CN200974828Y - Waste rubber recycling equipment - Google Patents
Waste rubber recycling equipment Download PDFInfo
- Publication number
- CN200974828Y CN200974828Y CNU2006201600738U CN200620160073U CN200974828Y CN 200974828 Y CN200974828 Y CN 200974828Y CN U2006201600738 U CNU2006201600738 U CN U2006201600738U CN 200620160073 U CN200620160073 U CN 200620160073U CN 200974828 Y CN200974828 Y CN 200974828Y
- Authority
- CN
- China
- Prior art keywords
- oil
- feed bin
- links
- recovery system
- waste old
- 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.)
- Expired - Fee Related
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 29
- 238000004064 recycling Methods 0.000 title abstract description 4
- 238000005336 cracking Methods 0.000 claims abstract description 37
- 238000011084 recovery Methods 0.000 claims abstract description 17
- 239000002893 slag Substances 0.000 claims abstract description 13
- 239000006148 magnetic separator Substances 0.000 claims description 13
- 229910000831 Steel Inorganic materials 0.000 claims description 12
- 239000010959 steel Substances 0.000 claims description 11
- -1 mechanical crusher Substances 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 18
- 238000011282 treatment Methods 0.000 abstract description 6
- 230000008901 benefit Effects 0.000 abstract description 5
- 239000002341 toxic gas Substances 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 11
- 239000006229 carbon black Substances 0.000 description 8
- 230000008569 process Effects 0.000 description 7
- 239000004033 plastic Substances 0.000 description 6
- 239000003818 cinder Substances 0.000 description 4
- 239000000295 fuel oil Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 150000002013 dioxins Chemical class 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229910000639 Spring steel Inorganic materials 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 238000012962 cracking technique Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000003895 groundwater pollution Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- GOLXNESZZPUPJE-UHFFFAOYSA-N spiromesifen Chemical compound CC1=CC(C)=CC(C)=C1C(C(O1)=O)=C(OC(=O)CC(C)(C)C)C11CCCC1 GOLXNESZZPUPJE-UHFFFAOYSA-N 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000010920 waste tyre Substances 0.000 description 1
Images
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
- 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
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses an old and useless rubber recovery plant belongs to a device with waste recycling. The device comprises a cracking kettle, a condenser and an oil-gas separator, wherein a feed inlet is formed in the upper part of the cracking kettle, a slag outlet is formed in the lower part of the cracking kettle, and a slag remover is connected to the slag outlet; an oil outlet pipe and an exhaust pipe are arranged at the upper part of the side surface of the cracking kettle, and an air inlet is arranged at the lower part of the side surface; the oil outlet pipe is connected with the condenser, the condenser is connected with the oil-gas separator through a pipeline, and an exhaust pipe is arranged on the oil-gas separator. The utility model discloses the beneficial effect who produces is, decomposes waste rubber under the lower temperature, does not produce toxic gas, and recycle rate is high, and degree of automation is high. Additionally, the utility model discloses still have treatment effeciency height, consume energy advantage such as few.
Description
Technical field
The utility model relates to a kind of equipment that reclaims waste old, and is specifically a kind of with the equipment of recycling after the waste old decomposition.
Background technology
When society developed by leaps and bounds, the progressive countless environmental problem of being brought was made us class worries very.Acid rain, groundwater pollution, deleterious waste discharge or the like.It is very serious abandoning at whole world waste tire.Also has our very familiar daily domestic refuse in addition.Daily household garbage field in the North America, handle these pollutents at present the simplest method bury exactly.This treatment process can not decontamination, and a lot of available renewable resource have been wasted.
As everyone knows, junked tire and plastic garbage can cause very big pollution to environment.Recognized this problem in many developed countries such as the U.S., Japan, Europe, and begun legislation and forbid that the landfill buries junked tire and plastic garbage.Because junked tire is can not decomposed by the Nature.Unless yet the effective ways that these junked tires and plastic garbage can recycle be implemented, otherwise decree can face bigger problem, that is exactly that the savings amount of junked tire and plastic garbage is in continuous growth.
