CN104772103B - Mobile pyrolysis reaction device and pyrolysis method - Google Patents
Mobile pyrolysis reaction device and pyrolysis method Download PDFInfo
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- CN104772103B CN104772103B CN201410016598.3A CN201410016598A CN104772103B CN 104772103 B CN104772103 B CN 104772103B CN 201410016598 A CN201410016598 A CN 201410016598A CN 104772103 B CN104772103 B CN 104772103B
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- bed body
- thermal source
- source bed
- reaction surface
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- 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
- C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
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- 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
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
- C10B47/40—Other processes in ovens with mechanical conveying means with endless conveying devices
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention provides a mobile pyrolysis reaction device and a pyrolysis method; the device comprises a pyrolysis reaction chamber, a heat source bed body located in the pyrolysis reaction chamber, and a mobile assembly matched with the heat source bed body; the heat source bed body at least includes a first reaction surface and a second reaction surface corresponding to the mobile assembly; the first reaction surface and the second reaction surface have temperature conditions suitable for a pyrolysis reaction; the pyrolysis reaction process of materials comprises a moving process of the materials on the first reaction surface, a process of the materials moving from the first reaction surface to the second reaction surface, and a process of the materials moving on the second reaction surface, so that under conditions of unchanging of whole reaction device internal space and the heat source bed body size, the stroke of the materials in the pyrolysis reaction process is effectively extended, the pyrolysis reaction efficiency of the materials is ensured, and pyrolysis process continuous production is facilitated to be achieved.
Description
Technical field
The present invention relates to pyrolytic reaction apparatus field, more particularly to a kind of portable pyrolysis consersion unit and its pyrolysis side
Method.
Background technology
The fast development of petroleum industry, promotes the extensive production of organic products and applies, and thing followed organic waste
Gurry is more and more, and such waste pollution problem is also increasingly serious, and this undoubtedly becomes environmental issue urgently to be resolved hurrily.
The method of conventional process organic waste is for landfill or burns, and it not only causes the secondary pollution to environment, and
The effective and reasonable utilization of resource can not be realized.Test and explore through constantly, industry is fully recognized that, waste and old organic materials
Potential very big market prospects are recycled, various treasured can be extracted from organic materials by organic materials pyrolytic technique
Your resource, including fuel oil, gas, carbon black, steel wire, while it realizes " turning waste into wealth ", the more conducively protection of ecological environment.Mesh
The front organic materials pyrolysis plant for being adopted in the industry generally includes grate-type, siege formula, fluidized bed type etc., siege formula pyrolysis plant
Including fixed-bed type and moving-bed type.Wherein, portable pyrolysis plant because its can long-time preferably continuously produce, and obtain
More it is widely applied.
With reference to shown in Fig. 1, in prior art, portable pyrolysis plant includes pyrolytic reaction room 1 ', is arranged at pyrolytic reaction
Thermal source bed body 2 ' and moving assembly 3 ' in room 1 ', pyrolytic reaction room 1 ' is with for importing the material inlet of material to be pyrolyzed
11 ' and corresponding product exit, the two ends of thermal source bed body 2 ' are respectively provided with thermal source import 21 ' and thermal source outlet 22 ', so as to thermal source bed
The surface 20 ' of body 2 ' can possess the temperature conditionss needed for pyrolysis；Wherein, thermal source bed body is driven by the running of moving assembly 3 '
Material on surface 20 ' is moved and is persistently pyrolyzed, and most at last the product of pyrolytic reaction is derived to pyrolysis from corresponding material outlet
Outside reative cell.However, in above prior art, due to being only provided with the single surface 20 ' for there is pyrolytic reaction, causing
The stroke length of the material in pyrolytic reaction room depends entirely on the size of whole pyrolysis plant and the length of thermal source bed body.Change speech
It, this kind of mode limits stroke of the material in pyrolytic reaction room, if need to reach higher pyrolysis effect in shorter stroke
Rate, just needs the indexs such as higher heat source temperature and heat exchange efficiency, and this causes unfavorable to the cost and security of pyrolytic reaction technique,
In view of this, it is necessary to which existing portable pyrolysis consersion unit is improved to solve existing issue.
The content of the invention
It is an object of the invention to provide a kind of portable pyrolysis consersion unit, is existed with solving material present in prior art
The problem of the stroke limiting of pyrolytic reaction chamber interior movement.
It is yet another object of the invention to provide a kind of method for pyrolysis of portable pyrolysis consersion unit, to solve prior art
Present in the problem of stroke limiting that moves in pyrolytic reaction chamber interior of material.
