JPS62132527A - Disperser of granule - Google Patents

Disperser of granule

Info

Publication number
JPS62132527A
JPS62132527A JP60271586A JP27158685A JPS62132527A JP S62132527 A JPS62132527 A JP S62132527A JP 60271586 A JP60271586 A JP 60271586A JP 27158685 A JP27158685 A JP 27158685A JP S62132527 A JPS62132527 A JP S62132527A
Authority
JP
Japan
Prior art keywords
powder
air streams
dispersed air
dispersion
airflow
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
JP60271586A
Other languages
Japanese (ja)
Other versions
JPH0785773B2 (en
Inventor
Tsutomu Iwamoto
勉 岩本
Kazuhiro Kubouchi
窪内 一博
Atsushi Saito
篤志 斉藤
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.)
Konica Minolta Inc
Original Assignee
Konica Minolta 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 Konica Minolta Inc filed Critical Konica Minolta Inc
Priority to JP60271586A priority Critical patent/JPH0785773B2/en
Publication of JPS62132527A publication Critical patent/JPS62132527A/en
Publication of JPH0785773B2 publication Critical patent/JPH0785773B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/10Mixing by creating a vortex flow, e.g. by tangential introduction of flow components

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)

Abstract

PURPOSE:To effectively disperse granule by providing plural introduction ports for the dispersed air streams wherein the dispersed air streams of granule are mutually rotated in the same direction to a rotation part discharging the dispersed air streams after rotating them. CONSTITUTION:A disperser is composed of a rotation part 1 and the feed mechanism 2, 2 for the dispersed air streams and plural e.g. two introduction ports 25 for the dispersed air streams are opened in a position symmetrical to an axis of the rotation part 1 in the inside peripheral face of the top of the rotating part 1. The high-pressure dispersed air streams of granule formed in the feed mechanisms 2, 2 for the dispersed air streams are introduced into the inside of the rotation part 1 via each introduction port 25, 25. Thereby since two introduction ports 25, 25 are provided so that the dispersed air streams are mutually rotated in the same direction, the deviation caused by the dispersed air streams introduced through one introduction port 25, is disturbed by the dispersed air streams introduced through the other introduction port 25. As a result, the concn. distribution of granule is uniformized in the direction along the circumferential direction of the rotation part 1.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、粉粒体の分散装置に関するものである。[Detailed description of the invention] [Industrial application field] The present invention relates to a dispersion device for powder and granular materials.

〔従来技術〕[Prior art]

従来、粉体または粒体よりなる粉粒体の分散装置として
、例えば粉粒体の分散気流を旋回部内において旋回させ
たうえ、旋回部用口から空円錐状に吐出させて分散させ
る装置が知られている。
Conventionally, as a dispersion device for powder or granules, there has been known a device in which, for example, a dispersion airflow of powder or granules is swirled within a swirling section and then discharged into an empty conical shape from an opening for the swirling section for dispersion. It is being

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、従来の粉粒体の分散装置においては、粉
粒体の分散気流を1個所より旋回部内に導入させるよう
にしているため、旋回部内において、その内周に沿った
方向における粉粒体のl】変分布に大きな偏りを生し、
粉粒体が吐出された後において、旋回中心軸に対して垂
直な平面における濃度分布が不均一となり、十分良好に
粉粒体が分散されず、−成粒子に分散した粉粒体の収率
が低いという問題点がある。
However, in conventional powder and granule dispersion devices, the airflow for dispersing powder and granules is introduced into the swirling section from one point, so the powder and granules are dispersed in the direction along the inner circumference of the swirling section. l] causes a large bias in the distribution,
After the powder is discharged, the concentration distribution in the plane perpendicular to the central axis of rotation becomes non-uniform, and the powder is not dispersed well enough, resulting in a decrease in the yield of the powder dispersed in particles. There is a problem in that it is low.

〔発明の目的〕[Purpose of the invention]

本発明は、以上の如き事情に基づいてなされたものであ
って、その目的は、粉粒体を十分良好に分散させること
ができ、分散吐出方向に対して垂直な平面における濃度
分布が均一となり、しかも分散効率の高い粉粒体の分散
装置を提供することにある。
The present invention has been made based on the above-mentioned circumstances, and its purpose is to be able to sufficiently disperse powder and granules so that the concentration distribution in a plane perpendicular to the dispersion and discharge direction is uniform. Moreover, it is an object of the present invention to provide a dispersion device for powder and granular material with high dispersion efficiency.

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

本発明の粉粒体の分散装置は、粉粒体の分散気流を旋回
した後吐出させる旋回部と、この旋回部においで、各々
粉粒体の分散気流が互いに同方向に旋回するよう設けた
?3J数の分散気流導入口とを存することを特徴とする
The dispersion device for powder and granular material of the present invention includes a swirling section that swirls and then discharges a dispersion airflow of powder and granular material, and a swirling section that is provided so that each dispersion airflow of powder and granular material swirls in the same direction. ? It is characterized by having 3J number of distributed airflow inlets.

〔作 用〕[For production]

斯かる装置によれば、粉粒体の分散気流が複数個所から
旋回部に導入され、−の導入口よりの分散気流が他の4
人口よりの分散気流と均一に旋回混合するため、旋回部
の内周に沿った方向における流速分布および粉粒体の濃
度分布が均一化されるようになり、この結果粉粒体を十
分良好に分散させることができる。
According to such a device, the dispersion airflow of powder and granular material is introduced into the swirling section from multiple locations, and the dispersion airflow from the inlet port - is introduced into the swirling section from multiple locations.
Because of uniform swirling and mixing with the artificially dispersed airflow, the flow velocity distribution in the direction along the inner circumference of the swirling part and the concentration distribution of the powder and granular material become uniform, and as a result, the powder and granular material can be mixed well. Can be dispersed.

(実施例〕 以下、本発明の実施例を図面を参照しながら詳細に説明
する。
(Example) Hereinafter, an example of the present invention will be described in detail with reference to the drawings.

第1図および第2図は、それぞれ本発明分散装置の一実
施例の要部を示す部分破断正面図および下方から見たと
きの説明用横断面図である。この分散装置は、基本的に
旋回部1と、この旋回部lに粉粒体の分散気流を供給す
るための分散気流供給機構2とよりなる。旋回部1は、
下方に開口する旋回部出口26を有する円筒状構造であ
り、この旋回部1の上部における内周面においては、旋
回部1の軸に関して対称の位置、即ちその内周に沿って
略等しい間隔の位置に開口するよう、2つの分散気流導
入口25が、これよりの分散気流が互いに同じ円周方向
(第2図においては反時計方向)に旋回するよう形成さ
れ、これら分散気流導入口25の各々に分散気流供給機
構2,2が接続されている。
FIGS. 1 and 2 are a partially cutaway front view and an explanatory cross-sectional view, respectively, showing essential parts of an embodiment of the dispersion apparatus of the present invention when viewed from below. This dispersion device basically consists of a swirling section 1 and a dispersion airflow supply mechanism 2 for supplying a dispersion airflow of powder to the swirling section 1. The rotating part 1 is
It has a cylindrical structure with a rotating part outlet 26 that opens downward, and on the inner circumferential surface of the upper part of the rotating part 1, there are holes arranged at approximately equal intervals along the inner circumference at symmetrical positions with respect to the axis of the rotating part 1. The two dispersed air flow inlets 25 are formed so that the dispersed air flows therefrom rotate in the same circumferential direction (counterclockwise in FIG. 2). A distributed airflow supply mechanism 2, 2 is connected to each.

