CN108905462A - Purification device and its method for wet type environment dehydration dedusting one - Google Patents
Purification device and its method for wet type environment dehydration dedusting one Download PDFInfo
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- CN108905462A CN108905462A CN201810698761.7A CN201810698761A CN108905462A CN 108905462 A CN108905462 A CN 108905462A CN 201810698761 A CN201810698761 A CN 201810698761A CN 108905462 A CN108905462 A CN 108905462A
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- 230000018044 dehydration Effects 0.000 title claims abstract description 34
- 238000006297 dehydration reaction Methods 0.000 title claims abstract description 34
- 238000000746 purification Methods 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims abstract description 20
- 239000000428 dust Substances 0.000 claims abstract description 76
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000002245 particle Substances 0.000 claims abstract description 19
- 230000008676 import Effects 0.000 claims abstract description 15
- 239000007921 spray Substances 0.000 claims abstract description 15
- 238000009826 distribution Methods 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 11
- 238000012545 processing Methods 0.000 claims description 11
- 239000012716 precipitator Substances 0.000 claims description 9
- 239000013618 particulate matter Substances 0.000 claims description 6
- 238000009833 condensation Methods 0.000 claims description 5
- 230000005494 condensation Effects 0.000 claims description 5
- 239000003595 mist Substances 0.000 claims description 5
- 238000004220 aggregation Methods 0.000 claims description 4
- 230000002776 aggregation Effects 0.000 claims description 4
- 230000002195 synergetic effect Effects 0.000 claims description 4
- 238000005191 phase separation Methods 0.000 abstract 1
- 238000002156 mixing Methods 0.000 description 4
- 239000004744 fabric Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000003796 beauty Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000005098 hot rolling Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000004630 mental health Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000031068 symbiosis, encompassing mutualism through parasitism Effects 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
-
- 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
- B01D53/002—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 condensation
-
- 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
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/06—Polluted air
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The present invention relates to a kind of purification devices and its method for wet type environment dehydration dedusting one, setting fine pressure case and sintered plate in dust collector box body, it is spaced apart from each other arrangement to several perpendicular shapes of sintered plate, tolerance distribution plate is arranged in the box inside of outlet or entrance location in dust collector box body setting outlet or import.Dehydrating demisting device is equipped with dust and gas import, several dehydrating demisting piece groups is laid inside dehydrating demisting device, stack combinations constitute dehydration runner to several dehydrating demisting piece groups spaced reciprocally, and dehydrating demisting device is mounted on the outlet or entrance of dust collector box body.Before aqueous spray dust gas enters deduster, it first will contain water spray haze dirt by dehydrating demisting device to handle, realize gas phase separation, dust and gas after separation is directly entered tolerance distribution plate, when flowing through sintered plate surface, large particle is intercepted in cabinet, is discharged by unloading valve, the cleaned chamber gas outlet discharge of small particle, to effectively administer the water under wet type environment, gas, dustiness dye.
Description
Technical field
The invention belongs to the cleaner under wet type environment, it is related to for dehydrating demisting and sintered plate dedusting being combined into one
Purification device, in particular to it is a kind of that dehydration demister is set to the processing dress of the synergistic purification inside or outside sinter-plate precipitator
It sets and its method.
Background technique
It promotes a conservation culture and beauty China, develops energy conservation and environmental protection industry, quality of improving the ecological environment is that cultivation and development is new
Kinetic energy, the important measure for promoting Green Competitiveness.Since the water under wet type environment, gas, the synthesis ratio of dirt are considerably complicated, especially
The heavy polluter of metallurgy industry such as sintering plant mixing system, the breaking down of hot rolling mill, mm finishing mill unit, be all iron and steel industry enterprise most
Big pollution sources generate ground.Main is dust pollution, and the dust of especially steam symbiosis is most difficult to administer, and current dedusting neck
Domain urgent problem to be solved.
For sintering process, this dust is caused by using hot returning ore technique, in addition mainly from mixing system
Two it is mixed change steam preheating or a large amount of water mixing techniques carry out mixture so that entire vestibule is diffused with unit surrounding enviroment steam, energy
Degree of opinion is extremely low；Especially autumn and winter, a large amount of ponding in ground freeze, and bring very big hidden danger to safety in production.This adverse circumstances
The control for seriously affecting technological parameter constrains the raising of product yield and quality.A large amount of steam, moisture are to mixing chamber brick wall body
Corrosion dusting is caused, and greatly shortens service life of equipment, also influences worker's physical and mental health.
