CN108758642A - A kind of gasified combustion apparatus - Google Patents
A kind of gasified combustion apparatus Download PDFInfo
- Publication number
- CN108758642A CN108758642A CN201810781284.0A CN201810781284A CN108758642A CN 108758642 A CN108758642 A CN 108758642A CN 201810781284 A CN201810781284 A CN 201810781284A CN 108758642 A CN108758642 A CN 108758642A
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- Prior art keywords
- vaporizer
- combustion chamber
- flue
- combustion apparatus
- air
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- 238000002485 combustion reaction Methods 0.000 title claims abstract description 61
- 239000006200 vaporizer Substances 0.000 claims abstract description 44
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000003546 flue gas Substances 0.000 claims abstract description 16
- 238000009826 distribution Methods 0.000 claims abstract description 13
- 238000005338 heat storage Methods 0.000 claims abstract description 10
- 238000000926 separation method Methods 0.000 claims abstract description 8
- 238000009825 accumulation Methods 0.000 claims abstract description 7
- 230000008901 benefit Effects 0.000 claims abstract description 6
- 238000012216 screening Methods 0.000 claims description 12
- 239000002893 slag Substances 0.000 claims description 10
- 239000003818 cinder Substances 0.000 claims description 7
- 239000011819 refractory material Substances 0.000 claims description 5
- 239000004744 fabric Substances 0.000 claims 2
- 238000002309 gasification Methods 0.000 abstract description 17
- 239000007789 gas Substances 0.000 description 13
- 239000002699 waste material Substances 0.000 description 13
- 239000004033 plastic Substances 0.000 description 8
- 229920003023 plastic Polymers 0.000 description 8
- 230000008859 change Effects 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000000446 fuel Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000008246 gaseous mixture Substances 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000036632 reaction speed Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000006004 Quartz sand Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000010908 plant waste Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
- F23G5/08—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
-
- 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
- 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
-
- 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
-
- 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
- F23L9/00—Passages or apertures for delivering secondary air for completing combustion of fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/10—Combustion in two or more stages
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/28—Plastics or rubber like materials
Landscapes
- 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
A kind of gasified combustion apparatus, including the vaporizer, combustion chamber, secondary furnace, the back-end ductwork that connect side by side successively, and form Zigzag type logistics corridor.Be equipped with top flue between vaporizer and combustion chamber and crossed in the flue of top and be provided with heat-accumulation combustor, in along flue gas flow direction be arranged in parallel with several heat storages, if being separated into dry flue gas circulation road by top flue is crossed；Several overfiren air ports are arranged in heat storage front end, and each overfiren air port tilts the direction of flow towards flue gas circulation road.Bottom of combustion chamber, which is connected to and is formed with secondary furnace bottom, turns to separation chamber.Combustion chamber top is provided with several tertiary air orifices, and tertiary air orifice is arranged on the wall surface of the combustion chamber opposite sides Liang Ge, is arranged in the way of from top flue outlet bottom excessively to top of combustion chamber oblique arrangement.Staged air distribution of the present invention, Zigzag type logistics extend fire stroke, and use low temperature gasification high-temp combustion, have the advantages that initial ejection is good, burn-off rate is high.
Description
Technical field
The present invention relates to a kind of gasified combustion apparatus, are used for the gasification and burning of plastics, damaged tire the like waste, belong to gas
Change combustion field.
Background technology
Plastics, damaged tire, scrap rubber the like waste recycling be constantly subjected to extensive concern.
Plastics, damaged tire, the heat treatment of scrap rubber the like waste and recycling include burning and pyrolytic gasification.Due to
Such waste calorific value is generally higher, has higher using energy source value.However, either burning or pyrolytic gasification utilizes
In, it often there are problems that direct utilization rate is not high and generate secondary pollution.And catalyzing manufacturing of hydrogen or alcohol gasification temperature processed height, technique
It is complicated.Likewise, the process system of most of gasification and melt-combustion also all utilizes high-temperature gasification and high-temperature fusion technology, energy
Consumption is big, and device structure is complicated.
Invention content
It being used for plastics, the gasification of damaged tire the like waste and burner the purpose of the present invention is to provide a kind of, is utilized
The temperature sensitive feature of thermochemical property, gasifies at a lower temperature, and reaction speed is low, be easy it is uniform thoroughly, then into
Row high-temp combustion can ensure initial ejection and burn-off rate simultaneously.
