WO2015151187A1 - 分級機 - Google Patents
分級機 Download PDFInfo
- Publication number
- WO2015151187A1 WO2015151187A1 PCT/JP2014/059519 JP2014059519W WO2015151187A1 WO 2015151187 A1 WO2015151187 A1 WO 2015151187A1 JP 2014059519 W JP2014059519 W JP 2014059519W WO 2015151187 A1 WO2015151187 A1 WO 2015151187A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- classification
- rotor
- classifier
- classification rotor
- powder
- Prior art date
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force
- B07B7/083—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force generated by rotating vanes, discs, drums, or brushes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/02—Arrangement of air or material conditioning accessories
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/06—Feeding or discharging arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B13/00—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices
- B07B13/10—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices using momentum effects
- B07B13/11—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices using momentum effects involving travel of particles over surfaces which separate by centrifugal force or by relative friction between particles and such surfaces, e.g. helical sorters
Definitions
- the present invention relates to a classifier, and more particularly to a classifier for obtaining ultrafine powder.
- It is constituted by a cylinder having a plurality of classification blades on the outer peripheral part, and has a classification rotor having an opening opened on one side surface in a direction along the axis of the cylinder,
- An apparatus main body that holds the powder to be classified from the outside and supplies it to the outer periphery of the classification rotor, and holds the powder classified by the classification rotor, while holding it rotatably around the shaft center
- the tip side portion of the discharge unit arranged so as to enter the inside of the classification rotor is attached to the classification rotor side, and is rotated integrally with the classification rotor.
- a classifier that reduces the relative speed difference between the powder passing through the tip side portion in a swiveling state and the inner wall of the tip side portion and suppresses wear of the inner wall of the tip side portion and adhesion of the powder.
- Known for example , See Patent Document 1).
- the tip side portion of the discharge portion is formed in a substantially tapered shape whose opening diameter gradually expands from the tip side toward the discharge side, and the powder passing through the tip side portion and the tip side portion are formed.
- a classifier that reduces the impact of the inner wall of the tip side portion from the powder and the friction between the inner wall and the powder by reducing the collision angle with the wall surface (see, for example, Patent Document 2).
- the present invention has been made in view of the above problems, and it is an object of the present invention to provide a classifier capable of classifying finer fine particles and obtaining a narrower particle size distribution.
- the classifier according to the present invention includes a cylinder having a plurality of classification blades on the outer periphery, and a classifier having an opening that opens on one side surface in the direction along the axis of the cylinder.
- a rotor, a throttle part provided in the opening and reducing the inner diameter thereof, and the classification rotor is accommodated and rotatably held around the axis, and the powder to be classified is introduced from the outside.
- a device main body that is supplied to the outer peripheral portion of the classification rotor, and a discharge unit that sucks and takes out the powder classified by the classification rotor to the outside of the device main body.
- the rotating shaft portion extending over the other side surface is provided so as to increase in diameter toward the other side surface.
- the diameter of the rotating shaft extending from the opening surface of the throttle portion to the other side surface of the classification rotor is expanded toward the other side surface.
- the throttle portion is formed so as to be reduced in diameter from the opening of the classification rotor to the inside of the classification rotor.
- the tip of the throttle portion enters the inside of the classification rotor, the difference in distance from each part of the classification blade to the opening surface can be reduced. For this reason, the flow state of the air inside the classification rotor can be equalized, and the classification accuracy is improved.
- the friction between the powder and the throttle part can be reduced by reducing the collision angle between the powder passing through the throttle part and the wall surface of the throttle part. It is possible to prevent the vortex flow velocity from decreasing.
- Another characteristic configuration of the present invention is that the ratio of the effective passing cross-sectional area of the classified powder at the opening surface to the inner cross-sectional area of the classifying rotor is 10% or less.
- the effective passage cross-sectional area of the powder means the area through which the classified powder can pass through the opening surface, and the inner cross-sectional area of the classification rotor is within the classification rotor. , Means the cross-sectional area including the rotating shaft.
