CN107191936A - Flammable solid waste pyrolytic gasification-swirl flow combustion system - Google Patents
Flammable solid waste pyrolytic gasification-swirl flow combustion system Download PDFInfo
- Publication number
- CN107191936A CN107191936A CN201710514516.1A CN201710514516A CN107191936A CN 107191936 A CN107191936 A CN 107191936A CN 201710514516 A CN201710514516 A CN 201710514516A CN 107191936 A CN107191936 A CN 107191936A
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- Prior art keywords
- air
- ash
- flue gas
- solid waste
- outlet
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- 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.)
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Classifications
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- 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
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- 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
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
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- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
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- 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
- F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The present invention relates to a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system.It includes pyrolysis installation, air preheater, flue gas chilling spray equipment, water circulating pump, air cooler, air blower and air-introduced machine, pyrolysis installation includes ash handling equipment from below to up, air distribution plate, heating response room, pyrolysis vaporizer and swirl combustion chamber, air preheater hot-blast outlet accesses the heat donor passage in air distribution plate all the way, swirl combustion chamber is accessed on another road, the outlet access air preheater of air blower, the exhanst gas outlet access air preheater of swirl combustion chamber, the exhanst gas outlet access flue gas chilling spray absorber of air preheater, the exhanst gas outlet access air-introduced machine of flue gas chilling spray absorber, the circulating water outlet access air cooler of flue gas chilling spray absorber, the outlet access flue gas chilling spray absorber of air cooler.A kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the present invention, pyrolysis efficiency high, emission amount are small, environmental pollution is small.
Description
Technical field
The present invention relates to a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system, for handling flammable solid discarded object.
Belong to environmental technology field.
Background technology
The main processing mode of current combustible solid wastes by utilizing, one is landfill, and two be to use high temperature incineration, and fills what is brought
Problem is：A large amount of soils are occupied, soil and underground water are contaminated, and nearby smell is big at landfill disposal scene；And high temperature burns
The a large amount of bioxin of institute's yield and NOx are burnt, is discharged into air, new pollutant is formed, what the living environment to the mankind was brought
Harm.Can clean, efficiently, low energy consumption processing flammable solid discarded object be human development demand, opening both at home and abroad at present
Hair and research flammable solid Castoff material energizing high-efficiency cleaning utilize study mechanism.
There is following problem in existing flammable solid offal treatment：1）Given up using land-fill method processing flammable solid
Thing so that a large amount of soils are occupied, causes soil and underground water contaminated；2）Combustible solid wastes by utilizing is handled using land-fill method,
Nearby smell is big at processing scene, and influence people normally produce and live；3）Given up using high temperature incineration processing flammable solid
Thing, a large amount of bioxin of yield and NOx emission are into air, the new pollutant of formation, the harm that the living environment to the mankind is brought,
4）The mode of either landfill or high temperature incineration, which handles the resource contained in combustible solid wastes by utilizing, combustible solid wastes by utilizing, not to be had
It is recovered.
The content of the invention
It is an object of the invention to overcome above-mentioned deficiency, there is provided a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system
System, it is pyrolyzed, and efficiency high, pyrolysis gas calorific value are high, emission amount is small, environmental pollution is small.
The object of the present invention is achieved like this：
A kind of flammable solid waste pyrolytic gasification-swirl flow combustion system, is characterized in：It includes pyrolysis installation, air preheater, cigarette
Cold water spray device out of breath, water circulating pump, air cooler, air blower and air-introduced machine, the pyrolysis installation include ash disposal and filled from below to up
Put, air distribution plate, heating response room, pyrolysis vaporizer and swirl combustion chamber, be provided with heat donor passage, the sky in the air distribution plate
The heat donor passage that air preheater hot-blast outlet is accessed in air distribution plate all the way is passed through a hot blast, and another road access swirl combustion chamber leads to
Enter secondary hot-air, the air intlet of the outlet access air preheater of the air blower, the exhanst gas outlet of the swirl combustion chamber
The gas approach of air preheater is accessed, the flue gas of the exhanst gas outlet access flue gas chilling spray absorber of air preheater enters
Mouthful, the exhanst gas outlet access air-introduced machine of flue gas chilling spray absorber, the circulating water outlet of flue gas chilling spray absorber is through following
Ring water pump accesses the import of air cooler, the circulating water intake of the outlet access flue gas chilling spray absorber of air cooler.
A kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the present invention, it is characterised in that：The ash handling equipment includes
First ash-draining gate, the first balance weight, the second ash-draining gate and the second balance weight, first ash-draining gate and the second ash-draining gate are arranged on
The exit of ash handling equipment, and the second ash-draining gate is located at the lower section of the first ash-draining gate, the first balance weight is arranged on the first ash-draining gate
Extension board end, the outlet wall of this extension board and ash handling equipment is hinged, and the second balance weight is arranged on the second ash-draining gate
The outlet wall of the end of extension board, this extension board and ash handling equipment is hinged, and the weight of first balance weight is flat equal to second
The weight of weighing apparatus block, the weight of the first balance weight is more than the weight of the first ash-draining gate, and the weight of the second balance weight is more than the second ash discharge
The weight of door.
A kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the present invention, it is characterised in that：It also includes altar lamp, institute
State altar lamp and be arranged on swirl combustion chamber side, altar lamp includes propane bottle, pressure-reducing valve and fire inspection, the outlet access of propane bottle
Fiery inspection is provided with swirl combustion chamber, both connecting lines, the exit of propane bottle is provided with pressure-reducing valve.
A kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the present invention, it is characterised in that：The side of heating response room
It is provided with peep hole.
A kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the present invention, it is characterised in that：It also includes automatic feed
Device and feed bin, the import of the outlet access automatic feeder of feed bin, outlet and the heating response room of automatic feeder
Import is connected.
Compared with prior art, the beneficial effects of the invention are as follows：
1. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the invention, has abandoned the place of traditional landfill and high temperature incineration
Reason mode, is handled flammable solid waste using anaerobic pyrolysis, and pyrolysis installation indoor temperature is uniform, and flammable solid waste is pyrolyzed tolerance
Greatly, institute's heat production calorific value of venting one's spleen is high, has fully reclaimed the resource contained in combustion solid waste.
2. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the invention, self-balancing dual chamber sealing ash handling equipment can be with
Pyrolytic gasification-swirl-flow devices on-line continuous deashing is realized, the moment ensures that system is in sealing state all the time so that system operation
During pyrolysis gas do not leak, it is full so as to ensure that flammable fixed-end forces are run in anaerobic condition while extraneous air also can not entering
Harsh process condition in foot pyrolysis gasification furnace, it is ensured that the operation steady in a long-term of equipment.
3. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the invention, the cyclone structure of swirl combustion chamber can extend
In the reaction time of pyrolysis gas, make pyrolysis solid/liquid/gas reactions complete.
4. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the invention, flue gas chilling spray absorber uses enclosed
Circulating cooling system, can continuously guarantee after a water filling, reduce water resources consumption.
5. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the invention, the hot blast that air preheater is provided is
Flammable solid waste provides the heat of reaction needed for pyrolytic gasification, and flammable solid waste contains a certain amount of moisture content, and a hot blast not only can be with
These moisture content are dried, it is also possible that flammable solid waste can reach the temperature needed for pyrolytic reaction in a short time, reduction is outer for combustion
The consumption of material, and then the operating cost of flammable solid waste is reduced, improve system overall efficiency；What air preheater was provided simultaneously is secondary
Hot blast is used for combustion-supporting to altar lamp and pyrolysis gas.
6. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system of the invention a, hot blast is passed through the heat supply in air distribution plate
Passage, this heat donor passage is isolated with lime-ash, effectively prevents lime-ash from blocking heat donor passage.
Brief description of the drawings
Fig. 1 is a kind of schematic diagram of flammable solid waste pyrolytic gasification-swirl flow combustion system of the present invention.
In figure：
Altar lamp 1,
Propane bottle 1.1,
Pressure-reducing valve 1.2,
Fire inspection 1.3,
Ash handling equipment 2,
First ash-draining gate 2.1,
First balance weight 2.2,
Second ash-draining gate 2.3,
Second balance weight 2.4,
Hot blast 3,
Air distribution plate 4,
Heating response room 5,
Pyrolysis vaporizer 6,
Secondary hot-air 7,
Swirl combustion chamber 8,
Automatic feeder 9,
Feed bin 10,
Peep hole 11,
Air preheater 12,
Flue gas chilling spray equipment 13,
Water circulating pump 14,
Air cooler 15,
Air blower 16,
Air-introduced machine 17,
Chimney 18.
