CN106975353B - A kind of tail gas processing mechanism and processing method - Google Patents
A kind of tail gas processing mechanism and processing method Download PDFInfo
- Publication number
- CN106975353B CN106975353B CN201710334868.9A CN201710334868A CN106975353B CN 106975353 B CN106975353 B CN 106975353B CN 201710334868 A CN201710334868 A CN 201710334868A CN 106975353 B CN106975353 B CN 106975353B
- Authority
- CN
- China
- Prior art keywords
- tail gas
- filtering body
- air inlet
- inlet pipe
- filter
- 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
- 230000007246 mechanism Effects 0.000 title claims abstract description 66
- 238000003672 processing method Methods 0.000 title description 3
- 238000001914 filtration Methods 0.000 claims abstract description 67
- 239000003054 catalyst Substances 0.000 claims abstract description 26
- 239000000843 powder Substances 0.000 claims abstract description 15
- 239000007789 gas Substances 0.000 claims description 56
- 239000000428 dust Substances 0.000 claims description 11
- 239000003814 drug Substances 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 9
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 9
- 229940079593 drug Drugs 0.000 claims description 8
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 7
- 239000000908 ammonium hydroxide Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 5
- 229910052593 corundum Inorganic materials 0.000 claims description 5
- 229910001845 yogo sapphire Inorganic materials 0.000 claims description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 4
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical group [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 4
- 238000007664 blowing Methods 0.000 claims description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 4
- 239000000920 calcium hydroxide Substances 0.000 claims description 4
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 4
- 239000000945 filler Substances 0.000 claims description 4
- 239000004571 lime Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 229920001214 Polysorbate 60 Polymers 0.000 claims description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 3
- 239000004202 carbamide Substances 0.000 claims description 3
- 239000000969 carrier Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 3
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 claims description 3
- DDXLVDQZPFLQMZ-UHFFFAOYSA-M dodecyl(trimethyl)azanium;chloride Chemical group [Cl-].CCCCCCCCCCCC[N+](C)(C)C DDXLVDQZPFLQMZ-UHFFFAOYSA-M 0.000 claims description 3
- 239000000835 fiber Substances 0.000 claims description 3
- 235000010989 polyoxyethylene sorbitan monostearate Nutrition 0.000 claims description 3
- 239000001818 polyoxyethylene sorbitan monostearate Substances 0.000 claims description 3
- 229940113124 polysorbate 60 Drugs 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 3
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 239000002270 dispersing agent Substances 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- XJWSAJYUBXQQDR-UHFFFAOYSA-M dodecyltrimethylammonium bromide Chemical compound [Br-].CCCCCCCCCCCC[N+](C)(C)C XJWSAJYUBXQQDR-UHFFFAOYSA-M 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 238000009413 insulation Methods 0.000 claims 1
- 239000011734 sodium Substances 0.000 claims 1
- 229910052708 sodium Inorganic materials 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 10
- 239000000126 substance Substances 0.000 abstract description 7
- 239000002245 particle Substances 0.000 abstract description 5
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 3
- 235000017557 sodium bicarbonate Nutrition 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- AISMNBXOJRHCIA-UHFFFAOYSA-N trimethylazanium;bromide Chemical compound Br.CN(C)C AISMNBXOJRHCIA-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- DOTMOQHOJINYBL-UHFFFAOYSA-N molecular nitrogen;molecular oxygen Chemical compound N#N.O=O DOTMOQHOJINYBL-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- 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
- B01D53/86—Catalytic processes
- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8628—Processes characterised by a specific catalyst
-
- 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
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2407—Filter candles
-
- 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
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/508—Sulfur oxides by treating the gases with solids
-
- 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
- B01D53/86—Catalytic processes
- B01D53/90—Injecting reactants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20707—Titanium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20723—Vanadium
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Biomedical Technology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Physics & Mathematics (AREA)
- Geometry (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a kind of tail gas processing mechanisms, including filtering body；Filter mechanism is equipped in the filtering body；The filtering body is equipped with air inlet pipe and exhaust pipe；Tail gas is entered in the filtering body by the air inlet pipe, after being filtered by the filter mechanism, is discharged by the exhaust pipe；The catalyst of catalytic exhaust is adsorbed on the filter mechanism.Therefore the tail gas of burning is entered in filtering body by air inlet pipe, by filter mechanism that powder particle filtering in tail gas is clear, and reacts to form innocuous gas discharge with the harmful substance in tail gas by catalyst.Tail gas processing mechanism, including filtering body；Filter mechanism is equipped in the filtering body；The filtering body is equipped with air inlet pipe and exhaust pipe；Tail gas is entered in the filtering body by the air inlet pipe, after being filtered by the filter mechanism, is discharged by the exhaust pipe；The catalyst of catalytic exhaust is adsorbed on the filter mechanism.
