JPH0433956Y2 - - Google Patents

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Publication number
JPH0433956Y2
JPH0433956Y2 JP1989122454U JP12245489U JPH0433956Y2 JP H0433956 Y2 JPH0433956 Y2 JP H0433956Y2 JP 1989122454 U JP1989122454 U JP 1989122454U JP 12245489 U JP12245489 U JP 12245489U JP H0433956 Y2 JPH0433956 Y2 JP H0433956Y2
Authority
JP
Japan
Prior art keywords
gas supply
supply nozzle
gas
supply pipe
main body
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
JP1989122454U
Other languages
Japanese (ja)
Other versions
JPH0361947U (en
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 filed Critical
Priority to JP1989122454U priority Critical patent/JPH0433956Y2/ja
Publication of JPH0361947U publication Critical patent/JPH0361947U/ja
Application granted granted Critical
Publication of JPH0433956Y2 publication Critical patent/JPH0433956Y2/ja
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 〔産業上の利用分野〕 この考案は分離装置に関し、特に、遠心力を利
用した分離装置に関するものである。
[Detailed Description of the Invention] [Industrial Field of Application] This invention relates to a separation device, and particularly to a separation device that utilizes centrifugal force.

〔従来の技術および解決しようとする課題〕 一般に、種々の大きさのものが混在している粉
粒体を分離する場合には、遠心力を利用して分離
することが一般的であるが、前処理としての分散
が重要である。
[Prior Art and Problems to be Solved] Generally, when separating powder and granules containing a mixture of various sizes, centrifugal force is generally used to separate them. Dispersion as a pretreatment is important.

しかし、分散が不充分のため目的の製品を得ら
れず効率の低下をまねいているのが現状である。
However, the current situation is that the desired product cannot be obtained due to insufficient dispersion, resulting in a decrease in efficiency.

この考案は前記の問題点を解決し、確実に大
小、軽重を分離することのできる分離装置を提供
することを目的とする。
The purpose of this invention is to solve the above-mentioned problems and provide a separation device that can reliably separate large and small objects and light and heavy objects.

〔課題を解決するための手段〕[Means to solve the problem]

上記の目的を達成するために縦置き円筒状をな
す本体の外周面に、その接線方向を向くガス供給
ノズルの一端を配設し、このガス供給ノズルの他
端を外方に湾曲状に拡開し、一端から内部に分散
すべき粉粒体を充填可能な供給管の他端を、前記
ガス供給ノズルの他端との間にわずかな間隙を有
して位置させるとともに、この間隙を保持した状
態で、前記ガス供給ノズルと供給管の他端どうし
を両端が閉塞した円筒状をなすガス溜まりの内部
に位置し、さらに、前記ガス溜まりに高圧ガス供
給管を接続し、この高圧ガス供給管を介して前記
ガス溜まりの内部に高圧ガスを供給した際、この
高圧ガスが前記間隙を通つて前記ガス供給ノズル
の湾曲状の他端に沿つて流入して壁面流を生じる
ようにしたものである。
In order to achieve the above purpose, one end of a gas supply nozzle is provided on the outer peripheral surface of the vertically cylindrical main body, facing in the tangential direction, and the other end of the gas supply nozzle is expanded outward in a curved manner. The other end of the supply pipe, which can be filled with the powder or granules to be dispersed inside, is positioned with a slight gap between it and the other end of the gas supply nozzle, and this gap is maintained. In this state, the gas supply nozzle and the other end of the supply pipe are located inside a cylindrical gas reservoir with both ends closed, and a high-pressure gas supply pipe is connected to the gas reservoir, and the high-pressure gas supply When high-pressure gas is supplied into the gas reservoir through the pipe, the high-pressure gas flows through the gap and along the other curved end of the gas supply nozzle to generate a wall flow. It is.