China's automobile pollution rises year by year, reached 2,500 ten thousand at present, all had every year a large amount of junked tires to produce, calendar year 2001 produces about 5,000 ten thousand, 2002 about 6,500 ten thousand, imbed the underground degraded that not only is difficult for, polluted source also destroys Soil structure, make the agricultural-food underproduction, quality descends, and damaged tire whole body again is precious, and order has the good reputation of " black gold ".At present, the junked tire procurement price is about 1400 yuan/ton, and its 12% contained steel wire is the raw material of high-quality spring steel, and the existing market price is about 2000 yuan/ton; Contained 28%-35% is reducible for recyclable carbon black is used for printing etc., and city's price can reach 3000 yuan-5000 yuan/ton.49%-56% is reducible to be fuel oil.Economic benefit is very considerable.The basic outlet of effecting a radical cure these " black pollutions " is to realize recycling, and the benign cycle economic model by " resource-product-renewable resource-reconstituted product " obtains good environment, society and economic benefit.
Therefore, all people that play an active part in environment protection wish to design the reliable treatments system of a kind of effectively cycling and reutilization junked tire and plastic garbage, and can not produce adverse influence to environment.On the basis of advanced person's science and technical study for many years, should be possible.
The old tire that extensively adopts in the world, the science treatment process of plastic garbage are at present: crush method is produced rubber powder, Pintsch process and local method oil refining etc.But Pintsch process can produce the part toxic gas and enter atmosphere, and from the strategy of sustainable development angle of environment, these are not the most effective treatment processs.
Summary of the invention
The technical problems to be solved in the utility model provide a kind of pollution-free, the rate of recovery is high, economy and the good waste old recovery system of social benefit.
The technical scheme that its technical problem that solves the utility model adopts is: the waste old recovery system, comprise cracking still, condenser and oil-gas separator, and described cracking still top is provided with opening for feed, and the bottom is provided with slag notch, is connected to skim gate on the described slag notch; The top, side of described cracking still is provided with oil outlet pipe and vapor pipe, and the bottom, side is provided with blast inlet; Described oil outlet pipe links to each other with described condenser, and described condenser links to each other with described oil-gas separator by pipeline, and described oil-gas separator is provided with vapor pipe.
Described waste old recovery system also comprises hotblast stove, and described hotblast stove is provided with burner; The escape pipe of described hotblast stove links to each other with blast inlet on the described cracking still.
Have at least the pipeline of leading up to link to each other in the oil of described oil-gas separator, the gas outlet with described burning gas.
Described waste old recovery system also comprises the automatic feeding device of being made up of former feed bin and conveying belt, and described automatic feeding device links to each other with the opening for feed of cracking still by filling tube, and described filling tube is provided with self-acting valve.
Described skim gate is made up of slag remover, magnetic separator, mechanical crusher, steel wire feed bin, clean feed bin, micronizer mill and pulse collector, links to each other by slideway between described slag remover and the magnetic separator; Between described magnetic separator and the steel wire feed bin, link to each other by conveying belt respectively between magnetic separator and the clean feed bin; Be provided with mechanical crusher between described magnetic separator and the clean feed bin; Described clean feed bin links to each other with described micronizer mill, and described micronizer mill links to each other with described pulse collector.
Also be connected with compressed air tank on the described micronizer mill, be connected with compressor on the described compressed air tank.
Be connected with high pressure blower on the described pulse collector.
The beneficial effect that the utility model produced is:
1, low temperature pyrolyzer, no poison gas produce: general old tire is cracked into the fuel oil need just can cracking more than-800 ℃ at 600 ℃.But it is cleavable that this equipment needs only at 280 ℃-420 ℃, owing to low temperature pyrolyzer, does not produce the condition of toxic gas Dioxins, does not also just have Dioxins and produces and discharge.
2, little negative pressure, cracking fast: the utility model has adopted little negative pressure cracking technique, has effectively accelerated cracked speed, thereby raises the efficiency 3 times.
3, this equipment also has processing power height, energy consumption low (only for similar techniques 22%), environmental protection advantages such as (no any three waste discharge and secondary pollutions) fully.
The fuel oil, carbon black, the steel wire that obtain after the cracking of this device of process all are the very high industrial raw material of added value, have realized the maximization of waste old is recycled.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is the structure principle chart of a kind of embodiment of waste old recovery system of the present utility model;
Fig. 2 is the structure principle chart of skim gate in the waste old recovery system of the present utility model.
Among the figure: 1. former feed bin, 2. output band, 3. filling tube, 4. hotblast stove, 5. burner, 6. blast inlet, 7. cracking still, 8. skim gate, 9. oil outlet pipe, 10. vapor pipe, 11. condenser, 12. oil-gas separators, 13. gas-holder, 14. storage tank, 15. slag removers, 16. slideway, 17. magnetic separators, 18. steel wire conveying belt, 19. steel wire feed bins, 20. clean feed bin, 21. mechanical crushers, 22. carbon black conveying belt, 23. micronizer mills, 24. compressor, 25. compressed air tanks, 26. gas blowers, 27. pulse collectors.
