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JPS6347515B2 - - Google Patents
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JPS6347515B2 - - Google Patents

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Publication number
JPS6347515B2
JPS6347515B2 JP3607985A JP3607985A JPS6347515B2 JP S6347515 B2 JPS6347515 B2 JP S6347515B2 JP 3607985 A JP3607985 A JP 3607985A JP 3607985 A JP3607985 A JP 3607985A JP S6347515 B2 JPS6347515 B2 JP S6347515B2
Authority
JP
Japan
Prior art keywords
classification
rotor
classification chamber
passage
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.)
Expired
Application number
JP3607985A
Other languages
Japanese (ja)
Other versions
JPS61197083A (en
Inventor
Katsuya Mizui
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.)
HOSOKAWA MIKURON KK
Original Assignee
HOSOKAWA MIKURON KK
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 HOSOKAWA MIKURON KK filed Critical HOSOKAWA MIKURON KK
Priority to JP3607985A priority Critical patent/JPS61197083A/en
Publication of JPS61197083A publication Critical patent/JPS61197083A/en
Publication of JPS6347515B2 publication Critical patent/JPS6347515B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、周部に分級ブレードを並設したロー
タをケース内に縦軸芯周りで駆動回転自在に設
け、分級ブレード間の隙間に連通する微粉粒通路
をロータ内に形成し、分級ブレードの外周部に形
成した環状の分級室に連通する原料供給口、粗粉
粒排出口及び選別風供給口と、微粉粒通路に連通
する微粉粒排出口とをケースに形成し、分級室内
において、ロータと分級ブレードの作用で原料を
回動させ、遠心力の小さい微粉粒を選別風で微粉
粒通路から微粉粒排出口に送り、遠心力の大きい
粗粉粒を選別風とは逆行させて粗粉粒排出口側に
送るように構成した粉粒体用分級機に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a rotor with classification blades arranged side by side on its periphery, which is provided in a case so as to be rotatable around a vertical axis, and which communicates with the gaps between the classification blades. A fine powder passage is formed in the rotor, and a raw material supply port, a coarse powder discharge port, and a sorting air supply port are connected to an annular classification chamber formed on the outer periphery of the classification blade, and a fine powder passage is connected to the fine powder passage. A discharge port is formed in the case, and in the classification chamber, the raw material is rotated by the action of the rotor and the classification blade, and the fine particles with a small centrifugal force are sent from the fine particle passage to the fine particle discharge port with a sorting wind, and the centrifugal force is The present invention relates to a classifier for powder and granular materials configured to send large coarse particles to a coarse powder discharge port in a direction opposite to a sorting wind.

〔従来の技術〕[Conventional technology]

従来、第3図に示すように、環状の分級室7を
単純な一室構成に形成し、原料供給口10からの
原料を通路11によつて分級室7に送り、選別風
供給口17からの風を通路18によつて分級室7
に送り、ロータ2の周部に設けた分級ブレード4
を通過した微粉粒を微粉粒通路5から微粉粒排出
口14に送り、分級室7の外周側に移動した粗粉
粒を粗粉粒排出口21に送るように構成していた
(例えば特公昭57−11269号公報)。
Conventionally, as shown in FIG. 3, the annular classification chamber 7 is formed into a simple one-room configuration, and the raw material from the raw material supply port 10 is sent to the classification chamber 7 through the passage 11, and the raw material is sent from the sorting air supply port 17 to the classification chamber 7. The wind is passed through the classification room 7 through the passage 18.
The classification blade 4 provided on the periphery of the rotor 2
The structure is such that the fine particles that have passed through are sent from the fine particle passage 5 to the fine particle outlet 14, and the coarse particles that have moved to the outer circumferential side of the classification chamber 7 are sent to the coarse particle outlet 21 (for example, 57-11269).

〔考案が解決しようとする問題点〕[Problem that the invention attempts to solve]

しかし、通路11から分級室7に供給される原
料の分散状態が不十分になると、微粉粒の一部が
粗粉粒排出口21に流入しやすく、分級効率が低
下しやすい欠点があつた。
However, if the dispersion of the raw material supplied from the passage 11 to the classification chamber 7 becomes insufficient, a portion of the fine particles tends to flow into the coarse particle outlet 21, resulting in a disadvantage that the classification efficiency tends to decrease.

本発明の目的は、簡単な改造でもつて、分級効
率を十分にかつ確実に向上できるようにする点に
ある。
An object of the present invention is to make it possible to sufficiently and reliably improve classification efficiency even with simple modification.

〔問題点を解決するための手段〕[Means for solving problems]

本発明の特徴構成は、ロータの周部に形成した
環状の分級室を、ロータの周部で微粉粒通路の入
口に設けた分級ブレード側の主分級室と粗粉粒排
出口及び選別風供給口が連通する再分級室とに区
画する筒状隔壁を、ロータとほぼ同芯状に配置
し、再分級室から主分級室に選別風及び微粉粒を
送る開口を、筒状隔壁にその全周にわたつて配置
して形成し、筒状隔壁の下端部とロータとの間
に、主分級室から再分級室に粗粉粒を送る通路を
形成し、その通路からの粗粉粒を再分級室内に分
散供給する分散ベーンをロータに設けたことにあ
り、その作用効果は次の通りである。
The characteristic configuration of the present invention is that an annular classification chamber is formed on the circumference of the rotor, a main classification chamber is provided on the classification blade side at the entrance of a fine powder passage on the circumference of the rotor, a coarse powder discharge port is provided, and a sorting air supply is provided. A cylindrical partition wall that divides the re-classification chamber into a re-classification chamber with an opening communicating with the rotor is placed almost concentrically with the rotor, and an opening for sending sorting air and fine particles from the re-classification chamber to the main classification chamber is placed in the cylindrical partition wall over its entire length. A passage is formed between the lower end of the cylindrical partition wall and the rotor to send coarse particles from the main classification chamber to the re-classification chamber, and the coarse particles from the passage are recycled. The rotor is provided with a dispersion vane that distributes supply into the classification chamber, and its effects are as follows.

〔作用〕[Effect]

つまり、粗粉粒は、主分級室内において遠心力
で筒状隔壁側に移動して重力で下降し、筒状隔壁
下端側の通路から再分級室に遠心力で送られ、分
散ベーンにより再分散させて再分級室に供給さ
れ、再び遠心力と選別風との協働により分級処理
される。
In other words, in the main classification chamber, the coarse powder particles are moved toward the cylindrical partition by centrifugal force, descend by gravity, are sent by centrifugal force to the re-classification chamber from the passage on the lower end of the cylindrical partition, and are redispersed by the dispersion vanes. Then, it is supplied to the re-classification room, where it is classified again by the cooperation of centrifugal force and sorting air.

したがつて、主分級室での分級において粗粉粒
中に微粉粒が混入しても、再分級室で粗粉粒と微
粉粒とが選別され、微粉粒は選別風によつて筒状
隔壁の開口から主分級室に戻され、粗粉粒排出口
に微粉粒が送られることを十分に阻止できる。
Therefore, even if fine particles are mixed into coarse particles during classification in the main classification chamber, the coarse particles and fine particles are separated in the re-classification chamber, and the fine particles are separated from the cylindrical partition by the sorting air. It is possible to sufficiently prevent fine particles from being returned to the main classification chamber through the opening and sent to the coarse particle outlet.

〔発明の効果〕〔Effect of the invention〕

その結果、粗粉粒中への微粉粒混入を十分かつ
確実に防止でき、分級効率が極めて高い優秀な分
級機を提供できるようになつた。
As a result, it has become possible to sufficiently and reliably prevent the mixing of fine particles into coarse particles, and to provide an excellent classifier with extremely high classification efficiency.

その上、単に筒状隔壁と分散ベーンを付加する
だけの単純な改造で済み、製作面及びコスト面に
おいても有利に分級性能向上を図れた。
In addition, the modification required was simple by simply adding a cylindrical partition wall and a dispersion vane, and the classification performance was advantageously improved in terms of manufacturing and cost.

〔実施例〕〔Example〕

次に、第1図及び第2図により実施例を示す。 Next, an example will be shown with reference to FIGS. 1 and 2.

原動機に連動する回転軸1にロータ2を取付け
て、ロータ2を縦軸芯周りで駆動回転自在にケー
ス3内に設け、多数の分級ブレード4をロータ2
の周部に並設し、分級ブレード4間の隙間に連通
する微粉粒通路5をロータ2内に形成し、その通
路5に吐出用ブレード6を設けてある。
A rotor 2 is attached to a rotating shaft 1 that is linked to a prime mover, and the rotor 2 is provided in a case 3 so as to be freely rotatable around the vertical axis, and a large number of classification blades 4 are attached to the rotor 2.
A fine particle passage 5 is formed in the rotor 2 and is arranged in parallel around the circumference of the rotor 2 and communicates with the gap between the classification blades 4. A discharge blade 6 is provided in the passage 5.

環状の分級室7a,7bを分級ブレード4の外
周部に形成し、その分級室7a,7bを区画する
筒状隔壁8をロータ2とほぼ同芯状に設けて、分
級ブレード4側の主分級室7aとその外側の再分
級室7bをいずれも環状にして形成してある。
Annular classification chambers 7a and 7b are formed on the outer periphery of the classification blade 4, and a cylindrical partition wall 8 that partitions the classification chambers 7a and 7b is provided approximately concentrically with the rotor 2, so that the main classification on the classification blade 4 side Both the chamber 7a and the reclassification chamber 7b outside thereof are formed into an annular shape.

空気輸送されてくる原料を、ロータ2の上部中
心に形成したガイドコーン9に向けて供給する原
料供給口10をケース3に形成し、原料供給口1
0と主分級室7aを連通する通路11の終端側
に、ロータ2の全周に分散付設した分散ベーン1
2を配置し、もつて、原料を主分級室7aの上部
に旋回させながら、かつ、分散して均等に供給す
るように構成してある。
A raw material supply port 10 is formed in the case 3 to supply the pneumatically transported raw material toward a guide cone 9 formed at the center of the upper part of the rotor 2.
Dispersion vanes 1 are distributed around the entire circumference of the rotor 2 on the terminal end side of a passage 11 that communicates with the main classification chamber 7a.
2 are arranged so that the raw material is swirled to the upper part of the main classification chamber 7a and is evenly supplied in a distributed manner.

微粉粒通路5に連通する環状路13と微粉粒排
出口14をケース3に形成し、筒状隔壁8の下端
部とロータ2の間に、主分級室7aから再分級室
7bに粗粉粒を送る通路15を形成し、その通路
15からの粗粉粒を再分級室7bに分散供給する
分散ベーン16を、ロータ2にその全周にわたつ
て分散して付設し、再分級室7bに選別風を供給
する選別風供給口17と環状路18をケース3に
形成し、再分級室7bに選別風を圧送する送風ベ
ーン19を、ロータ2に全周にわたつて分散して
付設し、再分級室7bと主分級室7aを連通する
開口20を、筒状隔壁8にその全周にわたつて分
散させて、かつ、主分級室7a内で選別風がロー
タ2の回転方向に旋回するように方向づけて形成
し、再分級室7bに連通する粗粉粒排出口21を
ケース3に形成してある。
An annular passage 13 communicating with the fine powder passage 5 and a fine powder discharge port 14 are formed in the case 3, and coarse powder is transferred from the main classification chamber 7a to the reclassification chamber 7b between the lower end of the cylindrical partition wall 8 and the rotor 2. Dispersion vanes 16 are attached to the rotor 2 to form a feeding passage 15 and distribute the coarse particles from the passage 15 to the re-classification chamber 7b, and are distributed over the entire circumference of the rotor 2. A sorting air supply port 17 and annular passage 18 for supplying sorting air are formed in the case 3, and blower vanes 19 for forcefully feeding the sorting air to the reclassification chamber 7b are attached to the rotor 2 in a distributed manner over the entire circumference, Openings 20 communicating the re-classification chamber 7b and the main classification chamber 7a are distributed over the entire circumference of the cylindrical partition wall 8, and the sorting air swirls in the rotation direction of the rotor 2 within the main classification chamber 7a. A coarse powder discharge port 21 is formed in the case 3 so as to be oriented as shown in FIG.

つまり、主分級室7aにおいて、原料の旋回に
よる遠心力とそれとは逆向きに作用する選別風と
の協働で、微粒子と粗粒子を分け、微粒子を選別
風により通路5から微粉粒排出口14に送るよう
に構成してある。そして、主分級室7a内の粗粉
粒を筒状隔壁8下方の通路15から再分級室7b
に分散ベーン16で再分散させて、かつ、旋回さ
せて送り、再分級室7bにおいて、遠心力と選別
風の協働で混入した微粉粒を粗粉粒から分け、粗
粉粒を粗粉粒排出口21に、かつ、微粉粒を選別
風により開口20から主分級室7aに送るように
構成してある。
That is, in the main classification chamber 7a, fine particles and coarse particles are separated by the cooperation of the centrifugal force caused by the rotation of the raw material and the sorting wind that acts in the opposite direction. It is configured to send to. Then, the coarse powder particles in the main classification chamber 7a are transferred from the passage 15 below the cylindrical partition wall 8 to the re-classification chamber 7b.
In the re-classification chamber 7b, the mixed fine particles are separated from the coarse particles by the cooperation of centrifugal force and sorting wind, and the coarse particles are separated from the coarse particles. The discharge port 21 is configured to send fine powder particles through the opening 20 to the main classification chamber 7a by means of a sorting air.

〔別実施例〕[Another example]

次に別の実施例を説明する。 Next, another embodiment will be described.

筒状隔壁8の形状や取付構成、あるいは、開口
20の形状、その他分級機の具体構造において適
宜変更が可能であり、例えば、ロータ2の下部
に、第1図にAで示す位置に、粗粉粒を回転半径
方向に押し出すシールフインを設けて、微粉粒回
収域への粗粉粒流入阻止をより一層信頼性の高い
状態で図れるようにする等が可能である。
The shape and mounting configuration of the cylindrical partition wall 8, the shape of the opening 20, and other specific structures of the classifier can be changed as appropriate. It is possible to provide a seal fin that pushes out the powder particles in the rotational radial direction to more reliably prevent coarse particles from flowing into the fine powder collection area.

対象とする粉粒体の種類や分級機の用途は不問
である。
The type of target powder and the purpose of the classifier do not matter.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の実施例を示す要部縦断面
図、第2図は第1図の―線断面図、第3図は
従来例の要部縦断面図である。 2…ロータ、3…ケース、4…分級ブレード、
5…微粉粒通路、7a,7b…分級室、7a…主
分級室、7b…再分級室、8…筒状隔壁、10…
原料供給口、14…微粉粒排出口、15…通路、
16…分散ベーン、17…選別風供給口、20…
開口、21…粗粉粒排出口。
FIG. 1 is a longitudinal cross-sectional view of a main part showing an embodiment of the present invention, FIG. 2 is a cross-sectional view taken along the line -- in FIG. 1, and FIG. 3 is a longitudinal cross-sectional view of a main part of a conventional example. 2...rotor, 3...case, 4...classifying blade,
5... Fine powder passageway, 7a, 7b... Classification chamber, 7a... Main classification chamber, 7b... Re-classification chamber, 8... Cylindrical partition wall, 10...
Raw material supply port, 14... Fine powder discharge port, 15... Passage,
16...Distribution vane, 17...Selecting air supply port, 20...
Opening, 21... Coarse powder outlet.

Claims (1)

【特許請求の範囲】[Claims] 1 周部に分級ブレード4を並設したロータ2を
ケース3内に縦軸芯周りで駆動回転自在に設け、
前記分級ブレード4間の隙間に連通する微粉粒通
路5を前記ロータ2内に形成し、前記分級ブレー
ド4の外周部に形成した環状の分級室7a,7b
に連通する原料供給口10、粗粉粒排出口21及
び選別風供給口17と、前記微粉粒通路5に連通
する微粉粒排出口14とを前記ケース3に形成し
た微粉体用分級機であつて、前記分級室7a,7
bを前記分級ブレード4側の主分級室7aと前記
粗粉粒排出口21及び選別風供給口17が連通す
る再分級室7bとに区画する筒状隔壁8を、前記
ロータ2とほぼ同芯状に配置し、前記再分級室7
bから前記主分級室7aに選別風及び微粉粒を送
る開口20を、前記筒状隔壁8にその全周にわた
つて配置して形成し、前記筒状隔壁8の下端部と
前記ロータ2との間に、前記主分級室7aから前
記再分級室7bに粗粉粒を送る通路15を形成
し、その通路15からの粗粉粒を前記再分級室7
b内に分散供給する分散ベーン16を前記ロータ
2に設けてある粉粒体用分級機。
1. A rotor 2 with classification blades 4 arranged side by side on its periphery is provided in a case 3 so as to be freely driven and rotatable around a vertical axis,
A fine powder passage 5 communicating with the gap between the classification blades 4 is formed in the rotor 2, and annular classification chambers 7a and 7b are formed on the outer periphery of the classification blades 4.
A classifier for fine powder, in which a raw material supply port 10, a coarse powder discharge port 21, and a sorting air supply port 17 communicating with the case 3, and a fine powder discharge port 14 communicating with the fine powder passage 5 are formed in the case 3. The classification rooms 7a, 7
A cylindrical partition wall 8 that partitions b into a main classification chamber 7a on the classification blade 4 side and a re-classification chamber 7b in which the coarse powder discharge port 21 and the screening air supply port 17 communicate is substantially coaxial with the rotor 2. The re-classification chamber 7
An opening 20 for sending a sorting air and fine particles from b to the main classification chamber 7a is formed in the cylindrical partition wall 8 over its entire circumference, and the lower end of the cylindrical partition wall 8 and the rotor 2 are connected to each other. In between, a passage 15 for sending coarse powder from the main classification chamber 7a to the re-classification chamber 7b is formed, and the coarse powder from the passage 15 is sent to the re-classification chamber 7.
A classifier for powder and granular materials, in which the rotor 2 is provided with a dispersion vane 16 for dispersing and supplying the material into the powder.
JP3607985A 1985-02-25 1985-02-25 Sorter for powdered and granular body Granted JPS61197083A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3607985A JPS61197083A (en) 1985-02-25 1985-02-25 Sorter for powdered and granular body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3607985A JPS61197083A (en) 1985-02-25 1985-02-25 Sorter for powdered and granular body

Publications (2)

Publication Number Publication Date
JPS61197083A JPS61197083A (en) 1986-09-01
JPS6347515B2 true JPS6347515B2 (en) 1988-09-22

Family

ID=12459731

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3607985A Granted JPS61197083A (en) 1985-02-25 1985-02-25 Sorter for powdered and granular body

Country Status (1)

Country Link
JP (1) JPS61197083A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022085505A1 (en) * 2020-10-23 2022-04-28 東邦チタニウム株式会社 METHOD OF PRODUCING Mg-CONTAINING PARTICLES

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5298926B2 (en) * 2009-02-18 2013-09-25 株式会社リコー Classification device, classification method, and toner production method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022085505A1 (en) * 2020-10-23 2022-04-28 東邦チタニウム株式会社 METHOD OF PRODUCING Mg-CONTAINING PARTICLES

Also Published As

Publication number Publication date
JPS61197083A (en) 1986-09-01

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