JPH02122875A - Gas circulating type powder classifier - Google Patents

Gas circulating type powder classifier

Info

Publication number
JPH02122875A
JPH02122875A JP27450388A JP27450388A JPH02122875A JP H02122875 A JPH02122875 A JP H02122875A JP 27450388 A JP27450388 A JP 27450388A JP 27450388 A JP27450388 A JP 27450388A JP H02122875 A JPH02122875 A JP H02122875A
Authority
JP
Japan
Prior art keywords
classifier
powder
air
pump
case
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.)
Granted
Application number
JP27450388A
Other languages
Japanese (ja)
Other versions
JP2840644B2 (en
Inventor
Yubun Ibori
井堀 雄文
Yukiyoshi Yamada
幸良 山田
Mutsuo Kokubu
国分 六男
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 JP63274503A priority Critical patent/JP2840644B2/en
Publication of JPH02122875A publication Critical patent/JPH02122875A/en
Application granted granted Critical
Publication of JP2840644B2 publication Critical patent/JP2840644B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To classify combustible powder by means of a simple structure by circulating non-combustible gas in a circulating line to refluxed gas flow from a discharge pipe of a classifier into a case and classifying the powder. CONSTITUTION:Air in a closed case 6 is sucked in from around a classifier 4 into a pump 11 through a cyclone 7 and a filter 9 and the pump 11 by driving a pump 11, and the air sucked in from a closed case 6 is discharged by opening an air discharge valve 19. When the air in the closed case 6 is almost discharged, the air discharge valve 19 is closed and a nitrogen injection valve 18 is opened to inject nitrogen of given volume, and then the nitrogen injection valve 18 is closed. When a powder to be classified is fed from a feeding inlet 1, the powder is fed into the classifier 4 by a screw feeder 2 and classified. The classifier 4 is operated in the nitrogen atmosphere, and conventional classifier and its piping system can be used as carrier by simply closing the classifier, and classification of combustible powder can be carried out by means of a simple structure.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は可燃性の粉体を分級することかできるガス循環
式粉体分級機に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a gas circulation type powder classifier capable of classifying combustible powder.

(従来技術) 粒度の比較的小さい粉体の分級には空気の旋回流を利用
して粒子を加速し、遠心力と空気流による抗力との作用
差により粉体粒子を分級する空気分級機か利用されてい
る。この種の空気分級機においては、空気を外側から分
級室へ導き、分級室内で渦流を生しせしめ、この渦流中
に粉体を投入し遠心力と空気流による抗力とのバランス
を利用して粉体を分級している。空気流は外側から流れ
込み、分級機中心部の排気管を通して機外へ排気させら
れるか、この排気中に分離された微粉成分か含まれ、粗
粉成分は分級室の外側壁側に移動するのて、この微粉成
分及び粗粉成分を各々収集すればよい。
(Prior art) Air classifiers are used to classify powders with relatively small particle sizes by accelerating the particles using a swirling flow of air and classifying the powder particles by the difference in action between the centrifugal force and the drag force caused by the air flow. It's being used. In this type of air classifier, air is introduced into the classification chamber from the outside, creating a vortex inside the classification chamber, and powder is introduced into this vortex to utilize the balance between centrifugal force and drag caused by the air flow. Classifying powder. Either the airflow flows in from the outside and is exhausted outside the machine through the exhaust pipe in the center of the classifier, or the separated fine powder components are included in this exhaust air, and the coarse powder components move to the outside wall of the classification chamber. Then, the fine powder component and the coarse powder component may be collected respectively.

ところで、このような分級機を用いて金属微粉体など可
燃物の粉体な分級すると、空気を用いるため粉体か燃焼
したりあるいは爆発したりするおそれかある。そのため
、このような分級機を用いて可燃性の粉体な分級する場
合は、分級機の周辺部にエアシールやロータリーフィー
ダなどを取り付けて空気を遮断し、空気の代わりに不活
性ガスを分級機内に供給してやる必要があるか、そうす
ると装置か非常に複雑になってしまう。
By the way, when such a classifier is used to classify combustible materials such as fine metal powder, there is a risk that the powder will burn or explode because air is used. Therefore, when using such a classifier to classify flammable powder, install an air seal or rotary feeder around the classifier to shut off the air, and inert gas is introduced into the classifier instead of air. It would be necessary to supply it to a large number of people, or the equipment would become very complex.

