CN203139955U - Large pyrophyllite micro-powder homogenization silo - Google Patents
Large pyrophyllite micro-powder homogenization silo Download PDFInfo
- Publication number
- CN203139955U CN203139955U CN201320017251.1U CN201320017251U CN203139955U CN 203139955 U CN203139955 U CN 203139955U CN 201320017251 U CN201320017251 U CN 201320017251U CN 203139955 U CN203139955 U CN 203139955U
- Authority
- CN
- China
- Prior art keywords
- storehouse
- powder
- silo
- storehouse body
- micro mist
- 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
Links
Images
Landscapes
- Nozzles (AREA)
Abstract
The utility model discloses a large pyrophyllite micro-powder homogenization silo which comprises one or multiple cylindrical silo bodies, wherein a discharging mechanism is arranged at the bottom of each silo body. The large pyrophyllite micro-powder homogenization silo is characterized in that a lifter is arranged outside the silo body; the top of the lifter is connected with a distribution mechanism on the top of each silo body; and an air blowing mechanism is arranged at the bottom of each silo body. By adoption of the large pyrophyllite micro-powder homogenization silo, because the powder is lifted to the top of the silo body by employing the lifter, and the powder distributed by the distribution mechanism is blown upwards through the air blowing system, so that the powder continuously rotates and flies in the silo body, and therefore, the powder is good in homogenization effect, a large-volume silo body can be adopted, and the component content uniformity in the discharged pyrophyllite micro-powder is guaranteed.
Description
Technical field
The utility model relates to a kind of process units of pyrophillite micro mist, relates to a kind of large-scale homogenizing storehouse of pyrophillite micro mist finished product being carried out homogenizing, storage specifically.
Background technology
The pyrophillite micro mist be a kind of be the composite raw material of base material with the pyrophillite.Be widely used in pottery, building materials, refractory material, chemical industry, industries such as light industry, electronics, the energy.In fields such as industrial, civilian, military affairs, wide use prospect is arranged, be mainly used in the manufacturing of pond cellar for storing things wire drawing with alkali-free glass fiber electronics cloth and other high-grade glass products.In pyrophillite micro mist production process, mainly comprise ore reduction, pre-homogenizing, carefully break, grind and step such as finished product homogenizing, particularly through behind the pyrophillite micro mist that is milled to, need enter a homogenizing storehouse and carry out final homogenizing, to reach the unanimity of composition ratio in the product.Existing homogenizing storehouse is generally a cylindric tank body, a feed pipe is set in the bottom of homogenizing storehouse, pyrophillite micro mist after mill is good is after entering homogenizing storehouse by this feed pipe under the effect of an air blast, under action of inertia, the pyrophillite micro mist can continue to fly upward to the homogenizing storehouse upper strata, thereby makes the pyrophillite micro mist in the homogenizing storehouse stir the effect that reaches homogenizing by this flying upward.But because flying upward of pyrophillite micro mist stirred just by himself inertia after under the effect of air blast, it is single, highly lower to make the pyrophillite micro mist fly upward track, cause homo-effect relatively poor, the height of homogenizing storehouse must be lower, volume can't be done greatly, and less because of the homogenizing storehouse volume, certainly will will adopt the homogenizing storehouse of greater number, the composition of the pyrophyllite micropowder in each homogenizing storehouse all can have different slightly, causes the composition disunity of the pyrophyllite micropowder that finally dispatches from the factory; And when more stock was arranged in the homogenizing storehouse, the pyrophillite micro mist can't fly upward at all.
The utility model content
For overcoming above-mentioned defective, the utility model aims to provide and a kind ofly can guarantee homo-effect, can improve the long-pending large-scale homogenizing storehouse of pyrophillite micro mist of storage capacity simultaneously again greatly.
For achieving the above object, the technical solution adopted in the utility model is: the large-scale homogenizing storehouse of a kind of pyrophillite micro mist, comprise one or more storehouses cylindraceous body, the bottom of described each storehouse body has a discharging mechanism, its innovative point is that described storehouse is external and also has an elevator, the top of described elevator is connected with the material-feeding mechanism that is arranged on each body top, storehouse, and the bottom of described each storehouse body is provided with a Blast mechanism.
Described material-feeding mechanism comprises a horizontal conveying worm that is connected with the elevator top, and the other end of described conveying worm is connected with a cloth funnel, and the below of described cloth funnel is provided with a downward-sloping rotation distributing trough.
Described Blast mechanism comprises a high pressure blower, and described high pressure blower is connected with the nozzle that a plurality of spouts make progress by pipeline, and described nozzle is that the center of circle is the multilayer circumference and evenly distributes with the center of storehouse body.
