JPH0639261A - Granular body mixing and transporting device - Google Patents

Granular body mixing and transporting device

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Publication number
JPH0639261A
JPH0639261A JP4087513A JP8751392A JPH0639261A JP H0639261 A JPH0639261 A JP H0639261A JP 4087513 A JP4087513 A JP 4087513A JP 8751392 A JP8751392 A JP 8751392A JP H0639261 A JPH0639261 A JP H0639261A
Authority
JP
Japan
Prior art keywords
conduit
inlet
swirl chamber
powder
spherical
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.)
Pending
Application number
JP4087513A
Other languages
Japanese (ja)
Inventor
Yasunobu Yoshida
康伸 吉田
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP4087513A priority Critical patent/JPH0639261A/en
Publication of JPH0639261A publication Critical patent/JPH0639261A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To provide a granular body mixing and transporting device capable of uniformly mixing and transporting the granular body with the generated spiral flow of air. CONSTITUTION:This granular body mixing and transporting device is provided with a spherical spiral flow chamber 10 having a tangential air inlet 12, a duct means passing through the center of the chamber 10 at right angles to the plane including the inlet 12 and a means 24 for introducing a granular body 22 to be treated into the chamber 10, and the duct means has an inlet 16 opened to the inside of the chamber 10 and an outlet 18 communicating with the outside of the chamber 10.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、粉粒体を混合しながら
搬送するサイクロン式の粉粒体混合搬送装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cyclone-type powder / granular material mixing and conveying device for conveying powder particles while mixing them.

【0002】[0002]

【従来技術】空気流に粉粒体を載せて軸線方向に移動さ
せながら、この空気流に対して半径方向に加圧空気を導
入することによって、渦流を発生させて粉粒体を均一に
混合させながら移送する粉粒体混合搬送装置は、たとえ
ば、特開昭63ー154522号、特開昭63ー267
424号などから公知である。これらの装置では、テー
パの付いた円筒管の軸線方向へ粉粒体を含んだ空気流を
流すと共に、円筒管の周壁に形成したスリットから加圧
空気を導入させている。
2. Description of the Related Art A powder vortex is placed on an air stream and moved in the axial direction, while pressurized air is introduced in the radial direction of the air vortex to generate a vortex flow to uniformly mix the granules. The powdery and granular material mixing and conveying device for transferring while moving is, for example, JP-A-63-154522 and JP-A-63-267.
It is known from No. 424 and the like. In these devices, an air flow containing powder particles is caused to flow in the axial direction of a tapered cylindrical tube, and pressurized air is introduced from a slit formed in the peripheral wall of the cylindrical tube.

【0003】[0003]

【発明が解決しようとする課題】この構成では、空気流
が不安定になったり、逆流が生じたりするという問題が
あるため、円筒管内にさらに軸線方向に延びる別の円筒
管を挿入したり、円筒管の流入口の断面積を調節できる
ようにしたりしている。したがって、装置が複雑にな
る。
In this configuration, since there is a problem that the air flow becomes unstable or a back flow occurs, another cylindrical tube extending in the axial direction may be inserted in the cylindrical tube, The cross-sectional area of the inlet of the cylindrical tube can be adjusted. Therefore, the device becomes complicated.

【0004】[0004]

【課題を解決するための手段】本発明の目的は、空気の
安定した渦流を生じさせ、それによって、粉粒体をさら
に均一に混合しながら搬送できる粉粒体混合搬送装置を
提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a powder and granular material mixing and conveying device capable of generating a stable vortex of air and thereby conveying powder and granular materials while mixing them more uniformly. is there.

【0005】この目的を達成するために、本発明は、接
線方向の空気流入口を有する球形の渦流室と、前記空気
流入口を含む平面に対して直角に渦流室の中心を通って
延びる導管手段と、渦流室内へ処理すべき粉粒体を導入
する導入口手段とを包含し、この導管手段が、渦流室内
に開口した入口と、渦流室の外部に通じる出口とを有す
ることを特徴とする粉粒体混合搬送装置を提供する。
To achieve this object, the invention provides a spherical swirl chamber having a tangential air inlet and a conduit extending through the center of the swirl chamber at right angles to the plane containing said air inlet. Means and inlet means for introducing the granular material to be treated into the swirl chamber, the conduit means having an inlet opening into the swirl chamber and an outlet leading to the outside of the swirl chamber. Provided is a powder and granular material mixing and conveying device.

