CN108557964A - A kind of pressurization sinuous flow mixing apparatus - Google Patents
A kind of pressurization sinuous flow mixing apparatus Download PDFInfo
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- CN108557964A CN108557964A CN201810706018.1A CN201810706018A CN108557964A CN 108557964 A CN108557964 A CN 108557964A CN 201810706018 A CN201810706018 A CN 201810706018A CN 108557964 A CN108557964 A CN 108557964A
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- column casing
- nozzle
- liquid
- sinuous flow
- pressurization
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- 238000002156 mixing Methods 0.000 title claims abstract description 45
- 239000007921 spray Substances 0.000 claims abstract description 38
- 238000005192 partition Methods 0.000 claims description 14
- 238000003860 storage Methods 0.000 claims description 13
- 239000004744 fabric Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 143
- 241000192700 Cyanobacteria Species 0.000 abstract description 49
- 230000000694 effects Effects 0.000 abstract description 49
- 239000007789 gas Substances 0.000 abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 13
- 239000003814 drug Substances 0.000 abstract description 7
- 239000002537 cosmetic Substances 0.000 abstract description 6
- 239000006185 dispersion Substances 0.000 abstract description 6
- 210000004027 cell Anatomy 0.000 description 55
- 210000002421 cell wall Anatomy 0.000 description 24
- 230000008859 change Effects 0.000 description 19
- 239000000203 mixture Substances 0.000 description 15
- 239000007787 solid Substances 0.000 description 12
- 241000195493 Cryptophyta Species 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- 238000012545 processing Methods 0.000 description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 8
- 230000001276 controlling effect Effects 0.000 description 8
- 230000001105 regulatory effect Effects 0.000 description 8
- 239000002344 surface layer Substances 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 7
- 241000192710 Microcystis aeruginosa Species 0.000 description 6
- 230000033228 biological regulation Effects 0.000 description 6
- 241001465754 Metazoa Species 0.000 description 5
- 230000006837 decompression Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 241000238578 Daphnia Species 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 239000001569 carbon dioxide Substances 0.000 description 4
- 230000000739 chaotic effect Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 150000004676 glycans Chemical class 0.000 description 4
- 230000008676 import Effects 0.000 description 4
- 230000002045 lasting effect Effects 0.000 description 4
- 210000004400 mucous membrane Anatomy 0.000 description 4
- 235000015097 nutrients Nutrition 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 229920001282 polysaccharide Polymers 0.000 description 4
- 239000005017 polysaccharide Substances 0.000 description 4
- 239000003053 toxin Substances 0.000 description 4
- 231100000765 toxin Toxicity 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 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 3
- 108010067094 microcystin Proteins 0.000 description 3
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- 230000002730 additional effect Effects 0.000 description 2
- 239000000729 antidote Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
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- -1 deodorizer Substances 0.000 description 2
- 230000001877 deodorizing effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 238000004043 dyeing Methods 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
- 230000000855 fungicidal effect Effects 0.000 description 2
- 239000000417 fungicide Substances 0.000 description 2
- 230000003834 intracellular effect Effects 0.000 description 2
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- 229910052757 nitrogen Inorganic materials 0.000 description 2
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- 230000035484 reaction time Effects 0.000 description 2
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- 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
- 230000001954 sterilising effect Effects 0.000 description 2
- 238000013022 venting Methods 0.000 description 2
- 206010038743 Restlessness Diseases 0.000 description 1
- 239000006286 aqueous extract Substances 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 239000002158 endotoxin Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
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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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
- B01F25/21—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
- B01F25/212—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers the injectors being movable, e.g. rotating
- B01F25/2122—Rotating during jetting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
- B01F25/25—Mixing by jets impinging against collision plates
-
- 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
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)
- Catching Or Destruction (AREA)
Abstract
The present invention relates to a kind of pressurization sinuous flow mixing apparatus, it includes force (forcing) pump and pipette and outlet tube on the force (forcing) pump, it further includes having column casing closed at both ends, the hollow pipe communicated with column casing inner cavity is equipped in the column casing, the hollow pipe is equipped with can carry out the nozzle that spray is poured to column casing inner surface, the outlet tube that the force (forcing) pump is equipped with the pipette for importing treatment liquid and is communicated with column casing left end, described column casing one end are connected with outlet tube, are equipped with efferent duct on an opposite end.Therefore the groups such as cyanobacteria cell steady by sinuous flow, constantly can both have been become the individual cells of dispersion by the present invention, can effectively control the water quality disaster of the groups such as cyanobacterial bloom outburst.In addition pressurized liquid can be mixed under pressure and the collective effect of sinuous flow with moment and other gases or liquid, so as to the occasion for needing to handle liquid applied to cosmetics, medicine field.