Embodiment
As shown in Figure 1, the waste old recovery system comprises a former feed bin, is used to store pending waste old; Be connected with conveying belt on the former feed bin, be used for pending waste old is transported to cracking still by former feed bin; Be provided with several filling tubes on conveying belt, this filling tube is connected on the opening for feed of cracking still, the corresponding filling tube of each cracking still, and the number of cracking still is determined according to the treatment capacity of waste old; In order conveniently to control inlet amount, can on filling tube, establish a self-acting valve, as required to controlling in the material that enters cracking still; Cracking still is provided with blast inlet, and this blast inlet is connected with hotblast stove, and hotblast stove burns device by alkene provides hot blast; The bottom of cracking still is provided with except that cinder notch, removes cinder notch and connects skim gate, so that realize the automatization slagging-off; Also be provided with vapor pipe and oil outlet pipe on the cracking still, vapor pipe is used to discharge the waste gas that cracking process produces, and oil outlet pipe links to each other with condenser.Pending waste old enters cracking still from the opening for feed on cracking still top, mix with the heat that blast inlet from the cracking still bottom enters, cracking under the effect of catalyzer, the gas-oil mixture that cracking produces enters into condenser by oil outlet, and the oil that vaporization temperature is lower in condenser is condensed into liquid state; Condenser links to each other with oil-gas separator, and the oil of liquid state is separated with the gasiform combustible gas, and liquid oil enters in the storage tank by transition pipeline and stores; The gasiform inflammable gas enters in the gas-holder by pneumatic tube and stores.
For save energy more, the employed fuel of burner can use this equipment cracking waste old to decompose resulting oil in back or combustible gas, promptly draws one road pipeline to burner from storage tank or gas-holder.In addition, also can directly quote oil or combustible gas from the outlet of oil-gas separator.
Waste old in cracking still after the cracking remaining major ingredient be that the residue of carbon black and steel wire is discharged from the cinder notch that removes of cracking still bottom, remove reason by skim gate.The structure of skim gate is sent into slideway by the residue that cinder notch comes out that removes of cracking still through slag remover as shown in Figure 2, enters magnetic separator through slideway.In magnetic separator, the steel wire in the residue is separated, and sends into the steel wire feed bin by the steel wire conveying belt and stores; Remaining carbon black is pulverized by mechanical crusher after the defeated band of carbon black is sent into clean feed bin, enter micronizer mill then, be connected with compressed air tank on the micronizer mill, the pressurized air in the compressed air tank enters micronizer mill, carbon black is further pulverized laggard horizontal pulse collector store.Be connected with gas blower on the pulse collector, the impurity in the high pressure draft removal carbon black is provided.Pressurized air in the compressed air tank is provided by the compressor that is attached thereto.
Claims (7)
1, the waste old recovery system is characterized in that, comprises cracking still, condenser and oil-gas separator, and described cracking still top is provided with opening for feed, and the bottom is provided with slag notch, is connected to skim gate on the described slag notch; The top, side of described cracking still is provided with oil outlet pipe and vapor pipe, and the bottom, side is provided with blast inlet; Described oil outlet pipe links to each other with described condenser, and described condenser links to each other with described oil-gas separator by pipeline, and described oil-gas separator is provided with vapor pipe.
2, waste old recovery system according to claim 1 is characterized in that, also comprises hotblast stove, and described hotblast stove is provided with burner; The escape pipe of described hotblast stove links to each other with blast inlet on the described cracking still.
3, waste old recovery system according to claim 2 is characterized in that, has at least the pipeline of leading up to link to each other with described burning gas in the oil of described oil-gas separator, the gas outlet.
4, waste old recovery system according to claim 1, it is characterized in that, also comprise the automatic feeding device of being made up of former feed bin and conveying belt, described automatic feeding device links to each other with the opening for feed of cracking still by filling tube, and described filling tube is provided with self-acting valve.
5, waste old recovery system according to claim 1, it is characterized in that, described skim gate is made up of slag remover, magnetic separator, mechanical crusher, steel wire feed bin, clean feed bin, micronizer mill and pulse collector, links to each other by slideway between described slag remover and the magnetic separator; Between described magnetic separator and the steel wire feed bin, link to each other by conveying belt respectively between magnetic separator and the clean feed bin; Be provided with mechanical crusher between described magnetic separator and the clean feed bin; Described clean feed bin links to each other with described micronizer mill, and described micronizer mill links to each other with described pulse collector.
