CN207797062U - A kind of organic solid castoff pyrogenation incinerator and its system - Google Patents
A kind of organic solid castoff pyrogenation incinerator and its system Download PDFInfo
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- CN207797062U CN207797062U CN201721921309.XU CN201721921309U CN207797062U CN 207797062 U CN207797062 U CN 207797062U CN 201721921309 U CN201721921309 U CN 201721921309U CN 207797062 U CN207797062 U CN 207797062U
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Abstract
A kind of organic solid castoff pyrogenation incinerator and its system, pyrogenation incinerator include furnace body, and casing is equipped with outside the furnace body；The furnace body includes left furnace body, right furnace body；Feed inlet is equipped at the top of the left furnace body, the left furnace body is additionally provided with supplemental fuel inlet, and high-temperature hot-air import is arranged in bottom；The right furnace body is equipped with exhanst gas outlet, and bottom is equipped with air intlet；The right bottom of furnace body is equipped with discharging mechanism.The system of the organic solid castoff pyrolytic incineration, including：Pretreatment system, quality coal in cement kiln systems, incinerator, storage device, siege is fixed by using pyrogenation incinerator and discharging technology is forced to be combined, in conjunction with high temperature pyrolysis and incineration technology, recycling, energy, the low cost that house refuse and organic solid castoff may be implemented are disposed.The utility model simple structure, reliable for operation, heat recovery rate is high, and adaptability range is wide.
Description
Technical field
The utility model is related to thermal technology's environmental technology fields, and in particular to a kind of organic solid castoff pyrogenation incinerator and
Its system.
Background technology
The works such as house refuse, garbage flying ash, various sludge, waste plastics, spent resin, scrap rubber, human and animal excreta, medical waste
The organic solid castoff with certain energy including agricultural wastes contains danger wastes to environment there are serious harm, adopts
It can make the thorough decomposition combustion of organic matter therein with the method that high temperature pyrolysis burns, eliminate toxicity, obtain its energy, burn out
Residue is less afterwards, and residue chemical property stablize, can be used as construction material and organic waste it is innoxious,
The optimal path of disposal of resources.
There are many solid waste pyrolysis plant type at present, there is the various types such as fixed bed, rotary kiln, fluid bed, double tower cycle
The pyrolysis oven of formula, vitreous clinker, blocking, cause unloading difficulties during generally existing in use is burned, and heat recovery efficiency is low, disposition
Not exclusively, the problems such as high equipment cost, equipment fault is high.
CN201748440U discloses a kind of vertical burning rotary grate slag discharging device, and incinerator is supported by holder
Main body, the lower part setting plate column for burning furnace main body are combed, and the lower part that plate column is combed connects residue outlet, and discharging transmission device passes through biography
Dynamic column connection plate column is combed, and air loop duct, Roche wind turbine and ring are installed on the burning furnace main body at setting plate column comb position
Shape air hose connects, and air inlet fan is mounted on residue outlet upper end.The patent only discloses deslagging device, is slagged tap crusher using abnormity
Structure has certain limitation to handle house refuse.
CN104534475B discloses a kind of processing house refuse comb grate formula incinerator and treatment process, including furnace body and
Deduster has air inducing pipeline, feeding equipment, exhaust duct and device for discharging, air inducing pipeline to be connect with hot air source in furnace body, furnace body
Top is equipped with feeding equipment, and wheel of combing is equipped with below feeding equipment, and lower part is equipped with grate bed in furnace body；Grate bed lower part is separated into multiple fill
Gas chamber, each plenum chamber is interior to be equipped with wind turbine, and the furnace body in grate tailstock portion is cooling bay, and cooling bay bottom is equipped with same grate plate, the grate
The plenum chamber of plate lower part is connect with air-cooler, and grate is taken in and is provided with pusher, is mostly fixed on lower portion with stick pusher.It should
Patent is carried out by incinerator and cement kiln synergic processing domestic waste after carrying out break process to rubbish by comb tooth again
It burns, but the problem of unresolved material burning vitreous clinker, blocking.
