CN204685256U - A kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine - Google Patents
A kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine Download PDFInfo
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- CN204685256U CN204685256U CN201520343099.5U CN201520343099U CN204685256U CN 204685256 U CN204685256 U CN 204685256U CN 201520343099 U CN201520343099 U CN 201520343099U CN 204685256 U CN204685256 U CN 204685256U
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Abstract
The utility model relates to a kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine, comprise coarse crushing main frame, the broken main frame of fine powder, classification main frame, powder collector, air-introduced machine, powder conveying pipeline and automatic control device, wherein, the discharging opening of described classification main frame comprises meal discharging opening and fine powder discharging opening, described coarse crushing main frame, the broken main frame of fine powder are connected by powder conveying pipeline successively with classification main frame, the fine powder discharging opening of classification main frame is connected with described powder collector by powder conveying pipeline, and powder collector is connected with air-introduced machine by powder conveying pipeline; The meal port of export of described classification main frame is connected with the arrival end of the broken main frame of described fine powder, and the broken main frame of coarse crushing main frame, fine powder, classification main frame, powder collector are all connected with described automatic control device with air-introduced machine.By coarse crushing main frame, circulation crushing and classification between the broken main frame of fine powder and classification main frame, realize the ultramicro grinding of low cost.
Description
Technical field
The utility model is specifically related to a kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine.
Background technology
At present, the common equipment for the preparation of Chinese herbal ultra-fine powder mainly contains jet mill, abrading type disintegrator etc.Due to jet mill apparatus expensive, pulverize cost high, be suitable for famous and precious Chinese medicine; Abrading type disintegrator production capacity is low, be applicable to little miniature clinic, so the preparation work of Chinese herbal ultra-fine powder for efficient, low cost, above two kinds of equipment have certain limitation.
Utility model content
In order to overcome the deficiency of existing Study on Supermicro-pulverization of Traditional Chinese Drugs machine, the purpose of this utility model is to provide a kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine, and this device realizes the ultramicro grinding of low cost by the circulation crushing and classification between coarse crushing main frame, the broken main frame of fine powder, classification main frame.
To achieve these goals, the utility model adopts following technical scheme:
A kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine, comprise coarse crushing main frame, the broken main frame of fine powder, classification main frame, powder collector, air-introduced machine, powder conveying pipeline and automatic control device, wherein, the discharging opening of described classification main frame comprises meal discharging opening and fine powder discharging opening, described coarse crushing main frame, the broken main frame of fine powder are connected by powder conveying pipeline successively with classification main frame, the fine powder discharging opening of classification main frame is connected with described powder collector by powder conveying pipeline, and powder collector is connected with air-introduced machine by powder conveying pipeline; The meal port of export of described classification main frame is connected with the arrival end of the broken main frame of described fine powder, and the broken main frame of coarse crushing main frame, fine powder, classification main frame, powder collector are all connected with described automatic control device with air-introduced machine.
Preferably, the meal discharging opening of described classification main frame is connected with discharger.
Preferably, pay-off is connected with between the charging aperture of described discharger and the broken main frame of fine powder.
Preferred further, described pay-off is double helix material feeder.
Preferably, described powder collector is cyclone collector.
Preferably, the lower end of described cyclone collector is provided with the first discharge port.
Preferably, deduster is connected with between described cyclone collector and air-introduced machine.
Preferably, the lower end of described deduster is provided with the second discharge port.
Preferably, muffler is connected with between described air-introduced machine and deduster.
Preferably, the pipeline between described coarse crushing main frame and the broken main frame of fine powder is connected with self-suction air device.The undesirable coarse dispersion entered in the broken main frame of fine powder is sucked back in coarse crushing main frame again by self-suction air device.
Preferably, described self-suction air device comprises several self-suction air blades and the self-suction air impeller base for installing described self-suction air blade.
Advantageous Effects of the present utility model is:
1, by coarse crushing main frame, circulation crushing and classification between the broken main frame of fine powder and classification main frame, the ultramicro grinding of low cost is realized;
2, by self-priming fan blade assembly rotate produce negative pressure make coarse crushing main frame pulverize after material automatically suck the broken main frame of fine powder, material after the broken main frame pulverizing of fine powder automatically sucks classification main frame and carries out classification, the material not being graded out, reenters the broken main frame of fine powder by discharger and pulverizes.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of self-suction air device;
Fig. 3 is the sectional view along A-A in Fig. 2.
