CN201769291U - Mixing and grinding device for phenolic resin - Google Patents
Mixing and grinding device for phenolic resin Download PDFInfo
- Publication number
- CN201769291U CN201769291U CN2010205132362U CN201020513236U CN201769291U CN 201769291 U CN201769291 U CN 201769291U CN 2010205132362 U CN2010205132362 U CN 2010205132362U CN 201020513236 U CN201020513236 U CN 201020513236U CN 201769291 U CN201769291 U CN 201769291U
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- tempering tank
- mixing
- powder
- cyclone separator
- phenolic resins
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Abstract
The utility model discloses a mixing and grinding device for phenolic resin, which includes a first powder mixing barrel (22), a second powder mixing barrel (23) connected with the output end of the first powder mixing barrel, a first auger conveyor (24) connected with an output end of the second powder mixing barrel, and a rubber mixing mill (30) connected with the output end of the first auger conveyor, wherein a cyclone separator (21) is connected with the input end of the first powder mixing barrel, both a grinder (20) and a deduster (25) are connected to the cyclone separator; a second auger conveyor (13) is arranged at the input hole of the grinder; and the input end of the second auger conveyor is connected with the output end of a third powder mixing barrel (11). The mixing and grinding device achieves the automatic and continuous mixing and grinding operations for production material and raw material of phenolic resin, improves the production efficiency, reduces the labor intensity and cost of workers, and avoids the phenomena of partial materials, such as caking and overwhelming fineness.
Description
Technical field
The utility model relates to a kind of reducing mechanism, especially relates to the mixing and pulverizing device of a kind of use in the phenolic resins production process.
Background technology
Phenolic resins is as in a kind of application research of polymer in composite very widely special status being arranged, phenolic resins has good acidproof, alkaline-resisting and insulation thermal insulation, is widely used on the fields such as chemical industry, military affairs, telecommunication, electrical equipment, instrument, commodity and building materials.And the traditional synthetic mode of production of phenolic resins is that bedding and padding mix with phenolic resins wood powder and various mineral matter, drops into consersion unit according to a certain percentage, and synthetic by certain technology again, mixing plasticizing generate the phenolic resins that passes through the injection machine moulding again.
Usually mix in the production process at phenolic resins, mix crushing process and be in automanual production status, also cause simultaneously partial material that caking and the excessive phenomenon of fineness are arranged easily, cause mixing inhomogeneous, influence controllable quality and raising, labor strength is also big simultaneously, needs to drop into more labor cost.
The utility model content
The utility model has caking and the excessive phenomenon of fineness for the existing phenolic resins of solution exists partial material in mixing the pulverizing production process, cause and mix present situation such as inhomogeneous and a kind ofly can better avoiding occurring partial material caking and the excessive phenomenon of fineness are arranged of providing, improve simultaneously and mix the phenolic resins mixing and pulverizing device of pulverizing automaticity in the production process.
The utility model is to solve the problems of the technologies described above the concrete technical scheme that is adopted to be: a kind of phenolic resins mixing and pulverizing device, comprise the first powder tempering tank, the second powder tempering tank that is connected with the first powder tempering tank output, the first auger conveyer that is connected with the second powder tempering tank output, be arranged on the rubber mixing machine of the first auger conveyer output, it is characterized in that: the input of the first powder tempering tank is connected with cyclone separator, be connected with pulverizer and deduster on the cyclone separator respectively, the input port of pulverizer is provided with the second auger conveyer, and the input of the second auger conveyer is connected with the output of the 3rd powder tempering tank.Add raw material by dog-house, mix at the 3rd powder tempering tank, through the quantitative feeding of the second auger conveyer to pulverizer, be fed to cyclone separator with blower fan again material is put into the first powder tempering tank, be put into the second powder tempering tank deposit after regularly mixing and mix, by the first auger conveyer quantitated material-feeding to removing rubber mixing machine.Realization mixes the pulverizing continuous operation automatically to the production material and the raw material of phenolic resins, enhances productivity, and reduces labor strength, reduces labor cost; Cyclone separator will be delivered to the first powder tempering tank through the material that meets fineness requirement after pulverizing, simultaneously will be through in batch mixing, the crushing process, the waste gas that may exist in the material, assorted dirt composition separate through realizing material gas behind the cyclone separator, the waste gas of separating is inserted deduster, handle the back through deduster and discharge.Because the work of cyclone separator and pulverizer is further controlled and avoided occurring in the production process partial material caking and the excessive phenomenon of fineness are arranged, improved the product quality of phenolic resins.
As preferably, the upper end position place of described deduster is connected with pipeline, and pipeline is provided with blower fan.Be discharged in the atmosphere after the waste gas of cyclone separator being separated by blower fan, assorted dirt are handled through deduster and go in the device.
As preferably, be provided with charge door on the staving of described the 3rd powder tempering tank.Add raw material by charge door to the 3rd powder tempering tank.
As preferably, described deduster is connected with the upper port of cyclone separator by tube connector.To handle in being linked into behind the deduster through removing waste gas, assorted dirt that cyclone separator separates.
The beneficial effects of the utility model are: avoided occurring in the production process appearance that partial material has caking and the excessive phenomenon of fineness, realize simultaneously the production material of phenolic resins is mixed the continuous production work of pulverizing automatically, enhance productivity, reduce labor strength, reduce labor cost.
Description of drawings:
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
Fig. 1 is the structural representation of the preferred implementation of the utility model phenolic resins mixing and pulverizing device.
