CN207446436U - A kind of ultra micro kudzuvine root starch preparation facilities - Google Patents
A kind of ultra micro kudzuvine root starch preparation facilities Download PDFInfo
- Publication number
- CN207446436U CN207446436U CN201720850007.1U CN201720850007U CN207446436U CN 207446436 U CN207446436 U CN 207446436U CN 201720850007 U CN201720850007 U CN 201720850007U CN 207446436 U CN207446436 U CN 207446436U
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- China
- Prior art keywords
- pipe
- airslide disintegrating
- disintegrating mill
- cyclone separator
- root starch
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Abstract
A kind of ultra micro kudzuvine root starch preparation facilities, including air compressor, air accumulator, airslide disintegrating mill, cyclone separator, pulse dust collector and ventilating mechanisms into；The source outlet of the air compressor connects the air inlet of air accumulator by snorkel, and the compressed gas outlet of air accumulator connects the compressed gas source interface of airslide disintegrating mill by snorkel；The airslide disintegrating mill is equipped with loading hopper；The discharge port of the airslide disintegrating mill is connected to powder delivering pipe.It is when actually crushing, the coarse fodder for being separated cyclone separator by screw conveyor, which is re-fed into airslide disintegrating mill, to be ground, so so that material particles are more tiny, actual discharging is not influenced under the setting of three-way pipe simultaneously, so after the grinding of certain number, coarse fodder gradually decreases, corresponding finished product is separated from pulse dust collector, the effect so entirely prepared is outstanding, while is manually operated without worker, avoids external germ contamination.
Description
Technical field
The utility model is related to kudzuvine root starch preparation field, more particularly, to a kind of ultra micro kudzuvine root starch preparation facilities.
Background technology
It is all to realize preparation using airslide disintegrating mill that existing kudzuvine root starch, which crushes, however in the process of actual production preparation
In, single crushing effect is bad, it is therefore desirable to which artificial feed back is re-grind, and corresponding material will be exposed in air very
For a long time, the quality of material is so easily influenced.
Utility model content
The utility model is to overcome the above situation insufficient, it is desirable to provide a kind of technical solution that can be solved the above problems.
A kind of ultra micro kudzuvine root starch preparation facilities, including air compressor, air accumulator, airslide disintegrating mill, cyclone separator, pulse
Deduster and ventilating mechanisms into；The source outlet of the air compressor connects the air inlet of air accumulator, gas storage by snorkel
The compressed gas outlet of tank connects the compressed gas source interface of airslide disintegrating mill by snorkel；The airslide disintegrating mill is equipped with charging
Bulky grain kudzuvine root starch by loading hopper is sent into airslide disintegrating mill, at this time compressed gas is coordinated to realize kudzuvine root starch circular grinding by bucket, from
And realize the preparation of Ultramicro-powder；The discharge port of the airslide disintegrating mill is connected to powder delivering pipe, high-speed flow mixing ultramicro powder
It is sent from powder delivering pipe；The powder delivering pipe is connected on the air inlet of cyclone separator, is realized using cyclone separator
The collection of powder；The top gas outlet of the cyclone separator is connected to vortex finder, and the bottom of cyclone separator is set
There is coarse fodder discharge pipe, through cyclone separator treated material is divided into more tiny fines and coarse fodder, wherein coarse fodder is from thick
Expect discharge pipe discharge, fines is from vortex finder as air-flow is discharged；The other end of the vortex finder
It is connected on the air inlet of pulse dust collector, the fines in gas is collected using pulse dust collector；The pulse dust collector also passes through
Pulse dust collector exhaust pipe is connected to ventilation blower；The coarse fodder discharge pipe of the cyclone separator is inclined to set, and coarse fodder discharge pipe
End be connected to three-way pipe, the other both ends of wherein three-way pipe are connected on respectively on the feed inlet of screw conveyor and production tube
On feed inlet, the delivery pipe of the screw conveyor is inclined to be set up, and the end on of the delivery pipe of screw conveyor
Feed back pipe is connected with, wherein position directly above of the outlet of the feed back pipe positioned at lower hopper, therefore when actually crushing, pass through
The coarse fodder that screw conveyor separates cyclone separator, which is re-fed into airslide disintegrating mill, to be ground, so that material
Particle is more tiny, while does not influence actual discharging under the setting of three-way pipe, so after the grinding of certain number, slightly
Material gradually decreases, and corresponding finished product is separated from pulse dust collector, and the effect so entirely prepared is outstanding, simultaneously
It is manually operated without worker, avoids external germ contamination.
As further program of the utility model：The snorkel, powder delivering pipe, vortex finder and
Valve is mounted on pulse dust collector exhaust pipe.
As further program of the utility model：The angle of inclination of the delivery pipe of the screw conveyor is 25 ° -30 °.
As further program of the utility model：The lower end outlet of the feed back pipe is socketed with horn-like dust cover.
As further program of the utility model：The feed back pipe is made of stainless steel.
