CN208130800U - Micro-nano bubble synergy ozone emission-control equipment - Google Patents
Micro-nano bubble synergy ozone emission-control equipment Download PDFInfo
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- CN208130800U CN208130800U CN201820117408.0U CN201820117408U CN208130800U CN 208130800 U CN208130800 U CN 208130800U CN 201820117408 U CN201820117408 U CN 201820117408U CN 208130800 U CN208130800 U CN 208130800U
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- nano bubble
- air
- ozone
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- 239000002101 nanobubble Substances 0.000 title claims abstract description 79
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 58
- 150000001450 anions Chemical class 0.000 claims abstract description 30
- 230000000740 bleeding effect Effects 0.000 claims abstract description 13
- 238000006243 chemical reaction Methods 0.000 claims abstract description 12
- 238000010992 reflux Methods 0.000 claims abstract description 8
- 239000000945 filler Substances 0.000 claims abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 67
- 238000009287 sand filtration Methods 0.000 claims description 12
- 125000004122 cyclic group Chemical group 0.000 claims description 11
- 238000005086 pumping Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 10
- 238000012545 processing Methods 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 30
- 238000000034 method Methods 0.000 description 11
- 230000008569 process Effects 0.000 description 7
- 239000010410 layer Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 239000012855 volatile organic compound Substances 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000002440 industrial waste Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- OUUQCZGPVNCOIJ-UHFFFAOYSA-M Superoxide Chemical compound [O-][O] OUUQCZGPVNCOIJ-UHFFFAOYSA-M 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002344 surface layer Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 244000286663 Ficus elastica Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- TUJKJAMUKRIRHC-UHFFFAOYSA-N hydroxyl Chemical compound [OH] TUJKJAMUKRIRHC-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- DCKVNWZUADLDEH-UHFFFAOYSA-N sec-butyl acetate Chemical compound CCC(C)OC(C)=O DCKVNWZUADLDEH-UHFFFAOYSA-N 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229950011008 tetrachloroethylene Drugs 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
A kind of micro-nano bubble synergy ozone emission-control equipment, including：Tangential air inlet cyclone, has ejection air port, refluxing opening and tangent air inlet；Air hose has bottom interface, top interface, anion inlet, micro-nano bubble inlet, ozone inlet and bleeding point；The bottom interface connects the ejection air port；Micro-nano bubble reaction unit tower has lower air inlet, filler demisting layer and upper air outlet；First shell is connected between the top interface and the lower air inlet；Anion generation system connects the anion inlet of the air hose side wall；Micro-nano bubble generation system connects the micro-nano bubble inlet of the air hose side wall；Ozone generating system connects the ozone inlet of the air hose side wall；Extract system connects the bleeding point of the air hose side wall.The micro-nano bubble synergy ozone emission-control equipment can be improved treatment effect, and reduce processing cost.
Description
Technical field
The utility model relates to environment protection field more particularly to a kind of micro-nano bubble synergy ozone emission-control equipments.
Background technique
Industrial waste gas has been always the important pollution sources since industrializing, and there are different journeys in many field of industrial production
The industrial gas emission amount of degree, such as oil plant, rubber plant, chemical plant, pharmaceutical factory, caused by air pollution at present
Paid attention to extensively, discharge becomes research hotspot after how purifying to industrial waste gas.
In industrial waste gas, the improvement of organic exhaust gas is to administer one of problem.The case where traditional VOCs treatment, technique are multiple
It is miscellaneous.If corresponding purification efficiency is not high, and treatment effect is bad using technique at low cost；If high using purification efficiency
Technique, corresponding operating cost is high, and early investment cost is also relatively high, cannot meet the demand of enterprise well.
Utility model content
The utility model solves the problems, such as to be to provide a kind of micro-nano bubble synergy ozone emission-control equipment, so as to
More high-quality and high-efficiency exhaust gas is handled.
