CN106635099A - Waste tire vacuum cracking system - Google Patents
Waste tire vacuum cracking system Download PDFInfo
- Publication number
- CN106635099A CN106635099A CN201611178080.5A CN201611178080A CN106635099A CN 106635099 A CN106635099 A CN 106635099A CN 201611178080 A CN201611178080 A CN 201611178080A CN 106635099 A CN106635099 A CN 106635099A
- Authority
- CN
- China
- Prior art keywords
- cracking
- gas
- flue gas
- cylinder
- tracheae axle
- 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.)
- Pending
Links
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
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0217—Separation of non-miscible liquids by centrifugal force
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
-
- 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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/502—Carbon monoxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
-
- 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
Abstract
The invention belongs to the technical field of waste tire cracking and particularly relates to a waste tire vacuum cracking system. The waste tire vacuum cracking system comprises a cracking roller, a hearth, a feeding gate, a cracking gas tube shaft, a drive gear, a connecting bearing, a cracking gas treating and recycling system and a fuel flue gas treating system. Solid carbon particles discharged after coal is burnt can be recycled and stored to be reused, the solid carbon particles are prevented from being deposited at the bottom of desulfurization equipment, fuel is saved, and following flue gas purification work is not affected. Hydrocarbon gas can be separated from cracking gas, the hydrocarbon gas serves as fuel, the burning effect is good, the heat value is high, and energy is saved. The interiors of blocky tires are fully cracked in the cracking process, and the reaction efficiency and the reaction effect are improved. After cracking is completed, water cooling is directly used for cooling, the cooling time is shortened, and the working efficiency is improved. The situation that carbon black particles escape to be turned into impurities in the cracking gas can be avoided.
Description
Technical field
The invention belongs to junked tire cracking technique field, and in particular to a kind of junked tire vacuum cracking system.
Background technology
With the fast development of automobile industry, the quantity of junked tire is also on the increase.Substantial amounts of junked tire is piled up,
It is not degradable under natural environment, cause to take a large amount of land resources, it is also easy to pollute environment, residents ' health is endangered, so needing
Junked tire is recycled.Junked tire is reclaimed mainly to heat in the environment of anaerobic or anoxic and cracked, and is taken off
Go out volatile materials, form solid carbon, realize resource reutilization.At present, junked tire cracking majority used is swinging envelope
The pyrolysis furnace for closing, it is difficult to it was observed that the response situation of furnace interior, can only determine the junked tire in stove with time and experience
Whether react complete, after blow-on, usually also have block tire not react abundant, in causing wastage of material, and tire
Steel wire distribution is not concentrated, and easily scratches staff.In cracking process, generally cracking stove heat, coal combustion are given using fire coal
After produce a large amount of flue gases, wherein the solid particle containing carbon, sour gas and for clean-burning carbon monoxide etc., these meetings
Serious harm is caused to environment, and the solid particle that junked tire recovery plant then thinks little of carbon is reclaimed, and realizes that resource is fully sharp
With.When the solid particle of carbon touches the liquid in release unit, release unit bottom can be deposited on, be difficult to discharge.Cracking gas
After generation, pyrolysis furnace separation and recovery can be discharged, but cracking gas can carry a part of particle carbon black and discharge pyrolysis furnace, cause raw material
Waste, and increase the impurity of the cracked oil isolated in cracking gas, reduce cracking oil quality.Can be left after cracking gas separating treatment
Substantial amounts of flammable hydrocarbon gas, but contain some impurity in gas, and being passed directly into hearth combustion can affect flammable hydrocarbon gas
Burning, cause burning it is insufficient.After cracking terminates, need to lower the temperature to pyrolysis furnace, prevent from scalding staff, traditional method
It is the heat that furnace body outer wall is constantly taken away by air exhauster exhausting, such cooling method is slow, and efficiency is low, high energy consumption.
The content of the invention
To solve the problems, such as above technology, the present invention provides a kind of junked tire vacuum cracking system, can reclaim storage
The solid carbon particles discharged after coal combustion are deposited, the hydrocarbon gas in cracking gas can be utilized to do fuel, the hydrocarbon gas of recovery are not contained
Impurity, combustion efficiency is good.