【0006】本発明の一特徴によれば、粉粒体混合搬送
装置は、導管手段の入口が導入口手段と整合しており、
また、導管手段が軸線方向に移動して入口と導入口手段
との間隔を調節できるようになっていることを特徴とす
る。
According to one feature of the invention, in a powder and granulate mixing and conveying device, the inlet of the conduit means is aligned with the inlet means.
Also, the conduit means is movable in the axial direction so that the distance between the inlet and the inlet means can be adjusted.

【0007】本発明の別の特徴によれば、粉粒体混合搬
送装置は、導管手段が内側導管部と外側導管部とからな
る二重構造となっており、内側導管部が渦流室内に開口
した入口と、渦流室外部に通じる出口とを有し、外側導
管部が内側導管部との間に環状の通路を形成しており、
この通路が前記導入口手段を構成しており、さらに、内
側導管部がその軸線方向に移動できるようになっている
ことを特徴とする。
According to another feature of the present invention, in the powder and granular material mixing and conveying device, the conduit means has a double structure consisting of an inner conduit part and an outer conduit part, and the inner conduit part is opened into the swirl chamber. And an outlet communicating with the outside of the swirl chamber, the outer conduit portion forming an annular passage between the inner conduit portion,
This passage constitutes the inlet means, and is further characterized in that the inner conduit portion is movable in the axial direction thereof.

【0008】本発明のさらに別の特徴によれば、粉粒体
混合搬送装置は、導管手段が、内側導管部と外側導管部
とからなる二重構造導管と、この二重構造導管の内端部
を囲む第2の球形渦流室と、この第2球形渦流室を取り
囲む半球形のシェルとを包含し、このシェルが第2球形
渦流室との間に半球形の連絡通路を構成しており、この
連絡通路が第2球形渦流室の壁を貫いて設けた連絡口と
連通しており、かつ、シェルに設けた導管部分と連絡し
ており、シェルのこの導管部分が導入口手段と整合して
渦流室に開口する入口を有することを特徴とする。
According to still another feature of the present invention, there is provided a powder and granular material mixing and conveying apparatus in which the conduit means has a dual structure conduit including an inner conduit part and an outer conduit part, and an inner end of the dual structure conduit. A second spherical swirl chamber surrounding the portion and a hemispherical shell surrounding the second spherical swirl chamber, the shell forming a hemispherical communication passage between the second spherical swirl chamber and the second spherical swirl chamber. The communication passage is in communication with a communication opening provided through the wall of the second spherical swirl chamber and in communication with a conduit section provided in the shell, which conduit section of the shell is aligned with the inlet means. And has an inlet opening to the swirl chamber.

【0009】[0009]

【作用】上記の構成によれば、空気流入口から渦流室へ
流入した空気は、従来の円筒管に比べて容易かつ簡単に
渦流となり、旋回しながら導管手段内を粉粒体を混合し
ながら移動し、渦流室外部へ流出する。
According to the above construction, the air flowing into the swirl chamber from the air inlet becomes a swirl more easily and easily than the conventional cylindrical pipe, and while swirling, the powder and granules are mixed in the conduit means. It moves and flows out of the swirl chamber.

【0010】[0010]

【実施例】以下、添付図面を参照しながら、本発明の実
施例を説明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

【0011】まず図1を参照して、ここには本発明の粉
粒体混合搬送装置の第1の実施例が示してあり、この粉
粒体混合搬送装置は、球形の渦流室10を包含し、この
渦流室は、図2で最も良くわかるように、接線方向の空
気流入口12を備える。
First, referring to FIG. 1, there is shown a first embodiment of a powder and granular material mixing and conveying apparatus of the present invention. The powder and granular material mixing and conveying apparatus includes a spherical swirl chamber 10. However, the swirl chamber comprises a tangential air inlet 12, as best seen in FIG.

【0012】空気流入口12を含む平面(すなわち、図
2の平面)に対して直角に渦流室10内へ導管14が延
びており、この導管14は、渦流室10内に開口する入
口16と、渦流室12の外部に通じる出口18とを有す
る。導管14は、図1の矢印20で示すようにその長手
軸線方向に移動できるようになっている。
A conduit 14 extends into the swirl chamber 10 at a right angle to the plane containing the air inlet 12 (ie, the plane of FIG. 2), the conduit 14 having an inlet 16 opening into the swirl chamber 10. , And an outlet 18 communicating with the outside of the swirl chamber 12. The conduit 14 is movable in the direction of its longitudinal axis, as indicated by the arrow 20 in FIG.

