CN202725185U - Energy-saving and efficient used tire pyrolysis reaction still - Google Patents
Energy-saving and efficient used tire pyrolysis reaction still Download PDFInfo
- Publication number
- CN202725185U CN202725185U CN2012204445369U CN201220444536U CN202725185U CN 202725185 U CN202725185 U CN 202725185U CN 2012204445369 U CN2012204445369 U CN 2012204445369U CN 201220444536 U CN201220444536 U CN 201220444536U CN 202725185 U CN202725185 U CN 202725185U
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- China
- Prior art keywords
- saving
- guide vane
- reaction still
- energy
- damaged tire
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- 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
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 13
- 238000000197 pyrolysis Methods 0.000 title abstract description 5
- 239000000463 material Substances 0.000 claims abstract description 22
- 238000005336 cracking Methods 0.000 claims description 23
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 239000000295 fuel oil Substances 0.000 abstract description 6
- 238000007599 discharging Methods 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 229910000831 Steel Inorganic materials 0.000 description 7
- 239000006229 carbon black Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000010962 carbon steel Substances 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000007233 catalytic pyrolysis Methods 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000009418 renovation Methods 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
Images
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The utility model provides an energy-saving and efficient used tire pyrolysis reaction still which comprises a still body (1), a feeding and discharging end seal head (2) and a feeding and discharging spiral (3). The reaction still is characterized in that the feeding and discharging end seal head (2) is a tapered seal head, and a guide fin I (4) and a guide fin II (5) are arranged between the tapered seal head and the still body (1). The reaction still has the advantages that hot-inlet and hot-outlet of materials are achieved, inlet and outlet of the materials under high-temperature conditions are effectively achieved, and the reaction still is safe, reliable, energy-saving and time-saving. Take 5 tons of the used tires to be treated for instance, before the technology is used, 24 hours, 150 KWh of power and 150 kilograms of fuel oil are consumed, and after the technology is used, only 16 hours, 100KWh of power and 110 kilograms of fuel oil are consumed, so that energy consumption can be greatly reduced, and production efficiencies are improved.
Description
Technical field
The utility model relates to a kind of damaged tire treatment facility, relates in particular to a kind of efficient energy-saving damaged tire cracking reaction still.
Background technology
At present the damaged tire generation in whole world every year has more than 300,000,000, places the waste that causes environmental pollution and resource for a long time, so the processing of damaged tire is a global problem.
The processing method of damaged tire has following several now: the damaged tire renovation; The whole utilization done fence; Damaged tire is done ground rubber; Fuel oil, carbon black, steel wire are produced in the damaged tire cracking.The three kinds of processing modes in front have only changed the geometry of damaged tire, do not change the molecular structure of damaged tire, and the physics existing way of the damaged tire that fundamentally terminated is processed in the damaged tire cracking, molecular composition and the version of tire have been changed, the dirt output new the energy-----fuel oil that can take full advantage of effectively, carbon black, steel wire.
The method of tire pyrolysis mainly is thermal cracking or catalytic pyrolysis at present, and used equipment has vertical, horizontal two kinds.By the mode of production continous way and batch (-type) are arranged, horizontal continuous equipment comparision of production is stable, but equipment price is high, the horizontal intermittent apparatus production cycle is long, and the process that there are a heating, cracking, cooling down in each cycle, slag tap is in this whole process, thermal energy consumption is many, and the production cycle is long, as complete at tire pyrolysis, under the condition that cracking still does not cool with the discharging in the still of carbon black, steel wire, and then charging, so namely saved the time, do not allow again kettle cool off, saved fuel
Under such environment and thinking, we have consulted great mass of data, do not have such equipment in damaged tire cracking field, there is not identical environment for use at other field yet, by a large amount of experiments, correction repeatedly, the input and output material fin is used at cracking apparatus at last, brings into play desirable effect.
Summary of the invention
The horizontal cracking apparatus production process of tradition be feed in raw material, heating, cracking, the one-period that cools off, slags tap, in this production cycle, duration is used in cooling, and the accumulation of heat of kettle is taken out of, is down to normal temperature and can slags tap.So not only waste the heat of kettle but also reduced production efficiency.
The utility model purpose is the defective for prior art, a kind of efficient energy-saving damaged tire cracking reaction still is provided, comprise kettle 1, input and output material end end socket 2 and input and output material spiral 3, it is characterized in that: input and output material end end socket is tapered end socket, and guide vane I4 and guide vane II5 are set between tapered end socket and the kettle 1.
Described guide vane I4 and guide vane II5 intersect mutually.
Described input and output material spiral 3 passes the infall of guide vane I4 and guide vane II5.
Described guide vane I4 and guide vane II5 are rectangle.
Described guide vane I4 and guide vane II5 are weldingly fixed in tapered end socket and the kettle 1.
The utility model advantage, the heat that has realized material is advanced heat and gone out, and has effectively solved the turnover of material under hot conditions, and is safe and reliable, the energy-and time-economizing.To process same 5 tons of damaged tires as example, do not use the front need of present technique 24 hours consuming time, power consumption 150 degree, 150 kilograms of consumption fuel oil; After using present technique: 16 hours times spent, power consumption 100 degree, 110 kilograms of consumption fuel oil.As seen greatly reduce energy resource consumption, improved production efficiency.
Description of drawings
Fig. 1 is the utility model structural representation.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is further specified.
