CN201823582U - Mixing and crushing production line of bakelite powder - Google Patents
Mixing and crushing production line of bakelite powder Download PDFInfo
- Publication number
- CN201823582U CN201823582U CN2010205131730U CN201020513173U CN201823582U CN 201823582 U CN201823582 U CN 201823582U CN 2010205131730 U CN2010205131730 U CN 2010205131730U CN 201020513173 U CN201020513173 U CN 201020513173U CN 201823582 U CN201823582 U CN 201823582U
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- China
- Prior art keywords
- moulding powder
- production line
- phenolic moulding
- conveyer
- cyclone separator
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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.)
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Abstract
The utility model discloses a mixing and crushing production line of bakelite powder, which comprises a storage vat (60) and a batch mixing vat (70) connected with the storage vat, and is characterized in that: the start end of a conveyer belt is joined with the mixed and crushed bakelite clinker and the tail end of the conveyer belt is connected with a rough crusher (20); the discharging end of the rough crusher is connected with an auger conveyer; the output end of the auger conveyer is connected with the inlet end of a crusher (40); the outlet end of the crusher is connected with the inlet end of a cyclone separator (50); and one outlet end of the cyclone separator is connected with the storage vat and the upper outlet end of the cyclone separator is connected with a dust collection processor (80). The mixing and crushing production line of bakelite powder ensures that the crushing effect is better and the quality is higher, improves the automation degree of the production, removes more manual operation steps, realizes the automatic crushing and continuous automatic production of the bakelite powder, enhances the production efficiency, and reduces the labor intensity of the worker and the labor cost.
Description
Technical field
The utility model relates to a kind of phenolic moulding powder production equipment, especially relates to the phenolic moulding powder of a kind of use in the phenolic moulding powder production process and mixes the pulverizing production line.
Background technology
Phenolic moulding powder has higher mechanical strength, good insulation performance performance, and the anticorrosion protection against the tide is high temperature resistant, is applicable to high-speed electric expreess locomotive commutator and pressing requirements height, complex-shaped electric, electronic component; Phenolic moulding powder is as in a kind of application research of polymer in composite very widely special status being arranged simultaneously, phenolic moulding powder 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 moulding powder is that bedding and padding mix with phenolic moulding 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 moulding powder that passes through the injection machine moulding again.Usually mix in the production process at phenolic moulding powder, mix crushing process and be in automanual production status, need carry out manually the mixing of materials blowing being operated, time-consuming consumption power, influence production efficiency, 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 need carry out manually the mixing of materials blowing being operated for solving to exist in the existing phenolic moulding powder production process, time-consuming consumption power, influence production efficiency, also cause simultaneously partial material that caking and the excessive phenomenon of fineness are arranged easily, cause mixing inhomogeneous, a kind of automatic discharging batch mixing work that can finish material that influences present situations such as controllable quality and raising and provide, improve automaticity in the production process, enhance productivity, the phenolic moulding powder that also can further improve the phenolic moulding powder product quality simultaneously mixes pulverizes production line.
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 moulding powder mixes pulverizes production line, comprise storage vat, batch tempering tank that is connected with storage vat, it is characterized in that: the initial front end of conveyer belt is connected mutually with the phenolic moulding powder thing grog that mixes after pulverizing, conveyer belt is terminal to be connected with Roughpulverizer, the discharge end of Roughpulverizer is connected with the auger conveyer, auger conveyer output is connected mutually with the pulverizer arrival end, the pulverizer port of export is connected with the cyclone inlet end, a port of export of cyclone separator is connected with storage vat, and the top port of export of cyclone separator is connected with the dust collection processor.After phenolic moulding powder grog after mixing is pulverized is transported to the conveyer belt end and delivers into Roughpulverizer from the initial front end of conveyer belt, in Roughpulverizer, carry out and to carry the phenolic moulding powder grog of coming in to carry out coarse crushing work, through after the coarse crushing of Roughpulverizer, outputing to pulverizer by the auger conveyer again, to carry out further fine powder broken, make crushing effect better, avoid the phenolic moulding powder that produces bulk or do not meet fineness requirement, to be input to and expect in the cyclone separator that gas separates through obtaining satisfactory phenolic moulding powder after pulverizing again, waste gas with phenolic moulding powder and production and processing generation, useless dirt is separated, after the phenolic moulding powder of separating enters storage vat and batch tempering tank, in batch tempering tank, be mixed into the phenolic moulding powder that conforms to quality requirements, again the phenolic moulding powder that conforms to quality requirements emitted to receive from a batch tempering tank and install to given place; Simultaneously after process cyclone separator separating treatment, the waste gas and the useless dirt that come out from cyclone separator insert the dust collection processor, with the dust collection collected in the dust collection processor, the waste gas of allow compliance with emission standards picked out through exhaust gas fan be discharged in the atmosphere, after dust collection arrives and to a certain degree measures simultaneously, can emit and be attached to given place.Can realize automatic discharging batch mixing work, improve automaticity in the production process, enhance productivity, avoid carrying out manually, time-consuming consumption power, influence production efficiency the operation of mixing of materials blowing to material; Also further improve simultaneously the phenolic moulding powder product quality.
