CN106076052A - A kind of atomizing air cleaning system - Google Patents
A kind of atomizing air cleaning system Download PDFInfo
- Publication number
- CN106076052A CN106076052A CN201610573191.XA CN201610573191A CN106076052A CN 106076052 A CN106076052 A CN 106076052A CN 201610573191 A CN201610573191 A CN 201610573191A CN 106076052 A CN106076052 A CN 106076052A
- Authority
- CN
- China
- Prior art keywords
- droplet
- dust
- laden
- atomization
- condensation
- Prior art date
Links
- 239000003570 air Substances 0.000 title claims abstract description 34
- 238000004140 cleaning Methods 0.000 title claims abstract description 15
- 238000009833 condensation Methods 0.000 claims abstract description 36
- 230000005494 condensation Effects 0.000 claims abstract description 35
- 239000007789 gases Substances 0.000 claims abstract description 27
- 238000000889 atomisation Methods 0.000 claims abstract description 21
- 239000007788 liquids Substances 0.000 claims abstract description 21
- 239000003595 mist Substances 0.000 claims abstract description 11
- 238000000746 purification Methods 0.000 claims abstract description 7
- 238000005057 refrigeration Methods 0.000 claims description 14
- 239000011901 water Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 4
- 239000000463 materials Substances 0.000 abstract description 7
- 230000002000 scavenging Effects 0.000 abstract description 7
- 230000000694 effects Effects 0.000 description 12
- 239000002245 particles Substances 0.000 description 6
- 230000002708 enhancing Effects 0.000 description 5
- 238000000034 methods Methods 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000006011 modification reactions Methods 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 230000000903 blocking Effects 0.000 description 2
- 239000004065 semiconductors Substances 0.000 description 2
- 238000002604 ultrasonography Methods 0.000 description 2
- 210000001331 Nose Anatomy 0.000 description 1
- 238000010521 absorption reactions Methods 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000000354 decomposition reactions Methods 0.000 description 1
- 239000000686 essences Substances 0.000 description 1
- 239000008187 granular materials Substances 0.000 description 1
- 239000004615 ingredients Substances 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters, i.e. particle separators or filtering processes specially modified for separating dispersed particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters, i.e. particle separators or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0057—Regenerating the filter material in the filter
- B01D46/0067—Regenerating the filter material in the filter by acting counter-currently on the filtering surface (e.g. flushing)
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D51/00—Auxiliary pretreatment of gases or vapours to be cleaned
- B01D51/02—Amassing the particles, e.g. by flocculation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D51/00—Auxiliary pretreatment of gases or vapours to be cleaned
- B01D51/10—Conditioning the gas to be cleaned
Abstract
Description
Technical field
The present invention relates to the technical field of air treating, particularly relate to a kind of atomizing air cleaning system.
Background technology
Dust pollution, as the primary ingredient of air pollution, directly affects the health of human body.Inhalable particles refers to Entered the general name of the granule of human respiratory tract by nose or mouth, use PM10Represent.Wherein, PM2.5It is referred to as ultra-fine grain.Particle Footpath is the least, the biggest to harm.Therefore, dust pollution question is controlled significant.
Air cleaning facility great majority in the market use dry-type multilayer Filtration Adsorption method (such as HEPA mistake Filter, activated carbon adsorption, Electrostatic Absorption etc.).There is certain defect in such technology, particularly high efficiency particulate air filter is led because of blockage problem Cause working life shorter, easily cause secondary pollution.And scavenging material need to frequently be changed, thus improve use cost.
Summary of the invention
The present invention, by providing a kind of atomizing air cleaning system, solves the work caused in prior art because of blocking Life-span is short and technical problem frequently changed by scavenging material, it is achieved that reduce the technique effect of use cost.
The invention provides a kind of atomizing air cleaning system, at least include:
Atomization portion, is used for producing atomized liquid；
Cohesion portion, for being condensed with air to be clean by described atomized liquid, forms dust-laden droplet；
Condensation part, for liquefying described dust-laden droplet；
Except mist portion, for removing the droplet in described dust-laden droplet, the gas after being purified.
