent duct and row
Outlet pipe is all that solid or the liquid handled well are discharged out of column casing using centrifugal force, and the axis of efferent duct and discharge pipe is and column
Cylinder can make the circulating direction of solid or the liquid handled well be overlapped with the direction of power at being vertically arranged, and accelerate its circulation speed
Degree.
Preferably, the outlet tube is equipped with hydralic pressure gauge, air gauge is equipped on the outer wall of right chamber.
Hydralic pressure gauge and barometric setting can measure the pressure value in column casing in real time, so as to keep inside and outside in time
The balance of pressure avoids column casing from generating explosion, improves the service life of the present invention.Additionally, due to the effect of interior external pressure, column casing selection
Need the resistance to pressure of emphasis material, including but not limited to stainless steel.
Preferably, the pressure in the column casing is maintained between 0.1MPa-10MPa.
Pressure in column casing is not a fixed value, can be with liquid flow changing of movable property.Pressure in column casing is maintained at
Between 0.1MPa-10MPa, at this time the present invention while breaing up group's cell for individual cells to the integrality of cell wall
Protection not enough, can break up cell wall.Therefore the present invention can be applied to not only to need under this range of pressure values to solve at
The cyanobacteria of group is formed by wawter bloom harm, and can need to smash the harm that protozoic flagellum is formed by red tide.Separately
It may also adapt to need break up cell wall in some cosmetics or drug outside to enhance the occasion of absorption of human body effect.Wherein,
According to experimental data between the pressure in column casing is maintained at 0.3MPa-0.5MPa, the present invention breaks up by group's cell at this time
To keep the effect of the integrality of cell wall good while individual cells.Therefore the present invention is applied to cyanobacteria under this range of pressure values
It when processing, can will not only facilitate the mucosal damage of cyanobacteria in groups, so that cyanobacteria in groups is spread out to solve wawter bloom harm, change
Kind water quality, and the cell wall of cyanobacteria can be retained, so that cyanobacteria is still can be used as the food of aquatic animal, restores biological chain, make life
State system reaches a new balance, avoids excess processes cyanobacteria so that the ecosystem is by new strike.Furthermore cyanobacteria is thin
Cell wall does not rupture, and can avoid causing the secondary dirt of water body to avoid intracellular toxin (such as Microcystin) outflow of cyanobacteria
Dye.Therefore the present invention only need to by regulate and control column casing in pressure value may be selected by whether break up cell wall, mobility is good, can be flexible
Ground is suitable for different occasions.
Based on this, the present invention compared with original technology, have the effectively water quality disaster of the groups such as control cyanobacterial bloom outburst and
The advantages of can effectively eliminate toxin, avoiding secondary pollution of water.
Description of the drawings
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution in the prior art
Embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, in being described below
Attached drawing is some embodiments of the present invention, for those of ordinary skill in the art, before not making the creative labor
It puts, other drawings may also be obtained based on these drawings.
Attached drawing 1 is the sectional view of cyanophycean toxin processing unit of the present invention；
Attached drawing 2 is the internal structure schematic diagram of cyanophycean toxin processing unit of the present invention；
Attached drawing 3 is the sectional view of blue-green algae disposing device embodiment one of the present invention；
Attached drawing 4 is the sectional view of blue-green algae disposing device embodiment two of the present invention；
Attached drawing 5 is another structure sectional view of blue-green algae disposing device embodiment one of the present invention；
Attached drawing 6 is that the internal structure of the pressurization sinuous flow mixing apparatus right chamber of blue-green algae disposing device embodiment one of the present invention is shown
It is intended to；
Attached drawing 7 is that the internal structure of the pressurization sinuous flow mixing apparatus left chamber of blue-green algae disposing device embodiment one of the present invention is shown
It is intended to.
Reference numeral：
1- force (forcing) pumps；11- pipette；12- outlet tubes；
13- hydralic pressure gauges；2- column casings；21- partition panels；
22- left chamber；23- right chambers；24- air gauges；
25- left end caps；251- deflectors；26- snorkels；
27- air storage chambers；3- hollow pipes；31- nozzles；
32- mixes pipeline；33- inlet pipes；34- storerooms；
4- efferent ducts；41- exports tube valve；5- discharge pipes；
Tube valve is discharged in 51-；6- reative cells；61- water inlet pipes；
611- solenoid valves；612- pipeline tachymeters；62- outlet pipes；
621- is discharged tube valve；63- left-hand cylinder bodies；64- right end caps；
65- fixes strut；7- ozone generators；71- ozone ingress pipes；
72- airways；The first airways of 721-；The second airways of 722-；
8- ultraviolet radiator；81- vitalight lamps；82- quartz burners；
9- connecting tubes.
