CN107514640A - The built-in garbage burning boiler of gas cleaning - Google Patents
The built-in garbage burning boiler of gas cleaning Download PDFInfo
- Publication number
- CN107514640A CN107514640A CN201710874419.3A CN201710874419A CN107514640A CN 107514640 A CN107514640 A CN 107514640A CN 201710874419 A CN201710874419 A CN 201710874419A CN 107514640 A CN107514640 A CN 107514640A
- Authority
- CN
- China
- Prior art keywords
- flue
- toilet
- built
- environmentally friendly
- furnace chamber
- 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.)
- Pending
Links
- 238000004140 cleaning Methods 0.000 title claims abstract description 14
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 13
- 239000007789 gas Substances 0.000 claims abstract description 15
- 239000003546 flue gas Substances 0.000 claims abstract description 13
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000003054 catalyst Substances 0.000 claims abstract description 11
- 239000000843 powder Substances 0.000 claims abstract description 8
- 238000001704 evaporation Methods 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims abstract description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 238000002347 injection Methods 0.000 claims abstract description 6
- 239000007924 injection Substances 0.000 claims abstract description 6
- 206010022000 influenza Diseases 0.000 claims abstract description 3
- 235000019504 cigarettes Nutrition 0.000 claims description 2
- 210000000038 chest Anatomy 0.000 claims 1
- 239000000779 smoke Substances 0.000 abstract description 8
- 239000000428 dust Substances 0.000 description 7
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000006477 desulfuration reaction Methods 0.000 description 3
- 230000023556 desulfurization Effects 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000006386 neutralization reaction Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 238000013517 stratification Methods 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
-
- 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
- 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
- B01D53/46—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
- B01D53/75—Multi-step processes
-
- 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
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- 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
- B01D53/81—Solid phase processes
-
- 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
- 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
- B01D53/8659—Removing halogens or halogen compounds
- B01D53/8662—Organic halogen compounds
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J3/00—Removing solid residues from passages or chambers beyond the fire, e.g. from flues by soot blowers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/22—Carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/26—Halogens or halogen 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2215/00—Preventing emissions
- F23J2215/10—Nitrogen; Compounds thereof
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Abstract
The invention discloses a kind of built-in garbage burning boiler of gas cleaning, includes furnace chamber, environmentally friendly flue, toilet and back-end ductwork, and the furnace chamber is made up of burner hearth, burning chamber and three flues, and environmentally friendly flue, toilet and back-end ductwork are set gradually after furnace chamber.The burner hearth is equipped with denitrification apparatus；Hydraulic(-ash) sluicing device is set in the burning chamber；Arrangement evaporating heating surface, superheater in three flue；The environmentally friendly flue is equipped with dry method superfine powder injection apparatus；Catalyst pottery fine chimney filter is set in the toilet；Arrangement smoke air preheater, economizer, boiler of the present invention not only can be also greatly reduced flue gas loss, be significantly improved boiler thermal output with purifying smoke in the back-end ductwork.
Description
Technical field
The present invention relates to it is a kind of burn domestic waste and produce steam be used for steam supply, generate electricity gas cleaning it is built-in
Garbage burning boiler.
Background technology
At present, domestic waste is handled using burning method, be widely applied in China.With governments at all levels pair
The pay attention to day by day of environmental protection, the pollutant emission after waste incineration require increasingly strict.Therefore, how safe, reliable, efficient,
Waste incineration is carried out environmentally friendlyly, and efficiently controls the discharge of pollutant, is already the newest problem of current garbage incineration technology.
In order to which the innoxious of domestic rubbish disposal, minimizing, recycling is better achieved, gas cleaning processing cost is effectively controlled, and
Meet harsh environment protection emission requirement, therefore develop a kind of built-in garbage burning boiler of gas cleaning first at home, that is, exist
Boiler internal sets efficient flue gas purification system, it is ensured that boiler exhaust gas can direct qualified discharge, without carrying out purified treatment again.
Further, since the gas cleaning efficiency of high efficiency boiler, the flue gas in back-end ductwork is very clean, without low-temperature corrosion and dust stratification
Etc. the influence of factor, the back-end surfaces such as economizer, smoke air preheater can be more arranged, the exhaust gas temperature of boiler can be by leading to
Normal 200 °C or so are down to about 130 °C, and system absorbs the heat content of about 70 °C of flue gases more, and therefore, boiler of the present invention is not
Only flue gas loss can also be greatly reduced, significantly improve boiler thermal output with purifying smoke.
The content of the invention
It is an object of the invention to provide a kind of built-in garbage burning boiler of gas cleaning.