Description
Technical field
The present invention relates to the field of tail gas treatment, and in particular to a kind of tail gas processing mechanism and processing method.
Background technique
Current incineration flue gas contains a large amount of particle, mostly uses water spray absorbed portion dust greatly at present, and cyclone type removes
Dirt is gone out most of large dust particle, and electron ion is in processing part dust, then passes through multiple dust removal step ability such as bag-type dust
Reach discharge standard, used device and operating cost are high, complex process, and waste water resource generates secondary pollution；It is lacked in view of above
It falls into, it is really necessary to design a kind of trunk opening and closing device.
Summary of the invention
Technical problem to be solved by the present invention lies in: a kind of trunk opening and closing device is provided, is burnt to solve to handle at present
Burning tail gas is at high cost, and technique is cumbersome, waste of resource, and can lead to the problem of secondary pollution.
In order to solve the above technical problems, the technical scheme is that a kind of tail gas processing mechanism, including filtering body；
Filter mechanism is equipped in the filtering body；The filtering body is equipped with air inlet pipe and exhaust pipe；Tail gas passes through the air inlet
Pipe enters in the filtering body, after being filtered by the filter mechanism, is discharged by the exhaust pipe；It is inhaled on the filter mechanism
With the catalyst of conversion tail gas.
Further, the filter mechanism includes: fixed plate inside the filtering body and is set to the fixed plate
On more filter core carriers；The Catalyst Adsorption is on the filter core carrier.
Further, the filter core carrier is alumina fibre high temperature filtration core；The gap of the filter core carrier is less than
0.1nm。
Further, the filter core carrier is Al2O3 fiber filament.
Further, the catalyst includes each component calculated in weight percent:
Further, the dispersion machine is polysorbate60；The duct filler is dodecyl trimethyl ammonium chloride or ten
Dialkyl group trimethylammonium bromide.
Further, the back-blowing mechanism being connected with the filter mechanism outlet side is additionally provided on the filtering body；It is described
The bottom end of filtering body is additionally provided with dust outlet.
Further, heating and heat-insulating device is additionally provided with inside the filtering body；The exhaust pipe is connect with heat exchanger；Through
The filtered tail gas of tail gas processing mechanism enters in the heat exchanger and enters the air heat exchange in boiler.
A kind of processing tail gas method, which is characterized in that add drug in the air inlet pipe in the removal air inlet pipe
Nitrogen oxides or sulfur oxide in tail gas.
Further, the drug is ammonium hydroxide, lime powder, sodium bicarbonate powder, calcium hydroxide powder, limewash, salt
Any one of water and urea.
Compared with prior art, the tail gas processing mechanism, including filtering body；Filter is equipped in the filtering body
Structure；The filtering body is equipped with air inlet pipe and exhaust pipe；Tail gas is entered in the filtering body by the air inlet pipe, is passed through
After the filter mechanism filtering, it is discharged by the exhaust pipe；The catalyst of catalytic exhaust is adsorbed on the filter mechanism.Therefore
The tail gas of burning is entered in filtering body by air inlet pipe, by filter mechanism that powder particle filtering in tail gas is clear, and is led to
Catalyst is crossed to react to form innocuous gas discharge with the harmful substance in tail gas.Tail gas processing mechanism, including filtering body；It is described
Filter mechanism is equipped in filtering body；The filtering body is equipped with air inlet pipe and exhaust pipe；Tail gas by the air inlet pipe into
Enter in the filtering body, after being filtered by the filter mechanism, is discharged by the exhaust pipe；It is adsorbed on the filter mechanism
The catalyst of catalytic exhaust.Therefore instead of traditional mechanism complexity, the tail gas processing mechanism of complex process is reduced costs, and is saved
About resource, and not will cause secondary pollution.
Detailed description of the invention
Fig. 1 is the mechanism view of tail gas processing mechanism of the present invention；
Fig. 2 is the cross-sectional view of tail gas processing mechanism of the present invention.
Specific embodiment
The following detailed description will be further explained with reference to the above drawings.
Hereinafter, a variety of specific details are elaborated, in order to provide to the saturating of the concept for constituting described embodiment basis
Thorough understanding.However, it will be apparent to those skilled in the art that described embodiment can be in these no specific details
In some or all situations get off practice.In other cases, well-known processing step is not specifically described.