Specific implementation mode
Technical scheme of the present invention is clearly and completely described below in conjunction with attached drawing, it is clear that described implementation
Example is a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, ordinary skill
The every other embodiment that personnel are obtained without making creative work, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that term "center", "upper", "lower", "front", "rear", "vertical",
The orientation or positional relationship of the instructions such as " liquid flat ", "inner", "outside" be based on the orientation or positional relationship shown in the drawings, merely to
Convenient for the description present invention and simplify description, do not indicate or imply the indicated device or element must have a particular orientation,
With specific azimuth configuration and operation, therefore it is not considered as limiting the invention.In addition, term " first ", " second ",
" third " is used for description purposes only, and is not understood to indicate or imply relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected；It can
Can also be electrical connection to be mechanical connection；It can be directly connected, can also indirectly connected through an intermediary, Ke Yishi
Connection inside two elements.For the ordinary skill in the art, above-mentioned term can be understood at this with concrete condition
Concrete meaning in invention.
The embodiment one of cyanophycean toxin processing unit：
See that Fig. 1, Fig. 2, a kind of cyanophycean toxin processing unit include reative cell 6 and ozone generator 7, set on reative cell 6
There are the water inlet pipe 61 communicated with reative cell 6 and outlet pipe 62, is equipped with ultraviolet radiator 8 in reative cell 6, ozone generator 7 is equipped with
Oxygen for the ozone ingress pipe 71 of delivery of ozone into reative cell 6 and for conveying from oxygen to ozone generator 7 imports
Pipe 72.
In practical application, can passing through existing blue-green algae disposing device, treated that liquid is passed through reative cell by water inlet pipe
It is interior, then irradiated by ultraviolet radiator, elimination is dissolved in liquid endotoxin, while oxygen is converted into ozone by ozone generator, and will be smelly
Oxygen, which imports, forms micro air bubble, that is, nano bubble in reative cell, generate negative pressure and mixed with liquid, to reach processing cyanobacteria poison
The effect of element, avoids toxin from being dissolved in water, causes secondary pollution of water, hidden danger is brought to health.In addition cyanophycean toxin is handled
Device is with ultraviolet radiator and ozone treatment cyanophycean toxin, and processing cost is low, energy consumption is low, and processing water is big, and secondary pollution is small, fits
Strong with property, treatment effect is reliable and stable, and operation and maintenance are simple, technical maturity.
Wherein, the interface of ozone ingress pipe and reative cell is equipped with two or more, and ozone ingress pipe is through reaction
Room, and stretch into reative cell.Ultraviolet radiator can be the LED lamp of internal battery or external power supply, can be covered with outside it
Transparent watertight set.The setting of transparent watertight set can improve durability when quartz burner directly uses under water, improve cyanobacteria
The service life of toxin processing unit.
See that Fig. 1, reative cell 6 are that cylindrical and reative cell 6 includes left-hand cylinder body 63 and right end cap of the one side at opening setting
64, the lid of right end cap 64 is closed can constitute closed container when on left-hand cylinder body 63 with left-hand cylinder body 63.
Wherein, left-hand cylinder body and right end cap are to be detachably connected, and include but not limited to be bolted.Reative cell is cylinder,
Not only material, it is simple in structure, it is easy to process, and reative cell be cylinder, in the unit interval can by the ability bigger of water,
And the tube wall uniform force of reative cell, it is not easy to deform.
See that Fig. 1, Fig. 2, ultraviolet radiator 8 include vitalight lamp 81 and quartz burner 82, vitalight lamp 81 is set to anti-
On the inner wall for answering room 6, fixed strut 65 is convexly equipped on right end cap 64, quartz burner 82 is set on fixed strut 65.
In addition, fixed strut and right end cap are at coaxial arrangement.Wherein quartz burner is low pressure lamp, and sudden and violent in ultraviolet light
Dew amount is 1000mJ/cm2The effect for handling cyanophycean toxin is best.
Ultraviolet radiator includes vitalight lamp and quartz burner, vitalight lamp be equipped with two or more and it is mutual
It is arranged at interval, and is evenly distributed on the inner wall of reative cell, the axis of vitalight lamp and reative cell is ultraviolet at being vertically arranged
Line fluorescent tube is equipped with two or more and is mutually arranged at interval, and is evenly distributed on fixed strut, quartz burner
Axis is coaxially disposed with reative cell so that can adequately be handled by the liquid of reative cell, avoids omitting, cause water body
Secondary pollution makes it bring hidden danger to health.
