CN206127213U - Cracking system equipment of junked tire micelle - Google Patents
Cracking system equipment of junked tire micelle Download PDFInfo
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- CN206127213U CN206127213U CN201621152579.4U CN201621152579U CN206127213U CN 206127213 U CN206127213 U CN 206127213U CN 201621152579 U CN201621152579 U CN 201621152579U CN 206127213 U CN206127213 U CN 206127213U
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- pipe
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- molten salt
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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
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses a cracking system equipment of junked tire micelle, including molten salt furnace and pyrolysis furnace, the molten salt furnace advances the salt pipe and manages with first salt and be connected with the pyrolysis furnace through first respectively, firstly advance still to install the salt pump on the salt pipe, still install the fuel intake pipe on the molten salt furnace, include gaseous chamber from top to bottom in the molten salt furnace, liquid chamber and slag charge chamber, the liquid chamber is passing through liquids pipe and gasification cauldron intercommunication still, the slag charge chamber is still through a discharging device and magnetic separation machine intercommunication, the gasification cauldron is still through the 2nd discharging device and magnetic separation machine intercommunication, the magnetic separation machine still is connected with carbon black jar and steel wire recovery unit respectively, gaseous chamber is still through first breather pipe and rectifying column intercommunication, the gasification cauldron is still through second breather pipe and rectifying column intercommunication, install gaseous pipe on the rectifying column, light oil pipe, heavy oil pipe, gas tank still communicates with the molten salt furnace. The utility model discloses in, tire micelle schizolysis rate is high, the lysate rate of recovery high, and can continuous production, the energy consumption is low.
Description
Technical field
This utility model is related to tire recycling technical field, more particularly to a kind of cracking system of junked tire micelle sets
It is standby.
Background technology
Plastics and rubber are two kinds of wide variety of synthetic macromolecular compounds, possess many superior functions.They
High consume the environmental pollution for causing and be on the rise.Both spent high molecular materials how to be processed and are utilized in current whole world model
Universal concern is caused in enclosing.
At present, the cracking apparatus of domestic many useless junked tires continuously can not be produced, and high energy consumption, cleavage rate are low, safety
Difference.
Utility model content
This utility model mainly solves the technical problem in the presence of prior art, so as to provide a kind of cleavage rate it is high,
The lysate response rate is high, and continuously can produce, the cracking system equipment of the junked tire micelle that energy consumption is low.
What above-mentioned technical problem of the present utility model was mainly addressed by following technical proposals：
A kind of cracking system equipment of junked tire micelle of the present utility model, including molten salt furnace and pyrolysis furnace, it is described molten
Salt stove is entered salt pipe and first by first respectively and goes out salt pipe and be connected with pyrolysis furnace, and described first to enter and be also equipped with salt pump on salt pipe,
It is also equipped with fuel air pipe on the molten salt furnace, the molten salt furnace includes air chamber from top to bottom, liquid chambers and slag charge
Chamber, the liquid chambers are also connected with gasification kettle by liquid line, and the slag charge chamber is also separated with magnetic separation by the first drawing mechanism
Machine connect, it is described gasification kettle also connected with magnetic separator by the second drawing mechanism, the magnetic separator also respectively with charcoal
Black tank and the connection of steel wire retracting device, the air chamber are also connected with rectifying column by the first breather, and the gasification kettle also leads to
Cross the second breather to connect with rectifying column, gas tube, light oil pipe, oil pipe are installed on the rectifying column, the gas tank is also
Connect with molten salt furnace.
Further, the fused salt furnace bottom is also connected with multiple emergent storage tanks by cooling plug.
Further, the gasification kettle enters salt pipe and second by second respectively and goes out salt pipe and molten salt furnace.
Further, the light oil pipe and oil pipe are connected with circulating water cooling device.
Further, the outlet pipe of the circulating water cooling device is also connected with heat-exchange device, the heat-exchange device
On the fuel air pipe.
