CN205974389U - Heat accumulation formula removes bed pyrolysis and cracking reactor - Google Patents

Heat accumulation formula removes bed pyrolysis and cracking reactor Download PDF

Info

Publication number
CN205974389U
CN205974389U CN201620456530.1U CN201620456530U CN205974389U CN 205974389 U CN205974389 U CN 205974389U CN 201620456530 U CN201620456530 U CN 201620456530U CN 205974389 U CN205974389 U CN 205974389U
Authority
CN
China
Prior art keywords
reactor
pyrolysis
cracking
heat
communication
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201620456530.1U
Other languages
Chinese (zh)
Inventor
耿层层
陈水渺
肖磊
薛逊
吴道洪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shenwu Technology Group Corp Co Ltd
Original Assignee
Beijing Shenwu Environmental and Energy Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Beijing Shenwu Environmental and Energy Technology Co Ltd filed Critical Beijing Shenwu Environmental and Energy Technology Co Ltd
Priority to CN201620456530.1U priority Critical patent/CN205974389U/en
Application granted granted Critical
Publication of CN205974389U publication Critical patent/CN205974389U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model provides a pyrolysis and cracking reactor, include: feed inlet, pyrolysis chamber, splitting chamber, regenerative radiant tube and cracked gas outlet still include: thermal -insulated brick wall, thermal -insulated brick wall setting is in 23 departments of the horizontal width of reactor, run through vertically in reactor will the inside space separation of reactor becomes the pyrolysis chamber with splitting chamber, communication member, communication member sets up in the lower part of thermal -insulated brick wall, be used for with the oil gas that the pyrolysis chamber produced, through communication member lets in splitting chamber. The oil gas that this reactor pyrolysis chamber produced can get into splitting chamber and carry out deep cracking, is the gaseous hydrocarbons of micro molecule with the burnt oil molecules schizolysis of macromolecule, and this reactor can produce a large amount of cracking gases to avoid the problem of production pyrolysis oil dust -laden, really realized fossil fuel's clean high -efficient utilization. In addition, can carry out two kinds of operations in the furnace body, unite two into one, save construction cost and area.