Its technical scheme is：
A kind of junked tire vacuum cracking system, including cracking cylinder, burner hearth, feeding gate, cracking tracheae axle, travelling gear, company
Joint bearing, cracking gas disposal recovery system and fuel smoke processing system, the cracking cylinder is arranged in burner hearth, sets on burner hearth
Feeding screw is equipped with, burner hearth top is provided with fuel smoke processing system, and the cracking cylinder side is provided with feeding gate, splits
Solution cylinder opposite side is connected to crack tracheae axle, and cracking tracheae axle is connected to crack gas disposal recovery system by connecting bearing,
Travelling gear is fixedly installed on the cracking tracheae axle；
The cracking gas disposal recovery system sets including centrifugal oil-water separator, cooler bin, water washing device, recovery tube and oxygen supply
Standby, the centrifugal oil-water separator is connected to crack tracheae axle by connecting bearing, and centrifugal oil-water separator lower end is arranged
There is delivery port, centrifugal oil-water separator upper end is connected to the baffling cooling tube in cooler bin, and baffling cooling tube lower end is connected to
Oil cooling service pipe, oil cooling service pipe is connected to fuel reserve tank, and the baffling cooling pipe end is connected to gas pipeline one end, and gas pipeline is another
Water washing device bottom is stretched into one end, and water washing device upper end is connected to recovery tube, and switch valve is provided with recovery tube, connects on recovery tube
Then oxygen supply equipment；
The fuel smoke processing system includes smoke discharge tube, ash fall room, absorption glue stick, web plate, flue gas delivery pipe, cigarette
Desulfurization equipment, exhaust gas combustion chamber and exhaust outlet, the smoke discharge tube upper end is arranged on ash fall room, in ash fall room
There are multiple absorption glue sticks in portion near the provided circumferentially about of inwall, adsorbs in the ash fall room above glue stick and is provided with web plate, institute
State web plate to be made up of closed plate and mesh plate, closed plate is arranged on mesh plate centre, ash fall room lower end side
Dust mouth is provided with, ash fall room upper end is connected to one end of flue gas delivery pipe, and the other end of flue gas delivery pipe is arranged on cigarette
Desulfurization device bottom, flue gas desulfurization device upper end is provided with exhaust gas combustion chamber, and exhaust gas combustion chamber is internally provided with burner, tail gas
Combustion chamber upper end is provided with exhaust outlet.
During present invention work, first open feeding gate and junked tire is put into cracking cylinder, fill a storehouse.Then cover into
Bin gate, by burner hearth cracking cylinder heating is given, and in heating process, power-equipment drives cracking cylinder rotation by travelling gear,
Cracking cylinder is set fully to be heated, the fire coal in burner hearth is provided by feeding screw, prevents inside smoke from running out of for mouth from fuel,
Pollution environment, burning oxygen used is provided by oxygen supply equipment.As temperature is raised, the junked tire cracked in cylinder starts to split
Solution, the cracking gas of generation enters centrifugal oil-water separator from cracking tracheae axle, and centrifugal oil-water separator passes through centrifugal force
The a small amount of moisture contained in cracking gas is separated, is collected downwards along centrifugal oil-water separator inwall.Isolate moisture
Cracking gas from centrifugal oil-water separator upper end enter cooler bin in baffling cooling tube, the cracking fluid after cooling
Change, in coming together in oil cooling service pipe, finally flow into interior.The cracking gas for isolating cracked oil also remains a large amount of flammable hydrocarbon gas and lacks
The impurity of amount, after water washing device, impurity is washed away in hydrocarbon gas, obtains pure hydrocarbon gas, on recovery tube with
The oxygen mix that oxygen supply equipment is provided, enters in burner hearth fully burn together.The heat that now hydrocarbon gas burning is produced is enough
The tire pyrolysis in cracking cylinder are made, so without continuously adding fire coal, having saved mass energy.In cracking process, coal combustion
Substantial amounts of flue gas can be produced, solid carbon particles therein are entered in ash fall room, and the closed plate on web plate can stop that flue gas is straight
Connected, and flue gas was guided to surrounding, contacted with the absorption glue stick of surrounding, solid carbon particles can be adsorbed glue stick and adsorb upper
Side, final settlement after waiting shutdown cooling, is collected charcoal ash and is recycled in ash fall room bottom from dust mouth.Remove charcoal particle
Flue gas enter in flue gas desulfurization device, remove sour gas therein, burning in exhaust gas combustion chamber, remove unburned
The carbon monoxide for fully producing, finally discharges from exhaust outlet.
Further, multiple steel balls are provided with the cracking cylinder.In cracking process, cracking cylinder rotarily drives steel ball and does
Random motion, breaks the block tire being carbonized in cracking process into pieces, block inside tires is fully cracked.Repeat to hit simultaneously
The steel wire beaten in tire, may eventually form a steel wire lump.