See Fig. 1, airway 72 include the first airway 721 communicated with 6 outside of reative cell and with reative cell 6
The second airway 722 communicated, side wall and close right end cap 64 of second airway 722 through left-hand cylinder body 63 are smelly
Oxygen ingress pipe 71 runs through the left end wall of left-hand cylinder body 63 and with right end cap 64 at being oppositely arranged, and ozone ingress pipe 71 is located at the second oxygen
The lower section of ingress pipe 722.
In practical application, ozone becomes oxygen again after reaction in reative cell and is returned to by the second airway
Ozone generator, then ozone is converted thereof by ozone generator, it continues on through and is sent into reative cell by ozone ingress pipe, processing is blue
Algae toxin.Second airway runs through the left end of left-hand cylinder body through the side wall and close right end cap, ozone ingress pipe of left-hand cylinder body
Wall and with right end cap at being oppositely arranged, ozone ingress pipe is located at the lower section of the second airway, ensure that the second oxygen import
Pipe and ozone ingress pipe and the distance between reative cell and interface difference and difference in height, are conducive to the reflux of oxygen, avoid ozone
It is passed straight back in ozone generator.
In addition, water inlet pipe 61 is equipped with the solenoid valve 611 for regulating and controlling flow rate of liquid in water inlet pipe 61, set on outlet pipe 62
There is drain valve 621.Water inlet pipe 61 is equipped with the pipeline tachymeter 612 for monitoring flow rate of liquid in water inlet pipe 61.
Since cyanophycean toxin processing unit can be used cooperatively with other cyanobacteria processing equipments, but pass through at other cyanobacterias
Managing equipment, treated that fluid flow is larger, and flow velocity is very fast, and cyanophycean toxin processing unit needs a more slow flow velocity,
To ensure the abundant irradiation time of ultraviolet light, toxin can be completely eliminated, therefore cyanophycean toxin processing unit is by being arranged electricity
Magnet valve, to reach slowing effect, keeps its treatment effect more preferable for regulating and controlling flow rate of liquid and flow in water inlet pipe.And outlet pipe
On drain valve setting, the switch of outlet pipe can be controlled, to adapt to actual liquid processing procedure, for example, close outlet pipe
To lengthen the cyanophycean toxin processing time of ultraviolet light, or opens outlet pipe and handled with the cyanophycean toxin for accelerating ultraviolet light.Pipeline
The setting of tachymeter for monitoring flow rate of liquid in water inlet pipe in real time, and is converted into electric signal and feeds back to set on water inlet
Solenoid valve on pipe, the flow velocity for liquid in pipe of being intake by solenoid valve adjust automatically, avoids flow rate of liquid in water inlet pipe too fast so that
The abundant irradiation time of ultraviolet light is insufficient, and treatment effect is bad.
The embodiment one of blue-green algae disposing device：
See the above-mentioned cyanophycean toxin processing of Fig. 3, Fig. 5, Fig. 6, a kind of blue-green algae disposing device, including pressurization sinuous flow mixing apparatus
Device, pressurization sinuous flow mixing apparatus includes column casing 2, force (forcing) pump 1 and 11 and of pipette on force (forcing) pump 1 closed at both ends
Outlet tube 12, be equipped with the hollow pipe 3 communicated with 2 inner cavity of column casing in column casing 2, hollow pipe 3 be equipped with can to 2 inner surface of column casing into
The nozzle 31 that row spray is poured, 2 one end of column casing are connected with outlet tube 12, are equipped with efferent duct 4, efferent duct 4 and water inlet pipe on an opposite end
61 are connected by connecting tube 9.
The present invention connects pressurization sinuous flow mixing apparatus with cyanophycean toxin processing unit by connecting tube, is used cooperatively, first
First cyanobacteria is handled using sinuous flow, then cyanophycean toxin is effectively treated so that cyanobacteria treatment effect is more preferable, and treatment effect is stablized
Reliably.
Wherein, it can also be the nozzle being convexly equipped on hollow pipe that nozzle, which can be through-hole,.Hollow pipe is communicated with column casing inner cavity,
I.e. hollow pipe is equipped with opening, and column liquid within the cartridge can be entered by opening in hollow pipe.Opening can be through-hole or hollow
Tube end is arranged at opening.
