CN203108535U - Device for dispersing powder - Google Patents

Device for dispersing powder Download PDF

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Publication number
CN203108535U
CN203108535U CN201220734624.2U CN201220734624U CN203108535U CN 203108535 U CN203108535 U CN 203108535U CN 201220734624 U CN201220734624 U CN 201220734624U CN 203108535 U CN203108535 U CN 203108535U
Authority
CN
China
Prior art keywords
disperser
cavity
treatment device
dispersion treatment
grading wheel
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
Application number
CN201220734624.2U
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Chinese (zh)
Inventor
王文川
王樱丽
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANGHAI BESTRY PERFORMANCE MATERIALS CO Ltd
Original Assignee
SHANGHAI BESTRY PERFORMANCE MATERIALS CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SHANGHAI BESTRY PERFORMANCE MATERIALS CO Ltd filed Critical SHANGHAI BESTRY PERFORMANCE MATERIALS CO Ltd
Priority to CN201220734624.2U priority Critical patent/CN203108535U/en
Application granted granted Critical
Publication of CN203108535U publication Critical patent/CN203108535U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a device for dispersing powder and belongs to the field of chemical industry machinery. The device comprises a disperser cavity, air blasting components and a grading wheel, wherein the wall of the disperser cavity is provided with a charging port and the air blasting components, the air blasting components are arranged below the charging port, a discharging port is formed in the top of the disperser cavity, and the grading wheel is arranged inside the disperser cavity and is arranged between the charging port and the discharging port. The device for dispersing the powder has the advantages that the powder can be subjected to continuous dispersion processing, the processed powder shows very good fluidity, the dispersion effect is good, the work efficiency is high, the energy consumption is low, the structure is simple, and the operation is convenient.

Description

Powder dispersion treatment device
Technical field
The utility model relates to chemical machinery field, is specifically related to a kind of powder dispersion treatment device.
Background technology
In the Chemical Manufacture, the superfine powder powder that produces is very little, and the surface of powder can be very big, forms the phenomenon of bulk easily, give the processing belt difficulty in later stage, traditional dispersion is to use machinery that powder is stirred, but so easy introducing iron or other impurity, thus influence processing in the subsequent handling, promote difficulty of processing, cause inefficiency, and power consumption is high, the weak effect of dispersion.
How to design a kind of material that makes and fully to continue to disperse, and the device that can efficiently powder be screened is the problem that those skilled in the art need solve.
Summary of the invention
Primary and foremost purpose of the present utility model just is to overcome the existing deficiency of existing treating apparatus, thereby a kind of powder dispersion treatment device is provided.
Powder dispersion treatment device of the present utility model, comprise disperser cavity, jet assembly and grading wheel, the wall of described disperser cavity is provided with feed opening and jet assembly, described jet assembly is arranged at the below of feed opening, the top of described disperser cavity is provided with discharging opening, described grading wheel is arranged at the disperser inside cavity, and described grading wheel is arranged between feed opening and the discharging opening.
Described jet assembly is at least four walls that are evenly arranged in the disperser cavity and insert the shower nozzle of disperser inside cavity, and described four shower nozzles are arranged at same horizontal level.
The center line of the shower nozzle of described insertion disperser inside cavity and the angle of horizontal plane are greater than 45 degree.The angle of this shower nozzle setting can make the compressed air of output blow afloat material and make most powders of lighter weight wherein be in position near disperser cavity top, be convenient to the filter element that powder passes grading wheel, is extracted into discharging opening, has improved the operating efficiency of device.
The Compressed Gas of described shower nozzle output is 0.01~0.80MPa.
The distance of disperser cavity bottom surface is arrived greater than 2/3rds of disperser housing depth in the axis of described feed opening.The position of this feed opening can make compressed air blow afloat most powders of lighter weight in the material to be in position near disperser cavity top, to be convenient to the filter element that powder passes grading wheel, be extracted into discharging opening, improved the operating efficiency of device.
Described feed opening is connected with blanking bin.
The mouth of pipe of described blanking bin is infundibulate, and the mouth of pipe of funnel shaped blanking bin makes things convenient for charging.
Described grading wheel is divided into the disperser cavity chamber of two isolation.
Described grading wheel rotating speed is at 100~3000 rev/mins.
Also be provided with dosing mouth on the wall of described disperser cavity, described dosing mouth is arranged between grading wheel and the jet assembly.
The below of described disperser cavity is provided with pedestal.
During the utility model work, material enters the disperser cavity from blanking bin by feed opening, the compressed air of shower nozzle output blows afloat material collides it mutually, and the inorganic agent that dosing mouth is added fully disperses reaction, make material have good flowability and dispersed, material moves in the disperser cavity, the inwall collision of material and disperser cavity makes powder scatter, grading wheel is divided into the disperser cavity chamber of two isolation, material upwards flows under the air inducing effect of grading wheel, the powder of required collection passes the filter element of grading wheel, is extracted into discharging opening.
The utility model can continue dispersion treatment to powder, and the powder after the processing presents extraordinary flowability, and dispersion effect is good, high efficiency, and it is low to consume energy, simple in structure and easy to operate.
Description of drawings
Fig. 1 is the structural representation of present embodiment.
Fig. 2 is the position view of shower nozzle of the insertion disperser inside cavity of present embodiment.
The specific embodiment
Below in conjunction with specific embodiment, the utility model is described in further detail.Should be understood that following examples are only for explanation the utility model but not for limiting scope of the present utility model.
As shown in Figure 1, powder dispersion treatment device of the present utility model, comprise disperser cavity 1, jet assembly 2 and grading wheel 3, the wall of described disperser cavity 1 is provided with feed opening 11 and jet assembly 2, described jet assembly 2 is arranged at the below of feed opening 11, the top of described disperser cavity 1 is provided with discharging opening 12, and described grading wheel 3 is arranged at disperser cavity 1 inside, and described grading wheel 3 is arranged between feed opening 11 and the discharging opening 12.
Described jet assembly 2 is at least four walls that are evenly arranged in disperser cavity 1 and insert the shower nozzle 21 of disperser cavity 1 inside, and described four shower nozzles 21 are arranged at same horizontal level.
As shown in Figure 2, the angle α of the center line of the shower nozzle 21 of described insertion disperser cavity 1 inside and horizontal plane is greater than 45 degree.The angle that this shower nozzle 21 arranges can make the compressed air of output blow afloat material to make most powders of lighter weight wherein be in position near disperser cavity 1 top, be convenient to the filter element that powder passes grading wheel 3, be extracted into discharging opening 12, improved the operating efficiency of device.
As shown in Figure 1, the Compressed Gas of described shower nozzle 21 outputs is 0.01~0.80MPa.
The distance H 1 of disperser cavity 1 bottom surface is arrived greater than 2/3rds of disperser cavity 1 height H 2 in the axis of described feed opening 11.The position of this feed opening 11 can make compressed air blow afloat most powders of lighter weight in the material to be in position near disperser cavity 1 top, to be convenient to the filter element that powder passes grading wheel 3, be extracted into discharging opening 12, improved the operating efficiency of device.
Described feed opening 11 is connected with blanking bin 5.
The mouth of pipe of described blanking bin 5 is infundibulate, and the mouth of pipe of funnel shaped blanking bin 5 makes things convenient for charging.
Described grading wheel 3 is divided into disperser cavity 1 chamber of two isolation.
Described grading wheel 3 rotating speeds are at 100~3000 rev/mins.
Also be provided with dosing mouth 4 on the wall of described disperser cavity 1, described dosing mouth 4 is arranged between grading wheel 3 and the jet assembly 2.
The below of described disperser cavity 1 is provided with pedestal 6.
During the utility model work, material enters disperser cavity 1 from blanking bin 5 by feed opening 11, the compressed air of shower nozzle 21 outputs blows afloat material collides it mutually, and the inorganic agent that dosing mouth 4 is added fully disperses reaction, make material have good flowability and dispersed, material moves in disperser cavity 1, the inwall collision of material and disperser cavity 1 makes powder scatter, grading wheel 3 is divided into disperser cavity 1 chamber of two isolation, material upwards flows under the air inducing effect of grading wheel 3, the powder of required collection passes the filter element of grading wheel 3, is extracted into discharging opening 12.
The utility model can continue dispersion treatment to powder, and the powder after the processing presents extraordinary flowability, and dispersion effect is good, high efficiency, and it is low to consume energy, simple in structure and easy to operate.

Claims (9)

1. powder dispersion treatment device, comprise disperser cavity, jet assembly and grading wheel, it is characterized in that, the wall of described disperser cavity is provided with feed opening and jet assembly, described jet assembly is arranged at the below of feed opening, the top of described disperser cavity is provided with discharging opening, and described grading wheel is arranged at the disperser inside cavity, and described grading wheel is arranged between feed opening and the discharging opening.
2. powder dispersion treatment device as claimed in claim 1 is characterized in that, described jet assembly is at least four walls that are evenly arranged in the disperser cavity and insert the shower nozzle of disperser inside cavity, and described four shower nozzles are arranged at same horizontal level.
3. powder dispersion treatment device as claimed in claim 2 is characterized in that, the center line of the shower nozzle of described insertion disperser inside cavity and the angle of horizontal plane are greater than 45 degree.
4. powder dispersion treatment device as claimed in claim 3 is characterized in that, the Compressed Gas of described shower nozzle output is 0.01~0.80MPa.
5. powder dispersion treatment device as claimed in claim 1 is characterized in that, the distance of disperser cavity bottom surface is arrived greater than 2/3rds of disperser housing depth in the axis of described feed opening.
6. powder dispersion treatment device as claimed in claim 5 is characterized in that described feed opening is connected with blanking bin.
7. powder dispersion treatment device as claimed in claim 1 is characterized in that, described grading wheel is divided into the disperser cavity chamber of two isolation.
8. powder dispersion treatment device as claimed in claim 7 is characterized in that, described grading wheel rotating speed is at 100~3000 rev/mins.
9. powder dispersion treatment device as claimed in claim 1 is characterized in that, also is provided with dosing mouth on the wall of described disperser cavity, and described dosing mouth is arranged between grading wheel and the jet assembly.
CN201220734624.2U 2012-12-27 2012-12-27 Device for dispersing powder Expired - Fee Related CN203108535U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201220734624.2U CN203108535U (en) 2012-12-27 2012-12-27 Device for dispersing powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201220734624.2U CN203108535U (en) 2012-12-27 2012-12-27 Device for dispersing powder

Publications (1)

Publication Number Publication Date
CN203108535U true CN203108535U (en) 2013-08-07

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201220734624.2U Expired - Fee Related CN203108535U (en) 2012-12-27 2012-12-27 Device for dispersing powder

Country Status (1)

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CN (1) CN203108535U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107790049A (en) * 2017-11-28 2018-03-13 佛山科学技术学院 A kind of industrial chemicals powder blender
CN108162233A (en) * 2017-12-21 2018-06-15 广东德新科技孵化器有限公司 A kind of automatic online powder treatment device of plastic extruding forming

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107790049A (en) * 2017-11-28 2018-03-13 佛山科学技术学院 A kind of industrial chemicals powder blender
CN108162233A (en) * 2017-12-21 2018-06-15 广东德新科技孵化器有限公司 A kind of automatic online powder treatment device of plastic extruding forming

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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: 20130807

Termination date: 20151227

EXPY Termination of patent right or utility model