To solve the above problems, the utility model provides a kind of micro-nano bubble synergy ozone emission-control equipment, packet
It includes：Tangential air inlet cyclone, has ejection air port, refluxing opening and tangent air inlet；Air hose, have bottom interface, top interface,
Anion inlet, micro-nano bubble inlet, ozone inlet and bleeding point；The bottom interface connects the top air-out
Mouthful；Micro-nano bubble reaction unit tower has lower air inlet, filler demisting layer and upper air outlet；First shell is connected to described
Between top interface and the lower air inlet；Anion generation system connects the anion inlet of the air hose side wall；
Micro-nano bubble generation system connects the micro-nano bubble inlet of the air hose side wall；Ozone generating system connects institute
State the ozone inlet of air hose side wall；Extract system connects the bleeding point of the air hose side wall.
Optionally, on the air hose side wall, the position of the micro-nano bubble inlet is injected higher than the anion
The position of mouth.
Optionally, on the air hose side wall, the position of the ozone inlet is higher than the micro-nano bubble inlet
Position.
Optionally, on the air hose side wall, the position of the bleeding point is higher than the position of the ozone inlet.
Optionally, the micro-nano bubble inlet includes the first inlet and the second inlet；In the air hose side wall
On, the position of second inlet is higher than the position of first inlet；The micro-nano bubble generation system includes the
One micro-nano air Bubble generating apparatus and the second micro-nano air Bubble generating apparatus；The first micro-nano air Bubble generating apparatus connects institute
The first inlet is stated, the second micro-nano air Bubble generating apparatus connects second inlet.
Optionally, the ozone generating system is pouring-in ozone generator.
Optionally, the micro-nano bubble synergy ozone emission-control equipment further includes water circulating pump, sandfiltration pot and circulation
Water tank, the refluxing opening connect the water inlet of the water circulating pump, and the water outlet of the water circulating pump connects the sandfiltration pot
Water inlet, the water outlet of the sandfiltration pot connect the water inlet of the cyclic water tank, and the water outlet of the cyclic water tank connects simultaneously
Connect the water inlet of the anion generation system and the water inlet of the micro-nano bubble generation system.
Optionally, the air hose includes multiple pipelines arranged side by side.
Optionally, the bleeding point is set to the top side wall of the pipeline, and the extract system is axial flow blower.
Optionally, the first shell includes first level shell section, the second horizontal shell section and upright shell section；First water
Flat shell section connects the top interface；The second horizontal shell section connects the lower air inlet；Described in the upright shell section connection
First level shell section and the second horizontal shell section；There is the flow-stopping plate being obliquely installed, the flow-stopping plate in the first shell
Between the upright shell section and the second horizontal shell section, it is horizontal that the flow-stopping plate lower edge is located at described second for top edge
In shell section.
In the technical solution of the utility model, by the design of system, so that using micro-nano bubble synergy ozone exhaust gas
When processing unit, almost problem without secondary pollution, resource consumption is small, and greenhouse effects are low, and facility operation is reliable and stable, failure rate pole
Low, maintenance is easy, and operating cost is low, and the waste disposal come out derived from treatment process is simple, can handle a variety of organic wastes
Gas, thus the problem of having taken into account treatment effect and cost.
Detailed description of the invention
Fig. 1 is micro-nano bubble synergy ozone emission-control equipment schematic diagram provided by the embodiment of the utility model.
Specific embodiment
Existing emission-control equipment can not take into account the problem of cost and treatment effect well.
For this purpose, the utility model provides a kind of new micro-nano bubble synergy ozone emission-control equipment, to improve exhaust gas
Clean-up effect, while reducing corresponding processing cost.
More clearly to indicate, the utility model is described in detail with reference to the accompanying drawing.
The utility model embodiment provides a kind of micro-nano bubble synergy ozone emission-control equipment, please refers to Fig. 1.