The cleaner that wet type environment uses at present has wet electric dust-removing and two kinds of pulsed bag filter, the former due to
For corona discharge electrode by the adherency of aqueous dust and gas, discharging efficiency is unstable, be easy to cause granular material discharged fluctuation too big and cannot accomplish to reach
Mark discharge；The latter is that bag-type dust easily is adhered to form paste bag in wet type environment by aqueous dust and gas, causes whole pulsed cloth
Bag dust collector failure, influences being normally carried out for production, and original cloth bag must be replaced by returning to normal production, in replacement process
The dust of cloth bag bonding causes secondary pollution, to affect ecological environment.
In view of this, dust removal field scientific research personnel is dedicated to researching and developing a kind of purification for wet type environment dehydration dedusting one
Device, with improve wet type environment go down water removal, gas, dirt collaboration processing technique and integrated technique.
Summary of the invention
The task of the present invention is a kind of purification device and its method for wet type environment dehydration dedusting one is provided, use
The purifying processing device that dehydrating demisting and sintered plate dedusting are combined into one, effectively improvement air pollution, especially improvement wet type
Water, gas under environment, dustiness dye, intercepting moisture content is more than 30% to 100% to contain water spray haze and partial size at 0.5 micron to 10 microns
Between particle dirt, solve the problems of above-mentioned prior art.
Technical solution of the invention is as follows：
A kind of purification device for wet type environment dehydration dedusting one, it includes dust collector box body and dehydrating demisting device；
Fine pressure case is arranged in top in the dust collector box body, and sintered plate, several sintered plates are arranged in the middle part in dust collector box body
It is spaced apart from each other to perpendicular shape arrangement, ash bucket, dust collector box body setting outlet or import is arranged in the lower part in dust collector box body,
Tolerance distribution plate is arranged in the box inside of dust collector box body outlet or entrance location；
The dehydrating demisting device is equipped with dust and gas import, and several dehydrating demisting piece groups are laid inside dehydrating demisting device, several de-
Water demisting piece group spaced reciprocally stack combinations constitute dehydration runner, dehydrating demisting device be mounted on dust collector box body outlet or
Entrance.
Filter screen is arranged in the dust collector box body outlet or entrance.
The filter screen multilayer folding, filter screen aperture takes 1 μm, with a thickness of 50-100mm.
Dehydrating demisting piece group in the dehydrating demisting device by upper piece and bottom sheet form.
Dehydrating demisting piece group shape in the dehydrating demisting device forms S type, constitutes S type and is dehydrated runner.
Dehydrating demisting piece group shape in the dehydrating demisting device forms V-type, constitutes V-type and is dehydrated runner.
The dehydrating demisting device is mounted on the inside portion of dust collector box body outlet or import.
The dehydrating demisting device is mounted on outside dust collector box body, and dehydrating demisting device is connected to deduster by adapter tube
The outlet or entrance of cabinet.
A kind of purification method using the above-mentioned purification device for wet type environment dehydration dedusting one, by aqueous dust and gas body
Dust collector box body outlet or import access dehydrating demisting device, dehydration runner is equipped with inside dehydrating demisting device, it is dewatered
Dust and gas is directly entered dust collector box body dedusting；
Before aqueous spray dust gas enters deduster, water spray haze dirt first will be contained by dehydrating demisting device and handled, the dirt containing water spray haze
Feature is that droplet amount is big, and the particle size distribution range of droplet is very wide, is mainly made of pulp-water drop, condensation drop and dirt particle, this
For a little drops usually by fine drop and particle aggregation, it is big that a large amount of fine drop and particle collide probability under the conditions of high-speed motion
Width increases, and is easy to agglomerate, assemble as bulky grain, and for bulky grain when through dehydration runner, the wind speed of outlet takes 6m/s, channel top
End setting filter device, to effectively realize that water mist is removed from gas, realizes the separation of gas phase；
Dust and gas after separation is directly entered sinter-plate precipitator tolerance distribution plate, when flowing through sintered plate surface, greater than 0.5 μm
Grain object is intercepted in cabinet, and by unloading valve timing discharge and outward transport, the cleaned chamber gas outlet of particulate matter less than 0.5 μm is by outer
If chimney high altitude discharge, the synergistic purification processing technique of dehydrating demisting dedusting one under wet type environment is thus constituted.
Purification device for wet type environment dehydration dedusting one of the invention is that a kind of be dehydrated in wet type environment next part is removed
The purifying processing device of mist dedusting one, be by dehydrating demisting dedusting cooperate with processing technique, by the technique of dehydrating demisting dedusting into
Row is integrated.
