CN107355791A - A kind of waste high temperature pyrolysis furnace - Google Patents
A kind of waste high temperature pyrolysis furnace Download PDFInfo
- Publication number
- CN107355791A CN107355791A CN201710555712.3A CN201710555712A CN107355791A CN 107355791 A CN107355791 A CN 107355791A CN 201710555712 A CN201710555712 A CN 201710555712A CN 107355791 A CN107355791 A CN 107355791A
- Authority
- CN
- China
- Prior art keywords
- dual firing
- firing chamber
- high temperature
- flue gas
- 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.)
- Withdrawn
Links
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
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/303—Burning pyrogases
-
- 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
- F23G2202/103—Combustion in two or more stages in separate chambers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2900/00—Special features of, or arrangements for incinerators
- F23G2900/50204—Waste pre-treatment by pyrolysis, gasification or cracking
Abstract
The invention discloses a kind of waste high temperature pyrolysis furnace, including with lower component:At least one cracking furnace body, for burning waste;Dual firing chamber is vortexed, for absorbing the flue gas after burning, rotation and second-time burning in eddy current pipeline;Exhaust gas cleaner, for by the gas cleaning after second-time burning;Blast pipe, for will be discharged by the flue gas of purification;The cracking furnace body, vortex dual firing chamber, exhaust gas cleaner, blast pipe are sequentially communicated.In the present invention, discarded object can burn in pyrolysis furnace, the flue gas of burning is transported to vortex dual firing chamber, flue gas rotational flow in dual firing chamber is vortexed, it is simultaneously combustion-supporting, fuel gas in flue gas is by second-time burning, so smoke combustion is abundant, the sufficient flue gas that burns is transported to purify in exhaust gas cleaner and discharged again by blast pipe later.The present invention can improve efficiency of combustion, the noxious material of burning fully, in reduction flue gas.
Description
Technical field
The present invention relates to incinerator technical field, more specifically, more particularly to a kind of waste high temperature pyrolysis furnace.
Background technology
The rubbish such as existing discarded object and biomass has the following disadvantages when burning:1st, incineration firing is insufficient, easily
Produce toxic gas, it is impossible to reach discharge standard, greatly compromise environment;2nd, using artificial feed, rubbish need be established and unloaded
Expect plateau increase civil engineering expense, while be fed inconvenience;3rd, material is sent into uneven in stove, influences efficiency of combustion.Therefore,
It is necessary to design a kind of incinerator of the rubbish such as new discarded object and biomass.
The content of the invention
It is an object of the invention to provide a kind of nuisance of simple in construction, burning fully and in effective filtering flue gas
Matter, discharge the waste high temperature pyrolysis furnace of clean gas.
In order to achieve the above object, the technical solution adopted by the present invention is as follows:
A kind of waste high temperature pyrolysis furnace, including with lower component:
At least one cracking furnace body, for burning waste;
Dual firing chamber is vortexed, for absorbing the flue gas after burning, rotation and second-time burning in eddy current pipeline;
Exhaust gas cleaner, for by the gas cleaning after second-time burning;
Blast pipe, for will be discharged by the flue gas of purification;
The cracking furnace body, vortex dual firing chamber, exhaust gas cleaner, blast pipe are sequentially communicated.
Further, each cracking furnace body includes main furnace shell, and being provided with inclination in the main furnace shell sets
Fire grate component is put, there is first end and the second end on the fire grate component, the first end is higher than the second end, the fire grate component
Main furnace shell intracoelomic cavity is divided into main chamber and ash discharge chamber, being also communicated with inclination in the main chamber of the first end side sets
The feeder channel put, and slag-drip opening and ash discharging hole are further opened with the main furnace shell, the slag-drip opening is arranged on fire grate component
Second end upper surface location, and connected with main chamber, the ash discharging hole is arranged on the second end of fire grate component lower surface position, and
Connected with ash discharge chamber, the main chamber top is also connected by smoke exhaust pipe with vortex dual firing chamber.
