CN201250197Y - Automatic continuous production device for plasticizing rubber powder - Google Patents
Automatic continuous production device for plasticizing rubber powder Download PDFInfo
- Publication number
- CN201250197Y CN201250197Y CNU2008202275263U CN200820227526U CN201250197Y CN 201250197 Y CN201250197 Y CN 201250197Y CN U2008202275263 U CNU2008202275263 U CN U2008202275263U CN 200820227526 U CN200820227526 U CN 200820227526U CN 201250197 Y CN201250197 Y CN 201250197Y
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- CN
- China
- Prior art keywords
- rubber powder
- thermal reaction
- automatic continuous
- reaction apparatus
- refrigerating unit
- 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
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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
- 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
Abstract
The utility model relates to an automatic continuous production device for desulphurizing and plasticizing rubber powder in the recycling processing application of the waste rubber, which is provided with a mixing device (1), a feeding device (2), a thermal reaction device (3) and a cooling device (4), which are communicated with each other in turn, wherein, the thermal reaction device (3) is provided with a heating device (5), and the cooling device (4) is provided with a cooling device (6). Rubber powder that is required to be plasticized, activating agent and softener are added into the mixing device (1) to be mixed, and the mixture after the mixing is sent to the feeding device (2) to be further mixed and to be conveyed to the thermal reaction device (3) to be undertaken the desulphurizing plasticizing treatment, and then the plasticized rubber powder is sent into the cooling device (4) to be cooled. The automatic continuous production device has the advantages that the requirements for desulphurizing and plasticizing rubber powder can be satisfied, the automatic continuous production can be realized, the structure is simple, the operation is convenient, the quality is stable, the device is easy to be controlled, the cost is low, and the like.
Description
One, technical field
The utility model is that a kind of waste old reclaims the device that in the processing and utilization rubber powder is carried out the automatic continuous production of desulfurization plastics processing.
Two, background technology
Rubber is as the important strategic goods and materials, and all there is strict control various countries to rubber.China is that a rubber uses big country, also is simultaneously a country that rubber sources is most deficient and the generation waste old is extremely many.For solving China's rubber sources scarcity, China is advocating always, is encouraging, is helping the production of utilizing again of waste old and reclaimed rubber.
Rubber powder is the intermediate product that regenerating waste or used rubber utilizes, and it is a valuable source of producing reclaimed rubber.Therefore its quality is determining the quality of reclaimed rubber.
At present the main dynamic vulcanization process that adopts is handled in the desulfurization of rubber powder, be that the rubber powder and a certain proportion of regenerator (being activator and tenderizer) that need desulfurization to handle are put into the pressurized vessel of sealing, pressurize, heat, add water and carry out the desulfurization processing, there is following defective:
1, pressure is big, and the operating pressure during desulfurization is 2.2～4.0MPa, and dynamically digester need adopt II class pressurized vessel, and life-time service or improper use, can cause potential safety hazards such as tank skin attenuation, even cause equipment and fatal accident.
2, Jia Shui and exhaust gas emission is arranged, for preventing under the hot conditions, rubber powder is heated inequality and charing will add a certain amount of water to form steam or directly feed water vapour as heat-transfer medium when desulfurization, yet water vapor with; Produce complicated reaction with the tenderizer that adds, the waste gas that causes difficulty to be smelt produces, and causes serious environmental to pollute.Though existing processing the, contaminated solution problem fundamentally still at present.
3, production process is that the gap produces, and hand-fed, can not continuous production, and productivity is low, labour intensity height, the effort of taking a lot of work.
4, power consumption is high, owing to be that the gap produces, and all in vain the discharging wastes of high pressure, steam, and production cost height.
5, the quality instability is wayward; Owing to be that the gap produces, quality fluctuation between each batch is big, wayward, and owing to be under the working condition of high pressure, high temperature, high humidity, to carry out complicated reaction, the quality of each batch only just can be known the quality of product behind release, discharge of steam, so the also bad control of the quality of each batch.
6, the rubber powder after handling must carry out just being used for after the processed production of reclaimed rubber products; And the complex process of processed needs a whole set of equipment, and investment is big, energy consumption height, cost height.
Three, summary of the invention
We have developed a kind of rubber powder plasticizing process recently, be waste old to be crushed to 10～40 purpose rubber powders add a certain proportion of activator and tenderizer, behind the uniform mixing, be heated to 180～320 ℃, be incubated 8～15 minutes, carry out the desulfurization plasticizing, promptly get the plasticizing rubber powder after plastifying after the cooling.This technology has can realize automatic continuous production, and no pressure, non-exhaust emission, pollution-free are safe and reliable, steady quality is easy to control, and the plasticizing rubber powder after the processing need not to dewater and both can be directly used in the production of rubber item, and is energy-saving and cost-reducing, less investment, characteristics such as cost is low.