Compared with prior art, the utility model has the advantage of：By arrange molten salt furnace, and by molten salt furnace come plus
Pyrocrack furnace and gasification kettle, tire micelle are added into pyrolysis furnace, and pyrolysis furnace decomposes micelle, micro-molecular gas, light oil and heavy oil
White carbon black solid after gasification, the metal in tire micelle and decomposition retains, and part heavy oil can be cooled to liquid after gasification again
It is attached on pyrolysis furnace, the metal and white carbon black in slag charge chamber can enter magnetic separator, magnetic separation point by the first drawing mechanism
Disembark and can separate metal and white carbon black, metal is transported to into steel wire retracting device then, white carbon black is transported in white carbon black tank, and
Again the heavy oil for liquefying enters gasification kettle by liquid line from liquid chambers, and molten salt furnace heating and gasifying kettle, heavy oil gasification are partially into
The metal and white carbon black of gasification kettle enters magnetic separator by the second drawing mechanism, it is possible to increase the collection rate of oil gas, air chamber
In gas enter rectifying column, rectification goes out gasoline, diesel oil and heavy oil, collects respectively, and lighter fuel gas is imported into molten salt furnace
Middle burning provides heat for molten salt furnace.By the device, tire micelle cleavage rate is high, the lysate response rate is high, and can be continuous
Production, energy consumption are low.
Description of the drawings
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or accompanying drawing to be used is briefly described needed for description of the prior art, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise for not paying creative work
Under, can be with according to these other accompanying drawings of accompanying drawings acquisition.
Fig. 1 is the structural representation of the cracking system equipment of junked tire micelle of the present utility model.
Specific embodiment
Below in conjunction with the accompanying drawings preferred embodiment of the present utility model is described in detail, so that advantage of the present utility model
Can be easier to be readily appreciated by one skilled in the art with feature, it is apparent clear and definite so as to make to protection domain of the present utility model
Define.
Refering to shown in Fig. 1, a kind of cracking system equipment of junked tire micelle that this utility model is provided, including molten salt furnace
1 and pyrolysis furnace 2, molten salt furnace 1 is entered salt pipe 3 and first by first respectively and goes out salt pipe 4 and be connected with pyrolysis furnace 2, and first enters on salt pipe 3
Be also equipped with salt pump 5, on molten salt furnace 1, be also equipped with fuel air pipe 6, molten salt furnace 1 include air chamber 101 from top to bottom,
Liquid chambers 102 and slag charge chamber 103, liquid chambers 102 are also connected with gasification kettle 8 by liquid line 7, and slag charge chamber 103 also passes through first
Drawing mechanism 9 is connected with magnetic separator 10, and gasification kettle 8 is also connected with magnetic separator 10 by the second drawing mechanism 11, magnetic
Select seperator 10 to be also connected with white carbon black tank 12 and steel wire retracting device 13 respectively, air chamber 101 also by the first breather 14 with
Rectifying column 15 is connected, and gasification kettle 8 is also connected with rectifying column 15 by the second breather 16, is provided with gas tube on rectifying column 15
201st, light oil pipe 202, oil pipe 203, gas tank 201 are also connected with molten salt furnace 1.By arranging molten salt furnace 1, and pass through fused salt
Heating pyrolysis furnace 2 and gasification kettle 8, tire micelle is added into pyrolysis furnace 2 stove 1, and pyrolysis furnace 2 decomposes micelle, micro-molecular gas,
White carbon black solid after light oil and heavy oil gasification, the metal in tire micelle and decomposition retains, and part heavy oil after gasification can be again
It is cooled to liquid to be attached on pyrolysis furnace 2, the metal and white carbon black in slag charge chamber 103 can enter magnetic by the first drawing mechanism 9
Select seperator 10, magnetic separator 10 separate metal and white carbon black, metal is transported to into steel wire retracting device 13, charcoal then
It is black to be transported in white carbon black tank 12, and the heavy oil for liquefying again enters gasification kettle 8, molten salt furnace by liquid line 7 from liquid chambers 102
1 heating and gasifying kettle 8, heavy oil gasification, the metal and white carbon black for being partially into gasification kettle 8 are divided into magnetic separation by the second drawing mechanism 11
Disembark 10, it is possible to increase the collection rate of oil gas, the gas in air chamber 101 enters rectifying column 15, rectification goes out gasoline, diesel oil and weight
Oil, is collected respectively, and burning during lighter fuel gas is imported into molten salt furnace 1 provides heat for molten salt furnace.By the device, tire
Micelle cleavage rate is high, the lysate response rate is high, and continuously can produce, energy consumption it is low.