(発明の目的および構成) 本発明は上記の点にかんがみてなされたちのて、簡単な
構成で可燃性の粉体な安全に分級できるようにすること
を目的とする。
(Object and structure of the invention) The present invention has been made in view of the above points, and an object of the present invention is to enable safe classification of flammable powders with a simple structure.

この目的を達成するため、外気を吸入して排気管から排
出する過程で旋回流を生じさせ、この旋回流中に粉体を
投入し、遠心力と気体流による抗力との作用差を利用し
て粉体を分級する分級機と、この分級機を密封するケー
スと、分級機の排気管からの気体流を前記ケース内へ環
流させる循環路とを設け、この循環路の中を不燃性ガス
を循環させて粉体を分級するように構成した。
To achieve this objective, a swirling flow is generated in the process of drawing in outside air and discharging it from the exhaust pipe, and powder is introduced into this swirling flow to utilize the difference in action between centrifugal force and drag caused by the gas flow. A classifier for classifying powder using a method, a case for sealing the classifier, and a circulation path for circulating a gas flow from the exhaust pipe of the classifier into the case. It was configured to circulate the powder to classify the powder.

(実施例) 以下本発明を図面に基づいて説明する。(Example) The present invention will be explained below based on the drawings.

第1図は本発明によるガス循環式分級機の一実施例を示
す概略線図てあり、図中、lはたとえば金属微粉などの
可燃性の粉体を投入する投入口。
FIG. 1 is a schematic diagram showing an embodiment of the gas circulation classifier according to the present invention, and in the figure, l represents an inlet into which combustible powder such as fine metal powder is introduced.

2は投入口lから投入された粉体を分級機4へ供給する
スクリューフィーダである。
Reference numeral 2 denotes a screw feeder that supplies the powder input from the input port 1 to the classifier 4.

分級機4は公知の形式のもので、周辺の外気を分級室へ
導き、分級室内で渦流を生じせしめ、この渦流中に粉体
を投入し遠心力と気体流による抗力性とのバランスを利
用して粉体を分級している。外気は分級機の円周方向か
ら流れ込み、中心部から排気管4aを通して機外へ排気
させられるか、この排気中に分離された微粉成分か含ま
れ、粗粉成分は分級室の外側壁側に移動して粗粉搬送管
4bにより収集される。この粗粉搬送管4bは粗粉回収
容器5に接続されている。
The classifier 4 is of a known type, which guides the surrounding outside air into the classification chamber, generates a vortex in the classification chamber, and injects the powder into this vortex, making use of the balance between centrifugal force and drag caused by the gas flow. to classify the powder. The outside air flows in from the circumferential direction of the classifier and is exhausted from the center through the exhaust pipe 4a, or the separated fine powder components are included in this exhaust, and the coarse powder components are discharged to the outside wall of the classification chamber. The coarse powder is moved and collected by the coarse powder conveying pipe 4b. This coarse powder conveying pipe 4b is connected to a coarse powder collection container 5.

スクリューフィーダ2、搬送管3および分級機4は密閉
ケース6中に設置されている。
The screw feeder 2, the conveying pipe 3, and the classifier 4 are installed in a closed case 6.

7は排気管4aか接続されたサイクロンてあり、排気管
4aに流れ込んだ微粉成分はサイクロン7において分離
されて微粉回収器8に回収される。9はサイクロン7を
管lOで接続され、サイクロン7で回収されなかった微
粉を取り除くためのフィルタボックス、11はフィルタ
ボックス9と管12により接続されたポンプ、13は気
体の断熱圧縮による温度−L昇を冷却する熱交換器てあ
り、この熱交換器13は管14によってポンプ11と接
続されている。また熱交換器13は管15により密閉ケ
ース6と接続され、したがって、密閉ケース6→サイク
ロン7→フイルタ9→ポンプ11→熱交換器13→密閉
ケース6の循環路か形成され、中の気体は図の矢印の方
向に流れる。
A cyclone 7 is connected to an exhaust pipe 4a, and the fine powder components flowing into the exhaust pipe 4a are separated in the cyclone 7 and collected in a fine powder collector 8. 9 is a filter box connected to the cyclone 7 by a pipe lO and used to remove fine powder not collected by the cyclone 7; 11 is a pump connected to the filter box 9 by a pipe 12; and 13 is a temperature -L due to adiabatic compression of gas. A heat exchanger is provided for cooling the pump, and this heat exchanger 13 is connected to the pump 11 by a pipe 14. Furthermore, the heat exchanger 13 is connected to the sealed case 6 through a pipe 15, thus forming a circulation path of the sealed case 6 → cyclone 7 → filter 9 → pump 11 → heat exchanger 13 → closed case 6, and the gas inside is Flows in the direction of the arrow in the figure.