図示の例における各分散気流供給機構2は、圧縮空気導
入口21と、粉粒体供給部22と、エゼクタ混合室23
と、エゼクタスロート部24とよりなり、圧縮空気導入
口21よりの圧縮空気がエゼクタ混合室23内に噴出さ
れてエゼクタスロート部24を通過することによって生
ずる吸引力により、粉粒体供給部22より粉粒体Pが少
しづつ供給されてエゼクタ混合室23において混合され
、高圧の粉粒体の分散気流が形成される。なお圧縮空気
導入口21は、前記旋回部1の軸を中心とする円の接線
方向に空気を送る方向とされる。
Each distributed airflow supply mechanism 2 in the illustrated example includes a compressed air inlet 21, a powder supply section 22, and an ejector mixing chamber 23.
The compressed air from the compressed air inlet 21 is ejected into the ejector mixing chamber 23 and passes through the ejector throat section 24, and the suction force generated when the compressed air is ejected from the powder supply section 22. The powder P is fed little by little and mixed in the ejector mixing chamber 23, forming a high-pressure dispersion airflow of the powder. Note that the compressed air inlet 21 is configured to send air in the tangential direction of a circle centered on the axis of the swirling section 1 .

以上のような構成においては、各分散気流供給機構2.
2において形成された高圧の粉粒体の分散気流が、各分
散気流導入口25を介して旋回部1内に導入され、旋回
部1内においてその圧力により旋回部1の内周に沿って
旋回しながら下降し、このとき粉粒体が高剪断力を受け
て分散され、その後旋回部出口26より吐出される。
In the above configuration, each distributed airflow supply mechanism 2.
The high-pressure dispersion airflow of powder and granular material formed in step 2 is introduced into the swirling section 1 through each dispersion airflow introduction port 25, and swirls along the inner periphery of the swirling section 1 due to the pressure inside the swirling section 1. At this time, the powder and granular material is dispersed under high shearing force, and is then discharged from the swirling section outlet 26.

而して旋回部1においては、粉粒体の分散気流が互いに
同方向に旋回するよう複数の分散気流導入口25が形成
されているため、−の分散気流4人口25より導入され
た分散気流によって生ずるべき偏りが、他の分散気流導
入口25より導入された分散気流によって乱されるよう
になる。例えば、−の分散気流導入口25より導入され
た分散気流により旋回部lにおいて形成されるべき高濃
度部分の形成が、互いに他の分散気流導入口25よりの
分散気流の力によって抑制されるようになり、この結果
、旋回部lの円周方向に沿った方向において粉粒体の4
度分布が均一化される。
In the swirling section 1, a plurality of dispersed airflow inlets 25 are formed so that the dispersed airflows of the powder and granular material swirl in the same direction. The deviation that should be caused by this is disturbed by the dispersed airflow introduced from the other dispersed airflow introduction port 25. For example, the formation of a high concentration portion in the swirling portion l due to the dispersion airflow introduced from the - dispersion airflow introduction port 25 is suppressed by the force of the dispersion airflow from the other dispersion airflow introduction ports 25. As a result, in the direction along the circumferential direction of the rotating part l, 4 of the powder and granular material
The degree distribution is made uniform.

複数の分散気流導入口25の位置は、旋回部1の軸に関
して対称の関係にあることが好ましく、これにより、旋
回部1におけるその内周に沿った空間全体の内周方向に
おける粉粒体の濃度分布をより均一化させることができ
る。そしてこの結果、粉粒体の分散を十分良好に達成す
ることができて一次粒子の収率を高くすることができる
と共に、複数の粉粒体供給機fi2により多量の粉粒体
を導入して処理することができるため、処理能力を高め
ることと同時に一次粒子の収率を向上させることができ
、結局きわめて高い効率で粉粒体の分散を達成すること
ができる。
The positions of the plurality of dispersed air flow introduction ports 25 are preferably in a symmetrical relationship with respect to the axis of the swirling section 1, so that the powder and granular material is distributed in the inner circumferential direction of the entire space along the inner circumference of the swirling section 1. The concentration distribution can be made more uniform. As a result, it is possible to achieve sufficiently good dispersion of the powder and granules, thereby increasing the yield of primary particles. Since it can be processed, it is possible to increase the processing capacity and the yield of primary particles at the same time, and as a result, it is possible to achieve dispersion of powder and granular materials with extremely high efficiency.

第3図および第4図はそれぞれ本発明の他の実施例を示
し、第3図の例においては3個、また第4図の例におい
ては4個の分散気流導入口25が旋回部lの軸に関して
対称となる位置に形成され、その各々に分散気流供給機
構2が接続されている。
3 and 4 respectively show other embodiments of the present invention, in which three distributed airflow inlets 25 are provided in the example shown in FIG. 3, and four distributed airflow inlets 25 are provided in the example shown in FIG. They are formed at symmetrical positions with respect to the axis, and a distributed airflow supply mechanism 2 is connected to each of them.

このように多数の分散気2ii導入口を形成することに
より、旋回部1の内周に沿った方向における均一性を一
層向上させることができ、更に処理量を増大させること
が可能である。
By forming a large number of dispersed air 2ii inlets in this way, it is possible to further improve the uniformity in the direction along the inner circumference of the swirling section 1, and it is possible to further increase the throughput.

第5図および第6図は本発明の更に他の実施例を示し、
この例においては上述のように旋回部lに複数の分散気
流導入口25を形成した上、更に、旋回部1の下方にお
いて、旋回する分散気流が衝突するよう障害物が設けら
れている。この例における障害物は4枚の粉粒体拡散羽
根27であり、各粉粒体拡散羽根27は、旋回部1の内
壁における旋回部1の軸に関して対称の位置において、
当該旋回部1の半径方向内方に向かって突出しかつ軸方
向に沿って伸びる状態で固定されている。
FIGS. 5 and 6 show further embodiments of the present invention,
In this example, in addition to forming the plurality of dispersed airflow introduction ports 25 in the swirling portion 1 as described above, an obstacle is further provided below the swirling portion 1 so that the swirling dispersed airflow collides with it. The obstacles in this example are four powder/granular material spreading vanes 27, and each powder/granular material spreading vane 27 is located at a symmetrical position with respect to the axis of the rotating part 1 on the inner wall of the rotating part 1.
It is fixed in a state in which it protrudes inward in the radial direction of the rotating portion 1 and extends along the axial direction.

このような構成によれば、旋回部1内における旋回によ
り粉粒体が分散された気流は、更に粉粒体拡散羽根27
に衝突し、その流れが内方に拡散されるように乱される
ため、旋回部1の内周に沿って流れる粉粒体分散気流の
気流層の厚さが増加するようになる。この結果、粉粒体
はより低い濃度状態で均一に分散されるようになり、粉
粒体の一次粒子の収率を大幅に向上させることができる
According to such a configuration, the airflow in which the powder particles are dispersed due to the swirling within the swirling section 1 further passes through the powder diffusion vanes 27.
, and the flow is disturbed so as to be diffused inward, so that the thickness of the air layer of the powder dispersion air flow flowing along the inner periphery of the swirling section 1 increases. As a result, the powder and granules are uniformly dispersed at a lower concentration, and the yield of primary particles of the powder and granules can be significantly improved.

本発明において上記のように障害物を設ける場合におい
ては、当該障害物は特に制限されるものではないが、図
示の例におけるように粉粒体拡散羽根とすることが好ま
しい。しかしその具体的形状等は限定されず、例えば三
角形状、長方形状、台形状、その他の多角形状であって
もよく、また湾曲したものであってもよい、勿論斯かる
粉粒体拡散羽根の数も任意に選定することができる。
In the case where an obstacle is provided as described above in the present invention, the obstacle is not particularly limited, but it is preferable to use a powder diffusion blade as in the illustrated example. However, its specific shape is not limited, and may be, for example, triangular, rectangular, trapezoidal, or other polygonal shapes, or may be curved. The number can also be arbitrarily selected.

〔発明の効果〕〔Effect of the invention〕

本発明は粉粒体の分散気流を旋回した後吐出させる旋回
部と、この旋回部において、各々粉粒体の分散気流が互
いに同方向に旋回するよう設けた複数の分散気流導入口
とを有することを特徴とする粉粒体の分散装置であるか
ら、粉粒体を十分良好な状態で分散させることができ、
所望の一次粒子の収率を大幅に向上させることができ、
しかも処理能力が増大してきわめて高い効率で粉粒体の
分散を達成することができる。
The present invention includes a swirling part that swirls and then discharges a dispersion airflow of powder and granular material, and a plurality of dispersion airflow inlets provided in this swirling part so that the dispersion airflow of powder and granular material swirls in the same direction. Since this is a dispersion device for powder and granular material, it is possible to disperse the powder and granular material in a sufficiently good condition.
The yield of desired primary particles can be significantly improved,
In addition, the processing capacity is increased and powder particles can be dispersed with extremely high efficiency.

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

第1図は本発明の一実施例の説明用部分破断正面図、第
2図は第1図の装置を下方から見たときの説明用横断面
図、第3図および第4図は各々本発明の他の実施例の説
明用平面図、第5図は本発明の更に他の実施例の説明用
部分破断正面図、第6図は第5図の装置を下方から見た
ときの説明用横断平面図である。 1・・・旋回部     2・・・分散気流供給機構2
1・・・圧縮空気導入口 22・・・粉粒体供給部23
・・・エゼクタ混合室 24・・・エゼクタスロート部
25・・・分散気流導入口 26・・・旋回部用口27
・・・粉粒体拡散羽根
FIG. 1 is a partially cutaway front view for explaining an embodiment of the present invention, FIG. 2 is a cross-sectional view for explaining the apparatus shown in FIG. 1 viewed from below, and FIGS. FIG. 5 is an explanatory plan view of another embodiment of the invention, FIG. 5 is an explanatory partially cutaway front view of yet another embodiment of the invention, and FIG. 6 is an explanatory diagram of the apparatus of FIG. 5 as viewed from below. FIG. 1...Swivel part 2...Distributed airflow supply mechanism 2
1... Compressed air inlet 22... Powder supply section 23
... Ejector mixing chamber 24 ... Ejector throat section 25 ... Dispersion airflow inlet 26 ... Swivel section port 27
...Powder diffusion vane

Claims (1)

【特許請求の範囲】 1)粉粒体の分散気流を旋回した後吐出させる旋回部と
、この旋回部において、各々粉粒体の分散気流が互いに
同方向に旋回するよう設けた複数の分散気流導入口とを
有することを特徴とする粉粒体の分散装置。 2)旋回部内に、旋回する分散気流が衝突するよう障害
物を配設したことを特徴とする特許請求の範囲第1項記
載の粉粒体の分散装置。
[Scope of Claims] 1) A swirling section that swirls and then discharges a dispersion airflow of powder and granules, and a plurality of dispersion airflows provided in this swirling section so that the dispersion airflows of powder and granular materials swirl in the same direction. A dispersion device for powder or granular material, characterized in that it has an inlet. 2) The apparatus for dispersing powder or granular material according to claim 1, characterized in that an obstacle is arranged in the swirling part so that the swirling dispersion airflow collides with it.
JP60271586A 1985-12-04 1985-12-04 Powder dispersion equipment Expired - Lifetime JPH0785773B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60271586A JPH0785773B2 (en) 1985-12-04 1985-12-04 Powder dispersion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60271586A JPH0785773B2 (en) 1985-12-04 1985-12-04 Powder dispersion equipment

Publications (2)

Publication Number Publication Date
JPS62132527A true JPS62132527A (en) 1987-06-15
JPH0785773B2 JPH0785773B2 (en) 1995-09-20

Family

ID=17502142

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60271586A Expired - Lifetime JPH0785773B2 (en) 1985-12-04 1985-12-04 Powder dispersion equipment

Country Status (1)

Country Link
JP (1) JPH0785773B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1989007006A1 (en) * 1988-01-29 1989-08-10 Applied Biosystems, Inc. Device for mixing solutions
JP2010058030A (en) * 2008-09-02 2010-03-18 Mirai Ind Co Ltd Mixer for granular material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1989007006A1 (en) * 1988-01-29 1989-08-10 Applied Biosystems, Inc. Device for mixing solutions
JP2010058030A (en) * 2008-09-02 2010-03-18 Mirai Ind Co Ltd Mixer for granular material

Also Published As

Publication number Publication date
JPH0785773B2 (en) 1995-09-20

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