6, waste old recovery system according to claim 5 is characterized in that, also is connected with compressed air tank on the described micronizer mill, is connected with compressor on the described compressed air tank.
7, waste old recovery system according to claim 5 is characterized in that, is connected with high pressure blower on the described pulse collector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201600738U CN200974828Y (en) | 2006-11-27 | 2006-11-27 | Waste rubber recycling equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201600738U CN200974828Y (en) | 2006-11-27 | 2006-11-27 | Waste rubber recycling equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200974828Y true CN200974828Y (en) | 2007-11-14 |
Family
ID=38901118
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2006201600738U Expired - Fee Related CN200974828Y (en) | 2006-11-27 | 2006-11-27 | Waste rubber recycling equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200974828Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101585037B (en) * | 2009-06-05 | 2011-05-18 | 上海绿人生态经济科技有限公司 | Steel wire conveyor for recycling waste and old tire |
| CN102304235A (en) * | 2011-03-21 | 2012-01-04 | 卓寿镛 | High-temperature feeding and deslagging cracking device for waste rubber and waste plastic |
| CN102925192A (en) * | 2012-11-19 | 2013-02-13 | 易林 | Environment-friendly energy-saving system device for producing fuel oil by using waste rubber |
| CN103586258A (en) * | 2013-11-11 | 2014-02-19 | 张艺璇 | Resource self-consuming type garbage treatment system for white garbage and catalyst of resource self-consuming type garbage treatment system |
| CN104650942A (en) * | 2014-06-09 | 2015-05-27 | 广西腾博再生能源有限公司 | Heat energy utilization device for waste rubber cracking production line |
| CN106111295A (en) * | 2016-06-21 | 2016-11-16 | 江苏密友粉体新装备制造有限公司 | A kind of deep cooling crush superfines preparation method |
-
2006
- 2006-11-27 CN CNU2006201600738U patent/CN200974828Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101585037B (en) * | 2009-06-05 | 2011-05-18 | 上海绿人生态经济科技有限公司 | Steel wire conveyor for recycling waste and old tire |
| CN102304235A (en) * | 2011-03-21 | 2012-01-04 | 卓寿镛 | High-temperature feeding and deslagging cracking device for waste rubber and waste plastic |
| CN102925192A (en) * | 2012-11-19 | 2013-02-13 | 易林 | Environment-friendly energy-saving system device for producing fuel oil by using waste rubber |
| CN103586258A (en) * | 2013-11-11 | 2014-02-19 | 张艺璇 | Resource self-consuming type garbage treatment system for white garbage and catalyst of resource self-consuming type garbage treatment system |
| CN103586258B (en) * | 2013-11-11 | 2015-11-18 | 张艺璇 | White garbage resource self consumption type refuse disposal system and catalyst thereof |
| CN104650942A (en) * | 2014-06-09 | 2015-05-27 | 广西腾博再生能源有限公司 | Heat energy utilization device for waste rubber cracking production line |
| CN106111295A (en) * | 2016-06-21 | 2016-11-16 | 江苏密友粉体新装备制造有限公司 | A kind of deep cooling crush superfines preparation method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: DONGKE HONGRI (BEIJING) SCIENCE + TECHNOLOGY DEVEL Free format text: FORMER OWNER: ZHUO SHOUYONG Effective date: 20130325 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: HONG KONG, CHINA TO: 100041 SHIJINGSHAN, BEIJING |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130325 Address after: 100041, building 3, building 3, No. 9654, West well road, Badachu hi tech park, Beijing, Shijingshan District Patentee after: East Red (Beijing) science and Technology Development Co., Ltd. Address before: Chinese new territories of Hongkong tin Chung court Songqi Ge 208 Patentee before: Zhuo Shouyong |
|
| ASS | Succession or assignment of patent right |
Owner name: ZHUO LEI Effective date: 20130626 Owner name: CHEN XIANGJUN Free format text: FORMER OWNER: DONGKE HONGRI (BEIJING) SCIENCE + TECHNOLOGY DEVELOPMENT CO., LTD. Effective date: 20130626 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 100041 SHIJINGSHAN, BEIJING TO: 256651 BINZHOU, SHANDONG PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130626 Address after: 256651 Shandong, Binzhou, Qin Qin Reservoir Road, No. 1, No. Patentee after: Chen Xiangjun Patentee after: Zhuo Lei Address before: 100041, building 3, building 3, No. 9654, West well road, Badachu hi tech park, Beijing, Shijingshan District Patentee before: East Red (Beijing) science and Technology Development Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071114 Termination date: 20151127 |