Embodiment 1
As shown in Figs. 1-2, a kind of tail gas processing mechanism, including filtering body 1；Filter is equipped in the filtering body 1
Structure 2；The filtering body 1 is equipped with air inlet pipe 3 and exhaust pipe 4；Tail gas enters the filtering body 1 by the air inlet pipe 3
It is interior, after being filtered by the filter mechanism 2, it is discharged by the exhaust pipe 4；Catalytic exhaust is adsorbed on the filter mechanism 2
Catalyst.The catalyst, including each component calculated in weight percent.
Embodiment 2
As shown in Figs. 1-2, a kind of tail gas processing mechanism, including filtering body 1；Filter is equipped in the filtering body 1
Structure 2；The filtering body 1 is equipped with air inlet pipe 3 and exhaust pipe 4；Tail gas enters the filtering body 1 by the air inlet pipe 3
It is interior, after being filtered by the filter mechanism 2, it is discharged by the exhaust pipe 4；Catalytic exhaust is adsorbed on the filter mechanism 2
Catalyst.The catalyst, including each component calculated in weight percent:
Embodiment 3
As shown in Figs. 1-2, a kind of tail gas processing mechanism, including filtering body 1；Filter is equipped in the filtering body 1
Structure 2；The filtering body 1 is equipped with air inlet pipe 3 and exhaust pipe 4；Tail gas enters the filtering body 1 by the air inlet pipe 3
It is interior, after being filtered by the filter mechanism 2, it is discharged by the exhaust pipe 4；Catalytic exhaust is adsorbed on the filter mechanism 2
Catalyst.The catalyst, including each component calculated in weight percent:
Embodiment 4
As shown in Figs. 1-2, a kind of tail gas processing mechanism, including filtering body 1；Filter is equipped in the filtering body 1
Structure 2；The filtering body 1 is equipped with air inlet pipe 3 and exhaust pipe 4；Tail gas enters the filtering body 1 by the air inlet pipe 3
It is interior, after being filtered by the filter mechanism 2, it is discharged by the exhaust pipe 4；Catalytic exhaust is adsorbed on the filter mechanism 2
Catalyst.The catalyst, including each component calculated in weight percent:
Vanadic anhydride has strong oxidizing property, catalyst is used as in catalytic oxidation, with aromatic compound and nitrogen oxygen
Compound is reacted, and titanium dioxide is carrier, and each section can be uniformly dispersed by dispersing agent point, and duct filler can be played and be led
To effect, Fast Filling is on the filter core carrier 21 of alumina fibre high temperature filtration core.It therefore, can be by the harmful substance in tail gas
It dispels.Wherein, catalyst is circulated into filter core carrier 21 in solution state by liquid filling mechanism by catalyst, so that catalysis
Agent is adsorbed on filter core carrier 21, using high-temperature baking, so that catalyst can securely be adsorbed on filter core carrier 21.
Therefore the tail gas of burning is entered in filtering body by air inlet pipe, by filter mechanism 2 by powder particle in tail gas
It filters clear, and reacts with the harmful substance in tail gas to form innocuous gas discharge by catalyst.Therefore instead of traditional machine
Structure is complicated, and the tail gas processing mechanism of complex process reduces costs, and has saved resource, and not will cause secondary pollution.
Further, the filter mechanism 2 includes: fixed plate 20 inside the filtering body 1 and is set to described solid
More filter core carriers 21 on fixed board 20；The Catalyst Adsorption is on the filter core carrier 21.
Further, the filter core carrier 21 is alumina fibre high temperature filtration core；The gap of the filter core carrier is less than
0.1nm.It can stop the above suspended particulates of partial size PM1.0, removal efficiency is up to 99%, and up to 99.9%, exhaust contains collection efficiency
Amount is less than 3mg/m3, and overall cost is low.Wherein, filter core carrier 21: being to be mixed using the Al2O3 of flocculence with colloidal solution
Uniformly, the substance that colloid is uniformly mixed with Al2O3 is transported in mold by constant displacement pump, using vacuum inhale so that be uniformly mixed
Substance is formed in mold, and is inhaled by vacuum, so that forming the gap for being less than 0.1nm between filter core carrier 21.
Further, the filter core carrier 21 is Al2O3 fiber filament.Therefore it is able to achieve high temperature resistant.
Further, the dispersion machine is polysorbate60；The duct filler is dodecyl trimethyl ammonium chloride or ten
Dialkyl group trimethylammonium bromide.