【0013】導管14の入口16と整合して、渦流室1
0には被処理粉粒体22を渦流室10へ導入するための
導入口手段24が設けてある。この導入口手段24は、
被処理粉粒体の逆流を防ぐロータリーバルブ26を備え
る。
Aligned with the inlet 16 of the conduit 14, the swirl chamber 1
At 0, inlet means 24 for introducing the powdery or granular material 22 to be treated into the swirl chamber 10 is provided. The inlet means 24 is
A rotary valve 26 is provided to prevent backflow of the powder or granular material to be treated.

【0014】作動にあたって、空気流入口12を通して
流入した空気は、渦流室10内で矢印によって示すよう
に旋回しながら導管14の入口16に向い、その中に流
入する。このとき、導入口手段24を通して供給された
被処理粉粒体22がこの渦流に巻き込まれ、混合されな
がら導管14を通って渦流によって導管14の出口18
に搬送される。
In operation, the air entering through the air inlet 12 swirls within the swirl chamber 10 as shown by the arrow toward the inlet 16 of the conduit 14 and into it. At this time, the powdery or granular material 22 to be treated supplied through the inlet means 24 is entrained in the vortex flow, and is mixed with the vortex flow through the conduit 14 to the outlet 18 of the conduit 14.
Be transported to.

【0015】被処理粉粒体のサイズや性質に従って、導
管14はその長手軸線方向に移動され、その入口16と
導入口手段24との間隔を変えることができる。
Depending on the size and nature of the particles to be treated, the conduit 14 can be moved in its longitudinal direction to change the distance between its inlet 16 and inlet means 24.

【0016】図3は、本発明の第2の実施例を示してお
り、この実施例では、第1実施例と同様の部分には同様
の参照符号を付けて、説明は省略している。
FIG. 3 shows a second embodiment of the present invention. In this embodiment, the same parts as those in the first embodiment are designated by the same reference numerals and the description thereof is omitted.

【0017】第2実施例は、二重導管構造30を有し、
この二重導管構造は、第1実施例の導管14と同様の構
造、機能を有する内側導管部32と、この内側導管部3
2を取り囲む外側導管部34とを包含する。内外の導管
部32、34の間には、環状の通路36が形成されてお
り、外側導管部34の渦流室10の外にある外端部38
は広がっており、ここに被処理粉粒体22を受け入れる
ようになっている。外側導管34の渦流室10内に位置
する内端部40は、内側導管部32の内端との間に材料
出口42を形成している。
The second embodiment has a double conduit structure 30,
This double conduit structure has an inner conduit part 32 having the same structure and function as the conduit 14 of the first embodiment, and this inner conduit part 3
And an outer conduit portion 34 that surrounds 2. An annular passage 36 is formed between the inner and outer conduit portions 32, 34, and an outer end portion 38 of the outer conduit portion 34 outside the swirl chamber 10 is formed.
Has spread and is adapted to receive the granular material 22 to be treated. An inner end 40 of the outer conduit 34 located within the swirl chamber 10 forms a material outlet 42 with the inner end of the inner conduit portion 32.

【0018】第2実施例でも、内側導管32はその長手
軸線方向に移動して、被処理粉粒体に応じて調節できる
ようになっている。
Also in the second embodiment, the inner conduit 32 is moved in the direction of its longitudinal axis so that it can be adjusted according to the granular material to be treated.

【0019】図4は、本発明の第3実施例を示してお
り、この実施例でも、第1、第2の実施例と同様の部分
には同様の参照符号を付して、説明は省略する。
FIG. 4 shows a third embodiment of the present invention. In this embodiment as well, the same parts as those in the first and second embodiments are designated by the same reference numerals and the description thereof will be omitted. To do.

【0020】この第3実施例では、第2実施例と同様
に、内側導管部32と外側導管部34とからなる二重導
管構造30が設けてあるが、この二重導管構造は、その
内端を第2の球形渦流室50で囲まれている。この第2
球形渦流室50は、そのほぼ下半分を半球形のシェル5
2で囲まれており、このシェル52と第2球形渦流室5
0との間には半球形の連絡通路54が形成してある。
In the third embodiment, similar to the second embodiment, the double conduit structure 30 including the inner conduit portion 32 and the outer conduit portion 34 is provided. The end is surrounded by a second spherical swirl chamber 50. This second
The spherical swirl chamber 50 has a hemispherical shell 5 in the lower half thereof.
The shell 52 and the second spherical swirl chamber 5 are surrounded by 2.
A communication path 54 having a hemispherical shape is formed between the two and 0.

