CN204548538U - Phenol resin processing unit (plant) - Google Patents
Phenol resin processing unit (plant) Download PDFInfo
- Publication number
- CN204548538U CN204548538U CN201520086329.4U CN201520086329U CN204548538U CN 204548538 U CN204548538 U CN 204548538U CN 201520086329 U CN201520086329 U CN 201520086329U CN 204548538 U CN204548538 U CN 204548538U
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- batch
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- feed pipe
- phenol resin
- plant
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Abstract
The utility model discloses a kind of phenol resin processing unit (plant), aim to provide a kind of phenol resin processing unit (plant) improving the production automation, its drip irrigation device is that material to be processed in storage material storehouse is sent in pulveriser by feedway, block phenol resin barreling is after the phenol resin of fine powdered by pulveriser, thinner Powdered phenolic resins is inhaled into feed pipe through the negative pressure of high pressure air suctiton ventilator, flowing in point batch can through feed pipe, because feed pipe and a point batch can are tangent vibrational power flow, and the extension of feed pipe in point batch can twist, therefore the phenol resin of fine powdered moves to sub-material pot bottom twist along dividing the inwall of batch can, because air specific weight is less than powdered phenol-formaldehyde resin, therefore air cannot be driven in point batch can, therefore powdered phenol-formaldehyde resin can along the gap between the inwall of point batch can and the outer wall of isolation bucket to whereabouts, finally fall into sub-material pot bottom to pack from discharge port blanking, realize the automation of manufacturing line.
Description
Technical field
The utility model relates to phenol resin manufacture field, and more particularly, it relates to a kind of phenol resin processing unit (plant).
Background technology
Phenolaldehyde moulding compound be with themoplasticity or thermosetting phenolic resin for matrix, add the thermosetting plastic that organic and inorganic filler and other compounding ingredient are processed into.Phenol resin and molding compound thereof are the kinds of suitability for industrialized production the earliest in synthetic resin, plastics, so far the history of existing nearly over one hundred year.Raw material sources based on them are wider, production technology and equipment simple, molding processibility is good, price is cheaper, and very excellent resistance to heat, mechanical property, electrical property, thermal behavior, ablation property, chemical nature and radiation resistance can be obtained by all means, especially there is good flame retardance, low rate of being fuming, little generation pernicious gas, become mechanical, electric, building, mining, national defence and the indispensable material of other industrial circle.
When processing phenolaldehyde moulding compound, wherein phenol resin requires the state in fine powder, it is collect pack after fine powdered that production phenol resin is normally processed in pulveriser, but phenol resin but cannot effectively be collected after the course of processing in prior art, all to be gone by artificial screening to collect effective finished product, inefficiency.
Utility model content
For the deficiency that prior art exists, the purpose of this utility model is to provide a kind of phenol resin processing unit (plant) improving the production automation.
For achieving the above object, the utility model provides following technical scheme: a kind of phenol resin processing unit (plant), comprise pulveriser and storage material storehouse, and for material to be processed in storage material storehouse being sent to the feedway in pulveriser, also include point batch can being provided with cavity volume, described point of batch can includes discharge port and inlet point and negative pressure mouth, described discharge port is positioned at the bottom of point batch can, described inlet point is positioned at the top of point batch can, described negative pressure mouth is positioned at the centre of sub-material tank top end face, described point of batch can internal clearance is provided with isolation bucket, described isolation bucket opening is arranged towards negative pressure mouth, described point of batch can is provided with one end and the through feed pipe of cavity volume relative to inlet point place, the described feed pipe other end and pulveriser conducting, described feed pipe is tangent vibrational power flow with a point batch can, the extension of described feed pipe in point batch can twist, described point of batch can is provided with the negative tube through with cavity volume relative to negative pressure mouth place, described negative tube one end extends in isolation bucket, the other end is provided with high pressure air suctiton ventilator.
Described discharge port place is provided with Blowing stopper.
Described feed pipe is downward-sloping to inlet point direction outside point batch can be arranged in horizon.
The bottom of described point of batch can is that inverted cone-shaped structure is arranged.