Description
Technical field
The present invention relates to liquid handling device technical fields, more particularly, to a kind of pressurization sinuous flow mixing apparatus.
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, at present domestic and international algae removal technology master
It is divided into physics and removes algae, chemical algae removing and biological algae removal three categories.Physics algae removal technology includes mainly salvaging, filtering, covering, gas
It floats, removes algae mode compared to other, physics is most widely used except algae.
Current physics algae-removing method mainly by liquid handling device to cyanobacteria carry out it is aqueous extract, boosting injection,
Strong impaction carries out cyanobacteria processing.Using pressurization, the method for injection, i.e., aqueous algae is ejected into through being overpressurized by nozzle high speed
On baffle, then falls by dead weight and carry out the processing of cyanobacteria, do not form sinuous flow.In addition it passes through the side such as pressurization, injection, collision
When method handles cyanobacteria, then when Cells of Blue-green Algae being made to be ruptured or is dead, the bait of other zooplankters can not be become, it is difficult to restore
The normal food chain of Aquatic Ecosystem 2, so that the ecosystem is unable to reach a new food chain recovery by new strike and puts down
Weighing apparatus.Meanwhile Cells of Blue-green Algae endotoxin (such as Microcystin) being caused to be discharged into water body, secondary pollution of water is caused, the mankind are given
Bring healthy hidden danger.
In addition, being also required to handle liquid in cosmetics, medicine field, it needs the group to various animals, plant
It knits and is homogenized and is mixed, it is also necessary to is micro- in the high efficiency dispersion, emulsification and water between incompatible two kinds of liquid to organic and water
Weight organic compounds, lipoclastic, organic solvents, the extraction of solable matter.Both in need in cosmetics, medicine field to break
Cell wall promotes the occasion of absorption of human body, also in need not break cell wall, avoids the occasion of nutrition leak.Existing processing
Device is also realized by stirring mostly, can not form sinuous flow, and the effect of mixing is bad.
Invention content
The purpose of the present invention is to provide a kind of pressurization sinuous flow mixing apparatus, to solve in the prior art not forming unrest
The technical issues of stream.
The above-mentioned technical problem of the present invention is mainly to be addressed by following technical proposals：A kind of pressurization sinuous flow mixing
Device, including force (forcing) pump and pipette and outlet tube on the force (forcing) pump, further include having column casing closed at both ends, the column
The hollow pipe communicated with the column casing inner cavity is equipped in cylinder, the hollow pipe is equipped with can carry out what spray was poured to column casing inner surface
Nozzle, described column casing one end are connected with outlet tube, are equipped with efferent duct on an opposite end.
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, therefore the groups such as cyanobacteria cell steady by sinuous flow, constantly can both have been become the list of dispersion by the present invention
A cell can effectively control the water quality disaster of the groups such as cyanobacterial bloom outburst.And impact force caused by sinuous flow is more steady, holds
It is continuous, can be small to the impact of the cell wall of Cells of Blue-green Algae and continue, can ensure the cell wall of Cells of Blue-green Algae to a certain extent
Integrality, avoid its internal toxin outflow.In addition pressurized liquid can be with moment under pressure and the collective effect of sinuous flow
It is mixed with other gases or liquid, therefore the present invention can be by the full and uniform mixing of processed liquid, mixing effect is good, so as to
The occasion for needing to handle liquid applied to cosmetics, medicine field.
