CN106949480A - A kind of pyrogenation incinerator - Google Patents
A kind of pyrogenation incinerator Download PDFInfo
- Publication number
- CN106949480A CN106949480A CN201710222910.8A CN201710222910A CN106949480A CN 106949480 A CN106949480 A CN 106949480A CN 201710222910 A CN201710222910 A CN 201710222910A CN 106949480 A CN106949480 A CN 106949480A
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- Prior art keywords
- combustion chamber
- pyrogenation incinerator
- outlet
- ash
- exhaust pipe
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- 238000002485 combustion reaction Methods 0.000 claims abstract description 67
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 239000007789 gas Substances 0.000 claims abstract description 22
- 239000007921 spray Substances 0.000 claims description 19
- 239000003595 mist Substances 0.000 claims description 17
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 16
- 239000003546 flue gas Substances 0.000 claims description 16
- 238000000197 pyrolysis Methods 0.000 claims description 15
- 239000000779 smoke Substances 0.000 claims description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 238000003032 molecular docking Methods 0.000 claims description 3
- 230000003647 oxidation Effects 0.000 abstract description 9
- 238000007254 oxidation reaction Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 7
- 238000010304 firing Methods 0.000 abstract description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 4
- 238000000354 decomposition reaction Methods 0.000 abstract description 3
- 238000009826 distribution Methods 0.000 abstract description 3
- 230000009977 dual effect Effects 0.000 abstract description 3
- 239000000428 dust Substances 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000000746 purification Methods 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 239000010813 municipal solid waste Substances 0.000 description 6
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000007857 degradation product Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000010525 oxidative degradation reaction Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 230000010259 detection of temperature stimulus Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 229960004424 carbon dioxide Drugs 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002510 pyrogen Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 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
- F23G5/02—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
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
- F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
-
- 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
- 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
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The invention discloses a kind of pyrogenation incinerator, including pyrogenation incinerator and exhaust gas cleaner, the pyrogenation incinerator is mainly made up of the first combustion chamber and the second combustion chamber, the wherein charging aperture of pyrogenation incinerator and the first combustion chamber, the present invention passes through hot conditions, pass through second-time burning, realize the purpose of pyrolytic incineration, exhaust gas cleaner is then used to realize the final purification to whole tail gas, sprayed including water and realize particulate collection, and demisting and the oxidation Decomposition of corresponding nuisance, it is final to realize discharge；Because primary air flow is few, flying dust yield is few；Nitrogen oxides yield is few, secondary to prevent secondary pollution；Compact conformation, easy to maintenance, high treating effect；Temperature control, high degree of automation can be achieved；Dual firing chamber's temperature is high, and burning is complete, and the residence time is long, is not likely to produce bioxin；Fractional combustion, controls hearth combustion operating mode, the release of reasonable distribution chemical energy burns most effect to reach by controlling air capacity.
Description
Technical field
The present invention relates to field of garbage disposal, specifically a kind of pyrogenation incinerator.
Background technology
Pyrolysis needs to absorb amount of heat；Primary product is flammable low molecular compound：Gaseous hydrogen, methane, one
Carbonoxide；The organic matters such as methanol, acetone, acetic acid, the acetaldehyde of liquid and tar, solvent naphtha etc..Mainly coke and the charcoal of solid-state
It is black；Pyrolysismethod is the thermal instability using organic matter in garbage, and heating distillation is carried out to it under anaerobic or anoxia condition, real
Matter is to heat the process that organic molecule is allowed to be cracked into small molecule precipitation, and it contains many complicated physical and chemical processes.
Early stage is concentrated mainly on two aspects to the exploitation purpose of pyrolytic technique.One is using the U.S. as representative, to return
For the purpose of sustainability of the harvesting and storing energy (fuel gas, fuel oil and carbon black)；Another is, using Japan as representative, to reduce and burn what is caused
Secondary pollution and the amount of waste for needing landfill stabilization, for the purpose of the exploitation of nuisanceless type processing system.
Pyrolysis is divided into snead process and indirect heating method, wherein snead process be supplied be pyrolyzed thing heat be by
Pyrogen（Handled discarded object）Part directly burning provides heat produced when supplementing fuel to pyrolysis reactor, due to
Burning needs to provide comburant oxygen, and uses air, oxygen-enriched or pure oxygen, and its fuel factor for being pyrolyzed combustible gas is different, pure oxygen
Make catalyst can produce the gases such as CO2, H2O be mixed in pyrolysis combustible gas in, dilute combustible gas, as a result reduce the heat of pyrolysis gas
Effect.Indirect heating method be the waste material being pyrolyzed by direct heating medium in pyrolysis reactor（Or pyrolysis oven）In separate
A kind of method come.It can be conducted heat using the heat conduction of dry wall formula or a kind of intermediate medium to do.Between solution heating major advantage be
The grade of its product is high, and its heat production value produces heat up to 18630 KJ/m3 equivalent to the snead process of air oxidant
The three times of value are more, can directly be utilized as combustion gas completely.
Processing of the tradition to rubbish is generally pyrolysis or burning, but both there is shortcoming, wherein directly burning away the refuse
Easy firing not exclusively, requires high, equipment investment is big to tail gas clean-up, and pyrolysis operating cost is high, energy consumption is big, and thermal decomposition product composition is answered
It is miscellaneous, it can not technically be converted resource and be used.
The content of the invention
It is an object of the invention to provide a kind of pyrogenation incinerator, the problem of to solve to propose in above-mentioned background technology.
To achieve the above object, the present invention provides following technical scheme：
A kind of pyrogenation incinerator, including pyrogenation incinerator and exhaust gas cleaner, the pyrogenation incinerator are main by the first combustion
Burn room and the second combustion chamber is constituted, wherein the charging aperture of pyrogenation incinerator and the first combustion chamber, the bottom of the first combustion chamber
Portion is exported provided with the first lime-ash, and the first lime-ash exit is provided with into oxygen support, and the pyrolysis of the first combustion chamber is compared with low temperature
Under degree control, carried out, measured the need for the inlet of limitation air is less than burning completely in this engineering with very low speed, this
Sample, rubbish heating, is dehydrated, pyrolysis, and then discharges moisture and volatile materials, and nonvolatile combustible is completely warm in a combustion room
Solution, and noncombustibles then rolls up lime-ash；First exhaust pipe of first combustion chamber and the air inlet of the second combustion chamber
Dock, and the first exhaust pipe is also associated with secondary wind inleting tube, the second combustion chamber being provided with burner, and the second combustion chamber
Bottom provided with the second lime-ash export, the first lime-ash outlet and the second lime-ash export lower section be provided with slag-drip opening；Second combustion chamber
Side wall on be also equipped with the second exhaust pipe, the second exhaust pipe is connected with the smoke exhaust pipe of pyrogenation incinerator, second
Combustion chamber is that the flue gas produced in the first combustion chamber is added combustion air further to aoxidize until thoroughly burning, passes through high temperature bar
First combustion chamber oxidative degradation products are carried out complete oxidation combustion reaction, also referred to as oxygen-enriched combusting by part；The exhaust gas cleaner
Mainly it is made up of high-pressure water mist shower spray device and flue gas cleaner, wherein smoke exhaust pipe and the bottom air inlet pair of high-pressure water mist shower spray device
Connect, the inside top of high-pressure water mist shower spray device is provided with sprayer, and the water inlet of sprayer connects high-pressure hydraulic pump by water inlet pipe,
The arrival end of high-pressure hydraulic pump accesses circulating water pool by water pipe, and the top gas outlet of high-pressure water mist shower spray device is connected with blast pipe,
Blast pipe connects the arrival end of flue gas cleaner, and flue gas cleaner is used to realize flue gas deep oxidation and demisting, and flue gas is net
The outlet for changing device is connected with cyclone separator, and the exhaust outlet of cyclone separator is connected with the smoke exhaust pipe being vertically arranged.
It is used as further scheme of the invention：The bottom of the high-pressure water mist shower spray device is provided with water return outlet, and water return outlet is logical
Cross in return pipe access circulating water pool, the water resource of accumulation can realize recycling in high-pressure water mist shower spray device.
It is used as further scheme of the invention：TEMP is mounted in first combustion chamber and the second combustion chamber
Device, the detection of temperature is realized using temperature sensor, so as to realize the regulation of intake.
It is used as further scheme of the invention：The bottom of the cyclone separator is provided with ash collection slot.
It is used as further scheme of the invention：The inner bottom part position of first combustion chamber is provided with rotary fire grate, so that
So that burning is more abundant.
Beneficial effects of the present invention：The present invention, by second-time burning, realizes the purpose of pyrolytic incineration by hot conditions,
Exhaust gas cleaner is then used to realize that the final purification to whole tail gas, including water spray and realize particulate collection, and demisting
With the oxidation Decomposition of corresponding nuisance, final realize is discharged；Because primary air flow is few, flying dust yield is few；Nitrogen oxides is produced
Amount is few, secondary to prevent secondary pollution；Compact conformation, easy to maintenance, high treating effect；Temperature control can be achieved, journey is automated
Degree is high；Dual firing chamber's temperature is high, and burning is complete, and the residence time is long, is not likely to produce bioxin；Fractional combustion, by controlling air capacity
Hearth combustion operating mode is controlled, the release of reasonable distribution chemical energy burns most effect to reach.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Fig. 2 is partial structural diagram of the present invention.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Refer in Fig. 1~2, the embodiment of the present invention, a kind of pyrogenation incinerator, including pyrogenation incinerator 1 and tail gas it is net
Makeup is put, the pyrogenation incinerator 1 is mainly made up of the first combustion chamber 16 and the second combustion chamber 18, wherein pyrogenation incinerator 1
Charging aperture 2 is connected with the first combustion chamber 16, and the bottom of the first combustion chamber 16 goes out provided with the first lime-ash outlet 3, and the first lime-ash
It is provided with mouth 3 into oxygen support 4, the pyrolysis of the first combustion chamber 16 is under lower temperature control, to be carried out with very low speed,
Measured the need for the inlet of limitation air is less than burning completely in this engineering, so, rubbish heating, dehydration, pyrolysis, and then release
Moisture and volatile materials are released, nonvolatile combustible is pyrolyzed completely in a combustion room, and noncombustibles then rolls up lime-ash；Institute
The first exhaust pipe 19 for stating the first combustion chamber 16 is docked with the air inlet of the second combustion chamber 18, and the first exhaust pipe 19
It is also associated with secondary wind inleting tube 20, the second combustion chamber 18 that burner is installed, and the bottom of the second combustion chamber 18 is provided with second
The lower section of lime-ash outlet 17, the outlet 3 of the first lime-ash and the second lime-ash outlet 17 is provided with slag-drip opening 5；The side wall of second combustion chamber 18
On be also equipped with the second exhaust pipe 21, the second exhaust pipe 21 is connected with the smoke exhaust pipe 6 of pyrogenation incinerator 1, second
Combustion chamber 18 is that the flue gas produced in the first combustion chamber 16 is added combustion air further to aoxidize until thoroughly burning, passes through height
The oxidative degradation products of first combustion chamber 16 are carried out complete oxidation combustion reaction, also referred to as oxygen-enriched combusting by warm condition；The tail gas is net
Makeup is put mainly to be made up of high-pressure water mist shower spray device 7 and flue gas cleaner 9, wherein smoke exhaust pipe 6 and the bottom of high-pressure water mist shower spray device 7
Portion's air inlet docking, the inside top of high-pressure water mist shower spray device 7 is provided with sprayer, and the water inlet of sprayer passes through water inlet pipe 14
High-pressure hydraulic pump 13 is connected, the arrival end of high-pressure hydraulic pump 13 accesses circulating water pool 15, the top of high-pressure water mist shower spray device 7 by water pipe
Gas outlet is connected with blast pipe 8, and blast pipe 8 connects the arrival end of flue gas cleaner 9, and flue gas cleaner 9 is used to realize flue gas
Deep oxidation and demisting, the outlet of flue gas cleaner 9 are connected with cyclone separator 10, the exhaust outlet connection of cyclone separator 10
There is the smoke exhaust pipe 11 being vertically arranged.
The bottom of the high-pressure water mist shower spray device 7 is provided with water return outlet, and water return outlet accesses circulating water pool 15 by return pipe
Interior, the water resource of accumulation can realize recycling in high-pressure water mist shower spray device 7.
Temperature sensor is mounted in the combustion chamber 18 of first combustion chamber 16 and second, is realized using temperature sensor
The detection of temperature, so as to realize the regulation of intake.
The bottom of the cyclone separator 10 is provided with ash collection slot.
The inner bottom part position of first combustion chamber 16 is provided with rotary fire grate, so that burning is more abundant.
The present invention operation principle be：The pyrolysis of first combustion chamber 16 is under lower temperature control, with very low speed
Carry out, measured the need for the inlet of limitation air is less than burning completely in this engineering, so, rubbish heating is dehydrated, heat
Solution, and then moisture and volatile materials are discharged, nonvolatile combustible is pyrolyzed completely in a combustion room, and noncombustibles is then accumulated
Into lime-ash, the second combustion chamber 18 is that the flue gas produced in the first combustion chamber 16 is added combustion air further to aoxidize until thoroughly
The oxidative degradation products of first combustion chamber 16, by hot conditions, are carried out complete oxidation combustion reaction, also referred to as oxygen-enriched combustion by burning
Burn, exhaust gas cleaner is then used to realize that the final purification to whole tail gas, including water spray and realize particulate collection, and removes
The oxidation Decomposition of mist and corresponding nuisance, it is final to realize discharge；Because primary air flow is few, flying dust yield is few；Nitrogen oxidation produce
Raw amount is few, secondary to prevent secondary pollution；Compact conformation, easy to maintenance, high treating effect；Temperature control, automation can be achieved
Degree is high；Dual firing chamber's temperature is high, and burning is complete, and the residence time is long, is not likely to produce bioxin；Fractional combustion, by controlling air
Amount control hearth combustion operating mode, reasonable distribution chemical energy release burns most effect to reach.
It is obvious to a person skilled in the art that the invention is not restricted to the details of above-mentioned one exemplary embodiment, Er Qie
In the case of without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, embodiment all should be regarded as exemplary, and be nonrestrictive, the scope of the present invention is by appended power
Profit is required rather than described above is limited, it is intended that all in the implication and scope of the equivalency of claim by falling
Change is included in the present invention.Any reference in claim should not be considered as to the claim involved by limitation.
Claims (5)
1. a kind of pyrogenation incinerator, it is characterised in that：Including pyrogenation incinerator（1）And exhaust gas cleaner, the pyrolysis burns
Burn stove（1）Mainly by the first combustion chamber（16）With the second combustion chamber（18）Constitute, wherein pyrogenation incinerator（1）Charging aperture（2）
With the first combustion chamber（16）It is connected, the first combustion chamber（16）Bottom provided with the first lime-ash export（3）, and the outlet of the first lime-ash
（3）Place is provided with into oxygen support（4）；First combustion chamber（16）The first exhaust pipe（19）With the second combustion chamber（18）
Air inlet docking, and the first exhaust pipe（19）It is also associated with secondary wind inleting tube（20）, the second combustion chamber（18）It is interior to install
There are burner, and the second combustion chamber（18）Bottom provided with the second lime-ash export（17）, the outlet of the first lime-ash（3）With the second lime-ash
Outlet（17）Lower section be provided with slag-drip opening（5）；Second combustion chamber（18）Side wall on be also equipped with the second exhaust pipe（21）,
Second exhaust pipe（21）With pyrogenation incinerator（1）Smoke exhaust pipe（6）It is connected；The exhaust gas cleaner is main by high pressure
Water smoke shower spray device（7）And flue gas cleaner（9）Constitute, wherein smoke exhaust pipe（6）With high-pressure water mist shower spray device（7）Bottom air inlet
Docking, high-pressure water mist shower spray device（7）Inside top sprayer is installed, the water inlet of sprayer passes through water inlet pipe（14）Connection
High-pressure hydraulic pump（13）, high-pressure hydraulic pump（13）Arrival end circulating water pool is accessed by water pipe（15）, high-pressure water mist shower spray device（7）'s
Top gas outlet is connected with blast pipe（8）, blast pipe（8）Connect flue gas cleaner（9）Arrival end, flue gas cleaner（9）'s
Outlet is connected with cyclone separator（10）, cyclone separator（10）Exhaust outlet be connected with the smoke exhaust pipe being vertically arranged（11）.
2. a kind of pyrogenation incinerator according to claim 1, it is characterised in that：The high-pressure water mist shower spray device（7）Bottom
Portion is provided with water return outlet, and water return outlet accesses circulating water pool by return pipe（15）It is interior.
3. a kind of pyrogenation incinerator according to claim 1, it is characterised in that：First combustion chamber（16）With the second combustion
Burn room（18）Inside it is mounted on temperature sensor.
4. a kind of pyrogenation incinerator according to claim 1, it is characterised in that：The cyclone separator（10）Bottom set
There is ash collection slot.
5. a kind of pyrogenation incinerator according to claim 1, it is characterised in that：First combustion chamber（16）Inner bottom part
Position is provided with rotary fire grate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201710222910.8A CN106949480A (en) | 2017-04-07 | 2017-04-07 | A kind of pyrogenation incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710222910.8A CN106949480A (en) | 2017-04-07 | 2017-04-07 | A kind of pyrogenation incinerator |
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| CN106949480A true CN106949480A (en) | 2017-07-14 |
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| CN201710222910.8A Pending CN106949480A (en) | 2017-04-07 | 2017-04-07 | A kind of pyrogenation incinerator |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107575877A (en) * | 2017-08-31 | 2018-01-12 | 陈凤仪 | A kind of medicinal health garbage incinerator and its technological process |
| CN108980853A (en) * | 2018-09-12 | 2018-12-11 | 中国环境科学研究院 | Incineration of refuse flyash and percolate cooperative processing method and device |
| CN109945193A (en) * | 2019-03-06 | 2019-06-28 | 钟康亮 | A combined device for recycling and purifying waste gas from waste incineration |
| CN110068014A (en) * | 2018-11-10 | 2019-07-30 | 自贡市现代秋收机械有限公司 | A kind of purification method of house refuse burning processing |
| CN110332547A (en) * | 2019-06-19 | 2019-10-15 | 中国铁道科学研究院集团有限公司节能环保劳卫研究所 | A pyrolysis and incineration treatment device for domestic waste in railway station area |
| CN111237766A (en) * | 2020-01-10 | 2020-06-05 | 沈俊欣 | Household garbage pyrolysis furnace equipment with movable slag discharging channel |
| CN113124410A (en) * | 2019-12-31 | 2021-07-16 | 浙江千尧环境工程有限公司 | Combustion device with low nitrogen oxide emission |
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