The purpose of this utility model is to provide a kind of automatic continuous producing device for this rubber powder plasticizing process.This device can satisfy the needs of rubber powder desulfurization plastics processing, can realize automatic continuous production, and is simple in structure, easy to operate, steady quality, and easy to control, cost is low.
For achieving the above object, the technology that the utility model is taked is: include whipping appts, feeding device, thermal reaction apparatus and refrigerating unit.Thermal reaction apparatus is provided with heating unit, and refrigerating unit is provided with cooling-cycle device.The discharge port of whipping appts is communicated with the opening for feed of feeding device, and the discharge port of feeding device is communicated with the opening for feed of thermal reaction apparatus, and the discharge port of thermal reaction apparatus is communicated with the opening for feed of refrigerating unit.
The structure formation of feeding device is a lot, can adopt helix transporting device I or other e Foerderanlage.
The structure formation of thermal reaction apparatus is a lot, also can adopt helix transporting device II, and in the arranged outside of helix transporting device II heating unit is arranged.The structure formation of heating unit is a lot, can adopt electric heater unit or heat-conducting oil heating circulation device etc.
The structure formation of refrigerating unit is a lot, can adopt helix transporting device III, and in the arranged outside of helix transporting device III cooling-cycle device is arranged.Cooling-cycle device can adopt air-cooled, also can adopt water-cooled etc.
Whipping appts, feeding device, thermal reaction apparatus and refrigerating unit are connected with electric control gear, can realize control and continuous production automatically.
Needing the rubber powder of plastics processing and activator, tenderizer to add in the whipping appts stirs, send into feeding device after stirring, further stir and be delivered to thermal reaction apparatus by feeding device and carry out the desulfurization plastics processing, sending into refrigerating unit then cools off, cooled plasticizing rubber powder is sent by the discharge port of refrigerating unit, just can supply packing, or directly be delivered to the reclaimed rubber products processing.
The utlity model has the needs that can satisfy rubber powder desulfurization plastics processing, can realize automatic continuous production, simple in structure, easy to operate, steady quality, easy to control, characteristics such as cost is low.
Four, description of drawings
Accompanying drawing is the utility model schematic representation of apparatus.
Five, specific implementation method
The utility model is the device that a kind of automatic continuous production is provided for rubber powder plasticizing process, includes whipping appts 1, feeding device 2, thermal reaction apparatus 3 and refrigerating unit 4.Thermal reaction apparatus 3 is provided with heating unit 5, and refrigerating unit 4 is provided with cooling-cycle device 6.The discharge port of whipping appts 1 is communicated with the opening for feed of feeding device 2, and the discharge port of feeding device 2 is communicated with the opening for feed of thermal reaction apparatus 3, and the discharge port of thermal reaction apparatus 3 is communicated with refrigerating unit 4 opening for feeds.
The structure formation of feeding device 2 is a lot, and present embodiment adopts helix transporting device I.As everyone knows, helix transporting device generally is to drive the screw rod rotation by motor by variator, and the material in the helix transporting device is carried, and has certain stirring action simultaneously.
The structure formation of thermal reaction apparatus 3 is a lot, and present embodiment adopts helix transporting device II, and in the arranged outside of helix transporting device II heating unit 5 is arranged.The structure formation of heating unit 5 is a lot, can adopt electric heater unit or heat-conducting oil heating circulation device etc.Because heat-conducting oil heating, relatively evenly, the heating unit 5 of present embodiment adopts the heat-conducting oil heating circulation device.The heat-conducting oil heating circulation device, can be communicated with the heating cycle cover that is arranged on the helix transporting device II outside by heating thermal oil device, thermal oil is heated in heating thermal oil device, enter the heating cycle cover, material in the helix transporting device II is heated, thermal oil flows back to heating thermal oil device more then, forms heating circulation system.Heating heat-conducting oil can adopt electrically heated.Or the like.
The structure formation of refrigerating unit 4 is a lot, and the refrigerating unit 4 of present embodiment adopts helix transporting device III, and in the arranged outside of helix transporting device III cooling-cycle device 6 is arranged.Cooling-cycle device 6 can adopt air-cooled, also can adopt water-cooled etc.For save energy, and or make full use of waste heat, the refrigerating unit of present embodiment adopts circulating water cooling device.
In order to realize control and continuous production automatically, present embodiment also is provided with electric control gear, and whipping appts 1, feeding device 2, thermal reaction apparatus 3 and refrigerating unit 4 are connected with electric control gear, can realize control and continuous production automatically.
Present embodiment is provided with the temperature sensor of electric control gear in thermal reaction apparatus 3 and refrigerating unit 4, can regulate and control the working temperature of thermal reaction apparatus 3 and refrigerating unit 4, and in electric control gear, be provided with converter plant, by converter plant the travelling speed of whipping appts 1, feeding device 2, thermal reaction apparatus 3 and refrigerating unit 4 is regulated and control.
Needing the rubber powder of plastics processing and activator, tenderizer to add in the whipping appts 1 stirs, send into feeding device 2 after stirring, further stir and be delivered to thermal reaction apparatus 3 by feeding device 2 and carry out the desulfurization plastics processing, sending into refrigerating unit 4 then cools off, cooled plasticizing rubber powder is sent by the discharge port of refrigerating unit 4, just can supply packing, or directly be delivered to the reclaimed rubber products processing.
Because the utility model is provided with and is communicated with whipping appts 1, feeding device 2, thermal reaction apparatus 3 and refrigerating unit 4 successively, and be provided with electric control gear that whipping appts 1, feeding device 2, thermal reaction apparatus 3 and refrigerating unit 4 are regulated and control; Therefore the utlity model has the needs that can satisfy rubber powder desulfurization plastics processing, can realize automatic continuous production, simple in structure, easy to operate, steady quality, easy to control, characteristics such as cost is low.
Claims (7)
1, a kind of rubber powder plasticizing automatic continuous producing device, it is characterized in that: include whipping appts (1), feeding device (2), thermal reaction apparatus (3) and refrigerating unit (4), thermal reaction apparatus (3) is provided with heating unit (5), refrigerating unit (4) is provided with refrigerating unit (6), the discharge port of whipping appts (1) is communicated with the opening for feed of feeding device (2), the discharge port of feeding device (2) is communicated with the opening for feed of thermal reaction apparatus (3), and the discharge port of thermal reaction apparatus (3) is communicated with refrigerating unit (4) opening for feed.
2, rubber powder plasticizing automatic continuous producing device according to claim 1 is characterized in that: feeding device (2) is helix transporting device I.
3, rubber powder plasticizing automatic continuous producing device according to claim 1 is characterized in that: thermal reaction apparatus (3) is helix transporting device II, and in the arranged outside of helix transporting device II heating unit (5) is arranged.
4, rubber powder plasticizing automatic continuous producing device according to claim 3 is characterized in that: the heating unit (5) of described thermal reaction apparatus (3) is the heat-conducting oil heating circulation device.
5, rubber powder plasticizing automatic continuous producing device according to claim 1 is characterized in that: refrigerating unit (4) is helix transporting device III, and in the arranged outside of helix transporting device III cooling-cycle device (6) is arranged.
6, rubber powder plasticizing automatic continuous producing device according to claim 5 is characterized in that: the cooling-cycle device (6) of described refrigerating unit (4) is a circulating water cooling device.
7, rubber powder plasticizing automatic continuous producing device according to claim 1 is characterized in that: also be provided with electric control gear, whipping appts (1), feeding device (2), thermal reaction apparatus (3) and refrigerating unit (4) are connected with electric control gear.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202275263U CN201250197Y (en) | 2008-12-18 | 2008-12-18 | Automatic continuous production device for plasticizing rubber powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202275263U CN201250197Y (en) | 2008-12-18 | 2008-12-18 | Automatic continuous production device for plasticizing rubber powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201250197Y true CN201250197Y (en) | 2009-06-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008202275263U Expired - Fee Related CN201250197Y (en) | 2008-12-18 | 2008-12-18 | Automatic continuous production device for plasticizing rubber powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201250197Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010069258A1 (en) * | 2008-12-18 | 2010-06-24 | 泰安市金山橡胶工业有限公司 | Automatic rubber powder plasticizing method and equipment for automatic rubber powder plasticizing method |
| CN104804215A (en) * | 2015-05-13 | 2015-07-29 | 福建省邵武市恒晖橡胶再生有限公司 | Desulfurizing method for regenerated rubber |
-
2008
- 2008-12-18 CN CNU2008202275263U patent/CN201250197Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010069258A1 (en) * | 2008-12-18 | 2010-06-24 | 泰安市金山橡胶工业有限公司 | Automatic rubber powder plasticizing method and equipment for automatic rubber powder plasticizing method |
| CN104804215A (en) * | 2015-05-13 | 2015-07-29 | 福建省邵武市恒晖橡胶再生有限公司 | Desulfurizing method for regenerated rubber |
| CN104804215B (en) * | 2015-05-13 | 2017-10-03 | 福建省邵武市恒晖橡胶再生有限公司 | A kind of reclaimed rubber sulfur method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20090603 Termination date: 20100118 |