Further, the back-blowing mechanism 5 being connected with 2 outlet side of filter mechanism is additionally provided on the filtering body 1；Institute
The bottom end for stating filtering body 1 is additionally provided with dust outlet 6.Therefore, when the dust absorption on 21 on filter core carrier is excessive, blowback
Mechanism 5 is blown into high pressure gas into filtering body 1, so as to which the dust being adsorbed on filtration supports 21 is blown off dust discharge
In mouth 6.Back-blowing mechanism 5 is high-pressure pump and solenoid valve, and when needing blowback, solenoid valve is opened, and high-pressure pump is by high pressure gas
It is blown into filtering body 1.
Further, heating and heat-insulating device 10 is additionally provided with inside the filtering body 1.Guarantee tail by heating and heat-insulating device 10
The catalytic temperature of gas.
A kind of processing tail gas method adds drug to the nitrogen in the air inlet pipe 3 in removal 3 inner exhaust gas of air inlet pipe
Oxide or sulfur oxide.
Further, the drug is ammonium hydroxide or urea；Ammonium hydroxide is injected in air inlet pipe by chemicals dosing plant with mist.Dosing dress
Setting 7 includes: liquid medicine barrel 70, high-pressure pump 71 and atomizer 72；The high-pressure pump 71 is by the ammonium hydroxide or urine in the liquid medicine barrel 70
Element is sprayed into the air inlet pipe 3 by the atomizer with mist；To which ammonia is formed with nitrogen oxides and catalyst reaction
Nitrogen；The inlet end of the air inlet pipe 3 is additionally provided with heating device.When exhaust temperature is not high, heating device can play ammonium hydroxide
Heating atomization effect.
Further, the drug be lime powder, sodium bicarbonate powder, drug described in calcium hydroxide powder be ammonium hydroxide,
Any one of lime powder, sodium bicarbonate powder, calcium hydroxide powder, limewash and salt water.Therefore desulfurization can be realized.
Further, the exhaust pipe 4 is connect with heat exchanger 8；Enter through the filtered tail gas of the tail gas processing mechanism
The heat exchanger 8 is interior and enters the air heat exchange in boiler 9.It is not only able to achieve and cools to tail gas, and can also be real
Existing recuperation of heat, improves heat recovery rate.
The present invention is not limited to above-mentioned specific embodiment, those skilled in the art from the above idea,
Without creative labor, the various transformation made are within the scope of the present invention.
Claims (6)
1. a kind of tail gas processing mechanism, including filtering body；Filter mechanism is equipped in the filtering body；On the filtering body
Equipped with air inlet pipe and exhaust pipe；Tail gas is entered in the filtering body by the air inlet pipe, is filtered by the filter mechanism
Afterwards, it is discharged by the exhaust pipe；It is characterized by: being adsorbed with the catalyst of conversion tail gas on the filter mechanism；The filtering
Mechanism includes: the fixed plate inside the filtering body and the more filter core carriers in the fixed plate；It is described to urge
Agent is adsorbed on the filter core carrier；The filter core carrier is alumina fibre high temperature filtration core；Between the filter core carrier
Gap is less than 0.1nm；The filter core carrier is Al2O3Fiber filament；The catalyst includes each component calculated in weight percent:
2. tail gas processing mechanism as described in claim 1, which is characterized in that the dispersing agent is polysorbate60；The duct is filled out
Filling agent is dodecyl trimethyl ammonium chloride or dodecyl trimethyl ammonium bromide.
3. tail gas processing mechanism as claimed in claim 2, which is characterized in that be additionally provided on the filtering body and the filtering
The back-blowing mechanism that mechanism outlet side is connected；The bottom end of the filtering body is additionally provided with dust outlet.
4. tail gas processing mechanism as claimed in claim 3, which is characterized in that be additionally provided with heating and thermal insulation inside the filtering body
Device；The exhaust pipe is connect with heat exchanger；Enter the heat exchanger through the filtered tail gas of the tail gas processing mechanism
The interior air heat exchange in entrance boiler.
5. with the processing tail gas methods of the described in any item tail gas processing mechanisms of claim 1-4, which is characterized in that by drug plus
Enter into the air inlet pipe nitrogen oxides or sulfur oxide removed in the air inlet pipe inner exhaust gas.