Dehydrating demisting and sintered plate dedusting are combined into one by purifying processing device of the invention, and dehydration demister is arranged
It is effective capital equipment for administering air pollution inside or outside sinter-plate precipitator, especially under improvement wet type environment
Water, gas, dustiness dye, intercept containing water spray haze and partial size between 0.5 micron to 10 microns that moisture content is more than 30% to 100%
Grain dirt.
For purification device of the invention due to the collective effect of dehydrating demisting device and sinter-plate precipitator, having it can
Dehydrating demisting, and energy dust and gas separation, and equipment has durable, Reusability function.After purification device processing
Dust and gas can achieve ultra-clean discharge, provide new option for wet type environment dehydrating demisting dedusting, apply valence with great
Value.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of purification device for wet type environment dehydration dedusting one of the invention, wherein
Dehydrating demisting device is installed in dust cleaning case.
Fig. 2 is a kind of structural schematic diagram of purification device for wet type environment dehydration dedusting one of the invention, wherein
Dehydrating demisting device is mounted on the outside of dust cleaning case.
Appended drawing reference：
1 is dust collector box body, and 2 be sintered plate, and 3 be ash bucket, and 4 be filter screen, and 5 be tolerance distribution plate, and 6 be S type runner, and 7 be de-
Water demister, 8 be V-type runner, and 9 be dust and gas import, and 10 be fine pressure case.
Specific embodiment
It elaborates with reference to the accompanying drawings and examples to the present invention.
Referring to Fig. 1 and Fig. 2, the present invention provides a kind of purification device for wet type environment dehydration dedusting one, it is main
It is made of dust collector box body 1 and dehydrating demisting device 7.
Fine pressure case 10 is arranged in top in dust collector box body 1.Sintered plate 2, several modelings are arranged in middle part in dust collector box body 1
It is spaced apart from each other arrangement with burning the perpendicular shape of plate 2.Ash bucket 3 is arranged in lower part in dust collector box body 1.The setting of dust collector box body 1 outlet
Or tolerance distribution plate 5 is arranged in import, the box inside in the outlet of dust collector box body 1 or entrance location.Dust collector box body 1 outlet or
Filter screen 4 is arranged in entrance.4 multilayer folding of filter screen, filter screen aperture takes 1 μm, with a thickness of 50-100mm.
Dehydrating demisting device 7 is equipped with dust and gas import 9.Several dehydrating demisting piece groups are laid inside dehydrating demisting device 7, it is several
Stack combinations constitute dehydration runner to dehydrating demisting piece group spaced reciprocally.Dehydrating demisting device 7 is mounted on going out for dust collector box body 1
Mouth or entrance.
Dehydrating demisting piece group in dehydrating demisting device 7 by upper piece and bottom sheet form.As shown in fig. 1, dehydrating demisting fills
The dehydrating demisting piece group shape set in 7 forms S type, constitutes S type and is dehydrated runner 6.As shown in Figure 2, in dehydrating demisting device 7
Dehydrating demisting piece group shape forms V-type, constitutes V-type and is dehydrated runner 8.
As shown in fig. 1, dehydrating demisting device 7 is mounted on the inside portion of the outlet of dust collector box body 1 or import.In Fig. 2
Shown, dehydrating demisting device 7 is mounted on outside dust collector box body 1, and dehydrating demisting device 7 is connected to dust collector box body by adapter tube
1 outlet or entrance.
The present invention also provides it is a kind of using it is above-mentioned for wet type environment dehydration dedusting one purification device purification method,
The outlet of dust collector box body 1 or import of aqueous dust and gas body are accessed into dehydrating demisting device 7, are equipped with inside dehydrating demisting device 7 de-
Water flow passage, dewatered dust and gas are directly entered 1 dedusting of dust collector box body.
Before aqueous spray dust gas enters deduster, water spray haze dirt first will be contained by dehydrating demisting device and handled, and contain water spray haze
The characteristics of dirt is that droplet amount is big, and the particle size distribution range of droplet is very wide, mainly by pulp-water drop, condensation drop and dirt particle group
At these drops are usually collided under the conditions of high-speed motion by fine drop and particle aggregation, a large amount of fine drop and particle
Probability is significantly increased, and is easy to agglomerate, assemble as bulky grain, and for bulky grain when through dehydration runner, the wind speed of outlet takes 6m/s,
Filter device is arranged in channel top, to effectively realize that water mist is removed from gas, realizes the separation of gas phase.
Dust and gas after separation is directly entered sinter-plate precipitator tolerance distribution plate, when flowing through sintered plate surface, is greater than 0.5 μm
Particulate matter be intercepted in cabinet, by unloading valve timing discharge and outward transport, the cleaned chamber gas outlet of particulate matter less than 0.5 μm
By peripheral hardware chimney high altitude discharge, the synergistic purification processing technique of dehydrating demisting dedusting one under wet type environment is thus constituted.
The present invention is referred to as a kind of purified treatment dress of wet type environment next part dehydrating demisting dedusting one in specific implementation
It sets.As shown in Figures 1 and 2, aqueous dirt gas feed is accessed into dehydrating demisting device cabinet, uniformly distributed S type or V-type dehydration in case
Demisting piece group, dehydrating demisting piece group by upper piece and bottom sheet form, constitute S type or V-type and be dehydrated runner, structure snd size are to dehydration
Efficiency and the pressure loss play a crucial role.At tank outlet or water screen is received in entrance installation（Determine depending on water size）.Case
The wind speed of body outlet takes 6m/s.This purification device may be mounted at the inside of sinter-plate precipitator（As shown in Figure 1）, avoid the summer in winter
Because the temperature difference generates condensed water；The outside of sinter-plate precipitator can also be installed in the form of vertical abutting（As shown in Figure 2）, lead to
It crosses and shortens adapter tube distance, the condensed water for reducing time condensation enters dust collector box body, and dewatered dust and gas is directly entered deduster
Dedusting becomes the purifying processing device of wet type environment next part dehydrating demisting dedusting one.
Decontamination process of the invention is：It, first will be aqueous by dehydrating demisting device before aqueous spray dust gas enters deduster
The characteristics of fog dirt is handled, dirt containing water spray haze is that droplet amount is big, and the particle size distribution range of droplet is very wide, mainly by pulp-water liquid
Drop, condensation drop and dirt particle composition, these drops are usually by fine drop and particle aggregation, a large amount of fine drop and particle
Probability is collided under the conditions of high-speed motion to be significantly increased, and is easy to agglomerate, be assembled as bulky grain, bulky grain is de- by S or V-type
When water flow passage, the wind speed of outlet takes 6m/s, and filter screen, filter screen multilayer folding is arranged in channel top, and aperture takes 1 μm, thickness 50-
100mm, to effectively realize that water mist is removed from gas, realizes the separation of gas phase.Dust and gas after separation is directly entered sintered plate
Deduster tolerance distribution plate, when flowing through sintered plate surface, the particulate matter greater than 0.5 μm is intercepted in cabinet, unloads ash by star-like
Valve timing discharge and outward transport；The cleaned chamber gas outlet of particulate matter less than 0.5 μm is by peripheral hardware chimney high altitude discharge.
Due to the collective effect of dehydrating demisting device and sinter-plate precipitator, having it can dehydrating demisting and dirt
Gas separation, and equipment has durable, Reusability function.Through the purification device, treated that dust and gas can achieve is super
Net discharge, provides new option for wet type environment dehydrating demisting dedusting, has great application value.
Certainly, those skilled in the art in the art are it should be appreciated that above-described embodiment is intended merely to illustrate this hair
It is bright, and be not used as limitation of the invention, if in spirit of the invention, to the variation of above-described embodiment,
Modification etc. will all be fallen within the scope of the claims.
Claims (9)
1. a kind of purification device for wet type environment dehydration dedusting one, it is characterised in that：It includes dust collector box body（1）With
Dehydrating demisting device（7）；
The dust collector box body（1）Fine pressure case is arranged in interior top（10）, dust collector box body（1）Sintered plate is arranged in interior middle part
（2）, several sintered plates（2）It is spaced apart from each other arrangement, dust collector box body to perpendicular shape（1）Ash bucket is arranged in interior lower part（3）, dedusting
Device cabinet（1）Setting outlet or import, in dust collector box body（1）Tolerance distribution plate is arranged in the box inside of outlet or entrance location
（5）；
The dehydrating demisting device（7）Equipped with dust and gas import（9）, dehydrating demisting device（7）Lay several dehydrating demisting pieces in inside
Group, stack combinations constitute dehydration runner, dehydrating demisting device to several dehydrating demisting piece groups spaced reciprocally（7）It is mounted on deduster
Cabinet（1）Outlet or entrance.
2. the purification device according to claim 1 for wet type environment dehydration dedusting one, it is characterised in that：It is described to remove
Dirt device cabinet（1）Filter screen is arranged in outlet or entrance（4）.
3. the purification device according to claim 2 for wet type environment dehydration dedusting one, it is characterised in that：The mistake
Strainer（4）Multilayer folding, filter screen aperture takes 1 μm, with a thickness of 50-100mm.
4. the purification device according to claim 1 for wet type environment dehydration dedusting one, it is characterised in that：It is described de-
Water demister（7）Interior dehydrating demisting piece group by upper piece and bottom sheet form.
5. the purification device according to claim 1 for wet type environment dehydration dedusting one, it is characterised in that：It is described de-
Water demister（7）Interior dehydrating demisting piece group shape forms S type, constitutes S type and is dehydrated runner（6）.
6. the purification device according to claim 1 for wet type environment dehydration dedusting one, it is characterised in that：It is described de-
Water demister（7）Interior dehydrating demisting piece group shape forms V-type, constitutes V-type and is dehydrated runner（8）.
7. the purification device according to claim 1 for wet type environment dehydration dedusting one, it is characterised in that：It is described de-
Water demister（7）It is mounted on dust collector box body（1）The inside portion of outlet or import.
8. the purification device according to claim 1 for wet type environment dehydration dedusting one, it is characterised in that：It is described de-
Water demister（7）It is mounted on dust collector box body（1）Outside, dehydrating demisting device（7）Dust collector box body is connected to by adapter tube
（1）Outlet or entrance.
9. a kind of purification method using the purification device described in claim 1 for wet type environment dehydration dedusting one,
It is characterized in that：By the dust collector box body of aqueous dust and gas body（1）Outlet or import access dehydrating demisting device（7）, dehydrating demisting dress
It sets（7）Inside is equipped with dehydration runner, and dewatered dust and gas is directly entered dust collector box body（1）Dedusting；
Before aqueous spray dust gas enters deduster, water spray haze dirt first will be contained by dehydrating demisting device and handled, the dirt containing water spray haze
Feature is that droplet amount is big, and the particle size distribution range of droplet is very wide, is mainly made of pulp-water drop, condensation drop and dirt particle, this
For a little drops usually by fine drop and particle aggregation, it is big that a large amount of fine drop and particle collide probability under the conditions of high-speed motion
Width increases, and is easy to agglomerate, assemble as bulky grain, and for bulky grain when through dehydration runner, the wind speed of outlet takes 6m/s, channel top
End setting filter device, to effectively realize that water mist is removed from gas, realizes the separation of gas phase；
Dust and gas after separation is directly entered sinter-plate precipitator tolerance distribution plate, when flowing through sintered plate surface, greater than 0.5 μm
Grain object is intercepted in cabinet, and by unloading valve timing discharge and outward transport, the cleaned chamber gas outlet of particulate matter less than 0.5 μm is by outer
If chimney high altitude discharge, the synergistic purification processing technique of dehydrating demisting dedusting one under wet type environment is thus constituted.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810698761.7A CN108905462A (en) | 2018-06-29 | 2018-06-29 | Purification device and its method for wet type environment dehydration dedusting one |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810698761.7A CN108905462A (en) | 2018-06-29 | 2018-06-29 | Purification device and its method for wet type environment dehydration dedusting one |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108905462A true CN108905462A (en) | 2018-11-30 |
Family
ID=64424358
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810698761.7A Pending CN108905462A (en) | 2018-06-29 | 2018-06-29 | Purification device and its method for wet type environment dehydration dedusting one |
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| Country | Link |
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| CN (1) | CN108905462A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110013744A (en) * | 2019-04-30 | 2019-07-16 | 上海华之邦科技股份有限公司 | A kind of low nitrogen boiler smoke recycling dehumidifier |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202369599U (en) * | 2011-12-13 | 2012-08-08 | 北京柯林柯尔科技发展有限公司 | Roller slag treating and flue gas dust removing device |
| CN203904294U (en) * | 2014-06-24 | 2014-10-29 | 中节能天辰(北京)环保科技有限公司 | Blast-furnace gas dedusting system |
| CN208448948U (en) * | 2018-06-29 | 2019-02-01 | 上海超高环保科技股份有限公司 | Purification device for wet type environment dehydration dedusting one |
-
2018
- 2018-06-29 CN CN201810698761.7A patent/CN108905462A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202369599U (en) * | 2011-12-13 | 2012-08-08 | 北京柯林柯尔科技发展有限公司 | Roller slag treating and flue gas dust removing device |
| CN203904294U (en) * | 2014-06-24 | 2014-10-29 | 中节能天辰(北京)环保科技有限公司 | Blast-furnace gas dedusting system |
| CN208448948U (en) * | 2018-06-29 | 2019-02-01 | 上海超高环保科技股份有限公司 | Purification device for wet type environment dehydration dedusting one |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110013744A (en) * | 2019-04-30 | 2019-07-16 | 上海华之邦科技股份有限公司 | A kind of low nitrogen boiler smoke recycling dehumidifier |
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Application publication date: 20181130 |