The present invention is achieved through the following technical solutions：
A kind of gasified combustion apparatus, including vaporizer, combustion chamber, secondary furnace, back-end ductwork and feeding equipment；The vaporizer,
Combustion chamber, secondary furnace and back-end ductwork are arranged in juxtaposition and are sequentially connected, and form Zigzag type logistics corridor；The vaporizer with it is described
Top flue was equipped between combustion chamber, described cross in the flue of top is provided with burner；The bottom of combustion chamber and the secondary furnace
Bottom is connected to and forms Zigzag type logistics corridor；The secondary furnace top is connected to the back-end ductwork top；The feed dress
It installs in the vaporizer front end；The vaporizer bottom side is provided with slagging channel.
In above-mentioned technical proposal, the air distribution plate that the vaporizer bottom is provided with air compartment and is arranged on the air compartment, institute
Air distribution plate inclination arrangement is stated, the least significant end in air distribution plate is arranged in the slagging channel.
In above-mentioned technical proposal, the vaporizer top is cross-section area, lower part is variable cross-section area；The vaporizer lower part
Variable cross-section area is up followed successively by flaring area and taper by bottom.
In above-mentioned technical proposal, the air compartment air distribution is by the minimum according to the vaporizer lower cross section area maximum
Wind speed 0.5≤w min ≤ 1m/s is arranged.
In above-mentioned technical proposal, the vaporizer internal face lays refractory material.
In above-mentioned technical proposal, described device further includes slag cooler and screening plant；The vaporizer lower part is logical with deslagging
The opposite side in road is provided with benefit cinder notch；The slag cooler is connected between the slagging channel and screening plant, the screening
Device is connected with the benefit cinder notch.
In above-mentioned technical proposal, the burner front end is provided with several overfiren air ports.
In above-mentioned technical proposal, the burner selects heat-accumulation combustor, in be arranged in parallel with along flue gas flow direction it is several
Heat storage, if the top flue of crossing is separated into dry flue gas circulation road；Several described overfiren air ports are arranged in heat storage front end,
And each overfiren air port tilts the direction of flow towards flue gas circulation road.
In above-mentioned technical proposal, the combustion chamber and secondary furnace bottom opposite tilt form and turn to separation chamber, described
It turns to separation chamber bottom and ash ejector is set；The secondary furnace top is provided with superheater.
In above-mentioned technical proposal, the combustion chamber top is provided with several tertiary air orifices, several described tertiary air orifices
It is arranged on the wall surface of the opposite sides the combustion chamber Liang Ge, according to from the top flue outlet bottom of crossing to the top of combustion chamber
The mode of oblique arrangement is arranged.
The present invention has the following advantages and beneficial effects：1）Plastics, tire the like waste fuel thermochemical property are to temperature
Sensitivity gasifies under lower temperature, and reaction speed is relatively low, then uniform thorough conversion easy to implement carries out high-temp combustion, energy
Enough while ensureing good initial ejection and very high burn-off rate；2）Variable cross-section low-speed turbulent gasifier bed so that fuel reaction is equal
It is even, and the refractory material insulated design of lower section can be gasified with accumulation of heat, greatly improved the adaptability of fuel and can be improved using energy source
Rate；3）The design of Zigzag type combustion chamber increases burning time promotion combustion efficiency, while can be in reversal chamber separate section flying dust.
Description of the drawings
Fig. 1 is a kind of gasified combustion apparatus schematic diagram according to the present invention.
Fig. 2 is heat-accumulation combustor schematic diagram according to the present invention.
In figure：1- vaporizers；The combustion chambers 2-；3- secondary furnaces；4- crosses top flue；5- back-end ductworks；6- burners；
7- charging gears；8- air compartments；9- overfiren air ports；10- tertiary air orifices；11- superheaters；12- economizers；13- is empty pre-
Device；14- slag coolers；15- screening plants；16- mends cinder notch；17- heat storages.
Specific implementation mode
The specific implementation mode and the course of work of the present invention are further described below in conjunction with the accompanying drawings.
The orientation such as upper, lower, left, right, front and rear in present specification term be position relationship based on ... shown in the drawings and
It establishes.Attached drawing is different, then corresponding position relationship is also possible to change therewith, therefore cannot be interpreted as with this to protecting model
The restriction enclosed.