【0021】シェル52は、二重導管構造30の連絡通
路36を通じて第2球形渦流室50内へ供給される被処
理粉粒体22とは別の被処理粉粒体を渦流室 内へ導入
する(矢印56で示す)導入口手段24と整合する導管
部分58を有し、この導管部分58は前記の半球形連絡
通路54と連絡している。また、この半球形連絡通路5
4は、第2球形渦流室50の壁を貫いて設けた連絡口6
0とも連絡していて第2球形渦流室50の内部に連通す
る。
The shell 52 introduces into the swirl chamber a target granular material different from the target granular material 22 to be supplied into the second spherical swirl chamber 50 through the communication passage 36 of the double conduit structure 30. It has a conduit portion 58 which is aligned with the inlet means 24 (indicated by arrow 56) and which communicates with said hemispherical communication passage 54. Also, this hemispherical connecting passage 5
4 is a communication port 6 provided through the wall of the second spherical swirl chamber 50.
It is also connected to 0 and communicates with the inside of the second spherical swirl chamber 50.

【0022】この第3実施例では、2種類の被処理粉粒
体22、56が、二回にわたって渦流によって混合され
ながら搬送されるので、より均一な混合を達成すること
ができる。
In the third embodiment, the two types of powder particles 22 and 56 to be treated are conveyed while being mixed by the vortex flow twice, so that more uniform mixing can be achieved.

【0023】[0023]

【発明の効果】以上に述べた構成によれば、円筒管を使
用する従来の構造に比べて、球形の渦流室ではより安定
した渦流を生成でき、しかも逆流を簡単な構造で防止す
ることができる。
According to the structure described above, a more stable vortex flow can be generated in the spherical vortex chamber as compared with the conventional structure using the cylindrical tube, and the backflow can be prevented with a simple structure. it can.

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

【図1】本発明の粉粒体混合搬送装置の第1実施例を示
す垂直断面図である。
FIG. 1 is a vertical sectional view showing a first embodiment of a powder / granular material mixing and conveying apparatus of the present invention.

【図2】図1に示す粉粒体混合搬送装置の、図1の平面
に対して直角の方向に沿った水平断面図である。
FIG. 2 is a horizontal cross-sectional view of the powdery- or granular-material mixing and conveying device shown in FIG. 1 taken along a direction perpendicular to the plane of FIG.

【図3】本発明の粉粒体混合搬送装置の第2実施例を示
す垂直断面図である。
FIG. 3 is a vertical sectional view showing a second embodiment of the powder and granular material mixing and conveying device of the present invention.

【図4】本発明の粉粒体混合搬送装置の第3実施例を示
す垂直断面図である。
FIG. 4 is a vertical sectional view showing a third embodiment of the powder and granular material mixing and conveying device of the present invention.

【符号の説明】[Explanation of symbols]

10 ・・・ 渦流室 12 ・・・ 空気流入口 14 ・・・ 導管 16 ・・・ 入口 18 ・・・ 出口 22 ・・・ 被処理粉粒体 24 ・・・ 導入口手段 26 ・・・ ロータリーバルブ 30 ・・・ 二重導管構造 32 ・・・ 内側導管 34 ・・・ 外側導管 36 ・・・ 環状通路 50 ・・・ 第2球形渦流室 52 ・・・ シェル 54 ・・・ 半球形連絡通路 58 ・・・ 導管部分 10 ... Vortex chamber 12 ... Air inlet 14 ... Conduit 16 ... Inlet 18 ... Outlet 22 ... To-be-processed powder / grain 24 ... Inlet means 26 ... Rotary valve 30 ... Double conduit structure 32 ... Inner conduit 34 ... Outer conduit 36 ... Annular passage 50 ... Second spherical swirl chamber 52 ... Shell 54 ... Hemispherical communication passage 58. ..Conduit parts

