CN202412519U - Drying device for preparing rubber composite material through liquid phase method - Google Patents
Drying device for preparing rubber composite material through liquid phase method Download PDFInfo
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- CN202412519U CN202412519U CN2011205462051U CN201120546205U CN202412519U CN 202412519 U CN202412519 U CN 202412519U CN 2011205462051 U CN2011205462051 U CN 2011205462051U CN 201120546205 U CN201120546205 U CN 201120546205U CN 202412519 U CN202412519 U CN 202412519U
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- drying device
- drying
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- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The utility model relates to a drying device for preparing a rubber composite material through a liquid phase method. The drying device comprises a feeding device (1) and a drying device (3), wherein a slurry distributing device (2) is mounted between the feeding device (1) and the drying device (3), and the drying device (3) comprises a microwave drying device (31) and a hot air drying device (32). The drying device disclosed by the utility model comprises the feeding device and the belt type drying device, and the adopted drying way is of the way combining microwave drying with hot air drying. A latex or latex compound is added from a first layer, then enters a second layer and is finally discharged from a bottom layer, and the water content of rubber after drying is less than 2%.
Description
Technical field
The utility model relates to a kind of drying equipment, particularly relates to the drying equipment that a kind of liquid phase method prepares rubber composite.
Background technology
It is method the most frequently used in the present commercial production that dry blending prepares rubber composite, all is usually in rubber, to add reinforcement auxiliary agent, vulcanizing agent and various compounding aid, processes through dry method is mixing.Mixing this process not only consumes energy but also contaminated environment, difficulty that rubber in mixing process " is eaten powder ", powder flies upward, and environment is produced pollute, also the serious harm health of operators.In addition; Because the limitation of dry method calendering process; Age resistor and the inorganic filler dispersion in rubber matrix can not be very even; Local meeting produces serious agglomeration, does not reach desirable anti-aging and reinforcing effect, also can sacrifice the valuable characteristics (like high resiliency, high-wearing feature etc.) of rubber such as natural rubber itself simultaneously.
The utility model content
To the problems referred to above, the main purpose of the utility model is to provide a kind of liquid phase method to prepare the drying equipment of rubber composite.
The utility model solves above-mentioned technical problem through following technical proposals: a kind of liquid phase method prepares the drying equipment of rubber composite; Comprise feeding device and drying device; Between feeding device and drying device, mortar distributor is installed, said drying device comprises microwave drier and hot-air drying device.
In the practical implementation example of the utility model, said drying device is the belt drying device.
In the practical implementation example of the utility model, said belt drying device is one or more layers formation.
In the practical implementation example of the utility model, the thickness of said belt drying device is 1-20mm.
The positive progressive effect of the utility model is: the drying equipment that the liquid phase method that the utility model provides prepares rubber composite has the following advantages: the utility model is made up of feeding device and belt drying device, and the drying mode of employing is the mode that microwave drying and heated-air drying combine.Latex or latex compound are added by ground floor, get into the second layer then, come out from orlop at last, and the water content of oven dry back rubber is less than 2%.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Fig. 2 is the vertical view of the utility model Fig. 1.
Fig. 3 is the process chart of the utility model.
The specific embodiment
Provide the utility model preferred embodiment below in conjunction with accompanying drawing, to specify the technical scheme of the utility model.
Fig. 1 is the structural representation of the utility model; Fig. 2 is the vertical view of the utility model Fig. 1; As illustrated in fig. 1 and 2: the utility model comprises feeding device 1 and drying device 3; Between feeding device 1 and drying device 3, mortar distributor 2 is installed, drying device 3 comprises microwave drier 31 and hot-air drying device 32, and drying device 3 is the belt drying device.In concrete operation, the belt drying device can be the pattern of one or more layers structure.
Fig. 3 is the process chart of the utility model.The utility model is at first to be that various known rubber chemicals are ground through milling apparatus separately or together; Make the water slurry or the emulsion of various auxiliary agents; Then these water slurries or emulsion are joined in the latex, after dispersed with stirring is even, directly is added to and carries out drying in the utility model drying equipment; Make the epoxy glue of the uncured that contains auxiliary agent, vulcanize then and make goods.Its technical process is as shown in Figure 3.