Embodiment
Referring to Fig. 1, the present invention relates to a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system, it include pyrolysis installation,
Altar lamp 1, automatic feeder 9, feed bin 10, air preheater 12, flue gas chilling spray equipment 13, water circulating pump 14, air cooling
Device 15, air blower 16, air-introduced machine 17 and chimney 18.
The pyrolysis installation includes ash handling equipment 2, air distribution plate 4, heating response room 5, pyrolysis vaporizer 6 and rotation from below to up
Flow combustion chamber 8.
The altar lamp 1 is arranged on the side of swirl combustion chamber 8, and altar lamp includes propane bottle 1.1, pressure-reducing valve 1.2 and fire inspection
1.3, the outlet of propane bottle 1.1, which is accessed, is provided with fire inspection 1.3, propane bottle on swirl combustion chamber 8, both connecting lines
1.1 exit is provided with pressure-reducing valve 1.2.
Heat donor passage is provided with the air distribution plate 4, the hot-blast outlet of air preheater 12 is accessed in air distribution plate 4 all the way
Heat donor passage for a hot blast 3 needed for flammable solid waste provides pyrolytic gasification, another road access swirl combustion chamber 8 provides kept burning day and night
Lamp 1 and the combustion-supporting required secondary hot-air 7 of pyrolysis gas, the air intlet of the outlet access air preheater 12 of the air blower 16,
The exhanst gas outlet of the swirl combustion chamber 8 accesses the gas approach of air preheater 12, and the exhanst gas outlet of air preheater 12 connects
Enter the gas approach of flue gas chilling spray absorber 13, the exhanst gas outlet of flue gas chilling spray absorber 13 is accessed through air-introduced machine 17
Chimney 18, the circulating water outlet of flue gas chilling spray absorber 13 enters the import of air cooler 15, air cooling by water circulating pump 14
The circulating water intake of the outlet access flue gas chilling spray absorber 13 of device 15.
The air that the high-temperature flue gas that swirl combustion chamber 8 comes out is blasted with air blower 16 is exchanged heat, and produces a He of hot blast 3
Secondary hot-air 7, wherein, one time hot blast 3 is passed through heat donor passage, and this heat donor passage is isolated with lime-ash, therefore lime-ash will not block confession
The passage of heat.
Hot blast 3 is the heat of reaction needed for flammable solid waste provides pyrolytic gasification, and flammable solid waste contains a certain amount of
Moisture content, one time hot blast 3 can not only dry these moisture content, it is also possible that flammable solid waste can reach that pyrolysis is anti-in a short time
Required temperature, the outer consumption for fuel of reduction, and then the operating cost of the flammable solid waste of reduction are answered, system overall efficiency is improved,
Secondary hot-air 7 is used for combustion-supporting to altar lamp and pyrolysis gas.
The import of the outlet access automatic feeder 9 of feed bin 10, outlet and the heating response room 5 of automatic feeder 9
Import be connected, flammable solid waste enters heating response room 5 and to fall on air distribution plate 4 in the presence of automatic feeder 9, one
Anaerobic pyrolysis is carried out under the heating of secondary hot blast 3, automatic feeder 9 provides one with feed bin 10 with the system that is combined into can continuous feed
Sealed environment, be further ensured that flammable solid waste is run under anaerobic condition.
It is that flammable solid waste carries out the pyrolysis gas of anaerobic pyrolysis precipitation, pyrolysis in heating response room 5 in the pyrolytic gasification floor 6
Enter swirl combustion chamber 8 after gas.
The cyclone structure of swirl combustion chamber 8, extends the residence time of pyrolysis gas oxidizing fire in limited space, it is ensured that
Pyrolysis gas reacts generation CO completely2And H2O。
The side of the heating response room 5 is provided with peep hole 11, and peep hole 11 can be used for reaction condition in observing system,
While can be used for lighting a fire when initial operating stage is without hot blast.