The micro-nano bubble synergy ozone emission-control equipment includes tangential air inlet cyclone 110, air hose 120, pumping
System 130, first shell 140, micro-nano bubble reaction unit tower 150, anion generation system 160, micro-nano bubble generate
System (not marking) and ozone generating system 190.
Tangential air inlet cyclone 110 has ejection air port (not shown), refluxing opening (not marking) and tangent air inlet 111.
Air hose 120 has bottom interface (not shown), top interface (not shown), anion inlet (not marking), micro-
Nano bubble inlet (not marking), ozone inlet (not marking) and bleeding point (not shown).
The ejection air port of the tangential air inlet cyclone 110 of bottom interface connection of air hose 120, so that air hose
120 are located at tangential 110 top of air inlet cyclone, as shown in Figure 1.
Micro-nano bubble reaction unit tower 150 has lower air inlet (not shown), filler demisting layer 151 and upper air outlet
152。
First shell 140 is connected to the top interface of air hose 120 and the lower air inlet of micro-nano bubble reaction unit tower 150
Between.
The anion inlet of connection 120 side wall of air hose of anion generation system 160.
The micro-nano bubble inlet of micro-nano bubble generation system (not marking) connection 120 side wall of air hose.
The ozone inlet of connection 120 side wall of air hose of ozone generating system 190.
The bleeding point of connection 120 side wall of air hose of extract system 130.
In the present embodiment, micro-nano bubble inlet includes that the first inlet (not marking) and the second inlet (are not marked
Note).On 120 side wall of air hose, the position of the second inlet is higher than the position of the first inlet.The micro-nano bubble generates system
System includes the first micro-nano air Bubble generating apparatus 170 and the second micro-nano air Bubble generating apparatus 180.First micro-nano bubble generates
Device 170 connects the first inlet, and the second micro-nano air Bubble generating apparatus 180 connects the second inlet.
In the present embodiment, setting air hose 120 stands on tangential 110 top of air inlet cyclone, i.e., air hose 120 is set up vertically.
In other embodiments, air hose can also have one tilt angle.
In the present embodiment, air hose 120 includes 4 pipelines arranged side by side, due to showing two pipelines therein in Fig. 1 (not
Distinguish mark), other two pipeline due to just being blocked by two pipelines shown in FIG. 1, do not show.Air hose 120 includes
Multiple pipelines, the sectional area for facilitating each pipeline reduces, and then is more advantageous to and handles exhaust gas therein.Other implementations
In example, air hose may include multiple pipelines of other numbers arranged side by side.
In the present embodiment, the bleeding point of air hose 120 is set to the top side wall of the pipeline, and extract system 130 is
Axial flow blower is arranged in 120 top side wall of air hose.
In the present embodiment, first shell 140 include first level shell section (not marking), the second horizontal shell section (not marking) and
Upright shell section (not marking).The top interface of the first level shell section connection air hose 120.The second horizontal shell section connection is micro-
The lower air inlet of nano bubble reaction unit tower 150.The upright shell section connects the first level shell section and second water
Flat shell section, at this point, " Z " type is presented in entire first shell 140.In other embodiments, first shell is also possible to other shapes.
In the present embodiment, there is the flow-stopping plate 141 being obliquely installed, 141 top edge of flow-stopping plate is located at institute in first shell 140
It states between upright shell section and the second horizontal shell section, also, 141 lower edge of flow-stopping plate is located in the described second horizontal shell section,
I.e. flow-stopping plate 141 is tilted to the described second horizontal shell section, as shown in fig. 1.The setting of flow-stopping plate 141 enables to, and has
Before entering micro-nano bubble reaction unit tower 150, corresponding steam condenses into the gas of steam because encountering flow-stopping plate 141
Liquid water, to drip back into first shell 140, to reduce steam into subsequent micro-nano bubble reaction unit tower 150
In.
In the present embodiment, ozone generating system 190 can be pouring-in ozone generator.