Further, described atomization portion at least includes: water tank and atomization member；Described atomization member is arranged on described water tank In, produce described atomized liquid.
Further, described cohesion portion is serpentine pipe.
Further, the medium input of described serpentine pipe is positioned at the lower end of described serpentine pipe, the medium of described serpentine pipe Outfan is positioned at the upper end of described serpentine pipe.
Further, described condensation part at least includes: condensation flow-inclining fin group and refrigeration part；The system of described refrigeration part Cold end is connected with described condensation flow-inclining fin group；Described dust-laden droplet is by described condensation flow-inclining fin group, and is liquefied.
Further, the condensation flow-inclining fin in described condensation flow-inclining fin group is staggered.
Further, described at least include except mist portion:
Drainage screen, for filtering described dust-laden droplet, removes the droplet in described dust-laden droplet, obtain described only Gas after change；
Watering portion, for keeping the moistening of described drainage screen.
Further, the most at least include:
Intensification portion, for heating up to the described purified gas obtained.
Further, described intensification portion at least includes: radiating fin group and heater block；The fire end of described heater block It is connected with described radiating fin group；Described purified gas is by described radiating fin group, and is heated up.
Further, described refrigeration part and described heater block are same temperature equipment or are not same temperature equipment.
The one or more technical schemes provided in the present invention, at least have the following technical effect that or advantage:
1, first atomized liquid is condensed with air to be clean, forms dust-laden droplet, then dust-laden droplet is liquefied, then Remove the droplet in dust-laden droplet, the gas after being purified, it is achieved that the atomization wet purification to dusty gas.With dry type mistake Filter mode is compared, and wet filter avoids the generation of the blocked state of filter plant, not only extends the working life of equipment, keeps away Exempt to cause secondary pollution, and avoid and frequently change scavenging material, reduce use cost.
2, the cohesion portion in the present invention is serpentine pipe, and the medium input of serpentine pipe is positioned at the lower end of serpentine pipe, spiral The medium outfan of pipe is positioned at the upper end of serpentine pipe, when extending the cohesion in serpentine pipe of atomized liquid and air to be clean Between, thus ensure that atomized liquid and air to be clean can fully condense, and then ensure that the clean-up effect of the present invention.
3, the condensation flow-inclining fin in the condensation flow-inclining fin group of the condensation part in the present invention is staggered, thus enhances The condensation effect of mixing air, and then enhance the clean-up effect of the present invention.
4, by arranging watering portion, it is achieved that the automatically cleaning to drainage screen, thus avoid drainage screen and block.
5, by arranging intensification portion, the temperature of condensed cryogenic gas is raised, thus improves the practicality of the present invention Property.
6, the refrigeration part in the present invention and heater block can be same temperature equipments, thus improve the utilization of equipment Rate.
Accompanying drawing explanation
The STRUCTURE DECOMPOSITION figure of the atomizing air cleaning system that Fig. 1 provides for the embodiment of the present invention；
The structural representation of the atomizing air cleaning system that Fig. 2 provides for the embodiment of the present invention；
Fig. 3 be in Fig. 2 along A-A to profile；
Fig. 4 be in Fig. 2 along B-B to profile；
Wherein, 1-atomization portion, 2-cohesion portion, 3-condensation part, 4-removes mist portion, and 5-water tank, 6-atomization member, 7-condenses baffling Fins set, 8-refrigeration part, 9-drainage screen, 10-intensification portion, 11-radiating fin group, 12-heater block, 13-air-introduced machine.
Detailed description of the invention
The embodiment of the present invention, by providing a kind of atomizing air cleaning system, solves in prior art and causes because of blocking Working life is short and technical problem frequently changed by scavenging material, it is achieved that reduce the technique effect of use cost.