Wherein, 1, coarse crushing main frame, 2, the broken main frame of fine powder, 3, double helix material feeder, 4, classification main frame, 5, cyclone collector, 6, underframe, 7, deduster, 8, muffler, 9, air-introduced machine, 10, self-priming fan blade assembly, 11, discharger, 12, self-suction air blade, 13, self-suction air impeller base.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, a kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine, comprise coarse crushing main frame 1, the broken main frame 2 of fine powder, classification main frame 4, cyclone collector 5, air-introduced machine 9, powder conveying pipeline and automatic control device, wherein, the discharging opening of described classification main frame 4 comprises meal discharging opening and fine powder discharging opening, described coarse crushing main frame 1, the broken main frame 2 of fine powder is connected by powder conveying pipeline successively with classification main frame 4, the fine powder discharging opening of classification main frame 4 is connected with described cyclone collector 5 by powder conveying pipeline, cyclone collector 5 is connected with air-introduced machine 9 by powder conveying pipeline, the meal port of export of described classification main frame 4 is connected with the arrival end of the broken main frame 2 of described fine powder, and the broken main frame of coarse crushing main frame 1, fine powder 2, classification main frame 4, cyclone collector 5 are all connected with described automatic control device with air-introduced machine 9.The broken main frame 2 of coarse crushing main frame 1, fine powder and classification main frame 4 are installed on underframe 6.
The meal discharging opening of classification main frame 4 is connected with discharger 11.
Double helix material feeder 3 is connected with between the charging aperture of described discharger 11 and the broken main frame 2 of fine powder.
The lower end of described cyclone collector is provided with the first discharge port.Deduster 7 is connected with between described cyclone collector 5 and air-introduced machine 9.The lower end of deduster 7 is provided with the second discharge port.Muffler 8 is connected with between described air-introduced machine 9 and deduster 7.
Pipeline between described coarse crushing main frame 1 and the broken main frame 2 of fine powder is connected with self-suction air device.The undesirable coarse dispersion entered in the broken main frame of fine powder 2 is sucked back in coarse crushing main frame 1 again by self-suction air device.
Shown in Fig. 2 and Fig. 3, described self-suction air device comprises several self-suction air blades 12 and the self-suction air impeller base 13 for installing described self-suction air blade 12.
The course of work of the present utility model is as follows:
First material enters coarse crushing main frame 1 and carries out coarse crushing processing, and pivotal pulverizing device and material and impact mutually between material particles and particle, collide in coarse crushing main frame 1 chamber, realize the coarse crushing of material.Enter the broken main frame of fine powder 2 through powder conveying pipeline under the negative-pressure sucking that satisfactory meal produces through air-introduced machine 9 and carry out the broken processing of fine powder, undesirable large granular materials is greater than the negative-pressure sucking that air-introduced machine 9 produces because of gravity, fall into the bottom of powder conveying pipeline, the larger negative-pressure sucking inspiration next time produced at self-priming fan blade assembly 10 enters coarse crushing main frame 1 cavity continuation pulverizing.Impact mutually between the particle of the pivotal pulverizing device of high speed and meal and meal and particle in fine powder broken main frame 2 chamber, collide, friction, shear and extruding broken with the fine powder realizing material.Fine powder enters classification main frame 4 through air-introduced machine 9 and pipeline and carries out Ultramicro-powder classification, and the Ultramicro-powder meeting Particle size requirements enters cyclone collector 5, carries out material collection.The fine powder not reaching Particle size requirements enters fine powder broken main frame 2 cavity through discharger 11 and carries out Matter Transfer processing, then enters classification main frame 4 and carry out classification.Air-introduced machine 9 makes to produce negative pressure in pipeline, and the gas containing dust enters cyclone collector 5 and deduster 7 carries out collecting by filtration dust, makes to discharge clean air from air-introduced machine 9, and then protection of the environment.
By reference to the accompanying drawings detailed description of the invention of the present utility model is described although above-mentioned; but the restriction not to utility model protection scope; one of ordinary skill in the art should be understood that; on the basis of the technical solution of the utility model, those skilled in the art do not need to pay various amendment or distortion that creative work can make still in protection domain of the present utility model.
Claims (10)
1. a circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine, it is characterized in that: comprise coarse crushing main frame, the broken main frame of fine powder, classification main frame, powder collector, air-introduced machine, powder conveying pipeline and automatic control device, wherein, the discharging opening of described classification main frame comprises meal discharging opening and fine powder discharging opening, described coarse crushing main frame, the broken main frame of fine powder are connected by powder conveying pipeline successively with classification main frame, the fine powder discharging opening of classification main frame is connected with described powder collector by powder conveying pipeline, and powder collector is connected with air-introduced machine by powder conveying pipeline; The meal port of export of described classification main frame is connected with the arrival end of the broken main frame of described fine powder, and the broken main frame of coarse crushing main frame, fine powder, classification main frame, powder collector are all connected with described automatic control device with air-introduced machine.
2. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 1, is characterized in that: the meal discharging opening of described classification main frame is connected with discharger.
3. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 2, is characterized in that: be connected with pay-off between the charging aperture of described discharger and the broken main frame of fine powder.
4. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 3, is characterized in that: described pay-off is double helix material feeder.
5. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 1, is characterized in that: described powder collector is cyclone collector.
6. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 5, is characterized in that: the lower end of described cyclone collector is provided with the first discharge port.
7. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 6, is characterized in that: be connected with deduster between described cyclone collector and air-introduced machine, and the lower end of described deduster is provided with the second discharge port.
8. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 7, is characterized in that: be connected with muffler between described air-introduced machine and deduster.
9. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 1, is characterized in that: the pipeline between described coarse crushing main frame and the broken main frame of fine powder is connected with self-suction air device.
10. circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine according to claim 9, is characterized in that: described self-suction air device comprises several self-suction air blades and the self-suction air impeller base for installing described self-suction air blade.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520343099.5U CN204685256U (en) | 2015-05-25 | 2015-05-25 | A kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520343099.5U CN204685256U (en) | 2015-05-25 | 2015-05-25 | A kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine |
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| Publication Number | Publication Date |
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| CN204685256U true CN204685256U (en) | 2015-10-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520343099.5U Expired - Fee Related CN204685256U (en) | 2015-05-25 | 2015-05-25 | A kind of circulating Study on Supermicro-pulverization of Traditional Chinese Drugs machine |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289797A (en) * | 2015-11-06 | 2016-02-03 | 嘉兴市高正高分子材料有限公司 | Mill for carbon fiber material production |
| CN108176148A (en) * | 2018-01-23 | 2018-06-19 | 湘潭大学 | A kind of circulation type powder filter device and filter method based on Bernoulli effect |
| CN108311263A (en) * | 2018-04-18 | 2018-07-24 | 高维科 | A kind of closed micron ultra shifter |
| CN108421620A (en) * | 2017-02-14 | 2018-08-21 | 漳州科益工贸有限公司 | Broken milling all-in-one machine |
| CN110841764A (en) * | 2019-11-19 | 2020-02-28 | 成都普美怡科技有限公司 | Discharging device for nonmetal powder of waste circuit board and matched superfine powder preparation process thereof |
| CN112916173A (en) * | 2020-12-23 | 2021-06-08 | 浙江德创环保科技股份有限公司 | Novel catalyst crushing system and crushing process thereof |
-
2015
- 2015-05-25 CN CN201520343099.5U patent/CN204685256U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289797A (en) * | 2015-11-06 | 2016-02-03 | 嘉兴市高正高分子材料有限公司 | Mill for carbon fiber material production |
| CN108421620A (en) * | 2017-02-14 | 2018-08-21 | 漳州科益工贸有限公司 | Broken milling all-in-one machine |
| CN108176148A (en) * | 2018-01-23 | 2018-06-19 | 湘潭大学 | A kind of circulation type powder filter device and filter method based on Bernoulli effect |
| CN108311263A (en) * | 2018-04-18 | 2018-07-24 | 高维科 | A kind of closed micron ultra shifter |
| CN110841764A (en) * | 2019-11-19 | 2020-02-28 | 成都普美怡科技有限公司 | Discharging device for nonmetal powder of waste circuit board and matched superfine powder preparation process thereof |
| CN112916173A (en) * | 2020-12-23 | 2021-06-08 | 浙江德创环保科技股份有限公司 | Novel catalyst crushing system and crushing process thereof |
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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: 20151007 Termination date: 20160525 |