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, column casing is divided into left chamber and right chamber, the left chamber by the column casing by partition panel
Be connected with outlet tube, right chamber is communicated with efferent duct, and one end of the hollow pipe is arranged at opening, the other end at silent setting,
The hollow pipe runs through the partition panel and the open end of the hollow pipe is communicated with the left chamber.
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.
Preferably, the mixing pipeline that spray is poured can be carried out to column casing inner surface by being covered with outside the nozzle, in fixed tube
Road is equipped with the inlet pipe through column casing outer wall, and described inlet pipe one end is communicated with pipeline is mixed, and storeroom is connected on the other end.
Air is stored in storeroom, during treatment liquid, processed liquid table into column casing by nozzle
Face carries out spray and pours, and is located at outside nozzle due to mixing pipeline, and processed liquid, which can be rested on briefly, to be mixed in pipeline, at this time
The air in storeroom is sent by inlet pipe and mixes pipeline, due to the effect of pressure, air moment in storeroom with located
The liquid of reason uniformly mixes.The air in storeroom, which enters mixing pipeline, simultaneously can form bubble, and self-assembling formation negative pressure, cause
Pressure change in column casing.Therefore the present invention can by regulate and control air importing, change column casing in pressure value, cause pressurization or
The effect of person's decompression, to promote the treatment effect of the present invention.The importing for regulating and controlling air, can be arranged solenoid valve on inlet pipe,
Or can enter to mix pipeline and can form the size of bubble from the air in regulation and control storeroom and start with, such as change the stream of air
Speed, the internal diameter for changing inlet pipe change the measures such as the pressure value size for storing indoor pressure value, or change force (forcing) pump.Wherein
It is found through experiment, 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
It is the characteristic due to cyanobacteria itself, it is fragile in the occasion of negative pressure.
In practical application, the gases such as ozone, carbon dioxide, oxygen, nitrogen can also be stored in storeroom, or can be with
The liquid such as fungicide, antidote, deodorizer, pigment, distintegrant are stored in storeroom.During treatment liquid, located
The liquid of reason carries out spray to column casing inner surface by nozzle and pours, and is located at outside nozzle due to mixing pipeline, processed liquid meeting
Briefly rest on mix pipeline in, at this time by inlet pipe by storeroom gas or liquid be sent into mix pipeline, storeroom
In gas or liquid rapidly with processed liquid mix or react, to reach sterilizing, deodorizing, dyeing, acidification etc.
Additional effect.
Preferably, further including left end cap, the setting of the left end cap in left chamber's left end and can make the left chamber
Room is convexly equipped at least two deflectors being arranged at interval with the column casing inner wall, institute at closed setting on the left end cap
It states deflector to be distributed at circumference array using the axis of the left end cap as front, wherein a deflector is arranged described
The lower section of outlet tube and towards the outlet tube at being obliquely installed.
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.
Preferably, described deflector one end is fixedly connected with the left end cap, one end offsets with the partition panel.
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.
Preferably, the nozzle is set in the right chamber, the nozzle is equipped with two or more, and described
Nozzle is on the outer wall of the hollow pipe at being uniformly distributed.
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.
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 lower section of the left chamber is equipped with discharge pipe, discharge tube valve, the output are equipped in discharge pipe
Pipe is equipped with output tube valve.
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.
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, for the present invention compared with original technology, sinuous flow can be formed by having, and be individual thin breaing up group's cell
The advantages of may also select whether break up cell wall while born of the same parents.
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 the embodiment of the present invention one；
Attached drawing 2 is the internal structure schematic diagram of one right chamber of embodiment；
Attached drawing 3 is the sectional view of the embodiment of the present invention two；
Attached drawing 4 is the internal structure schematic diagram of two left chamber of the embodiment of the present invention.
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-.
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.