As preferably, described auger conveyer comprises the first auger conveyer and the second auger conveyer, the first auger conveyer is connected with the Roughpulverizer output, the first auger conveyer output is connected with the second auger conveyer, and the second auger conveyer port of export is connected mutually with the pulverizer arrival end.The layout that two-stage auger conveyer can better utilization be saved place, production space makes the layout of production site more reasonable, reduces place input cost expense.
As preferably, described cyclone separator is provided with blower fan at the linkage section place with storage vat.The adding of blower fan is used and has been guaranteed that better phenolic moulding powder can enter in the storage vat fully more reliably, avoids occurring pouring in down a chimney the into generation of the interior phenomenon of cyclone separator.
As preferably, described Roughpulverizer adopts two roller grinding modes, makes the crushing effect of coarse crushing reach better.
As preferably, described conveyer belt is provided with the blower fan cooling section on its conveyer belt.To cool from the phenolic moulding powder grog on the conveyer belt, so that in Roughpulverizer, obtain better crushing effect.
As preferably, described dust collection processor is connected with exhaust output tube at an upper portion thereof, and the output of exhaust output tube is provided with exhaust gas fan, with the toxic emission of allow compliance with emission standards in atmosphere.
The beneficial effects of the utility model are: improve production automation degree, remove the manually-operated steps that need to adopt more, realize the automatic pulverizing production work automatically continuously to phenolic moulding powder, enhance productivity, reduce labor strength, reduce labor cost.Avoid occurring in the production process appearance that partial material has caking and the excessive phenomenon of fineness simultaneously, improved the product quality of phenolic moulding powder.
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 that the utility model phenolic moulding powder mixes the preferred implementation of pulverizing production line.
The specific embodiment
Among the embodiment shown in Figure 1, a kind of phenolic moulding powder mixes pulverizes production line, comprise storage vat 60, batch tempering tank 70 that is connected with storage vat 60, be connected with conveyer belt 10 initial front ends and through the phenolic moulding powder grog after mix pulverizing and be input on the conveyer belt, conveyer belt 10 ends are equipped with Roughpulverizer 20 and are connected mutually with Roughpulverizer 20, Roughpulverizer 20 belows are equipped with the first auger conveyer 21, the discharge end of Roughpulverizer 20 is connected with the first auger conveyer 21, the first auger conveyer, 21 belows are equipped with the second auger conveyer 30, the first auger conveyer, 21 outputs are connected mutually with the second auger conveyer 30, the second auger conveyer, 30 belows are equipped with pulverizer 40, the second auger conveyer, 30 ports of export are connected mutually with pulverizer 40 arrival ends, pulverizer 40 ports of export are connected with cyclone separator 50 arrival ends by pipeline 41, a port of export of cyclone separator 50 is connected with storage vat 60, the top port of export of cyclone separator 50 is connected with dust collection processor 80 by pipeline 52, is input in the dust collection processor 80.Cyclone separator 50 is equipped with blower fan 51 at the linkage section place with storage vat 60.Two rollers are installed on the Roughpulverizer 20 adopt two roller grinding modes.Conveyer belt 10 is equipped with the blower fan cooling section on its conveyer belt.Dust collection processor 80 is connected with exhaust output tube 81 at an upper portion thereof, and the output of exhaust output tube 81 is equipped with exhaust gas fan 90.
During production, after phenolic moulding powder grog after mixing is pulverized is transported to the conveyer belt end and delivers into Roughpulverizer 20 from conveyer belt 10 initial front ends, in Roughpulverizer 20, carry out and to carry the phenolic moulding powder grog of coming in to carry out coarse crushing work, through after the coarse crushing of Roughpulverizer, again by after 21 output of the first auger conveyer and being transferred to the second auger conveyer 30, outputing to pulverizer 40 from the delivery outlet 31 of the second auger conveyer 30, to carry out further fine powder broken, making that crushing effect is better more conforms to quality requirements, and avoids the phenolic moulding powder that produces bulk or do not meet fineness requirement; To be input to and expect in the cyclone separator 50 that gas separates through obtaining satisfactory phenolic moulding powder after pulverizing again, the waste gas of phenolic moulding powder and production and processing generation, useless dirt are separated, after the phenolic moulding powder of separating enters storage vat 60 and batch tempering tank 70, in batch tempering tank 70, be mixed into the phenolic moulding powder that finally conforms to quality requirements, again the phenolic moulding powder that conforms to quality requirements emitted to receive from batch tempering tank 70 and install to given place; Simultaneously after process cyclone separator 50 separating treatment, the waste gas and the useless dirt that come out from cyclone separator insert the dust collection processor 80, with the dust collection collected in dust collection processor 80, the waste gas of allow compliance with emission standards picked out through exhaust gas fan 90 be discharged in the atmosphere, after dust collection arrives and to a certain degree measures simultaneously, can emit and be attached to given place.