A kind of gasified combustion apparatus of the present invention is suitable for the gasification and burning of a variety of wastes such as plastics, damaged tire.
As shown in Figure 1, a kind of gasified combustion apparatus, including vaporizer 1, combustion chamber 2, secondary furnace 3, back-end ductwork 5 and into
Expect device 7.Charging gear 7 is arranged in 1 front end of vaporizer.Vaporizer 1, combustion chamber 2, secondary furnace 3 and back-end ductwork 5 are arranged side by side successively
It arranges and connects, form the multiple Zigzag type logistics corridor of rising-downlink-rising-downlink-rising, prolong to the greatest extent
The distinguished and admirable journey of cigarette has been grown, fire stroke has especially been extended and so that burning is thoroughly abundant.
1 top of vaporizer is cross-section area, lower part is variable cross-section area.1 lower part variable cross-section area of vaporizer by bottom up according to
Secondary is flaring area and taper.The intersecting horizontal face sectional area in flaring area and taper（That is vaporizer cross-sectional area）Maximum, gradually
It is connected with cross-section area at the top of contracting area.Plastics, tire the like waste feed vaporizer 1,1 bottom of vaporizer by feeding equipment 7
It is provided with air compartment 8 and is passed through First air as gasifying agent and waste progress gasification reaction.Air compartment 8 is equipped with air distribution plate and blast cap.
In order to ensure that 1 lower part of vaporizer is in low-speed turbulent state, so that waste gasification is evenly and more thorough, air compartment is according to gas
The minimum windspeed 0.5 of change 1 lower cross section area maximum of room≤w min ≤ 1m/s air distributions.With this condition, 1 lower part of vaporizer
In Turbulent Fluidization state, the particle carrying amount very little at maximum cross-section so that the waste as raw material is maintained at vaporizer 1
Lower part；First air, that is, gasifying agent supply amount is small simultaneously, but disturbs strong so that the waste gasification in vaporizer 1 is thorough.
Air distribution plate is in tilted layout, and the least significant end of air distribution plate is provided with slagging channel.Residue after gasification reaction is made in blast cap
Collected to slagging channel with lower, and vaporizer 1 is discharged from slagging channel.1 bottom of vaporizer is provided with slag cooler 14 and screening fills
Set 15.Slagging channel is connected to slag cooler 14, is sent into screening plant 15 after the residue after gasifying of discharge is cooled down and is sieved.Screening plant
Waste treatment is discharged in 15 built-in screening wires, the thick slag of oversize, and screenings fine slag can be used as 1 bed material of vaporizer to supplement.Under vaporizer 1
The portion side opposite with slagging channel, which is provided with, mends cinder notch 16 as fine slag material inlet.Since plastics and tire the like waste are most
Ash content is low, is insufficient for the requirement of bed bed material.When necessary, the bed materials such as quartz sand substance also can enter gas by mending cinder notch 16
Change room 1.
To realize that refractory material is laid in low-temperature heat accumulating gasification, 1 internal face of vaporizer.
It is connected by horizontal top flue 4 of crossing between vaporizer 1 and combustion chamber 2.Vaporizer 1 gasify after gaseous product be
The gas that gasifies enters combustion chamber 2 by crossing top flue 4.It crosses in top flue 4 and is provided with burner 6,6 front end of burner is provided with several
A overfiren air port 9 lights gasification gas and is passed through Secondary Air（Oxidant）It is set to start to burn.
As shown in Fig. 2, burner 6 selects heat-accumulation combustor, inside along flue gas flow direction be arranged in parallel with several accumulation of heats
Body 17, heat storage 17 is by refractory material laying, the arc-shaped transition on flue gas flow direction.Several heat storages 17 in the vertical direction will
If crossing top flue 4 is separated into dry flue gas circulation road.Several overfiren air ports 9 setting at this time is in 17 front end of heat storage, and each two
Secondary air port tilts the direction of flow towards flue gas circulation road.So that gasification gas is uniformly mixed with Secondary Air, efficiency of combustion is improved.