Technical scheme in the embodiment of the present invention is for solving above-mentioned technical problem, and general thought is as follows:
First atomized liquid is condensed with air to be clean, forms dust-laden droplet, then dust-laden droplet is liquefied, then remove Remove the droplet in dust-laden droplet, the gas after being purified, it is achieved that the atomization wet purification to dusty gas.With dry filter Mode is compared, and wet filter avoids the generation of the blocked state of filter plant, not only extends the working life of equipment, it is to avoid Cause secondary pollution, and avoid and frequently change scavenging material, reduce use cost.
In order to be more fully understood that technique scheme, below in conjunction with Figure of description and specific embodiment to upper State technical scheme to be described in detail.
See Fig. 1 and Fig. 2, the atomizing air cleaning system that the embodiment of the present invention provides, at least include:
Atomization portion 1, is used for producing atomized liquid；
In the present embodiment, atomization portion 1 at least includes: water tank 5 and atomization member 6；Atomization member 6 is arranged in water tank 5, Produce atomized liquid.
Wherein, atomization member 6 can be but not limited to ultrasound atomizer.
Cohesion portion 2, for being condensed with air to be clean by atomized liquid, forms dust-laden droplet；
In the present embodiment, cohesion portion 2 is serpentine pipe.
In order to extend atomized liquid and the air to be clean pool time in serpentine pipe, thus ensure atomized liquid and treat Purifying air can fully condense, the medium input of serpentine pipe is positioned at the lower end of serpentine pipe, the medium outfan position of serpentine pipe Upper end in serpentine pipe.
Condensation part 3, for liquefying dust-laden droplet；
In the present embodiment, condensation part 3 at least includes: condensation flow-inclining fin group 7 and refrigeration part 8；The system of refrigeration part 8 Cold end is connected with condensation flow-inclining fin group 7；Dust-laden droplet is by condensation flow-inclining fin group 7, and is liquefied.
Seeing Fig. 3, in order to strengthen the condensation effect of mixing air, the condensation flow-inclining fin in condensation flow-inclining fin group 7 is handed over Staggered arrangement arranges.
Except mist portion 4, for removing the droplet in dust-laden droplet, the gas after being purified.
In the present embodiment, at least include except mist portion 4:
Drainage screen 9, for filtering dust-laden droplet, removes the droplet in dust-laden droplet, the gas after being purified；
In the present embodiment, drainage screen 9 is 120 mesh steel wires.
Watering portion, for keeping the moistening of drainage screen 9.
In order to the gas heating after the low temperature purification that will obtain is to room temperature, the most at least include:
Intensification portion 10, for heating up to the purified gas obtained.
Seeing Fig. 4, in the present embodiment, intensification portion 10 at least includes: radiating fin group 11 and heater block 12；Heating part The fire end of part 12 is connected with radiating fin group 11；Purified gas passes through radiating fin group 11, and is heated up.
It should be noted that refrigeration part 8 and heater block 12 are same temperature equipment or are not same temperature equipment.
When refrigeration part 8 and heater block 12 are same temperature equipment, refrigeration part 8 and heater block 12 can be but It is not limited to semiconductor chilling plate.
The operation principle of the embodiment of the present invention is as follows:
The most mixed at serpentine pipe by 10 μm atomization particles produced by ultrasound atomizer and the respirable dust below 5 μm Conjunction, mutually collision, capture are condensed into larger particles and enter condensation part 3.Semiconductor chilling plate will condensation by condensation flow-inclining fin The temperature in portion 3 is reduced to below condensing temperature, and bulky grain droplet, through condensation flow-inclining fin group 7, is liquefied.Surplus air is with few Part droplet enters except mist portion 4.120 mesh steel wires decompose the bubble contact area with increase bubble with water, absorb residue droplet. After except mist portion 4, residual gas is low temperature pure air, and it is by carrying out heat convection with radiating fin, and temperature raises Draw to room temperature and by air-introduced machine 13.
[technique effect]
1, first atomized liquid is condensed with air to be clean, forms dust-laden droplet, then dust-laden droplet is liquefied, then Remove the droplet in dust-laden droplet, the gas after being purified, it is achieved that the atomization wet purification to dusty gas.With dry type mistake Filter mode is compared, and wet filter avoids the generation of the blocked state of filter plant, not only extends the working life of equipment, keeps away Exempt to cause secondary pollution, and avoid and frequently change scavenging material, reduce use cost.