Claims (6)
1. a phenolic moulding powder mixes the pulverizing production line, comprise storage vat (60), batch tempering tank (70) that is connected with storage vat (60), it is characterized in that: the initial front end of conveyer belt (10) is connected mutually with the phenolic moulding powder thing grog that mixes after pulverizing, conveyer belt (10) is terminal to be connected with Roughpulverizer (20), the discharge end of Roughpulverizer (20) is connected with the auger conveyer, auger conveyer output is connected mutually with pulverizer (40) arrival end, pulverizer (40) port of export is connected with cyclone separator (50) arrival end, a port of export of cyclone separator (50) is connected with storage vat (60), and the top port of export of cyclone separator (50) is connected with dust collection processor (80).
2. mix according to the described phenolic moulding powder of claim 1 and pulverize production line, it is characterized in that: described auger conveyer comprises the first auger conveyer (21) and the second auger conveyer (30), the first auger conveyer (21) is connected with Roughpulverizer (20) output, first auger conveyer (21) output is connected with the second auger conveyer (30), and second auger conveyer (30) port of export is connected mutually with pulverizer (40) arrival end.
3. mix according to the described phenolic moulding powder of claim 1 and pulverize production line, it is characterized in that: described cyclone separator (50) is provided with blower fan (51) at the linkage section place with storage vat (60).
4. mix according to claim 1 or 2 described phenolic moulding powder and pulverize production line, it is characterized in that: described Roughpulverizer (20) adopts two roller grinding modes.
5. mix according to the described phenolic moulding powder of claim 1 and pulverize production line, it is characterized in that: described conveyer belt (10) is provided with the blower fan cooling section on its conveyer belt.
6. mix according to the described phenolic moulding powder of claim 1 and pulverize production line, it is characterized in that: described dust collection processor (80) is connected with exhaust output tube (81) at an upper portion thereof, and the output of exhaust output tube (81) is provided with exhaust gas fan (90).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205131730U CN201823582U (en) | 2010-09-02 | 2010-09-02 | Mixing and crushing production line of bakelite powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205131730U CN201823582U (en) | 2010-09-02 | 2010-09-02 | Mixing and crushing production line of bakelite powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201823582U true CN201823582U (en) | 2011-05-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205131730U Expired - Fee Related CN201823582U (en) | 2010-09-02 | 2010-09-02 | Mixing and crushing production line of bakelite powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201823582U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102513199A (en) * | 2011-12-13 | 2012-06-27 | 舟山市金寿船舶机械有限公司 | Fine grinding system and grinding method thereof |
| CN104129656A (en) * | 2014-07-24 | 2014-11-05 | 武汉日和汽车零部件有限公司 | Feeding mechanism for bakelite powder |
| CN104643272A (en) * | 2015-01-22 | 2015-05-27 | 成都蜀星饲料有限公司 | Superfine crushing device and superfine crushing method for preparing mixed feed |
| RU170230U1 (en) * | 2016-04-19 | 2017-04-18 | Михаил Андреевич Серёдкин | ENERGY-SAVING INSTALLATION FOR PREPARING TWO-COMPONENT SINTERING CHARGE |
| CN108722625A (en) * | 2017-04-24 | 2018-11-02 | 胡伟明 | Complex magnesium aluminum silicate energy-saving and heat-insulating material process equipment |
-
2010
- 2010-09-02 CN CN2010205131730U patent/CN201823582U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102513199A (en) * | 2011-12-13 | 2012-06-27 | 舟山市金寿船舶机械有限公司 | Fine grinding system and grinding method thereof |
| CN104129656A (en) * | 2014-07-24 | 2014-11-05 | 武汉日和汽车零部件有限公司 | Feeding mechanism for bakelite powder |
| CN104129656B (en) * | 2014-07-24 | 2016-03-23 | 武汉日和汽车零部件有限公司 | A kind of phenolic moulding powder feed mechanism |
| CN104643272A (en) * | 2015-01-22 | 2015-05-27 | 成都蜀星饲料有限公司 | Superfine crushing device and superfine crushing method for preparing mixed feed |
| RU170230U1 (en) * | 2016-04-19 | 2017-04-18 | Михаил Андреевич Серёдкин | ENERGY-SAVING INSTALLATION FOR PREPARING TWO-COMPONENT SINTERING CHARGE |
| CN108722625A (en) * | 2017-04-24 | 2018-11-02 | 胡伟明 | Complex magnesium aluminum silicate energy-saving and heat-insulating material process 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: 20110511 Termination date: 20140902 |
|
| EXPY | Termination of patent right or utility model |