16は密閉ケース6内の気圧を測定する圧力計、17は
密閉ケース6内の気圧を調整するためのレリーフ弁、1
8は管15に接続された窒素注入弁、19は管14に設
けられた空気放出弁である。
16 is a pressure gauge for measuring the atmospheric pressure inside the sealed case 6; 17 is a relief valve for adjusting the atmospheric pressure inside the sealed case 6;
8 is a nitrogen injection valve connected to the pipe 15, and 19 is an air release valve provided on the pipe 14.

さて始動時には密閉ケース6には空気か入っているので
、その空気を抜いて空気と不燃性のガス(実施例では窒
素)を入れ換える必要がある。
Now, since some air is contained in the sealed case 6 at the time of startup, it is necessary to remove the air and replace the air with nonflammable gas (nitrogen in the embodiment).

そこで、まずポンプ11を駆動して密閉ケース6内の空
気を分級機4の周りからサイクロン7→フイルタ9→ポ
ンプ11という経路で吸入し、このとき空気放出弁19
を開放しておいて密閉ケース6から吸入した空気を放出
する。一方、窒素注入弁18には予め窒素ボンベ20を
接続しておき、密閉ケース6内の空気かほぼ抜かれたら
空気放出弁19を閉して窒素注入弁18を開き、所定量
の窒素を注入しその後窒素注入弁18を閉しる。窒素は
管15から密閉ケース6へ流入し、分級a4は窒素の雰
囲気中で動作することになる。
Therefore, first, the pump 11 is driven to suck the air inside the sealed case 6 from around the classifier 4 through the cyclone 7 → filter 9 → pump 11, and at this time, the air release valve 19
is opened and the air sucked in from the sealed case 6 is released. On the other hand, the nitrogen cylinder 20 is connected to the nitrogen injection valve 18 in advance, and when most of the air in the sealed case 6 has been removed, the air release valve 19 is closed, the nitrogen injection valve 18 is opened, and a predetermined amount of nitrogen is injected. Thereafter, the nitrogen injection valve 18 is closed. Nitrogen flows into the closed case 6 from the pipe 15, and the classifier a4 operates in a nitrogen atmosphere.

次に分級すべき粉体な投入口lから投入すると、粉体は
スクリューフィーダ2によって分級機4へ供給され1分
級か開始される。すなわち密閉ケース6内の窒素は分級
機4の外周部から吸入されて排気管13からサイクロン
7へ送られるか、その過程において粗粉は粗粉搬送管4
bを経て粗粉回収容器5で回収され、微粉はサイクロン
7において微粉回収器8に回収される。窒素はサイクロ
ン7からフィルタボックス9を経てポンプ11へ流入す
る。その後ポンプ11から流出されて熱交換器13て冷
却され再び密閉ケース6へ環流する。
Next, when the powder to be classified is inputted from the inlet 1, the powder is supplied to the classifier 4 by the screw feeder 2, and one classification is started. That is, the nitrogen in the sealed case 6 is sucked in from the outer periphery of the classifier 4 and sent to the cyclone 7 from the exhaust pipe 13, or in the process, the coarse powder is transferred to the coarse powder conveying pipe 4.
The fine powder is collected in a coarse powder collecting container 5 via a cyclone 7, and the fine powder is collected in a fine powder collecting device 8 in a cyclone 7. Nitrogen flows from the cyclone 7 through the filter box 9 to the pump 11. Thereafter, it flows out from the pump 11, is cooled by the heat exchanger 13, and then flows back into the sealed case 6.

