CN1758163A - Automatic control treatment equipment for waste tyre - Google Patents
Automatic control treatment equipment for waste tyre Download PDFInfo
- Publication number
- CN1758163A CN1758163A CNA2005101048812A CN200510104881A CN1758163A CN 1758163 A CN1758163 A CN 1758163A CN A2005101048812 A CNA2005101048812 A CN A2005101048812A CN 200510104881 A CN200510104881 A CN 200510104881A CN 1758163 A CN1758163 A CN 1758163A
- Authority
- CN
- China
- Prior art keywords
- cracking
- warehouse
- automatic control
- waste tyre
- treatment equipment
- 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.)
- Granted
Links
Classifications
-
- 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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
A device for automatically controlling and processing waste tyre includes a feed storehouse set at the top of the device and connected to a cracking storehouse at its back and an outgoing storehouse at the bottom characterizing that said feed storehouse contains a heat insulation house and a chain drive device in it, said cracking device includes a jacket heating house and a heat insulation house shell with a sealed gate in it, the cracking one is connected with a hot wind furnace as the heat supply source, said outgoing one includes two gates and a house and the total process of feeding, cracking and outgoing is automatically controlled, which can operate continuously, not necessary to crack waste tyre in advance and recover black carbon, steel wires, fuel oil and combustible gas, besides, harmful gas over the standard will not be generated since it works under the low or lower middle temperature.
Description
Technical field
The utility model belongs to automatic control production line field, specially refers to the automatic control treatment equipment that carries out the cracking recycling for junked tire.
Background technology
Fast development along with national economic modernization, the continuous expansion of communications and transportation, automobile industry, a large amount of outputs of junked tire have become universally acknowledged Harmful Waste, how to make whole tire reclaim and recycling, promptly become a key link, at present the method for utilizing that goes up for junked tire of society mainly contains three kinds: 1. directly utilize, directly integral body is overhauled, or be used for dock fender, seawall, floating on water surface station etc.; 2. regeneration, but peeling is used for industry indoor floor, modification regeneration tire or liner, feed belt etc., but also preparation, regeneration glue, rubber powder, or be used for the ground paver, the roof covers material etc.; 3, thermal decomposition utilization, can carry out pyrolytic, and reclaim educt gas, oil, carbon black, also can directly burn and be used for cement material, boiler and metal smelt etc., but no matter be which kind of method, because butadiene acrylonitrile rubber can produce HCl and HCN in the pyrolytic process, so unsuitable pyrolysis, the product of junked tire pyrolysis is very complicated, gas comprises 14.3%, liquid accounted for 43% during the pyrolysis products obtained therefrom was formed, the charcoal ash accounts for 32%, steel wire accounts for 10.7%, and gas composition is mainly methane, ethane, propane, ethene, propylene, carbon monoxide etc.; It mainly is benzene, toluene, low-carbon alkene and aromatics etc. that liquid is formed, and also has a small amount of sulfuretted hydrogen simultaneously, defends diene and thiophene, and these all are industrial chemicals of great use.At present, both at home and abroad when carrying out the rubber high temperature pyrolysis, its temperature controlling range majority is to carry out under 600 ℃～800 ℃ high temperature, along with high temperature pyrolysis produces a large amount of harmful gases, cause second environmental pollution, do not meet environmental requirement, all the same feeling is thorny to cause Chinese and overseas scholars, for a long time, junked tire is treated as an international question that needs to be resolved hurrily.
Our company relies on chemical industry, the tyre industry experience for many years of being engaged in, through test of long duration research, successfully developed a kind of new technology that the junked tire cracking is handled that under middle low-temperature condition, (generally is controlled at 280 ℃～420 ℃ scopes) and carries out, through a large amount of tests and scientific appraisal, the feasibility and the practicality of this technology have been determined, not only solve the pollution problem in the processing procedure, brought considerable economic simultaneously.
Summary of the invention
The technical issues that need to address of the present invention, be in the prior art, adopt both at home and abroad in the junked tire pyrolytic process, all be to adopt high temperature pyrolysis, temperature range is at 600 ℃～800 ℃, along with the generation of harmful gas causes very big pollution to environment, the also back works such as precrushing of the advanced road wheel tire of important affair before high temperature pyrolysis simultaneously, in order to overcome above-mentioned existing weak point, in order to reduce the seriousness of environmental pollution, the present invention innovates the new technology that has proposed to carry out pyrolysis processing under middle low-temperature condition.Purpose of the present invention provides a kind of automatic control treatment equipment for waste tyre, and this equipment can make tire carry out the automatic continuous operation under middle low-temperature condition.