Embodiment one：
See Fig. 1, Fig. 2, a kind of pressurization sinuous flow mixing apparatus, including force (forcing) pump 1 and the pipette 11 on force (forcing) pump 1
The outlet tube 12 of sum further includes having column casing 2 closed at both ends, and the hollow pipe 3 communicated with 2 inner cavity of column casing is equipped in column casing 2, hollow
Pipe 3 is equipped with can carry out the nozzle 31 that spray is poured to 2 inner surface of column casing, and 2 one end of column casing is connected with outlet tube 12, sets on an opposite end
There is efferent duct 4.
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 enter sky by being open
In heart pipe.
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, therefore the groups such as cyanobacteria cell steady by sinuous flow, constantly can both have been become the list of dispersion by the present invention
A cell can effectively control the water quality disaster of the groups such as cyanobacterial bloom outburst.And impact force caused by sinuous flow is more steady, holds
It is continuous, can be small to the impact of the cell wall of Cells of Blue-green Algae and continue, can ensure the cell wall of Cells of Blue-green Algae to a certain extent
Integrality, avoid its internal toxin outflow.In addition pressurized liquid can be with moment under pressure and the collective effect of sinuous flow
It is mixed with other gases or liquid, therefore the present invention can be by the full and uniform mixing of processed liquid, so as to be applied to make up
Product, medicine field need the occasion handled liquid.
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 Fig. 1, Fig. 2, column casing 2 is divided into left chamber 22 and right chamber 23 by column casing 2 by partition panel 21, left chamber 22 with
Outlet tube 12 is connected, and right chamber 23 is communicated with efferent duct 4, one end of hollow pipe 3 at opening setting, the other end at silent setting,
Hollow pipe 3 is communicated through the open end of partition panel 21 and hollow pipe 3 with left chamber 22.
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 one end is at silent setting, open end and left chamber phase of the hollow pipe through partition panel and hollow pipe
Logical, 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, due to
The other end of hollow pipe can only be sprayed by nozzle and be poured on column casing inner surface at silent setting, then hollow liquid in pipe, be increased
Dynamics is poured in spray, can reinforce breaing up effect.
See Fig. 1, Fig. 2, the mixing pipeline 32 that spray is poured can be carried out to 2 inner surface of column casing by being covered with outside nozzle 31, in fixed tube
Road 32 is equipped with the inlet pipe 33 through 2 outer wall of column casing, and 33 one end of inlet pipe is communicated with pipeline 32 is mixed, and storage is connected on the other end
Room 34.
Air is stored in storeroom, during treatment liquid, processed liquid table into column casing by nozzle
Face carries out spray and pours, and is located at outside nozzle due to mixing pipeline, and processed liquid, which can be rested on briefly, to be mixed in pipeline, at this time
The air in storeroom is sent by inlet pipe and mixes pipeline, due to the effect of pressure, air moment in storeroom with located
The liquid of reason uniformly mixes.The air in storeroom, which enters mixing pipeline, simultaneously can form bubble, and self-assembling formation negative pressure, cause
Pressure change in column casing.Therefore the present invention can by regulate and control air importing, change column casing in pressure value, cause pressurization or
The effect of person's decompression, to promote the treatment effect of the present invention.The importing for regulating and controlling air, can be arranged solenoid valve on inlet pipe,
Or can enter to mix pipeline and can form the size of bubble from the air in regulation and control storeroom and start with, such as change the stream of air
Speed, the internal diameter for changing inlet pipe change the measures such as the pressure value size for storing indoor pressure value, or change force (forcing) pump.Wherein
It is found through experiment, 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
It is the characteristic due to cyanobacteria itself, it is fragile in the occasion of negative pressure.
In practical application, the gases such as ozone, carbon dioxide, oxygen, nitrogen can also be stored in storeroom, or can be with
The liquid such as fungicide, antidote, deodorizer, pigment, distintegrant are stored in storeroom.During treatment liquid, located
The liquid of reason carries out spray to column casing inner surface by nozzle and pours, and is located at outside nozzle due to mixing pipeline, processed liquid meeting
Briefly rest on mix pipeline in, at this time by inlet pipe by storeroom gas or liquid be sent into mix pipeline, storeroom
In gas or liquid rapidly with processed liquid mix or react, to reach sterilizing, deodorizing, dyeing, acidification etc.