Above-mentioned purpose is realized, the present invention adopts the following technical scheme that, a kind of built-in garbage burning boiler of gas cleaning, bag
Furnace chamber, environmentally friendly flue, toilet and back-end ductwork are included.It is characterized in that：The furnace chamber is by burner hearth, burning chamber and three flue groups
Into setting gradually environmentally friendly flue, toilet and back-end ductwork after furnace chamber.
The further setting of the present invention is：The burner hearth is equipped with denitrification apparatus；Hydraulic(-ash) sluicing device is set in the burning chamber；
Arrangement evaporating heating surface, superheater in three flue；The environmentally friendly flue is equipped with dry method superfine powder injection apparatus；The cleaning
The fine chimney filter of indoor setting catalyst pottery；Arrangement smoke air preheater, economizer in the back-end ductwork.
The further setting of the present invention is：The denitrification apparatus sets several layers of denitration spout in burner hearth.
By using such scheme, the present invention has advantages below：
1st, because reaction temperature window optimal denitration in the stove SNCR is 800 ~ 1000 °C, therefore burner hearth is built with SNCR denitration device,
Several layers of denitration spout are set in burner hearth, to select appropriate spout in real time according to chamber flue gas temperature, it is ensured that denitration efficiency.
The 2nd, hydraulic(-ash) sluicing device is set in burning chamber.When implementing ash disposal, the blowing pipe of crispation type is extended in burning chamber, is aligned
Minimal amount of water is sprayed at coking/dust stratification, the globule bursts, come off at once after encountering coke button, with this, quickly and efficiently removes water
The coking of cold wall surface and dust stratification.
3rd, evaporating heating surface is arranged at three chimney intakes, the import cigarette temperature of superheater can be effectively reduced, prevent superheater from going out
The problem of existing high temperature corrosion, and can effectively uniform flue gas stream and retention flying dust to ash bucket.
4th, environmentally friendly flue is equipped with dry method superfine powder injection apparatus, by the sodium acid carbonate superfine powder of jet drying, make its with
Neutralization reaction occurs for the acidic materials in flue gas, and the purpose of depickling desulfurization is reached with this.Due to the sodium acid carbonate superfine powder of penetrating
Touch in environmentally friendly flue after 300 °C ~ 400 °C of hot flue gas, sodium acid carbonate is quickly converted to sodium carbonate, and possesses it
10 times of surface area at high proportion and porosity of increase, the sodium carbonate of high surface area quickly and effectively with sour gas（HCl、SO2、
HF etc.）Generation neutralization reaction；Also, environmentally friendly flue has enough height, it can be ensured that neutralization reaction has the sufficient reaction time, therefore
The reaction efficiency of this dry-process deacidification desulfurization is higher.
The 5th, the fine chimney filter of catalyst pottery is set in toilet, i.e., by adding catalyst in ceramic fiber tube（Catalyst）, in the lump
Realize Chalk-dust filtering, accelerate catalytic elimination nitrogen oxides He the purpose of bioxin.The stock of chimney filter is fine for superfine ceramics
Dimension, its high porosity, resistant to elevated temperatures characteristic, the dust collection target of dust ＜ 5mg/Nm3 under high temperature can be achieved.Ceramic fibre chimney filter is straight
Connect on orifice plate, its excellent rigid structure, it can be ensured that higher filter efficiency and long-acting, stable performance.And
And be distributed in by catalyst on chimney filter, effectively increase the contact area of flue gas and catalyst, make gas residence time and denitration anti-
Efficiency is answered to maximize.Moreover, , bioxin and oxygen reaction in the presence of catalytic component based on vanadium, are broken down into CO2、H2O, HCl etc.
Innocuous substance is discharged.The group technology of fine chimney filter therefore, SNCR+ dry-process deacidifications desulfurization+catalyst is made pottery, it can be ensured that toilet exit
Flue gas reaches clean emission.
6th, smoke air preheater is arranged in back-end ductwork, may replace conventional arrangement of steam type airheater.Steam is empty
Air preheater is to be exchanged heat by extracting drum saturated vapor with air, therefore, smoke air preheater substitutes steam air
The setting of preheater, can reduce the extraction of drum saturated vapor, thus effectively increase the evaporation capacity of boiler.
Brief description of the drawings
Fig. 1 is boiler total figure of the embodiment of the present invention.
Each reference is in figure：1 is burner hearth, and 2 be burning chamber, and 3 be three flues, and 4 be evaporating heating surface, and 5 be superheater,
6 be environmentally friendly flue, and 7 be toilet, and 8 be back-end ductwork, and 9 be denitrification apparatus, and 10 be wet precipitator, and 11 be dry method superfine powder
Injection apparatus, 12 be the fine chimney filter of catalyst pottery, and 13 be smoke air preheater, and 14 be economizer.
Embodiment
The invention will be further described below in conjunction with the accompanying drawings.
