CN206549862U - A kind of high efficiency grinding production system - Google Patents
A kind of high efficiency grinding production system Download PDFInfo
- Publication number
- CN206549862U CN206549862U CN201720062224.4U CN201720062224U CN206549862U CN 206549862 U CN206549862 U CN 206549862U CN 201720062224 U CN201720062224 U CN 201720062224U CN 206549862 U CN206549862 U CN 206549862U
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- CN
- China
- Prior art keywords
- cyclopneumatic separator
- production system
- transport unit
- high efficiency
- feeding mouth
- 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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Abstract
The utility model discloses a kind of high efficiency grinding production system, it includes flour mill, transport unit, cyclopneumatic separator and collection portion；The discharging opening of flour mill and the feeding mouth of transport unit are connected, the discharging opening of transport unit and the feeding mouth of cyclopneumatic separator are connected, the bottom discharge mouthful of cyclopneumatic separator is connected with the feeding mouth of flour mill, the top discharge mouthful of cyclopneumatic separator is connected with the feeding mouth of collection portion, transport unit includes seal closure and the conveyer belt being arranged in seal closure, and the lower end of conveyer belt is provided with vibrator；Cyclopneumatic separator includes cylinder and the whirlwind bucket being arranged under cylinder；One end of whirlwind bucket is connected with inside a high pressure positive blower, whirlwind bucket by ajutage and is provided with a baffle plate away from whirlwind bucket and the madial wall of high pressure positive blower junction, and baffle plate is wave-shape board；It is connected between cylinder and the ajutage on backwind tube, backwind tube and is provided with dust-separation cloth, the inwall of cyclopneumatic separator is provided with spiral lamination；The high efficiency grinding production system low energy, with higher production efficiency.
Description
Technical field
The utility model is specifically related to a kind of high efficiency grinding production system.
Background technology
Lignocellulosic is organic wadding fibrous thing that natural reproducible timber is obtained by chemical treatment, Mechanical Method processing
Matter, it is nontoxic, tasteless, pollution-free, "dead", it is widely used in concrete mortar, plastering, wood pulp sponge, asphalt roads etc.
Field, to preventing coating cracking, improving water-retaining property, the incorporation degree of the stability of raising production and construction, increase intensity, enhancing pair
The adhesive force on surface etc. has good effect；At present, when producing fiber powder, sufficiently effective profit is not carried out to material and the energy
With causing the waste of a large amount of materials and the energy.
Utility model content
The purpose of this utility model is to provide the high high efficiency grinding production system of a kind of low energy, production efficiency.
In order to solve the above technical problems, the utility model provides a kind of high efficiency grinding production system, it includes flour mill, biography
Send portion, cyclopneumatic separator and collection portion；The discharging opening of flour mill and the feeding mouth of transport unit are connected, the discharging opening of transport unit and rotation
The feeding mouth connection of wind seperator, the bottom discharge mouthful of cyclopneumatic separator is connected with the feeding mouth of flour mill, cyclopneumatic separator
Top discharge mouthful is connected with the feeding mouth of collection portion；
Transport unit includes seal closure and the conveyer belt being arranged in seal closure, and the lower end of conveyer belt is used to drive provided with one to be passed
Send the vibrator with vibration；Cyclopneumatic separator includes the cylinder for presenting small lower typhon shape and the whirlwind bucket being arranged under cylinder；
One end of whirlwind bucket is connected with inside a high pressure positive blower, whirlwind bucket away from whirlwind bucket and high pressure positive blower junction by ajutage
Madial wall is provided with a baffle plate, and baffle plate is wave-shape board；It is connected with a backwind tube, backwind tube and sets between cylinder and the ajutage
Dust-separation cloth is equipped with, the inwall of cyclopneumatic separator is provided with spiral lamination.
Further, ajutage is provided with a refrigeration section.
Further, the discharging opening of flour mill is provided with a discharger, and discharger is by controlling circuit to be connected with floor push.
Further, a deduster is provided with seal closure.
Further, deduster is pulse dust collector.
Further, collection portion is dust-removal cloth-bag.
The beneficial effects of the utility model are：The top discharge mouthful of the cyclopneumatic separator of the high efficiency grinding production system is with receiving
The feeding mouth connection in collection portion, the coarse fodder unloaded from the bottom discharge mouth of cyclopneumatic separator enters again to be ground in flour mill, is filled
Divide and make use of resource, reduce cost, improve production efficiency；Wind in cyclopneumatic separator is sent to whirlwind point through backwind tube again
In disembarking, now, it is possible to decrease the power output of high pressure positive blower, sufficient utilization is carried out to wind, the energy has been saved；Dust-separation cloth
Setting avoids fiber powder from entering backwind tube, influences the normal work of the cyclopneumatic separator；Sent into through high pressure positive blower or backwind tube
Wind carries out cooling refrigeration so that it can cool down fiber powder and be rubbed in cyclonic separation with cylinder in the presence of refrigeration section to wind
Wipe the heat produced, it is ensured that the final product quality of fiber powder.