Additional effect.
See Fig. 1, Fig. 2, mix pipeline 32 and be convexly equipped on the outer wall of hollow pipe 3, and mixes pipeline 32 with nozzle 31 at coaxial
Setting.
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.And when the axis of nozzle and hollow pipe are at being vertically arranged, it can be with
Enable liquid after mixing be also that vertical spray is poured on column casing inner surface by mixing pipeline so that the liquid after mixing by
Reaction force direction to column casing inner surface is identical as its flow direction, to the impact force maximum for making it be subject to, enables the present invention
It faster can more fully break up group's cell.It can also enable and mix height value of the height value of pipeline more than nozzle, such one
Come, pipeline is mixed when sinuous flow to column casing inner surface will be full of while spray is poured by nozzle.
See that Fig. 1, Fig. 2, the lower section of left chamber 22 are equipped with discharge pipe 5, discharge tube valve 51, efferent duct 4 are equipped in discharge pipe 5
It is equipped with output tube valve 41.
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.
See that Fig. 1, Fig. 2, 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 31 are equipped with two or more, and nozzle 31 is on the outer wall of hollow pipe 3 at being uniformly distributed.And it sprays
Mouth 31 is set in right chamber 23.
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；Nozzle is set in right chamber, is mixed pipeline and is located at nozzle
Outside, then sinuous flow is formed in right chamber, and right chamber can be by set on the inlet pipe mixed on pipeline, regulating and controlling the importing of air to adjust
The pressure change for controlling right chamber, to cause the effect pressurizeed or depressurized, 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 Fig. 1, Fig. 2, 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. 1, Fig. 2, 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. 1, 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. 1, 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 the experimental result statistical form that the embodiment of the present invention one handles the liquid containing cyanobacteria under 0.4MPa pressure values:
The method for treating liquids of embodiment one, includes the following steps,
The numerical value of hydralic pressure gauge 13 and air gauge 24 is monitored at any time to keep the balance of interior external pressure；
Liquid to be processed is sent into force (forcing) pump 1 through pipette 11 to pressurize, then is sent into column casing 2 by outlet tube 12；
Discharge tube valve 51 is opened, the solid with constant weight is discharged from discharge pipe 5；
Liquid through being overpressurized flowing and enters right chamber 23 in the column casing 2 by hollow pipe 3, then via nozzle 31 to column
2 inner surfaces of cylinder carry out spray and pour to form sinuous flow；
By inlet pipe 33 by storeroom 34 gas or liquid be sent into and mix pipeline 32, gas or liquid in storeroom 34
Body moment uniformly mixes with processed liquid；
Output tube valve 41 is opened, the liquid handled well is discharged by efferent duct 4.
It chooses whether break up cell wall and is realized by regulating and controlling the pressure value in column casing 2.
Embodiment two：
See Fig. 3, Fig. 4, 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 embodiment one.
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 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.
The method for treating liquids of embodiment two, includes the following steps,
The numerical value of hydralic pressure gauge 13 and air gauge 24 is monitored at any time to keep the balance of interior external pressure；
Liquid to be processed is sent into force (forcing) pump 1 through pipette 11 to pressurize, then is sent into column casing 2 by outlet tube 12；
Air importing moment in air storage chamber 27 is uniformly mixed with processed liquid by snorkel 26；
Liquid through being overpressurized is drained and is circulated by deflector in left chamber 22；
Discharge tube valve 51 is opened, the solid with constant weight is discharged from discharge pipe 5；
Processed liquid enters right chamber by hollow pipe 3, then is sprayed to 23 inner surface of right chamber via nozzle 31
It pours to form sinuous flow；
By inlet pipe 33 by storeroom 34 gas or liquid be sent into and mix pipeline 32, gas or liquid in storeroom 34
Body moment uniformly mixes with processed liquid；
Liquid after mixing carries out spray to 23 inner surface of right chamber by mixing pipeline 32 and pours；
Output tube valve 41 is opened, the liquid handled well is discharged by efferent duct 4.
