JP3625554B2 - Powder classifier - Google Patents

Powder classifier Download PDF

Info

Publication number
JP3625554B2
JP3625554B2 JP34200195A JP34200195A JP3625554B2 JP 3625554 B2 JP3625554 B2 JP 3625554B2 JP 34200195 A JP34200195 A JP 34200195A JP 34200195 A JP34200195 A JP 34200195A JP 3625554 B2 JP3625554 B2 JP 3625554B2
Authority
JP
Japan
Prior art keywords
powder
classification
air
rotor
casing
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
JP34200195A
Other languages
Japanese (ja)
Other versions
JPH09173985A (en
Inventor
幸良 山田
聡 秋山
孝博 市川
英雄 岡部
秀之 飯島
幸雄 岩田
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.)
Nisshin Engineering Co Ltd
Nisshin Seifun Group Inc
Original Assignee
Nisshin Engineering Co Ltd
Nisshin Seifun Group Inc
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 Nisshin Engineering Co Ltd, Nisshin Seifun Group Inc filed Critical Nisshin Engineering Co Ltd
Priority to JP34200195A priority Critical patent/JP3625554B2/en
Publication of JPH09173985A publication Critical patent/JPH09173985A/en
Application granted granted Critical
Publication of JP3625554B2 publication Critical patent/JP3625554B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Description