Brief description of the drawings
Fig. 1 is the structural representation of high efficiency grinding production system.
Wherein：1st, flour mill；2nd, transport unit；3rd, cyclopneumatic separator；4th, collection portion；5th, seal closure；6th, conveyer belt；7th, vibrate
Device；8th, cylinder；9th, whirlwind bucket；10th, ajutage；11st, high pressure positive blower；12nd, baffle plate；13rd, backwind tube；14th, dust-separation cloth；15th, freeze
Portion；16th, discharger；17th, deduster.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a kind of embodiment of the utility model, rather than whole realities
Apply example.Based on the embodiment in the utility model, those of ordinary skill in the art institute under the premise of creative work is not made
The every other embodiment obtained, belongs to protection domain of the present utility model.
To make the purpose, technical scheme and advantage of the application clearer, below in conjunction with drawings and the specific embodiments, to this
Application is described in further detail.
In the following description, the reference to " one embodiment ", " embodiment ", " example ", " example " etc. shows
The embodiment or example so described can include special characteristic, structure, characteristic, property, element or limit, but not each real
Applying example or example all necessarily includes special characteristic, structure, characteristic, property, element or limit.In addition, reuse phrase " according to
One embodiment of the application " is not necessarily referring to identical embodiment although it is possible to refer to phase be the same as Example.
According to one embodiment of the application there is provided a kind of high efficiency grinding production system, as shown in figure 1, the high efficiency grinding
Production system, it includes flour mill 1, transport unit 2, cyclopneumatic separator 3 and collection portion 4；The discharging opening of flour mill 1 and transport unit 2
Feeding mouth connection, the discharging opening of transport unit 2 is connected with the feeding mouth of cyclopneumatic separator 3, the bottom discharge mouth of cyclopneumatic separator 3
It is connected with the feeding mouth of flour mill 1, the top discharge mouthful of cyclopneumatic separator 3 is connected with the feeding mouth of collection portion 4.
In specific implementation, wood fibre powder raw material（Thick wood chip material）It is ground, is ground through flour mill 1 into flour mill 1
Fiber dust after mill enters in transport unit 2, then is sent in cyclopneumatic separator 3 and is separated；Wherein, thin fiber powder due to
Lighter in weight, is brought to the top discharge mouthful of cyclopneumatic separator 3, thick fiber powder drops down onto cyclonic separation downwards due to conducting oneself with dignity by whirlwind
The bottom discharge mouthful of machine 3；, can be by adjusting the size of the internal cyclone wind-force of cyclopneumatic separator 3 in practical operation, and then control to divide
The fine granules size separated out, selects fiber powder up to standard.
Wherein, the coarse fodder unloaded from the bottom discharge mouth of cyclopneumatic separator 3 enters again to be ground in flour mill 1, fully
Resource is make use of, cost is reduced, production efficiency is improved；Transport unit 2 includes seal closure 5 and the biography being arranged in seal closure 5
Band 6 is sent, the lower end of conveyer belt 6 is provided with a vibrator 7 for driving conveyer belt 6 to vibrate；In matching somebody with somebody for conveyer belt 6 and vibrator 7
Under cooperation is used, the fiber powder after grinding is shaken and dissipated, it is to avoid fiber powder lumps, and is difficult by cyclonic separation, cause fines from whirlwind point
3 bottom discharge of disembarking mouthful is unloaded, and is entered back into the phenomenon that flour mill 1 is ground repeatedly, both be ensure that the quality of fiber powder, and effectively
Ground improves production efficiency.
Cyclopneumatic separator 3 includes the cylinder 8 for presenting small lower typhon shape and the whirlwind bucket 9 being arranged under cylinder 8；Whirlwind bucket
9 one end is connected with a high pressure positive blower 11 by ajutage 10, and the inside of whirlwind bucket 9 is connected away from whirlwind bucket 9 with high pressure positive blower 11
The madial wall at place is provided with a baffle plate 12, and baffle plate 12 is wave-shape board；A backwind tube is connected between cylinder 8 and the ajutage 10
13, dust-separation cloth 14 is provided with backwind tube 13, the inwall of cyclopneumatic separator 3 is provided with spiral lamination.