Description

A kind of thermal storage type moving bed pyrolysis and cracking reactor
Technical field
This utility model belongs to the pyrolysis of Fossil fuel and cracking technique field and in particular to one kind is mainly for oil shale Thermal storage type moving bed pyrolysis with resources such as coals and cracking reactor, are used for producing combustible gas and semicoke product.
Background technology
World today's petroleum resources gradually decreases, increasingly deficient, China more so it is necessary to rely on substantial amounts of imported crude oil, this It is related to national energy security problem.However, China has very abundant oil shale and coal resources, the heat of current China Solution shale oil yield ranks first in the world, and has the trend increasing year by year.Existing oil shale and coal pyrolysis type of furnace master There are Fushun stove, three river gas combustion side stoves, the solid heat carrier retort of big work, the Ge Luote of Ai Shaniya(Galoter)Stove, The ATP stove of Australia and American Association oil company gas retort etc..Existing pyrolysis the type of furnace all to produce oil product as main purpose, But mostly it is pyrolyzed the type of furnace, especially to process the type of furnace as raw material for the fine coal, in pyrolysis oil, contains a large amount of dirt, cause pyrolysis oil difficult With effectively utilizes, be pyrolyzed oil value high the problems such as.Therefore, a kind of high-effective dust-removing, system structure and technological process how are designed All simple reactor becomes the problem of this area urgent need to resolve.
Utility model content
This utility model is directed to the deficiencies in the prior art, designs and develop a kind of pyrolysis and cracking reactor, this reaction In device integration devise pyrolysis chamber and cracking room, the oil gas that pyrolysis chamber produces, cracking room can be entered and carry out deep pyrolytic, The tar molecules of macromole are cracked into the gaseous hydrocarbons of small molecule, thus avoiding the problem producing pyrolysis oil dust-laden, really The clean and effective achieving Fossil fuel utilizes.
For solving above-mentioned technical problem, the technical solution adopted in the utility model is:
This utility model provides a kind of pyrolysis and cracking reactor.According to embodiment of the present utility model, this reactor Including:Charging aperture, pyrolysis chamber, cracking room and cracking gas outlet, described charging aperture is arranged on the roof of described pyrolysis chamber, described Cracking gas outlet is arranged on the side wall of described cracking room it is characterised in that also including:Heat accumulation type radiant tube, described heat accumulating type Radial canal along described reactor short transverse multi-tier arrangement inside described pyrolysis chamber and described cracking room, every layer has many The described heat accumulation type radiant tube arranged in the horizontal direction;Heat-insulated brick wall, it is laterally wide that described heat-insulated brick wall is arranged on described reactor At the 2/3 of degree, vertically through in described reactor, the inner space of described reactor is separated into described pyrolysis chamber and institute State cracking room;Communication member, described communication member is arranged on the bottom of heat-insulated brick wall, for the oil producing described pyrolysis chamber Gas, by described communication member, is passed into described cracking room.
Inventor finds, the system structure of the reactor according to this utility model embodiment is simple, easy to operate, pyrolysis chamber The oil gas producing, can enter cracking room and carry out deep pyrolytic, the tar molecules of macromole are cracked into the gaseous hydrocarbon of small molecule Class, this reactor can produce substantial amounts of cracking gas, thus avoiding the problem producing pyrolysis oil dust-laden, is truly realized fossil combustion The clean and effective of material utilizes.Additionally, two kinds of operations can be carried out in a body of heater, unite two into one, save construction cost and take up an area face Long-pending, and, this reactor employs heat accumulation type radiant tube heating technique without gas, solid heat carrier heating, improves reactor System process is simplified while the thermal efficiency.
According to embodiment of the present utility model, described communication member is the multiple hole of inclusion being arranged on described heat-insulated brick wall Pore area.
According to embodiment of the present utility model, described communication member is on described heat-insulated brick wall longitudinal length, positioned at bottom The opening of position.
According to embodiment of the present utility model, the thickness of described heat-insulated brick wall is 5-15cm.
According to embodiment of the present utility model, the height of described pore area is 3-15cm.
According to embodiment of the present utility model, a diameter of 1-3cm in described hole.
According to embodiment of the present utility model, the height of described opening is 3-15cm.
According to embodiment of the present utility model, hopper is connected with described charging aperture by feed arrangement.
According to embodiment of the present utility model, further include that semicoke exports, described semicoke outlet is arranged on described pyrolysis The bottom of room, described semicoke outlet is connected with described semicoke conveyer device.
The beneficial effects of the utility model are:
1)Reactor is divided into pyrolysis chamber and cracking room, the oil gas that pyrolysis chamber produces, and can carry out deep pyrolytic in cracking room, greatly The tar molecules of molecule are cracked into the gaseous hydrocarbons of small molecule, fuel gas yield is high, it is to avoid the problem of pyrolysis oil dust-laden, very The clean and effective just achieving Fossil fuel utilizes.
2)Two kinds of operations can be carried out in one body of heater, unite two into one, save construction cost and floor space.
3)Pyrolysis gas calorific value is high, quality better.
4)Take heat accumulation type radiant tube heat supply, response system structure is simple, easy to operate, uniformity of temperature profile, heating effect Really good.
Brief description
Fig. 1 is the structure chart of this utility model pyrolysis and cracking reactor.
Fig. 2 is the front view of the heat-insulated brick wall of this utility model.