In actual treatment liquid, liquid to be processed is entered into force (forcing) pump pressurization through pipette, then send by outlet tube
Enter in column casing；Liquid through being overpressurized flows in column casing, and carrying out spray to column casing inner surface via nozzle again by hollow pipe pours
Form sinuous flow.It is internal that there is certain impact force to be formed by impact less than injection again with the sinuous flow that the liquid of pressurization is formed
Power is poured when processed liquid carries out spray by nozzle to column casing inner surface, generates certain collision, processed liquid dispersion
Come, but convergence form new sinuous flow, continue through hollow pipe again via nozzle to column casing inner surface carry out spray pour to be formed it is new
Sinuous flow, repetitive cycling flowing can be to a certain degree to generate a steady, lasting impact force to processed liquid
Upper segregating population cell, thus first using pressurization sinuous flow mixing apparatus both can it is steady by sinuous flow, constantly by groups such as cyanobacterias
Body cell becomes the individual cells of dispersion, can effectively control the water quality disaster of the groups such as cyanobacterial bloom outburst.And produced by sinuous flow
Impact force it is more steady, continue, can be small to the impact of the cell wall of Cells of Blue-green Algae and continue, can protect to a certain extent
The integrality for demonstrate,proving the cell wall of Cells of Blue-green Algae avoids its internal toxin outflow.
In addition, Microcystis aeruginosa, is the group's eucaryotic cell structure surrounded by polysaccharide mucous membrane, and there is gas vesica inside it.
Therefore Microcystis aeruginosa avoids the ability of the animal predation of planktonic organism, photosynthetic ability, carbonate absorption compared with other algae
Ability, fertility is more outstanding, and the present apparatus can destroy its polysaccharide mucous membrane, can be by planktonic organisms such as daphnias
It is edible, while destroying it and administering the gas vesica of surface layer movement, Microcystis aeruginosa surface layer emersion and bottom movement are avoided, to eliminate
The photosynthesis and carbon dioxide absorption function of its surface layer emersion.The bottom nutrients uptake ability after bottom movement is eliminated, into
And eliminate the nutrients uptake ability for moving horizontally ability for blowing stream after being moved based on surface layer.
See that Fig. 5, water inlet pipe 61 are located at the lower section of efferent duct 4, cyanophycean toxin processing unit is equipped with two or more, and
Adjacent cyanophycean toxin processing unit is connected by water inlet pipe 61 with outlet pipe 62, and each cyanophycean toxin processing unit is set at contour
It sets.
Water inlet pipe is located at the lower section of efferent duct, i.e. pressurization sinuous flow mixing apparatus and cyanophycean toxin processing unit has centainly
Difference in height, and the sinuous flow mixing apparatus that pressurizes is higher than cyanophycean toxin processing unit so that cyanobacteria treatment effect is more preferable.Again by multiple
Contour cyanophycean toxin processing unit, it is ensured that comprehensive removing of cyanophycean toxin avoids omitting, causes secondary pollution of water, makes
It brings hidden danger to health.
See that column casing 2 is divided into left chamber 22 and right chamber 23, left chamber by Fig. 3, Fig. 5, Fig. 6, column casing 2 by partition panel 21
22 are connected with outlet tube 12, and right chamber 23 is communicated with efferent duct 4, and one end of hollow pipe 3 is arranged at opening, and the other end is set at silent
It sets, hollow pipe 3 is communicated through the open end of partition panel 21 and hollow pipe 3 with left chamber 22.The lower section of left chamber 22 is equipped with discharge
Pipe 5 is equipped with discharge tube valve 51 in discharge pipe 5, and efferent duct 4 is equipped with output tube valve 41.
Left chamber is as the first reative cell at this time, and right chamber is as the second reative cell, by the way that column casing is divided into two phases
The reative cell of connection had both fully comprehensively broken up group's cell in processed liquid, and can also reinforce breaing up effect.It is hollow
One end of pipe is arranged at opening, and the other end is at silent setting, open end and left chamber of the hollow pipe through partition panel and hollow pipe
It communicating, the closed end of hollow pipe is located at right chamber, then the liquid of left chamber is entered by the open end of hollow pipe in hollow pipe, by
In hollow pipe the another other end at silent setting, then hollow liquid in pipe can only be sprayed by nozzle and be poured on column casing inner surface,
It increases spray and pours dynamics, can reinforce breaing up effect.
It is equipped with discharge pipe in the lower section of left chamber, due to the effect of centrifugal force, some solids with constant weight will
It is detached from sinuous flow, is discharged from discharge pipe, the solid that can be tentatively filtered in processed liquid, for waste material to be tentatively discharged,
To reach certain clean-up effect.Wherein, discharge pipe is normally closed.The setting for exporting tube valve, tube valve being discharged, can control
It switchs to efferent duct and discharge pipe processed, to adapt to actual liquid processing procedure.Pressure-regulating valve can also be set on efferent duct, from
And control the flow velocity for the liquid for flowing into cyanophycean toxin processing unit.