- the classification cut point can be reduced, the particle size distribution can be reduced, and the classification accuracy can be improved.
- Another feature of the present invention is that the ratio of the cross-sectional area of the rotating shaft portion in the opening surface to the cross-sectional area of the opening surface is set to 30% or more.
- the rotational speed of the classification rotor can be increased by increasing the cross-sectional area of the rotating shaft portion, the classification accuracy can be improved.
- classification rotor is formed of silicon nitride ceramics.
- the classification rotor can be reduced in weight by using silicon nitride ceramics, the rotation speed of the classification rotor can be increased. As a result, classification accuracy is improved. Moreover, since silicon nitride ceramics have high hardness, it is possible to impart excellent wear resistance to the classification rotor.
- the particle diameter distribution of the raw material powder used by the Example and comparative example of this invention is shown.
- the particle size distribution of the fine powder obtained when using the classifier 1 of the present invention is shown.
- the particle size distribution of the fine powder obtained when using the classifier 1 'of the comparative example of the present invention is shown.
- the particle size distribution of the fine powder obtained when using the classifier 1 of the present invention is shown.
- the modification of the rotating shaft part 2 in the classifier 1 which concerns on this invention is shown.
- the modification of the rotating shaft part 2 in the classifier 1 which concerns on this invention is shown.
- FIG. 1 is an axial longitudinal sectional view schematically showing a main configuration of a classifier 1 in one embodiment of the present invention.
- FIG. 2 is an axial cross-sectional view schematically showing the classification rotor 3
- FIG. 3 is a top view schematically showing the classification rotor 3.
- the classifier 1 accommodates the classifying rotor 3 and the classifying rotor 3 so as to be rotatable about the axis X, and introduces the raw material powder P, which is a classifying target powder, from the outside.
- the apparatus main body 5 supplied to the outer peripheral part and the discharge part 52 which sucks the fine powder b classified by the classification rotor 3 and takes it out of the apparatus main body 5 are provided.
- the classification rotor 3 is a cylindrical body having a plurality of classification blades 33 on the outer peripheral portion, and is configured to be rotatable around the axis X. Further, the classification rotor 3 is provided with an opening 34 that opens on one side surface in the direction along the axis X.
- the classification blades 33 are arranged at predetermined intervals along the radial direction of the cylinder so as to protrude toward the axis X, and a forced vortex is generated around the classification rotor 3 by the rotation of the classification rotor 3. At the same time, the gap 32 formed between the classification blades 33 is configured to allow powder and air to flow into the classification rotor 3.
- the opening 34 of the classifying rotor 3 is provided with a dip pipe 4 as a throttle portion that reduces the inner diameter.
- the dip pipe 4 is formed in a substantially tapered shape so that the diameter of the dip pipe 4 is reduced from the opening 34 of the classifying rotor 3 to the inside.
- the rotary shaft portion 2 has a first shaft portion 21 and a second shaft portion 22 in order from the bottom, and the upper end portion is connected to drive means (not shown) as a drive shaft of the classification rotor 3.
- the shaft 23 is formed so as to be rotatable integrally with the classifying rotor 3 around the axis X.
- the first shaft portion 21 is formed integrally with the classifying rotor 3 and is provided so as to be able to penetrate the shaft 23, and is connected to the shaft 23 on the lower surface of the classifying rotor 3 so as to be integrally rotatable.
- the first shaft portion 21 has a substantially truncated cone shape whose diameter decreases from the bottom surface portion 31 which is the other side surface of the classifying rotor 3 to the opening surface O of the dip pipe 4.
- a passage surface E through which the fine powder b passes toward the discharge portion 52 is formed by the tip portion 41 of the pipe 4.
- the second shaft portion 22 is provided in a substantially inverted truncated cone shape with respect to the first shaft portion 21 so as to increase in diameter upward from the opening surface O of the classification rotor 3. Thereby, the discharge flow path 521 with few steps can be formed together with the cover of the second shaft portion 22 and the shaft 23. As a result, it is possible to reduce the resistance of the airflow in the discharge flow path 521 and to prevent the powder from adhering to the discharge flow path 521 and the powder from entering the shaft. Similar to the first shaft portion 21, the second shaft portion 22 is provided so as to be able to pass through the shaft 23, and can rotate integrally with the shaft 23 and the first shaft portion 21.
- the material of the classification rotor 3 general steel materials, alumina, zirconia, silicon nitride ceramics, and the like can be used.
- silicon nitride ceramics when silicon nitride ceramics are used, the classification rotor 3 can be reduced in weight because of its light weight and strength, and the rotational speed can be further increased.
- the apparatus main body 5 includes a casing 50 that accommodates the classification rotor 3, a raw material supply unit 51 that supplies the raw material powder P, and a coarse powder that is prevented from flowing into the classification rotor 3 by the classification blades 33 of the classification rotor 3. a coarse powder discharger 53 for discharging a.
- the classifier of the present invention is configured as a device having only the function of the classifier. It can also be configured as a device having other functions.
- the classifier of the present invention can be provided as a part of the pulverizer, and the powder pulverization process and the classification process can be performed continuously.
- the discharge part 52 has a discharge channel 521, and sucks air inside the classification rotor 3 through the discharge channel 521 by suction means (not shown) such as a blower.
- suction means such as a blower.
- the suction strength can be changed freely.
- the rotational speed of the suction fan can be changed, or the amount of air to be sucked can be changed as appropriate using a flow rate adjustment valve or the like.
- the classifying rotor 3 can be rotated at high speed by the driving means, and the air inside the classifying rotor 3 is sucked by the suction means so that the air around the classifying rotor 3 is rotated at high speed. It can be drawn from the gap 32 of the rotor 3. As a result, fine powder b having a predetermined particle diameter or less is taken into the classification rotor 3, and coarse powder a having an excessive particle diameter is prevented from flowing into the classification rotor 3 by the rotating classification blade 33.
- the first-stage classification can be performed.
- the air that flows into the classifying rotor 3 together with the fine powder b becomes a semi-free vortex inside the classifying rotor 3 due to the high speed rotation of the classifying rotor 3, and passes through the passage surface E while rising. Due to the centrifugal force of the semi-free vortex, among the fine powders b taken into the classification rotor 3, those having a relatively large particle size are blown to the outside, and the solid-gas ratio (dust concentration) in the semi-free vortex is low. Thus, since only the fine powder b having a smaller particle diameter passes through the passage surface E, the second-stage classification is performed here.
- the outer diameter of the first shaft portion 21 on the passage surface E is reduced to allow the passage surface E to pass from the center side of the semi-free vortex, and the passage surface E is reduced by the dip pipe 4 to reduce the area of the passage surface E.
- the first shaft portion 21 into a substantially truncated cone shape so that the angle between the outer peripheral surface portion 211 of the first shaft portion 21 and the bottom surface portion 31 of the classification rotor 3 is an obtuse angle, the inside of the classification rotor 3 is formed. Since the inflowing air is less likely to stay between the first shaft portion 21 and the bottom surface portion 31, it is possible to prevent the flow velocity from decreasing due to the resistance of a semi-free vortex.
- the dip pipe 4 so as to be able to rotate integrally with the classification rotor 3
- friction between the air inside the classification rotor 3 and the dip pipe 4 can be prevented, and a decrease in the flow velocity of the semi-free vortex can be prevented.
- the dip pipe 4 is moved into the classifying rotor 3, the difference in distance from each part of the classifying blade 33 to the passage surface E can be reduced. The air flow state can be equalized.
- the fine powder b classified by the classification rotor 3 is discharged by the discharge unit 52, and then guided to a collecting means such as a bag filter, and taken out as a product.
- the ratio (ratio A) of the effective passage cross-sectional area (S E ) of fine powder in the opening surface O to the inner cross-sectional area (S R ) of the classification rotor 3, the cross-sectional area (S The ratio (ratio B) of the cross-sectional area (S c ) of the first shaft portion 21 on the opening surface O to o ) and the particle size distribution of the fine powder obtained were examined.
- the ratio A, the ratio B, and the fine particles obtained The diameter distribution was examined.
- the calculation method of the ratio A and the ratio B is as shown in the following formula 1 and formula 2.
- r o is the distance from the axis X to the distal end 41 of the dip pipe 4
- r c is the radius of the rotation shaft 2 in the aperture plane O
- r R is the classification rotor 3 is a radius of the inner cross section of 3 (distance from the axis X to the inside of the classification blade 33).
- Table 1 shows the dimensions and ratios of the classifier 1 used in the example and the classifier 1 'used in the comparative example.
- Example 1 Using a raw material powder of the particle size distribution shown in FIG. 4, in the classifier 1, the operating conditions, the operating air volume: 7.0 m 3 / min, capacity: the particle size distribution, when classified as 6.4 kg / h This is shown in FIG. 5 and Table 2.
- the classifier 1 of the example can have a smaller particle size than the classifier 1 'of the comparative example.
- the classifier 1 (a) and (b) with different dimensions and ratios were used as the classifier 1 according to this embodiment, and the same results as in the examples were obtained. It was.
- the classification accuracy was high.
- the classifier 1 according to the present embodiment can reduce the particle size of the fine powder obtained by classification and sharpen the particle size distribution as compared with the conventional classifier.
- the ratio A is preferably 10% or less, more preferably 8.6% to 9.4%, and the ratio B is preferably 30% or more, more preferably 30.0% to 44%. Found 4%.
- rotating shaft part 2 has illustrated the case where the 1st shaft part 21 and the 2nd shaft part 22 are formed with another member, the 1st shaft part 21 and the 2nd shaft part are illustrated. 22 may be integrally formed.
- the first shaft portion 21 is formed integrally with the classifying rotor 3, but in the present invention, it may be formed separately from the classifying rotor 3.
- the second shaft portion 22 is exemplified by the case where the outer peripheral surface portion 211 expands upward, but the shape of the second shaft portion 22 is not limited.
- the rotating shaft portion 2 is exemplified by the case where the shaft 23 connected to the driving means is penetrated and connected to the lower surface of the classifying rotor 3, but the classifying rotor 3 only needs to be rotatable.
- the shape, arrangement, connection mode and the like of the shaft 23 are not limited.
- the plate-like classification blades 33 may have a predetermined angle with respect to the axis X and are attached obliquely with respect to the radial direction. May be.
- the classification blade 33 can also be configured in an inclined shape or a curved shape.
Landscapes
- Combined Means For Separation Of Solids (AREA)
Abstract
Description
以下に、本発明に係る分級機を用いた実施例を示し、本発明をより詳細に説明する。但し、本発明はこれらの実施例に限定されるものではない。
図4に示す粒径分布の原料粉体を用い、分級機1で、運転条件を、運転風量:7.0m3/min、処理能力:6.4kg/hとして分級したときの粒径分布を図5及び表2に示した。このときのトップサイズの切れ(D90/D50)は、1.437(μm)/0.726(μm)=2.0であった。
実施例と同様の原料粉体を用い、比較例として分級機1’で、運転条件を、運転風量:7.0m3/min、処理能力:7.7kg/hとして分級したときの粒径分布を図6及び表3に示した。このときのD90/D50は、1.892(μm)/0.982(μm)=1.9であった。
分級機1を用い、比較例と同様の粒径とするべく、運転条件を、運転風量:7.0m3/min、処理能力:8.7kg/hとして、同様に分級したときの粒径分布を図7及び表4に示した。このときのD90/D50は、1.615(μm)/0.908(μm)=1.8であり、比較例に比べてシャープな粒径分布が得られることが分かった。
上記実施形態では、回転軸部2は、第1軸部21と第2軸部22とは、別部材で形成されている場合を例示しているが、第1軸部21と第2軸部22とは一体に形成されてもよい。
2 回転軸部
21 第1軸部
211 外周面部(第1軸部)
22 第2軸部
23 シャフト
3 分級ロータ
31 底面部
32 間隙
33 分級羽根
34 開口部
4 ディップパイプ(絞り部)
41 先端部
5 装置本体
50 ケーシング
51 原料供給部
52 排出部
521 排出流路
53 粗粉排出部
X 軸心
O 開口面
E 通過面
P 原料粉体
a 粗粉
b 微粉
Claims (5)
- 複数の分級羽根を外周部に有する筒体で構成されると共に、前記筒体の軸心に沿った方向の一方の側面に開口する開口部を有する分級ロータと、
前記開口部に設けられ、その内径を小さくする絞り部と、
前記分級ロータを収容して前記軸心周りに回転自在に保持すると共に、分級対象の粉体を外部から導入して前記分級ロータの外周部に供給する装置本体と、
前記分級ロータで分級される粉体を、吸引して前記装置本体の外部に取り出す排出部とを備える分級機であって、
前記絞り部の開口面から前記分級ロータの他方の側面に亘る回転軸部を、前記他方の側面に向かって拡径するように設けた分級機。 - 前記絞り部は、前記分級ロータの開口部から前記分級ロータの内部へ縮径するように形成してある請求項1に記載の分級機。
- 前記分級ロータの内側断面積に対する前記開口面における前記分級される粉体の有効通過断面積の比率は10%以下である請求項1又は2に記載の分級機。
- 前記開口面の断面積に対する前記開口面における前記回転軸部の断面積の比率は30%以上である請求項1から3のいずれか1項に記載の分級機。
- 前記分級ロータは、窒化ケイ素セラミックスから形成される、請求項1から4のいずれか1項に記載の分級機。
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP14888418.2A EP3127621A4 (en) | 2014-03-31 | 2014-03-31 | Classifier |
PCT/JP2014/059519 WO2015151187A1 (ja) | 2014-03-31 | 2014-03-31 | 分級機 |
JP2016511210A JP6328229B2 (ja) | 2014-03-31 | 2014-03-31 | 分級機 |
US15/129,565 US20170136498A1 (en) | 2014-03-31 | 2014-03-31 | Classifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/JP2014/059519 WO2015151187A1 (ja) | 2014-03-31 | 2014-03-31 | 分級機 |
Publications (1)
Publication Number | Publication Date |
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WO2015151187A1 true WO2015151187A1 (ja) | 2015-10-08 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/JP2014/059519 WO2015151187A1 (ja) | 2014-03-31 | 2014-03-31 | 分級機 |
Country Status (4)
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US (1) | US20170136498A1 (ja) |
EP (1) | EP3127621A4 (ja) |
JP (1) | JP6328229B2 (ja) |
WO (1) | WO2015151187A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105880161A (zh) * | 2016-04-07 | 2016-08-24 | 湘潭大学 | 一种超细粉体射流分级提纯方法及装置 |
Families Citing this family (1)
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JP7136192B2 (ja) * | 2018-03-30 | 2022-09-13 | 日本ゼオン株式会社 | 分離回収方法 |
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2014
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- 2014-03-31 WO PCT/JP2014/059519 patent/WO2015151187A1/ja active Application Filing
- 2014-03-31 EP EP14888418.2A patent/EP3127621A4/en not_active Withdrawn
- 2014-03-31 JP JP2016511210A patent/JP6328229B2/ja active Active
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US20170136498A1 (en) | 2017-05-18 |
EP3127621A1 (en) | 2017-02-08 |
EP3127621A4 (en) | 2017-12-06 |
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JPWO2015151187A1 (ja) | 2017-04-13 |
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