To solve above-mentioned technical problem, the technical scheme of the embodiment of the present invention is as follows：A kind of portable pyrolysis consersion unit,
It includes：Pyrolytic reaction room, with for importing the material inlet of material to be pyrolyzed and the material for deriving thermal decomposition product goes out
Mouthful；Moving assembly, is arranged at the pyrolytic reaction chamber interior, and the moving assembly is used for the material to be pyrolyzed from the thing
Expect into port transmission to the material outlet；And thermal source bed body, the thermal source bed body includes corresponding with the moving assembly
First reaction surface and the second reaction surface, first, second reaction surface is separately positioned and possesses needed for material pyrolysis
Temperature conditionss, the moving assembly mobile material to be pyrolyzed on first reaction surface, and treat pyrogen by described
Material is transferred to second reaction surface from first reaction surface, to treat heat described in mobile on second reaction surface
Solution material.
As a further improvement on the present invention, the thermal source bed body is hot including the first separately positioned thermal source bed body and second
Source bed body, the first thermal source bed body possesses first reaction surface, and the Secondary Heat Source bed body possesses second reaction
Surface.
As a further improvement on the present invention, the first thermal source bed body, Secondary Heat Source bed body possess respectively for circulating
First heat source passages of heat source body, Secondary Heat Source passage, the separate setting of first, second heat source passages.
As a further improvement on the present invention, the moving assembly include chain assemblies and at least two with the chain group
The bearing wheels that part coordinates, the chain assemblies make gyration on first, second reaction surface, wrap in the bearing wheels
Active bearing wheels are included, to be provided with the chain assemblies and scrape materials and parts for drive material movement to be pyrolyzed.
As a further improvement on the present invention, the materials and parts of scraping are including main part and opposite on the main part
The first wiper for arranging and the second wiper, first wiper drives material to be pyrolyzed on first reaction surface
Motion, second wiper drives material to be pyrolyzed to move on second reaction surface.
As a further improvement on the present invention, the end that material to be pyrolyzed is accepted in the Secondary Heat Source bed body extends beyond
The active bearing wheels position.
As a further improvement on the present invention, the end for material to be pyrolyzed being accepted in the Secondary Heat Source bed body is provided with a use
In the deflector being drained to material on the second reaction surface, the deflector is located at the active bearing wheels away from described first
The side of thermal source bed body.
As a further improvement on the present invention, the first thermal source bed body has that thermal source enters tube portion and thermal source goes out pipe portion
Point, the thermal source enters tube portion including the first pipeline, second pipe and the 3rd pipeline being connected between first, second pipeline,
The thermal source enters tube portion including the 4th pipeline, the 5th pipeline and the 6th pipeline being connected between the four, the 5th pipelines, described
The sidepiece of second pipe, the 4th pipeline respectively from the first thermal source bed body stretches out, first pipeline, the 5th pipeline
Highly less than the height of the moving assembly.
Correspondingly, a kind of method for pyrolysis of portable pyrolysis consersion unit, comprises the steps：There is provided in the heat
The heat source body of source bed body internal circulation, to obtain the pyrolysis temperature condition on first, second reaction surface；Start described mobile group
The motion of part；Material to be pyrolyzed is directed in the pyrolytic reaction room；Material to be pyrolyzed is made in first reaction surface
It is mobile concurrently to give birth to pyrolytic reaction；Material to be pyrolyzed is transferred to into second reaction surface from first reaction surface；To treat
Pyrolysis material makees mobile concurrently raw pyrolytic reaction in second reaction surface；The product that pyrolytic reaction is obtained is derived to institute
State the outside of pyrolytic reaction room.
As a further improvement on the present invention, the material to be pyrolyzed includes damaged tire, rubber, plastics, other organic wastes
One or more in material.
As a further improvement on the present invention, methods described also specifically includes following steps：First thermal source bed is provided respectively
Body and Secondary Heat Source bed body, and the first, second thermal source bed body is placed in pyrolytic reaction room, the first thermal source bed body
With the first reaction surface, the Secondary Heat Source bed body has the second reaction surface；Moving assembly is placed in into the pyrolysis anti-
Indoor relevant position is answered, to guarantee that the moving assembly can make gyration in first, second reaction surface, wherein, mobile group
Part includes the Part I with the first reaction surface phase separation and the Part II with the second reaction surface phase separation.
As a further improvement on the present invention, methods described also specifically includes following steps：Respectively described first, second
Thermal source bed body internal circulation thermal source, wherein, material on the circulating direction and the first thermal source bed body of the first thermal source bed body endogenous pyrogen
The direction of motion is conversely, the circulating direction of Secondary Heat Source bed body endogenous pyrogen is consistent with the direction of motion of material in Secondary Heat Source bed body.