The present invention relies on following technical scheme to realize, a kind of automatic control treatment equipment for waste tyre, mainly include the feeding warehouse that is positioned at its upper side, the feed bin that goes out that it is connected to cracking bin device thereafter and is positioned at the bottom, it is characterized in that described feeding warehouse comprises insulation charging warehouse and places the chain transmission system in the warehouse, the infrared location system of mensuration article position; Described cracking bin device mainly comprises the warehouse shell of telescopic heating pyrolyze warehouse and insulation, and shell inside is provided with the gate of sealing, and cracking bin is connecting the heat generator as the device supplying heat source; Describedly go out feed bin, comprise twice gate and warehouse, also be furnished with nitrogen protection; The overall process of this charging, cracking and discharging all is subjected to the microcomputor program control of automatic control system to time, stroke.
Whole operation process is by the system controlled by computer automatic continuous operation, junked tire enters feeding warehouse by travelling belt, in described feeding warehouse through one gate and the action of chain elevator structure once, the then coupled roller feeding mechanism of dialling is sent into one on tire, the hoister action once pushed tire 3 seconds consuming time, back circulation 10 times reset, push 10 on tire and be total to 70 seconds consuming time, the nitrogen circulation heating arrangements that is positioned at downside heats the cracking storehouse, open the cracking bin gate, push tire again, tire is carried out cracking, during control 10 minutes.Should design maximum feed velocity be 40 tires per hour in the cracking process.
In order to spray desulfurization and to carry out cracking and catalyzing, need the dispensing port of adjuvant is arranged on the feeding warehouse upper end.
Shell links to each other, and outer rim is provided with the packing support set, and interior still adopts the fin plate welded structure to strengthen heat transfer, also is provided with the pyrolysis gas reclaim line and the exhanst gas outlet pipeline that connect with flange respectively on warehouse; The outside of interior still is welded with the heat radiator that increases endotherm area, and periphery is welded with not equidistant spoiler, can make hot blast produce cyclone in the storehouse outside, can fully absorb cracking in the heat supply warehouse.Going back cloth simultaneously has point for measuring temperature in the cracking storehouse, makes Control System of Microcomputer can accurately regulate and control heating load.Solid such as the carbon black of warehouse, steel wire are delivered to out in the feed bin by gravity, the valuable gases that cracking produces derives from interior still, by being built up in the recovery mouth on top, storehouse, to send into tanks by compressor again after the gas cooled, a part is made fuel for gas furnace, be the aqueous fuel oil drum of sending into after another part condensation.Described charging and discharging door all adopts gate valve structure, and the connection of each feed bin all adopts ring flange to connect.Tight in order to seal, go out the feed bin warehouse and be welded, and adopt two slide valves with the high-quality heat-resisting steel sheet and plate.
The invention has the beneficial effects as follows that the automatically continuous action of this equipment need not to carry out the prior fragmentation to junked tire; Can reclaim carbon black, steel wire, fuel oil, inflammable gas in the junked tire, owing to, do not have the harmful gas that exceeds standard and produce only at middle low-temperature operation comprehensively.
Description of drawings
Fig. 1 is automatic control treatment equipment for waste tyre action synoptic diagram
Fig. 2 is the cracking bin section of structure
Fig. 3 is the action flow chart of automatic control treatment equipment for waste tyre
Embodiment
With reference to Fig. 1, the overall operation synoptic diagram of expression automatic control treatment equipment for waste tyre, among the figure, the junked tire that is recovered utilization is 1, it enters charging warehouse 3 by chain transmission system 2, tire advances Hatch Opening by hoisting gear 4, by group roller mechanism 5 tire 1 is controlled to the porch in cracking storehouse 7 again through the 1st road gate valve 6, the front upper place in cracking storehouse 7 is provided with pyrolysis gas and reclaims mouth 8, the harmful gas that cracking process produces is derived from interior still and is drawn after cooling by this outlet 8, compressed again machine is sent into the fuel gas tank outside this device, and the fuel oil drum outside the liquid feeder that condensation is got off is taken away by pump.Finish a period when cracking storehouse 7 and transport end, the closed front end gate, unlatching rear end gate is sent transitional storehouse internal solid thing into out feed bin 9 and is separated, and closes the rear end gate after the discharging and prepares action next time, so the cycle repetition.Also be provided with adjuvant dispensing port 10 in the feeding warehouse the top, throw in spraying desulfurizing agent and catalyst for cracking at this mouthful.Heat generator 11 is supplying heat sources of entire equipment, and the heating principle that this equipment adopts is the flue gas heating, and promptly the flue gas of gas-fired heater enters by utilidor in the top layer in cracking storehouse and heats.
With reference to Fig. 2, expression cracking bin section of structure, cracking bin 7 is divided into outer still 7.1 and interior still 7.2 again among the figure, and outer still links to each other with insulation warehouse shell, and the outside is provided with packing support set 7.11; Interior still outside is welded with the heat radiator 7.21 that increases endotherm area, and periphery is welded with and does not equidistantly hold together to flow plate 7.22.
With reference to Fig. 3, the action flow chart of expression automatic control treatment equipment for waste tyre, show among the figure junked tire be through clean, oven dry, be sent to the feeding warehouse of described equipment by belt, enter the cracking storehouse again and carry out cracking, enter recovery stage at last.
Claims (4)
1. automatic control treatment equipment for waste tyre, mainly include the feeding warehouse that is positioned at its upper side, the feed bin that goes out that it is connected to cracking bin device thereafter and is positioned at the bottom is characterized in that, described feeding warehouse comprises insulation charging warehouse and places the interior chain transmission system of warehouse; Described cracking bin device mainly comprises telescopic heating pyrolyze warehouse and insulation warehouse shell, and shell inside is provided with the gate of sealing, and cracking bin is connecting the heat generator as the device supplying heat source; Describedly go out feed bin, comprise twice gate and warehouse; The overall process of this charging, cracking and discharging is controlled the microcomputor program of time, stroke by automatic control system all.
2. a kind of automatic control treatment equipment for waste tyre according to claim 1 is characterized in that, through one gate and the action of chain elevator structure once, the then coupled roller feeding mechanism of dialling is sent into 1 on tire in described feeding warehouse.
3. a kind of automatic control treatment equipment for waste tyre according to claim 1, it is characterized in that, described cracking bin, be divided into outer still and interior still again, outer still links to each other with insulation warehouse shell, outer rim is provided with the packing support set, and interior still adopts the fin plate welded structure to strengthen heat transfer, also is provided with the pyrolysis gas reclaim line and the exhanst gas outlet pipeline that connect with flange respectively on warehouse; The outside of interior still is welded with the heat radiator that increases endotherm area, and periphery is welded with not equidistant spoiler.
4. a kind of automatic control treatment equipment for waste tyre according to claim 1 is characterized in that, described charging and discharging door all adopts gate valve structure, and the connection of each feed bin all adopts ring flange to connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101048812A CN100412735C (en) | 2005-09-27 | 2005-09-27 | Automatic control treatment equipment for waste tyre |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101048812A CN100412735C (en) | 2005-09-27 | 2005-09-27 | Automatic control treatment equipment for waste tyre |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1758163A true CN1758163A (en) | 2006-04-12 |
| CN100412735C CN100412735C (en) | 2008-08-20 |
Family
ID=36703579
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005101048812A Expired - Fee Related CN100412735C (en) | 2005-09-27 | 2005-09-27 | Automatic control treatment equipment for waste tyre |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100412735C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008061467A1 (en) * | 2006-11-23 | 2008-05-29 | Daguang Li | A high efficient and energy-saving cracking apparatus for waste/used rubber |
| CN101307151B (en) * | 2008-03-21 | 2013-04-10 | 北京天海元科技有限公司 | Apparatus for treating waste and old tyres |
| CN103160306A (en) * | 2013-03-19 | 2013-06-19 | 启东金匙环保科技有限公司 | Continuous waste rubber low-temperature micro-pressure catalysis-free pyrolysis complete production unit |
| WO2015085662A1 (en) * | 2013-12-13 | 2015-06-18 | 王新明 | Process and apparatus for scrap tire pyrolysis and material feeding |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2404800C3 (en) * | 1974-02-01 | 1982-05-19 | Schäfer, Winfried, 6234 Hattersheim | Smoldering generator for the production of gaseous and liquid hydrocarbons and other substances by heat treatment of automobile tires |
| US4925532A (en) * | 1989-04-24 | 1990-05-15 | Pto, Inc. | Apparatus for thermal conversion of organic matter |
| CN1117517A (en) * | 1994-08-24 | 1996-02-28 | 中国长江动力公司(集团) | Method and equipment for catalytic cracking waste rubber |
| JP3094359B2 (en) * | 1994-12-20 | 2000-10-03 | 幸男 檜山 | Decomposition equipment for waste tires and waste FRP |
| CN1129553C (en) * | 1997-09-30 | 2003-12-03 | 邓健郎 | Method and device for intermittent continuous recovery waste tyre for extracting active carbon |
| CN2528772Y (en) * | 2002-02-04 | 2003-01-01 | 上海绿人生态经济科技有限公司 | Thermal cracking furnace for treating waste-old tyre |
| PL199261B1 (en) * | 2003-02-17 | 2008-08-29 | Zbigniew Tokarz | Method for continuous processing of organic wastes, particularly highly contaminated plastic wastes and used motor vehicle tyres and a system designed for continuous processing of organic wastes, particularly plastic wastes and used motor vehicle tyres |
-
2005
- 2005-09-27 CN CNB2005101048812A patent/CN100412735C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008061467A1 (en) * | 2006-11-23 | 2008-05-29 | Daguang Li | A high efficient and energy-saving cracking apparatus for waste/used rubber |
| CN1962735B (en) * | 2006-11-23 | 2010-12-08 | 李大光 | High-performance energy-saving waste rubber cracking apparatus |
| CN101307151B (en) * | 2008-03-21 | 2013-04-10 | 北京天海元科技有限公司 | Apparatus for treating waste and old tyres |
| CN103160306A (en) * | 2013-03-19 | 2013-06-19 | 启东金匙环保科技有限公司 | Continuous waste rubber low-temperature micro-pressure catalysis-free pyrolysis complete production unit |
| CN103160306B (en) * | 2013-03-19 | 2014-11-26 | 启东金匙环保科技有限公司 | Continuous waste rubber low-temperature micro-pressure catalysis-free pyrolysis complete production unit |
| WO2015085662A1 (en) * | 2013-12-13 | 2015-06-18 | 王新明 | Process and apparatus for scrap tire pyrolysis and material feeding |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100412735C (en) | 2008-08-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101942313B (en) | Huadian type process and device for dry distillation of oil shale | |
| CN207227348U (en) | Waste rubber cracking system | |
| CN105546546B (en) | One kind is innoxious to exempt from classify solid waste cracking apparatus and cleavage method | |
| CN103952165B (en) | A kind of small particles material method for destructive distillation based on multilayer rotary kiln | |
| CN102432914B (en) | Method and equipment for decomposing and recovering glass fiber reinforced plastics | |
| CN101984018B (en) | External heating internal coal decomposing equipment | |
| CN101851522B (en) | External heating type retort furnace | |
| CN109609190A (en) | A kind of refuse gasification and tar catalytic gasification device | |
| CN108410494B (en) | EPT waste tire continuous cracking device and method | |
| CN104830353A (en) | Dry-wet-combined coke quenching method | |
| CN100412735C (en) | Automatic control treatment equipment for waste tyre | |
| CN202246511U (en) | Decomposition recycling device of glass fiber reinforced plastics | |
| CN104910948B (en) | A kind of serialization cracking technology and equipment | |
| CN104531189B (en) | Oil shale distillation equipment employing dry coke extract gas heat carrier | |
| CN203999502U (en) | A kind of organic solid castoff mummification charing integrated system | |
| CN2846413Y (en) | Automatic control treating device for waste tire | |
| CN201390727Y (en) | External heating type retort furnace | |
| WO2016127674A1 (en) | Hybrid heating equipment and application thereof | |
| CN101307152B (en) | Apparatus for treating waste and old tyres | |
| CN107954411A (en) | The Processes and apparatus of vertical continuous carbonization production lithium cell cathode material | |
| CN204644266U (en) | The full circulation carbonization furnace that a kind of destructive distillation is lower-grade metamorphic bituminous | |
| CN204138600U (en) | High-temperature hot is vented one's spleen recycling system | |
| CN203159541U (en) | Continuous pollution-free low-energy consumption waste plastics oil refining device | |
| CN206590602U (en) | A kind of automatic ration charging feed system of life refuse high temperature pyrolysis furnace | |
| CN105505474A (en) | Combined type pyrolysis and gasification furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080820 Termination date: 20120927 |