It chooses whether break up cell wall and is realized by regulating and controlling the pressure value in column casing 2.
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 pressurization sinuous flow mixing apparatus, including force (forcing) pump and the pipette on the force (forcing) pump and outlet tube,
It is characterized in that：Further include having column casing closed at both ends, the hollow pipe communicated with the column casing inner cavity, institute are equipped in the column casing
The hollow pipe stated is equipped with can carry out the nozzle that spray is poured to the column casing inner surface, described column casing one end and the outlet tube phase
Even, it is equipped with efferent duct on an opposite end.
2. pressurization sinuous flow mixing apparatus according to claim 1, it is characterised in that：The column casing is by partition panel by institute
State column casing and be divided into left chamber and right chamber, the left chamber is connected with the outlet tube, the right chamber with it is described defeated
Outlet pipe communicates, and one end of the hollow pipe is arranged at opening, and the other end runs through the partition at silent setting, the hollow pipe
The open end of plate and the hollow pipe is communicated with the left chamber.
3. pressurization sinuous flow mixing apparatus according to claim 2, it is characterised in that：Being covered with outside the nozzle can be to described
Column casing inner surface carries out the mixing pipeline that spray is poured, and the inlet pipe through the column casing outer wall is equipped on the mixing pipeline, described
Inlet pipe one end communicated with the mixing pipeline, storeroom is connected on the other end.
4. pressurization sinuous flow mixing apparatus according to claim 3, it is characterised in that：Further include left end cap, the left end cap
Left end in the left chamber is set and the left chamber can be made at closed setting, be convexly equipped on the left end cap at least two with
The deflector that the column casing inner wall is arranged at interval, the deflector are that front divides at circumference array using the axis of the left end cap
Cloth, wherein a deflector be arranged the lower section of the outlet tube and towards the outlet tube at being obliquely installed.
5. pressurization sinuous flow mixing apparatus according to claim 4, it is characterised in that：Described deflector one end and the left end
Lid is fixedly connected, and one end offsets with the partition panel.
6. pressurization sinuous flow mixing apparatus according to claim 4, it is characterised in that：Further include snorkel and air storage chamber, institute
The outer wall that snorkel runs through the left chamber is stated, and one end is close to the nozzle of the outlet tube, the other end and the air storage chamber phase
Connection.
7. pressurization sinuous flow mixing apparatus according to claim 3, it is characterised in that：The nozzle is set to the right chamber
Interior, the nozzle is equipped with two or more, and the nozzle on the outer wall of the hollow pipe at being uniformly distributed.
8. pressurization sinuous flow mixing apparatus according to claim 3, it is characterised in that：The nozzle is convexly equipped in described hollow
On the outer wall of pipe, and the internal diameter of the nozzle tapers off setting successively along the axis of itself, and the mixing pipeline is convexly equipped in described
On the outer wall of hollow pipe, and the mixing pipeline and the nozzle are at coaxial arrangement.
9. pressurization sinuous flow mixing apparatus according to claim 2, it is characterised in that：The lower section of the left chamber is equipped with discharge
Pipe, is equipped with discharge tube valve on the discharge pipe, and the efferent duct is equipped with output tube valve, is set on the outlet tube
There is hydralic pressure gauge, air gauge is equipped on the outer wall of the right chamber.
10. according to claim 1 to 9 any one of them pressurization sinuous flow mixing apparatus, it is characterised in that：Pressure in the column casing
Power is maintained between 0.1MPa-10MPa.
