CN205948569U - High -efficient wet dust collector - Google Patents
High -efficient wet dust collector Download PDFInfo
- Publication number
- CN205948569U CN205948569U CN201620683529.2U CN201620683529U CN205948569U CN 205948569 U CN205948569 U CN 205948569U CN 201620683529 U CN201620683529 U CN 201620683529U CN 205948569 U CN205948569 U CN 205948569U
- Authority
- CN
- China
- Prior art keywords
- dust collector
- type dust
- air inlet
- air
- efficiency wet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000000428 dust Substances 0.000 title claims abstract description 31
- 230000000694 effects Effects 0.000 claims abstract description 7
- 238000012423 maintenance Methods 0.000 claims abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 37
- 238000005204 segregation Methods 0.000 claims description 8
- 230000003139 buffering effect Effects 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 11
- 239000002912 waste gas Substances 0.000 abstract description 10
- 238000000746 purification Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000012545 processing Methods 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 5
- 238000000889 atomisation Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 230000006378 damage Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000002685 pulmonary effect Effects 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 206010058467 Lung neoplasm malignant Diseases 0.000 description 1
- 206010035745 Pneumonitis chemical Diseases 0.000 description 1
- 206010040047 Sepsis Diseases 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 125000005605 benzo group Chemical group 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000011258 core-shell material Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 239000004531 microgranule Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000243 photosynthetic effect Effects 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 208000013223 septicemia Diseases 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 201000001811 toxic pneumonitis Diseases 0.000 description 1
Landscapes
- Separation Of Particles Using Liquids (AREA)
Abstract
The utility model provides a high -efficient wet dust collector, including the air inlet, the air inlet is linked together with humidifier tube, one side that humidifier tube kept away from the air inlet is linked together with helical coiled passage, be provided with helical blade in the helical coiled passage, the spiral is said and still is linked together with central bobbin, whirl board defroster is connected to the one end of center bobbin, other end connection air -purifying chamber, the air -purifying chamber still is linked together with the gas vent. The utility model discloses compact structure, simple structure and reliable, a great deal of characteristics such as dust removal separation efficiency is high, the occupation of land space is little, investment province, environmental protection and energy saving, operate is reliable and stable, the maintenance is convenient. The dust waste gas that produces in the time of effectively getting rid of the production and processing operation etc. And purifying effect is good, and the high not high scheduling problem of big efficiency that takes up an area of of traditional wet purification investment consuming excessive quantities of energy and resources has been solved effectively to the security height.
Description
Technical field
This utility model is related to a kind of cleaner, more particularly, to a kind of high-efficiency wet-type dust collector.
Background technology
During the operation such as sanding and polishing, sanding, cut of dusting, the middle small particle dust waste gas of generation is that a kind of pollution is expanded
Dissipate big waste gas, the health of the dust waste gas main harm mankind.Elegant dust in an atmosphere often contains many toxic components,
As chromium, manganese, cadmium, lead, hydrargyrum, the heavy metal such as arsenic.After human body sucks dust, the microgranule less than 5 μm, easily gos deep into pulmonary, causes
Toxic pneumonitiss or pneumosilicosis, also can cause pulmonary carcinoma sometimes.Being deposited on the pollutant of pulmonary once being dissolved, blood will be directly invaded
Liquid, causes septicemia, and the pollutant not being dissolved, it is also possible to be absorbed by cell, lead to cyto-architectural destruction.Additionally,
Dust also can stain building, so that valuable ancient architecture is corroded.Drop to plant leaf surface dust can hinder photosynthetic
Effect, suppresses its growth.Additionally, various harmful gass and other pollutant of in the air can be adsorbed in the surface of dust grit,
And become their carrier, enter and can carry strong carcinogen benzo and antibacterial etc..The particularly floating dust containing heavy metal, energy
Promote the various chemical reactions in air, form secondary pollution.For this reason, dust waste gas is all severe contamination to human body to environment
Thing is it is necessary to perform dust waste gas purification dust removal process.
Utility model content
The purpose of this utility model is to solve involved technical problem in background technology, there is provided a kind of high-efficiency wet
Formula cleaner unit.
This utility model provides a kind of high-efficiency wet-type dust collector, and including air inlet, described air inlet is connected with humidifier tube
Logical, described humidifier tube is connected with helical duct away from the side of air inlet, is provided with helical blade, institute in described helical duct
State spiral channel to be also connected with center bobbin, one end of described center bobbin connects rotational flow plate defroster, and the other end connects net gas
Room, described air-purifying chamber is also connected with air vent.
When dusty gas is when entering air inlet, it is to make dusty gas and water close contact, using the mist in humidifier tube
Dust granules in shape water droplet and waste gas are fully contacted mixing, make gas humidity reach saturation, and fierce cohesion occurs in humidifier tube
After becoming larger dust-laden water droplet；Guide functions through spiral stream guidance passage, rotate advance.Get rid of under the action of the centrifugal force to wall
The grit in face is adhered to by the constantly dirty moisture film of inner wall of tower, flows down entrance circulating water pool along barrel, most of water droplet is in centrifugal force
Get rid of after removing to barrel under effect, purification gas carry out depth under built-in rotational flow plate defroster acts on and go divided by guaranteeing high going
Wet rate；Then pass through outer again after built-in vent passage enters tower top air-purifying chamber row.Solve the pollution of this dust waste gas air with thorough
Problem.
Preferably, it is provided with several nozzles in described humidifier tube, described nozzle is connected with feed pipe, described feed pipe is even
It is connected to water circulating pump.
Preferably, described water circulating pump draws water in water tank, is provided with thick effect dirt water segregation net and efficiently in described water tank
Dirt water segregation net.
Preferably, also include main tower, described main tower is arranged on base.
Preferably, described main tower is also equipped with observe maintenance door.
Preferably, also include electric cabinet, described electric cabinet is used for controlling the operation of water circulating pump.
Preferably, it is provided with the retaining hood for buffering in described air-purifying chamber.
In sum, this utility model has the advantage that：
This utility model compact conformation, structure is simple and reliable, and dedusting demisting efficiency is high, occupation of land space is little, reduced investment, ring
Protect energy-conservation, operation stable and reliable operation, the various features such as easy to maintenance.The dust producing during production and processing operation can effectively be removed
Waste gas etc., and good purification, the safe traditional wet that efficiently solves purifies the investment highly energy-consuming big efficiency of high occupation of land not
High the problems such as.
Brief description
Fig. 1 is the schematic diagram of the present embodiment；
Fig. 2 is the schematic top plan view of Fig. 1.
Specific embodiment
As shown in Figure 1-2, a kind of high-efficiency wet-type dust collector, including air inlet 1, described air inlet 1 is connected with humidifier tube 2
Logical, described humidifier tube 2 is connected with helical duct 3 away from the side of air inlet 1, is provided with helical-blade in described helical duct 3
Piece 4, described helical duct 3 is also connected with center bobbin 6, and one end of described center bobbin 6 connects rotational flow plate defroster 5, separately
One end connects air-purifying chamber 7, and described air-purifying chamber 7 is also connected with air vent 9.
It is provided with several nozzles 15, described nozzle 15 is connected with feed pipe 14, described feed pipe 14 in described humidifier tube 2
Connect to water circulating pump 13.Described water circulating pump 13 draws water in water tank 10, is provided with thick effect dirt water segregation in described water tank 10
Net 11 and efficient dirt water segregation net 12.
Also include main tower a, described main tower a is arranged on base 18.It is also equipped with described main tower a observing maintenance
Door 16.
Also include electric cabinet 17, described electric cabinet 17 is used for controlling the operation of water circulating pump 13.Setting in described air-purifying chamber 7
There is the retaining hood 8 for buffering.
In the presence of centrifugal induced draught fan malleation or negative pressure, dust waste gas enters humidifier tube 2 by air inlet 1 and carries out abundant gas
Liquid humidification contact mixing, is inside provided with nozzle 15 humidification and carries out water droplet atomization, contacted with each other collision with high speed dusty gas, make gas
Body humidity reaches saturation, and the air film of grit surface attachment is broken through, and so that grit is processed by water smoke high moisture.And tangentially enter at a high speed
Enter in main tower a, between the innovative inner core of this device-specific and shell, integral screw blade 4 particular design, makes inner core shell
Gap is in a complete helix passage 3, makes the atomization of humidification sections of atomization gas-liquid make rotation type motion after being fully contacted in passage and advances,
It is subject to the collision effect of centrifugal force etc. with the spin dust ion of motion of gas-liquid flow, light by the top-down moisture film of outer tube inner wall
Simple capture after dirty and flow to bottom of towe water tank 10 and so that gas-liquid is sufficiently separated, reach the purpose of dedusting eliminating water with moisture film；And
Add the rotational flow plate defroster layer 5 of a dehydrating demisting ultrahigh in efficiency in row, depth guarantee removes fog effect, through the gas after abundant process
Body enters tower upper end air-purifying chamber 7 by center bobbin 6, is externally arranged by tower top exhaust outlet 9 for gas after purifying for 8 through retaining hood
Put.This equipment only need to guarantee air inlet 1 connection sealing during using, and water circulating pump 13 works well, slightly imitates dirt water segregation
Net 11 and efficient dirt water segregation net 12 is intact and water tank 10 loads aqueous in specified range, such as notes abnormalities, please closes in time
Close power supply, normal use after exclusion exception, can be put into.
Described above is only to explain so that those of ordinary skill in the art's can completely implements this to of the present utility model
Scheme, but be not to restriction of the present utility model, those skilled in the art can be as needed after reading this specification
The present embodiment is made does not have the modification of creative contribution, and these are all not creative modifications.But as long as in this practicality
All protected by Patent Law in new right.
Claims (7)
1. a kind of high-efficiency wet-type dust collector it is characterised in that：Including air inlet (1), described air inlet (1) and humidifier tube (2) phase
Connection, described humidifier tube (2) is connected with helical duct (3) away from the side of air inlet (1), sets in described helical duct (3)
It is equipped with helical blade (4), described helical duct (3) is also connected with center bobbin (6), the one end at described center bobbin (6) is even
Connect rotational flow plate defroster (5), the other end connects air-purifying chamber (7), described air-purifying chamber (7) is also connected with air vent (9).
2. a kind of high-efficiency wet-type dust collector according to claim 1 it is characterised in that：It is provided with described humidifier tube (2)
Several nozzles (15), described nozzle (15) is connected with feed pipe (14), and described feed pipe (14) connects to water circulating pump (13).
3. a kind of high-efficiency wet-type dust collector according to claim 2 it is characterised in that：Described water circulating pump (13) is from water tank
(10) draw water in, in described water tank (10), be provided with thick effect dirt water segregation net (11) and efficient dirt water segregation net (12).
4. a kind of high-efficiency wet-type dust collector according to claim 1 it is characterised in that：Also include main tower (a), described master
Tower body (a) is arranged on base (18).
5. a kind of high-efficiency wet-type dust collector according to claim 4 it is characterised in that：Also install on described main tower (a)
There is observation maintenance door (16).
6. a kind of high-efficiency wet-type dust collector according to claim 2 it is characterised in that：Also include electric cabinet (17), described
Electric cabinet (17) is used for controlling the operation of water circulating pump (13).
7. a kind of high-efficiency wet-type dust collector according to claim 1 it is characterised in that：It is provided with described air-purifying chamber (7)
Retaining hood (8) for buffering.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620683529.2U CN205948569U (en) | 2016-06-29 | 2016-06-29 | High -efficient wet dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620683529.2U CN205948569U (en) | 2016-06-29 | 2016-06-29 | High -efficient wet dust collector |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205948569U true CN205948569U (en) | 2017-02-15 |
Family
ID=57969543
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620683529.2U Expired - Fee Related CN205948569U (en) | 2016-06-29 | 2016-06-29 | High -efficient wet dust collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205948569U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107572561A (en) * | 2017-10-27 | 2018-01-12 | 四川省洪雅青衣江元明粉有限公司 | A kind of six effects vacuum evaporation technique prepares the production system and method for glauber salt |
| CN108525459A (en) * | 2018-06-27 | 2018-09-14 | 伍世伟 | Negative pressure wet type high speed centrifugation air-borne dust isolation of purified equipment |
| CN109550339A (en) * | 2017-09-27 | 2019-04-02 | 东北大学 | A kind of method and device for gathering dust containing volatility valuable element gas with purification |
| CN110170378A (en) * | 2019-04-11 | 2019-08-27 | 华北水利水电大学 | A kind of wet-esp haze prevention and treatment system and application method |
| CN110170379A (en) * | 2019-04-11 | 2019-08-27 | 华北水利水电大学 | A kind of haze prevention and treatment wet electrical dust precipitator and application method |
-
2016
- 2016-06-29 CN CN201620683529.2U patent/CN205948569U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109550339A (en) * | 2017-09-27 | 2019-04-02 | 东北大学 | A kind of method and device for gathering dust containing volatility valuable element gas with purification |
| CN107572561A (en) * | 2017-10-27 | 2018-01-12 | 四川省洪雅青衣江元明粉有限公司 | A kind of six effects vacuum evaporation technique prepares the production system and method for glauber salt |
| CN108525459A (en) * | 2018-06-27 | 2018-09-14 | 伍世伟 | Negative pressure wet type high speed centrifugation air-borne dust isolation of purified equipment |
| CN110170378A (en) * | 2019-04-11 | 2019-08-27 | 华北水利水电大学 | A kind of wet-esp haze prevention and treatment system and application method |
| CN110170379A (en) * | 2019-04-11 | 2019-08-27 | 华北水利水电大学 | A kind of haze prevention and treatment wet electrical dust precipitator and application method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170215 |