The mixed gas of the gaseous mixture and partially combusted flue gas of gasification gas and Secondary Air together enters from top flue 4 is crossed
Combustion chamber 2.2 top of combustion chamber is provided with several tertiary air orifices 10, to gaseous mixture and the further air distribution of partially combusted flue gas
Make its optimization burning.Two opposite sides at 2 top of combustion chamber for crossing top 4 exit of flue are arranged in several tertiary air orifices 10
On face, arranged by being exported in the way of bottom is arranged to 2 top droop of combustion chamber from top flue 4 excessively.So that from cross top flue 4 into
The mixed gas and tertiary air for entering combustion chamber 2 are sufficiently mixed into the mixed gas containing more multi-oxidizer.
2 bottom of combustion chamber is connected to 3 bottom of secondary furnace and forms Zigzag type logistics corridor.Preferably, combustion chamber 2 and after-flame
3 bottom opposite tilt of room, which is formed, turns to separation chamber, turns to separation chamber bottom and ash ejector is arranged.Mixed gas is in 2 downlink of combustion chamber
Further burning in the process, and so that the ash contained in gas grades, impurity is detached during 2 bottom of combustion chamber turns to
Get off, and is discharged from ash ejector.
3 top of secondary furnace is provided with superheater 11, and gas carries out heat while secondary furnace 3 burns complete with superheater 11
It exchanges.3 top of secondary furnace is connected to 5 top of back-end ductwork, by the flue gas after superheater 11 tentatively cooling with setting in tail portion cigarette
Economizer 12 and air preheater 13 in road 5 exchange heat in succession.
It according to circumstances needs, superheater 11 and economizer 12 can be arranged multigroup.
Drum can be arranged in 1 top of vaporizer, be used for steam-water separation.
The foregoing is only a preferred embodiment of the present invention, is not intended to restrict the invention, for the skill of this field
For art personnel, the invention may be variously modified and varied.All within the spirits and principles of the present invention, any made by repair
Change, equivalent replacement, improvement etc., should all be included in the protection scope of the present invention.
Claims (10)
1. a kind of gasified combustion apparatus, it is characterised in that：Described device includes vaporizer（1）, combustion chamber（2）, secondary furnace（3）,
Back-end ductwork（5）And feeding equipment（7）；The vaporizer（1）, combustion chamber（2）, secondary furnace（3）And back-end ductwork（5）Cloth arranged side by side
It sets and is sequentially connected, form Zigzag type logistics corridor；The vaporizer（1）With the combustion chamber（2）Between be equipped with top flue
（4）, described to cross top flue（4）Inside it is provided with burner（6）；The combustion chamber（2）Bottom and the secondary furnace（3）Bottom is connected to
And form Zigzag type logistics corridor；The secondary furnace（3）Top and the back-end ductwork（5）Top is connected to；The charging gear
（7）It is arranged in the vaporizer（1）Front end；The vaporizer（1）Bottom side is provided with slagging channel.
2. a kind of gasified combustion apparatus according to claim 1, it is characterised in that：The vaporizer（1）Bottom is provided with
Air compartment（8）With setting in the air compartment（8）On air distribution plate, the air distribution plate is in tilted layout, and the slagging channel is arranged in cloth
The least significant end of aerofoil.
3. a kind of gasified combustion apparatus according to claim 1 or 2, it is characterised in that：The vaporizer（1）Top be etc.
Cross-sectional area, lower part are variable cross-section area；The vaporizer（1）Lower part variable cross-section area is up followed successively by flaring area and tapered by bottom
Area.
4. a kind of gasified combustion apparatus according to claim 3, it is characterised in that：The air compartment（8）Air distribution is by according to institute
State vaporizer（1）The minimum windspeed 0.5 of lower cross section area maximum≤w min ≤ 1m/s is arranged.
5. a kind of gasified combustion apparatus according to claim 3, it is characterised in that：The vaporizer（1）Internal face is laid
Refractory material.
6. a kind of gasified combustion apparatus according to claim 1, it is characterised in that：Described device further includes slag cooler（14）
And screening plant（15）；The vaporizer（1）The lower part side opposite with slagging channel is provided with benefit cinder notch（16）；The cold slag
Device is connected to the slagging channel and screening plant（15）Between, the screening plant（15）With the benefit cinder notch（16）It is connected.
7. a kind of gasified combustion apparatus according to claim 1, it is characterised in that：The burner（6）Front end is provided with
Several overfiren air ports（9）.
