CN109045931A - A kind of box-like flue gas pollutant cooperation-removal device of horizontal group - Google Patents
A kind of box-like flue gas pollutant cooperation-removal device of horizontal group Download PDFInfo
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- CN109045931A CN109045931A CN201811091600.8A CN201811091600A CN109045931A CN 109045931 A CN109045931 A CN 109045931A CN 201811091600 A CN201811091600 A CN 201811091600A CN 109045931 A CN109045931 A CN 109045931A
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- China
- Prior art keywords
- shell
- flue gas
- removal device
- box
- absorbing
- Prior art date
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- Pending
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 239000003546 flue gas Substances 0.000 title claims abstract description 32
- 239000003344 environmental pollutant Substances 0.000 title claims abstract description 17
- 231100000719 pollutant Toxicity 0.000 title claims abstract description 17
- 239000002250 absorbent Substances 0.000 claims abstract description 24
- 230000002745 absorbent Effects 0.000 claims abstract description 24
- 229910000831 Steel Inorganic materials 0.000 claims description 5
- 239000010959 steel Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 4
- 230000007246 mechanism Effects 0.000 claims description 4
- 239000012774 insulation material Substances 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 238000003466 welding Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 14
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 9
- 238000006477 desulfuration reaction Methods 0.000 abstract description 8
- 229910021529 ammonia Inorganic materials 0.000 abstract description 7
- 230000023556 desulfurization Effects 0.000 abstract description 7
- 238000012545 processing Methods 0.000 abstract description 7
- 238000007664 blowing Methods 0.000 abstract description 5
- 239000007800 oxidant agent Substances 0.000 abstract description 3
- 239000000428 dust Substances 0.000 abstract description 2
- 230000008676 import Effects 0.000 abstract description 2
- 238000005201 scrubbing Methods 0.000 abstract description 2
- 230000001590 oxidative effect Effects 0.000 abstract 2
- 239000000571 coke Substances 0.000 description 14
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 229910052711 selenium Inorganic materials 0.000 description 1
- 239000011669 selenium Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/30—Particle separators, e.g. dust precipitators, using loose filtering material
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/76—Gas phase processes, e.g. by using aerosols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/104—Ozone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/106—Peroxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/20—Reductants
- B01D2251/206—Ammonium compounds
- B01D2251/2062—Ammonia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/40—Alkaline earth metal or magnesium compounds
- B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/302—Sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
- B01D2257/404—Nitrogen oxides other than dinitrogen oxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/60—Heavy metals or heavy metal compounds
- B01D2257/602—Mercury or mercury compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
Abstract
A kind of box-like flue gas pollutant cooperation-removal device of horizontal group, including shell, the different zones of shell are each passed through multiple absorbing cabins, the top of absorbing cabin is connect with feeding bin, the bottom of absorbing cabin is connected with discharge bin, and discharge bin connects removal device, is provided with conveyer below removal device；The intermediate position of shell is provided with blowing mouth B and denitration mixer；When use, flue gas enters from the import A of shell, enter second absorbing cabin after first absorbing cabin reduces dust, for demercuration, into desulfurization absorbing cabin scrubbing CO_2, enters blowing area, ammonia or oxidant later and sprayed into via blowing mouth B, pass through ribbon mixer later, mixes ammonia or oxidant and flue gas uniformly.Through entering denitration region after mixed uniformly flue gas, by several absorbing cabins, the outlet C through shell is expelled to rear portion discharge after removing nitrogen oxides；The present invention have reduce absorbent consumption, improve processing specific aim and overall operation economy the advantages of.
Description
Technical field
The invention belongs to environmental technology fields, and in particular to a kind of box-like flue gas pollutant cooperation-removal device of horizontal group.