Compared with prior art, the invention has the beneficial effects as follows：It is provided with the pyrolytic reaction room of the present invention and possesses pyrolysis
First reaction surface and the second reaction surface of temperature conditionss, and by the way that material is directed in pyrolytic reaction room from material inlet
Portion carries out pyrolytic reaction process, after being moved and be pyrolyzed on the first reaction surface due to material, and from the transfer of the first reaction surface
Proceed to move and be pyrolyzed to the second reaction surface so that in whole consersion unit inner space and thermal source bed body chi
It is very little it is constant in the case of, effectively extended stroke of the material during pyrolytic reaction, so that it is guaranteed that material pyrolytic reaction effect
Rate, beneficial to the continuous prodution for realizing pyrolytic process.
Description of the drawings
Fig. 1 is the structural representation of pyrolytic reaction equipment in prior art；
Fig. 2 is structural representation of the pyrolytic reaction equipment on main perspective in the specific embodiment of the invention；
Fig. 3 is structural representation of the pyrolytic reaction equipment on depression angle in the specific embodiment of the invention；
Fig. 4 is structural representation of the pyrolytic reaction equipment on LOOK LEFT in the specific embodiment of the invention；
Fig. 5 is the close-up schematic view in Fig. 1 at label A；
Fig. 6 is that the position of first, second thermal source bed body and bearing wheels in pyrolytic reaction equipment in one embodiment of the invention is closed
It is schematic diagram；
Fig. 7 is the position of first, second thermal source bed body and bearing wheels in pyrolytic reaction equipment in another embodiment of the present invention
Relation schematic diagram.
Specific embodiment
Describe the present invention below with reference to specific embodiment shown in the drawings.The portable pyrolysis of the present invention
Consersion unit can be applicable to one or more the pyrolytic process in damaged tire, rubber, plastics, other organic materials.With useless
As a example by the pyrolytic process of tire, the product of its pyrolytic reaction includes carbon black, steel wire, a small amount of other metals, fuel oil and gas.
Coordinate with reference to shown in Fig. 2, Fig. 3 and Fig. 4, in the specific embodiment of the invention, movable type pyrolysis consersion unit 100 includes
Pedestal 1 and the pyrolytic reaction room 2 being arranged on pedestal 1, the inside of the pyrolytic reaction room 2 is closed, hot environment, on its wall body
Offer for material to be pyrolyzed to be directed in pyrolytic reaction room the material inlet 21 for making pyrolytic reaction.Additionally, the present embodiment
In, the material outlet for deriving thermal decomposition product is further opened with the wall body of pyrolytic reaction room 2, material outlet includes being located at pyrolysis instead
Answer the gaseous state discharging opening 23 and the solid-state discharging opening 25 positioned at the bottom of pyrolytic reaction room 2 at the top of room 2.Wherein, carbon black and steel wire etc.
Product is derived from solid-state discharging opening 25, and product derived from gaseous state discharging opening passes through condensation procedure, realization wherein heavy, light component
Separate.
In the present embodiment, pyrolytic reaction room 2 is internally provided with the first thermal source bed body 3, Secondary Heat Source bed body 4 and with
First, the moving assembly 5 that Secondary Heat Source bed body is engaged.First thermal source bed body 3 and Secondary Heat Source bed body 4 are separately positioned, both of which
By the heat source body that internally circulates, so as to reach the hot conditions needed for pyrolytic reaction on each face；Moving assembly 5 is used for
Realize mobile pyrolytic process of the material to be pyrolyzed in first, second thermal source bed body.In the present embodiment, heat source body is high temperature cigarette
Gas, however, in other embodiments of the present invention, the high temperature heat source is not limited to high-temperature flue gas.
In the present embodiment, the first thermal source bed body 3 and Secondary Heat Source bed body 4 have respectively separate heat source passages, with
Guarantee the heat transfer efficiency of two thermal source bed bodies and facilitate implementation temperature control.Wherein, the first thermal source bed body 3 has and is communicated in thermal source
The thermal source of bed body 3 enters tube portion and thermal source goes out tube portion, the thermal source enter tube portion including the first pipeline 31, second pipe 35 and
The 3rd pipeline 33 being connected between first, second pipeline, thermal source enters tube portion including the 4th pipeline 37, the 5th pipeline 32 and connects
The 6th pipeline 39 being connected between the four, the 5th pipelines, second pipe 35, the 4th pipeline 37 are respectively from the first thermal source bed body
3 sidepiece stretches out, and first pipeline 31, the height of the 5th pipeline 32 are less than the height of the moving assembly.3rd pipe
The pipeline 39 of road 33 and the 6th is in respectively arc-shaped.
In the present embodiment, Secondary Heat Source bed body 4 then includes being connected to the thermal source inlet pipe 44 and thermal source outlet pipe 45 of bed body, its
In, the height of the height of thermal source inlet pipe 44 and the first pipeline 31 maintains an equal level, consequently facilitating supplying high temperature heat source simultaneously for the complete equipment.