In specific implementation, the wind that baffle plate 12 is blown into high pressure positive blower 11 takes blocking effect, and wind is increased in Scrawl, enters
And fiber powder in cyclopneumatic separator 3 is more effectively separated, improve separative efficiency；Wind in cyclopneumatic separator 3 through backwind tube 13 again
It is sent in cyclopneumatic separator 3, now, it is possible to decrease the power output of high pressure positive blower 11, sufficient utilization has been carried out to wind, saves
The energy；Wherein, the setting of dust-separation cloth 14 avoids fiber powder from entering backwind tube 13, influences the normal work of the cyclopneumatic separator 3；
The setting of spiral lamination had both enhanced the dynamics of bearing of cylinder 8, and the separative efficiency of fiber powder is improved again.
According to one embodiment of the application, ajutage 10 is provided with a refrigeration section 15；In specific implementation, through high-pressure blast
The wind that machine 11 or backwind tube 13 are sent into carries out cooling refrigeration so that it can cool down fiber in the presence of refrigeration section 15 to wind
The heat that powder is produced in cyclonic separation with the friction of cylinder 8, it is ensured that the final product quality of fiber powder.
According to one embodiment of the application, the discharging opening of flour mill 1 is provided with a discharger 16, and discharger 16 passes through control
Circuit is connected with floor push；In specific implementation, the discharging quantity of discharger 16 can be controlled by floor push, it is to avoid a large amount of fine
Tie up powder and enter the phenomenon of transport unit 2 simultaneously, and then ensure that the fiber powder entered in transport unit 2 can be dissipated by abundant shake, improve
The efficiency of cyclonic separation.
According to one embodiment of the application, a deduster 17 is provided with seal closure 5, to entering the fibre in transport unit 2
While dimension powder carries out shaking scattered, pass through deduster 17 and carry out dedusting, it is to avoid be full of greatly in transport unit 22 during fiber powder shakes
The dust of amount；And preferably deduster 17 is pulse dust collector 17, with higher efficiency of dust collection.
According to one embodiment of the application, collection portion 4 is dust-removal cloth-bag, it is to avoid when collecting fiber powder, fiber powder is flown upward
Cause the phenomenon of environmental pollution.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or new using this practicality
Type.A variety of modifications to these embodiments will make it will be apparent that defined herein for those skilled in the art
General Principle can in other embodiments be realized in the case where not departing from the spirit or scope of utility model.Therefore, originally
Utility model will not be limited and the embodiments shown herein, and be to fit to and principles disclosed herein and novelty
The property consistent most wide scope of feature.
Claims (6)
1. a kind of high efficiency grinding production system, it is characterised in that：Including flour mill, transport unit, cyclopneumatic separator and collection portion；Institute
The discharging opening for stating flour mill is connected with the feeding mouth of the transport unit, the discharging opening of the transport unit and the cyclopneumatic separator
Feeding mouth is connected, and the bottom discharge mouthful of the cyclopneumatic separator is connected with the feeding mouth of the flour mill, the cyclopneumatic separator
Top discharge mouthful be connected with the feeding mouth of the collection portion, the transport unit includes seal closure and the biography being arranged in seal closure
Band is sent, the lower end of the conveyer belt is provided with a vibrator for driving conveyer belt to vibrate；
The cyclopneumatic separator includes the cylinder for presenting small lower typhon shape and the whirlwind bucket being arranged under the cylinder；The rotation
One end of wind scoop is connected with inside a high pressure positive blower, the whirlwind bucket away from whirlwind bucket and high pressure positive blower junction by ajutage
Madial wall be provided with a baffle plate, the baffle plate be wave-shape board；A backwind tube is connected between the cylinder and the ajutage,
Dust-separation cloth is provided with the backwind tube, the inwall of cyclopneumatic separator is provided with spiral lamination.
2. high efficiency grinding production system according to claim 1, it is characterised in that：The ajutage is provided with a refrigeration
Portion.
3. high efficiency grinding production system according to claim 1, it is characterised in that：The discharging opening of the flour mill is provided with one
Discharger, the discharger is by controlling circuit to be connected with floor push.
4. high efficiency grinding production system according to claim 1, it is characterised in that：A dedusting is provided with the seal closure
Device.
5. high efficiency grinding production system according to claim 4, it is characterised in that：The deduster is pulse dust collector.
6. high efficiency grinding production system according to claim 1, it is characterised in that：The collection portion is dust-removal cloth-bag.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720062224.4U CN206549862U (en) | 2017-01-19 | 2017-01-19 | A kind of high efficiency grinding production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720062224.4U CN206549862U (en) | 2017-01-19 | 2017-01-19 | A kind of high efficiency grinding production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206549862U true CN206549862U (en) | 2017-10-13 |
Family
ID=60358752
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720062224.4U Expired - Fee Related CN206549862U (en) | 2017-01-19 | 2017-01-19 | A kind of high efficiency grinding production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206549862U (en) |
-
2017
- 2017-01-19 CN CN201720062224.4U patent/CN206549862U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20171013 Termination date: 20180119 |