A kind of phenol resin processing unit (plant), comprise pulveriser and storage material storehouse, and for material to be processed in storage material storehouse being sent to the feedway in pulveriser, also include point batch can being provided with cavity volume, described point of batch can includes discharge port and inlet point and negative pressure mouth, described discharge port is positioned at the bottom of point batch can, described inlet point is positioned at the top of point batch can, described negative pressure mouth is positioned at the centre of sub-material tank top end face, described point of batch can internal clearance is provided with isolation bucket, described isolation bucket opening is arranged towards negative pressure mouth, described point of batch can is provided with one end and the through feed pipe of cavity volume relative to inlet point place, the described feed pipe other end and pulveriser conducting, described feed pipe is tangent vibrational power flow with a point batch can, the extension of described feed pipe in point batch can twist, described point of batch can is provided with the negative tube through with cavity volume relative to negative pressure mouth place, described negative tube one end extends in isolation bucket, the other end is provided with high pressure air suctiton ventilator.By adopting technique scheme, phenol resin to be processed is inserted after in storage material storehouse, by feedway, material to be processed is sent in pulveriser, block phenol resin barreling is after the phenol resin of fine powdered by pulveriser, by the feed pipe be connected with pulveriser discharging opening, thinner Powdered phenolic resins is inhaled into feed pipe through the negative pressure of high pressure air suctiton ventilator and (it should be noted that the phenol resin because block grain is larger cannot be siphoned away by negative pressure herein, therefore be conducive to screening effective finished product fast by the structure of negative pressure suction pulverulent material), flowing in point batch can through feed pipe, because feed pipe and a point batch can are tangent vibrational power flow, and the extension of feed pipe in point batch can twist, therefore the phenol resin of fine powdered moves to sub-material pot bottom twist along dividing the inwall of batch can, because air specific weight is less than powdered phenol-formaldehyde resin, therefore air cannot be driven in point batch can, therefore powdered phenol-formaldehyde resin can along the gap between the inwall of point batch can and the outer wall of isolation bucket to whereabouts, finally fall into sub-material pot bottom to pack from discharge port blanking, realize the automation of manufacturing line, easily easy and simple to handle, reduce labour intensity and the productive costs of operator, improve production efficiency, be conducive to market competition.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model phenol resin processing unit (plant);
Fig. 2 is the cross-sectional view of point batch can.
Reference numeral: 1, divide batch can; 11, cavity volume; 12, discharge port; 13, inlet point; 14, negative pressure mouth; 15, bucket is isolated; 16, feed pipe; 17, negative tube; 2, pulveriser; 3, storage material storehouse; 4, feedway; 5, high pressure air suctiton ventilator; 6, Blowing stopper.
Detailed description of the invention
With reference to Fig. 1, Fig. 2, the utility model phenol resin processing unit (plant) embodiment is described further.
A kind of phenol resin processing unit (plant), comprise pulveriser 2 and storage material storehouse 3, and for material to be processed in storage material storehouse 3 being sent to the feedway 4 in pulveriser 2, also include point batch can 1 being provided with cavity volume 11, described point of batch can 1 includes discharge port 12 and inlet point 13 and negative pressure mouth 14, described discharge port 12 is positioned at the bottom of point batch can 1, described inlet point 13 is positioned at the top of point batch can 1, described negative pressure mouth 14 is positioned at the centre of point batch can 1 top end face, described point of batch can 1 internal clearance is provided with isolation bucket 15, described isolation bucket 15 opening is arranged towards negative pressure mouth 14, described point of batch can 1 is provided with one end and the through feed pipe 16 of cavity volume 11 relative to inlet point 13 place, described feed pipe 16 other end and pulveriser 2 conducting, described feed pipe 16 and point batch can 1 are in tangent vibrational power flow, the extension of described feed pipe 16 in point batch can 1 twist, described point of batch can 1 is provided with the negative tube 17 through with cavity volume 11 relative to negative pressure mouth 14 place, described negative tube 17 one end extends in isolation bucket 15, the other end is provided with high pressure air suctiton ventilator 5.Phenol resin to be processed is inserted after in storage material storehouse 3, by feedway 4, material to be processed is sent in pulveriser 2, block phenol resin barreling is after the phenol resin of fine powdered by pulveriser 2, by the feed pipe 16 be connected with pulveriser 2 discharging opening, thinner Powdered phenolic resins is inhaled into feed pipe 16(through the negative pressure of high pressure air suctiton ventilator 5 and it should be noted that the phenol resin because block grain is larger cannot be siphoned away by negative pressure herein, therefore be conducive to screening effective finished product fast by the structure of negative pressure suction pulverulent material), flowing in point batch can 1 through feed pipe 16, because feed pipe 16 and point batch can 1 are in tangent vibrational power flow, and the extension of feed pipe 16 in point batch can 1 twist, therefore the phenol resin of fine powdered moves twist along dividing the inwall of batch can 1 bottom point batch can 1, because air specific weight is less than powdered phenol-formaldehyde resin, therefore air cannot be driven in point batch can 1, therefore powdered phenol-formaldehyde resin can along the gap between the inwall of point batch can 1 and the outer wall of isolation bucket 15 to whereabouts, finally fall into bottom point batch can 1 and pack from discharge port 12 blanking, realize the automation of manufacturing line, easily easy and simple to handle, reduce labour intensity and the productive costs of operator, improve production efficiency, be conducive to market competition.Because powdered phenol-formaldehyde resin can along the gap between the inwall of point batch can 1 and the outer wall of isolation bucket 15 to whereabouts, therefore powdered phenol-formaldehyde resin can not fall in isolation bucket 15, to keep in point batch can 1, while negative pressure state, also powdered phenol-formaldehyde resin to be taken out of from negative tube 17 so negative tube 17 one end extends to isolation bucket 15 inherence.
