CN109201217A - One kind can be with quantity-produced zirconium ball powder homogenizing device - Google Patents
One kind can be with quantity-produced zirconium ball powder homogenizing device Download PDFInfo
- Publication number
- CN109201217A CN109201217A CN201811185795.2A CN201811185795A CN109201217A CN 109201217 A CN109201217 A CN 109201217A CN 201811185795 A CN201811185795 A CN 201811185795A CN 109201217 A CN109201217 A CN 109201217A
- Authority
- CN
- China
- Prior art keywords
- powder
- cyclone separator
- main cylinder
- air hose
- feeding chamber
- 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
- 239000000843 powder Substances 0.000 title claims abstract description 50
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 title claims abstract description 17
- 229910052726 zirconium Inorganic materials 0.000 title claims abstract description 17
- 239000004744 fabric Substances 0.000 claims abstract description 12
- 230000005540 biological transmission Effects 0.000 claims abstract description 10
- 239000000428 dust Substances 0.000 claims abstract description 10
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 abstract description 4
- 238000010924 continuous production Methods 0.000 abstract description 2
- 239000011324 bead Substances 0.000 description 3
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 229910001928 zirconium oxide Inorganic materials 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012797 qualification Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- SIWVEOZUMHYXCS-UHFFFAOYSA-N oxo(oxoyttriooxy)yttrium Chemical compound O=[Y]O[Y]=O SIWVEOZUMHYXCS-UHFFFAOYSA-N 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/10—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls with one or a few disintegrating members arranged in the container
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/18—Details
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/18—Details
- B02C17/183—Feeding or discharging devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/18—Details
- B02C17/183—Feeding or discharging devices
- B02C17/186—Adding fluid, other than for crushing by fluid energy
- B02C17/1865—Adding fluid, other than for crushing by fluid energy after crushing
- B02C17/187—Adding fluid, other than for crushing by fluid energy after crushing with recirculation of material to crushing zone
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Cyclones (AREA)
Abstract
The present invention provides one kind can be with quantity-produced zirconium ball powder homogenizing device, including main cylinder, main cylinder support frame, feeding chamber, second level feeding chamber, cyclone separator, feeding-passage, cloth bag pulse dust collector, powder exports air hose, transmission device, centrifugal blower, described main cylinder one end connects feeding-passage, feeding-passage connects second level feeding chamber, second level feeding chamber connects feeding chamber and cyclone separator, the main cylinder other end connection powder exports air hose, the other end that powder exports air hose connects cyclone separator, it connects cyclone separator and cloth bag pulse dust collector is connected by air hose.The present invention in process of production can be with continuous production, underproof coarse fodder is constantly converted into qualified material, it ensure that the continuity of entire production process and the utilization rate of raw material improved as far as possible, to improve the yield of entire zirconium ball production, while greatly reducing production cost.
Description
Technical field
The invention belongs to grinder fields, and in particular to one kind can be with quantity-produced zirconium ball powder homogenizing device.
Background technique
Zirconium oxide bead is using micron order and Subnano-class zirconium oxide and yttrium oxide made of raw material, to be for requiring "
No pollution " and high viscosity, the extra-fine grinding of high rigidity material and a kind of grinding bead of dispersion.It is mainly used in requirement " no pollution "
And the extra-fine grinding and dispersion of high viscosity, high rigidity material.Such as: electronic ceramics, magnetic material, extraordinary chemical industry.Oxidation
The production technology of zirconium pearl is general are as follows: defibrination, drying, homogenizing, Cheng Fu, balling-up, screening have in the production technology of zirconium oxide bead
One step needs zirconium pearl powder material to dry, and zirconium pearl powder has the non-uniform phenomenons such as agglomeration after drying, at this moment needs by equal
Makeup, which is set, screens powder, the thicker raw material of a part is further refined, while also to delete meticulous powder, is reached
Fineness to requirement just can enter the next step.Equipment generally currently on the market is separately processed by several equipment
Thick and meticulous unqualified material, and excessively thick material is refined by other equipment again, treatment effeciency is low.
