CN107308788A - A kind of microbubble industrial waste gas processing system - Google Patents
A kind of microbubble industrial waste gas processing system Download PDFInfo
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- CN107308788A CN107308788A CN201710558960.3A CN201710558960A CN107308788A CN 107308788 A CN107308788 A CN 107308788A CN 201710558960 A CN201710558960 A CN 201710558960A CN 107308788 A CN107308788 A CN 107308788A
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- microbubble
- waste gas
- industrial waste
- processing system
- gas processing
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- 239000007789 gas Substances 0.000 title claims abstract description 30
- 239000002440 industrial waste Substances 0.000 title claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 11
- 238000000746 purification Methods 0.000 claims description 10
- 239000007921 spray Substances 0.000 claims description 8
- 239000002912 waste gas Substances 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 abstract description 17
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 abstract description 9
- 230000005684 electric field Effects 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 5
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract description 3
- 238000003487 electrochemical reaction Methods 0.000 abstract description 3
- 238000007254 oxidation reaction Methods 0.000 abstract description 3
- 230000035568 catharsis Effects 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 4
- 238000004880 explosion Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- -1 arene compounds Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- DOTMOQHOJINYBL-UHFFFAOYSA-N molecular nitrogen;molecular oxygen Chemical compound N#N.O=O DOTMOQHOJINYBL-UHFFFAOYSA-N 0.000 description 1
- 239000003471 mutagenic agent Substances 0.000 description 1
- 231100000707 mutagenic chemical Toxicity 0.000 description 1
- 230000003505 mutagenic effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000007348 radical reaction Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 230000000638 stimulation Effects 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 210000001835 viscera Anatomy 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
- B01D53/323—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00 by electrostatic effects or by high-voltage electric fields
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/76—Gas phase processes, e.g. by using aerosols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/14—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/26—Details
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/26—Details
- B02C13/28—Shape or construction of beater elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/104—Ozone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/12—Methods and means for introducing reactants
- B01D2259/124—Liquid reactants
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Food Science & Technology (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Dispersion Chemistry (AREA)
- Treating Waste Gases (AREA)
Abstract
The present invention relates to industrial waste gas processing system, more particularly to a kind of microbubble industrial waste gas processing system.The system includes microbubble breaker, and microbubble breaker, which hits a diameter of 50 500 nanometers of microbubble, to be divided, and quantity of formation is more, the smaller microbubble of diameter, so as to improve the treatment effect of industrial waste gas.And microbubble breaker can form sinuous flow area in treating column, extremely many extreme physical environments are formed in sinuous flow area, form high-voltage corona electric field, the oxygen molecule in electric field or around electric field is set to occur electrochemical reaction, so as to manufacture ozone, ozone produces oxidation reaction with the compound in air, preferably realizes catharsis.
Description
【Technical field】
The present invention relates to industrial waste gas processing system, more particularly to a kind of microbubble industrial waste gas processing system.
【Background technology】
VOC materials refer to the general name of organic substance readily volatilized at normal temperatures, common are formaldehyde, toluene and dimethylbenzene
Etc..Traditional spraying industry uses substantial amounts of nitrate paint raw and auxiliary material in product spraying process, and nitrate paint raw and auxiliary material contains
There is substantial amounts of machine solvent, the aromatic hydrocarbon that especially high volatile solvent such as dimethylbenzene, toluene, benzene contains was not only poisonous but also inflammable, and
Highly volatile causes to have discharged numerous VOC into air into environment, pollutes atmospheric environment and is detrimental to health.Organise
Compound not only has a stimulation to human body, and wherein many to the toxic effect of internal organ, also have plenty of mutagen with it is carcinogenic
Thing.Alkene and some arene compounds in organic compound, in an atmosphere, can also be with nitrogen oxygen in the presence of sunlight
Compound reacts to form the photochemical fog or industrial photochemical fog of Los Angeles type, causes secondary pollution.
And pass through many experiments and find, nano level microbubble, which can be realized, to be divided the VOC gases contained in air
Solution, concrete principle is as follows：Nanoscale microbubble is in collapse blasting process, and moment can produce 4000K high temperature, 50MPa high pressures,
After last microseconds, focus is cooled down therewith, and with strong shock wave and the microjet up to 100m/s speed.These conditions
It is enough to make organic matter that chemical bond rupture, aqueous phase burning, pyrolytic or radical reaction occur in nanoscale microbubble, is
VOC degraded creates an extreme physical environment.When liquid is in ultrasonic field, pressure waveform is sufficient into condition of high voltage
To open the stronger chemical bond of adhesion so that hydrone H2O is decomposed into-H and-OH free radicals or generation H2O2, the oxygen of generation
Change free love base to be diffused into water body, then reacted by way of nanometer microbubble with VOC so that VOC is degraded.
And in above-mentioned course of reaction, show through many experiments, the diameter of microbubble is smaller, more obvious to VOC degradations,
But the smaller microbubble of diameter is sprayed by nozzle, prior art is not accomplished also.Therefore the diameter of reduction microbubble is needed,
Also need to by other means realize.And in microbubble and air in compound course of reaction, if necessary to in air
The compound progress oxidation reaction contained, which is only filled with ozone, to be realized.Therefore offer one kind is needed to reduce microbubble diameter
With can automatically generate the industrial waste gas processing system of ozone.
【The content of the invention】
Present invention seek to address that above mentioned problem and providing a kind of reduce microbubble diameter and can automatically generate the one of ozone
Plant microbubble industrial waste gas processing system
To achieve the above object, a kind of microbubble industrial waste gas processing system of the invention, includes the processing of U-shaped design
Air inlet 11 and air outlet 12 are provided with tower 10, described treating column 10, described air inlet 11 and air outlet 12 is set respectively
Put on the two ends for the treatment of column 10, water body input pipe 40, the described end of water body input pipe 40 are provided with described air inlet 11
End is connected with some microbubble nozzles 50, and the water spray that described microbubble nozzle 50 inputs water body input pipe 40 is into a diameter of
Microbubble breaker, the broken dress of described microbubble are additionally provided with 50-500 nanometers of microbubble, described treating column 10
Put including a rotary shaft 60 and some broken rods 61 being arranged in rotary shaft 60, described broken rod 61 is around rotary shaft 60
It is rotated in treating column 10 and forms air sinuous flow area, micro- gas that the industrial waste gas that air inlet 11 enters sprays with microbubble nozzle 50
Bubble is sufficiently mixed in sinuous flow area.
Further, the cross sectional shape of described broken rod 61 is circle, triangle, square, trapezoidal one of which.
Further, the rotary speed of described rotary shaft 60 is 5-15 turns of each second.
Further, some spines 62 are additionally provided with described broken rod 61.
Further, described treating column 10U types bottom fills the purification liquid 30 that depth is 30-50 centimetres, described
Purify the longitudinal section of the not submerged impinging jet tower 10U types bottom of liquid 30.
Further, described treating column 10 is additionally provided with some layer of air screen packs 70, some layer of air screen packs 70
Height be not less than 30 centimetres.
Further, described airstrainer 70 is adsorbed with water droplet.
Further, the wind speed of described air inlet 11 is not more than 5 meter per seconds, the section of air inlet 11 and cutting for treating column
Face ratio is 1: 5-15.
Further, blower fan 20 is additionally provided with described air outlet 12, described blower fan 20 is axial flow blower.
The contribution of the present invention is the provision of a kind of microbubble industrial waste gas processing system, and the system is set below nozzle
There is microbubble breaker, breaker includes rotary shaft and broken rod, and rotary shaft drives what broken rod rotation sprayed nozzle
Microbubble is smashed, and a big microbubble of diameter is hit into several small microbubbles of diameter, is formed more microbubbles and is caught
The hazardous compound in air is caught, makes discomposing effect more preferable.Spine is additionally provided with breaker, spine also can be helped preferably
Realize the division to microbubble.Rotary shaft, which is rotated in treating column, forms sinuous flow area, and some air is towards nozzle direction
Motion, is so more beneficial for air and is mixed with the microbubble that nozzle is formed.Meanwhile, due to the quantity of microbubble explosion in sinuous flow area
Sharply increase, more 4000K of formation high temperature, the local environment of 50MPa high pressures, so as to form high-voltage corona electric field, make electricity
Electrochemical reaction occurs for the oxygen molecule in or around electric field, so as to automatically generate ozone, oxygen is carried out to the compound in air
Change, without being additionally filled with ozone.
【Brief description of the drawings】
Fig. 1 is structural representation of the invention.
Fig. 2 is that the broken rod section of the present invention is circular microbubble breaker structural representation.
Fig. 3 is the microbubble breaker structural representation that the broken rod section of the present invention is triangle.
【Embodiment】
The following example is being explained further and supplementing to the present invention, and the present invention is not limited in any way.