Further, the inclination angle of the fire grate component is 30 ° to 60 °, and the inclination angle of the feeder channel is 70 ° to 80 °.
Further, an ash discharge deslagging arched door, the slag-drip opening, ash discharge are also associated with outside each main furnace shell
Mouth is opened in the ash discharge deslagging arched door.
Further, the feeder channel upper end has inlet, and the inlet opening position is hinged with feed slot device.
Further, being set up above each cracking furnace body has portal frame, and driving is provided with the portal frame
It is fed the chain block of slot device upset.
Further, the side of the cracking furnace body is additionally provided with feeding platform, and the feed slot device is seated in institute
State on feeding platform.
Further, the vortex dual firing chamber includes combustion chamber cylinder, eddy current separators, burner, the combustion chamber cylinder
In staggeredly be provided with multiple eddy current separators, the burner is arranged on one end of vortex dual firing chamber, and stretches to the vortex
In dual firing chamber, the gas outlet for being vortexed dual firing chamber is arranged on the other end of vortex dual firing chamber, and the air inlet for being vortexed dual firing chamber is arranged on
In the vortex dual firing chamber side wall of burner side, multiple ash discharge slag-drip openings are also communicated with below the vortex dual firing chamber.
Further, the exhaust gas cleaner includes centrifugal separator, and spraying dress is provided with the centrifugal separator
Put.
Further, the exhaust gas cleaner also includes water-cooled wall apparatus, for the flue gas after cooling and purifying.
By setting at least one cracking furnace body, discarded object can be burnt in pyrolysis furnace, and the flue gas of burning is conveyed
To vortex dual firing chamber, flue gas rotational flow in dual firing chamber is vortexed, while combustion-supporting, the fuel gas in flue gas is by secondary combustion
Burn, so smoke combustion is abundant, the sufficient flue gas that burns is transported to purify in exhaust gas cleaner passes through blast pipe again later
Discharge.
Compared with prior art, the advantage of the invention is that:The present invention can improve efficiency of combustion, and burning is abundant, reduces cigarette
Noxious material in gas.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
There is the required accompanying drawing used in technology description to be briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, can be with
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is the structural representation of waste high temperature pyrolysis furnace of the present invention.
Fig. 2 is the right view of waste high temperature pyrolysis furnace of the present invention;
Fig. 3 is the top view of waste high temperature pyrolysis furnace of the present invention.
Embodiment
The preferred embodiments of the present invention are described in detail below in conjunction with the accompanying drawings, so that advantages and features of the invention energy
It is easier to be readily appreciated by one skilled in the art, apparent is clearly defined so as to be made to protection scope of the present invention.
Refering to shown in Fig. 1 to Fig. 3, the present embodiment provides a kind of waste high temperature pyrolysis furnace, including with lower component:
At least one cracking furnace body 1, for burning waste;Furnace body 1 is cracked in the present embodiment and is provided with two, two
Individual cracking furnace body is arranged side by side, and internal interconnected.
Dual firing chamber 2 is vortexed, for absorbing the flue gas after burning, rotation and second-time burning in eddy current pipeline;In vortex two
Combustion can be passed through air or oxygen in room 2, can further improve efficiency of combustion, can also install and help in the vortex dual firing chamber 2
Burner 5, it is that flue gas is combustion-supporting that combustion-supporting, which is used for convenient,.
Exhaust gas cleaner 3, for by the gas cleaning after second-time burning;The exhaust gas cleaner 3 can be filter-type
Cleaning system or spraying purification system.
Blast pipe 4, for will be discharged by the flue gas of purification;
The cracking furnace body 1, vortex dual firing chamber 2, exhaust gas cleaner 3, blast pipe 4 are sequentially communicated.