〔作用〕[Effect]

上記の手段を採用したので、高圧ガスを流入し
た際に、供給ノズルの内周部が負圧になることに
より、供給ノズルに充填してある粉粒体が吸引さ
れてバラバラになつた状態で本体の内部に投入さ
れ、この投入状態が、円筒形の本体の内部に投入
され、この投入状態が、円筒形の本体の接線方向
であるので遠心力の作用を受けて大きく粒子や重
い粒子はより外側に、また、小さい粒子や軽い粒
子は内側に位置することになつて確実に分離され
ることになる。
By adopting the above method, when high-pressure gas flows in, the inner periphery of the supply nozzle becomes negative pressure, and the powder and granules filled in the supply nozzle are sucked and broken into pieces. The particles are thrown into the inside of the main body, and in this state, they are thrown into the inside of the cylindrical main body, and since this thrown state is in the tangential direction of the cylindrical main body, large particles and heavy particles are The outermost particles and the smaller and lighter particles will be located on the inner side to ensure separation.

〔実施例〕〔Example〕

以下、図面に示すこの考案の実施例について説
明する。
Embodiments of this invention shown in the drawings will be described below.

第1図にはこの考案による分離装置の概略縦断
面図が、また、第2図には第1図の−線に沿
つてみた状態がそれぞれ示されている。
FIG. 1 is a schematic vertical cross-sectional view of the separating device according to this invention, and FIG. 2 is a view taken along the line -- in FIG. 1.

この分離装置は、上部が直円筒状となつている
とともに、下部が順次小径となる逆円錐状となつ
ている本体1を有し、この本体1の下部開口部に
連結部2を介して捕集容器3の上部口部を連結
し、また、前記本体1の上部には、同心に細管4
が設けられている。
This separation device has a main body 1 whose upper part has a right cylindrical shape and whose lower part has an inverted conical shape with the diameter gradually decreasing. The upper opening of the collection container 3 is connected, and a thin tube 4 is concentrically connected to the upper part of the main body 1.
is provided.

前記本体1の上部の任意の位置には、その接線
方向を向いた状態でガス供給ノズル5の一端が連
結され、このガス供給ノズル5の他端部は湾曲し
て外方に広がつている。
One end of a gas supply nozzle 5 is connected to an arbitrary position on the upper part of the main body 1 while facing in the tangential direction thereof, and the other end of the gas supply nozzle 5 is curved and spread outward. .

そして、前記ガス供給ノズル5の他端とわずか
な間隙lを有して供給管6の一端が位置し、この
供給管6の上端は上方を向いていて全体がほぼL
字状に屈曲している。
One end of the supply pipe 6 is located with a slight gap 1 from the other end of the gas supply nozzle 5, and the upper end of the supply pipe 6 faces upward and the entire length is approximately L.
It is curved in the shape of a letter.

そして、前記ガス供給ノズル5の他端と前記供
給管6の一端とは前記わずかな間隙lを有した状
態で、その外周が両端が閉塞した円筒状をなすガ
ス溜まり7の内部に収納され、このガス溜まり7
の円周面上の任意の位置には高圧ガス供給管8が
接続されている。
The other end of the gas supply nozzle 5 and one end of the supply pipe 6 are housed in a gas reservoir 7 having a cylindrical outer periphery with both ends closed, with a slight gap l between them, This gas pool 7
A high-pressure gas supply pipe 8 is connected to an arbitrary position on the circumferential surface.

つぎに前記のものの作用について説明する。 Next, the operation of the above will be explained.

まず、前記供給管6の内部に分離すべき粉粒体
9を充填し、つぎに前記高圧ガス供給管8を介し
て高圧ガスを前記ガス溜まり7の内部に供給する
と、この高圧ガスは前記ガス供給ノズル5の他端
部が湾曲しているのでこの湾曲に沿い付着流とな
つてガス供給ノズル5の内部に流入することにな
る。
First, the inside of the supply pipe 6 is filled with powder 9 to be separated, and then high pressure gas is supplied to the inside of the gas reservoir 7 through the high pressure gas supply pipe 8. Since the other end of the supply nozzle 5 is curved, the gas flows into the interior of the gas supply nozzle 5 as an adhering flow along this curve.

この場合、高圧ガスは湾曲している他端部に沿
つて流入して壁面流を生ぜしめ、所謂、コアンダ
効果が生じることになり、ガス供給ノズル5の軸
心部分が負圧になる。
In this case, the high-pressure gas flows in along the other curved end, creating a wall flow, resulting in the so-called Coanda effect, and the axial center of the gas supply nozzle 5 becomes under negative pressure.