Embodiment 1
As shown in Figure 1, 2, 3, a kind of microbubble industrial waste gas processing system of the present embodiment, includes the place of U-shaped design
Manage and be provided with air inlet 11 and air outlet 12 on tower 10, described treating column 10, described air inlet 11 and air outlet 12 is distinguished
On the two ends for being arranged on treating column 10, water body input pipe 40, described water body input pipe 40 are provided with described air inlet 11
End is connected with some microbubble nozzles 50, and the water spray that described microbubble nozzle 50 inputs water body input pipe 40 is into diameter
For 50-500 nanometers of microbubble, microbubble breaker is additionally provided with described treating column 10, described microbubble is crushed
Device includes a rotary shaft 60 and some broken rods 61 being arranged in rotary shaft 60, and described broken rod 61 is around rotary shaft
It is micro- that 60 industrial waste gases and microbubble nozzle 50 for being rotated in the entrance of formation air sinuous flow area air inlet 11 in treating column 10 spray
Bubble is sufficiently mixed in sinuous flow area.Air inlet 11 is passed through the industrial waste gas containing VOC, is passed through after industrial waste gas, microbubble nozzle
50 spray a diameter of 50-500 nanometers of microbubble, and are mixed with industrial waste gas, because microbubble is through nozzle by water in itself
Formed after ejection, therefore itself has certain adhesive force, explosion after microbubble is mixed with the compound in air, moment can produce
Raw 4000K high temperature, 50MPa high pressures, so as to be the molecular scission of compound, reach degraded VOC purpose.Due to microbubble
Diameter is smaller, and the effect for the VOC that degrades is more obvious.Microbubble breaker is also provided with the present embodiment below nozzle 50, it is micro-
Bubble breaking device is a rotary shaft 60 and some broken rods 61, and the rotation of rotary shaft 60 drives broken rod 61 and microbubble high
Speed collision, makes a microbubble split into several microbubbles, while increase microbubble quantity, also can preferably realize micro- gas
Steep and the compound contained in air is caught, sufficiently complete degraded.The other rotation of rotary shaft 60 can be in treating column 10
The combination probability of compound and microbubble can also be increased by forming the various collisions formed in sinuous flow area, sinuous flow area.Nozzle 50 is down
Microbubble is sprayed, and rotary shaft 60 can also form upward air-flow, air clashes with microbubble, and microbubble catches the several of compound
Rate can also increase.Simultaneously as microbubble explosion can produce the physical environment of local extreme, high-voltage corona electric field is formed, is made
Electrochemical reaction occurs for the oxygen molecule in electric field or around electric field, so as to automatically generate ozone, the compound in air is carried out
Oxidation, without being additionally filled with ozone.
Embodiment 2
As shown in Figure 1, 2, 3, the cross sectional shape of described broken rod 61 be circle, triangle, square, it is trapezoidal wherein
It is a kind of.The rotary speed of described rotary shaft 60 is 5-15 turns of each second.Some spines are additionally provided with described broken rod 61
62.Circular broken rod 51 forms swirling eddy after air is scratched in rotary course, makes air in sinuous flow area towards difference
Direction is operated, the success rate that increase microbubble is combined with compound.And the broken rod 61 of triangle divides air after rotating at a high speed
Isolate, negative pressure is formed by part, then air filling head-on collision, the success rate that increase microbubble is combined with compound, simultaneously
The broken rod of triangle can also form upward air-flow, the probability for the microbubble head-on collision that increase air sprays with nozzle.Spine
62 can help to puncture microbubble, form the smaller microbubble of more more dense, diameters.
Embodiment 3
As shown in figure 1, described treating column 10U types bottom fills the purification liquid 30 that depth is 30-50 centimetres, it is described
Purify the longitudinal section of the not submerged impinging jet tower 10U types bottom of liquid 30.Because microbubble is to pass through microbubble nozzle 50 by water in itself
Formed after atomization, therefore be also to form vaporific small water droplet after its explosion, small water droplet is attached in compound, when increasing small
Can form the globule after water droplet attachment, so as to fall, drop into purification liquid 30, purification liquid 30 can be water or
There is the solvent of clean-up effect.The longitudinal section of purification liquid 30 not submerged impinging jet tower 10U types bottom is to ensure that ventilation is smooth.
Embodiment 4
As shown in figure 1, described treating column 10 is additionally provided with some layer of air screen packs 70, some layer of air screen packs 70
Height be not less than 30 centimetres.Described airstrainer 70 is adsorbed with water droplet.When the air containing industrial waste gas passes through sinuous flow
Area, and during by purification liquid 30, contained compounds content polar region in it, but in order to preferably realize purification effect
Really, it is also provided with being adsorbed with water droplet on airstrainer 70, airstrainer 70 before air outlet 12, further realization pair
The purification of air.
Although being disclosed by above example to the present invention, protection scope of the present invention is not limited thereto,
Under conditions of without departing from present inventive concept, deformation, replacement that each component is done to more than etc. will fall into the right of the present invention
In claimed range.
Claims (9)
1. a kind of microbubble industrial waste gas processing system, is included on the treating column (10) of U-shaped design, described treating column (10)
Air inlet (11) and air outlet (12) are provided with, described air inlet (11) and air outlet (12) is separately positioned on treating column (10)
Two ends on, it is characterised in that：Described air inlet (11) place is provided with water body input pipe (40), described water body input pipe
(40) end is connected with some microbubble nozzles (50), the water that described microbubble nozzle (50) inputs water body input pipe (40)
Spray into a diameter of 50-500 nanometers microbubble, described treating column (10) and be additionally provided with microbubble breaker, it is described
Microbubble breaker include a rotary shaft (60) and some broken rods (61) being arranged in rotary shaft (60), it is described
Broken rod (61) be rotated in around rotary shaft (60) in treating column (10) and form air sinuous flow area, the industry that air inlet (11) enters
The microbubble that waste gas sprays with microbubble nozzle (50) is sufficiently mixed in sinuous flow area.
2. a kind of microbubble industrial waste gas processing system as claimed in claim 1, it is characterised in that：Described broken rod (61)
Cross sectional shape be circle, triangle, square, trapezoidal one of which.
3. a kind of microbubble industrial waste gas processing system as claimed in claim 1, it is characterised in that：Described rotary shaft (60)
Rotary speed for each second 5-15 turn.
4. a kind of microbubble industrial waste gas processing system as claimed in claim 3, it is characterised in that：Described broken rod (61)
On be additionally provided with some spines (62).
5. a kind of microbubble industrial waste gas processing system as claimed in claim 1, it is characterised in that：Described treating column (10)
It is 30-50 centimetres of purification liquid (30) that U-shaped bottom, which fills depth, described purification liquid (30) not submerged impinging jet tower (10) U
The longitudinal section of type bottom.
6. a kind of microbubble industrial waste gas processing system as claimed in claim 5, it is characterised in that：Described treating column (10)
Some layer of air screen packs (70) are additionally provided with, the height of some layer of air screen packs (70) is not less than 30 centimetres.
7. a kind of microbubble industrial waste gas processing system as claimed in claim 6, it is characterised in that：Described airstrainer
(70) it is adsorbed with water droplet.
8. a kind of microbubble industrial waste gas processing system as described in claim 1-7 is any, it is characterised in that：Described air intake
The wind speed of mouth (11) is not more than 5 meter per seconds, and the section of air inlet (11) and the section ratio for the treatment of column are 1: 5-15.
9. a kind of microbubble industrial waste gas processing system as claimed in claim 1, it is characterised in that：Described air outlet (12)
Place is additionally provided with blower fan (20), and described blower fan (20) is axial flow blower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710558960.3A CN107308788A (en) | 2017-07-11 | 2017-07-11 | A kind of microbubble industrial waste gas processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710558960.3A CN107308788A (en) | 2017-07-11 | 2017-07-11 | A kind of microbubble industrial waste gas processing system |
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| Publication Number | Publication Date |
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| CN107308788A true CN107308788A (en) | 2017-11-03 |
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| CN201710558960.3A Pending CN107308788A (en) | 2017-07-11 | 2017-07-11 | A kind of microbubble industrial waste gas processing system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117619254A (en) * | 2024-01-25 | 2024-03-01 | 东北大学 | Nanoparticle generation device and generation method |
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|---|---|---|---|---|
| JP2013027855A (en) * | 2011-07-26 | 2013-02-07 | Yamaguchi Kogyo:Kk | Cavitation bubble cleaning device |
| CN103933832A (en) * | 2014-05-06 | 2014-07-23 | 石博天 | Device for eliminating haze and atmospheric pollutant |
| CN104941353A (en) * | 2015-07-10 | 2015-09-30 | 河南五星科技有限公司 | Purifier |
| CN206935072U (en) * | 2017-07-11 | 2018-01-30 | 钟会琴 | A kind of microbubble industrial waste gas processing system |
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2017
- 2017-07-11 CN CN201710558960.3A patent/CN107308788A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013027855A (en) * | 2011-07-26 | 2013-02-07 | Yamaguchi Kogyo:Kk | Cavitation bubble cleaning device |
| CN103933832A (en) * | 2014-05-06 | 2014-07-23 | 石博天 | Device for eliminating haze and atmospheric pollutant |
| CN104941353A (en) * | 2015-07-10 | 2015-09-30 | 河南五星科技有限公司 | Purifier |
| CN206935072U (en) * | 2017-07-11 | 2018-01-30 | 钟会琴 | A kind of microbubble industrial waste gas processing system |
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Application publication date: 20171103 |