Wherein, 1, hopper;2nd, feed arrangement;3rd, pyrolysis chamber;310th, cracking gas outlet;320th, charging aperture;330th, semicoke goes out Mouthful;340th, heat accumulation type radiant tube;4th, cracking room;5th, heat-insulated brick wall;510th, communication member;6th, semicoke conveyer device;7th, combustion gas enters Mouthful;8th, exhanst gas outlet;9th, air intake;10th, source of the gas.
Specific embodiment
In order that those skilled in the art more fully understand the technical solution of the utility model, with reference to specific embodiment The utility model is described in further detail.The embodiments described below is exemplary, is only used for explaining that this practicality is new Type, and it is not intended that to restriction of the present utility model.Unreceipted particular technique or condition in embodiment, according in the art The technology described by document or condition or carry out according to product description.
According to one side of the present utility model, this utility model provides a kind of thermal storage type moving bed pyrolysis and cracking is anti- Answer device, Fig. 1 is the structure chart of this pyrolysis and cracking reactor, as shown in figure 1, reactor includes charging aperture 320, pyrolysis chamber 3, splits Solution room 4, cracking gas outlet 310, heat accumulation type radiant tube 340, heat-insulated brick wall 5 and communication member 510, wherein, described charging aperture sets Put on the roof of described pyrolysis chamber, described cracking gas outlet is arranged on the side wall of described cracking room, and described heat-insulated brick wall erects Directly through in reactor, the inner space of reactor is separated into pyrolysis chamber and cracking room, described communication member is arranged on On described heat-insulated brick wall, pyrolysis chamber is connected it is preferred that described communication member is arranged on the bottom of heat-insulated brick wall with cracking room, The oil gas that pyrolysis chamber is produced, by communication member, is passed into cracking room.
Inventor finds, this system structure setting reactor according to this utility model embodiment is simply, easy to operate, hot The oil gas that solution room produces, can enter cracking room and carry out deep pyrolytic, the tar molecules of macromole are cracked into the gas of small molecule State hydro carbons, this reactor can produce substantial amounts of cracking gas, thus avoiding the problem producing pyrolysis oil dust-laden, being truly realized The clean and effective of stone fuel utilizes.Additionally, this reactor employs heat accumulation type radiant tube heating technique adding without gas, solid heat carrier Heat, simplifies system process while the thermal efficiency that improve reactor.
According to specific embodiment of the utility model it is adaptable to the concrete species of pyrolysis material of this reactor and particle diameter are not subject to Especially limit, according to embodiment of the present utility model, be pyrolyzed material can be the Fossil fuels such as oil shale, coal or rubbish, Mud, junked tire etc., pyrolysis material can also be pyrolyzed material for little particle for block pyrolysis material, more of the present utility model In preferred embodiment, the pyrolysis that this reactor adopts is expected for particle diameter 20mm particles below and powdery Fossil fuel, thus, it is possible to Make full use of little particle pyrolysis material, resource utilization is high, and can solve the problem that bulk deposition pollutes the problem of environment.
According to specific embodiment of the utility model it is adaptable to the type of furnace of this reactor is not particularly limited, can be to store Hot type moving bed can also be other types, such as non-heat accumulating type or non-moving type etc., as long as can be by heat-insulated brick wall integration It is divided into pyrolysis chamber and cracking room.
According to specific embodiment of the utility model, heat-insulated brick wall is arranged in reactor it is preferred that being located at reactor horizontal stroke To at the 2/3 of width, the thickness of heat-insulated brick wall is 5-15cm, heat-insulated brick wall vertically through in reactor, by reactor Inner space is separated into pyrolysis chamber and cracking room, and this structure makes to be provided with pyrolysis chamber and cracking room in a body of heater, pyrolysis The oil gas that room produces, can enter cracking room and carry out deep pyrolytic, the tar molecules of macromole are cracked into the gaseous state of small molecule Hydro carbons, produces substantial amounts of cracking gas, thus avoiding the problem producing pyrolysis oil dust-laden.And, two can be carried out in a body of heater Plant operation, unite two into one, save construction cost and floor space.
According to specific embodiment of the utility model, the concrete species of communication member is not particularly limited, as long as can be by Pyrolysis chamber connects with cracking room, thus the oil gas that pyrolysis chamber is produced is passed into cracking room.More of the present utility model In embodiment, when Fig. 2 is in terms of the from left to right of reactor, the front view of heat-insulated brick wall, as shown in Fig. 2 communication member can be It is arranged on the pore area in the multiple holes of inclusion on heat-insulated brick wall, under preferable case, the height of described pore area is 3-15cm, described hole A diameter of 1-3cm.Communication member can also be on heat-insulated brick wall longitudinal length, positioned at the opening of lower position, under preferable case, The height of described opening is 3-15cm.
According to specific embodiment of the utility model, as shown in figure 1, described charging aperture is arranged on the roof on pyrolysis chamber top On, hopper 1 is connected with described charging aperture by feed arrangement 2;The concrete species of feed arrangement is not particularly limited, as long as permissible Pyrolysis material in hopper is effectively delivered in reactor.In some embodiments of the present utility model, feed arrangement Can be star feeder or feed screw.Thereby, it is possible to realize the Automatic Conveying to pyrolysis material, conveying capacity is controlled, and Device structure is simple, easy to operate.