【0001】
【発明の属する技術分野】
本発明は、回転自在の分級ロータをケーシング内に備えて遠心力と空気流とを利用して粉体を分級する粉体分級機に関し、特に分級ロータの周縁部における粉体の流れを制御し、分級精度の向上と粉体の詰りや固着等を防止した粉体分級機に関する。
【0002】
【従来の技術】
分級ロータを備え分級ロータの回転と空気流とを利用して粉体を分級する粉体分級機の一つに特公平6−61535号公報に示すような分級機が知られている。この分級機は、周囲に分級羽根を多数設けた分級ロータをケーシング内で高速回転させるとともに、分級ロータ内に周辺から中心に向う空気流を形成し、粉体に空気流と回転による遠心力とを作用させて所望の基準値を境に粉体を選り分けている。
【0003】
具体的には、分級ロータの外周部分内部に上述したように複数の分級羽根を備え、かつ内部には空気導入路を形成し、更に分級ロータの上部外周に分級羽根部分に粉体が落下するように粉体導入口を円周に沿って形成し、一方ケーシングには上部中央に粉体を投入する粉体投入口を設け、粉体投入口から投入された粉体が分級ロータの上面で四方に分散されながら粉体導入口から分級ロータ内の分級羽根、すなわち分級室に入るようになっている。そして分級室に入った粉体は、分級羽根によって遠心力を受けるとともに分級ロータの内部方向へ流れる空気流によって周辺から中心に向って運ばれ、空気粘性抵抗の影響を大きく受ける小径の粉体が空気流によって中心部に運ばれ中心部分に設けられた微粉取出口から取り出され、遠心力を大きく受ける大径の粉体が遠心力によって分級ロータ外方に飛ばされ周囲に設けられた粗粉取出口にて収集され、所定の粒径を境にして粉体の分級が行なわれる。
【0004】
【発明が解決しようとする課題】
しかしながら従来の粉体分級機は、投入した粉体が粉体導入口内に全て落下せず分級ロータの外端方向に運ばれることがあった。すると、粉体が分級ロータの外周から分級室に入るため、分級室にて正確に分級がなされず、細かい粉体が粗粉側に含まれたり粗粉が微粉側に分級されるなど分級精度が低下するという問題があった。又、分級ロータとケーシングとの間は元来気密を保つ必要から間隔を狭めてあり、更にラビリンス構造をとっていることから、かかる隙間に粉体が入ると粉体が固まりとなって詰まったり、更に樹脂材等溶融性を有する粉体を分級した場合には、この部分に該粉体が流れこむと分級ロータの回転による摩擦熱で粉体が溶融し隙間に固着して分級ロータの回転不良を発生させることがあった。
【0005】
【課題を解決するための手段】
本発明は上記の課題を解決するため、ケーシング内に垂直回転軸を有する分級ロータを回転自在に備え、該分級ロータの回転による遠心力と該分級ロータ内の空気流とのバランスによって粉体を分級する粉体分級機において、
前記分級ロータは、上下平行に配置されたほぼ同径の2枚の円板間に円周から軸中心方向に空気を流通させる空気流通空胴部を備え、該空気流通空胴部の外周部分に複数の分級羽根を設け、該分級羽根に連通する粉体導入口を前記上部円板に周状に配し、かつ前記ケーシングの上部中央に設けられた粉体投入口より投入した粉体が前記分級ロータの上面にて四方に分散された後、該粉体導入口を通して前記空気流通空洞部に落下するように形成し、
前記ケーシングには、前記粉体導入口と前記分級ロータ外周端との間の円還状の部分の気圧を前記粉体導入口内の気圧より高くする高圧部分を形成して粉体分級機を構成した。したがって、高圧部分、例えば前記ケーシングの内側部に溝を設けて形成した空気導入路に高圧空気を送り、粉体導入口の周囲に空気を吹き出させ気圧を高くすると、粉体は粉体導入口より外方へは運ばれず、ほぼ全ての粉体を粉体導入口内に落下させることができる。
【0006】
又、粉体導入口と該粉体導入口より外方とを区画する仕切板を周状に設けて粉体分級機を構成した。仕切板は、粉体導入口の外周に沿って設け、粉体導入口の開口面積を所定量保持する。これにより、中心部の投入口から投入された粉体は円滑に粉体導入口内に落下する。仕切板はケーシングに取り付け、分級ロータとの間に所定量の隙間を設けることとするが、分級ロータの粉体導入口の外周端に沿って仕切板を設けてもよい。
【0007】
仕切板を前記ケーシングから前記分級ロータに向けて設け、かつ該仕切板の外方にリング状に空気導入路を形成し、該空気導入路に高圧空気を送り、前記粉体導入口より半径方向外周部分の気圧を前記粉体導入口内の気圧より高めることとして粉体分級機を構成した。この空気導入路はロータとの対向面を多孔質の部材とし、該多孔質部材を通して前記ケーシング内に空気を送ることとした。
【0008】
このようにすると、高圧空気を円周に沿って均一に噴出でき、圧力を均等に加えることができる。更に、多孔質の部材でなく、多数のノズルを円周状に配してもよいし、スリット状の隙間をロータ方向へあけて一様に空気を吹き出させてもよい。
【0009】
かかる粉体分級機によれば、粉体投入口から粉体分級機内に粉体が投入されると、分級ロータの上面で粉体が周囲に分散され、分級ロータ上面の粉体導入口から分級ロータ内部に落下する。その際、粉体導入口の外側には仕切板が設けられ、更に仕切板の外周側には空気が送り込まれ粉体導入口内より圧力が高められていることから、粉体が仕切板を越えて外方に運ばれることはあまりなく、分級精度の低下や分級ロータとケーシングとの間での粉体のつまりが発生することがない。
【0010】
【発明の実施の形態】
本発明にかかる粉体分級機の一実施例を図面を用いて説明する。
【0011】
図1は、粉体分級機1の断面図であり、図2は、分級ロータ4の一部を切り欠いた粉体分級機1の平面図である。
【0012】
まず、図1を用いて説明する。
【0013】
分級機1は、ケーシング2とケーシング2内に回転自在に収容された分級ロータ4等からなり、ケーシング2の上面中心部には、粉体供給装置(図示せず)と連結される粉体投入口23が、又側部には空気導入口24が形成してある。ケーシング2は全体が円形で、内部には図3に示すように仕切板5と空気導入路6等が設けられている。
【0014】
仕切板5は、ケーシング2の外周付近に円周状に設けられており、後述する分級ロータ4の粉体導入口10の外側にその先端部が位置している。空気導入路6は、仕切板5の外側に仕切板5と同様に円周状に形成してあり、接続口17を介して空気圧縮機(図示せず)に接続している。更に空気導入路6には、微細な孔を備えた多孔質部材9が下方に取り付けられており、空気圧縮機から送られた空気はこの多孔質部材9を通してケーシング2内に噴出される。
【0015】
分級ロータ4は、2枚の円板(上板4a、下板4b)を上下に組み合わせた形の円盤状で、外周部から軸心部下方に連通する空洞部26を備え、ケーシング2の軸心部に軸受25、25により垂直に取り付けられた回転軸36の上端に固着されている。
【0016】
分級ロータ4の空胴部26内には、図2に示すように外方分級羽根7と内方分級羽根8が放射状に多数円周に沿って等間隔に配列してあり、これらにより分級室11が形成されている。分級ロータ4の上板4aには、外方分級羽根7と内方分級羽根8の間の分級羽根間隙37に対向して分級室11内に連通する粉体導入口10がリング状に形成してある。又分級ロータ4の下板4bの下面には、多数の補助羽根12が放射状に等間隔に配列されており、分級ロータ4が回転したときこの補助羽根12が空気に回転方向の流れを与え、分級室11の方向へ空気を旋回した状態で導入させる。
【0017】
15は分級ロータ4の上板4aとケーシング2の天板間に形成された空所で、粉体投入口23と分級ロータ4の粉体導入口10とを連通させている。この空所15には、分級ロータ4の上板4aの中央部側に軸心部から外周方向に伸びる多数の粉体分散羽根16が放射状に設けられ、そして分散羽根16の半径方向終端と粉体導入口10間の上板4a上を平坦にして、粉体を二次分散させる分散間隙28が連続して形成されている。
【0018】
18は、分級ロータ4とほぼ同様に円周部から軸心部に連通する空洞部27を有する円盤状のバランスロータで、このバランスロータ18は分級ロータ4と上下対称となるように、かつ空胴部27が分級ロータ4の空胴部26と連通するようにしてケーシング2内の回転軸36に一体に固着されている。更に、バランスロータ18の開口周縁部の空胴部27内には多数の羽根20が放射状に設けられ、このバランスロータ18の開口外周囲にはこれを包囲するようにした渦巻きケーシング21がケーシング2に一体かつ気密に取り付けられている。なおこの渦巻きケーシング21には図示しないサイクロン、バッグフィルタなどの捕集装置とファン、ブロワーなどが連結されている。
【0019】
次に、粉体分級機1の作動を説明する。
【0020】
まず、分級ロータ4およびバランスロータ18を図示しない電動機により所定の速度で回転させ、外部に連結されたブロアーの吸引作用で粉体分級機1の内部に空気流を生じさせる。これによりケーシング2の空気導入口24から流入された空気は補助羽根12によって回転方向の流れに変換され、旋回した状態で分級室11に入り、分級室11で分級羽根7、8により分級ロータ4の放射方向の気流となり、そしてバランスロータ18を通過した空気は渦巻きケーシング21を介してサイクロンに流入する。又、空気圧縮機を作動させ、空気導入路6に空気を送り込む。
【0021】
この状態で分級しようとする粉体を粉体投入口23から投入すると、粉体は粉体投入口23からの空気流に乗り、分散羽根16間を通過する間に分級ロータ4の軸心を中心とする放射方向にほぼ均一に分割され、粉体の一次分散が行われる。そして分散羽根16の終端から出た粉体は分級ロータ4の回転に伴い分散羽根16の配列円のほぼ放射方向に放射され、分散間隙28内で二次分散される。
【0022】
十分に分散された粉体は分級ロータ4の外周部にリング状に設けられた粉体導入口10から分級室11に落下する。その際、仕切板5が粉体導入口10の外方に周状に形成されていることから、粉体は粉体導入口10に落下し、更に空気導入路6から噴出する空気によって、粉体導入口10の外周側の気圧が高められていることから、粉体が仕切板5を越えて分級ロータ4の外周端に運ばれることはない。したがって、粉体が分級ロータ4の外周端でケーシング2との狭い隙間に入り込むことがなく、分級精度の低下や固着等を発生させることがない。
【0023】
そして、分級室11に落下した粉体の各粒子は分級ロータ4の回転による遠心力と軸心方向への空気の流れによる抗力を受け、遠心力<抗力の関係が成り立つ細かい粒子は半径方向の空気流に乗った状態でバランスロータ18、渦巻きケーシング21を介して粉体分級機1の外に空気輸送され、サイクロン、バッグフィルタなどの捕集機により捕集される。一方、遠心力>抗力の関係が成り立つ粗い粒子は分級ロータ4の外周に飛ばされ、粗粉取出口14よりロータリーバルブなどを用いてエアシールした状態で粉体分級機1の外部に取り出される。
【0024】
【実施例】
次に、本発明にかかる粉体分級機1の実験例について説明する。
【0025】