The beneficial effects of the utility model：The utility model is when actually crushing, by screw conveyor by cyclonic separation
The coarse fodder that device is separated, which is re-fed into airslide disintegrating mill, to be ground, so that and material particles are more tiny, while
Actual discharging is not influenced under the setting of three-way pipe, so after the grinding of certain number, coarse fodder gradually decreases, accordingly into
Product are separated from pulse dust collector, and the effect so entirely prepared is outstanding, while are manually operated without worker, keep away
Exempt from external germ contamination.
The additional aspect and advantage of the utility model will be set forth in part in the description, partly will be from following description
In become apparent or recognized by the practice of the utility model.
Description of the drawings
It in order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
It puts, can also be obtained according to these attached drawings other attached drawings.
Fig. 1 is the utility model structure diagram；
In figure：1- air compressors, 2- air accumulators, 3- airslide disintegrating mills, 4- lower hoppers, 5- feed backs pipe, 6- powder carries
Pipe, 7- cyclone separators, 8- vortex finders, 9- coarse fodders discharge pipe, 10- pulse dust collectors, 11- pulse dust collectors row
Tracheae, 12- ventilation blowers, 13- valves.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
Referring to Fig. 1, in the utility model embodiment, a kind of ultra micro kudzuvine root starch preparation facilities, including air compressor 1, storage
Gas tank 2, airslide disintegrating mill 3, cyclone separator 4, pulse dust collector 10 and ventilation blower 12 are formed；The air compressor 1
Source outlet connects the air inlet of air accumulator 2 by snorkel, and the compressed gas of air accumulator 2 is exported connects air-flow crushing by snorkel
The compressed gas source interface of machine 3；The airslide disintegrating mill 3 is equipped with loading hopper, and bulky grain kudzuvine root starch is sent into air-flow by loading hopper
In pulverizer 3, at this time compressed gas is coordinated to realize kudzuvine root starch circular grinding 1, so as to fulfill the preparation of Ultramicro-powder；The air-flow crushing
The discharge port of machine 3 is connected to powder delivering pipe 6, and high-speed flow mixing ultramicro powder is sent from powder delivering pipe 6；The powder is defeated
Pipe 6 is sent to be connected on the air inlet of cyclone separator 4, the collection of powder is realized using cyclone separator 4；The cyclone separator 4
Top gas outlet be connected to vortex finder 8, the bottom of cyclone separator 4 is equipped with coarse fodder discharge pipe 9, through cyclonic separation
Treated that material is divided into more tiny fines and coarse fodder for device 4, and wherein coarse fodder is discharged from coarse fodder discharge pipe 9, and fines is from rotation
Wind separator exhaust pipe 8 is discharged with air-flow；The vortex finder 8 it is another terminate at pulse dust collector 10 into
On gas port, the fines in gas is collected using pulse dust collector 10；The pulse dust collector 10 is also vented by pulse dust collector
Pipe 11 is connected to ventilation blower 12；The coarse fodder discharge pipe 9 of the cyclone separator 7 is inclined to set, and the end of coarse fodder discharge pipe 9 connects
There is three-way pipe, the other both ends of wherein three-way pipe are connected on respectively on the feed inlet of screw conveyor and the feed inlet of production tube
On, the delivery pipe of the screw conveyor is inclined to be set up, and the end on of the delivery pipe of screw conveyor is connected with
Feed back pipe 5, wherein position directly above of the outlet of the feed back pipe 5 positioned at lower hopper 4, therefore when actually crushing, pass through strand
The coarse fodder that cyclone separator 7 is separated is re-fed into airslide disintegrating mill 3 and is ground by imperial conveyer, so that material
Particle is more tiny, while does not influence actual discharging under the setting of three-way pipe, so after the grinding of certain number, slightly
Material gradually decreases, and corresponding finished product is separated from pulse dust collector 10, and the effect so entirely prepared is outstanding, together
Shi Wuxu worker is manually operated, and avoids external germ contamination.
Pacify on the snorkel, powder delivering pipe 6, vortex finder 8 and pulse dust collector exhaust pipe 11
Equipped with valve 13.
The angle of inclination of the delivery pipe of the screw conveyor is 25 ° -30 °.
The lower end outlet of the feed back pipe 5 is socketed with horn-like dust cover.
The feed back pipe 5 is made of stainless steel.
The operation principle of the utility model is：When actually crushing, cyclone separator 7 is isolated by screw conveyor
The coarse fodder come, which is re-fed into airslide disintegrating mill 3, to be ground, so that and material particles are more tiny, while in three-way pipe
Actual discharging is not influenced under setting, so after the grinding of certain number, coarse fodder gradually decreases, and corresponding finished product is from arteries and veins
It rushes deduster 10 to be separated, the effect so entirely prepared is outstanding, while is manually operated without worker, avoids outside
Germ contamination.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned exemplary embodiment, and
And in the case of the spirit or essential attributes without departing substantially from the utility model, it can realize that this practicality is new in other specific forms
Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this practicality is new
The scope of type is indicated by the appended claims rather than the foregoing description, it is intended that will fall containing in the equivalent requirements of the claims
All changes in justice and scope are embraced therein.Any reference numeral in claim should not be considered as limitation
Involved claim.