Described discharge port 12 place is provided with Blowing stopper 6.Owing to being in negative pressure state in point batch can 1, therefore Blowing stopper 6 can make discharge port 12 place become windless condition, facilitates the blanking of powdered phenol-formaldehyde resin.
Described feed pipe 16 is arranged to inlet point 13 direction is downward-sloping in horizon outside point batch can 1.Feed pipe 16 is downward-sloping, makes the powdered phenol-formaldehyde resin of drive have the stronger trend be rotated down, and is conducive to the blanking accelerating powdered phenol-formaldehyde resin, increases work efficiency, improve the automatization level of manufacturing line.
The bottom of described point of batch can 1 is that inverted cone-shaped structure is arranged.Powdered phenol-formaldehyde resin in convenient point batch can 1 concentrates downward landing, is conducive to increasing work efficiency, improves the automatization level of manufacturing line.
Claims (4)
1. a phenol resin processing unit (plant), comprise pulveriser and storage material storehouse, and for material to be processed in storage material storehouse being sent to the feedway in pulveriser, it is characterized in that: also include point batch can being provided with cavity volume, described point of batch can includes discharge port and inlet point and negative pressure mouth, described discharge port is positioned at the bottom of point batch can, described inlet point is positioned at the top of point batch can, described negative pressure mouth is positioned at the centre of sub-material tank top end face, described point of batch can internal clearance is provided with isolation bucket, described isolation bucket opening is arranged towards negative pressure mouth, described point of batch can is provided with one end and the through feed pipe of cavity volume relative to inlet point place, the described feed pipe other end and pulveriser conducting, described feed pipe is tangent vibrational power flow with a point batch can, the extension of described feed pipe in point batch can twist, described point of batch can is provided with the negative tube through with cavity volume relative to negative pressure mouth place, described negative tube one end extends in isolation bucket, the other end is provided with high pressure air suctiton ventilator.
2. phenol resin processing unit (plant) according to claim 1, is characterized in that: described discharge port place is provided with Blowing stopper.
3. phenol resin processing unit (plant) according to claim 1 and 2, is characterized in that: described feed pipe is downward-sloping to inlet point direction outside point batch can be arranged in horizon.
4. phenol resin processing unit (plant) according to claim 3, is characterized in that: the bottom of described point of batch can is that inverted cone-shaped structure is arranged.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520086329.4U CN204548538U (en) | 2015-02-06 | 2015-02-06 | Phenol resin processing unit (plant) |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520086329.4U CN204548538U (en) | 2015-02-06 | 2015-02-06 | Phenol resin processing unit (plant) |
Publications (1)
Publication Number | Publication Date |
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CN204548538U true CN204548538U (en) | 2015-08-12 |
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Application Number | Title | Priority Date | Filing Date |
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CN201520086329.4U Expired - Fee Related CN204548538U (en) | 2015-02-06 | 2015-02-06 | Phenol resin processing unit (plant) |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105435898A (en) * | 2016-01-07 | 2016-03-30 | 高碧 | Phenolic resin treatment device |
-
2015
- 2015-02-06 CN CN201520086329.4U patent/CN204548538U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105435898A (en) * | 2016-01-07 | 2016-03-30 | 高碧 | Phenolic resin treatment device |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150812 Termination date: 20170206 |