Certainly, in other embodiments of the present invention, the shape of thermal source pipeline, position, and the number of thermal source import or thermal source outlet
Respective change is carried out according to design requirement.
Continue to coordinate with reference to shown in Fig. 2, Fig. 3 and Fig. 4, moving assembly 5 include chain assemblies 51 and with the chain assemblies 51
The active bearing wheels 53 for coordinating and a driven bearing wheels 55, active bearing wheels 53 have a rotating shaft 530, driven bearing wheels
55 have a rotating shaft 550.Wherein, active bearing wheels 53 provide driving force by drive train 6, so as to drive the edge of chain assemblies 51
The first thermal source bed body 3, the apparent motion of Secondary Heat Source bed body 4.However, those of ordinary skill in the art will be readily apparent,
The unlimited number of bearing wheels is in two, while the number of driving and driven bearing wheels and its position can be made to change as the case may be
Become.
With reference to shown in Fig. 2, Fig. 5, in the present embodiment, the first thermal source bed body 3 have for carry out material pyrolytic reaction the
One reaction surface 30, and Secondary Heat Source bed body 4 has for carrying out the second reaction surface 40 of material pyrolytic reaction, first, the
Two reaction surfaces are respectively the upper surfaces of horizontal thermal source bed body.It is provided with chain assemblies 51 for pushing scraping for material to be pyrolyzed
Materials and parts 57, as the swinging of chain assemblies 51 is moved, the chain assemblies 51 remain some with the first reaction surface
30 contact, the state that another part contacts with the second reaction surface 40.In the preferred embodiment of the invention, the first thermal source bed
The direction of motion of material is conversely, shown in ginseng Fig. 5, material is first on the circulating direction of the endogenous pyrogen of body 3 and the first thermal source bed body 3
Move along direction D1 on reaction surface 30, and flue gas circulates inside the first reaction bed body 3 along direction D2, due to flue gas certainly
The thermal losses of body, it can be ensured that when material is moved on first aspect surface, its pyrolysis temperature is stepped up, and can so alleviate thing
Material is in thermal source bed body surface coking situation；It is further preferable that the circulating direction of the endogenous pyrogen of Secondary Heat Source bed body 4 and Secondary Heat Source bed
The direction of motion of material is consistent on body 4, i.e., material is moved on the first reaction surface 40 along direction D2, and flue gas is anti-first
Answer and circulated along direction D2 inside bed body 4, such material from the first reaction surface when being transferred on the second reaction surface, and it is hot
Solution temperature is not changed in substantially, so as to be more conducive to the continuity of pyrolytic reaction.
Coordinate with reference to shown in Fig. 2, Fig. 3, Fig. 4 and Fig. 5, in the present embodiment, chain assemblies 51 include being located at the first thermal source bed
Part between body 3 and material inlet 21, and the part between the first thermal source bed body 3 and Secondary Heat Source bed body 4, chain
It is interval with component 51 and some scrapes materials and parts 57.Surface 30 and Secondary Heat Source bed of the chain assemblies 51 along the first thermal source bed body 3
Gyration is made on the surface 40 of body 4, scrapes materials and parts 57 and is respectively arranged at the surface 30 of thermal source bed body 3 and the surface of thermal source bed body 4
40 top, wherein, scrape and allow to leave certain gap between materials and parts 57 and reaction surface 30 or 40.In the present embodiment, scraper
Part 57 includes main part 570 and the wiper 571 being disposed opposite to each other and wiper 572 on the main part 570.This is scraped
Materials and parts 57 substantially in lamellar, its main part 570 substantially with chain assemblies in vertical state, along with the revolution of chain assemblies,
Scrape on materials and parts 57 two wiper and also make corresponding flip-flop movement, i.e. wiper 572 drives material to be pyrolyzed in reaction surface 30
Upper motion, wiper 571 drives material to be pyrolyzed to move on reaction surface 40.In various embodiments of the present invention, scraping materials and parts can
It is designed as the forms such as strip, bent plate shape.
With reference to shown in Fig. 3 and Fig. 4, in the present embodiment, chain assemblies 51 include chain 51a and chain arranged in parallel
51b, if individual materials and parts 57 of scraping are fixed on chain 51a, 51b, wherein, the bearing of trend of chain 51a, 51b and material to be pyrolyzed
Flow direction is consistent, and scrapes the bearing of trend and the first chain 51a or the bearing of trend of the first chain 51b of materials and parts 57
It is perpendicular.Certainly, in other possible embodiments, the number of chain and scrape the fixed form of materials and parts and can make according to actual needs to change
Become.And those of ordinary skill in the art are it is envisioned that moving assembly also can be above-mentioned to replace by modes such as conveyer belts
Chain.