See that Fig. 3, Fig. 5, Fig. 6, nozzle 31 are equipped with two or more, nozzle 31 is on the outer wall of hollow pipe 3 at uniform
Distribution.And nozzle 31 is set in right chamber 23, the mixing pipeline that spray is poured can be carried out to 2 inner surface of column casing by being covered with outside nozzle 31
32, the inlet pipe 33 through 2 outer wall of column casing is equipped on mixing pipeline 32,33 one end of inlet pipe is communicated with pipeline 32 is mixed, the other end
Lead on the outside of column casing.
Wherein, 33 one end of inlet pipe is communicated with pipeline 32 is mixed, and the other end can also be connected with storeroom 34.
In practical application, air on the outside of column casing can be entered by inlet pipe in column casing due to the pressure difference inside and outside column casing.Quilt
The liquid of processing carries out spray to column casing inner surface by nozzle and pours, and is located at outside nozzle due to mixing pipeline, processed liquid
It can briefly rest on and mix in pipeline, air is sent by inlet pipe mix pipeline at this time, due to the effect of pressure, air wink
Between uniformly mixed with processed liquid.Air, which enters mixing pipeline, simultaneously can form bubble, and self-assembling formation negative pressure, cause column
Pressure change in cylinder.Therefore can by regulate and control air importing, change column casing in pressure value, cause pressurize or depressurize
Effect, to promote the treatment effect of cyanobacteria.The importing for regulating and controlling air, can be arranged solenoid valve on inlet pipe, or can be from
Air in regulation and control storeroom, which enters to mix pipeline and can form the size of bubble, starts with, for example, change the flow velocity of air, change into
The internal diameter of pipe changes the measures such as the pressure value size for storing indoor pressure value, or change force (forcing) pump.Wherein sent out through experiment
Existing, in the importing using regulation and control air, when causing effect of easing stress, the present invention is best to the treatment effect of cyanobacteria.This is because blue
The characteristic of algae itself, it is fragile in the occasion of negative pressure.
Nozzle is equipped with two or more, nozzle spray can be made to pour the sinuous flow to be formed more chaotic, to promote the present invention
Treatment effect；Nozzle is set in right chamber, is mixed pipeline and is located at outside nozzle, then sinuous flow is formed in right chamber, right chamber
It can be by set on the inlet pipe mixed on pipeline, regulating and controlling the importing of air to regulate and control the pressure change of right chamber, to cause to add
Pressure or the effect of decompression, to promote the treatment effect of the present invention.
Wherein, nozzle is at least provided with 8, and at being uniformly distributed on the outer wall of hollow pipe, to ensure to be sprayed in right chamber
Mouth vertically left and right four direction to the inner surface of column casing carry out spray pour, enable the sinuous flow in left chamber and right chamber more chaotic and
Full of column casing so that the more abundant group's cell comprehensively broken up in processed liquid of the present invention.
Furthermore it is possible to which the length that left chamber is arranged is less than the length of right chamber, left chamber is as the first reative cell at this time, just
Step is filtered the solid in processed liquid, can import gas with air storage chamber and mix.Right chamber as the second reative cell,
Sinuous flow is formed by the lasting guiding flow of 16 nozzles, fully comprehensively breaks up group's cell in processed liquid.
See that Fig. 3, Fig. 6, nozzle 31 are convexly equipped on the outer wall of hollow pipe 3, and the internal diameter of nozzle 31 along nozzle 31 axis according to
The secondary setting that tapers off.
Nozzle is convexly equipped on the outer wall of hollow pipe, and the internal diameter of nozzle tapers off setting, i.e. nozzle successively along the axis of nozzle
Section can be convex half cone-shaped or oppositely arranged T shapes.Nozzle is the interior table along the axis direction of nozzle to column casing
Face carries out spray and pours, and tapers off successively setting since its internal diameter pours direction along spray, then makes the circulation passage in nozzle interior gradual
Narrow, can give processed liquid certain impact force, its spray is made to pour dynamics bigger, is formed by sinuous flow with more impact
Power, so that the present invention more effectively breaks up group's cell.Nozzle is equipped with two or more, and nozzle spray can be made to pour shape
At sinuous flow it is more chaotic, to promote the present invention treatment effect.
See Fig. 3, Fig. 6, hollow pipe 3 and column casing 2 are at coaxial arrangement, and the axis of nozzle 31 and hollow pipe 3 are at being vertically arranged.