Claims (5)
1. a kind of ultra micro kudzuvine root starch preparation facilities, is removed including air compressor, air accumulator, airslide disintegrating mill, cyclone separator, pulse
Dirt device and ventilating mechanisms into；The source outlet of the air compressor connects the air inlet of air accumulator, air accumulator by snorkel
Compressed gas outlet the compressed gas source interface of airslide disintegrating mill is connect by snorkel；The airslide disintegrating mill is equipped with charging
Bucket；The discharge port of the airslide disintegrating mill is connected to powder delivering pipe；The powder delivering pipe is connected on the air inlet of cyclone separator
On；The top gas outlet of the cyclone separator is connected to vortex finder, and the bottom of cyclone separator is arranged equipped with coarse fodder
Outlet pipe；The another of the vortex finder is terminated on the air inlet of pulse dust collector；The pulse dust collector is also logical
Extra pulse deduster exhaust pipe is connected to ventilation blower；It is characterized in that, the coarse fodder discharge pipe of the cyclone separator is inclined to set,
And the end of coarse fodder discharge pipe is connected to three-way pipe, the other both ends of wherein three-way pipe are connected on the feed inlet of screw conveyor respectively
And on the feed inlet of production tube, the delivery pipe of the screw conveyor is inclined to be set up, and the conveying of screw conveyor
The end on of pipe is connected with feed back pipe, wherein position directly above of the outlet of the feed back pipe positioned at lower hopper.
2. ultra micro kudzuvine root starch preparation facilities according to claim 1, which is characterized in that the snorkel, powder delivering pipe, rotation
Valve is mounted on wind separator exhaust pipe and pulse dust collector exhaust pipe.
3. ultra micro kudzuvine root starch preparation facilities according to claim 1, which is characterized in that the delivery pipe of the screw conveyor
Angle of inclination is 25 ° -30 °.
4. ultra micro kudzuvine root starch preparation facilities according to claim 1, which is characterized in that the lower end outlet socket of the feed back pipe
There is horn-like dust cover.
5. ultra micro kudzuvine root starch preparation facilities according to claim 1, which is characterized in that the feed back pipe uses stainless steel
It is made.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720850007.1U CN207446436U (en) | 2017-07-13 | 2017-07-13 | A kind of ultra micro kudzuvine root starch preparation facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720850007.1U CN207446436U (en) | 2017-07-13 | 2017-07-13 | A kind of ultra micro kudzuvine root starch preparation facilities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207446436U true CN207446436U (en) | 2018-06-05 |
Family
ID=62247643
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720850007.1U Expired - Fee Related CN207446436U (en) | 2017-07-13 | 2017-07-13 | A kind of ultra micro kudzuvine root starch preparation facilities |
Country Status (1)
| Country | Link |
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| CN (1) | CN207446436U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109201217A (en) * | 2018-10-11 | 2019-01-15 | 宜兴市海科耐火材料制品有限公司 | One kind can be with quantity-produced zirconium ball powder homogenizing device |
| CN111318356A (en) * | 2020-04-09 | 2020-06-23 | 文山市华信三七科技有限公司 | Panax notoginseng medicinal material crushing system and use method thereof |
| CN111388516A (en) * | 2020-04-09 | 2020-07-10 | 文山市华信三七科技有限公司 | Cooked pseudo-ginseng powder production process and equipment |
| CN111729739A (en) * | 2020-04-09 | 2020-10-02 | 文山市华信三七科技有限公司 | Superfine pseudo-ginseng powder production process based on automatic feeding grinder |
| CN114247688A (en) * | 2021-12-23 | 2022-03-29 | 宣城鸿升钙业有限公司 | Superfine calcium carbonate production device and production process thereof |
-
2017
- 2017-07-13 CN CN201720850007.1U patent/CN207446436U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109201217A (en) * | 2018-10-11 | 2019-01-15 | 宜兴市海科耐火材料制品有限公司 | One kind can be with quantity-produced zirconium ball powder homogenizing device |
| CN111318356A (en) * | 2020-04-09 | 2020-06-23 | 文山市华信三七科技有限公司 | Panax notoginseng medicinal material crushing system and use method thereof |
| CN111388516A (en) * | 2020-04-09 | 2020-07-10 | 文山市华信三七科技有限公司 | Cooked pseudo-ginseng powder production process and equipment |
| CN111729739A (en) * | 2020-04-09 | 2020-10-02 | 文山市华信三七科技有限公司 | Superfine pseudo-ginseng powder production process based on automatic feeding grinder |
| CN114247688A (en) * | 2021-12-23 | 2022-03-29 | 宣城鸿升钙业有限公司 | Superfine calcium carbonate production device and production process thereof |
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| Date | Code | Title | Description |
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| 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: 20180605 Termination date: 20210713 |