CN201061764Y - Rotating nozzle type airflow crashing device - Google Patents
Rotating nozzle type airflow crashing device Download PDFInfo
- Publication number
- CN201061764Y CN201061764Y CNU2007200254501U CN200720025450U CN201061764Y CN 201061764 Y CN201061764 Y CN 201061764Y CN U2007200254501 U CNU2007200254501 U CN U2007200254501U CN 200720025450 U CN200720025450 U CN 200720025450U CN 201061764 Y CN201061764 Y CN 201061764Y
- Authority
- CN
- China
- Prior art keywords
- crushing chamber
- fixed cylinder
- chamber
- crushing
- airflow
- 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
- 230000005540 biological transmission Effects 0.000 claims abstract description 4
- 238000010298 pulverizing process Methods 0.000 claims description 32
- 238000007789 sealing Methods 0.000 claims description 5
- 238000003801 milling Methods 0.000 claims 2
- 238000010902 jet-milling Methods 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 239000000843 powder Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003082 abrasive agent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000009856 non-ferrous metallurgy Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Disintegrating Or Milling (AREA)
Abstract
本实用新型涉及一种旋转喷嘴式气流粉碎装置，包括粉碎室、喷嘴和固定筒，粉碎室侧壁通过轴承设于固定筒内，粉碎室底部与穿过固定筒底部的旋转传动轴连接，粉碎室的筒体圆周方向均匀分布有至少一对喷嘴，粉碎室上部与气流分级装置连接件相连接，固定筒上设有进气口。本实用新型在筒形粉碎室靠近底部的侧壁上，沿圆周方向均匀分布至少一对喷嘴，通过动力装置和传动轴带动粉碎室与喷嘴一起旋转，使得粉碎装置工作时形成旋转的高速气流，从而减少粉碎室内的流场死区，增加物料的碰撞几率，提高粉碎效率，降低能耗。
The utility model relates to a rotating nozzle type airflow crushing device, which comprises a crushing chamber, a nozzle and a fixed cylinder. There are at least one pair of nozzles evenly distributed in the circumferential direction of the cylinder body of the chamber, the upper part of the crushing chamber is connected with the connecting piece of the air classification device, and an air inlet is provided on the fixed cylinder. In the utility model, at least a pair of nozzles are evenly distributed along the circumferential direction on the side wall of the cylindrical crushing chamber near the bottom, and the power device and the transmission shaft drive the crushing chamber and the nozzles to rotate together, so that the rotating high-speed airflow is formed when the crushing device is working. Thereby reducing the flow field dead zone in the crushing chamber, increasing the collision probability of materials, improving crushing efficiency and reducing energy consumption.
Description
Technical field
The utility model relates to a kind of reducing mechanism, specifically a kind of rotating nozzle type air flow crushing device that is applicable to various graininess powder products such as processing carborundum, aluminium oxide.
Background technology
We know that powder products such as carborundum, aluminium oxide have a wide range of applications in various fields such as abrasive material, grinding tool, cutter, iron and steel industry, nonferrous metallurgy, silicate, chemicals.At present, the process equipment of powder product is based on the fluidized bed type airslide disintegrating mill both at home and abroad, and this machine is made up of reducing mechanism, grading plant two large divisions.The operation principle of reducing mechanism is, by nozzle 0.6～0.8MPa compressed air is converted into high velocity air, quickens particle and also makes it to produce mutual collision, thereby reach the purpose that reduces grain graininess.Traditional fluidized bed type airslide disintegrating mill reducing mechanism adopts fixed nozzle formula structure, nozzle and pulverizing chamber are transfixion, pulverize in the process at particle, easily form the part dead band, pile up material, not only reduce crush efficiency, increased energy consumption, and increased the probability that undesirable product is sneaked into finished product.
Summary of the invention
The utility model is for overcoming above-mentioned the deficiencies in the prior art, and providing a kind of can significantly increase effective crushed work zone, reduces the dead band of pulverizing chamber inside, improves the collision probability of particle, improves crush efficiency, the rotating nozzle type air flow crushing device that cuts down the consumption of energy.
The purpose of this utility model is to adopt following technical proposals to realize:
A kind of rotating nozzle type air flow crushing device, comprise pulverizing chamber, nozzle and stationary magazine creel, the pulverizing chamber sidewall is located in the stationary magazine creel by bearing, the pulverizing chamber bottom is connected with the rotating drive shaft that passes the stationary magazine creel bottom, the cylindrical shell circumferencial direction of pulverizing chamber is evenly distributed with at least one pair of nozzle, pulverizing chamber top is connected with the airflow classification device connector, and stationary magazine creel is provided with air inlet.
Bearing between pulverizing chamber outer wall and stationary magazine creel inwall is respectively equipped with sealing device up and down.
Described pulverizing chamber is connected with the grading plant connector by rubber liner.
Between pulverizing chamber bottom and the stationary magazine creel bottom compressed air cell is arranged.
On the airflow classification device connector, be provided with feeding mouth.
Rotating drive shaft is located on the stationary magazine creel by supporting mechanism.
The utility model is on the close sidewall of bottom of tubular pulverizing chamber, along the circumferential direction be evenly distributed with at least one pair of nozzle, driving pulverizing chamber by power set and power transmission shaft rotates with nozzle, form the high velocity air of rotation when making reducing mechanism work, thereby the dead band, flow field in the minimizing pulverizing chamber, increase the collision probability of material, improve crush efficiency, cut down the consumption of energy.
Description of drawings
Fig. 1 is the utility model structural representation.
1, airflow classification device connector, 2, feeding mouth, 3, rubber liner, 4, screw, 5, sealing device, 6, bearing, 7, pulverizing chamber, 8, nozzle, 9, compressed air cell, 10, supporting device, 11, rotating drive shaft, 12, air inlet, 13. stationary magazine creels.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further specified.
Among Fig. 1, pulverizing chamber 7 sidewalls are located in the stationary magazine creel 13 by bearing 6, pulverizing chamber 7 bottoms are connected with the rotating drive shaft 11 that passes stationary magazine creel 13 bottoms, the cylindrical shell circumferencial direction of pulverizing chamber 7 is evenly distributed with at least one pair of nozzle 8, pulverizing chamber 7 tops are connected with airflow classification device connector 1 with screw 4 by rubber liner 3, and stationary magazine creel 13 is provided with compressed air inlet port 12.Bearing 6 between pulverizing chamber 7 outer walls and stationary magazine creel 13 inwalls is respectively equipped with sealing device 5 up and down.Between pulverizing chamber 7 bottoms and stationary magazine creel 13 bottoms compressed air cell 9 is arranged.On airflow classification device connector 1, be provided with feeding mouth 2.Rotating drive shaft 11 is located on the stationary magazine creel 13 by supporting mechanism 10.
During work, the clean compressed air of 0.6～0.8MPa enters into compressed air cell 9 by air inlet 12, by being installed in rotation many to along the equally distributed nozzle 8 of cylindrical shell circumferencial direction on the pulverizing chamber 7, compressed air is converted into high velocity air.Granular material utilizes self gravitation to drop in the rotation pulverizing chamber 7 by feeding mouth 2, near nozzle 8 positions, quickens and produces collision mutually by high velocity air, thereby reach the purpose of particle pulverizing.The particle that has reached granularity requirements sieves by the airflow classification device that links with airflow classification device connector 1, shifts out the working region, and the relative ground of grading plant is inactive state.Power set drive pulverizing chamber 7 and nozzle 8 rotations by rotating drive shaft 11, form the high velocity air of rotation, can effectively reduce the dead band in the pulverizing chamber.5 pairs of compressed air cells 9 of labyrinth-type excluder seal, and do not produce loss with the pressure that guarantees the chamber compressed air, and guarantee that particle can not leak into bearing 6 places.Because there is the pressure about 0.2MPa in pulverizing chamber 7 inside, pulverizing chamber 7 and grading plant are partly located and can be formed sealing by the pressure differential between inside and outside.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200254501U CN201061764Y (en) | 2007-07-26 | 2007-07-26 | Rotating nozzle type airflow crashing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200254501U CN201061764Y (en) | 2007-07-26 | 2007-07-26 | Rotating nozzle type airflow crashing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201061764Y true CN201061764Y (en) | 2008-05-21 |
Family
ID=39450133
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200254501U Expired - Fee Related CN201061764Y (en) | 2007-07-26 | 2007-07-26 | Rotating nozzle type airflow crashing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201061764Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102441474A (en) * | 2011-12-28 | 2012-05-09 | 潍坊正远粉体工程设备有限公司 | Cyclonic jet mill |
| CN114408954A (en) * | 2022-01-26 | 2022-04-29 | 株洲科能新材料股份有限公司 | Preparation method of single crystal alumina micro powder |
-
2007
- 2007-07-26 CN CNU2007200254501U patent/CN201061764Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102441474A (en) * | 2011-12-28 | 2012-05-09 | 潍坊正远粉体工程设备有限公司 | Cyclonic jet mill |
| CN114408954A (en) * | 2022-01-26 | 2022-04-29 | 株洲科能新材料股份有限公司 | Preparation method of single crystal alumina micro powder |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205833335U (en) | Automatization's pulverizer with precomminution mechanism | |
| CN204892075U (en) | High -efficient breaker of mine building stones | |
| CN103752388B (en) | Environment-friendly and energy-efficient eddy mill | |
| CN107497560A (en) | A kind of material pneumatic crushing grinding device | |
| CN205868473U (en) | Rubbing crusher with environmental protection | |
| CN104437784A (en) | Pulverizer | |
| CN104028355B (en) | A kind of tea pulverizer structure | |
| CN106391272A (en) | Ore material crushing device | |
| CN206823967U (en) | A kind of nano-calcium carbonate continuously crushes depolymerizer | |
| CN207694920U (en) | A kind of graphite crushing processing unit (plant) | |
| CN201061764Y (en) | Rotating nozzle type airflow crashing device | |
| CN205361601U (en) | Can improve vortices air flow balling machine that spherical graphite smashed efficiency | |
| CN204261734U (en) | A kind of micronizer with knot screen | |
| CN102441474A (en) | Cyclonic jet mill | |
| CN204261792U (en) | A kind of vertical superfine crusher without sieve | |
| CN114226029A (en) | Horizontal alumina powder ball mill | |
| CN205550459U (en) | Contrarotating rubbing crusher | |
| CN214864156U (en) | Novel double-rotor flour mill | |
| CN217164768U (en) | Rotary collision type air flow crusher | |
| CN205761425U (en) | There is the mechanical crusher of grading function | |
| CN105214784A (en) | A kind of flour mill | |
| CN211487938U (en) | Medical nutrition powder raw material grinding machine | |
| CN102189033A (en) | High-efficiency anti-oxidation combined grinding machine and grinding method thereof | |
| CN209829233U (en) | Aquatic feed ultrafine grinder | |
| CN201008801Y (en) | Airflow, mechanical combination ultrafine pulverizer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080521 |