Shown in ginseng Fig. 2, for the present invention is better achieved, chain assemblies are equipped with one or more governor motions 56,
The governor motion 56 is used for according to the spacing between actual condition two bearing wheels 53,55 of regulation, so as to realize the elastic of chain
The regulatory function of degree.
Fig. 6 is the position relationship schematic diagram of first, second thermal source bed body and bearing wheels in one embodiment of the invention.Wherein,
First thermal source bed body 3 is arranged between two bearing wheels 53,55.First thermal source bed body 3 includes mutually close with active bearing wheels 53
First end 34 and the second end 36 mutually close with driven bearing wheels 55, first end 34 have a top edge 341 and
Lower limb 342, the distance between top edge 341 and active bearing wheels 53 than between lower limb 342 and active bearing wheels 53 away from
From little, material is guided to into the surface of Secondary Heat Source bed body 4 from the surface of the first thermal source bed body 3 so as to more utilize.
In the present embodiment, to guarantee material during Secondary Heat Source bed body 4 is transferred to from the first thermal source bed body 3, no
Outside as overflow to bed body, accept in the Secondary Heat Source bed body 4 material to be pyrolyzed the 3rd end 41 extend beyond it is described
The position of active bearing wheels 53；And for the 4th end 42 relative with the 3rd end in Secondary Heat Source bed body 4, its institute
Solid-state export mouth position can not be exceeded in position, consequently facilitating solid product is derived from solid-state export mouth.
Fig. 7 is the position relationship schematic diagram of first, second thermal source bed body and bearing wheels in another embodiment of the present invention.Its
In, it sets up a deflector 43 on the basis of above-described embodiment, and the deflector 43 is arranged to be accepted in Secondary Heat Source bed body and treats
One end of pyrolysis material, and deflector 43 is located at side of the active bearing wheels 53 away from the first thermal source bed body 3.
It is noted that be only described in detail to part preferred embodiment of the present invention herein, not for it is all can
Row embodiment is described one by one, and for example, above-mentioned first reaction surface and the second reaction surface can be in same thermal source bed body
Two surfaces being disposed opposite to each other, or, Secondary Heat Source bed body only plays a part of water conservancy diversion material, and by the first thermal source bed body
Spacing between lower surface and Secondary Heat Source bed body furthers, so as to the lower surface of the first thermal source bed body is second reaction table
Face.
Next, with reference to shown in Fig. 2 and Fig. 5, in the embodiment of the present invention, using the pyrolysis side of above-mentioned pyrolytic reaction equipment
Method, comprises the steps：
S1, provide to the heat source body in the thermal source bed body internal circulation, to obtain on first, second reaction surface
Pyrolysis temperature condition；Wherein, the first thermal source bed body 3 and Secondary Heat Source bed body 4 be provided respectively, and by first, second thermal source
Bed body is placed in pyrolytic reaction room 2, and the first thermal source bed body 3 has first reaction surface 30, and Secondary Heat Source bed body 2 has
Second reaction surface 40；Moving assembly 5 is placed in into the relevant position in the pyrolytic reaction room 2, to guarantee the movement
Component 5 can make gyration in first, second reaction surface, wherein, moving assembly 5 includes and the phase separation of the first reaction surface 30
Forward part and the rotating part with the phase separation of the second reaction surface 40.
It is highly preferred that the present embodiment is respectively in the first, second thermal source bed body internal circulation thermal source, wherein, first is hot
The direction of motion of material is conversely, hot in Secondary Heat Source bed body 4 on the circulating direction of the endogenous pyrogen of source bed body 3 and the first thermal source bed body 3
The circulating direction in source is consistent with the direction of motion of material in Secondary Heat Source bed body 4.
S2, startup drive train 6, to drive the moving assembly 5 to make gyration；
S3, material to be pyrolyzed is directed in the pyrolytic reaction room 2；Wherein, material to be pyrolyzed need first by it is broken,
The pretreatment process such as melting, then by the liquid material in molten condition obtained after pretreating process toward in pyrolytic reaction room 2
Conveying.
S4, moving assembly 5 scraping effect under, material be pyrolyzed first reaction surface 30 make move and occur
Pyrolytic reaction；
After S5, material make the movement of certain stroke on the first reaction surface 30, just it is transferred to from the first reaction surface 30
On second reaction surface 40；
S6, under the scraping effect of moving assembly 5, material be pyrolyzed is made to move and continue on the second reaction surface 40
Raw pyrolytic reaction；
S7, the outside derived the product that pyrolytic reaction is obtained to the pyrolytic reaction room, material is in pyrolytic reaction mistake
The products such as carbon black, oil gas are produced in journey, carbon black is moved to behind the end of Secondary Heat Source bed body 4, and can be from solid-state discharging opening 25
Derive to reative cell, wherein, solid-state discharging opening goes out to arrange corresponding sealing mechanism, anti-to prevent extraneous air from entering pyrolysis
Should interior；Gaseous oil gas is then derived from gaseous state discharging opening 23.