Technical background
With the fast development of China's economic society, the emission request of each pollutant is also continuously improved.Correspondingly, right
The dedusting of industrial smoke, desulphurization and denitration, the requirement of de- dioxin and demercuration are also higher and higher.Currently, having developed for flue gas
The many kinds of solids absorbent of improvement, such as particle calcium base and activated coke absorbent.Wherein activated coke is to flue gas desulfurization, denitration, de-
The integrative coordinated processing capacity of mercury and de- dioxin is most strong, and therefore the scope of application is also wider, and current application is more universal.But it is right
Regular activated coke, since it is limited to the removing ability of Elemental Mercury, it is therefore necessary to the activated coke through special modification is used, by
This makes the higher cost using demercuration activated coke.The activated coke for having adsorbed mercury belongs to dangerous solid waste, it is necessary to by professional machine
Structure processing, expense are also very high.In view of above-mentioned application characteristic, moving-bed type activated coke desulfurization denitration system currently on the market
System, since structure limits, it is necessary to which same batch of activated coke mixing and absorption all contaminants and a batch concentration discharge are bound to cause in this way
It purchases and processing cost is larger, economy is bad.In addition, existing system is damaged big there is also absorbent, flue gas fluctuation is fitted
Answering property is poor, and the detection and temperaturing lifting abnormality to temperature change handle the problems such as difficult.These so that it can not meet market very well
It is required that, it is necessary to the new construction and corresponding process system that exploitation adapts to therewith.
Summary of the invention
In order to overcome the above-mentioned deficiencies of the prior art, dirty it is an object of the invention to propose a kind of box-like flue gas of horizontal group
Object cooperation-removal device is contaminated, can aid in reduction operating cost, reduces absorbent consumption, improves the specific aim of processing and whole
The economy of running body；Disposition absorbent can be collected separately.
In order to achieve the above object, the technical solution adopted by the present invention are as follows:
A kind of box-like flue gas pollutant cooperation-removal device of horizontal group, including shell 2, the different zones of shell 2 are worn respectively
Multiple absorbing cabins 3 are crossed, the top of absorbing cabin 3 is connect with feeding bin 1, and the bottom of absorbing cabin 3 is connected with discharge bin 5, discharge bin 5
Removal device 6 is connected, the lower section of removal device 6 is provided with conveyer 7；The intermediate position of shell 2 is provided with blowing mouth B and denitration mixing
Device 8.
The absorbing cabin 3 is cube structure, and the horizontally arranged of absorbing cabin 3 has 2-5 width for 10-20mm
Separate cavities 9.
Part of the absorbing cabin 3 inside shell 2 is constituted using netted or shutter steel plate.
Along the vertical direction in absorbent channel, staggeredly welding multi-group hole spaced apart in the absorbing cabin 3
Arc supporting plate 10.
The feeding bin 1 is welded into the working box for being used to store absorbent of sealing using steel plate, working box
Top is provided with automatic distributing mechanism.
The shell 2 is arranged in parallel with multiple, and the air inlet of each shell 2 vertically connects inlet manifold 11, each shell
The gas outlet of body 2 vertically connects outlet general pipeline 12.
The air inlet of the shell 2 is provided with flue gas even distribution mechanism.
The shell 2 is arranged in the support 4 of steelframe or concrete；The outside of shell 2 is coated using thermal insulation material.
The different parts of 2 length direction of shell are separately installed with temperature, pressure transmitter.
Beneficial effects of the present invention:
The different zones of inventive shell 2 are each passed through multiple absorbing cabins 3, convenient for reasonable Arrangement dedusting, desulfurization, demercuration and
Denitration region is also convenient for loading different types of absorbent respectively, improves the specific aim of processing and the economy of overall operation.It is right
For the dangerous waste absorbent of demercuration, disposition can be collected separately；It also helps and subregion replacement absorbent is determined according to control target, mention
The utilization rate of high-selenium corn agent is equally beneficial for reducing operating cost, reduces absorbent consumption.Dedusting absorbent channel also can be used
The absorbent of rest part discharge.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is the top view of absorbing cabin of the present invention.
Fig. 3 is the schematic diagram arranged in parallel of inventive shell.
Specific embodiment
The present invention will be further explained below with reference to the attached drawings.
Shown in referring to Fig.1, a kind of box-like flue gas pollutant cooperation-removal device of horizontal group, including shell 2, shell 2 is not
Multiple absorbing cabins 3 are each passed through with region, the top of absorbing cabin 3 is connect with feeding bin 1, and the bottom of absorbing cabin 3 is connected with discharge
Storehouse 5, discharge bin 5 connect removal device 6, and the lower section of removal device 6 is provided with conveyer 7；The intermediate position of shell 2 is provided with spray ammonia mouth
B and denitration mixer 8.The shell 2 is arranged in the support 4 of steelframe or concrete.
Referring to shown in Fig. 2, the absorbing cabin 3 is cube structure, and the horizontally arranged of absorbing cabin 3 has 2-5 a wide
Degree is the separate cavities 9 of 10-20mm.It is spaced apart to interlock along the vertical direction in absorbent channel in the absorbing cabin 3
Weld multi-group hole arc support plate 10.
Referring to shown in Fig. 3, shell 2 is arranged in parallel with multiple, and the air inlet of each shell 2 vertically connects inlet manifold 11,
The gas outlet of each shell 2 vertically connects outlet general pipeline 12.
The working principle of the invention is for using activated coke:
When work, flue gas enters from the import A of shell 2, posteriorly moves under the action of blower in tail portion.First pass around
One absorbing cabin 3.Pollutant effects are removed to reduce dust to rear portion, this storehouse is to carry out powder filtering filtration storehouse using particulate matter.
Filtering absorption of agent can be used the absorbent of other absorbing cabin discharges, convenient for reducing the consumption of new absorbent.Flue gas after dedusting into
Enter second absorbing cabin 3, loads dedicated demercuration absorbent herein for demercuration.Flue gas is after demercuration, into desulfurization zone, by number
A desulfurization absorbing cabin, scrubbing CO_2 enter the area Pen An later.Ammonia is sprayed into via blowing mouth B, passes through thread mixing later
Device 8 mixes ammonia and flue gas uniformly.Through entering denitration region after mixed uniformly flue gas, by several absorbing cabins 3, removing
Outlet C after nitrogen oxides through shell 2 is expelled to rear portion discharge.
Absorbent in absorbing cabin 3 is provided by feeding bin 1, via each 3 channel of absorbing cabin, periodically or by outlet is polluted
Object exit concentration testing result determines efflux time.The absorbent of adsorption saturation via discharge bin 5, removal device 6 and conveyer 7,
Regeneration or unified disposition are sent to after centralized collection.Demercuration dangerous waste absorbent centrally disposes after being collected separately.In operational process, such as
It detects that any 3 temperature of absorbing cabin is excessively high, can determine whether to take being passed through inert gas or the quickly suction of discharge this part after burning
The methods of agent is received to be handled.
When amount of sulfur contenting in smoke is higher, to eliminate influence of the sulfur dioxide to demercuration, can after dedusting next stage absorbing cabin
Desulphurizing activated coke is loaded, a part of sulfur dioxide is first deviate from, later, flue gas enters back into demercuration absorbing cabin and carries out demercuration, and demercuration is inhaled
Receiving agent can be used such as modified load bromine or carries sulphur activated coke, for carrying out the oxidation and absorption of Elemental Mercury.After adsorption saturation, our department
Point dangerous waste activated coke can be handled individually.
The flue gas or leading portion generate to burning natural gas has desulfurizer, big at present such as the sintering machine of steel industry
Have been provided with ammonia desulfuration equipment more.It has not needed to carry out desulfurization again for such, can remove present apparatus leading portion dust-removal and desulfurizing section, directly
Connect arrangement denitration dark zone and denitration region.To activated coke denitrating system, being blown mouth B is spray ammonia mouth.To calcium-base absorbing agent, penetrating
It can be the oxidants such as ozone, hydrogen peroxide, carry out removal of nitrogen oxide by being mixed into denitration region later.