According to specific embodiment of the utility model, as shown in figure 1, reactor further comprises semicoke outlet 330, institute State the bottom that semicoke outlet is arranged on described pyrolysis chamber, described semicoke outlet is connected with described semicoke conveyer device 6.Thus, may be used The semicoke obtaining in reactor to be conveyed using semicoke conveyer device.The concrete species of semicoke conveyer device 6 is not subject to spy Do not limit, including but not limited to star or feed screw.Thereby, it is possible to realize the Automatic Conveying to semicoke, and conveying capacity Controlled, device structure is simple, easy to operate.
According to specific embodiment of the utility model, described inside reactor has the short transverse along described reactor for the multilamellar Be arranged in the heat accumulation type radiant tube within described pyrolysis chamber and described cracking room, every layer of heat accumulation type radiant tube can include multiple that The heat accumulation type radiant tube of this parallel and horizontally spaced distribution.According to embodiment of the present utility model, described pyrolysis chamber and Cracking interior distributed at least one described heat accumulation type radiant tube respectively it is preferred that described at least one heat accumulation type radiant tube is equal Even distribution.Heat accumulation type radiant tube can be heated so as to be pyrolyzed effective for the oil gas indoor to pyrolysis material and cracking And cracking reaction, specifically, combustible gas and air can be passed through into heat accumulation type radiant tube, so that combustible gas is burnt and realize to pyrolysis The heating function of material.This equipment adopts heat accumulation type radiant tube heating technique, and without gas, the heating of solid heat carrier, pyrolysis gas will not be by Dilution, calorific value is high, and reactor temperature is evenly distributed, and surface temperature difference is little, and exhaust gas temperature is low, and the thermal efficiency is high, improves reaction System process is simplified, response system structure is simple, easy to operate while the thermal efficiency of device.
In described reactor, pyrolysis material moves from top to bottom, and in described reactor, the heat accumulation type radiant tube of setting is permissible Pyrolysis material is broken up makes it be uniformly distributed, and pyrolysis material stops 1-30 minute in the reactor from top to bottom, and is heated to 500-600 ℃.According to embodiment of the present utility model, the shape of heat accumulation type radiant tube is not particularly limited, in some realities of the present utility model Apply in example, can be cylinder, thus be conducive to being pyrolyzed breaing up of material, realize uniform point in the reactor of mixed pyrolysis material Dissipate.The level interval of radial canal is 200-500mm, and vertical interval is 200-700mm, and the radial canal number of plies is 10-25 layer, reactor Width is 2-6m, and height for reactor is 3-20m.In addition, heat accumulation type radiant tube can be the unidirectional heat accumulating type radiation being evenly arranged Pipe, the temperature of tube wall can control in 450-1000 DEG C of scope by gas control valve, and heat accumulation type radiant tube can be taken periodically The combustion system of commutation, so that the surface temperature difference of single heat accumulation type radiant tube only has 30 DEG C about, does not have area of localized hyperthermia, by This, be conducive to improving the thermal efficiency.
According to specific embodiment of the utility model, described reactor is provided with fuel gas inlet 7, air intake 9 and flue gas Outlet 8, wherein, fuel gas inlet and exhanst gas outlet are connected with heat accumulation type radiant tube respectively, are respectively used to be passed through combustible gas and discharge Flue gas, air intake is connected with source of the gas 10 and heat accumulation type radiant tube respectively, and the air for producing source of the gas is passed through heat accumulating type spoke Penetrate in pipe.
In other side of the present utility model, this utility model provides one kind to be carried out using foregoing reactor Pyrolysis and the method for cracking.According to embodiment of the present utility model, the method may comprise steps of:
A. pyrolysis material is added in described reactor by the charging aperture on reactor top, in the pyrolysis of described reactor Pyrolytic process is completed in room.Wherein, described pyrolysis material is added to reactor from the charging aperture on reactor top, and by reactor Interior heat accumulation type radiant tube is broken up, and pyrolysis char is discharged from the semicoke outlet of reactor bottom, and through semicoke conveyer device(Preferably Conveying worm)Discharge.
According to embodiment of the present utility model, the concrete species of pyrolysis material and particle diameter are not particularly limited, and pyrolysis material is permissible It is the Fossil fuels such as oil shale, coal or rubbish, mud, junked tire etc., pyrolysis material can also may be used for block pyrolysis material Think little particle pyrolysis material, in some preferred embodiments of the present utility model, the pyrolysis that this reactor adopts is expected for particle diameter 20mm particles below and powdery Fossil fuel, thus, it is possible to make full use of little particle pyrolysis material, resource utilization is high, and energy Enough solve the problems, such as bulk deposition pollution environment.
According to embodiment of the present utility model, in the pyrolysis chamber of reactor, the heat accumulation type radiant tube of setting can be by pyrolysis material Break up and so that it is uniformly distributed, pyrolysis material stops 1-30 minute in the reactor from top to bottom, and pyrolysis material is by reactor pyrolysis chamber Heat accumulation type radiant tube be heated to 500-600 DEG C, specifically, can by gas valve control heat accumulation type radiant tube tube wall temperature For 450-750 DEG C, pyrolysis material is heated to rapidly 500-600 DEG C in the reactor, completes pyrolytic process.
B. it is pyrolyzed the oil gas of generation, by the communication member of setting on the heat-insulated brick wall of described reactor, enter into described anti- Answer the cracking room of device.