By setting at least one cracking furnace body 1, discarded object can be burnt in pyrolysis furnace, and the flue gas of burning is conveyed
To vortex dual firing chamber 2, flue gas rotational flow in dual firing chamber 2 is vortexed, while combustion-supporting, the fuel gas in flue gas is by secondary combustion
Burn, so smoke combustion is abundant, the sufficient flue gas that burns is transported to purify in exhaust gas cleaner 3 passes through blast pipe again later
4 discharges, the present invention can improve efficiency of combustion, the noxious material of burning fully, in reduction flue gas.
In the present embodiment, each cracking furnace body 1 includes main furnace shell 11, is installed in the main furnace shell 11
Fire grate component 12 is obliquely installed, there is the end 122 of first end 121 and second on the fire grate component 12, the first end 121 is high
In the second end 122, the main inner chamber of furnace shell 11 is divided into main chamber 101 and ash discharge chamber 102 by the fire grate component 12, and described
The feeder channel 13 being obliquely installed also is communicated with the main chamber 101 of the side of one end 121, and is also opened on the main furnace shell 11
Provided with slag-drip opening 14 and ash discharging hole 15, the slag-drip opening 14 is arranged on the upper surface location of the second end 122 of fire grate component 12, and with
Main chamber 101 connects, and the ash discharging hole 15 is arranged on the lower surface position of the second end 122 of fire grate component 12, and and ash discharge chamber
102 connections, the top of main chamber 101 are also connected by smoke exhaust pipe 16 with vortex dual firing chamber 2.Discarded object and rubbish are from feed
Passage 13 is fitted into main chamber 101, and the rubbish of bottom burns into main chamber 101, and the rubbish in middle level is by high temperature fumigation,
Steam is mingled with flue gas and enters vortex dual firing chamber 2 by smoke exhaust pipe 16, and the middle level rubbish after fumigating is fallen into main chamber 101
Burn later and conveniently, and the rubbish on upper strata has the function that to block inlet 131, prevents flue gas from being discharged from feeder channel 13.
Cracking furnace body 1 can also set one or more in the waste high temperature pyrolysis furnace of the present invention, be arranged side by side
The high-temperature cracking furnace of a variety of different tonnages can be manufactured, the pyrolysis furnace suitable for handling different tonnage rubbish daily.
Preferably, the inclination angle of the fire grate component 12 is 30 ° to 60 °, and easily accumulation forms bottom rubbish, middle level rubbish to rubbish
Rubbish and upper strata rubbish, and sanitary fill is not will not fall into before smoke-dried beancurd into the combustion chamber 103 in main chamber 101;
The inclination angle of the feeder channel 13 is 70 ° to 80 °, after the discarded object or incineration firing in combustion chamber 103, less ash and
Grain enters ash discharge chamber 102 through fire grate component 12, and the larger metal that can not be burnt, stone etc. are tumbled to the second end 122
Slag-drip opening 14.
Preferably, it is also associated with an ash discharge deslagging arched door 17 outside each main furnace shell 11, the slag-drip opening 14,
Ash discharging hole 15 is opened in the ash discharge deslagging arched door 17.The ash discharge deslagging arched door 17 can stop slag-drip opening 14 and ash discharging hole
15, it is attractive in appearance, and can be slag and the grey windproof grey and slag easily cleaning kept off the rain, dried, do not pollute the environment yet.
Discarded object or rubbish are added into feeder channel 13 in order to convenient, the upper end of feeder channel 13 has feed
Mouth 131, the opening position of inlet 131 are hinged with feed slot device 6.Each top of cracking furnace body 1, which is set up, dragon
Door frame 7, the chain block 8 that driving feed slot device 6 is overturn is installed on the portal frame 7.The side of the cracking furnace body 1
Feeding platform 9 is additionally provided with, the feed slot device 6 is seated on the feeding platform 9.When in use, garbage truck can be straight
Feeding platform 9 is connect out, then garbage truck is filled by rubbish self-unloading to being fed on slot device 6 by chain block 8 or electronic lifting
Put, the rubbish being fed in slot device 6 is poured in feeder channel 13.The rubbish of the bottom of feeder channel 13 after combustion slowly under
It is heavy.
In the present embodiment, the vortex dual firing chamber 2 includes combustion chamber cylinder 21, eddy current separators 22, burner 5, described
What is interlocked in combustion chamber cylinder 21 is provided with multiple eddy current separators 22, and the burner 5 is arranged on one end of vortex dual firing chamber 2,
And stretch in the vortex dual firing chamber 2, the gas outlet 23 of vortex dual firing chamber 2 is arranged on the other end of vortex dual firing chamber 2, vortex
The air inlet 24 of dual firing chamber 2 is arranged in the side wall of vortex dual firing chamber 2 of the side of burner 5, and the lower section of vortex dual firing chamber 2 also connects
It is connected with multiple ash discharge slag-drip openings 25.Flue gas can be burned device 5 later into vortex dual firing chamber 2 and light, the gas to be burnt incompletely in flue gas
Body burns away, and is vortexed in dual firing chamber 2 that can also to be passed through air or oxygen combustion-supporting, improves efficiency of combustion, makes smoke combustion
Fully, toxic gas is reduced.In rotational flow in being vortexed dual firing chamber 2, part cigarette ash can settle flue gas, and ash discharge slag-drip opening 25
It is to be used for periodically to vortex dual firing chamber 2 ash discharge deslagging.
The exhaust gas cleaner 3 includes centrifugal separator 31, and sprayer unit 32 is provided with the centrifugal separator 31.
Water smoke can absorb the impurity in flue gas, and the water smoke for absorbing impurity is centrifuged flue gas clean after machine 31 centrifuges
It can discharge, and absorb the water smoke of impurity by centrifugal classification, final drying discharge lime-ash.Preferably, the exhaust gas cleaner 3
Also include water-cooled wall apparatus 33, for the flue gas after cooling and purifying.Due to the flue-gas temperature by centrifugal separator 31 still compared with
Height, and the water droplet for wherein also having part to vaporize is suspended in flue gas with dust impurity, and this partial fume is passing through water cooling
Heat exchange after wall device 33, water droplet cooling condenses, with the ash fall in flue gas.So water-cooled wall apparatus 33 is set on the one hand
On the other hand in flue gas water droplet and impurity can further be removed with cooled flue gas, improve tail gas clean-up efficiency.
Although being described in conjunction with the accompanying embodiments of the present invention, patent owner can be in appended claims
Within the scope of make various deformations or amendments, as long as no more than the present invention claim described by protection domain, all should
Within protection scope of the present invention.
Claims (10)
- A kind of 1. waste high temperature pyrolysis furnace, it is characterised in that:Including with lower component:At least one cracking furnace body, for burning waste;Dual firing chamber is vortexed, for absorbing the flue gas after burning, rotation and second-time burning in eddy current pipeline;Exhaust gas cleaner, for by the gas cleaning after second-time burning;Blast pipe, for will be discharged by the flue gas of purification;The cracking furnace body, vortex dual firing chamber, exhaust gas cleaner, blast pipe are sequentially communicated.
- 2. waste high temperature pyrolysis furnace according to claim 1, it is characterised in that:Each cracking furnace body includes Main furnace shell, it is provided with the main furnace shell and is obliquely installed fire grate component, there is first end and second on the fire grate component End, the first end are higher than the second end, and main furnace shell intracoelomic cavity is divided into main chamber and ash discharge chamber by the fire grate component, described The feeder channel being obliquely installed also is communicated with the main chamber of first end side, and deslagging is further opened with the main furnace shell Mouth and ash discharging hole, the slag-drip opening is arranged on the second end of fire grate component upper surface location, and is connected with main chamber, the ash discharge Mouth is arranged on the second end of fire grate component lower surface position, and is connected with ash discharge chamber, and the main chamber top also passes through smoke exhaust pipe Dual firing chamber connects with vortex.
- 3. waste high temperature pyrolysis furnace according to claim 2, it is characterised in that:The inclination angle of the fire grate component is 30 ° To 60 °, the inclination angle of the feeder channel is 70 ° to 80 °.
- 4. waste high temperature pyrolysis furnace according to claim 2, it is characterised in that:Also connect outside each main furnace shell An ash discharge deslagging arched door is connected to, the slag-drip opening, ash discharging hole are opened in the ash discharge deslagging arched door.
- 5. waste high temperature pyrolysis furnace according to claim 2, it is characterised in that:The feeder channel upper end has feed Mouthful, the inlet opening position is hinged with feed slot device.
- 6. waste high temperature pyrolysis furnace according to claim 4, it is characterised in that:Above each cracking furnace body Erection has portal frame, and the chain block of driving feed slot device upset is provided with the portal frame.
- 7. waste high temperature pyrolysis furnace according to claim 5, it is characterised in that:The side of the cracking furnace body is also set Feeding platform is equipped with, the feed slot device is seated on the feeding platform.
- 8. waste high temperature pyrolysis furnace according to claim 1, it is characterised in that:The vortex dual firing chamber includes combustion chamber Cylinder, eddy current separators, burner, in the combustion chamber cylinder staggeredly be provided with multiple eddy current separators, the burner installation In one end of vortex dual firing chamber, and stretch in the vortex dual firing chamber, the gas outlet for being vortexed dual firing chamber is arranged on the combustion of vortex two The other end of room, the air inlet for being vortexed dual firing chamber are arranged in the vortex dual firing chamber side wall of burner side, the combustion of vortex two Multiple ash discharge slag-drip openings are also communicated with below room.
- 9. waste high temperature pyrolysis furnace according to claim 1, it is characterised in that:The exhaust gas cleaner includes centrifugation Seperator, sprayer unit is installed in the centrifugal separator.
- 10. waste high temperature pyrolysis furnace according to claim 9, it is characterised in that:The exhaust gas cleaner also includes Water-cooled wall apparatus, for the flue gas after cooling and purifying.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710555712.3A CN107355791A (en) | 2017-07-10 | 2017-07-10 | A kind of waste high temperature pyrolysis furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710555712.3A CN107355791A (en) | 2017-07-10 | 2017-07-10 | A kind of waste high temperature pyrolysis furnace |
Publications (1)
Publication Number | Publication Date |
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CN107355791A true CN107355791A (en) | 2017-11-17 |
Family
ID=60292698
Family Applications (1)
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CN201710555712.3A Withdrawn CN107355791A (en) | 2017-07-10 | 2017-07-10 | A kind of waste high temperature pyrolysis furnace |
Country Status (1)
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CN (1) | CN107355791A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109114542A (en) * | 2018-09-06 | 2019-01-01 | 黑龙江赫尔特生物质能源发展有限公司 | It is particularly suitable for the gasification installation of the self-feeding, entire bundle burning of plant haulm etc. |
CN110743319A (en) * | 2019-12-23 | 2020-02-04 | 佛山市骏鹰环境能源装备有限公司 | Container modular organic gas or flue gas tail gas treatment device |
-
2017
- 2017-07-10 CN CN201710555712.3A patent/CN107355791A/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109114542A (en) * | 2018-09-06 | 2019-01-01 | 黑龙江赫尔特生物质能源发展有限公司 | It is particularly suitable for the gasification installation of the self-feeding, entire bundle burning of plant haulm etc. |
CN110743319A (en) * | 2019-12-23 | 2020-02-04 | 佛山市骏鹰环境能源装备有限公司 | Container modular organic gas or flue gas tail gas treatment device |
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WW01 | Invention patent application withdrawn after publication |
Application publication date: 20171117 |
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WW01 | Invention patent application withdrawn after publication |