The height of described nozzle is from reducing gradually near the limit tube of mind-set the body of storehouse near the storehouse body.
Adopted the large-scale homogenizing storehouse of pyrophillite micro mist of the present utility model, carry out cloth again owing to adopt elevator that powder is risen to body top, storehouse, by blower system the powder that material-feeding mechanism plants is upwards blowed again, making powder do constantly rotation in the body of storehouse flies upward, not only make the homo-effect of powder better, and can adopt the storehouse body of bigger volume, the homogeneity of component content in the pyrophillite micro mist that guaranteed to dispatch from the factory.
Description of drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is Blast mechanism plan structure schematic diagram of the present utility model.
Among the figure: 1-storehouse body, the 2-elevator, the 3-material-feeding mechanism, the 4-Blast mechanism, the 5-discharging mechanism, the 6-conveying worm, 7-cloth funnel, 8-rotates distributing trough, 9-high pressure blower, 10-nozzle.
The specific embodiment
As shown in Figure 1, the utility model discloses the large-scale homogenizing storehouse of a kind of pyrophillite micro mist, comprise one or more storehouses cylindraceous body 1, when adopting a plurality of storehouses body 1, the bottom of each storehouse body 1 has a discharging mechanism 5, and is low in the middle of usually the bottom of storehouse body 1 being arranged to, the funnel-form that periphery is high, described discharging mechanism 5 is connected the minimum point of storehouse body 1 bottom, and described discharging mechanism 5 generally includes one or more screw conveyer, by screw conveyer the powder in the storehouse body 1 is transported to outside the storehouse;
Innovative point of the present utility model mainly is also have an elevator 2 outside the described storehouse body 1, and the top of described elevator 2 is connected with the material-feeding mechanism 3 that is arranged on each storehouse body 1 top, and the bottom of described each storehouse body 1 is provided with a Blast mechanism 4.If only adopt a storehouse body 1, then elevator 2 is arranged on the limit of storehouse body 1, if adopt a plurality of storehouses body 1, then elevator 2 is arranged on the center that a plurality of storehouses body 1 surrounds, and namely elevator 2 is roughly the same with the distance of each storehouse body 1.
Powder after levigate rises to the top of storehouse body 1 by elevator 2, by material-feeding mechanism 3 powder is fallen downwards in storehouse body 1 from top to bottom again, meanwhile, Blast mechanism 4 upwards carries out air blast, the powder that falls is upwards blown afloat, make the powder in the whole storehouse body 1 fly upward rotation up and down, the powder after stirring obtains homogenizing.
In the specific implementation, common described material-feeding mechanism 3 comprises a horizontal conveying worm 6 that is connected with elevator 2 tops, the other end of described conveying worm 6 is connected with a cloth funnel 7, the below of described cloth funnel 7 is provided with a downward-sloping rotation distributing trough 8, and described rotation distributing trough 8 can be done the rotation of 360 degree by manual or driven by motor.Elevator 2 can adopt the helical feed formula, powder is after elevator 2 rises to elevator 2 tops, again in conveying worm 6 is delivered to cloth funnel 7, the opening of powder by cloth funnel 7 bottoms falls into rotation distributing trough 8 and falls to storehouse body 1 bottom, continuous rotation by rotation distributing trough 8, powder can not fallen to storehouse body 1 bottom with upper/lower positions, make that the homo-effect of homogenizing storehouse is better.
As shown in Figure 2, in the specific implementation, common described Blast mechanism 4 comprises a high pressure blower 9, and described high pressure blower 9 is connected by the nozzle 10 that pipeline and a plurality of spouts make progress, and described nozzle 10 is that the center of circle is the multilayer circumference and evenly distributes with the center of storehouse body 1.Like this, the some circles of a plurality of nozzles 10 formation are the nozzle group in the center of circle with the center of storehouse body 1, and the distance between adjacent two nozzles 10 is roughly the same.The height of nozzle 10 is from reducing gradually near the limit tube of mind-set the storehouse body 1 near storehouse body 1, that is to say the height maximum of a circle nozzle 10 at close center, farthest excentric one the circle nozzle 10 the height minimum, as shown in Figure 1, described nozzle 10 is high in the middle of forming one, the taper battle array that periphery is low.Because the wind energy that the nozzle 10 of higher position blows out is dashed more near the top of storehouse body 1, namely the wind height of every circle nozzle 10 ejections differs, and seethes thereby make body 1 interior powder in storehouse the peritropous swirl shape in center occur, makes that the homogenizing of powder is more abundant.
Claims (4)
1. large-scale homogenizing storehouse of pyrophillite micro mist, comprise one or more storehouse cylindraceous bodies (1), the bottom of described each storehouse body (1) has a discharging mechanism (5), it is characterized in that also having an elevator (2) outside the described storehouse body (1), the top of described elevator (2) is connected with the material-feeding mechanism (3) that is arranged on each storehouse body (1) top, and the bottom of described each storehouse body (1) is provided with a Blast mechanism (4).
2. the large-scale homogenizing storehouse of pyrophillite micro mist according to claim 1, it is characterized in that described material-feeding mechanism (3) comprises a horizontal conveying worm (6) that is connected with elevator (2) top, the other end of described conveying worm (6) is connected with a cloth funnel (7), and the below of described cloth funnel (7) is provided with a downward-sloping rotation distributing trough (8).
3. the large-scale homogenizing storehouse of pyrophillite micro mist according to claim 1, it is characterized in that described Blast mechanism (4) comprises a high pressure blower (9), described high pressure blower (9) is connected by the nozzle (10) that pipeline and a plurality of spouts make progress, and described nozzle (10) is that the center of circle is the multilayer circumference and evenly distributes with the center of storehouse body (1).
4. the large-scale homogenizing storehouse of pyrophillite micro mist according to claim 3 is characterized in that the height of described nozzle (10) is from reducing gradually near the limit tube of mind-set the storehouse body (1) near storehouse body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320017251.1U CN203139955U (en) | 2013-01-14 | 2013-01-14 | Large pyrophyllite micro-powder homogenization silo |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320017251.1U CN203139955U (en) | 2013-01-14 | 2013-01-14 | Large pyrophyllite micro-powder homogenization silo |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203139955U true CN203139955U (en) | 2013-08-21 |
Family
ID=48967512
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320017251.1U Expired - Fee Related CN203139955U (en) | 2013-01-14 | 2013-01-14 | Large pyrophyllite micro-powder homogenization silo |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203139955U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103055745A (en) * | 2013-01-14 | 2013-04-24 | 浙江磊纳微粉材料有限公司 | Large pyrophyllite micro powder homogenization silo |
| CN107790049A (en) * | 2017-11-28 | 2018-03-13 | 佛山科学技术学院 | A kind of industrial chemicals powder blender |
-
2013
- 2013-01-14 CN CN201320017251.1U patent/CN203139955U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103055745A (en) * | 2013-01-14 | 2013-04-24 | 浙江磊纳微粉材料有限公司 | Large pyrophyllite micro powder homogenization silo |
| CN107790049A (en) * | 2017-11-28 | 2018-03-13 | 佛山科学技术学院 | A kind of industrial chemicals powder blender |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104493967B (en) | System for preparing ceramsite through sludge | |
| CN206262384U (en) | A kind of discontinuity medicinal powder sprays mixing arrangement | |
| CN203139955U (en) | Large pyrophyllite micro-powder homogenization silo | |
| CN103055745A (en) | Large pyrophyllite micro powder homogenization silo | |
| CN106904446A (en) | A kind of powder feeder | |
| CN102342469B (en) | Proportioning apparatus for flavorings | |
| CN103406041B (en) | There is the blender of flat hydraulic barrier | |
| CN103406040B (en) | There is the blender of folded plate type hydraulic barrier | |
| CN203653446U (en) | Kiln ash kiln-entering system | |
| CN103086625A (en) | Preparation and production equipment for unclassified tailing filling material and preparation process | |
| CN203437094U (en) | Novel mixing device | |
| CN110156301B (en) | Continuous melting device and method for quartz tube production | |
| CN1673149A (en) | Active lime producing process | |
| CN203862448U (en) | Automatic glue spraying powder scattering machine | |
| CN202289983U (en) | Barrel body of disk granulating machine | |
| CN111730741A (en) | Ceramic raw material preparation system | |
| CN203959328U (en) | Wind-force feed mechanism for sheet material | |
| CN105836485B (en) | Circular coal yard unloader | |
| CN211521006U (en) | Storage bin emptying device of refractory material production line | |
| CN205634246U (en) | Circular coal yard unloader | |
| CN201671383U (en) | Air homogenization storage | |
| CN203790911U (en) | Coating grain granulating machine | |
| CN216996656U (en) | Snake-shaped conveying device for ultrafine powder | |
| CN114505011B (en) | Catalyst forming device and application thereof | |
| CN102527271A (en) | Homogenizing device of solid materials |
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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130821 Termination date: 20180114 |