8. a kind of gasified combustion apparatus according to claim 7, it is characterised in that：The burner（6）Select accumulation of heat combustion
Burner, it is interior to be arranged in parallel with several heat storages along flue gas flow direction（17）, top flue is crossed by described（4）If being separated into dry flue gas stream
Channel；Several described overfiren air ports（9）It is arranged in heat storage（17）Front end, and each overfiren air port is tilted towards flue gas stream
The direction of flow in channel.
9. a kind of gasified combustion apparatus according to claim 1, it is characterised in that：The combustion chamber（2）With the after-flame
Room（3）Bottom opposite tilt, which is formed, turns to separation chamber, and ash ejector is arranged in the steering separation chamber bottom；The secondary furnace（3）On
Portion is provided with superheater（11）.
10. a kind of gasified combustion apparatus according to claim 1, it is characterised in that：The combustion chamber（2）Top is provided with
Several tertiary air orifices（10）, several described tertiary air orifices according to from it is described cross top flue（4）Bottom is exported to the burning
Room（2）The mode of top droop arrangement is arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810781284.0A CN108758642A (en) | 2018-07-17 | 2018-07-17 | A kind of gasified combustion apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810781284.0A CN108758642A (en) | 2018-07-17 | 2018-07-17 | A kind of gasified combustion apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108758642A true CN108758642A (en) | 2018-11-06 |
Family
ID=63974053
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810781284.0A Pending CN108758642A (en) | 2018-07-17 | 2018-07-17 | A kind of gasified combustion apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108758642A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112254156A (en) * | 2020-11-05 | 2021-01-22 | 北京一亚高科能源科技有限公司 | Sludge TFB gasification incinerator |
| CN112254143A (en) * | 2020-11-05 | 2021-01-22 | 北京一亚高科能源科技有限公司 | TFB gasification incinerator |
| CN112254137A (en) * | 2020-11-05 | 2021-01-22 | 北京一亚高科能源科技有限公司 | TFB gasification incinerator with drying bed |
| CN112358155A (en) * | 2020-11-05 | 2021-02-12 | 北京一亚高科能源科技有限公司 | Sludge drying, gasifying and incinerating system and method thereof |
| CN115342354A (en) * | 2022-09-06 | 2022-11-15 | 西安热工研究院有限公司 | Burner with a burner head |
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| CN203336581U (en) * | 2013-06-17 | 2013-12-11 | 山西天兰锅炉有限公司 | Smokeless combustor |
| CN104998888A (en) * | 2015-06-30 | 2015-10-28 | 航天神洁（北京）环保科技有限公司 | Medical waste plasma processing apparatus |
| CN107795981A (en) * | 2017-11-27 | 2018-03-13 | 清华大学 | the gasification combustion system of complex mixed fuel |
| CN208620355U (en) * | 2018-07-17 | 2019-03-19 | 北京一亚高科能源科技有限公司 | A kind of gasified combustion apparatus |
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2018
- 2018-07-17 CN CN201810781284.0A patent/CN108758642A/en active Pending
Patent Citations (4)
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|---|---|---|---|---|
| CN203336581U (en) * | 2013-06-17 | 2013-12-11 | 山西天兰锅炉有限公司 | Smokeless combustor |
| CN104998888A (en) * | 2015-06-30 | 2015-10-28 | 航天神洁（北京）环保科技有限公司 | Medical waste plasma processing apparatus |
| CN107795981A (en) * | 2017-11-27 | 2018-03-13 | 清华大学 | the gasification combustion system of complex mixed fuel |
| CN208620355U (en) * | 2018-07-17 | 2019-03-19 | 北京一亚高科能源科技有限公司 | A kind of gasified combustion apparatus |
Cited By (5)
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| CN112254156A (en) * | 2020-11-05 | 2021-01-22 | 北京一亚高科能源科技有限公司 | Sludge TFB gasification incinerator |
| CN112254143A (en) * | 2020-11-05 | 2021-01-22 | 北京一亚高科能源科技有限公司 | TFB gasification incinerator |
| CN112254137A (en) * | 2020-11-05 | 2021-01-22 | 北京一亚高科能源科技有限公司 | TFB gasification incinerator with drying bed |
| CN112358155A (en) * | 2020-11-05 | 2021-02-12 | 北京一亚高科能源科技有限公司 | Sludge drying, gasifying and incinerating system and method thereof |
| CN115342354A (en) * | 2022-09-06 | 2022-11-15 | 西安热工研究院有限公司 | Burner with a burner head |
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