実験に用いた分級機は、分級ロータの外径が15cmで、分級ロータの回転数は10000rpm、ブロアーの風量は2.5m/min であり、空気導入路には多孔質の燒結金属を用いた。
【0026】
分級した粉体は、中位径が5μmのエポキシ系粉体塗料で、時間当たりの供給量は1.0kg/h、1.7kg/h、2.5kg/h、3.1kg/hとした。
【0027】
又空気圧縮機からの送風は、空気圧を0kgf/cm(流速0m/min)、0.5kgf/cm(流速0.20m/min)、1.0kgf/cm(流速0.41m/min)、2kgf/cm(流速0.83m/min)、3kgf/cm(流速1.23m/min)、4kgf/cm(流速1.64m/min)、5kgf/cm(流速2.05m/min)、とし、各条件において10分間分級を行なった。
【0028】
結果を図4に示す。この結果から、従来の空気圧0kgf/cmでは粉体の融着により分級動作の停止が発生していたが、空気導入路に空気を送り込んだときは空気圧力0.5kgf/cmの場合を除き融着の発生は見られなかった。更に、図5に示すように分級精度kは、0.5kgf/cm〜1.0kgf/cmの間で向上し、良好な結果を得ることができた。尚、分級精度指数は、部分分級効率25%に相当する粒径DP25と部分分級効率75%に相当する粒径DP75の比、すなわちDP25/ DP75であり、1に近い程精度が良いことを表す指数である。
【0029】
【発明の効果】
本発明によれば、粉体導入口の外周側の気圧を粉体導入口より高くし、しかも粉体導入口の外側に仕切板を設けたので、粉体投入口に投入された粉体が粉体導入口の外周側に運ばれることがなく粉体導入口の内部に全ての粉体が落下し、分級精度が低下したり、ケーシングと分級ロータの隙間において粉体が固着したりする等の不都合が発生しない。
【図面の簡単な説明】
【図1】本発明による粉体分級機の縦断面図である。
【図2】図1に示した粉体分級機の一部を切り欠いて示す平面図である。
【図3】本発明による粉体分級機の部分拡大断面図である。
【図4】実験結果を示すグラフである。
【図5】実験結果を示すグラフである。
【符号の説明】
1 粉体分級機
2 ケーシング
4 分級ロータ
5 仕切板
6 空気導入路
7 外方分級羽根
8 内方分級羽根
9 多孔質部材
10 粉体導入口
11 分級室
12 補助羽根
14 粗粉取出口
15 空所
16 分散羽根
17 接続口
18 バランスロータ
20 羽根
21 渦巻ケーシング
23 粉体投入口
24 空気導入口
25 軸受
26、27 空洞部
28 分散間隙
36 回転軸
37 分級羽根間隙
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a powder classifier that includes a rotatable classification rotor in a casing and classifies powder using centrifugal force and air flow, and in particular, controls the flow of powder at the periphery of the classification rotor. The present invention relates to a powder classifier that improves classification accuracy and prevents powder clogging and sticking.
[0002]
[Prior art]
A classifier as disclosed in Japanese Patent Publication No. 6-61535 is known as one of powder classifiers that include a classifying rotor and classify powder using the rotation of the classifying rotor and air flow. This classifier rotates a classification rotor provided with a large number of classification blades around it at high speed in the casing, forms an air flow from the periphery to the center in the classification rotor, and generates an air flow and rotational centrifugal force on the powder. Is used to select powders at the desired reference value.
[0003]
Specifically, as described above, a plurality of classification blades are provided inside the outer peripheral portion of the classification rotor, an air introduction path is formed inside, and the powder falls on the classification blade portion on the upper outer periphery of the classification rotor. The powder inlet is formed along the circumference, while the casing is provided with a powder inlet at the center of the upper part, and the powder introduced from the powder inlet is placed on the upper surface of the classification rotor. While being dispersed in all directions, the powder enters the classification blade in the classification rotor, that is, the classification chamber from the powder inlet. The powder entering the classification chamber is subjected to centrifugal force by the classification blades and is carried from the periphery to the center by the air flow flowing in the internal direction of the classification rotor. Coarse powder collection that is carried to the center by the air flow and taken out from the fine powder extraction outlet provided in the central part, and is blown out of the classification rotor by centrifugal force, and receives large centrifugal force. The powder is collected at the outlet, and the powder is classified at a predetermined particle size.
[0004]
[Problems to be solved by the invention]
However, in the conventional powder classifier, all of the charged powder does not fall into the powder inlet, and is sometimes conveyed toward the outer end of the classification rotor. Then, since the powder enters the classification chamber from the outer periphery of the classification rotor, classification is not performed accurately in the classification chamber, and classification accuracy such as fine powder is included on the coarse powder side or coarse powder is classified on the fine powder side. There was a problem that decreased. In addition, the gap between the classification rotor and the casing is originally narrow because it is necessary to maintain airtightness, and since a labyrinth structure is adopted, if powder enters this gap, the powder becomes hard and clogs. Furthermore, when a powder having melting properties such as a resin material is classified, if the powder flows into this part, the powder is melted by frictional heat due to the rotation of the classification rotor and fixed in the gap, and the rotation of the classification rotor is performed. Defects may occur.