Further, it is provided with atomization into liquid pipe on the feeding gate of the cracking cylinder.In cracking process, atomization into liquid pipe can
For spraying into the catalyst of atomization, lysis efficiency is improved；After cracking terminates, atomization into liquid pipe can be used to spray into cooling water, quickly
The temperature in cracking cylinder is reduced, shortens cool time, improve operating efficiency.From cracking tracheae axle after the cooling water evaporation of penetrating
Discharge.
Further, one end that the cracking cylinder is connected to cracking tracheae axle is set to cone shape.Can effectively converge
Poly- cracking gas, facilitates cracking gas to enter in cracking tracheae axle.
Further, the cracking gas inlet diameter of the cracking tracheae axle enters less than the internal diameter for cracking tracheae axle, and cracking gas
Mouth is obliquely installed, and in cracking tracheae axle spiral plate is provided with.Cracking gas quick slant enters cracking gas import, coordinates splitting for rotation
Solution tracheae axle, forms centrifugal force, and the carbon black pellet in cracking gas is got rid of to cracking tracheae axle inwall, then the spiral plate by rotating
Push back in cracking cylinder.
Beneficial effects of the present invention：
（1）The present invention can reclaim the solid carbon particles discharged after storage coal combustion and recycle, and prevent solid carbon particles to be deposited on de-
Sulphur device bottom, has saved fuel, does not affect follow-up gas cleaning operation；
（2）The present invention can isolate hydrocarbon gas in cracking gas, and do fuel using hydrocarbon gas, save the energy, reclaim
Hydrocarbon gas in impurity remove through washing, obtain pure hydrocarbon gas, the oxygen for coordinating oxygen supply equipment to provide, burning
Effect is good, and calorific value is high；
（3）In the cracking process of the present invention, cracking cylinder rotarily drives steel ball and does random motion, breaks into pieces in cracking process and is carbonized
Block tire, block inside tires is fully cracked, improve reaction efficiency and reaction effect.Repeat impact wheel simultaneously
Steel wire in tire, may eventually form a steel wire lump, collect convenient；
（4）The present invention can in the reaction increase catalyst and improve lysis efficiency, after cracking terminates, directly using water-cooled cooling, and contracting
Short cool time, improve operating efficiency；
（5）The cracking gas energy fast convergence that present invention work is produced is tilted into entering cracking gas import, coordinates the cracking of rotation
Tracheae axle, forms centrifugal force, and the carbon black pellet in cracking gas is got rid of to cracking tracheae axle inwall, then is pushed away by the spiral plate for rotating
Return in cracking cylinder, prevent carbon black pellet from running out of the impurity become in cracking gas；
（6）Produce bubble explanation cracking gas in the water washing device of the present invention to start to produce, producing the amount of bubble can intuitively reflect
The severe degree of reaction, the extent of reaction acutely opens afterwards the switch valve on recovery tube, it is possible to stops fire coal and continuously adds；Washing
There is not bubble to produce in device, illustrating that reaction is abundant, just can start cooling；Change fuel heating and react sufficient opportunity
Can intuitively reflect, reduce operation difficulty, reduce energy consumption, improve lytic effect and efficiency.
Description of the drawings
Fig. 1 is the structural representation of junked tire vacuum cracking system；
Fig. 2 is the cut-away view for cracking tracheae axle；
Fig. 3 is the sectional view in the A-A faces of Fig. 1；
Fig. 4 is the structural representation of web plate；
Wherein, 1- cracking cylinder, 2- burner hearths, 3- feeding gates, 4- cracking tracheae axles, 401-, 402-, 5- travelling gear, 6- connections
Bearing, 7- centrifugal oil-water separators, 8- delivery ports, 9- cooler bins, 10- baffling cooling tubes, 11- oil cooling service pipes, 12- oil storages
Case, 13- gas pipelines, 14- water washing devices, 15- feeding screws, 16- recovery tubes, 17- switch valves, 18- oxygen supply equipments, 19-
Smoke discharge tube, 20- ash falls room, 21- absorption glue sticks, 22- web plates, 221- closed plates, 222- mesh plates, 23- flue gases are defeated
Send pipe, 24- flue gas desulfurization devices, 25- exhaust gas combustion chambers, 26- exhaust outlets.
Specifically embodiment
A kind of cylinder 1 of junked tire vacuum cracking system, including cracking as Figure 1-Figure 4, burner hearth 2, feeding gate 3, cracking gas
Pipe axle 4, travelling gear 5, connection bearing 6, cracking gas disposal recovery system and fuel smoke processing system, the cracking cylinder 1
It is arranged in burner hearth 2, feeding screw 15 is provided with burner hearth 2, the top of burner hearth 2 is provided with fuel smoke processing system, described
Cracking cylinder 1 side is provided with feeding gate 3, and the cracking opposite side of cylinder 1 is connected to crack tracheae axle 4, and cracking tracheae axle 4 is by connecting
Joint bearing 6 is connected to crack gas disposal recovery system, and on the cracking tracheae axle 4 travelling gear 5 is fixedly installed；
The cracking gas disposal recovery system includes centrifugal oil-water separator 7, cooler bin 9, water washing device 14, the and of recovery tube 16
Oxygen supply equipment 18, the centrifugal oil-water separator 7 is connected to crack tracheae axle 4, centrifugal water-oil separating by connection bearing 6
The lower end of device 7 is provided with delivery port 8, and the upper end of centrifugal oil-water separator 7 is connected to the baffling cooling tube 10 in cooler bin 9, baffling
The lower end of cooling tube 10 is connected to oil cooling service pipe 11, and oil cooling service pipe 11 is connected to fuel reserve tank 12, and the end of baffling cooling tube 10 connects
Then one end of gas pipeline 13, the other end of gas pipeline 13 stretches into the bottom of water washing device 14, and the upper end of water washing device 14 is connected to back
Closed tube 16, is provided with switch valve 17 on recovery tube 16, oxygen supply equipment 18 is connected on recovery tube 16；
The fuel smoke processing system includes smoke discharge tube 19, ash fall room 20, absorption glue stick 21, web plate 22, flue gas
Delivery pipe 23, flue gas desulfurization device 24, exhaust gas combustion chamber 25 and exhaust outlet 26, the upper end of the smoke discharge tube 19 is arranged on dust
There are multiple absorption glue sticks 21, the top of absorption glue stick 21 in expansion chamber 20, the inside of ash fall room 20 near the provided circumferentially about of inwall
Ash fall room 20 in be provided with web plate 22, the web plate 22 is made up of closed plate 221 and mesh plate 222, and closed plate 221 sets
Put in the centre of mesh plate 222, the lower end side of the ash fall room 20 is provided with dust mouth, the upper end of ash fall room 20 connects
Then one end of flue gas delivery pipe 23, the other end of flue gas delivery pipe 23 is arranged on the bottom of flue gas desulfurization device 24, flue gas desulfurization
The upper end of equipment 24 is provided with exhaust gas combustion chamber 25, and exhaust gas combustion chamber 25 is internally provided with burner, and the upper end of exhaust gas combustion chamber 25 is arranged
There is exhaust outlet 26.
Multiple steel balls 15 are provided with the cracking cylinder 1.
Atomization into liquid pipe 28 is provided with the feeding gate 3 of the cracking cylinder 1.
One end that the cracking cylinder 1 is connected to cracking tracheae axle 4 is set to cone shape.
The diameter of cracking gas import 401 of the cracking tracheae axle 4 is less than the internal diameter of cracking tracheae axle 4, and cracking gas import
401 are obliquely installed, and in cracking tracheae axle 4 spiral plate 402 is provided with.
Claims (5)
1. a kind of junked tire vacuum cracking system, it is characterised in that including cracking cylinder（1）, burner hearth（2）, feeding gate（3）、
Cracking tracheae axle（4）, travelling gear（5）, connection bearing（6）, cracking gas disposal recovery system and fuel smoke processing system, institute
State cracking cylinder（1）It is arranged on burner hearth（2）It is interior, burner hearth（2）On be provided with feeding screw（15）, burner hearth（2）Top is provided with
Fuel smoke processing system, the cracking cylinder（1）Side is provided with feeding gate（3）, crack cylinder（1）Opposite side is connected to split
Solution tracheae axle（4）, crack tracheae axle（4）By connecting bearing（6）It is connected to crack gas disposal recovery system, the cracking tracheae
Axle（4）On be fixedly installed travelling gear（5）；
The cracking gas disposal recovery system includes centrifugal oil-water separator（7）, cooler bin（9）, water washing device（14）, reclaim
Pipe（16）And oxygen supply equipment（18）, the centrifugal oil-water separator（7）By connecting bearing（6）It is connected to crack tracheae axle
（4）, centrifugal oil-water separator（7）Lower end is provided with delivery port（8）, centrifugal oil-water separator（7）Upper end is connected to cooling
Case（9）Interior baffling cooling tube（10）, baffling cooling tube（10）Lower end is connected to oil cooling service pipe（11）, oil cooling service pipe（11）Connection
Fuel reserve tank（12）, the baffling cooling tube（10）End is connected to gas pipeline（13）One end, gas pipeline（13）The other end
Stretch into water washing device（14）Bottom, water washing device（14）Upper end is connected to recovery tube（16）, recovery tube（16）On be provided with switch
Valve（17）, recovery tube（16）On be connected to oxygen supply equipment（18）；
The fuel smoke processing system includes smoke discharge tube（19）, ash fall room（20）, absorption glue stick（21）, web plate
（22）, flue gas delivery pipe（23）, flue gas desulfurization device（24）, exhaust gas combustion chamber（25）And exhaust outlet（26）, the flue gas discharge
Pipe（19）Upper end is arranged on ash fall room（20）, ash fall room（20）It is internal to have multiple suctions near the provided circumferentially about of inwall
Attached glue stick（21）, adsorb glue stick（21）The ash fall room of top（20）Inside it is provided with web plate（22）, the web plate（22）By sealing
Closing plate（221）And mesh plate（222）Composition, closed plate（221）It is arranged on mesh plate（222）Centre, the ash fall
Room（20）Lower end side is provided with dust mouth, ash fall room（20）Upper end is connected to flue gas delivery pipe（23）One end, flue gas
Delivery pipe（23）The other end be arranged on flue gas desulfurization device（24）Bottom, flue gas desulfurization device（24）Upper end is provided with tail gas combustion
Burn room（25）, exhaust gas combustion chamber（25）It is internally provided with burner, exhaust gas combustion chamber（25）Upper end is provided with exhaust outlet（26）.
2. a kind of junked tire vacuum cracking system, it is characterised in that the cracking cylinder（1）Inside it is provided with multiple steel balls
（15）.
3. a kind of junked tire vacuum cracking system, it is characterised in that the cracking cylinder（1）Feeding gate（3）On be provided with
Atomization into liquid pipe（28）.
4. a kind of junked tire vacuum cracking system, it is characterised in that the cracking cylinder（1）With cracking tracheae axle（4）Connection
The one end for is set to cone shape.
5. a kind of junked tire vacuum cracking system, it is characterised in that the cracking tracheae axle（4）Cracking gas import（401）
Diameter is less than cracking tracheae axle（4）Internal diameter, and cracking gas import（401）It is obliquely installed, cracks tracheae axle（4）Inside it is provided with spiral shell
Rotating plate（402）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611178080.5A CN106635099A (en) | 2016-12-19 | 2016-12-19 | Waste tire vacuum cracking system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611178080.5A CN106635099A (en) | 2016-12-19 | 2016-12-19 | Waste tire vacuum cracking system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106635099A true CN106635099A (en) | 2017-05-10 |
Family
ID=58833441
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611178080.5A Pending CN106635099A (en) | 2016-12-19 | 2016-12-19 | Waste tire vacuum cracking system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106635099A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110305678A (en) * | 2019-06-04 | 2019-10-08 | 珠海格力电器股份有限公司 | A kind of cracking technology, pyrolysis furnace and rubber material cracking apparatus |
| CN112391177A (en) * | 2019-08-14 | 2021-02-23 | 招远市汇潮新能源科技有限公司 | Cracking system and cracking process |
| CN115216323A (en) * | 2021-04-16 | 2022-10-21 | 慕尔(大连)科技有限公司 | Processing equipment is united with oil gas to pyrolysis carbon black |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008019237A1 (en) * | 2007-05-18 | 2008-11-27 | Roland Bender | Process and plant for the treatment of hydrocarbon-containing products |