When processing exhaust gas volumn is larger, flue gas is divided equally through inlet manifold 11 in its arrival end and enters each shell 2, in its outlet
Discharge is summarized by outlet general pipeline 12 at end., will also be by screening removal fine powder to activated coke to the absorbent of each blowdown discharge, it
Regeneration is uniformly sent to afterwards.To calcium-base absorbing agent, sends to and centrally dispose after unified collection.
Claims (9)
1. a kind of box-like flue gas pollutant cooperation-removal device of horizontal group, which is characterized in that including shell (2), shell (2) is no
It is each passed through multiple absorbing cabins (3) with region, the top of absorbing cabin (3) is connect with feeding bin (1), and the bottom of absorbing cabin (3) connects
It is connected to discharge bin (5), discharge bin (5) connects removal device (6), is provided with conveyer (7) below removal device (6)；Shell (2)
Intermediate position is provided with spout B and denitration mixer (8).
2. the box-like flue gas pollutant cooperation-removal device of a kind of horizontal group according to claim 1, which is characterized in that described
Absorbing cabin (3) be cube structure, absorbing cabin (3) it is horizontally arranged have 2-5 width for 10-20mm separate cavities
(9)。
3. the box-like flue gas pollutant cooperation-removal device of a kind of horizontal group according to claim 1, which is characterized in that described
Absorbing cabin (3) in the internal part of shell (2) using netted or shutter steel plate composition.
4. the box-like flue gas pollutant cooperation-removal device of a kind of horizontal group according to claim 1, which is characterized in that described
Absorbing cabin (3) in along absorbent channel vertical direction, it is spaced apart staggeredly welding multi-group hole arc support plate
(10)。
5. the box-like flue gas pollutant cooperation-removal device of a kind of horizontal group according to claim 1, which is characterized in that described
Feeding bin (1) using steel plate be welded into sealing for storing the working box of absorbent, the top of working box is provided with
Automatic distributing mechanism.
6. the box-like flue gas pollutant cooperation-removal device of a kind of horizontal group according to claim 1, which is characterized in that described
Shell (2) be arranged in parallel with multiple, the air inlet of each shell (2) vertically connects inlet manifold (11), each shell (2)
Gas outlet vertically connects outlet general pipeline (12).
7. the box-like flue gas pollutant cooperation-removal device of a kind of horizontal group according to claim 1, which is characterized in that described
The air inlet of shell (2) be provided with flue gas even distribution mechanism.
8. the box-like flue gas pollutant cooperation-removal device of a kind of horizontal group according to claim 1, which is characterized in that described
Shell (2) be arranged in the support (4) of steelframe or concrete；The outside of shell (2) is coated using thermal insulation material.
9. the box-like flue gas pollutant cooperation-removal device of a kind of horizontal group according to claim 1, which is characterized in that described
The different parts of shell (2) length direction be separately installed with temperature, pressure transmitter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811091600.8A CN109045931A (en) | 2018-09-19 | 2018-09-19 | A kind of box-like flue gas pollutant cooperation-removal device of horizontal group |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811091600.8A CN109045931A (en) | 2018-09-19 | 2018-09-19 | A kind of box-like flue gas pollutant cooperation-removal device of horizontal group |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109045931A true CN109045931A (en) | 2018-12-21 |
Family
ID=64762130
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811091600.8A Pending CN109045931A (en) | 2018-09-19 | 2018-09-19 | A kind of box-like flue gas pollutant cooperation-removal device of horizontal group |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109045931A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117138548A (en) * | 2023-09-12 | 2023-12-01 | 山东康源环保科技有限公司 | Vertical fixed bed desulfurization, denitrification and dust removal equipment and application method thereof |
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