Summary of the invention
Goal of the invention: can be with quantity-produced it is an object of the invention to aiming at the shortcomings in the prior art, provide one kind
Zirconium ball powder homogenizing device.
In order to achieve the object of the present invention, use following technical scheme: one kind can be with quantity-produced zirconium ball powder homogenizing
Device, including main cylinder, main cylinder support frame, feeding chamber, second level feeding chamber, cyclone separator, feeding-passage, cloth bag pulse remove
Dirt device, powder export air hose, transmission device, centrifugal blower, and described main cylinder one end connects feeding-passage, feeding-passage connection two
Grade feeding chamber, second level feeding chamber connect feeding chamber and cyclone separator, and the main cylinder other end connection powder exports air hose, powder
The other end that body exports air hose connects cyclone separator, connects cyclone separator by air hose and connects cloth bag pulse dust collector.
The main cylinder inner wall is equipped with rectangle raised line, and rectangle raised line is uniformly distributed in main cylinder inner wall, along axial phase
Adjacent two raised lines arrangement straggly is more advantageous to powder and exists due to being provided with raised line equivalent to increase the frictional force of main cylinder inner wall
It rolls in main cylinder, increases the touch opportunity of powder and abrading-ball, improve the refining efficiency of powder.
The transmission device includes speed regulating motor, driving belt driving wheel, driving belt driven wheel, driving belt.
The feeding-passage is screw transfer passage, can prevent powder from overflowing and dissipate, protect ambient enviroment, ensured behaviour
The physical safety of workmanship.
The connection type of the other end connection cyclone separator of the powder output air hose is that powder exports air hose along whirlwind
The connection of separator inner wall tangent line, powder export the qualification in air hose and enter cyclone separator by tangent line with unqualified mixture,
Qualified and underproof fines, is distributed in the central area of cyclone separator, is collected by pipeline and enters cloth bag pulse dust collector,
Underproof coarse fodder falls along the inner wall of cyclone separator to bottom, enters back into second level feeding chamber and re-grinds, effectively connects
The underproof coarse fodder of continuous separation, circulation are converted into underproof coarse fodder qualified fines.
Beneficial effect
Underproof coarse fodder constantly can be converted into qualified material with continuous production in process of production by the present invention, ensure that whole
The continuity of a production process and the utilization rate of raw material is improved as far as possible, to improve the yield of entire zirconium ball production, together
When greatly reduce production cost.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is raised line layout drawing.
Fig. 3 is the concrete structure schematic diagram of transmission device.
In figure: 1, main cylinder 2, main cylinder support frame 3, feeding chamber 4, second level feeding chamber 5, cyclone separator 6, charging are logical
Road 7, cloth bag pulse dust collector 8, powder output air hose 9, transmission device 10, centrifugal blower 11, raised line 12, speed regulating motor 13,
Driving belt driving wheel 14, driving belt driven wheel 15, driving belt.
Specific embodiment
The present invention is further illustrated with reference to the accompanying drawings and examples.
As shown in Figure 1, Figure 2, shown, one kind can be with quantity-produced zirconium ball powder homogenizing device, including main cylinder 1, main cylinder
Support frame 2, feeding chamber 3, second level feeding chamber 4, cyclone separator 5, feeding-passage 6, cloth bag pulse dust collector 7, powder export wind
Pipe 8, transmission device 9, centrifugal blower 10, described 1 one end of main cylinder connect feeding-passage 6, and feeding-passage 6 connects second level feeding chamber
4, second level feeding chamber 4 connects feeding chamber 3 and cyclone separator 5, and 1 other end of the main cylinder connection powder exports air hose 8, powder
The other end for exporting air hose 8 connects cyclone separator 5, and cyclone separator connects cloth bag pulse dust collector 7 by air hose.
1 inner wall of main cylinder is equipped with rectangle raised line 11, and rectangle raised line 11 is uniformly distributed in main cylinder inner wall, along axis
To adjacent two raised lines arrangement straggly, due to being provided with raised line 11, equivalent to increase the frictional force of 1 inner wall of main cylinder, more favorably
It rolls in main cylinder 1 in powder, increases the touch opportunity of powder and abrading-ball, improve the refining efficiency of powder.
The transmission device 9 includes speed regulating motor 12, driving belt driving wheel 13, driving belt driven wheel 14, transmission skin
Band 15.
The feeding-passage 6 is screw transfer passage, can prevent powder from overflowing and dissipate, protect ambient enviroment, ensure
The physical safety of operative employee.
The connection type of the other end connection cyclone separator 5 of the powder output air hose 8 is that powder exports air hose 8 along rotation
The connection of 5 inner wall tangent line of wind separator, powder export the qualification in air hose 8 and enter cyclonic separation by tangent line with unqualified mixture
Device 5, qualified and underproof fines, is distributed in the central area of cyclone separator 5, is collected by pipeline into cloth bag pulse and is removed
Dirt device, underproof coarse fodder fall to bottom along the inner wall of cyclone separator 5, enter back into second level feeding chamber 4 and re-grind, have
The underproof coarse fodder of continuously separation of effect, circulation are converted into underproof coarse fodder qualified fines.
Workflow: powder is continuously added to feeding chamber, opens machine, adjusts suitable wind-force and drum speed, sets
Good cyclone separator, qualified powder enter next procedure by the outlet of cloth bag pulse dust collector, and underproof coarse fodder passes through
Cyclone separator enters back into cylinder grinding, and continuous to recycle, in addition to meticulous unqualified powder, excessively thick unqualified powder turns always
Turn to qualified powder.
Claims (5)
1. one kind can be with quantity-produced zirconium ball powder homogenizing device, which is characterized in that including main cylinder, main cylinder support frame,
Feeding chamber, second level feeding chamber, cyclone separator, feeding-passage, cloth bag pulse dust collector, powder output air hose, transmission device, from
Heart blower, described main cylinder one end connect feeding-passage, and feeding-passage connects second level feeding chamber, and second level feeding chamber connects feeding chamber
And cyclone separator, the main cylinder other end connection powder export air hose, powder exports the other end connection whirlwind point of air hose
From device, cyclone separator connects cloth bag pulse dust collector by air hose.
2. according to claim 1 can be with quantity-produced zirconium ball powder homogenizing device, which is characterized in that the main cylinder
Inner wall is equipped with rectangle raised line.
3. according to claim 1 can be with quantity-produced zirconium ball powder homogenizing device, which is characterized in that the transmission dress
It sets including speed regulating motor, driving belt driving wheel, driving belt driven wheel, driving belt.
4. according to claim 1 can be with quantity-produced zirconium ball powder homogenizing device, which is characterized in that the charging is logical
Road is screw transfer passage.
5. according to claim 1 can be with quantity-produced zirconium ball powder homogenizing device, which is characterized in that the powder is defeated
The connection type of the other end connection cyclone separator of discharge pipe is that powder exports air hose along the connection of cyclone separator inner wall tangent line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811185795.2A CN109201217A (en) | 2018-10-11 | 2018-10-11 | One kind can be with quantity-produced zirconium ball powder homogenizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811185795.2A CN109201217A (en) | 2018-10-11 | 2018-10-11 | One kind can be with quantity-produced zirconium ball powder homogenizing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109201217A true CN109201217A (en) | 2019-01-15 |
Family
ID=64979997
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811185795.2A Pending CN109201217A (en) | 2018-10-11 | 2018-10-11 | One kind can be with quantity-produced zirconium ball powder homogenizing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109201217A (en) |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4039079A1 (en) * | 1990-12-07 | 1992-06-11 | Heinz Jaeger | Limestone reduction - using hammer mill and rotary crusher before material is finely ground for cement |
| RU2060054C1 (en) * | 1994-06-23 | 1996-05-20 | Томский филиал Института структурной макрокинетики РАН | Device for grinding loose materials |
| CN202460706U (en) * | 2012-01-17 | 2012-10-03 | 潍坊特钢集团新型建材有限公司 | Pre-grinding device for producing steel slag powder |
| CN103521334A (en) * | 2013-10-10 | 2014-01-22 | 徐州天正活性炭厂 | Active carbon dust-free grinding device and method |
| CN205269784U (en) * | 2015-12-20 | 2016-06-01 | 王龙昭 | High -efficient inverter type ore crushing device |
| CN205887107U (en) * | 2016-07-22 | 2017-01-18 | 天津水泥工业设计研究院有限公司 | Whole grinding system of cement roll squeezer of parallelly connected two selection powder machines |
| CN106732919A (en) * | 2016-11-27 | 2017-05-31 | 安徽喜洋洋农业科技有限公司 | A kind of production method of middle micro- granular fertilizer |
| CN206823967U (en) * | 2017-05-24 | 2018-01-02 | 福建鸿丰纳米科技有限公司 | A kind of nano-calcium carbonate continuously crushes depolymerizer |
| CN207287568U (en) * | 2017-09-21 | 2018-05-01 | 孙玉美 | A kind of medicine material comminuting dasher |
| CN207446436U (en) * | 2017-07-13 | 2018-06-05 | 湖北黄仙洞葛业食品有限公司 | A kind of ultra micro kudzuvine root starch preparation facilities |
| CN209465121U (en) * | 2018-10-11 | 2019-10-08 | 宜兴市海科耐火材料制品有限公司 | One kind can be with quantity-produced zirconium ball powder homogenizing device |
-
2018
- 2018-10-11 CN CN201811185795.2A patent/CN109201217A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4039079A1 (en) * | 1990-12-07 | 1992-06-11 | Heinz Jaeger | Limestone reduction - using hammer mill and rotary crusher before material is finely ground for cement |
| RU2060054C1 (en) * | 1994-06-23 | 1996-05-20 | Томский филиал Института структурной макрокинетики РАН | Device for grinding loose materials |
| CN202460706U (en) * | 2012-01-17 | 2012-10-03 | 潍坊特钢集团新型建材有限公司 | Pre-grinding device for producing steel slag powder |
| CN103521334A (en) * | 2013-10-10 | 2014-01-22 | 徐州天正活性炭厂 | Active carbon dust-free grinding device and method |
| CN205269784U (en) * | 2015-12-20 | 2016-06-01 | 王龙昭 | High -efficient inverter type ore crushing device |
| CN205887107U (en) * | 2016-07-22 | 2017-01-18 | 天津水泥工业设计研究院有限公司 | Whole grinding system of cement roll squeezer of parallelly connected two selection powder machines |
| CN106732919A (en) * | 2016-11-27 | 2017-05-31 | 安徽喜洋洋农业科技有限公司 | A kind of production method of middle micro- granular fertilizer |
| CN206823967U (en) * | 2017-05-24 | 2018-01-02 | 福建鸿丰纳米科技有限公司 | A kind of nano-calcium carbonate continuously crushes depolymerizer |
| CN207446436U (en) * | 2017-07-13 | 2018-06-05 | 湖北黄仙洞葛业食品有限公司 | A kind of ultra micro kudzuvine root starch preparation facilities |
| CN207287568U (en) * | 2017-09-21 | 2018-05-01 | 孙玉美 | A kind of medicine material comminuting dasher |
| CN209465121U (en) * | 2018-10-11 | 2019-10-08 | 宜兴市海科耐火材料制品有限公司 | One kind can be with quantity-produced zirconium ball powder homogenizing device |
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| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20190115 |