In sum, portable pyrolysis consersion unit of the invention and its method for pyrolysis, by arranging at least two and moving
The thermal source bed body 3,4 that dynamic component 5 is engaged, the thermal source bed body 3,4 branches have to material pyrolytic reaction reaction surface 30,
40, after moving and be pyrolyzed on the first reaction surface due to material, and it is transferred on the second reaction surface from the first reaction surface
Proceed to move and be pyrolyzed so that in the case of whole consersion unit inner space and thermal source bed body size constancy,
Effectively extended stroke of the material during pyrolytic reaction, so that it is guaranteed that the pyrolytic reaction efficiency of material, beneficial to realization pyrolysis
The continuous prodution of technique.
It should be understood that, although this specification is been described by according to embodiment, but not each embodiment is only only comprising one
Vertical technical scheme, this narrating mode of specification is only that for clarity those skilled in the art should be by specification
As an entirety, the technical scheme in each embodiment can also Jing it is appropriately combined, formed it will be appreciated by those skilled in the art that
Other embodiment.
The a series of detailed description of those listed above is only for illustrating for the possible embodiments of the present invention,
They simultaneously are not used to limit the scope of the invention, all Equivalent embodiments made without departing from skill spirit of the present invention or change
Should be included within the scope of the present invention.
Claims (13)
1. a kind of movable type is pyrolyzed consersion unit, it is characterised in that the equipment includes：
Pyrolytic reaction room, with for importing the material inlet and material outlet for deriving thermal decomposition product of material to be pyrolyzed；
Moving assembly, is arranged at the pyrolytic reaction chamber interior, and the moving assembly is used for the material to be pyrolyzed from described
Material inlet is transmitted to the material outlet；And
Thermal source bed body, the thermal source bed body is arranged at the pyrolytic reaction chamber interior, and the thermal source bed body includes and the movement
The first corresponding reaction surface of component and the second reaction surface, first, second reaction surface is separately positioned and possesses thing
Temperature conditionss needed for material pyrolysis, the moving assembly mobile material to be pyrolyzed on first reaction surface, and will
The material to be pyrolyzed is transferred to second reaction surface from first reaction surface, with second reaction surface
The mobile material to be pyrolyzed；
The moving assembly includes chain assemblies and at least two bearing wheels coordinated with the chain assemblies, the chain assemblies
Make gyration on first, second reaction surface, the bearing wheels include active bearing wheels, on the chain assemblies
It is provided with and scrape materials and parts for drive material movement to be pyrolyzed；
The thermal source bed body includes separately positioned the first thermal source bed body and Secondary Heat Source bed body, and the first thermal source bed body possesses
First reaction surface, the Secondary Heat Source bed body possesses second reaction surface；
The first thermal source bed body, Secondary Heat Source bed body possess respectively the first heat source passages for the heat source body that circulates, second hot
Source channels, the separate setting of first, second heat source passages；
The direction of motion of the circulating direction of the first thermal source bed body endogenous pyrogen body and material in the first thermal source bed body conversely,
The circulating direction of the Secondary Heat Source bed body endogenous pyrogen is consistent with the direction of motion of material in the Secondary Heat Source bed body；
Wherein, the moving assembly includes the Part I being located between material inlet and the first thermal source bed body, and positioned at first
Part II between thermal source bed body and Secondary Heat Source bed body.
2. portable pyrolysis consersion unit according to claim 1, it is characterised in that it is described scrape materials and parts including main part,
And the first wiper being disposed opposite to each other and the second wiper on the main part, first wiper drives to be waited to be pyrolyzed
Material is moved on first reaction surface, and second wiper drives material to be pyrolyzed on second reaction surface
Motion.
3. movable type according to claim 1 is pyrolyzed consersion unit, it is characterised in that accept in the Secondary Heat Source bed body
The end of material to be pyrolyzed extends beyond the active bearing wheels position.
4. movable type according to claim 3 is pyrolyzed consersion unit, it is characterised in that accept in the Secondary Heat Source bed body
The end of material to be pyrolyzed is provided with a deflector for being drained to material on the second reaction surface, and the deflector is located at institute
State side of the active bearing wheels away from the first thermal source bed body.