In the presence of air blower 16, the flue gas that swirl combustion chamber 8 is produced enters flue gas chilling through air preheater 12 and sprayed
Absorption tower 13 is drenched, flue gas chilling spray absorber 13 is used to remove bioxin in flue gas, and cooled flue gas, while can remove cigarette
Some other impurity in gas, cold flue gas enters smoke stack emission in the presence of air-introduced machine 17.
In the presence of water circulating pump 14, cooling water and high-temperature flue gas heat exchange after, hot water enter air cooler 15 exchange heat after into
Flue gas chilling spray absorber 13 is reentered for cooling water.
The ash handling equipment 2 is in funnel-form, and it includes the first ash-draining gate 2.1, the first balance weight 2.2, the second ash-draining gate 2.3
With the second balance weight 2.4, the ash-draining gate 2.3 of the first ash-draining gate 2.1 and second is arranged on the exit of ash handling equipment 2, and
Two ash-draining gates 2.3 are located at the lower section of the first ash-draining gate 2.1, and the first balance weight 2.2 is arranged on the extension board of the first ash-draining gate 2.1
End, the outlet wall of this extension board and ash handling equipment 2 is hinged, and the second balance weight 2.4 is arranged on the extension of the second ash-draining gate 2.3
The end of plate, the outlet wall of this extension board and ash handling equipment 2 is hinged, and the weight of first balance weight 2.2 is flat equal to second
The weight of weighing apparatus block 2.4, the weight of the first balance weight 2.2 is more than the weight of the first ash-draining gate 2.1, the weight of the second balance weight 2.4
More than the weight of the second ash-draining gate 2.3, when the lime-ash accumulated on the first ash-draining gate 2.1 reaches a certain amount of, i.e. lime-ash and first row
The weight of grey door 2.1 and during more than the first balance weight 2.2, the first ash-draining gate 2.1 falls opening, and lime-ash falls on the second ash-draining gate
On 2.3, until when the first ash-draining gate 2.1 is with the weight of residual ash slag thereon and less than the first balance weight 2.2, the first balance weight
2.2 push so that 2.1 first ash-draining gates 2.1 lift closing, when the weight of lime-ash and the second ash-draining gate 2.3 and more than the second balance
During block 2.4, the second ash-draining gate 2.3 falls opening, discharges lime-ash；When the first ash-draining gate 2.1 is opened, the second ash-draining gate 2.3 is in
Closed mode, and when the second ash-draining gate 2.3 opens discharge lime-ash, the first ash-draining gate 2.1 is closed, therefore, ash disposal
Device 2 can ensure that system is in sealing state all the time constantly so that pyrolysis gas does not leak in system operation, while outside empty
Gas also can not entering, so as to ensure that flammable fixed-end forces are run in anaerobic condition, meets technique behaviour harsh in pyrolysis gasification furnace
Make condition, it is ensured that the operation steady in a long-term of equipment.
Claims (5)
1. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system, it is characterised in that：It includes pyrolysis installation, air preheat
Device, flue gas chilling spray equipment, water circulating pump, air cooler, air blower and air-introduced machine, the pyrolysis installation include removing from below to up
Heat donor passage is provided with apparatus for ash, air distribution plate, heating response room, pyrolysis vaporizer and swirl combustion chamber, the air distribution plate, institute
State the heat donor passage that air preheater hot-blast outlet accesses in air distribution plate all the way and be passed through a hot blast, swirl flow combustion is accessed on another road
Room is passed through secondary hot-air, the air intlet of the outlet access air preheater of the air blower, the flue gas of the swirl combustion chamber
The gas approach of outlet access air preheater, the exhanst gas outlet of air preheater accesses the flue gas of flue gas chilling spray absorber
Import, the exhanst gas outlet access air-introduced machine of flue gas chilling spray absorber, the circulating water outlet warp of flue gas chilling spray absorber
Water circulating pump accesses the import of air cooler, the circulating water intake of the outlet access flue gas chilling spray absorber of air cooler.
2. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system according to claim 1, it is characterised in that：It is described to remove
Apparatus for ash includes the first ash-draining gate, the first balance weight, the second ash-draining gate and the second balance weight, first ash-draining gate and second row
Grey door is arranged on the exit of ash handling equipment, and the second ash-draining gate is located at the lower section of the first ash-draining gate, and the first balance weight is arranged on
The outlet wall of the end of the extension board of first ash-draining gate, this extension board and ash handling equipment is hinged, and the second balance weight is arranged on
The outlet wall of the end of the extension board of two ash-draining gates, this extension board and ash handling equipment is hinged, the weight of first balance weight
Equal to the weight of the second balance weight, the weight of the first balance weight is more than the weight of the first ash-draining gate, and the weight of the second balance weight is big
In the weight of the second ash-draining gate.
3. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system according to claim 1 or 2, it is characterised in that：It
Also include altar lamp, the altar lamp is arranged on swirl combustion chamber side, and altar lamp includes propane bottle, pressure-reducing valve and fire inspection, third
Fiery inspection is provided with the outlet access swirl combustion chamber of alkane bottle, both connecting lines, the exit of propane bottle is provided with
Pressure-reducing valve.
4. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system according to claim 1 or 2, it is characterised in that：Plus
The side of thermal reaction chamber is provided with peep hole.
5. a kind of flammable solid waste pyrolytic gasification-swirl flow combustion system according to claim 1 or 2, it is characterised in that：It
Also include automatic feeder and feed bin, the import of the outlet access automatic feeder of feed bin, the outlet of automatic feeder
Import with heating response room is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710514516.1A CN107191936A (en) | 2017-06-29 | 2017-06-29 | Flammable solid waste pyrolytic gasification-swirl flow combustion system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710514516.1A CN107191936A (en) | 2017-06-29 | 2017-06-29 | Flammable solid waste pyrolytic gasification-swirl flow combustion system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107191936A true CN107191936A (en) | 2017-09-22 |
Family
ID=59880706
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710514516.1A Pending CN107191936A (en) | 2017-06-29 | 2017-06-29 | Flammable solid waste pyrolytic gasification-swirl flow combustion system |
Country Status (1)
| Country | Link |
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| CN (1) | CN107191936A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108061303A (en) * | 2017-11-21 | 2018-05-22 | 华中科技大学 | Suitable for the pollutant removing structure and burner of domestic garbage pyrolysis gasification gas |
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| JP2009186120A (en) * | 2008-02-07 | 2009-08-20 | Ihi Corp | Pyrolyzing device |
| CN104197337A (en) * | 2014-07-31 | 2014-12-10 | 南通星球石墨设备有限公司 | Incineration tail gas treatment process based on quench tower |
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| CN205740765U (en) * | 2016-05-17 | 2016-11-30 | 寻乌县宁达科机械设备开发有限公司 | A kind of kiln automatic ash-discharging device |
| CN207006173U (en) * | 2017-06-29 | 2018-02-13 | 江苏焱鑫科技股份有限公司 | Flammable solid waste pyrolytic gasification-swirl flow combustion system |
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2017
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Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009186120A (en) * | 2008-02-07 | 2009-08-20 | Ihi Corp | Pyrolyzing device |
| CN104197337A (en) * | 2014-07-31 | 2014-12-10 | 南通星球石墨设备有限公司 | Incineration tail gas treatment process based on quench tower |
| CN104930517A (en) * | 2015-06-30 | 2015-09-23 | 中国科学院广州能源研究所 | Rubbish pyrolysis swirling combustion device |
| CN204784908U (en) * | 2015-07-09 | 2015-11-18 | 中节能（石家庄）环保能源有限公司 | Automatic keep apart and turn over board -like grey valve of putting |
| CN205740765U (en) * | 2016-05-17 | 2016-11-30 | 寻乌县宁达科机械设备开发有限公司 | A kind of kiln automatic ash-discharging device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108061303A (en) * | 2017-11-21 | 2018-05-22 | 华中科技大学 | Suitable for the pollutant removing structure and burner of domestic garbage pyrolysis gasification gas |
| CN108061303B (en) * | 2017-11-21 | 2019-08-13 | 华中科技大学 | Pollutant removing structure and burner suitable for domestic garbage pyrolysis gasification gas |
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