According to embodiment of the present utility model, heat-insulated brick wall is arranged in reactor it is preferred that to be located at reactor laterally wide At the 2/3 of degree, the thickness of heat-insulated brick wall is 5-15cm, heat-insulated brick wall vertically through in reactor, by the inside of reactor Space is separated into pyrolysis chamber and cracking room, and this structure makes to be provided with pyrolysis chamber and cracking room in a body of heater, and is produced from pyrolysis chamber Raw oil gas, can enter cracking room and carry out deep pyrolytic, the tar molecules of macromole are cracked into the gaseous hydrocarbons of small molecule. Thus, two kinds of operations can be carried out in a body of heater, unite two into one, save construction cost and floor space.According to this utility model Embodiment, communication member can be the inclusion pore area in multiple holes being arranged on heat-insulated brick wall or heat-insulated brick wall is indulged To in length, positioned at the opening of lower position.Specifically, the oil gas that pyrolysis produces, by the hole of reactor heat-insulated brick wall bottom Band or opening, enter into cracking room.
C. the oil gas being pyrolyzed generation completes thermal cracking processes in described cracking interior, produces cracking gas.
According to embodiment of the present utility model, described cracking interior distributed at least one described heat accumulation type radiant tube, excellent Choosing, described at least one heat accumulation type radiant tube is uniformly distributed.Heat accumulation type radiant tube can be effective for the oil indoor to cracking Gas is heated so as to be carried out cracking reaction.Specifically, pyrolysis oil gas is heated by the heat accumulation type radiant tube in reactor cracking room To 650-900 DEG C, specifically, can be 450-1000 DEG C by the temperature that gas valve controls heat accumulation type radiant tube tube wall, pyrolysis Material is heated to rapidly 650-900 DEG C in the reactor, completes thermal cracking processes, thus, the tar molecules of macromole are cracked into The gaseous hydrocarbons of small molecule, produces substantial amounts of cracking gas, it is to avoid the problem of pyrolysis oil dust-laden, is truly realized Fossil fuel Clean and effective utilizes.
D. described cracking gas is exported by cracking gas and discharges.
According to embodiment of the present utility model, cracking gas outlet is arranged on the side wall on reactor cracking room top, and it can To be connected with outside gas treatment and collection device(Not shown), such as spray column, fuel cartridge etc..For purifying and collecting cracking Gas, to prepare LNG or LPG.
Inventor finds, the oil gas being produced according to the method for this utility model embodiment, pyrolysis chamber, can enter cracking Room carries out deep pyrolytic, the tar molecules of macromole is cracked into the gaseous hydrocarbons of small molecule, and this reactor can produce substantial amounts of Cracking gas, thus avoiding the problem producing pyrolysis oil dust-laden, the clean and effective being truly realized Fossil fuel utilizes, meanwhile, Two kinds of operations can be carried out in one body of heater, unite two into one, save construction cost and floor space.
Using thermal storage type moving bed pyrolysis and cracking reactor, Korea's oil shale is processed, the basic data of raw material is shown in Table 1.
Table 1:Korea's oil shale basic data
Using this reactor for treatment Korea oil shale, the gas products yield obtaining is 16%, far above laboratory aluminum rice steamer heat Factor of created gase obtained by solution, pyrolytic tar almost all is cracked into gaseous products, and factor of created gase is high.Cracking gas calorific value is up to 5000kcal/m3, quality is high.
It is to be understood that term " first ", " second " are only used for describing purpose in description of the present utility model, and It is not intended that instruction or hint relative importance or the implicit quantity indicating indicated technical characteristic.Thus, define The feature of " first ", " second " can be expressed or implicitly include one or more this feature.
In this utility model, unless otherwise clearly defined and limited, term " installation ", " being connected ", " connection ", " Gu Fixed " etc. term should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected or integral;Can be It is mechanically connected or electrically connect;Can be to be joined directly together it is also possible to be indirectly connected to by intermediary, can be two The connection of element internal or the interaction relationship of two elements.For the ordinary skill in the art, can basis Concrete condition understands concrete meaning in this utility model for the above-mentioned term.
In this utility model, unless otherwise clearly defined and limited, fisrt feature second feature " on " or D score Can be the first and second feature directly contacts, or the first and second features pass through intermediary mediate contact.And, first is special Levy second feature " on ", " top " and " above " but fisrt feature directly over second feature or oblique upper, or only Represent that fisrt feature level height is higher than second feature.Fisrt feature second feature " under ", " lower section " and " below " permissible Be fisrt feature immediately below second feature or obliquely downward, or be merely representative of fisrt feature level height and be less than second feature.
In the description of this specification, reference term " embodiment ", " some embodiments ", " example ", " specifically show The description of example " or " some examples " etc. means specific features, structure, material or the spy describing with reference to this embodiment or example Point is contained at least one embodiment of the present utility model or example.In this manual, the schematic table to above-mentioned term State that be not necessarily referring to is identical embodiment or example.And, the specific features of description, structure, material or feature can be Combine in an appropriate manner in any one or more embodiments or example.Additionally, in the case of not conflicting, this area Technical staff the feature of the different embodiments described in this specification or example and different embodiment or example can be entered Row combines and combines.
Although of the present utility model embodiment has been shown and described above it is to be understood that above-described embodiment is Exemplary it is impossible to be interpreted as that those of ordinary skill in the art is in scope of the present utility model to restriction of the present utility model Interior above-described embodiment can be changed, change, replacing and modification, simultaneously for one of ordinary skill in the art, foundation The thought of the application, all will change in specific embodiments and applications.

Claims (9)

1. a kind of pyrolysis and cracking reactor, including the outlet of charging aperture, pyrolysis chamber, cracking room and cracking gas, described charging aperture sets Put on the roof of described pyrolysis chamber, described cracking gas outlet is arranged on the side wall of described cracking room it is characterised in that also wrapping Include:
Heat accumulation type radiant tube, described heat accumulation type radiant tube along described reactor short transverse multi-tier arrangement in described pyrolysis chamber and Inside described cracking room, every layer has the many described heat accumulation type radiant tubes arranged in the horizontal direction;
Heat-insulated brick wall, described heat-insulated brick wall is arranged at the 2/3 of described reactor transverse width, vertically through in described reaction In device, the inner space of described reactor is separated into described pyrolysis chamber and described cracking room;
Communication member, described communication member is arranged on the bottom of heat-insulated brick wall, for the oil gas producing described pyrolysis chamber, passes through Described communication member, is passed into described cracking room.
2. reactor according to claim 1 is it is characterised in that described communication member is to be arranged on described heat-insulated brick wall Inclusion multiple holes pore area.
3. reactor according to claim 1 is it is characterised in that described communication member is described heat-insulated brick wall longitudinal length On, positioned at the opening of lower position.
4. reactor according to claim 2 is it is characterised in that the thickness of described heat-insulated brick wall is 5-15cm.
5. reactor according to claim 2 is it is characterised in that the height of described pore area is 3-15cm.
6. reactor according to claim 2 is it is characterised in that a diameter of 1-3cm in described hole.
7. reactor according to claim 3 is it is characterised in that the height of described opening is 3-15cm.
8. the reactor according to any one of claim 1-7 it is characterised in that hopper pass through feed arrangement with described enter Material mouth is connected.
9. the reactor according to any one of claim 1-7 is it is characterised in that further including that semicoke exports, described Semicoke outlet is arranged on the bottom of described pyrolysis chamber, and described semicoke outlet is connected with described semicoke conveyer device.
CN201620456530.1U 2016-05-19 2016-05-19 Heat accumulation formula removes bed pyrolysis and cracking reactor Active CN205974389U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620456530.1U CN205974389U (en) 2016-05-19 2016-05-19 Heat accumulation formula removes bed pyrolysis and cracking reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620456530.1U CN205974389U (en) 2016-05-19 2016-05-19 Heat accumulation formula removes bed pyrolysis and cracking reactor