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| CN201810706018.1A CN108557964A (en) | 2018-06-26 | 2018-06-26 | A kind of pressurization sinuous flow mixing apparatus |
| 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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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020001419A1 (en) * | 2018-06-26 | 2020-01-02 | 温州大学 | Pressurized turbulent mixing device, liquid treatment method, cyanobacteria treatment device and cyanobacteria treatment method |
| CN112174292A (en) * | 2020-10-21 | 2021-01-05 | 安徽中环环保科技股份有限公司 | Advanced treatment device and method for printing and dyeing wastewater |
| CN113856510A (en) * | 2021-10-12 | 2021-12-31 | 兵器工业卫生研究所 | Real-time mixed inhalation exposure device for multi-component gas of laboratory mouse |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1468808A (en) * | 2002-07-17 | 2004-01-21 | 伟将有限公司 | Eddy speeding ultraviolet ray sterilizing and algae-killing liquid treater |
| CN101734352A (en) * | 2008-11-25 | 2010-06-16 | 上海浦劲实业有限公司 | Blue-green algae disposing device |
| JP2010188315A (en) * | 2009-02-20 | 2010-09-02 | Nishi Nippon Gijutsu Kaihatsu Kk | Treating method and facility of raw water containing organic pollutant or toxic substance |
| CN102616956A (en) * | 2012-03-22 | 2012-08-01 | 丛海兵 | Water treatment system for removing algae by pressure strengthening and sedimentation coagulating and water treatment method |
| CN104671464A (en) * | 2015-02-02 | 2015-06-03 | 石家庄顺瑞节能科技有限公司 | Water jet and micropore aeration integrated device |
| CN208429919U (en) * | 2018-06-26 | 2019-01-25 | 温州大学 | A kind of pressurization sinuous flow mixing apparatus |
-
2018
- 2018-06-26 CN CN201810706018.1A patent/CN108557964A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1468808A (en) * | 2002-07-17 | 2004-01-21 | 伟将有限公司 | Eddy speeding ultraviolet ray sterilizing and algae-killing liquid treater |
| CN101734352A (en) * | 2008-11-25 | 2010-06-16 | 上海浦劲实业有限公司 | Blue-green algae disposing device |
| JP2010188315A (en) * | 2009-02-20 | 2010-09-02 | Nishi Nippon Gijutsu Kaihatsu Kk | Treating method and facility of raw water containing organic pollutant or toxic substance |
| CN102616956A (en) * | 2012-03-22 | 2012-08-01 | 丛海兵 | Water treatment system for removing algae by pressure strengthening and sedimentation coagulating and water treatment method |
| CN104671464A (en) * | 2015-02-02 | 2015-06-03 | 石家庄顺瑞节能科技有限公司 | Water jet and micropore aeration integrated device |
| CN208429919U (en) * | 2018-06-26 | 2019-01-25 | 温州大学 | A kind of pressurization sinuous flow mixing apparatus |
Non-Patent Citations (1)
| Title |
|---|
| 谌永红: "《给水排水工程》", 北京：中国环境科学出版, pages: 490 - 492 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020001419A1 (en) * | 2018-06-26 | 2020-01-02 | 温州大学 | Pressurized turbulent mixing device, liquid treatment method, cyanobacteria treatment device and cyanobacteria treatment method |
| CN112174292A (en) * | 2020-10-21 | 2021-01-05 | 安徽中环环保科技股份有限公司 | Advanced treatment device and method for printing and dyeing wastewater |
| CN113856510A (en) * | 2021-10-12 | 2021-12-31 | 兵器工业卫生研究所 | Real-time mixed inhalation exposure device for multi-component gas of laboratory mouse |
| CN113856510B (en) * | 2021-10-12 | 2023-10-13 | 兵器工业卫生研究所 | Real-time mixed inhalation exposure device for multi-component gas of laboratory mice |
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Inventor after: Hao Aimin Inventor after: Jing Qinning Inventor after: Zhao Min Inventor after: Chen Jianying Inventor after: Zhang Xianglei Inventor after: Xu Mingming Inventor after: Gao Cheng Inventor after: Wu Mingjiang Inventor before: Hao Aimin Inventor before: Jing Qinning Inventor before: Zhao Min Inventor before: Chen Jianying Inventor before: Zhang Xianglei Inventor before: Xu Mingming Inventor before: Gao Cheng Inventor before: Wu Mingjiang |
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Application publication date: 20180921 |