6. processing tail gas method according to claim 5, which is characterized in that the drug is ammonium hydroxide, lime powder, carbon
Any one of sour hydrogen sodium powder end, calcium hydroxide powder, limewash, salt water and urea.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710334868.9A CN106975353B (en) | 2017-05-12 | 2017-05-12 | A kind of tail gas processing mechanism and processing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710334868.9A CN106975353B (en) | 2017-05-12 | 2017-05-12 | A kind of tail gas processing mechanism and processing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106975353A CN106975353A (en) | 2017-07-25 |
| CN106975353B true CN106975353B (en) | 2019-11-12 |
Family
ID=59342754
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710334868.9A Expired - Fee Related CN106975353B (en) | 2017-05-12 | 2017-05-12 | A kind of tail gas processing mechanism and processing method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106975353B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110339688A (en) * | 2018-04-08 | 2019-10-18 | 富利康科技股份有限公司 | Coke oven flue gas dust removal, desulfurization, and denitrification integrated method and equipment |
| CN111804077A (en) * | 2020-07-14 | 2020-10-23 | 罗峰 | Harmful gas processing system for metal material hot working |
| CN111921294B (en) * | 2020-10-19 | 2021-01-12 | 山东中航天业科技有限公司 | Can realize metal of SOx/NOx control dust removal integration and strain a section of thick bamboo |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1039192A (en) * | 1988-06-01 | 1990-01-31 | 泰森工业公司 | The dry method separation method of harmful substance and implement the device of this method in the flue gas |
| CN106132505A (en) * | 2014-03-21 | 2016-11-16 | 托普索公司 | filter bag assembly |
-
2017
- 2017-05-12 CN CN201710334868.9A patent/CN106975353B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1039192A (en) * | 1988-06-01 | 1990-01-31 | 泰森工业公司 | The dry method separation method of harmful substance and implement the device of this method in the flue gas |
| CN106132505A (en) * | 2014-03-21 | 2016-11-16 | 托普索公司 | filter bag assembly |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106975353A (en) | 2017-07-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103706238B (en) | System and method for removing SO2, NO and Hg in smoke on the basis of heterogeneous Fenton | |
| CN105080332B (en) | Agglomerates of sintered pellets reclamation system and process | |
| CN102294171B (en) | Flue gas purifying system | |
| CN105688566A (en) | Desulfurization and denitrification device and method for sintering flue gas | |
| CN105688873B (en) | Activated carbon Thermal desorption method and its device | |
| CN103239985A (en) | Efficient coal-fired flue gas sulfur removal and mercury removal method and device | |
| CN209155342U (en) | A kind of flue gas multiple pollutant dry method cooperation-removal device | |
| CN206642490U (en) | Low temperature SCR denitration cooperates with dust arrester in a kind of industrial smoke | |
| CN104607015A (en) | Multi-pollutant co-purification method and multi-pollutant co-purification system for sintering flue gas | |
| CN104857834A (en) | Fume denitration device and method based on ozone | |
| CN106975331A (en) | A kind of smoke catalytic absorbing synergic mercury removal device and its method | |
| CN110252051B (en) | Method for dedusting, desulfurizing and denitrating boiler flue gas and removing dioxin | |
| CN206253015U (en) | Low temperature is from heat exchange type SCR denitration reaction tower | |
| CN111545026A (en) | Low-temperature efficient desulfurization and denitrification device and method for flue gas | |
| CN105833692B (en) | Industrial smoke dry type low temperature cooperates with dust-removal and desulfurizing denitration removal of mercury integrated apparatus and technique | |
| CN106975353A (en) | A kind of tail gas processing mechanism and processing method | |
| CN112933920B (en) | Desulfurization, denitrification and dedusting integrated reaction device for flue gas and desulfurization, denitrification and dedusting method | |
| CN108114591B (en) | Low-temperature flue gas treatment method | |
| CN110141966A (en) | Ozone desulfurization and denitrification system | |
| CN202136916U (en) | Flue gas purification system | |
| CN204952658U (en) | Sintering pelletizing flue gas resource system | |
| CN208542022U (en) | Incineration flue gas non-catalytic reduction denitrating system based on high concentration reducing agent | |
| CN107238297B (en) | Sintering flue gas quality directional circulation and online denitrification system | |
| CN109529575A (en) | Civil boiler for warming system for desulfuration and denitration | |
| CN205948624U (en) | Industry flue gas dry -type low temperature is in coordination with removing dust SOx/NOx control removal of mercury integrated device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20181225 Address after: 516000 No. 2 factory building, Xiao Tie Shan Village (Overseas Chinese Industrial Park), Kimcheon Road, Xiao Jin Kou Town, Huizhou, Guangdong Applicant after: Huizhou Xinyu Environmental Protection Technology Co.,Ltd. Address before: 516000 Xiaojin village, Luoyang Town, Boluo County, Huizhou, Guangdong Applicant before: BOLUO XINYU JEWELRY Co.,Ltd. |
|
| TA01 | Transfer of patent application right | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191112 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |