CN105057062A - Airflow crushing device of fluidized bed - Google Patents
Airflow crushing device of fluidized bed Download PDFInfo
- Publication number
- CN105057062A CN105057062A CN201510425107.5A CN201510425107A CN105057062A CN 105057062 A CN105057062 A CN 105057062A CN 201510425107 A CN201510425107 A CN 201510425107A CN 105057062 A CN105057062 A CN 105057062A
- Authority
- CN
- China
- Prior art keywords
- fluidized bed
- crushing device
- high pressure
- air flow
- cavity
- 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.)
- Pending
Links
Abstract
The invention discloses an airflow crushing device of a fluidized bed. The device comprises a supporting base and a body. A grading cavity, a crushing cavity, a raw material feed inlet, a raw material discharging port, a compressed air annular pipe and high-pressure nozzles are arranged on the body. The compressed air annular pipe surrounds the body of the airflow crushing device of the fluidized bed and is connected with the high-pressure nozzles of the airflow crushing device of the fluidized bed through a guide pipe. The airflow crushing device has the advantages of being short in crushing time, simple in structure, low in noise and free of vibration, and is low in energy consumption. Compared with airflow grinding of other types, energy can be saved by one third.
Description
Technical field
The present invention relates to material-pulverizing device, particularly relate to a kind of fluidized bed air flow crushing device.
Background technology
Fluid bed airflow milling realizes the fine equipment of dry type material fining with high velocity air, is widely used in mineral products, chemical industry, electronics, the fields such as agricultural chemicals.
When external high pressure air, by high pressure nozzle to pulverizing chamber jet-stream wind, material reaches pulverizing after being subject to air-flow repeated stock head-on collision, pulverizes fine particle material along with ascending air and enters grading room, and fine particle enters cyclone separator along with air-flow, trap is collected, complete crushing process, corase particles returns pulverizing chamber and continues impact comminution, and the particle that traditional fluidized bed plant obtains exists uneven, and complex structure, inconvenient operation.
Summary of the invention
The technical problem that the present invention mainly solves is to provide a kind of fluidized bed air flow crushing device, can crush efficiency high, can pulverize continuously, and keep pulverizing goods purity.
For solving the problems of the technologies described above, described fluidized bed air flow crushing device comprises supports base and body, body is provided with graded chamber, pulverizes cavity, raw materials mouth, raw material discharging opening, compressed air goes in ring pipe, high pressure nozzle, and described compressed air goes in ring the body of circumference of cannon bone around fluidized bed air flow crushing device, by the high pressure nozzle of tubes connection fluidized bed air flow crusher
A kind of optimal technical scheme, described high pressure nozzle quantity is 4 to 9 nozzles, and nozzle is positioned at pulverizes cavity, operation, and high pressure nozzle is to pulverizing cavity inject high pressure supersonic airstream.
Described raw materials mouth is positioned at pulverizes cavity upper end, and material enters pulverizing cavity by raw materials mouth, and high pressure supersonic airstream sprays intersection repeated stock, and crushing material, pulverized material enters graded chamber along with ascending air,
Graded chamber upper end outer wall is provided with classification drive motors, and grading wheel, grading wheel is High Rotation Speed under drive motors drives, produce centrifugal force, at this time material particle had both been subject to the centrifugal force that grading rotor produces, and was subject to again the centripetal force that air-flow viscous effect produces, when particle be subject to centrifugal force be less than centripetal force when, corase particles returns pulverizing chamber and continues impact comminution, and finished particle can be discharged from raw material discharging opening along with air-flow, enters the devices such as separator.
In order to control compressed-air actuated temperature, air heater can be connected at the compressed air pipe that goes in ring, controlling the temperature of high pressure compressed gas.
A kind of optimal technical scheme, for the ease of detecting the problem of high pressure compressed gas, is provided with temperature-detecting device on compressed air goes in ring pipeline.
The invention has the beneficial effects as follows: it is short that the present invention has grinding time, structure is simple, and operation maintenance is convenient, and floor space is little, low noise and vibrationless advantage, and energy consumption is low, compared with the Gas grinding of other type, and energy energy-conservation 1/3rd.
Accompanying drawing explanation
Fig. 1 is a kind of airflow crushing system of fluidized bed structural representation of the present invention;
In accompanying drawing, the mark of each parts is as follows:
1 is graded chamber, and 2 for pulverizing cavity, and 3 is raw materials mouth, and 4 manage for compressed air goes in ring, and 5 is material outlet, and 6 is high pressure nozzle, and 7 for supporting base, and 8 is classification drive motors, and 9 is grading wheel.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present invention is described in detail, can be easier to make advantages and features of the invention be readily appreciated by one skilled in the art, thus more explicit defining is made to protection scope of the present invention.
Refer to Fig. 1, the embodiment of the present invention comprises:
Fluidized bed air flow crushing device comprises supports base and body, body is provided with graded chamber, pulverizes cavity, raw materials mouth, raw material discharging opening, compressed air goes in ring and manages, high pressure nozzle, described compressed air goes in ring the body of circumference of cannon bone around fluidized bed air flow crushing device, by the high pressure nozzle of tubes connection fluidized bed air flow crusher, described high pressure nozzle quantity is 4 nozzles, and nozzle is positioned at pulverizes cavity, operation, high pressure nozzle is to pulverizing cavity inject high pressure supersonic airstream.
Described raw materials mouth is positioned at pulverizes cavity upper end, and material enters pulverizing cavity by raw materials mouth, and high pressure supersonic airstream sprays intersection repeated stock, and crushing material, pulverized material enters graded chamber along with ascending air.
Graded chamber upper end outer wall is provided with classification drive motors, and grading wheel, grading wheel is High Rotation Speed under drive motors drives, produce centrifugal force, at this time material particle had both been subject to the centrifugal force that grading rotor produces, and was subject to again the centripetal force that air-flow viscous effect produces, when particle be subject to centrifugal force be less than centripetal force when, corase particles returns pulverizing chamber and continues impact comminution, and finished particle can be discharged from raw material discharging opening along with air-flow, enters the devices such as separator.
In order to control compressed-air actuated temperature, air heater can be connected at the compressed air pipe that goes in ring, controlling the temperature of high pressure compressed gas.
The foregoing is only embodiments of the invention; not thereby the scope of the claims of the present invention is limited; every utilize description of the present invention and accompanying drawing content to do equivalent structure or equivalent flow process conversion; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present invention.
Claims (3)
1. a fluidized bed air flow crushing device, it is characterized in that, comprise: support base and body, body is provided with graded chamber, pulverize cavity, raw materials mouth, raw material discharging opening, compressed air goes in ring and manages, high pressure nozzle, described compressed air goes in ring the body of circumference of cannon bone around fluidized bed air flow crushing device, by the high pressure nozzle of tubes connection fluidized bed air flow crusher, nozzle is positioned at pulverizes cavity, described raw materials mouth is positioned at pulverizes cavity upper end, material enters pulverizing cavity by raw materials mouth, graded chamber upper end outer wall is provided with classification drive motors, and grading wheel, grading wheel is High Rotation Speed under drive motors drives, produce centrifugal force, in order to control compressed-air actuated temperature, compressed air go in ring pipe connect air heater, control the temperature of high pressure compressed gas.
2. fluidized bed air flow crushing device according to claim 1, described high pressure nozzle quantity is 4 to 9.
3. fluidized bed air flow crushing device according to claim 1, for the ease of detecting the problem of high pressure compressed gas, is provided with temperature-detecting device on compressed air goes in ring pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510425107.5A CN105057062A (en) | 2015-07-20 | 2015-07-20 | Airflow crushing device of fluidized bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510425107.5A CN105057062A (en) | 2015-07-20 | 2015-07-20 | Airflow crushing device of fluidized bed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105057062A true CN105057062A (en) | 2015-11-18 |
Family
ID=54486700
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510425107.5A Pending CN105057062A (en) | 2015-07-20 | 2015-07-20 | Airflow crushing device of fluidized bed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105057062A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107282251A (en) * | 2017-08-23 | 2017-10-24 | 太仓市璜泾新海农机专业合作社 | One kind automation thermal current fuel pulverizing plant |
| CN107837923A (en) * | 2017-10-24 | 2018-03-27 | 廊坊新龙立机械制造有限公司 | A kind of fluidized bed air flow crusher and airflow pulverization method |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2297247Y (en) * | 1997-06-25 | 1998-11-18 | 上海化工机械三厂 | fluidized bed airflow pulverizer |
| CN201333422Y (en) * | 2008-12-02 | 2009-10-28 | 北京航空航天大学 | Air-flow crushing and surface modification integrated device for preparing ultra-fine grains |
| CN201475991U (en) * | 2009-09-03 | 2010-05-19 | 王昌祺 | Superfine pulverizing apparatus of large fluidized bed |
| JP4732794B2 (en) * | 2005-05-13 | 2011-07-27 | 株式会社リコー | Grinding device and grinding method |
| CN202621258U (en) * | 2012-04-09 | 2012-12-26 | 无锡豪普钛业有限公司 | Titanium dioxide crushing device adopting low-pressure saturated steam |
| CN203355834U (en) * | 2013-07-30 | 2013-12-25 | 山东申达作物科技有限公司 | Fluidized bed jet mill for biological pesticide production |
| CN203990835U (en) * | 2014-08-25 | 2014-12-10 | 邢台九明科技有限公司 | Fluid bed micro jet |
-
2015
- 2015-07-20 CN CN201510425107.5A patent/CN105057062A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2297247Y (en) * | 1997-06-25 | 1998-11-18 | 上海化工机械三厂 | fluidized bed airflow pulverizer |
| JP4732794B2 (en) * | 2005-05-13 | 2011-07-27 | 株式会社リコー | Grinding device and grinding method |
| CN201333422Y (en) * | 2008-12-02 | 2009-10-28 | 北京航空航天大学 | Air-flow crushing and surface modification integrated device for preparing ultra-fine grains |
| CN201475991U (en) * | 2009-09-03 | 2010-05-19 | 王昌祺 | Superfine pulverizing apparatus of large fluidized bed |
| CN202621258U (en) * | 2012-04-09 | 2012-12-26 | 无锡豪普钛业有限公司 | Titanium dioxide crushing device adopting low-pressure saturated steam |
| CN203355834U (en) * | 2013-07-30 | 2013-12-25 | 山东申达作物科技有限公司 | Fluidized bed jet mill for biological pesticide production |
| CN203990835U (en) * | 2014-08-25 | 2014-12-10 | 邢台九明科技有限公司 | Fluid bed micro jet |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107282251A (en) * | 2017-08-23 | 2017-10-24 | 太仓市璜泾新海农机专业合作社 | One kind automation thermal current fuel pulverizing plant |
| CN107837923A (en) * | 2017-10-24 | 2018-03-27 | 廊坊新龙立机械制造有限公司 | A kind of fluidized bed air flow crusher and airflow pulverization method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205109808U (en) | Little reducing mechanism of traditional chinese medicine | |
| CN106955774A (en) | A kind of use gas shock mode carries out the micronizer of sub-material | |
| CN102698848A (en) | Fluidized bed airflow grinding system | |
| CN203494602U (en) | Large-sized multi-rotor ultrafine air jet pulverization and classification all-in-one machine | |
| CN207102821U (en) | A kind of air flow crushing device for preparing titanium dioxide | |
| CN102671747A (en) | Supersonic jet milling system | |
| CN105057062A (en) | Airflow crushing device of fluidized bed | |
| CN202207621U (en) | Jet mill used for pesticide powder | |
| CN206152933U (en) | Fluidized bed jet mill | |
| CN102441474B (en) | Cyclonic jet mill | |
| CN205199666U (en) | Cryrogenic formula is ground jet stream | |
| CN204034826U (en) | Air flow crushing device | |
| CN106944231A (en) | A kind of medicinal material pulverizer of high-efficiency precision refinement | |
| CN105107594A (en) | Fluidized-bed airflow pulverizing system | |
| CN208642900U (en) | A kind of airslide disintegrating mill that noise control effect is good | |
| CN207371671U (en) | A kind of board-like supersonic jet mill of normal impact | |
| CN207478753U (en) | A kind of fluidized bed air flow crusher of controllable grain fineness | |
| CN217164768U (en) | Rotary collision type air flow crusher | |
| CN203281398U (en) | Feeding device for titanium dioxide steam flow pulverizer | |
| CN205095915U (en) | Jet pulverizing device | |
| CN201728145U (en) | Vertical grinder high-fineness dynamic-static combined separator device | |
| CN104971813B (en) | A kind of magnesium hydroxide grinds grading plant | |
| CN105084705A (en) | Sludge treating apparatus | |
| CN204396118U (en) | The disc type airslide disintegrating mill of built-in classifying turbine | |
| CN201692671U (en) | Spray-drying device of anhydrous calcium chloride |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20151118 |
|
| WD01 | Invention patent application deemed withdrawn after publication |