The utility model is made up of feeding device and belt drying device, and the drying mode of employing is the mode that microwave drying and heated-air drying combine.Latex or latex compound are added by ground floor, get into the second layer then, come out from orlop at last, and the water content of oven dry back rubber is less than 2%.
In dry run, the baking temperature of the belt drying device of the utility model is controlled in 30-100 ℃ the scope.The thickness that latex or latex compound are added to the belt drying device is 1-20mm.Belt drying device delivery band is that polytetrafluoroethylene (PTFE) is done.The mode of heating that drying device adopted also can be other higher mode of heatings of the thermal efficiency.
More than show and described basic principle of the utility model and the advantage of principal character and the utility model.The technical staff of the industry should understand; The utility model is not restricted to the described embodiments; The principle of describing in the foregoing description and the specification that the utility model just is described, under the prerequisite that does not break away from the utility model spirit and scope, the utility model also has various changes and modifications; These variations and improvement all fall in the utility model scope that requires protection, and the utility model requires protection domain to be defined by appending claims and equivalent thereof.
Claims (4)
1. a liquid phase method prepares the drying equipment of rubber composite; It is characterized in that: said drying equipment comprises feeding device (1) and drying device (3); Between feeding device (1) and drying device (3), mortar distributor (2) is installed, said drying device (3) comprises microwave drier (31) and hot-air drying device (32).
2. liquid phase method according to claim 1 prepares the drying equipment of rubber composite, it is characterized in that: said drying device (3) is the belt drying device.
3. liquid phase method according to claim 2 prepares the drying equipment of rubber composite, it is characterized in that: said belt drying device is one or more layers formation.
4. liquid phase method according to claim 2 prepares the drying equipment of rubber composite, it is characterized in that: the thickness of said belt drying device is 1-20mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205462051U CN202412519U (en) | 2011-12-23 | 2011-12-23 | Drying device for preparing rubber composite material through liquid phase method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205462051U CN202412519U (en) | 2011-12-23 | 2011-12-23 | Drying device for preparing rubber composite material through liquid phase method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202412519U true CN202412519U (en) | 2012-09-05 |
Family
ID=46737311
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205462051U Expired - Fee Related CN202412519U (en) | 2011-12-23 | 2011-12-23 | Drying device for preparing rubber composite material through liquid phase method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202412519U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105643832A (en) * | 2016-03-31 | 2016-06-08 | 北京万向新元科技股份有限公司 | Natural rubber production process and natural rubber production equipment with solar hot-air pre-dehumidification function |
| CN107449264A (en) * | 2017-09-15 | 2017-12-08 | 四川宏图普新微波科技有限公司 | A kind of polytetrafluoroethyldispersion dispersion resin particle wet feed drying system and method |
| CN109702925A (en) * | 2018-12-19 | 2019-05-03 | 福建三农新材料有限责任公司 | A kind of polytetrafluoroethyldispersion dispersion resin drying equipment |
-
2011
- 2011-12-23 CN CN2011205462051U patent/CN202412519U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105643832A (en) * | 2016-03-31 | 2016-06-08 | 北京万向新元科技股份有限公司 | Natural rubber production process and natural rubber production equipment with solar hot-air pre-dehumidification function |
| CN107449264A (en) * | 2017-09-15 | 2017-12-08 | 四川宏图普新微波科技有限公司 | A kind of polytetrafluoroethyldispersion dispersion resin particle wet feed drying system and method |
| CN107449264B (en) * | 2017-09-15 | 2023-05-26 | 四川宏图普新微波科技有限公司 | Polytetrafluoroethylene dispersion resin particle wet material drying system and method |
| CN109702925A (en) * | 2018-12-19 | 2019-05-03 | 福建三农新材料有限责任公司 | A kind of polytetrafluoroethyldispersion dispersion resin drying equipment |
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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: 20120905 Termination date: 20151223 |
|
| EXPY | Termination of patent right or utility model |