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 接線方向の空気流入口を有する球形の渦
流室と、前記空気流入口を含む平面に対して直角に渦流
室の中心を通って延びる導管手段と、渦流室内へ処理す
べき粉粒体を導入する導入口手段とを包含し、この導管
手段が、渦流室内に開口した入口と、渦流室の外部に通
じる出口とを有することを特徴とする粉粒体混合搬送装
置。
1. A spherical vortex chamber having a tangential air inlet, conduit means extending through the center of the vortex chamber at right angles to the plane containing the air inlet, and powder to be treated into the vortex chamber. An inlet / outlet means for introducing particles, wherein the conduit means has an inlet opening into the swirl chamber and an outlet communicating with the outside of the swirl chamber.
【請求項2】 請求項1記載の粉粒体混合搬送装置にお
いて、前記導管手段の入口が前記導入口手段と整合して
おり、また、前記導管手段が軸線方向に移動して前記入
口と前記導入口手段との間隔を調節できるようになって
いることを特徴とする粉粒体混合搬送装置。
2. The powder and granular material mixing and conveying apparatus according to claim 1, wherein the inlet of the conduit means is aligned with the inlet means, and the conduit means moves in the axial direction to move the inlet and the inlet. A powder / granule mixing / conveying device, characterized in that the distance between the powder and granules can be adjusted.
【請求項3】 請求項1記載の粉粒体混合搬送装置にお
いて、前記導管手段が内側導管部と外側導管部とからな
る二重構造となっており、内側導管部が渦流室内に開口
した入口と、渦流室外部に通じる出口とを有し、外側導
管部が内側導管部との間に環状の通路を形成しており、
この通路が前記導入口手段を構成しており、さらに、前
記内側導管部がその軸線方向に移動できるようになって
いることを特徴とする粉粒体混合搬送装置。
3. The powdery-particles mixing and conveying apparatus according to claim 1, wherein the conduit means has a double structure consisting of an inner conduit part and an outer conduit part, and the inner conduit part is an inlet opening into the swirl chamber. And an outlet communicating with the outside of the swirl chamber, and the outer conduit portion forms an annular passage between the inner conduit portion and
This passage constitutes the inlet means, and further, the inner conduit portion is configured to be movable in the axial direction thereof.
【請求項4】 請求項1記載の粉粒体混合搬送装置にお
いて、前記導管手段が、内側導管部と外側導管部とから
なる二重構造導管と、この二重構造導管の内端部を囲む
第2の球形渦流室と、この第2球形渦流室を取り囲む半
球形のシェルとを包含し、このシェルが前記第2球形渦
流室との間に半球形の連絡通路を構成しており、この連
絡通路が前記第2球形渦流室の壁を貫いて設けた連絡口
と連通しており、かつ、前記シェルに設けた導管部分と
連絡しており、シェルのこの導管部分が前記導入口手段
と整合して前記渦流室に開口する入口を有することを特
徴とする粉粒体混合搬送装置。
4. The powder and granular material mixing and conveying apparatus according to claim 1, wherein the conduit means surrounds a dual structure conduit consisting of an inner conduit part and an outer conduit part, and an inner end part of the dual structure conduit. A second spherical swirl chamber and a hemispherical shell surrounding the second spherical swirl chamber, the shell defining a hemispherical communication passage between the second spherical swirl chamber and the second spherical swirl chamber; A communication passage communicates with a communication port provided through the wall of the second spherical swirl chamber and communicates with a conduit portion of the shell, the conduit portion of the shell communicating with the inlet means. An apparatus for mixing and transporting powdery particles, characterized in that it has an inlet that is aligned and opens into the swirl chamber.
JP4087513A 1992-03-12 1992-03-12 Granular body mixing and transporting device Pending JPH0639261A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4087513A JPH0639261A (en) 1992-03-12 1992-03-12 Granular body mixing and transporting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4087513A JPH0639261A (en) 1992-03-12 1992-03-12 Granular body mixing and transporting device

Publications (1)

Publication Number Publication Date
JPH0639261A true JPH0639261A (en) 1994-02-15

Family

ID=13917073

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4087513A Pending JPH0639261A (en) 1992-03-12 1992-03-12 Granular body mixing and transporting device

Country Status (1)

Country Link
JP (1) JPH0639261A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006349538A (en) * 2005-06-17 2006-12-28 Kowa Co Particle supply device
JP4563496B1 (en) * 2009-10-22 2010-10-13 株式会社H&S Microbubble generator

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006349538A (en) * 2005-06-17 2006-12-28 Kowa Co Particle supply device
JP4690790B2 (en) * 2005-06-17 2011-06-01 興和株式会社 Particle feeder
JP4563496B1 (en) * 2009-10-22 2010-10-13 株式会社H&S Microbubble generator
JP2011088079A (en) * 2009-10-22 2011-05-06 H&S Co Ltd Apparatus for generating fine bubble

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