Publications (1)

Publication Number Publication Date
CN205974389U true CN205974389U (en) 2017-02-22

Family

ID=58019581

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620456530.1U Active CN205974389U (en) 2016-05-19 2016-05-19 Heat accumulation formula removes bed pyrolysis and cracking reactor

Country Status (1)

Country Link
CN (1) CN205974389U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105838404A (en) * 2016-05-19 2016-08-10 北京神雾环境能源科技集团股份有限公司 Heat accumulating type moving bed pyrolysis and catalytic cracking reactor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105838404A (en) * 2016-05-19 2016-08-10 北京神雾环境能源科技集团股份有限公司 Heat accumulating type moving bed pyrolysis and catalytic cracking reactor

Similar Documents

Publication Publication Date Title
CN205974389U (en) Heat accumulation formula removes bed pyrolysis and cracking reactor
CN205974388U (en) Oil shale pyrolysis and catalytic cracking system
CN205974391U (en) From oil shale pyrolysis of dust removal type and cracking system
CN205974396U (en) Heat accumulation formula removes bed pyrolysis and pyrolysis tube cracking reactor
CN206143120U (en) From pyrolysis of dust removal type and cracking reactor
CN205974373U (en) Syngas system is produced in pyrolysis of coal and pyrolysis tube schizolysis
CN205974374U (en) Syngas system is produced in pyrolysis of coal and schizolysis
CN205974375U (en) Syngas system is produced to pyrolysis of coal and catalytic cracking
CN205974387U (en) Oil shale pyrolysis and pyrolysis tube system
CN205974386U (en) Oil shale pyrolysis and cracking system
CN205974443U (en) Gas combination gas electricity generation system is produced in pyrolysis of coal and pyrolysis tube schizolysis
CN205974444U (en) Gas electricity generation system is united to pyrolysis of coal and schizolysis product gas
CN105802685B (en) A kind of pyrolysis of coal and cracking tube cracking produce gas and combine gas power generation system
CN205974382U (en) Produce syngas system from pyrolysis of dust removal moulded coal and schizolysis
CN205974371U (en) Living beings pyrolysis and catalytic cracking system
CN105838404A (en) Heat accumulating type moving bed pyrolysis and catalytic cracking reactor
CN205974370U (en) Living beings pyrolysis and pyrolysis tube cracking system
CN206051946U (en) One kind is from dedusting type oil shale pyrolysis and catalytic cracking system
CN105885898B (en) One kind is pyrolyzed from dedusting type and catalytic cracking reaction device
CN205974393U (en) Junked tire pyrolysis and pyrolysis tube cracking system
CN205974369U (en) Living beings pyrolysis and cracking system
CN205974392U (en) Junked tire pyrolysis and cracking system
CN205974390U (en) Heat accumulation formula removes bed pyrolysis and catalytic cracking reactor
CN206051945U (en) It is a kind of to be pyrolyzed from dedusting type and cracking tube cracking reactor
CN105838460A (en) Coal pyrolysis and cracking gas production combined gas power generation system

Legal Events

Date Code Title Description
GR01 Patent grant
C14 Grant of patent or utility model
CP03 Change of name, title or address

Address after: 102200 Beijing City, Changping District science and Technology Park Chang Huai Lu No. 155

Patentee after: Shenwu science and technology group Limited by Share Ltd

Address before: 102200 Beijing City, Changping District Changping District Machi Town kamis Road No. 18

Patentee before: Beijing Shenwu Environment Energy Technology Group Co., Ltd.

CP03 Change of name, title or address
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Heat accumulating type moving bed pyrolysis and catalytic cracking reactor

Effective date of registration: 20180327

Granted publication date: 20170222

Pledgee: Tianfeng securities Limited by Share Ltd

Pledgor: Shenwu science and technology group Limited by Share Ltd

Registration number: 2018990000230

PE01 Entry into force of the registration of the contract for pledge of patent right
PP01 Preservation of patent right

Effective date of registration: 20190121

Granted publication date: 20170222

PP01 Preservation of patent right