2, the cohesion portion 2 in the embodiment of the present invention is serpentine pipe, and the medium input of serpentine pipe is positioned under serpentine pipe End, the medium outfan of serpentine pipe is positioned at the upper end of serpentine pipe, extends atomized liquid and air to be clean in serpentine pipe Pool time, thus ensure that atomized liquid and air to be clean can fully condense, and then ensure that the embodiment of the present invention Clean-up effect.
3, the condensation flow-inclining fin in the condensation flow-inclining fin group 7 of the condensation part 3 in the embodiment of the present invention is staggered, from And enhance the condensation effect of mixing air, and then enhance the clean-up effect of the embodiment of the present invention.
4, the drainage screen 9 in the embodiment of the present invention is 120 mesh steel wires, and its effect is to be divided by the bubble that condensed gas produces Solution becomes minute bubbles, thus beneficially remains droplet in condensing gas and be fully contacted with water, and then disposes residue droplet and condense Grain, enhances the purification function of the embodiment of the present invention.
5, by arranging watering portion, it is achieved that the automatically cleaning to drainage screen 9, thus avoid drainage screen 9 and block.
6, by arranging intensification portion 10, the temperature of condensed cryogenic gas is raised, thus improve the present invention and implement The practicality of example.
7, the refrigeration part 8 in the embodiment of the present invention and heater block 12 can be same temperature equipments, thus improve The utilization rate of equipment.
The particle disposal of the embodiment of the present invention is effective, and when the ratio of mist particle diameter, 1.25 < k, < time in 5, capture rate can Reach 82%-91%.The embodiment of the present invention makes traditional air cleaning facility have new extension on new technique, from dry filter Formula, inefficient highly water intensive wet cleaner expand to efficient ultrasonic atomized agglomeration technology.
Although preferred embodiments of the present invention have been described, but those skilled in the art once know basic creation Property concept, then can make other change and amendment to these embodiments.So, claims are intended to be construed to include excellent Select embodiment and fall into all changes and the amendment of the scope of the invention.
Obviously, those skilled in the art can carry out various change and the modification essence without deviating from the present invention to the present invention God and scope.So, if these amendments of the present invention and modification belong to the scope of the claims in the present invention and equivalent technologies thereof Within, then the present invention is also intended to comprise these change and modification.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610573191.XA CN106076052A (en) | 2016-07-20 | 2016-07-20 | A kind of atomizing air cleaning system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610573191.XA CN106076052A (en) | 2016-07-20 | 2016-07-20 | A kind of atomizing air cleaning system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106076052A true CN106076052A (en) | 2016-11-09 |
Family
ID=57221105
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610573191.XA CN106076052A (en) | 2016-07-20 | 2016-07-20 | A kind of atomizing air cleaning system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106076052A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107638759A (en) * | 2017-09-20 | 2018-01-30 | 华北理工大学 | A kind of atmosphere pollution processing equipment |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2348731A1 (en) * | 1976-04-23 | 1977-11-18 | Brunswick Corp | Filtration system for particle loaded gas - esp. fast moving, hot, corrosive gas, is cleaned repetitively |
| CN1191290A (en) * | 1997-02-10 | 1998-08-26 | 北星技术有限公司 | Separation apparatus and method |
| CN101224367A (en) * | 2007-10-26 | 2008-07-23 | 东南大学 | Method of removing PM2.5 and gaseous pollutant using steam phase transition and device thereof |