Comprise kettle 1, input and output material end end socket 2 and input and output material spiral 3, it is characterized in that: input and output material end end socket 2 is tapered end socket, and guide vane I4 and guide vane II5 are set between tapered end socket and the kettle 1.
Described guide vane I4 and guide vane II5 intersect mutually.
Described input and output material spiral 3 passes the infall of guide vane I4 and guide vane II5.
Described guide vane I4 and guide vane II5 are rectangle.
Described guide vane I4 and guide vane II5 are weldingly fixed in tapered end socket and the kettle 1.
Cutting into block damaged tire adds from charging aperture 6, input and output material spiral 3 rotates clockwise, tyre block is to the tapered end socket 2 of kettle and fin 4,5, cracking still kettle 1 rotates clockwise, with mass transport to cracking still kettle 1, treat 1 heating of cracking still kettle, after tire pyrolysis is complete, only have carbon black and steel wire in the cracking still kettle 1, at this moment, counterclockwise rotation of cracking still kettle 1, carbon black and steel wire are to the tapered end socket 2 of kettle and fin 4,5, along with the rotation of cracking still kettle 1, carbon black and steel wire are to input and output material spiral 3, counterclockwise rotation of input and output material spiral 3, carbon black and steel wire are finished and are slagged tap to slag notch 7.As seen, by the rotation of cracking still kettle 1, fin 4,5 and the effect of input and output material spiral 3 under the heat of finishing material advance heat and go out.
In addition, the utility model and not meaning that by schematic diagram and specification limits to, and can change to some extent under the prerequisite that does not break away from design aim and principle thereof.
Claims (5)
1. efficient energy-saving damaged tire cracking reaction still, comprise kettle (1), input and output material end end socket (2) and input and output material spiral (3), it is characterized in that: input and output material end end socket (2) is tapered end socket, and guide vane I (4) and guide vane II (5) are set between tapered end socket and the kettle (1).
2. a kind of efficient energy-saving damaged tire cracking reaction still according to claim 1 is characterized in that: the mutual intersection of described guide vane I (4) and guide vane II (5).
3. a kind of efficient energy-saving damaged tire cracking reaction still according to claim 2, it is characterized in that: described input and output material spiral (3) passes the infall of guide vane I (4) and guide vane II (5).
4. according to claim 1 to the described a kind of efficient energy-saving damaged tire cracking reaction still of 3 arbitrary claims, it is characterized in that: described guide vane I (4) and guide vane II (5) are rectangle.
5. according to claim 1 to the described a kind of efficient energy-saving damaged tire cracking reaction still of 3 arbitrary claims, it is characterized in that: described guide vane I (4) and guide vane II (5) are weldingly fixed in tapered end socket and the kettle (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204445369U CN202725185U (en) | 2012-08-28 | 2012-08-28 | Energy-saving and efficient used tire pyrolysis reaction still |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204445369U CN202725185U (en) | 2012-08-28 | 2012-08-28 | Energy-saving and efficient used tire pyrolysis reaction still |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202725185U true CN202725185U (en) | 2013-02-13 |
Family
ID=47650937
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012204445369U Expired - Fee Related CN202725185U (en) | 2012-08-28 | 2012-08-28 | Energy-saving and efficient used tire pyrolysis reaction still |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202725185U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106118708A (en) * | 2016-08-12 | 2016-11-16 | 青岛双星环保设备有限公司 | Scrap rubber cracking deslagging device and slag tapping method |
| CN112745867A (en) * | 2021-01-21 | 2021-05-04 | 华中科技大学 | Heat accumulation roller pyrolysis reactor |
| CN117138732A (en) * | 2023-09-14 | 2023-12-01 | 山东明晟环保科技有限公司 | A homogenization cracking reaction device |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
| US12031097B2 (en) | 2021-10-14 | 2024-07-09 | Ecolab Usa Inc. | Antifouling agents for plastic-derived synthetic feedstocks |
| US12304888B2 (en) | 2021-03-10 | 2025-05-20 | Ecolab Usa Inc. | Stabilizer additives for plastic-derived synthetic feedstock |
-
2012
- 2012-08-28 CN CN2012204445369U patent/CN202725185U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106118708A (en) * | 2016-08-12 | 2016-11-16 | 青岛双星环保设备有限公司 | Scrap rubber cracking deslagging device and slag tapping method |
| CN106118708B (en) * | 2016-08-12 | 2018-03-06 | 青岛双星环保设备有限公司 | Scrap rubber cracks deslagging device and slag tapping method |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
| US12503663B2 (en) | 2020-09-14 | 2025-12-23 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
| CN112745867A (en) * | 2021-01-21 | 2021-05-04 | 华中科技大学 | Heat accumulation roller pyrolysis reactor |
| US12304888B2 (en) | 2021-03-10 | 2025-05-20 | Ecolab Usa Inc. | Stabilizer additives for plastic-derived synthetic feedstock |
| US12031097B2 (en) | 2021-10-14 | 2024-07-09 | Ecolab Usa Inc. | Antifouling agents for plastic-derived synthetic feedstocks |
| CN117138732A (en) * | 2023-09-14 | 2023-12-01 | 山东明晟环保科技有限公司 | A homogenization cracking reaction device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130213 Termination date: 20140828 |
|
| EXPY | Termination of patent right or utility model |