| CN101679871A (en) * | 2007-05-25 | 2010-03-24 | 罗地格兄弟机械制造有限责任公司 | Method and apparatus with foreign particles thermolysis starting raw material |
| CN202158655U (en) * | 2011-06-29 | 2012-03-07 | 杨光辉 | Straight-seam hot blast furnace provided with smoke dust settling chamber |
| CN202164274U (en) * | 2011-08-20 | 2012-03-14 | 罗聿训 | Biomass energy air-returning type dry distillation furnace |
| CN205056044U (en) * | 2015-09-22 | 2016-03-02 | 天津斯瑞吉高新科技研究院有限公司 | Micro - observer of epoxy reaction |
| CN205115389U (en) * | 2015-07-03 | 2016-03-30 | 青岛裕盛源橡胶有限公司 | Junked tire thermal cracking oil refining equipment |
-
2016
- 2016-12-19 CN CN201611178080.5A patent/CN106635099A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008019237A1 (en) * | 2007-05-18 | 2008-11-27 | Roland Bender | Process and plant for the treatment of hydrocarbon-containing products |
| CN101679871A (en) * | 2007-05-25 | 2010-03-24 | 罗地格兄弟机械制造有限责任公司 | Method and apparatus with foreign particles thermolysis starting raw material |
| CN202158655U (en) * | 2011-06-29 | 2012-03-07 | 杨光辉 | Straight-seam hot blast furnace provided with smoke dust settling chamber |
| CN202164274U (en) * | 2011-08-20 | 2012-03-14 | 罗聿训 | Biomass energy air-returning type dry distillation furnace |
| CN205115389U (en) * | 2015-07-03 | 2016-03-30 | 青岛裕盛源橡胶有限公司 | Junked tire thermal cracking oil refining equipment |
| CN205056044U (en) * | 2015-09-22 | 2016-03-02 | 天津斯瑞吉高新科技研究院有限公司 | Micro - observer of epoxy reaction |
Non-Patent Citations (2)
| Title |
|---|
| 刘立忠: "《大气污染控制工程》", 31 January 2015, 中国建材工业出版社 * |
| 西安交通大学动力机械系: "《活塞式压缩机》", 31 August 1972, 西安交通大学出版社 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110305678A (en) * | 2019-06-04 | 2019-10-08 | 珠海格力电器股份有限公司 | A kind of cracking technology, pyrolysis furnace and rubber material cracking apparatus |
| CN112391177A (en) * | 2019-08-14 | 2021-02-23 | 招远市汇潮新能源科技有限公司 | Cracking system and cracking process |
| CN115216323A (en) * | 2021-04-16 | 2022-10-21 | 慕尔(大连)科技有限公司 | Processing equipment is united with oil gas to pyrolysis carbon black |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104804775B (en) | The method and system of domestic garbage pyrolysis gasification production combustible gas | |
| CN101824332B (en) | Production equipment for comprehensively utilizing renewable energy resources of waste and old plastics, tires and waste engine oil | |
| CN102329653B (en) | Plasma garbage gasification device and process | |
| CN206646064U (en) | A kind of dry coke quenching auxiliary | |
| CN102145343B (en) | Integrated garbage treatment and utilization method for effectively controlling dioxin | |
| CN107513389B (en) | Carbonizing device capable of treating garbage | |
| CN106635099A (en) | Waste tire vacuum cracking system | |
| CN101798531B (en) | Refuse breaking and cracking treatment process and cracking furnace | |
| CN105757676A (en) | Garbage cracking furnace system | |
| CN106675589A (en) | Exhaust gas and waste heat recovery technology for biochar preparation by sludge reduction gasification | |
| CN101962558B (en) | Biomass combustible gas high-temperature oxygen-free reinforced dry-distillation pyrolysis plant | |
| CN101270288B (en) | Biomass raw material gas making equipment and technique | |
| CN109943357A (en) | A kind of oily waste multistage method for cracking treatment and equipment | |
| CN1289634C (en) | Smoke and dust eliminating process for loading coal and pushing coke used in medium and small type coke oven | |
| CN105444180B (en) | A kind of refuse gasification boiler and its application process | |
| CN101974351A (en) | Scale fixed bed biomass gasification power generation production technology and complete equipment | |
| CN102580676B (en) | Preparation method of active coke for wastewater advanced treatment | |
| CN105038828A (en) | Rotary low-temperature pyrolyzing system and method for indirect heating of low-rank coal | |
| CN205640918U (en) | Floated waste incinerator that can clean and fully burn | |
| CN106675592A (en) | Energy-efficient indirect thermal desorption carbonization device and treatment method thereof | |
| CN208904180U (en) | A kind of Non-oxygen pyrolytic processing recyclable device of waste lithium cell positive plate | |
| WO2019184592A1 (en) | Household refuse gasification pyrolysis treatment device for saving energy and decreasing energy consumption | |
| CN106047382A (en) | Automatic-dust-removal refuse pyrolysis and cracking system | |
| CN102676234B (en) | Biomass gas device capable of realizing refluxing and recycling of tar | |
| CN113578933B (en) | Elementary self-circulation treatment system for household garbage |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170510 |