この負圧によつて一端がガス溜まり7の内部に
位置している供給管6の他端から大気が吸い込ま
れ、これと同時に分離すべき原料である粉粒体も
吸い込まれ、前記ガス供給ノズル5の内部で粉粒
体は強力な分散作用を受け、本体1の内部に、そ
の接線方向に空気流とともに投入されるので本体
1の内部で旋回流を生じさせることになる。
Due to this negative pressure, the atmosphere is sucked in from the other end of the supply pipe 6, one end of which is located inside the gas reservoir 7, and at the same time, the powder or granular material that is the raw material to be separated is also sucked in, and the gas supply nozzle The powder and granules are subjected to a strong dispersion action inside the main body 1 and are thrown into the main body 1 along with the air flow in the tangential direction thereof, so that a swirling flow is generated inside the main body 1.

一方、本体1の内部の空気は、本体1の上部に
軸心に位置した細管4を介して流出させるので旋
回流は連続することとなる。
On the other hand, since the air inside the main body 1 is discharged through the thin tube 4 located in the upper part of the main body 1 at the axis, the swirling flow continues.

したがつて、この旋回流によつて遠心力が発生
することにより、大きい粒子や重い粒子はより外
側に、また、小さい粒子や軽い粒子は内側に分離
されることになる。
Therefore, as centrifugal force is generated by this swirling flow, large particles and heavy particles are separated to the outside, and small particles and light particles are separated to the inside.

そして、分離された粉粒体は本体1の下部の逆
円錐部を滑落して、本体1の下部に連結部2を介
して連結された捕集容器3の内部に分離された状
態で位置することになる。
Then, the separated powder and granules slide down the inverted conical part at the bottom of the main body 1 and are located in a separated state inside the collection container 3 connected to the bottom of the main body 1 via the connecting part 2. It turns out.

したがつて、前記ガス供給ノズル5の内部にお
いて、ガス供給ノズル5の内壁の付着流と、吸引
する二次ガス流、すなわち、供給管6から流入す
る空気流とによつて発生する速度差によつて粉粒
体9を強力に分散し、この状態で分離場所である
本体1の内部に供給するので粉粒体を構成する各
粒子を、大きいものや重いものと、小さいものや
軽いものとに効率よく分離することができる。
Therefore, inside the gas supply nozzle 5, due to the speed difference generated between the flow adhering to the inner wall of the gas supply nozzle 5 and the secondary gas flow to be sucked, that is, the air flow flowing in from the supply pipe 6. Therefore, the powder 9 is strongly dispersed and in this state is fed into the main body 1, which is the separation location, so that the particles constituting the powder are divided into large and heavy particles and small and light particles. can be efficiently separated.

この場合、効率良く分離するためには粉粒体を
構成する各粒子がバラバラになつていることが最
も重要であり、これが不十分であると効率良く分
離することができないものであるが、上記のよう
にコアンダ効果を利用することで粉粒体を構成す
る各粒子を確実にバラバラにして本体の内部で確
実に分離することができる。
In this case, in order to efficiently separate the particles, it is most important that each particle constituting the powder or granule material is separated, and if this is insufficient, efficient separation will not be possible. By utilizing the Coanda effect, it is possible to reliably break apart the particles that make up the powder and separate them inside the main body.

〔考案の効果〕[Effect of idea]