Utility model content
In view of the deficiencies of the prior art, the utility model provides a kind of organic solid castoff pyrogenation incinerator and its is
System using fixed siege and forces discharging technology to be combined, in conjunction with high temperature pyrolysis and incineration technology, may be implemented house refuse and
The recycling of organic solid castoff, energy, low cost disposition, the simple in equipment is reliable for operation, and heat recovery rate is high,
Adaptability range is wide.
The technical issues of to solve the utility model, the technical solution taken are as follows：
On the one hand, the utility model provides a kind of organic solid castoff pyrogenation incinerator, including furnace body, the stove sheet
Casing is equipped with outside body；The furnace body includes left furnace body, right furnace body；
Feed inlet is equipped at the top of the left furnace body, high-temperature hot-air import is arranged in bottom, and the left furnace body is additionally provided with auxiliary combustion
Expect import；The right furnace body is equipped with exhanst gas outlet, and bottom is equipped with air intlet；
The right bottom of furnace body is equipped with discharging mechanism, and the discharging mechanism includes rotatable tower fire grate, is driven and stands
Axis, aggregate bin, tremie pipe, driving mechanism, the tower fire grate and driving mechanism are connected by being driven vertical shaft, the aggregate bin
Upper end is connected with casing, and aggregate bin lower end is connected with tremie pipe；
The discharging mechanism further includes wear-resisting annular steel lining, and the wear-resisting annular steel substrate portion is connected with aggregate bin.
Preferably, the driving mechanism includes speed reducer and motor, and the driving mechanism is directly installed on concrete branch
On seat.
Further, the left furnace body is separated with right furnace body by partition wall, the partition wall be equipped with deflector, pyrolysis smoke from every
Deflector is sent into right furnace body in the middle part of wall, so that right furnace body air themperature is increased, is conducive to the utilization of flue gas.
Further, the high-temperature hot-air entrance is equipped with stationary furnace double-edged fine-toothed comb, the stationary furnace double-edged fine-toothed comb by bar steel plate or
Steel-casting forms.
Further, the exhanst gas outlet is equipped with pressure monitor, temperature monitor, flow with high-temperature hot-air import and supervises
Instrument is surveyed, the pressure monitor, temperature monitor, flow monitoring instrument are connected with the computer control system of peripheral hardware, provide respectively
Each data transmission to computer control system is implemented simulation control by running in due course online monitoring data by transmitter,
Automatic governing air quantity, inlet amount and discharge rate realize automation mechanized operation.
Further, ash temperature monitor, the meter of the ash temperature monitor and peripheral hardware are set in the tremie pipe
Calculation machine control system is connected, and realizes automation mechanized operation.
On the other hand, the utility model also provides a kind of organic using the progress of above-mentioned organic solid castoff pyrogenation incinerator
The system of solid waste pyrolytic incineration, including：Pretreatment system, quality coal in cement kiln systems, incinerator, storage device, it is described to burn
It burns device to connect with storage device, the pretreatment system, incinerator, storage device pass through pipeline and quality coal in cement kiln systems respectively
Connection；
The incinerator includes above-mentioned pyrogenation incinerator, further includes air blower, suction machine one, board-like discharging machine, described
Suction machine one is connected with the exhanst gas outlet of pyrogenation incinerator, and the air blower is connected with the air intlet of pyrogenation incinerator, institute
Board-like discharging machine is stated with the discharging mechanism of pyrogenation incinerator to be connected.
Further, the pretreatment system includes sequentially connected solid waste repository, board-like metering feeding machine one, rubbish
Crusher, belt conveyer, current stabilization feeding bin；
The solid waste repository is closed structure, and side is equipped with automatic disengaging hermatic door, and top is equipped with forced ventilation mouth, institute
It states forced ventilation mouth and is equipped with suction machine two；It is additionally provided with storage bin in the solid waste repository；Suction machine two passes through pipeline and deodorization
Device is connected, and solid waste repository forces air draft by suction machine two, and the wind of discharge is sent into deodoriser and eliminates foreign odor smell heel row
It puts, or is sent directly into incinerator high-temperature oxydation deodorization；
The discharge port of the storage bin is connected with the feed inlet of board-like metering feeding machine one, the board-like metering feeding machine one
Discharge port be connected with the feed inlet of refuse grinder, the discharge port of the refuse grinder is fed by belt conveyer and current stabilization
The feed inlet of feed bin connects；
Preferably, the refuse grinder is double-roll crusher, by refuse breaking or is shredded into particle less than 15cm again
It is sent directly into current stabilization feeding bin by belt conveyor；
Suction machine three, discharge port and the pyrogenation incinerator of the current stabilization feeding bin are equipped at the top of the current stabilization feeding bin
Feed inlet be connected.
Further, the high-temperature hot-air import that the suction machine two and suction machine three pass through pipeline and the pyrogenation incinerator
It is connected, the exhaust gas of suction is all participated in as cold wind, realizes the harmless treatment of concentration.
Further, the quality coal in cement kiln systems includes cement kiln waste-heat power generation system, cement kiln flue gas processing system；
The cement kiln waste-heat power generation system is connected with the high-temperature hot-air import of above-mentioned pyrogenation incinerator；
The cement kiln flue gas processing system is connected with the suction machine one, the pyrolysis gas after organic solid castoff burning
Body is discharged by exhanst gas outlet using suction machine one, and the gas of discharge enters cement kiln flue gas processing system and thoroughly burns, and is burned
Heat afterwards is used for cement kiln calcining, and pyrolysis gas thoroughly eliminates toxicity under cement kiln high-temperature strong basicity environment, and at unification
Reason discharge.
Further, the storage device includes roto-siofter, collecting bin, board-like metering feeding machine two, recycling metal storage
Library；
The roto-siofter is arranged at the top of collecting bin, the discharging that the roto-siofter passes through elevator and the board-like discharging machine
Mouth is connected；The roto-siofter is also connected by pipeline with recycling metal repository；
The discharge port of the collecting bin bottom is connected with the feed inlet of board-like metering feeding machine two, the board-like metering feeding
The discharge port of machine two is connect by pipeline with cement kiln flue gas processing system.
The operation principle of the utility model：
Organic solid castoff after pretreatment system enter pyrogenation incinerator, material due to gravity effect on to
Lower movement, high-temperature hot-air preheating, the drying entered from pyrolytic incineration furnace bottom, organic matter decomposes and part is burnt；Pyrolysis is burnt
It burns stove air import with air blower to be connected, the ashes after pyrolysis lead into right furnace chamber by fixed grate and further burned
Entirely, continue to burn the oxygen needed by the feeding fresh air offer of bottom blast machine；Ashes after burning enter cold with bottom
Air directly carries out heat exchange and is cooled, and possible bulk material is squeezed and crushed by the pagoda type grate grinding of discharging mechanism,
Pyrogenation incinerator is uniformly drawn off by board-like discharging machine.The boosted machine of ashes drawn off is sent to roto-siofter and is sieved, ashes sieve
Fine powder after point falls into storage coarse powder in the feed bin being connected with roto-siofter and enters metal recovery system recycling metal, the fine powder sifted out
The tail smoke-box for being sent directly into cement kiln flue gas processing system is handled as cement raw material by cement kiln collaboration.
The beneficial effects of the utility model are as follows：
1, the utility model burns gasification, gasification by will be directly entered pyrogenation incinerator after organic solid waste crushing
Pyrolysis gas and ashes, that is, all waste gases waste material are all sent into cement kiln and carry out carrying out water in high temperature strong basicity environment afterwards
Stall collaboration is handled, and heat recovery efficiency improves；Useful metal can be recycled simply from the ashes, simple and reliable process,
There is no secondary pollution risk, it is ensured that the innoxious, inexpensive of house refuse, Low investment processing meet sustainable development cycle warp
The direction of Ji.
2, the utility model can handle house refuse, garbage flying ash, various sludge, waste plastics, spent resin, scrap rubber,
Including the industrial and agricultural wastes such as human and animal excreta, medical waste with certain energy etc. all kinds of organic solid castoffs or dangerous useless
Gurry, it is applied widely.The utility model is simple for process, reliable, and using existing quality coal in cement kiln systems, operating cost is low, has
Sustainability.
3, organic solid castoff moves from top to bottom in the left furnace body of pyrogenation incinerator, and hot wind moves from bottom to top, heat
Wind realizes heat exchange with material, and heat transfer efficiency is high, and solid flying dust is few, completes material from preheating, drying and pyrolysis, obtains clean
Fuel gas；Ashes are automatically fallen into right furnace body after pyrolysis, it is understood that there may be melting bulk be rotated the grinding of tower fire grate,
It squeezes and fragmentation, furnace body will not be blocked, can continuously long-term safety run, right lower portion of furnace body, which enters air, can recycle ashes
Waste heat makes ashes cool down, and oxygen can be replenished in time in the air newly increased, and the lime-ash for not having burning in ashes is promoted to continue to complete
Burning is thoroughly burned.
4, automation control may be implemented in the utility model, it is ensured that wind, material, gas three balance.
5, during the utility model processing solid waste, by pyrolytic incineration and quality coal in cement kiln systems, high temperature is burnt twice
It burns, is conducive to the decomposition combustion of solid waste, be conducive to the firing of clinker, effectively eliminate having for solid waste incineration generation
Evil gas, such as：Bioxin completely eliminates the risk of secondary pollution, realizes environment and production safety.
Description of the drawings
It, below will be to required use in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment
Attached drawing be briefly described, it should be apparent that, the accompanying drawings in the following description is only some embodiments of the utility model, right
For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings
His attached drawing.
Fig. 1：Organic solid castoff pyrogenation incinerator schematic diagram in embodiment 1；
Fig. 2：Organic solid castoff pyrogenation incinerator discharging mechanism schematic diagram；
Fig. 3：D-D section structure diagrams in embodiment 1；
Fig. 4：The system of organic solid castoff pyrolytic incineration；
Fig. 5：Organic solid castoff pyrogenation incinerator schematic diagram in embodiment 2.
Specific implementation mode
Below in conjunction with specific embodiment of the utility model, the technical solution in the present embodiment is carried out clear, complete
Ground describes, it is clear that described embodiment is only a part of the embodiment of the utility model, instead of all the embodiments.Base
In the embodiments of the present invention, institute that those of ordinary skill in the art are obtained without creative efforts
There is other embodiment, shall fall within the protection scope of the present invention.
In addition, the technical solution between each embodiment of the utility model can be combined with each other, but must be with ability
Domain those of ordinary skill can be implemented as basis, will be understood that when the combination of technical solution appearance is conflicting or cannot achieve
The combination of this technical solution is not present, also not within the protection domain of the requires of the utility model.
Embodiment 1
As shown in Figs. 1-3, described the present embodiment provides a kind of organic solid castoff pyrogenation incinerator, including furnace body
Casing 609 is equipped with outside furnace body；The furnace body includes left furnace body, right furnace body,
Feed inlet 601 is equipped at the top of the left furnace body, high-temperature hot-air import 603 is arranged in bottom；The right furnace body is equipped with cigarette
Gas outlet 605, bottom is equipped with air intlet 604；
The right bottom of furnace body is equipped with discharging mechanism 608, and the discharging mechanism 608 includes rotatable tower fire grate
6081, vertical shaft 6083, aggregate bin 6085, tremie pipe 6086, driving mechanism 6084, the tower fire grate 6081 and driving are driven
Mechanism 6084 by be driven vertical shaft 6083 be connected, 6085 upper end of the aggregate bin is connected with casing 609,6085 lower end of aggregate bin and
Tremie pipe 6086 is connected；
The discharging mechanism 608 further includes wear-resisting annular steel lining 6082, wear-resisting annular 6082 bottom of steel lining with gather materials
Bucket 6085 is connected.
Preferably, the driving mechanism 6084 includes speed reducer and motor, and the driving mechanism 6084 is directly installed on
In concrete bearing.
The left furnace body is separated with right furnace body by partition wall 607, the partition wall 607 be equipped with deflector 602, pyrolysis smoke from every
607 middle part deflector 602 of wall is sent into right furnace body, so that right furnace body air themperature is increased, is conducive to the utilization of flue gas.
Preferably, stationary furnace double-edged fine-toothed comb 606 is equipped at the high-temperature hot-air import 603, the stationary furnace double-edged fine-toothed comb 606 is by bar shaped
Steel plate forms, and bar steel plate is obliquely installed.
The exhanst gas outlet 605 is equipped with pressure monitor, temperature monitor, flow monitoring with high-temperature hot-air import 603
Instrument, the pressure monitor, temperature monitor, flow monitoring instrument are connected with the computer control system of peripheral hardware respectively, provide fortune
Each data transmission to computer control system is implemented simulation control by the in due course online monitoring data in row by transmitter, from
Dynamic allotment air quantity, inlet amount and discharge rate, realize automation mechanized operation.
Ash temperature monitor, the computer control of the ash temperature monitor and peripheral hardware are set in the tremie pipe 6086
System processed is connected, and realizes automation mechanized operation.
Had as shown in figure 4, the utility model also provides a kind of above-mentioned organic solid castoff pyrogenation incinerator of use
The system of machine solid waste pyrolytic incineration, including：Pretreatment system, quality coal in cement kiln systems, incinerator, storage device, it is described
Incinerator is connect with storage device, and the pretreatment system, incinerator, storage device pass through pipeline and cement kiln system respectively
System connection；
The incinerator includes above-mentioned pyrogenation incinerator 6, further includes air blower 13, suction machine 1, board-like discharging machine
7, the suction machine 1 is connected with the exhanst gas outlet of pyrogenation incinerator 6, the air of the air blower 13 and pyrogenation incinerator 6 into
Mouth is connected, and the board-like discharging machine 7 is connected with the discharging mechanism of pyrogenation incinerator 6,6 discharging mechanism of the pyrogenation incinerator
Lower section is additionally provided with flow valve f2 control blowings.
The pretreatment system includes sequentially connected solid waste repository 1, board-like metering feeding machine 1, refuse grinder
3, belt conveyer 4, current stabilization feeding bin 5；
Preferably, the solid waste repository is the closed structure that armored concrete pours, and side is equipped with automatic disengaging and seals
Door is readily transported vehicle 101 and enters discharging, and top is equipped with forced ventilation mouth, and the forced ventilation mouth is equipped with suction machine two；It is described
Storage bin 102 is additionally provided in solid waste repository, various solid wastes enter classified emission after storage bin 102, and according to characteristic at top
It sprays disinfectant and carries out sterilizing；Suction machine two is connected by pipeline with deodoriser 12, and solid waste repository 1 passes through suction machine
Two force air drafts, and the wind of discharge is sent into after deodoriser 12 eliminates foreign odor smell and will be discharged, or to be sent directly into pyrogenation incinerator 6 high
Temperature oxidation deodorization；
The discharge port of the storage bin 102 is connected with the feed inlet of board-like metering feeding machine 1, the board-like metering feeding
The discharge port of machine 1 is connected with the feed inlet of refuse grinder 3, and the discharge port of the refuse grinder 3 passes through belt conveyer 4
It is connect with the feed inlet of current stabilization feeding bin 5；
Preferably, the refuse grinder 3 is double-roll crusher, by refuse breaking or is shredded into particle less than 15cm again
It is sent directly into current stabilization feeding bin 5 by belt conveyor 4；
5 top of the current stabilization feeding bin is equipped with suction machine three, discharge port and the pyrolytic incineration of the current stabilization feeding bin 5
The feed inlet of stove 6 is connected, and the discharge port of current stabilization feeding bin 5 is additionally provided with flow valve f1.
The suction machine two and suction machine three are connected by pipeline with the high-temperature hot-air import of the pyrogenation incinerator 6, are taken out
The exhaust gas of suction is all participated in as cold wind, realizes the harmless treatment of concentration.
The quality coal in cement kiln systems includes cement kiln waste-heat power generation system, cement kiln flue gas processing system；
The cement kiln waste-heat power generation system is connected with the high-temperature hot-air import of above-mentioned pyrogenation incinerator 6, pyrogenation incinerator 6
Hot wind inlet and cement kiln waste-heat power generation system tertiary-air pipe opening 16 be connected, access 1100 DEG C or so of high-temperature hot-air, together
When participate in cold wind and be formulated to 600-900 DEG C；
The cement kiln flue gas processing system is connected with above-mentioned suction machine one, the pyrolysis gas after organic solid castoff burning
Body is discharged by exhanst gas outlet using suction machine one, and the gas of discharge enters cement kiln flue gas processing system and thoroughly burns, and is burned
Heat afterwards is used for cement kiln calcining, and pyrolysis gas thoroughly eliminates toxicity under cement kiln high-temperature strong basicity environment, and at unification
Reason discharge.
The storage device includes roto-siofter 10, collecting bin 9, board-like metering feeding machine 2 11, recycling metal repository 17；
The setting of the roto-siofter 10 passes through elevator 8 and the board-like discharging machine in 9 top of collecting bin, the roto-siofter 10
7 discharge port is connected；The roto-siofter 10 is also connected by pipeline with recycling metal repository 17, after unloading ash discharging screening
Fine powder fall into storage in the feed bin 9 that is connected with roto-siofter 10, coarse powder enters recycling metal system 17 and recycles metal；
The discharge port of 9 bottom of the collecting bin is connected with the feed inlet of board-like metering feeding machine 2 11, the board-like metering
The discharge port of feeder 2 11 is connect by pipeline with the tail smoke-box of cement kiln flue gas processing system, the fine powder that roto-siofter 9 sifts out
The tail smoke-box 15 for being sent directly into cement kiln flue gas processing system is handled as cement raw material by cement kiln collaboration, and organic solid is discarded
Energy existing for object itself is all recycled in processing procedure by quality coal in cement kiln systems, so as to make up the heat needed for pyrolysis.
Embodiment 2
As shown in figure 5, embodiment 2 provide a kind of organic solid castoff pyrogenation incinerator come it is discarded to powdery organic solid
Object burns, and the boiling type that can be used for granular material pyrolytic incineration is transformed on the basis of 1 pyrogenation incinerator of embodiment
Pyrogenation incinerator, garbage flying ash, the powdery solids waste such as organic abraum salt can be handled by being pyrolyzed burning stove using boiling type.
Embodiment 2 and embodiment 1 difference lies in：
Setting auxiliary combustion import 610 in the middle part of the left sidewall of the furnace body, the high temperature air inlet 603 is arranged at left furnace body bottom
Portion.
The discharging mechanism 608 is arranged in the right bottom of furnace body.
The left and right furnace body is separated by partition wall 607, and deflector is not arranged on partition wall.
Stationary furnace grate 606 in left furnace body is horizontally set on to the top of high temperature air inlet 603, the stationary furnace grate
For the steel-casting composition with blast cap.
Claims (10)
1. a kind of organic solid castoff pyrogenation incinerator, which is characterized in that including furnace body, machine is equipped with outside the furnace body
Shell；The furnace body includes left furnace body, right furnace body；
Be equipped with feed inlet at the top of the left furnace body, bottom is arranged high-temperature hot-air import, the left furnace body be additionally provided with auxiliary fuel into
Mouthful；The right furnace body is equipped with exhanst gas outlet, and bottom is equipped with air intlet；
The right bottom of furnace body is equipped with discharging mechanism, and the discharging mechanism includes rotatable tower fire grate, transmission vertical shaft, collection
Hopper, tremie pipe, driving mechanism, the tower fire grate and driving mechanism are connected by being driven vertical shaft, the aggregate bin upper end
It is connected with casing, aggregate bin lower end is connected with tremie pipe；
The discharging mechanism further includes wear-resisting annular steel lining, and the wear-resisting annular steel substrate portion is connected with aggregate bin.
2. a kind of organic solid castoff pyrogenation incinerator according to claim 1, which is characterized in that the left furnace body with
Right furnace body is separated by partition wall, and the partition wall is equipped with deflector.
3. a kind of organic solid castoff pyrogenation incinerator according to claim 1, which is characterized in that the high-temperature hot-air
Entrance is equipped with stationary furnace double-edged fine-toothed comb, and the stationary furnace double-edged fine-toothed comb is made of bar steel plate or steel-casting.
4. a kind of organic solid castoff pyrogenation incinerator according to claim 1, which is characterized in that the exhanst gas outlet
It is equipped with pressure monitor, temperature monitor, flow monitoring instrument, the pressure monitor, temperature monitoring with high-temperature hot-air import
Instrument, flow monitoring instrument are connected with the computer control system of peripheral hardware respectively.
5. a kind of organic solid castoff pyrogenation incinerator according to claim 1, which is characterized in that in the tremie pipe
Ash temperature monitor is set, and the ash temperature monitor is connected with the computer control system of peripheral hardware.
6. a kind of system of organic solid castoff pyrolytic incineration, which is characterized in that including：Pretreatment system, quality coal in cement kiln systems,
Incinerator, storage device, the pretreatment system are connect with incinerator, and the incinerator is connect with storage device, institute
Pretreatment system, incinerator, storage device is stated to connect with quality coal in cement kiln systems by pipeline respectively；
The incinerator includes the pyrogenation incinerator described in claim 1-4 any one, further includes air blower, suction machine
One, board-like discharging machine, the suction machine one are connected with the exhanst gas outlet of pyrogenation incinerator, the air blower and pyrogenation incinerator
Air intlet is connected, and the board-like discharging machine is connected with the discharging mechanism of pyrogenation incinerator.
7. a kind of system of organic solid castoff pyrolytic incineration according to claim 6, which is characterized in that the pre- place
Reason system include sequentially connected solid waste repository, board-like metering feeding machine one, refuse grinder, belt conveyer, current stabilization feed
Feed bin；
The solid waste repository is closed structure, and side is equipped with automatic disengaging hermatic door, and top is equipped with forced ventilation mouth, described strong
Ventilation opening processed is equipped with suction machine two；It is additionally provided with storage bin in the solid waste repository；
The discharge port of the storage bin is connected with the feed inlet of board-like metering feeding machine one, and the board-like metering feeding machine one goes out
Material mouth is connected with the feed inlet of refuse grinder, and the discharge port of the refuse grinder passes through belt conveyer and current stabilization feeding bin
Feed inlet connection；
Suction machine three is equipped at the top of the current stabilization feeding bin, discharge port and the pyrogenation incinerator of the current stabilization feeding bin are fed
Mouth is connected.
8. a kind of system of organic solid castoff pyrolytic incineration according to claim 7, which is characterized in that the suction
Machine two and suction machine three are connected by pipeline with the high-temperature hot-air import of the pyrogenation incinerator.
9. a kind of system of organic solid castoff pyrolytic incineration according to claim 6, which is characterized in that the cement
Kiln system includes cement kiln waste-heat power generation system, cement kiln flue gas processing system；
The cement kiln waste-heat power generation system is connected with the high-temperature hot-air import of above-mentioned pyrogenation incinerator；
The cement kiln flue gas processing system is connected with the suction machine one.
10. a kind of system of organic solid castoff pyrolytic incineration according to claim 6, which is characterized in that the storage
Cryopreservation device includes roto-siofter, collecting bin, board-like metering feeding machine two, recycling metal repository；
The roto-siofter is arranged at the top of collecting bin, the discharge port phase that the roto-siofter passes through elevator and the board-like discharging machine
Connection；The roto-siofter is also connected by pipeline with recycling metal repository；
The discharge port of the collecting bin bottom is connected with the feed inlet of board-like metering feeding machine two, the board-like metering feeding machine two
Discharge port connect with quality coal in cement kiln systems by pipeline.
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| CN110171935A (en) * | 2019-05-23 | 2019-08-27 | 惠州市环境科学研究所 | A kind of method of cement kiln synergic processing footwear material leftover pieces |
| CN110906337A (en) * | 2019-11-28 | 2020-03-24 | 上海锅炉厂有限公司 | Integrated fixed bed garbage high-efficiency gasification combustion furnace |
| CN111322866A (en) * | 2020-03-04 | 2020-06-23 | 高原晨曦 | Gasification and calcination device for low-calorific-value materials |
| CN113390082A (en) * | 2021-05-31 | 2021-09-14 | 上海海琦环保科技有限公司 | Fixed bed continuous upper air suction furnace for waste treatment |
| CN114307033A (en) * | 2021-12-21 | 2022-04-12 | 山东天力能源股份有限公司 | Waste salt drying and pyrolyzing system and method |
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Address after: 410075 D-244, No. 199 Lugu Road, Lugu Lu, high tech Zone, Changsha, Hunan Patentee after: Changsha Zhongsi Environmental Protection Technology Co., Ltd Address before: 410075 Hunan province Changsha hi tech Development Zone, Lu Valley Road No. 199 Lulong Lugu D Business Center No. 224 Patentee before: Changsha silicon cement technology development Co Ltd |