5. movable type according to claim 1 is pyrolyzed consersion unit, it is characterised in that the first thermal source bed body has heat
Tube portion is entered in source and thermal source goes out tube portion, the thermal source enter tube portion including the first pipeline, second pipe and be connected to first, the
The 3rd pipeline between two pipelines, the thermal source enters tube portion including the 4th pipeline, the 5th pipeline and is connected to the four, the 5th pipes
The 6th pipeline between road, the sidepiece of the second pipe, the 4th pipeline respectively from the first thermal source bed body stretches out, institute
State the first pipeline, the 5th pipeline height less than the moving assembly height.
6. movable type according to claim 1 is pyrolyzed consersion unit, it is characterised in that the stream of the first thermal source bed body endogenous pyrogen
The direction of motion of logical direction and material in the first thermal source bed body is conversely, the circulating direction of Secondary Heat Source bed body endogenous pyrogen is warm with second
The direction of motion of material is consistent in the bed body of source.
7. a kind of movable type is pyrolyzed consersion unit, it is characterised in that the equipment includes：
Pyrolytic reaction room, with for importing the material inlet and material outlet for deriving thermal decomposition product of material to be pyrolyzed；
The first thermal source bed body and the Secondary Heat Source bed body being placed in the pyrolytic reaction room, the first thermal source bed body possesses
One reaction surface, the Secondary Heat Source bed body possesses the second reaction surface, and first, second reaction surface possesses material pyrolysis
Required temperature conditionss；
Moving assembly, the moving assembly makees gyration in the pyrolytic reaction room, and the moving assembly includes being located at thing
Part I between material import and the first thermal source bed body, and second between the first thermal source bed body and Secondary Heat Source bed body
Part, moving assembly material to be pyrolyzed on first reaction surface, and by the material to be pyrolyzed from
First reaction surface is transferred to second reaction surface, to treat pyrogen described in mobile on second reaction surface
Material；
The moving assembly includes chain assemblies and at least two bearing wheels coordinated with the chain assemblies, the chain assemblies
Make gyration on first, second reaction surface, the bearing wheels include active bearing wheels, on the chain assemblies
It is provided with and scrape materials and parts for drive material movement to be pyrolyzed；
The first thermal source bed body, Secondary Heat Source bed body possess respectively the first heat source passages for the heat source body that circulates, second hot
Source channels, the separate setting of first, second heat source passages；
The direction of motion of the circulating direction of the first thermal source bed body endogenous pyrogen body and material in the first thermal source bed body conversely,
The circulating direction of the Secondary Heat Source bed body endogenous pyrogen is consistent with the direction of motion of material in the Secondary Heat Source bed body.
8. portable pyrolysis consersion unit according to claim 7, it is characterised in that it is described scrape materials and parts including main part,
And the first wiper being disposed opposite to each other and the second wiper on the main part, first wiper drives to be waited to be pyrolyzed
Material is moved on first reaction surface, and second wiper drives material to be pyrolyzed on second reaction surface
Motion.
9. movable type according to claim 7 is pyrolyzed consersion unit, it is characterised in that accept in the Secondary Heat Source bed body
The end of material to be pyrolyzed extends beyond the active bearing wheels position.
10. movable type according to claim 9 is pyrolyzed consersion unit, it is characterised in that hold in the Secondary Heat Source bed body
The end of reception pyrolysis material is provided with a deflector for being drained to material on the second reaction surface, and the deflector is located at
Side of the active bearing wheels away from the first thermal source bed body.
11. portable pyrolysis consersion units according to claim 7, it is characterised in that the first thermal source bed body has
Thermal source enters tube portion and thermal source goes out tube portion, the thermal source enter tube portion including the first pipeline, second pipe and be connected to first,
The 3rd pipeline between second pipe, the thermal source enters tube portion including the 4th pipeline, the 5th pipeline and is connected to the four, the 5th
The 6th pipeline between pipeline, the sidepiece of the second pipe, the 4th pipeline respectively from the first thermal source bed body stretches out,
First pipeline, the height of the 5th pipeline are less than the height of the moving assembly.
12. a kind of method for pyrolysis of portable pyrolysis consersion unit, it is characterised in that the pyrolytic reaction equipment includes that pyrolysis is anti-
The moving assembly answered room, the thermal source bed body in the pyrolytic reaction room and be engaged with the thermal source bed body, thermal source bed body
Including first reaction surface and second reaction surface corresponding with the moving assembly, methods described comprises the steps：
There is provided to the heat source body in the thermal source bed body internal circulation, to obtain the suitable thing on first, second reaction surface
The temperature conditionss of material pyrolytic reaction；
Start the motion of the moving assembly；
Material to be pyrolyzed is directed in the pyrolytic reaction room；
Material to be pyrolyzed is made into mobile concurrently raw pyrolytic reaction in first reaction surface；
Material to be pyrolyzed is transferred to into second reaction surface from first reaction surface；
Material to be pyrolyzed is made into mobile concurrently raw pyrolytic reaction in second reaction surface；
The product that pyrolytic reaction is obtained is derived to the outside of the pyrolytic reaction room；
Wherein, the moving assembly includes chain assemblies and at least two bearing wheels coordinated with the chain assemblies, the chain
Bar assembly makees gyration on first, second reaction surface, and the bearing wheels include active bearing wheels, the chain
It is provided with component and scrape materials and parts for drive material movement to be pyrolyzed；
Methods described also specifically includes following steps：
First thermal source bed body and Secondary Heat Source bed body are provided respectively, and it is anti-that the first, second thermal source bed body is placed in into pyrolysis
Should be indoor, the first thermal source bed body has first reaction surface, and the Secondary Heat Source bed body has second reaction
Surface；
Moving assembly is placed in into the relevant position in the pyrolytic reaction room, to guarantee that the moving assembly can be first, second
Reaction surface makees gyration, wherein, moving assembly include the Part I with the first reaction surface phase separation and with institute
State the Part II of the second reaction surface phase separation, the Part I be located at the material inlet of the pyrolytic reaction room with it is described
Between first thermal source bed body, the Part II is located between the first thermal source bed body and the Secondary Heat Source bed body；
Methods described also specifically includes following steps：
Respectively in the first, second thermal source bed body internal circulation thermal source, wherein, the circulating direction of the first thermal source bed body endogenous pyrogen
With the direction of motion of material in the first thermal source bed body conversely, the circulating direction of Secondary Heat Source bed body endogenous pyrogen and Secondary Heat Source bed body
The direction of motion of upper material is consistent.
The method for pyrolysis of 13. portable pyrolysis consersion units according to claim 12, it is characterised in that described to wait to be pyrolyzed
Material includes one or more in damaged tire, rubber, plastics, other organic waste materials.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410016598.3A CN104772103B (en) | 2014-01-14 | 2014-01-14 | Mobile pyrolysis reaction device and pyrolysis method |
| US14/194,730 US20150197692A1 (en) | 2014-01-14 | 2014-03-01 | Moving pyrolyzing apparatus and method for applying the apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410016598.3A CN104772103B (en) | 2014-01-14 | 2014-01-14 | Mobile pyrolysis reaction device and pyrolysis method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104772103A CN104772103A (en) | 2015-07-15 |
| CN104772103B true CN104772103B (en) | 2017-04-26 |
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ID=53520800
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410016598.3A Active CN104772103B (en) | 2014-01-14 | 2014-01-14 | Mobile pyrolysis reaction device and pyrolysis method |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US20150197692A1 (en) |
| CN (1) | CN104772103B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105778955A (en) * | 2016-05-19 | 2016-07-20 | 杨中光 | Dynamic continuous organic solid waste gas-carbon oil cogeneration device |
| KR20230066548A (en) | 2020-09-14 | 2023-05-16 | 에코랍 유에스에이 인코퍼레이티드 | Cold Flow Additives for Plastic-Derived Synthetic Feedstocks |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1522985A (en) * | 1921-02-14 | 1925-01-13 | George A Taff | Apparatus for extracting petroleum from shale and other minerals |
| US2335611A (en) * | 1941-09-03 | 1943-11-30 | Pray Res Corp | Apparatus for heat treating oil shale and other finely divided materials |
| JPH09291284A (en) * | 1996-04-26 | 1997-11-11 | Chiyuugai Technos Kk | Apparatus for treating waste vinyl chloride resin |
| CA2196841C (en) * | 1997-02-05 | 2001-04-03 | Christian Roy | Horizontal moving and stirred bed reactor |
| EP1217318A1 (en) * | 2000-12-19 | 2002-06-26 | Sea Marconi Technologies Di Wander Tumiatti S.A.S. | Plant for the thermal treatment of material and operation process thereof |
| MX2012000737A (en) * | 2009-07-17 | 2012-03-26 | Advanced Pyrotech Sdn Bhd | An apparatus for decomposing rubber products through pyrolysis. |
| CN202016986U (en) * | 2011-03-18 | 2011-10-26 | 刘建波 | Continuous cracking device for waste plastics |
| CN202558808U (en) * | 2012-03-28 | 2012-11-28 | 刘建波 | Chain scrapper plate type heat cracking device of waste rubber |
-
2014
- 2014-01-14 CN CN201410016598.3A patent/CN104772103B/en active Active
- 2014-03-01 US US14/194,730 patent/US20150197692A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| CN104772103A (en) | 2015-07-15 |
| US20150197692A1 (en) | 2015-07-16 |
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