As shown in figure 1, the built-in garbage burning boiler of gas cleaning of the present invention, include furnace chamber, environmentally friendly flue 6, clean
Clean room 7 and back-end ductwork 8.The furnace chamber is made up of burner hearth 1, the flue 3 of burning chamber 2 and three.Environmentally friendly flue is set gradually after furnace chamber
6th, toilet 7 and back-end ductwork 8.Burner hearth 1 is equipped with denitrification apparatus 9, and the denitrification apparatus 9 sets several layers of denitration to spray in burner hearth 1
Mouthful；Hydraulic(-ash) sluicing device 10 is set in burning chamber 2；Arrangement evaporating heating surface 4, superheater 5 in three flue 3；Environmentally friendly flue 6 fills
There is dry method superfine powder injection apparatus 11；Catalyst pottery fine chimney filter 12 is set in toilet 7；Arrangement flue gas is empty in the back-end ductwork 8
Air preheater 13 and economizer 14.
Claims (3)
1. a kind of built-in garbage burning boiler of gas cleaning, includes furnace chamber, environmentally friendly flue, toilet and back-end ductwork, its
It is characterised by：The furnace chamber is made up of burner hearth, burning chamber and three flues, and environmentally friendly flue, toilet and tail are set gradually after furnace chamber
Portion's flue.
2. the built-in garbage burning boiler of gas cleaning according to claim 1, it is characterized in that：The burner hearth is equipped with denitration
Device；Hydraulic(-ash) sluicing device is set in the burning chamber；Arrangement evaporating heating surface, superheater in three flue；The environment protecting cigarette
Road is equipped with dry method superfine powder injection apparatus；Catalyst pottery fine chimney filter is set in the toilet；Arrangement flue gas in the back-end ductwork
Air preheater, economizer.
3. the built-in garbage burning boiler of gas cleaning according to claim 1, it is characterized in that：The denitrification apparatus is in stove
Several layers of denitration spout are set in thorax.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710874419.3A CN107514640A (en) | 2017-09-25 | 2017-09-25 | The built-in garbage burning boiler of gas cleaning |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710874419.3A CN107514640A (en) | 2017-09-25 | 2017-09-25 | The built-in garbage burning boiler of gas cleaning |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107514640A true CN107514640A (en) | 2017-12-26 |
Family
ID=60726537
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710874419.3A Pending CN107514640A (en) | 2017-09-25 | 2017-09-25 | The built-in garbage burning boiler of gas cleaning |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107514640A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108905615A (en) * | 2018-08-31 | 2018-11-30 | 江苏绿景环保设备有限公司 | Smoke processing system and method after a kind of dangerous waste incineration |
| CN109595558A (en) * | 2018-12-05 | 2019-04-09 | 南通万达锅炉有限公司 | A kind of denitration type garbage burning boiler |
| CN110252124A (en) * | 2019-05-22 | 2019-09-20 | 山东中琦环保设备制造有限公司 | A kind of full-dry desulfurizing technique and system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205208551U (en) * | 2015-12-18 | 2016-05-04 | 哈尔滨锅炉厂有限责任公司 | A boiler structure for burning remove dust in middle of gangue |
| CN105698186A (en) * | 2016-04-26 | 2016-06-22 | 浙江伟明环保股份有限公司 | Garbage incineration boiler |
| CN107166405A (en) * | 2017-06-26 | 2017-09-15 | 浙江伟明环保股份有限公司 | A kind of refuse incineration smoke processing system |
| CN207394869U (en) * | 2017-09-25 | 2018-05-22 | 浙江伟明环保股份有限公司 | The built-in garbage burning boiler of gas cleaning |
-
2017
- 2017-09-25 CN CN201710874419.3A patent/CN107514640A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205208551U (en) * | 2015-12-18 | 2016-05-04 | 哈尔滨锅炉厂有限责任公司 | A boiler structure for burning remove dust in middle of gangue |
| CN105698186A (en) * | 2016-04-26 | 2016-06-22 | 浙江伟明环保股份有限公司 | Garbage incineration boiler |
| CN107166405A (en) * | 2017-06-26 | 2017-09-15 | 浙江伟明环保股份有限公司 | A kind of refuse incineration smoke processing system |
| CN207394869U (en) * | 2017-09-25 | 2018-05-22 | 浙江伟明环保股份有限公司 | The built-in garbage burning boiler of gas cleaning |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108905615A (en) * | 2018-08-31 | 2018-11-30 | 江苏绿景环保设备有限公司 | Smoke processing system and method after a kind of dangerous waste incineration |
| CN109595558A (en) * | 2018-12-05 | 2019-04-09 | 南通万达锅炉有限公司 | A kind of denitration type garbage burning boiler |
| CN110252124A (en) * | 2019-05-22 | 2019-09-20 | 山东中琦环保设备制造有限公司 | A kind of full-dry desulfurizing technique and system |
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