In the present embodiment, on 120 side wall of air hose, be arranged the micro-nano bubble inlet position be higher than it is described bear from
The position of sub- inlet, the position that the ozone inlet is arranged are higher than the position of the micro-nano bubble inlet, institute are arranged
The position for stating bleeding point is higher than the position of the ozone inlet, can be in conjunction with reference to shown in Fig. 1.Such set-up mode is advantageous
Anion processing is first passed through in corresponding exhaust gas, is handled using micro-nano bubble, and it is corresponding to participate in provided ozone
Treatment process, to be conducive to preferably handle exhaust gas.
With continued reference to FIG. 1, micro-nano bubble synergy ozone emission-control equipment provided by the present embodiment further includes following
Ring water pump 101, sandfiltration pot 102 and cyclic water tank 103.The refluxing opening of tangential air inlet cyclone 110 connects water circulating pump 101
Water inlet (not marking), to be conducive to the water extraction that will be generated in tangential air inlet cyclone 110 by water circulating pump 101.
The water inlet (not marking) of water outlet (not marking) the connection sandfiltration pot 102 of water circulating pump 101, sandfiltration pot 102 is by corresponding water
It is filtered.The water inlet (not marking) of water outlet (not marking) the connection cyclic water tank 103 of sandfiltration pot 102, cyclic water tank 103
Water outlet (not marking) and meanwhile connect anion generation system 160 water inlet (not marking) and micro-nano bubble generation system
Water inlet (not marking).As it can be seen that the present embodiment directly utilizes cyclic water tank 103, while supplying water, simplifies to two systems
System.
In micro-nano bubble synergy ozone emission-control equipment provided in this embodiment, cut when exhaust gas (organic exhaust gas) enters
To after air inlet cyclone 110, due to tangentially enter the wind 111 section of tangent air inlet of cyclone 110 much smaller than internal chamber and
The open-topped section (again smaller than the total cross section of each pipeline of air hose 120), therefore, the flow section of exhaust gas increased dramatically,
Exhaust gas wind speed decreased.At this point, the exhaust gas containing big grit (particulate matter) can be settled under the effect of gravity, and contain smaller
The exhaust gas (can also claim dusty gas) of grain object enters air hose 120.
During dusty gas is walked in air hose 120, anion generation system 160 is passed through anion.Anion produces
Raw 160 mesohigh of system atomization promotes the movement (anion generation system 160 usually has high voltage functionality) of water, makes the micro- of electrification
Small water droplet is split into that surface layer is negatively charged and internal layer is positively charged.Electronegative water droplet surface layer and atom or molecule combination in air,
Form anion.Heavier water droplet internal layer then sinks under the effect of gravity, thus can obtain a large amount of anion in air.
After smaller particle object and part organic gas micel in exhaust gas are coated by anion, settle down.
The exhaust gas for continuing uplink can be in conjunction with the micro-nano bubble for continuing injection in air hose 120, and micro-nano bubble is immediately right
Part organic exhaust gas carries out oxygenolysis.These micro-nano bubbles generate (micro-nano bubble production by micro-nano bubble generation system
Raw system is generally also integrated with the action function of high-pressure hydraulic pump).Micro-nano bubble is that generation diameter is micro- 50 when bubble occurs
Rice (μm) micro-bubble below, can also be micron bubble or nano bubble according to its diameter range respectively.Micro-nano bubble
After generation, bubble oneself is shunk, and in this process because bubble becomes small so the rate of climb is slowed by, causes to melt efficiency
It is high.Thawing efficiency is higher, and the energy of generation is bigger, is better able to interrupt the macromolecular chain of organic matter, this i.e. corresponding super oxygen
Change effect.And the micro-nano air Bubble generating apparatus of two-stage is used in the present embodiment, so that organic matter in exhaust gas more be made to decompose
More thoroughly.
Later, exhaust gas uplink.The ozone that ozone generating system 190 generates, ozone is added can be big by what is do not interrupted completely
Molecular organic continues to be oxidized to small organic molecule or carbon dioxide and water.
And in 120 side wall of air hose, it is arranged corresponding axial flow blower (extract system 130), axial flow blower can will purify
Gas afterwards is passed to micro-nano bubble reaction unit tower 150, and the filler demisting layer 151 into tower, to remove water mist, then is discharged into
In atmosphere.
In above process, in air hose 120, anion generation system 160 and micro-nano bubble generation system are being handled
In the process, liquid water is all generated, remains pollutant component in these liquid waters, after returning to tangential air inlet cyclone 110,
It is first extracted by water circulating pump 101, the refluxing opening by tangentially entering the wind cyclone 110 is passed through water circulating pump 101, then by recirculated water
The water outlet of pump 101 is sent into the water inlet of sandfiltration pot 102.It is filtered by sandfiltration pot 102, clean water after filtering is entered
Cyclic water tank 103, then via cyclic water tank 103, it is supplied to anion generation system 160 and micro-nano bubble generation system, i.e.,
Clean water is returned again in processing equipment system.Therefore, corresponding system usually only needs periodic cleaning water tank.
In micro-nano bubble synergy ozone emission-control equipment provided in this embodiment, anion high-pressure atomization system is utilized
(anion generation system 160) is combined with micro-nano air bubble apparatus (micro-nano bubble generation system), will be generated distinctive super
Oxide (super oxide, wherein super oxygen indicates super oxidation, passes through micro-nano bubble and realizes super oxidation) and work
Property hydroxy (hydroxyl radical), these substance diameters at 50 microns hereinafter, the large specific surface area of its own, rise
Speed is slow, itself pressurization dissolution, surface electrification, can generate a large amount of free radicals, shows energy instantaneous relase huge energy, has
Strong oxidizing property.Also, in reaction environment, suitable ozone is added by ozone generating system 190, supplements and disappears in cracking reaction
The oxygen element of consumption, meanwhile, make treatment process that there is stronger oxidisability, can organic matter is dirty or subdivision solution eliminate that (chemistry is anti-
Answer), while dirty component damage can be separated and suspension surface, promote volatile organic matter (volatile organic
Compounds, VOCs) it is partially converted into carbon dioxide and water, or be mineralized and to form graininess submerged.Submerged portion
The characteristic divided will not be burnt, not dissolved, without toxicity.It is tested through engineer application, corresponding system is to toluene, dimethylbenzene, vinegar
The VOCs such as acid butyl ester, acetone, isopropanol, tetrachloro-ethylene can reach 85% or more removal rate.
The design scheme of micro-nano bubble synergy ozone emission-control equipment provided in this embodiment gives up with domestic traditional
Gas disposal scheme thinking is different, almost problem without secondary pollution, and resource consumption is small, and greenhouse effects are low, and facility operation is reliable and stable,
Failure rate is extremely low, and maintenance is easy, and operating cost is low, and the waste disposal come out derived from treatment process is simple, can handle more
Kind organic exhaust gas.
Although the utility model discloses as above, the utility model is not limited to this.Anyone skilled in the art,
It does not depart from the spirit and scope of the utility model, can make various changes or modifications, therefore the protection scope of the utility model
It should be defined by the scope defined by the claims..
Claims (10)
1. a kind of micro-nano bubble synergy ozone emission-control equipment, which is characterized in that including：
Tangential air inlet cyclone, has ejection air port, refluxing opening and tangent air inlet；
Air hose has bottom interface, top interface, anion inlet, micro-nano bubble inlet, ozone inlet and pumping
Mouthful；
The bottom interface connects the ejection air port；
Micro-nano bubble reaction unit tower has lower air inlet, filler demisting layer and upper air outlet；
First shell is connected between the top interface and the lower air inlet；
Anion generation system connects the anion inlet of the air hose side wall；
Micro-nano bubble generation system connects the micro-nano bubble inlet of the air hose side wall；
Ozone generating system connects the ozone inlet of the air hose side wall；
Extract system connects the bleeding point of the air hose side wall.
2. micro-nano bubble synergy ozone emission-control equipment as described in claim 1, which is characterized in that in the air hose side
On wall, the position of the micro-nano bubble inlet is higher than the position of the anion inlet.
3. micro-nano bubble synergy ozone emission-control equipment as claimed in claim 2, which is characterized in that in the air hose side
On wall, the position of the ozone inlet is higher than the position of the micro-nano bubble inlet.
4. micro-nano bubble synergy ozone emission-control equipment as claimed in claim 3, which is characterized in that in the air hose side
On wall, the position of the bleeding point is higher than the position of the ozone inlet.
5. micro-nano bubble synergy ozone emission-control equipment as claimed in claim 4, which is characterized in that the micro-nano gas
Steeping inlet includes the first inlet and the second inlet；On the air hose side wall, the position of second inlet is higher than
The position of first inlet；The micro-nano bubble generation system includes that the first micro-nano air Bubble generating apparatus and second are micro-
Nano bubble generation device；The first micro-nano air Bubble generating apparatus connects first inlet, and described second is micro-nano
Air Bubble generating apparatus connects second inlet.
6. micro-nano bubble synergy ozone emission-control equipment as described in claim 1, which is characterized in that the ozone generates
System is pouring-in ozone generator.
7. micro-nano bubble synergy ozone emission-control equipment as described in claim 1, which is characterized in that further include recirculated water
Pump, sandfiltration pot and cyclic water tank, the refluxing opening connect the water inlet of the water circulating pump, and the water outlet of the water circulating pump connects
The water inlet of the sandfiltration pot is connect, the water outlet of the sandfiltration pot connects the water inlet of the cyclic water tank, the cyclic water tank
Water outlet connect the water inlet of the anion generation system and the water inlet of the micro-nano bubble generation system simultaneously.
8. micro-nano bubble synergy ozone emission-control equipment as described in claim 1, which is characterized in that the air hose includes
Multiple pipelines arranged side by side.
9. micro-nano bubble synergy ozone emission-control equipment as claimed in claim 8, which is characterized in that the bleeding point is set
It is placed in the top side wall of the pipeline, the extract system is axial flow blower.
10. micro-nano bubble synergy ozone emission-control equipment as described in claim 1, which is characterized in that the first shell
Body includes first level shell section, the second horizontal shell section and upright shell section；The first level shell section connects the top interface；Institute
It states the second horizontal shell section and connects the lower air inlet；The upright shell section connects the first level shell section and second level
Shell section；There is the flow-stopping plate being obliquely installed, the flow-stopping plate top edge is located at the upright shell section and institute in the first shell
It states between the second horizontal shell section, the flow-stopping plate lower edge is located in the described second horizontal shell section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820117408.0U CN208130800U (en) | 2018-01-24 | 2018-01-24 | Micro-nano bubble synergy ozone emission-control equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820117408.0U CN208130800U (en) | 2018-01-24 | 2018-01-24 | Micro-nano bubble synergy ozone emission-control equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208130800U true CN208130800U (en) | 2018-11-23 |
Family
ID=64285418
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820117408.0U Expired - Fee Related CN208130800U (en) | 2018-01-24 | 2018-01-24 | Micro-nano bubble synergy ozone emission-control equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN208130800U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111760718A (en) * | 2020-05-09 | 2020-10-13 | 四川省宜宾环球集团有限公司 | Paint spraying process waste gas treatment system |
-
2018
- 2018-01-24 CN CN201820117408.0U patent/CN208130800U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111760718A (en) * | 2020-05-09 | 2020-10-13 | 四川省宜宾环球集团有限公司 | Paint spraying process waste gas treatment system |
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Granted publication date: 20181123 |