以上のようにすれば、分級機を密閉するたけて従来の分
級機およびその配管系をそのまま用いることかてき、簡
単な構成で可燃性粉体の分級を行うことかできる。また
窒素注入弁18および空気放出弁19をともに開放して
装置を稼動させれば、従来と同様の空気分級機となる。
With the above method, the conventional classifier and its piping system can be used as is while the classifier is sealed, and combustible powder can be classified with a simple configuration. Furthermore, if the device is operated by opening both the nitrogen injection valve 18 and the air release valve 19, the air classifier becomes similar to the conventional air classifier.

上記実施例では金属微粉体の分級な例にとったげ、本発
明はそれに限らず、石炭粉、プラスチックス粉などその
他の可燃性粉体の分級にも好適である。また不燃性ガス
も窒素に限らすアルゴンなどの不活性ガスや、これらと
空気との混合ガスを用いてもよいのはもちろんである。
Although the above embodiment deals with the classification of fine metal powder, the present invention is not limited thereto, but is also suitable for classifying other combustible powders such as coal powder and plastic powder. Further, the nonflammable gas is limited to nitrogen, but it goes without saying that an inert gas such as argon or a mixed gas of these and air may be used.

(発明の効果) 以上説明したように、本発明によれば、不燃性ガスの雰
囲気下で分級を行うので、簡単な構成で可燃性の粉体を
安全に分級することかできる。
(Effects of the Invention) As described above, according to the present invention, since classification is performed in an atmosphere of nonflammable gas, combustible powder can be safely classified with a simple configuration.

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

第1図は本発明によるガス循環式分級機の一実施例を示
す顆路線図である。 l−・・投入口、4・・・分級機、6・・・密封ケース
、7・・・サイクロン、9・・・フィルタ、11・・・
ポンプ、18・・・窒素注入弁、19・・・空気放出弁
、20・・・窒素ボンベ
FIG. 1 is a diagram showing an embodiment of the gas circulation classifier according to the present invention. l-...Inlet, 4...Classifier, 6...Sealed case, 7...Cyclone, 9...Filter, 11...
Pump, 18...Nitrogen injection valve, 19...Air release valve, 20...Nitrogen cylinder

Claims (1)

【特許請求の範囲】[Claims]  外気を吸入して排気管から排出する過程で旋回流を生
じさせ、この旋回流中に粉体を投入し、遠心力と気体流
による抗力との作用差を利用して粉体を分級する分級機
と、この分級機を密封するケースと、前記排気管からの
気体流を前記ケース内へ環流させる循環路を有し、この
循環路の中を不燃性ガスを循環させて粉体を分級するこ
とを特徴とするガス循環式分級機。
A classification method that creates a swirling flow during the process of sucking in outside air and discharging it from the exhaust pipe, inserting powder into this swirling flow, and classifying the powder using the difference in action between centrifugal force and drag caused by the gas flow. the classifier, a case that seals the classifier, and a circulation path that circulates the gas flow from the exhaust pipe into the case, and classifies the powder by circulating nonflammable gas in the circulation path. A gas circulation classifier characterized by:
JP63274503A 1988-11-01 1988-11-01 Gas circulation type powder classifier Expired - Lifetime JP2840644B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63274503A JP2840644B2 (en) 1988-11-01 1988-11-01 Gas circulation type powder classifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63274503A JP2840644B2 (en) 1988-11-01 1988-11-01 Gas circulation type powder classifier

Publications (2)

Publication Number Publication Date
JPH02122875A true JPH02122875A (en) 1990-05-10
JP2840644B2 JP2840644B2 (en) 1998-12-24

Family

ID=17542601

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63274503A Expired - Lifetime JP2840644B2 (en) 1988-11-01 1988-11-01 Gas circulation type powder classifier

Country Status (1)

Country Link
JP (1) JP2840644B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01148781U (en) * 1988-04-01 1989-10-16

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01148781U (en) * 1988-04-01 1989-10-16

Also Published As

Publication number Publication date
JP2840644B2 (en) 1998-12-24

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