この考案は前記のように構成したので、高圧ガ
ス供給管を介してガス溜まりの内部に高圧ガスを
供給すると、高圧ガスが供給管とガス供給ノズル
との間隙を通つてガス供給ノズルの壁面流となつ
て内部に流入し、これにより、ガス供給ノズルの
軸心部分が負圧となつて供給管の内部の粉粒体を
空気ととともに吸い込み、粉粒体がガス供給ノズ
ルの内部で強力な分散作用を受けてバラバラにな
り、このバラバラの状態で本体の内部に投入され
て本体の内部で遠心力による分離作用を受けるの
で、大きい粒子や重い粒子はより外側に、小さい
粒子や軽い粒子は内側に確実に分離され、しか
も、上記の分散作用および分離作用は高圧ガスを
供給するだけで行われるという効果を有してい
る。
Since this device is configured as described above, when high-pressure gas is supplied into the gas reservoir through the high-pressure gas supply pipe, the high-pressure gas passes through the gap between the supply pipe and the gas supply nozzle and flows onto the wall of the gas supply nozzle. As a result, the axial center of the gas supply nozzle becomes negative pressure, and the powder and granules inside the supply pipe are sucked together with air, causing the powder and granules to generate a strong force inside the gas supply nozzle. They are broken apart by dispersion, and in this broken state they are thrown into the main body, where they are separated by centrifugal force, so large and heavy particles are placed on the outside, while small and light particles are placed inside the main body. It has the advantage that the separation is reliably carried out on the inside, and the above-mentioned dispersion and separation effects can be performed simply by supplying high-pressure gas.

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

第1図はこの考案による分離装置を示す概略断
面図、第2図は第1図の−線に沿つてみた図
である。 1……本体、2……連結部、3……捕集容器、
4……細管、5……ガス供給ノズル、6……供給
管、7……ガス溜まり、8……高圧ガス供給管、
9……粉流体、l……間隙。
FIG. 1 is a schematic sectional view showing a separation device according to this invention, and FIG. 2 is a view taken along the - line in FIG. 1. 1...Main body, 2...Connection part, 3...Collection container,
4... thin tube, 5... gas supply nozzle, 6... supply pipe, 7... gas reservoir, 8... high pressure gas supply pipe,
9...Powder fluid, l...Gap.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 縦置き円筒状をなす本体の外周面に、その接線
方向を向くガス供給ノズルの一端を配設し、該ガ
ス供給ノズルの他端を外方に湾曲状に拡開し、一
端から内部に分散すべき粉粒体を充填可能な供給
管の他端を、前記ガス供給ノズルの他端との間に
わずかな間隙を有して位置させるとともに、この
間隙を保持した状態で、前記ガス供給ノズルと供
給管の他端どうしを両端が閉塞した円筒状をなす
ガス溜まりの内部に位置し、さらに、前記ガス溜
まりに高圧ガス供給管を接続し、該高圧ガス供給
管を介して前記ガス溜まりの内部に高圧ガスを供
給した際、この高圧ガスが前記間隙を通つて前記
ガス供給ノズルの湾曲状の他端に沿つて流入して
壁面流を生じるようにしたことを特徴とする分離
装置。
One end of a gas supply nozzle facing in the tangential direction is arranged on the outer circumferential surface of a vertically cylindrical main body, the other end of the gas supply nozzle is expanded outward in a curved shape, and is dispersed inward from one end. The other end of the supply pipe that can be filled with the powder or granular material to be filled is positioned with a slight gap between it and the other end of the gas supply nozzle, and while maintaining this gap, the gas supply nozzle is and the other end of the supply pipe are located inside a cylindrical gas reservoir with both ends closed, and a high-pressure gas supply pipe is connected to the gas reservoir, and the gas reservoir is connected to the gas reservoir through the high-pressure gas supply pipe. A separation device characterized in that when high-pressure gas is supplied into the interior, the high-pressure gas flows through the gap and along the other curved end of the gas supply nozzle to generate a wall flow.
JP1989122454U 1989-10-19 1989-10-19 Expired JPH0433956Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1989122454U JPH0433956Y2 (en) 1989-10-19 1989-10-19

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1989122454U JPH0433956Y2 (en) 1989-10-19 1989-10-19

Publications (2)

Publication Number Publication Date
JPH0361947U JPH0361947U (en) 1991-06-18
JPH0433956Y2 true JPH0433956Y2 (en) 1992-08-13

Family

ID=31670452

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1989122454U Expired JPH0433956Y2 (en) 1989-10-19 1989-10-19

Country Status (1)

Country Link
JP (1) JPH0433956Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2580193B2 (en) * 1987-09-17 1997-02-12 日清製粉株式会社 Cyclone type dry classifier

Also Published As

Publication number Publication date
JPH0361947U (en) 1991-06-18

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