The specific embodiment
Among the embodiment shown in Figure 1, a kind of phenolic resins mixing and pulverizing device, comprise the first powder tempering tank 22, the second powder tempering tank 23 that is connected with the first powder tempering tank, 22 outputs, the first auger conveyer 24 that is connected with the second powder tempering tank, 23 outputs, be installed in the rubber mixing machine 30 of the first auger conveyer, 24 outputs, the input of the first powder tempering tank 22 is connected with cyclone separator 21, cyclone separator 21 upper ends are connected with pulverizer 20 and deduster 25 by tube connector respectively, pulverizer 20 is connected with cyclone separator 21 by pipeline 211, and the material that will satisfy fineness requirement after will pulverizing through pulverizer 20 is input in the cyclone separator 21 by pipeline 211 and goes; The input that the place, input port of pulverizer 20 is equipped with the second auger conveyer, 13, the second auger conveyers 13 is connected with the output of the 3rd powder tempering tank 11, and the output of the second auger conveyer 13 is aimed at the input port 201 of pulverizer 20.The upper end position place of deduster 25 is connected with pipeline 251, and blower fan 26 is installed on the pipeline 251, and blower fan 26 works the discharge effect of strengthening after waste gas is handled from deduster.The staving bottom that the staving upper end of the 3rd powder tempering tank 11 has charge door 12, the three powder tempering tanks 11 is connected with the input of the second auger conveyer 13.Deduster 25 is connected with the upper port of cyclone separator 21 by tube connector 252, and the waste gas that will separate from cyclone separator, assorted dirt are input in the deduster.
During production, add material by dog-house 12, mix at the 3rd powder tempering tank 11, through the second auger conveyer, 13 quantitative feedings to pulverizer 20, being put into the second powder tempering tank, 23 deposits after regularly mixing mixes, to removing rubber mixing machine 30, finish the continuous production work that production material and raw material to phenolic resins mix pulverizing automatically by the first auger conveyer, 24 quantitated material-feedings; Cyclone separator will be delivered to the first powder tempering tank through the material that meets fineness requirement after pulverizing in process of production, simultaneously will be through in batch mixing, the crushing process, the waste gas that may exist in the material, assorted dirt composition separate through realizing material gas behind the cyclone separator, the waste gas of separating is inserted deduster, handle the back through deduster and discharge.
Claims (4)
1. phenolic resins mixing and pulverizing device, comprise the first powder tempering tank (22), the second powder tempering tank (23) that is connected with first powder tempering tank (22) output, the first auger conveyer (24) that is connected with second powder tempering tank (23) output, be arranged on the rubber mixing machine (30) of first auger conveyer (24) output, it is characterized in that: the input of the first powder tempering tank (22) is connected with cyclone separator (21), be connected with pulverizer (20) and deduster (25) on the cyclone separator (21) respectively, the input port of pulverizer (20) is provided with the second auger conveyer (13), and the input of the second auger conveyer (13) is connected with the output of the 3rd powder tempering tank (11).
2. according to the described phenolic resins mixing and pulverizing device of claim 1, it is characterized in that: the upper end position place of described deduster (25) is connected with pipeline (251), and pipeline (251) is provided with blower fan (26).
3. according to the described phenolic resins mixing and pulverizing device of claim 1, it is characterized in that: the staving upper end of described the 3rd powder tempering tank (11) is provided with charge door (12).
4. according to claim 1 or 2 described phenolic resins mixing and pulverizing devices, it is characterized in that: described deduster (25) is connected with the upper port of cyclone separator (21) by tube connector (252).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205132362U CN201769291U (en) | 2010-09-02 | 2010-09-02 | Mixing and grinding device for phenolic resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205132362U CN201769291U (en) | 2010-09-02 | 2010-09-02 | Mixing and grinding device for phenolic resin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201769291U true CN201769291U (en) | 2011-03-23 |
Family
ID=43749127
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205132362U Expired - Fee Related CN201769291U (en) | 2010-09-02 | 2010-09-02 | Mixing and grinding device for phenolic resin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201769291U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104428842A (en) * | 2012-06-28 | 2015-03-18 | 西屋电气（德国）有限公司 | Ion exchanger resin crushing apparatus and ion exchanger resin crushing process |
| CN108544681A (en) * | 2018-04-16 | 2018-09-18 | 宁波绿华橡塑机械工贸有限公司 | Plastic film crushes recycling prilling granulator and recycling prilling process |
| CN108544682A (en) * | 2018-04-16 | 2018-09-18 | 宁波绿华橡塑机械工贸有限公司 | The stable crushing plastic film recycling comminutor of feed and recycling prilling process |
-
2010
- 2010-09-02 CN CN2010205132362U patent/CN201769291U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104428842A (en) * | 2012-06-28 | 2015-03-18 | 西屋电气（德国）有限公司 | Ion exchanger resin crushing apparatus and ion exchanger resin crushing process |
| CN104428842B (en) * | 2012-06-28 | 2016-12-28 | 西屋电气（德国）有限公司 | The reducing mechanism of ion exchange resin and the breaking method of ion exchange resin |
| CN108544681A (en) * | 2018-04-16 | 2018-09-18 | 宁波绿华橡塑机械工贸有限公司 | Plastic film crushes recycling prilling granulator and recycling prilling process |
| CN108544682A (en) * | 2018-04-16 | 2018-09-18 | 宁波绿华橡塑机械工贸有限公司 | The stable crushing plastic film recycling comminutor of feed and recycling prilling process |
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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: 20110323 Termination date: 20140902 |
|
| EXPY | Termination of patent right or utility model |