CN107286967A - One kind circulation pyrolysis furnace - Google Patents
One kind circulation pyrolysis furnace Download PDFInfo
- Publication number
- CN107286967A CN107286967A CN201710692514.1A CN201710692514A CN107286967A CN 107286967 A CN107286967 A CN 107286967A CN 201710692514 A CN201710692514 A CN 201710692514A CN 107286967 A CN107286967 A CN 107286967A
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- China
- Prior art keywords
- reactor
- rotating disk
- sealing plate
- pyrolysis furnace
- heater
- Prior art date
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Links
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 26
- 238000007789 sealing Methods 0.000 claims abstract description 60
- 238000010438 heat treatment Methods 0.000 claims abstract description 32
- 238000001816 cooling Methods 0.000 claims abstract description 27
- 238000006243 chemical reaction Methods 0.000 claims abstract description 12
- 238000004891 communication Methods 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 13
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 238000009413 insulation Methods 0.000 claims description 5
- 238000005507 spraying Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 9
- 238000007599 discharging Methods 0.000 abstract description 5
- 239000000945 filler Substances 0.000 abstract description 3
- 238000005336 cracking Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 5
- 239000002360 explosive Substances 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000004519 grease Substances 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000700605 Viruses Species 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- -1 aqueous vapor Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000013015 e-cracking Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 239000011276 wood tar Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The present invention is disclosed and sets at least three reactors in a kind of circulation pyrolysis furnace, rotating disk, and its openend is fixed in the side plate face of rotating disk；The plate face palette of sealing plate and rotating disk；The openend of at least one reactor is in communication with the outside；Rotating disk and sealing plate can be rotated against；It is used for discharging and filler when the openend of reactor is exposed, rotates against and closed by sealing plate after the completion of filling, is loaded on by heaters set on this reactor and carries out heating response；It is axially sliding that reaction completes post-heater, and rotating disk is rotated, cooler can be set on the reactor after heated device heating response and be cooled down, and cooling completes aftercooler and slides removal, rotating rotating disk makes reactor turn to the state do not closed by sealing plate, can carry out discharging.There is material to be heated or cooled in synchronization, material handling is carried out to another reactor do not closed during heating with cooling, to prepare next reaction cycle, so as to improve the utilization rate of reactor.
Description
Technical field
The present invention relates to Pintsch process equipment technical field, a kind of circulation pyrolysis furnace is further related to.
Background technology
The effect of high-temperature cracking furnace is that organic matter is decomposed to waste and old organic matter, harmful organic substance, virus etc. by high temperature
Into small molecule and the process of inorganic matter.It is divided into from energy usage type：Coal-fired cracking system, natural gas pyrolysis system, electric cracking
The class of system three, is divided into clearance-type cracking system and successive cracking system from the continuity of work.It can handle including plastics, stone
Raw material including oil, industrial and agricultural production rubbish, medical waste and house refuse.
Existing cracking apparatus includes combustion furnace, cracking still, liquid-gas separator, cooler, water seal, fuel tank, water tank, air storage
Tank etc..Current system cost is high, and the clearance-type cracking system of ten tons of processing in a set of day usually requires hundreds of thousands, at a set of day
Ten tons of successive cracking system of reason is up to two or three million, bulky, the floor space of set of system at least hundreds of of equipment
Square metre, at most thousands of square metres；Due to systems bulky, it is necessary to very big area of dissipation.Cracking still needs to be fed,
Heating, three steps of cooling, the completion to be cooled such as need can carry out next heating operation, plus hot and cold by filler again after heating
But process can not be carried out simultaneously, caused the time to be superimposed, reduced production efficiency.
Therefore, for those skilled in the art, how to design one kind can be while be heated and cooling procedure
Cracker, be the current technical issues that need to address.
The content of the invention
The present invention provides a kind of circulation pyrolysis furnace, can simultaneously be heated and cooling procedure, improve overall reaction
Utilization rate, concrete scheme is as follows：
One kind circulation pyrolysis furnace, including：
Rotating disk, is along the circumferential direction uniformly fixedly installed at least three reactors thereon, and the reactor is cylindrical in shape, described
The openend of reactor is fixed in the side plate face of the rotating disk, is opened up the reactor and the external world in the rotating disk
The through hole of connection；
Sealing plate, the plate face palette with the rotating disk closes the openend of the reactor；With for the moment
Carve, the openend of at least one reactor is exposed the sealing plate and is in communication with the outside；The rotating disk and the sealing plate
It can be rotated against around the central point of the reactor, the reactor can be exposed to outside the sealing plate one by one；
Heater, can slide axially and can be set in one of them the described reactor closed by the sealing plate
Upper carry out heating response；
Cooler, can slide axially, and can be set on the reactor after the heater heating response
Cooled down.
Alternatively, set in the rotating disk and fixed gear group, institute in rotary shaft, the rotary shaft are set perpendicular to plate face
Stating gear train can drive the rotating disk to rotate.
Alternatively, the rotary shaft passes through the sealing plate, and the external part of the rotary shaft sets nut by the sealing
Plate presses with the rotary shaft.
Alternatively, the sealing plate is in major arc, and the center is provided for avoiding the U-type groove of the rotary shaft.
Alternatively, steam vent and pressure-releasing hole are set on the sealing plate；The steam vent is set corresponding to the heater,
The gas discharge that heating response process can be produced；The pressure-releasing hole is used to be passed through water vapour.
Alternatively, position corresponding with the heater sets a steam vent and a pressure-releasing hole；With institute
State the corresponding position of cooler and two pressure-releasing hole are set, one of them is used to be passed through water vapour into the reactor, separately
One is used to be passed through water vapour between the reactor and the cooler.
Alternatively, the heater includes magnetic metal bucket, heat-insulation layer and the heating coil set gradually from inside to outside；Institute
The two ends for stating heating coil connect the heating of electromagnetic oven main frame respectively.
Alternatively, the cooler includes being located at the cooling bucket outside the reactor, the cooling bucket and institute
State rotating disk and keep sealing；It is provided for spraying the water inlet of current at the top of the cooling bucket to the reactor, it is described cold
But the bottom of bucket is provided for the delivery port of the water discharge in the cooling bucket.
Alternatively, the rotating disk and the plate face of the sealing plate are vertically arranged, the rotating disk horizontal rotation；Not by institute
The reactor for stating sealing plate closing is located at lower section.
The present invention provides and at least three reactions is along the circumferential direction uniformly fixedly installed in a kind of circulation pyrolysis furnace, rotating disk
Kettle, reactor is cylindrical in shape, and its openend is fixed in the side plate face of rotating disk, and other positions keep sealing, only passes through rotation
The through hole opened up on disk is in communication with the outside；The plate face palette of sealing plate and rotating disk, can be by the opening end seal of reactor
Close；In synchronization, the openend of at least one reactor is not sealed with plate closing, is in communication with the outside；Rotating disk and sealing
Plate can be rotated against around the central point of reactor, and reactor can be exposed to outside sealing plate one by one；In the openend of reactor
It is used for discharging and filler when exposed, rotates against and closed by sealing plate after the completion of filling, by heaters set loaded on this reactor
Carry out heating response；Reaction completion post-heater is axially sliding, and rotates rotating disk, and cooler can be set in heated device and add
Cooled down on reactor after thermal response, cooling completes aftercooler and slides removal, rotating rotating disk turns to reactor
The state do not closed by sealing plate, can carry out discharging.
Heating response, cooling and the handling of material are required for time, the structure that the present invention passes through at least three reactors
Design, has material to be heated or cooled in synchronization, and another reactor do not closed is entered during heating with cooling
Row material handling, to prepare next reaction cycle, so as to improve the utilization rate of reactor, it is to avoid single reaction kettle must be waited
And material filling, it is ensured that the continuity of reaction；Simple in construction, the low cost of the present invention, is easy to promote the use of.
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 accompanying drawing used required 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.
Circulation a kind of partial exploded view of angle of pyrolysis furnace part-structure that Figure 1A provides for the present invention；
The partial exploded view for circulation another angle of pyrolysis furnace part-structure that Figure 1B provides for the present invention；
Fig. 2A is rotating disk, reactor and a kind of axonometric drawing of angle of structure thereon；
Fig. 2 B are rotating disk, reactor and the axonometric drawing of another angle of structure thereon；
Fig. 3 A are a kind of front view of concrete structure of sealing plate；
Fig. 3 B are a kind of axonometric drawing of concrete structure of sealing plate；
Fig. 4 A are the axonometric drawing of heater；
Fig. 4 B are the explosive view of heater；
Fig. 5 is the axonometric drawing of cooler.
Figure includes：
Rotating disk 1, sealing plate 2, steam vent 21, pressure-releasing hole 22, reactor 3, heater 4, magnetic metal bucket 41, insulation
Layer 42, heating coil 43, cooler 5, cooling bucket 51, water inlet 52, delivery port 53, rotary shaft 6, gear train 61.
Embodiment
The core of the present invention is to provide a kind of circulation pyrolysis furnace, can simultaneously be heated and cooling procedure, improved
Overall reaction utilization rate.
In order that those skilled in the art more fully understands technical scheme, below in conjunction with accompanying drawing and specifically
Embodiment, to the present invention circulation pyrolysis furnace explanation is described in detail.
As shown in FIG. 1A and 1B, it is respectively the office for the different angles of two kinds of circulation pyrolysis furnace part-structure that the present invention is provided
Portion's explosive view.The circulation pyrolysis furnace includes the structures, rotating disk such as rotating disk 1, sealing plate 2, reactor 3, heater 4, cooler 5
1 keeps being brought into close contact with the plate face of sealing plate 2；At least three reactors 3 are along the circumferential direction uniformly fixedly installed in rotating disk 1,
Reactor 3 is cylindrical in shape, and its one end sets opening, and the openend of reactor 3 is fixed in the side plate face of rotating disk 1, rotating disk 1
On open up the through hole that reactor 3 is in communication with the outside, after reactor 3 and rotating disk 1 are fixed, be only capable of the plate by rotating disk 1
Face can just be in communication with the outside.
Sealing plate 2 and the plate face of rotating disk 1 are smooth, both plate face palettes, by the opening end seal of reactor 3
Close, seal grease is set between reactor 3 and sealing plate 2, when both are brought into close contact, hermetic seal is realized by grease；Same
Expose sealing plate 2 and be in communication with the outside in one moment, the openend of at least one reactor 3, that is to say, that the plate face of sealing plate 2 can not
All reactors 3 are all closed simultaneously, at least one holding is exposed.Reactor 3 is circumferentially uniform point in rotating disk 2
Cloth, be centrosymmetric setting, and rotating disk 1 and sealing plate 2 can be rotated against around the central point of reactor 3, because reactor 3 is uniformly set
Put, reactor 3 can be exposed to outside sealing plate 2 one by one in rotary course.
Heater 4 can slide axially, and can be set on reactor 3 or skid off, and can be set in by sealing plate 2
Heating response is carried out on one of reactor 3 of closing.After one of reactor 3 has loaded material, respective corners are rotated
Closed after degree by sealing plate 2, heater 4 is set on this reactor 3 and begun to warm up, and material is internally reacted.
Cooler 5 can slide axially, and can be set on the reactor 3 after the heated heating response of device 4 carry out it is cold
But.After the completion of the heating response of reactor 3, heater 4 is skidded off, the position that cooler 5 is reached after turning an angle stops,
Cooler 5 is slided again and is inserted on this reactor 3, process is begun to cool down, now reactor 3 is still closed by sealing plate 2.Until cold
But after the completion of, cooler 5 is skidded off, then reactor 3 is rotated into removal sealing plate 2 after certain angle, makes this reactor 3 and outer
Boundary is connected, and reacted material can be taken out into discharging, and recharges new reaction mass, and the circulation for being ready for next round is anti-
Answer process.
The present apparatus can be heated and cooling procedure simultaneously, correspond respectively to different reactors 3, in synchronization, respectively
Individual reactor 3 is respectively at different states, and the course of reaction moved in circles is realized by rotating rotating disk 1, will not be because a certain
Reactor 3 needs to cool down and take the heat time, and utilization rate is greatly enhanced., can be right respectively at least provided with three reactors 3
Answer loading and unloading, heating, the process of cooling, if necessary, greater number of reactor 3 can be set, these setting forms are all can
With.As shown in Figure 2 A and 2 B, respectively rotating disk 1, reactor 3 and the axonometric drawing of the different angles of two, structure thereon,
Illustrated in accompanying drawing by taking three reactors as an example, the line angle between three reactors 3 with central point is 120 degree, is in
Decile is set, and 120 degree of rotation is rotated every time and is stopped.
Set in rotating disk 1 where plate face sets fixed gear group 61 in rotary shaft 6, rotary shaft 6, gear train 61
Position be higher than the height of reactor 3, gear train 61 can drive rotating disk 1 to rotate as drive mechanism.Heater 4 and cold
But axial stretching of the device 5 along rotary shaft 6 is moved, and its specific driving structure can be arranged as required to, and the present invention is no longer limited herein.
In addition to by rotary shaft 6 and gear train 61, using other setting forms；Sealing plate 2 is fixed in above-described embodiment
Fixed, rotating disk 1 is rotated, if setting on the contrary, rotating disk 1 is kept fixation, is made sealing plate 2, heater 4, cooler 5
The setting form of synchronous axial system is also possible, and these specific embodiments should be all included within protection scope of the present invention.
Rotary shaft 6 passes through and sets nut on sealing plate 2, the external part of rotary shaft 6, by nut by sealing plate 2 with rotating
Axle 1 presses, while ensure that can relatively rotate between the two.
As shown in Figure 3 A and Figure 3 B, the respectively front view and axonometric drawing of a kind of concrete structure of sealing plate 2, sealing plate 2
In major arc tabular, equivalent to cutting about 1/3rd in circular plate face, retain wherein larger part, two are covered at the same time
Or multiple reactors 3, the center be provided for avoid rotary shaft 6 U-type groove, think that rotary shaft 6 is stepped down, in rotary shaft 6
Nut is pressed in the both sides of U-type groove.
Further, steam vent 21 and pressure-releasing hole 22 are set on sealing plate 2；Steam vent 21 is set corresponding to heater 4
Put, the gas discharge that heating response process can be produced, when the air pressure inside reactor 3 is more than an atmospheric pressure, thus
Hole, which is deflated, depressurizes；Discharge duct is connected on steam vent 21, by the unified collection of gas, pollution is prevented.Pressure-releasing hole 22 is used to be passed through water
Steam, when there is negative pressure inside reactor 3, water vapour can be passed through thereto, keep internal pressure to maintain all the time one big
Air pressure.
As shown in Figure 3 B, one steam vent 21 and a pressure-releasing hole 22 are set with the corresponding position of heater 4, are respectively used to
Exhaust and the gas transmission into reactor 3 from reactor 3；Two pressure-releasing hole 22 are set with the corresponding position of cooler 5, wherein one
It is individual to be used to be passed through water vapour into reactor 3；Because cooler 5 and rotating disk 1 keep sealing, negative pressure also occurs during cooling, because
This another pressure-releasing hole 22 is used to, to water vapour is passed through between reactor 3 and cooler 4, keep between reactor 3 and cooler 4
Air pressure it is normal.
As shown in Figure 4 A and 4 B shown in FIG., the respectively axonometric drawing and explosive view of heater 4, heater 4 include from inside to outside according to
Magnetic metal bucket 41, heat-insulation layer 42 and the heating coil 43 of secondary setting；The two ends of heating coil 43 connect electromagnetic oven main frame respectively
Heated, make to produce vortex in magnetic metal bucket 41 by way of sensing, quick heating, the thermal efficiency of this mode of heating is very
Height, up to more than 95%.Heat-insulation layer 42 is set between magnetic metal bucket 41 and heating coil 43, heating coil 43 can be prevented
Temperature is too high and melts.
As shown in figure 5, being the axonometric drawing of cooler 5, cooler 5 includes being located at the cooling bucket outside reactor 3
51, the space between cooling bucket 51 and reactor 3 is larger, the flowing for current.When cooling bucket 51 is set on reactor 3,
Sealing is kept to dock with rotating disk 1.The top of cooling bucket 51 is provided for spraying the water inlet 52 of current, cooling to reactor 3
The bottom of bucket 51 is provided for the delivery port 53 of the water discharge cooled down in bucket 51, and cooling water enters from water inlet 52, from upper
Side, which is sprayed on reactor 3, to be cooled, and the downward convergence of water for absorbing heat is discharged from delivery port 53, water inlet 52 and delivery port
53 difference connecting water pipes.
The plate face of rotating disk 1 and sealing plate 2 in the present apparatus is vertically arranged, rotary shaft 6 in horizontally disposed, rotating disk 1 around
Rotary shaft 6 is horizontally rotated.The reactor 3 do not closed in three reactors 3 by sealing plate 2 is located at lower section, namely when a certain anti-
Answer kettle 3 move to lower section when its opening expose, with easy-unloading and filling.
The system can be used for the cracking of the debirs such as junked tire and plastics, waste lithium cell, straw.Junked tire and
The pyrolysis product of plastics mainly has：Can fuel oil, carbon black and a part of fuel gas；Lithium battery pyrolysis product mainly has：Lead, aluminium,
Carbon black and a part of fuel gas, a small amount of rare element；Straw pyrolysis product mainly has：Fuel gas, aqueous vapor, wood tar etc..
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or using the present invention.
A variety of modifications to these embodiments will be apparent for those skilled in the art, as defined herein
General Principle, can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, this hair
It is bright to be not intended to be limited to the embodiments shown herein, and be to fit to and principles disclosed herein and features of novelty phase
Consistent most wide scope.
Claims (9)
1. one kind circulation pyrolysis furnace, it is characterised in that including：
Rotating disk (1), is along the circumferential direction uniformly fixedly installed at least three reactors (3) thereon, and the reactor (3) is in cylinder
Shape, the openend of the reactor (3) is fixed in the side plate face of the rotating disk (1), opened up on the rotating disk (1) by
The through hole that the reactor (3) is in communication with the outside；
Sealing plate (2), the plate face palette with the rotating disk (1) closes the openend of the reactor (3)；
Expose the sealing plate (2) and be in communication with the outside in synchronization, the openend of at least one reactor (3)；The rotating disk
(1) it can be rotated against with the sealing plate (2) around the central point of the reactor (3), the reactor (3) can be exposed one by one
Outside the sealing plate (2)；
Heater (4), can slide axially and can be set in one of them the described reaction closed by the sealing plate (2)
Kettle carries out heating response on (3)；
Cooler (5), can slide axially, and can be set in the reactor after the heater (4) heating response
(3) cooled down on.
2. circulation pyrolysis furnace according to claim 1, it is characterised in that set on the rotating disk (1) perpendicular to plate face
Fixed gear group (61) on rotary shaft (6), the rotary shaft (6) is set, and the gear train (61) can drive the rotating disk
(1) rotate.
3. circulation pyrolysis furnace according to claim 2, it is characterised in that the rotary shaft (6) passes through the sealing plate
(2), the external part of the rotary shaft (6) sets nut to press the sealing plate (2) with the rotary shaft (1).
4. circulation pyrolysis furnace according to claim 3, it is characterised in that the sealing plate (2) is in major arc, the center is set
Put the U-type groove for avoiding the rotary shaft (6).
5. circulation pyrolysis furnace according to claim 1, it is characterised in that steam vent (21) is set on the sealing plate (2)
With pressure-releasing hole (22)；The steam vent (21) is set corresponding to the heater (4), the gas that can produce heating response process
Body is discharged；The pressure-releasing hole (22) is used to be passed through water vapour.
6. circulation pyrolysis furnace according to claim 5, it is characterised in that position corresponding with the heater (4) is set
One steam vent (21) and a pressure-releasing hole (22)；Position corresponding with the cooler (5) is set described in two
Pressure-releasing hole (22), one of them is used to be passed through water vapour into the reactor (3), and another is used for the reactor (3)
Water vapour is passed through between the cooler (4).
7. circulation pyrolysis furnace according to claim 1, it is characterised in that the heater (4) is included from inside to outside successively
Magnetic metal bucket (41), heat-insulation layer (42) and the heating coil (43) of setting；The two ends of the heating coil (43) are connected respectively
Electromagnetic oven main frame is heated.
8. circulation pyrolysis furnace according to claim 1, it is characterised in that the cooler (5) includes that institute can be located at
The outside cooling bucket (51) of reactor (3) is stated, the cooling bucket (51) keeps sealing with the rotating disk (1)；The cooling bucket
(51) it is provided for spraying the water inlet (52) of current at the top of to the reactor (3), the bottom of the cooling bucket (51) is set
Put the delivery port (53) for the water in the cooling bucket (51) to be discharged.
9. circulation pyrolysis furnace according to claim 1, it is characterised in that the rotating disk (1) and the sealing plate (2)
Plate face is vertically arranged, rotating disk (1) horizontal rotation；Under the reactor (3) do not closed by the sealing plate (2) is located at
Side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710692514.1A CN107286967B (en) | 2017-08-14 | 2017-08-14 | Circulation pyrolysis furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710692514.1A CN107286967B (en) | 2017-08-14 | 2017-08-14 | Circulation pyrolysis furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107286967A true CN107286967A (en) | 2017-10-24 |
| CN107286967B CN107286967B (en) | 2024-01-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710692514.1A Active CN107286967B (en) | 2017-08-14 | 2017-08-14 | Circulation pyrolysis furnace |
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| Country | Link |
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| CN (1) | CN107286967B (en) |
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| CN109971960A (en) * | 2017-12-27 | 2019-07-05 | 山东锂想新能源科技有限公司 | A kind of lithium battery cracking system |
| CN111732960A (en) * | 2020-08-06 | 2020-10-02 | 安徽奉念城机电设计服务有限公司 | High-temperature carbonization treatment assembly for household garbage |
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|---|---|---|---|---|
| CN109971960A (en) * | 2017-12-27 | 2019-07-05 | 山东锂想新能源科技有限公司 | A kind of lithium battery cracking system |
| CN111732960A (en) * | 2020-08-06 | 2020-10-02 | 安徽奉念城机电设计服务有限公司 | High-temperature carbonization treatment assembly for household garbage |
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| CN107286967B (en) | 2024-01-12 |
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