Hollow pipe and column casing at coaxial arrangement, the axis of nozzle with hollow pipe at being vertically arranged so that processed
Liquid is that vertical spray is poured on left chamber chamber internal surface by nozzle, so that anti-work of the processed liquid by column casing inner surface
Power thrusts are identical as its flow direction, to the impact force maximum for making it be subject to, the present invention enabled faster can more fully to beat
Dissipate group's cell.
See Fig. 3, Fig. 6, the axis of outlet tube 12, efferent duct 4 and discharge pipe 5 is with column casing 2 at being vertically arranged.
Outlet tube with column casing at being vertically arranged, then so that by outlet tube entering column casing after processed liquid is pressurized
When, circulating direction is identical as the direction of outlet tube, and the inner wall of processed liquid and outlet tube is avoided to generate unnecessary collision
And the pressure that venting is certain, to cause the waste of resource, but also the liquid handling effect of the present invention is bad.Efferent duct and row
Outlet pipe is all that solid or the liquid handled well are discharged out of column casing using centrifugal force, and the axis of efferent duct and discharge pipe is and column
Cylinder can make the circulating direction of solid or the liquid handled well be overlapped with the direction of power at being vertically arranged, and accelerate its circulation speed
Degree.
See that Fig. 3, outlet tube 12 are equipped with hydralic pressure gauge 13, air gauge 24 is equipped on the outer wall of right chamber 23.
Hydralic pressure gauge and barometric setting can measure the pressure value in column casing in real time, so as to keep inside and outside in time
The balance of pressure avoids column casing from generating explosion, improves the service life of the present invention.Additionally, due to the effect of interior external pressure, column casing selection
Need the resistance to pressure of emphasis material, including but not limited to stainless steel.
See that Fig. 3, the pressure in column casing 2 are maintained between 0.1MPa-10MPa.
Pressure in column casing is not a fixed value, can be with liquid flow changing of movable property.Pressure in column casing is maintained at
Between 0.1MPa-10MPa, at this time the present invention while breaing up group's cell for individual cells to the integrality of cell wall
Protection not enough, can break up cell wall.Therefore the present invention can be applied to not only to need under this range of pressure values to solve at
The cyanobacteria of group is formed by wawter bloom harm, and can need to smash the harm that protozoic flagellum is formed by red tide.Separately
It may also adapt to need break up cell wall in some cosmetics or drug outside to enhance the occasion of absorption of human body effect.Wherein,
According to experimental data between the pressure in column casing is maintained at 0.3MPa-0.5MPa, the present invention breaks up by group's cell at this time
To keep the effect of the integrality of cell wall good while individual cells.Therefore the present invention is applied to cyanobacteria under this range of pressure values
It when processing, can will not only facilitate the mucosal damage of cyanobacteria in groups, so that cyanobacteria in groups is spread out to solve wawter bloom harm, change
Kind water quality, and the cell wall of cyanobacteria can be retained, so that cyanobacteria is still can be used as the food of aquatic animal, restores biological chain, make life
State system reaches a new balance, avoids excess processes cyanobacteria so that the ecosystem is by new strike.Furthermore cyanobacteria is thin
Cell wall does not rupture, and can avoid causing the secondary dirt of water body to avoid intracellular toxin (such as Microcystin) outflow of cyanobacteria
Dye.Therefore the present invention only need to by regulate and control column casing in pressure value may be selected by whether break up cell wall, mobility is good, can be flexible
Ground is suitable for different occasions.Such as when cyanobacteria is toxic, pressurization sinuous flow mixing apparatus can not destroy the cell of Cells of Blue-green Algae
Wall, so that it can be ingested by planktonic organisms such as daphnias, when cyanobacteria is nontoxic, pressurization sinuous flow mixing apparatus can destroy Cells of Blue-green Algae
Cell wall, so as to its can be ingested by planktonic organisms such as daphnias save the energy.And whether the present invention destroys the cell of Cells of Blue-green Algae
Wall is achieved by regulating and controlling the pressure value in column casing.The pressure value regulated and controled in column casing can be by the pressure of regulation and control force (forcing) pump
The importing of force value and regulation and control air is achieved.
Following table is that the pressurization of blue-green algae disposing device embodiment one sinuous flow mixing apparatus of the present invention is handled under 0.4MPa pressure values
The experimental result statistical form of liquid containing cyanobacteria:
Following table is the present invention processing cyanophycean toxin i.e. experimental result statistical form of Microcystin:
To the explanation of upper table：Raw water can be proliferated to field cyanobacteria, that is, Microcystis aeruginosa, cyanophycean toxin, that is, Microcystin
It can increase；Jet impact device, that is, existing blue-green algae disposing device bumps against shock plate after the injection by the thing for making raw water pressurize
Impact force can cause a part of cyanophycean toxin i.e. Microcystin to reduce；Pressurization sinuous flow mixing apparatus passes through pressurization, sinuous flow, air
It imports and mixes, cause to repeat the process depressurized of pressurizeing, to cause cyanophycean toxin i.e. Microcystin to reduce, and three days in the wild
Half is reduced after standing；Using this blue-green algae disposing device, due to the treatment with irradiation of micro air bubble and ultraviolet radiator that ozone generates,
Microcystin is reduced to 1/5th after processing, and quantitation limit or less will be disappeared in after standing 3 days in the wild.
The embodiment two of blue-green algae disposing device：
See Fig. 5, Fig. 7, further include left end cap 25, left end cap 25 is arranged in 22 left end of left chamber and left chamber 22 can be made at close
Setting is closed, at least two deflectors 251 being arranged at interval with 2 inner wall of column casing are convexly equipped on left end cap 25, deflector 251 is with a left side
The axis of end cap 25 is that front is distributed at circumference array, wherein a deflector 251 is arranged in the lower section of outlet tube 12 and direction
Outlet tube 12 is at being obliquely installed.251 one end of deflector is fixedly connected with left end cap 25, and one end offsets with partition panel 21.Further include
Snorkel 26 and air storage chamber 27, snorkel 26 runs through the outer wall of left chamber 22, and one end is close to the nozzle of outlet tube 12, the other end
It is connected with air storage chamber 27.Rest part is identical as the embodiment one of blue-green algae disposing device.
Wherein, left end cap is to be detachably connected with left chamber, includes but not limited to be bolted.The indoor hollow pipe of left chamber
On can be equipped with nozzle nozzle can not also be set, in the case where being not provided with nozzle, liquid to be treated can lead in left chamber
It crosses deflector and realizes drainage.Angle of inclination, that is, deflector of deflector and the axis angulation of outlet tube 10 ° to 75 ° it
Between, wherein 30 ° to 45 ° effects are more preferable.
It in practical application, is imported from the processed liquid that force (forcing) pump sucks from outlet tube, processed liquid is first beaten
It is arranged on the deflector at outlet tube nozzle, then liquid is flowed along column casing inner wall, is beaten on next deflector, is continued
Flowed along column casing inner wall, processed liquid circulation flows so that pressure generates continuous variation, then again by hollow pipe into
Enter right chamber.Deflector be arranged the lower section of outlet tube and towards outlet tube at being obliquely installed, i.e., in the nozzle place of outlet tube
Negative pressure is formed, contributes to the flowing of processed liquid, and Cells of Blue-green Algae is made to rupture.Deflector is using the axis of left end cap as front
It is distributed at circumference array so that the angle of inclination of deflector constantly changes, and helps to change the pressure value in column casing, causes to pressurize
Or the effect of decompression, while increasing the point of impingement of cyanobacteria, so that Cells of Blue-green Algae is ruptured, to promote the treatment effect of the present invention.
Deflector one end is fixedly connected with left end cap, and one end offsets with partition panel, reduces the flowing of processed liquid
Path so that processed liquid can only be flowed along column casing inner wall, i.e., all producing continuous pressure by deflector drainage becomes
Change, to promote the treatment effect of the present invention.The indoor air of gas storage enters left chamber by snorkel can also form negative pressure, make
It is fragile to obtain Cells of Blue-green Algae, and snorkel one end is close to the nozzle of outlet tube, the i.e. air of snorkel importing and outlet tube importing
Liquid distance is closer, can be directed on deflector, not only facilitates the mixing of air and liquid to be treated body, and raising is handled
The dissolved oxygen value of liquid, and the variation of pressure value can be aggravated, contribute to the processing to liquid of the present invention.
Finally it should be noted that：The above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations；To the greatest extent
Present invention has been described in detail with reference to the aforementioned embodiments for pipe, it will be understood by those of ordinary skill in the art that：Its according to
So can with technical scheme described in the above embodiments is modified, either to which part or all technical features into
Row equivalent replacement；And these modifications or replacements, various embodiments of the present invention technology that it does not separate the essence of the corresponding technical solution
The range of scheme.
Claims (10)
1. a kind of cyanophycean toxin processing unit, it is characterised in that：Including reative cell and ozone generator, set on the reative cell
There is the water inlet pipe and outlet pipe communicated with the reative cell, ultraviolet radiator is equipped in the reative cell, the ozone occurs
Device is equipped with for the ozone ingress pipe of delivery of ozone into the reative cell and for conveying oxygen into the ozone generator
The airway of gas.
2. cyanophycean toxin processing unit according to claim 1, it is characterised in that：The reative cell is cylindrical and described
Reative cell includes one side into the left-hand cylinder body and right end cap of opening setting, the right end cap lid close when on the left-hand cylinder body can and
The left-hand cylinder body constitutes closed container.
3. cyanophycean toxin processing unit according to claim 2, it is characterised in that：The ultraviolet radiator includes ultraviolet radiator
Bubble and quartz burner, the vitalight lamp are set on the inner wall of the reative cell, and fixed branch is convexly equipped on the right end cap
Bar, the quartz burner are set on the fixed strut.
4. cyanophycean toxin processing unit according to claim 2, it is characterised in that：The airway includes and institute
State the first airway communicated and the second airway communicated with the reative cell on the outside of reative cell, described second
Side wall and the close right end cap of the airway through the left-hand cylinder body, the ozone ingress pipe is through the left-hand cylinder body
Left end wall and with the right end cap at being oppositely arranged, the ozone ingress pipe is located at the lower section of second airway.
5. a kind of blue-green algae disposing device, it is characterised in that：Including pressurization any one of sinuous flow mixing apparatus and Claims 1-4 institute
The cyanophycean toxin processing unit stated, the pressurization sinuous flow mixing apparatus include column casing closed at both ends, force (forcing) pump and are set to
Pipette on the force (forcing) pump and outlet tube, the column casing is interior equipped with the hollow pipe communicated with the column casing inner cavity, described
Hollow pipe be equipped with and can carry out the nozzle that pours of spray, described column casing one end and the outlet tube phase to the column casing inner surface
Even, it is equipped with efferent duct on an opposite end, the efferent duct is connect with the water inlet pipe by connecting tube.
6. blue-green algae disposing device according to claim 5, it is characterised in that：The water inlet pipe is located under the efferent duct
Side, the cyanophycean toxin processing unit is equipped with two or more, and the adjacent cyanophycean toxin processing unit passes through institute
Water inlet pipe is stated with the outlet pipe to be connected, each cyanophycean toxin processing unit at etc. high settings.
7. blue-green algae disposing device according to claim 6, it is characterised in that：The column casing is by partition panel by the column
Cylinder is divided into left chamber and right chamber, and the left chamber is connected with the outlet tube, the right chamber and the efferent duct
Communicate, one end of the hollow pipe is arranged at opening, the other end at silent setting, the hollow pipe through the partition panel and
The open end of the hollow pipe is communicated with the left chamber, and the lower section of the left chamber is equipped with discharge pipe, on the discharge pipe
Equipped with discharge tube valve, the efferent duct is equipped with output tube valve.
8. blue-green algae disposing device according to claim 7, it is characterised in that：The nozzle is set in the right chamber, institute
The nozzle stated is equipped with two or more, and the nozzle on the outer wall of the hollow pipe at being uniformly distributed, the nozzle
Outer be covered with can carry out the mixing pipeline that spray is poured to the column casing inner surface, be equipped on the mixing pipeline and run through the column casing
The inlet pipe of outer wall, described inlet pipe one end are communicated with the mixing pipeline, and the other end leads on the outside of the column casing.
9. blue-green algae disposing device according to claim 8, it is characterised in that：Further include left end cap, the left end cap setting
The left chamber left end and the left chamber can be made at closed setting, be convexly equipped on the left end cap at least two with it is described
The deflector that column casing inner wall is arranged at interval, the deflector are distributed using the axis of the left end cap as front at circumference array,
Wherein, a deflector be arranged the lower section of the outlet tube and towards the outlet tube at being obliquely installed, the water conservancy diversion
Plate one end is fixedly connected with the left end cap, and one end offsets with the partition panel.
10. blue-green algae disposing device according to claim 9, it is characterised in that：Further include snorkel and air storage chamber, it is described logical
Tracheae runs through the outer wall of the left chamber, and one end, close to the nozzle of the outlet tube, the other end is connected with the air storage chamber.
Priority Applications (2)
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| CN201810672792.5A CN108569745B (en) | 2018-06-26 | 2018-06-26 | Blue algae toxin processing device and blue algae processing device |
| PCT/CN2019/092697 WO2020001419A1 (en) | 2018-06-26 | 2019-06-25 | Pressurized turbulent mixing device, liquid treatment method, cyanobacteria treatment device and cyanobacteria treatment method |
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| CN201810672792.5A CN108569745B (en) | 2018-06-26 | 2018-06-26 | Blue algae toxin processing device and blue algae processing device |
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| CN108569745B CN108569745B (en) | 2024-05-03 |
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