[0005]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the present invention is provided with a classification rotor having a vertical rotation shaft in a casing so as to be rotatable, and powder is distributed by balancing the centrifugal force generated by the rotation of the classification rotor and the air flow in the classification rotor. In the powder classifier that classifies,
The classification rotor includes an air circulation cavity that circulates air from the circumference toward the axial center between two disks having substantially the same diameter arranged in parallel in the vertical direction, and an outer peripheral portion of the air circulation cavity A plurality of classification blades are provided, a powder introduction port communicating with the classification blades is arranged circumferentially on the upper disk, and the powder charged from the powder injection port provided in the upper center of the casing is After being dispersed in all directions on the upper surface of the classification rotor, it is formed so as to fall into the air circulation cavity through the powder inlet,
The casing is configured with a high-pressure portion in which a pressure in a return-shaped portion between the powder inlet and the outer peripheral end of the classification rotor is made higher than an air pressure in the powder inlet. did. Therefore, when high pressure air is sent to an air introduction path formed by providing a groove in the high pressure portion, for example, the inner portion of the casing, and air is blown out around the powder introduction port to increase the atmospheric pressure, the powder becomes the powder introduction port. Almost all the powder can be dropped into the powder introduction port without being conveyed outward.
[0006]
Further, a powder classifier was configured by providing a powder introduction port and a partition plate that divides the outside from the powder introduction port in a circumferential shape. The partition plate is provided along the outer periphery of the powder inlet and holds a predetermined amount of the opening area of the powder inlet. As a result, the powder charged from the central inlet smoothly falls into the powder inlet. The partition plate is attached to the casing, and a predetermined amount of clearance is provided between the partition plate and the classification rotor. However, the partition plate may be provided along the outer peripheral end of the powder inlet of the classification rotor.
[0007]
A partition plate is provided from the casing toward the classification rotor, and an air introduction path is formed in a ring shape outside the partition plate, high-pressure air is sent to the air introduction path, and the radial direction from the powder introduction port A powder classifier was constructed by increasing the air pressure in the outer peripheral portion above the air pressure in the powder inlet. The air introduction path has a surface facing the rotor as a porous member, and air is sent into the casing through the porous member.
[0008]
If it does in this way, high pressure air can be ejected uniformly along a circumference, and pressure can be applied uniformly. Furthermore, instead of a porous member, a large number of nozzles may be arranged circumferentially, or a slit-like gap may be opened in the direction of the rotor to uniformly blow out air.
[0009]
According to such a powder classifier, when powder is introduced into the powder classifier from the powder inlet, the powder is dispersed around the upper surface of the classification rotor and classified from the powder inlet on the upper surface of the classification rotor. It falls into the rotor. At that time, a partition plate is provided outside the powder inlet, and air is sent to the outer periphery of the partition plate to increase the pressure from the inside of the powder inlet. Therefore, the classification accuracy is not lowered and powder clogging between the classification rotor and the casing does not occur.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
An embodiment of a powder classifier according to the present invention will be described with reference to the drawings.
[0011]
FIG. 1 is a cross-sectional view of the powder classifier 1, and FIG. 2 is a plan view of the powder classifier 1 with a part of the classifying rotor 4 cut away.
[0012]
First, it demonstrates using FIG.
[0013]
The classifier 1 includes a casing 2 and a classifying rotor 4 housed in the casing 2 so as to be rotatable. A powder supply device connected to a powder supply device (not shown) is connected to the center of the upper surface of the casing 2. An opening 23 is formed on the side and an air inlet 24 is formed on the side. The casing 2 has a circular shape as a whole, and a partition plate 5, an air introduction path 6 and the like are provided therein as shown in FIG.
[0014]