| CN102059033A (en) * | 2010-12-21 | 2011-05-18 | 哈尔滨工程大学 | Condensation agglomeration trapping method and device of ultrafine particulate matter in combustion gas |
| CN202221262U (en) * | 2011-08-01 | 2012-05-16 | 无锡市众博换热器有限公司 | Heat exchange fins of condenser |
| CN104864523A (en) * | 2014-02-25 | 2015-08-26 | 崔骥 | Personal air cleaning device using washing and active air feeding principles |
| CN204815978U (en) * | 2015-07-30 | 2015-12-02 | 中电投远达环保工程有限公司 | Install in dust removal defroster of desulfurizing tower |
| CN105180187A (en) * | 2015-07-27 | 2015-12-23 | 航天环境工程有限公司 | Zero-water-consumption zero-wastewater-draining desulfurization system and application |
-
2016
- 2016-07-20 CN CN201610573191.XA patent/CN106076052A/en not_active Application Discontinuation
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2348731A1 (en) * | 1976-04-23 | 1977-11-18 | Brunswick Corp | Filtration system for particle loaded gas - esp. fast moving, hot, corrosive gas, is cleaned repetitively |
| CN1191290A (en) * | 1997-02-10 | 1998-08-26 | 北星技术有限公司 | Separation apparatus and method |
| CN101224367A (en) * | 2007-10-26 | 2008-07-23 | 东南大学 | Method of removing PM2.5 and gaseous pollutant using steam phase transition and device thereof |
| CN102059033A (en) * | 2010-12-21 | 2011-05-18 | 哈尔滨工程大学 | Condensation agglomeration trapping method and device of ultrafine particulate matter in combustion gas |
| CN202221262U (en) * | 2011-08-01 | 2012-05-16 | 无锡市众博换热器有限公司 | Heat exchange fins of condenser |
| CN104864523A (en) * | 2014-02-25 | 2015-08-26 | 崔骥 | Personal air cleaning device using washing and active air feeding principles |
| CN105180187A (en) * | 2015-07-27 | 2015-12-23 | 航天环境工程有限公司 | Zero-water-consumption zero-wastewater-draining desulfurization system and application |
| CN204815978U (en) * | 2015-07-30 | 2015-12-02 | 中电投远达环保工程有限公司 | Install in dust removal defroster of desulfurizing tower |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107638759A (en) * | 2017-09-20 | 2018-01-30 | 华北理工大学 | A kind of atmosphere pollution processing equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2121866C1 (en) | Method and device for wet cleaning of gases | |
| CN204678528U (en) | A kind of air cleaning unit | |
| CN104764098A (en) | Air comprehensive purifying and regulating method and air comprehensive purifying and regulating device | |
| US3353335A (en) | Exhaust gas treatment | |
| EP2466085A2 (en) | Centrifugal, wet-type air cleaner | |
| CN204170568U (en) | Micropore bubbling formula air purifier | |
| CN103657326A (en) | Direct injection type air purifier | |
| CN105107365B (en) | Flue gas composite phase-change dust-removing and desulfurization process and device | |
| CN103480223B (en) | Wet-type fume purification system and purification method for high smoke speed PM2.5 and pollutant | |
| CN104226479A (en) | Efficient wet type electric dedusting and purifying device and method for smoke obtained after wet desulphurization | |
| CN205613230U (en) | Fountain air purification device | |
| CN105749679B (en) | A kind of high temperature fume dust removal method and system | |
| US6638343B1 (en) | Exhaust gas treating device | |
| CN206560761U (en) | One kind welding flue gas purifying equipment | |
| CN205783364U (en) | A kind of ventilating system air pollutant purification apparatus | |
| CN105318443B (en) | A kind of air purifier | |
| CN205700102U (en) | A kind of exhaust gas purification and treatment device of band gas washing function | |
| CN108019852A (en) | A kind of air purifier for being convenient for changing filtration apparatus | |
| CN104815495A (en) | Water mist air purifier | |
| CN202401267U (en) | System for utilizing flue gas waste heat of setting machine and conducting wet type electrostatic process on flue gas of setting machine | |
| CN104548824B (en) | For removing the fine grain apparatus and method in gas | |
| CN108561212B (en) | Automobile exhaust treatment device | |
| CN205461614U (en) | Waste gas dust collecting equipment | |
| CN106178829A (en) | A kind of air cleaner and air purification method | |
| CN102872671B (en) | Asphalt waste gas purifying method and device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161109 |