In the present embodiment, 1 bottom of molten salt furnace is also connected with multiple emergent storage tanks 18 by cooling plug 17.For molten
When in salt stove 1, pressure is excessive, storage medium salt, and medium is added in molten salt furnace 1 when medium salt is inadequate in molten salt furnace 1
Salt.Gasification kettle 8 enters salt pipe 19 and second by second respectively and goes out salt pipe 20 and molten salt furnace 1.It is gas for the convenient molten salt furnace 1 that passes through
Change 8 heat supply of kettle.Heating-up temperature is high, and the thermal efficiency is high.Preferably, light oil pipe 202 and oil pipe 203 with circulating water cooling device 21
Connection.For cooling down to the fluid in light oil pipe 202 and oil pipe 203, the outlet pipe of circulating water cooling device 21 is also handed over heat
Changing device 22 connects, and heat-exchange device 22 is arranged on fuel air pipe 6.WATER AS FLOW MEDIUM after by heat absorption is entered heating fuel
Fuel in trachea 6.Improve the thermal efficiency.
The above, specific embodiment only of the present utility model, but protection domain of the present utility model do not limit to
In this, any change or replacement expected without creative work should all be covered within protection domain of the present utility model.
Therefore, the protection domain that protection domain of the present utility model should be limited by claims is defined.
Claims (3)
1. a kind of cracking system equipment of junked tire micelle, it is characterised in that：Including molten salt furnace and pyrolysis furnace, the molten salt furnace
Enter salt pipe and first by first respectively to go out salt pipe and be connected with pyrolysis furnace, described first enters salt pump is also equipped with salt pipe, described
It is also equipped with fuel air pipe on molten salt furnace, the molten salt furnace includes air chamber from top to bottom, liquid chambers and slag charge chamber, institute
State liquid chambers also to connect with gasification kettle by liquid line, the slag charge chamber is also connected with magnetic separator by the first drawing mechanism
Logical, the gasification kettle is also connected with magnetic separator by the second drawing mechanism, the magnetic separator also respectively with white carbon black tank
Connect with steel wire retracting device, the air chamber also connected with rectifying column by the first breather, the kettle that gasifies also passes through the
Two breathers are connected with rectifying column, are provided with gas tube, light oil pipe, oil pipe on the rectifying column, the gas tank also with it is molten
Salt stove is connected；
The fused salt furnace bottom is also connected with multiple emergent storage tanks by cooling plug；The gasification kettle enters salt by second respectively
Pipe and second goes out salt pipe and molten salt furnace.
2. the cracking system equipment of junked tire micelle according to claim 1, it is characterised in that：The light oil pipe and weight
Oil pipe is connected with circulating water cooling device.
3. the cracking system equipment of junked tire micelle according to claim 2, it is characterised in that：The circulating water
The outlet pipe of device is also connected with heat-exchange device, and the heat-exchange device is arranged on the fuel air pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621152579.4U CN206127213U (en) | 2016-10-24 | 2016-10-24 | Cracking system equipment of junked tire micelle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621152579.4U CN206127213U (en) | 2016-10-24 | 2016-10-24 | Cracking system equipment of junked tire micelle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206127213U true CN206127213U (en) | 2017-04-26 |
Family
ID=58575587
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621152579.4U Active CN206127213U (en) | 2016-10-24 | 2016-10-24 | Cracking system equipment of junked tire micelle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206127213U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111484758A (en) * | 2020-04-15 | 2020-08-04 | 安徽省克林泰迩再生资源科技有限公司 | Method for preparing carbon black by adopting molten salt to thermally treat waste tires |
-
2016
- 2016-10-24 CN CN201621152579.4U patent/CN206127213U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111484758A (en) * | 2020-04-15 | 2020-08-04 | 安徽省克林泰迩再生资源科技有限公司 | Method for preparing carbon black by adopting molten salt to thermally treat waste tires |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200827 Address after: 100089 building 3, 11 Changchun Road, Haidian District, Beijing 801 Patentee after: SINOHOPE GROUP Co.,Ltd. Address before: 100081, No. 76, South Road, Haidian District college, Haidian District, Beijing, Beijing Patentee before: CISRI ENERGY SAVING TECHNOLOGY Co.,Ltd. |
|
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20230329 Granted publication date: 20170426 |