The partition plate 5 is provided in a circumferential shape near the outer periphery of the casing 2, and a tip portion thereof is located outside a powder introduction port 10 of the classification rotor 4 described later. The air introduction path 6 is formed on the outer side of the partition plate 5 in the same manner as the partition plate 5 and is connected to an air compressor (not shown) via the connection port 17. Further, a porous member 9 having fine holes is attached below the air introduction path 6, and the air sent from the air compressor is jetted into the casing 2 through the porous member 9.
[0015]
The classifying rotor 4 has a disk shape in which two disks (upper plate 4a and lower plate 4b) are vertically combined, and includes a hollow portion 26 that communicates from the outer peripheral portion to the lower portion of the axial center. It is fixed to the upper end of a rotary shaft 36 that is vertically attached to the center by bearings 25 and 25.
[0016]
In the cavity portion 26 of the classification rotor 4, as shown in FIG. 2, the outer classification blades 7 and the inner classification blades 8 are radially arranged at equal intervals along the circumference. 11 is formed. In the upper plate 4a of the classification rotor 4, a powder inlet 10 that communicates with the classification chamber 11 is formed in a ring shape so as to face the classification blade gap 37 between the outer classification blade 7 and the inner classification blade 8. It is. A large number of auxiliary blades 12 are radially arranged at equal intervals on the lower surface of the lower plate 4b of the classifying rotor 4. When the classifying rotor 4 rotates, the auxiliary blades 12 give the air a flow in the rotational direction. Air is introduced in the state of swirling air toward the classification chamber 11.
[0017]
Reference numeral 15 denotes a space formed between the upper plate 4 a of the classification rotor 4 and the top plate of the casing 2, and communicates the powder inlet 23 with the powder inlet 10 of the classification rotor 4. In this void 15, a large number of powder dispersion blades 16 extending radially from the axial center to the center of the upper plate 4 a of the classification rotor 4 are provided radially, and the radial ends of the dispersion blades 16 and the powder The upper plate 4a between the body inlets 10 is flattened to continuously form a dispersion gap 28 for secondary dispersion of the powder.
[0018]
18 is a disk-shaped balance rotor having a hollow portion 27 that communicates from the circumferential portion to the shaft center portion in substantially the same manner as the classification rotor 4. The balance rotor 18 is symmetric with respect to the classification rotor 4 and is empty. The body 27 is integrally fixed to the rotary shaft 36 in the casing 2 so as to communicate with the cavity 26 of the classifying rotor 4. Further, a large number of blades 20 are provided radially in the cavity portion 27 at the peripheral edge of the opening of the balance rotor 18, and a spiral casing 21 surrounding the balance rotor 18 is provided around the outer periphery of the opening of the balance rotor 18. It is attached to the unit in an airtight manner. The spiral casing 21 is connected to a collecting device such as a cyclone and a bag filter (not shown), a fan, a blower, and the like.
[0019]
Next, the operation of the powder classifier 1 will be described.
[0020]
First, the classifying rotor 4 and the balance rotor 18 are rotated at a predetermined speed by an electric motor (not shown), and an air flow is generated inside the powder classifier 1 by the suction action of a blower connected to the outside. As a result, the air flowing in from the air inlet 24 of the casing 2 is converted into a flow in the rotational direction by the auxiliary blades 12, enters the classification chamber 11 in a swirled state, and in the classification chamber 11 by the classification blades 7 and 8, the classification rotor 4. The air passing through the balance rotor 18 flows into the cyclone via the spiral casing 21. Further, the air compressor is operated to send air into the air introduction path 6.
[0021]
When the powder to be classified in this state is charged from the powder inlet 23, the powder rides on the air flow from the powder inlet 23 and moves the axis of the classification rotor 4 while passing between the dispersion blades 16. The powder is divided almost uniformly in the center radial direction, and primary dispersion of the powder is performed. The powder coming out from the end of the dispersion blade 16 is radiated almost in the radial direction of the array circle of the dispersion blades 16 as the classification rotor 4 rotates, and is secondarily dispersed in the dispersion gap 28.
[0022]
The sufficiently dispersed powder falls into the classification chamber 11 from the powder inlet 10 provided in a ring shape on the outer periphery of the classification rotor 4. At that time, since the partition plate 5 is formed in a circumferential shape outside the powder inlet 10, the powder falls into the powder inlet 10 and is further blown out by the air blown out from the air introduction path 6. Since the air pressure on the outer peripheral side of the body introduction port 10 is increased, the powder does not go over the partition plate 5 to the outer peripheral end of the classification rotor 4. Therefore, the powder does not enter a narrow gap with the casing 2 at the outer peripheral end of the classification rotor 4, so that the classification accuracy is not deteriorated or fixed.
[0023]
Each particle of the powder falling into the classification chamber 11 is subjected to a centrifugal force due to the rotation of the classification rotor 4 and a drag due to the air flow in the axial direction, and fine particles satisfying the relationship of centrifugal force <drag are in the radial direction. The air is transported to the outside of the powder classifier 1 through the balance rotor 18 and the spiral casing 21 while being in an air flow, and is collected by a collector such as a cyclone or a bag filter. On the other hand, coarse particles satisfying the relationship of centrifugal force> drag are blown to the outer periphery of the classification rotor 4 and are taken out of the powder classifier 1 from the coarse powder outlet 14 in an air-sealed state using a rotary valve or the like.
[0024]
【Example】
Next, an experimental example of the powder classifier 1 according to the present invention will be described.
[0025]
The classifier used in the experiment has an outer diameter of the classification rotor of 15 cm, the rotation speed of the classification rotor is 10,000 rpm, the air volume of the blower is 2.5 m 3 / min, and a porous sintered metal is used for the air introduction path. It was.
[0026]
The classified powder was an epoxy-based powder paint having a median diameter of 5 μm, and the supply amount per hour was 1.0 kg / h, 1.7 kg / h, 2.5 kg / h, 3.1 kg / h. .
[0027]
The air sent from the air compressor, the air pressure 0 kgf / cm 2 (flow rate 0m 3 /min),0.5kgf/cm 2 (flow rate 0.20m 3 /min),1.0kgf/cm 2 (flow rate 0.41m 3 / min), 2 kgf / cm 2 (flow rate 0.83 m 3 / min), 3 kgf / cm 2 (flow rate 1.23 m 3 / min), 4 kgf / cm 2 (flow rate 1.64 m 3 / min), 5 kgf / cm 2 (flow rate 2.05 m 3 / min), and classification was performed for 10 minutes under each condition.
[0028]
The results are shown in FIG. From this result, although the classification operation stopped due to powder fusion at the conventional air pressure of 0 kgf / cm 2 , the case where the air pressure was 0.5 kgf / cm 2 when the air was fed into the air introduction path. Except for the fusion, there was no occurrence. Furthermore, classification accuracy k as shown in Figure 5, improves between 0.5kgf / cm 2 ~1.0kgf / cm 2 , it was possible to obtain good results. The classification accuracy index is a ratio of the particle size DP 25 corresponding to the partial classification efficiency of 25% to the particle size DP 75 corresponding to the partial classification efficiency of 75%, that is, DP 25 / DP 75. An index that represents good things.
[0029]
【The invention's effect】
According to the present invention, since the air pressure on the outer peripheral side of the powder inlet is higher than that of the powder inlet, and the partition plate is provided outside the powder inlet, the powder introduced into the powder inlet is Without being carried to the outer periphery of the powder inlet, all powder falls into the powder inlet and the classification accuracy is lowered, or the powder is fixed in the gap between the casing and the classification rotor, etc. Inconvenience does not occur.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of a powder classifier according to the present invention.
FIG. 2 is a plan view showing a part of the powder classifier shown in FIG.
FIG. 3 is a partially enlarged cross-sectional view of a powder classifier according to the present invention.
FIG. 4 is a graph showing experimental results.
FIG. 5 is a graph showing experimental results.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Powder classifier 2 Casing 4 Classification rotor 5 Partition plate 6 Air introduction path 7 Outer classification blade 8 Inner classification blade 9 Porous member 10 Powder inlet 11 Classification chamber 12 Auxiliary blade 14 Coarse powder outlet 15 Space 16 Dispersion blade 17 Connection port 18 Balance rotor 20 Blade 21 Spiral casing 23 Powder inlet 24 Air introduction port 25 Bearings 26 and 27 Cavity 28 Dispersion gap 36 Rotating shaft 37 Classification blade gap

Claims (4)

ケーシング内に垂直回転軸を有する分級ロータを回転自在に備え、該分級ロータの回転による遠心力と該分級ロータ内の空気流とのバランスによって粉体を分級する粉体分級機において、
前記分級ロータは、上下平行に配置されたほぼ同径の2枚の円板間に円周から軸中心方向に空気を流通させる空気流通空胴部を備え、該空気流通空胴部の外周部分に複数の分級羽根を設け、該分級羽根に連通する粉体導入口を前記上部円板に周状に、かつ前記ケーシングの上部中央に設けられた粉体投入口より投入した粉体が前記分級ロータの上面にて四方に分散された後、該粉体導入口を通して前記空気流通空胴部に落下するように形成し、
前記ケーシングには、前記粉体導入口と前記分級ロータ外周端との間の円環状の部分の気圧を前記粉体導入口の気圧より高くする高圧部分を形成したことを特徴とする粉体分級機。
In a powder classifier that comprises a classification rotor having a vertical rotating shaft in a casing so as to be rotatable, and classifies powder by balancing the centrifugal force generated by the rotation of the classification rotor and the air flow in the classification rotor.
The classification rotor includes an air circulation cavity that circulates air from the circumference toward the axial center between two disks having substantially the same diameter arranged in parallel in the vertical direction, and an outer peripheral portion of the air circulation cavity A plurality of classification blades are provided in the powder, and a powder introduction port communicating with the classification blades is circumferentially formed in the upper disk, and a powder charged from a powder injection port provided at an upper center of the casing is the classification. After being dispersed in all directions on the upper surface of the rotor, it is formed so as to fall into the air circulation cavity through the powder inlet,
The powder classification is characterized in that the casing is formed with a high-pressure portion that makes the pressure of the annular portion between the powder inlet and the outer peripheral end of the classification rotor higher than the pressure of the powder inlet. Machine.
前記粉体導入口と該粉体導入口より外方とを区画する仕切り板を、前記ケーシング上部から前記分級ロータに向けて延在するように、かつ周状に設けたことを特徴とする請求項1に記載の粉体分級機。A partition plate that partitions the powder introduction port and the outside from the powder introduction port is provided so as to extend from the upper part of the casing toward the classification rotor and in a circumferential shape. Item 2. A powder classifier according to Item 1. 前記ケーシングの上部で、前記仕切り板の外方に空気導入路を形成し、該空気導入路に高圧空気を送り、前記粉体導入口と前記分級ロータ外周端との間の円環状の部分の気圧を前記粉体導入口の気圧よりも高めたことを特徴とする請求項1または2に記載の粉体分級機。 An air introduction path is formed on the outside of the partition plate at the upper part of the casing , high-pressure air is sent to the air introduction path, and an annular portion between the powder introduction port and the classification rotor outer peripheral end is formed . The powder classifier according to claim 1 or 2 , wherein the air pressure is higher than the air pressure at the powder inlet. 前記空気導入路に多孔質の部材を設け、該多孔質部材を通して前記ケーシング内に空気を送ることを特徴とする請求項1〜3のいずれか1項に記載の粉体分級機。The powder classifier according to any one of claims 1 to 3, wherein a porous member is provided in the air introduction path, and air is sent into the casing through the porous member.
JP34200195A 1995-12-28 1995-12-28 Powder classifier Expired - Fee Related JP3625554B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34200195A JP3625554B2 (en) 1995-12-28 1995-12-28 Powder classifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34200195A JP3625554B2 (en) 1995-12-28 1995-12-28 Powder classifier

Publications (2)

Publication Number Publication Date
JPH09173985A JPH09173985A (en) 1997-07-08
JP3625554B2 true JP3625554B2 (en) 2005-03-02

Family

ID=18350413

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34200195A Expired - Fee Related JP3625554B2 (en) 1995-12-28 1995-12-28 Powder classifier

Country Status (1)

Country Link
JP (1) JP3625554B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6506940B2 (en) * 2014-10-15 2019-04-24 株式会社アドマテックス Method of producing inorganic filler, method of producing resin composition, and method of producing molded article

Also Published As

Publication number Publication date
JPH09173985A (en) 1997-07-08

Similar Documents

Publication Publication Date Title
JP2575961B2 (en) Pneumatic centrifuge
KR101263541B1 (en) Powder classifying device
US6276534B1 (en) Classifier apparatus for particulate matter/powder classifier
EP0159766B1 (en) Particulate classifying apparatus
GB1154358A (en) Improvements in or relating to methods of and apparatus for the Classification of Materials
JP3625554B2 (en) Powder classifier
JP2792576B2 (en) Vertical crusher
JPS594477A (en) Powder classifier
US4409097A (en) Improved pivotable centrifugal classifier and method of classifying
US4390419A (en) Centrifugal classifier
JPH105696A (en) Powder classifier
JP2007117825A (en) Classifier
JP2597794B2 (en) Method and apparatus for classifying powder raw materials
JP3515089B2 (en) Airflow classifier
JP3999497B2 (en) Powder classifier
JP3388610B2 (en) Powder classifier
JPS6024477Y2 (en) Classifier for powder and granular materials
JP3632425B2 (en) Airflow classifier
US4728047A (en) Separator-disintegrator
JP2617832B2 (en) Vertical crusher
JP3485624B2 (en) Powder classifier and its operation method
JP3733349B2 (en) Airflow classifier
JP2017159215A (en) Pulverization device with classification function
KR940002840B1 (en) Powdered-body sorter
JP2839117B2 (en) Vertical crusher

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040630

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040907

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20041018

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20041124

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20041130

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071210

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081210

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081210

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091210

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101210

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111210

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121210

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131210

Year of fee payment: 9

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees