JP2547233Y2 - Nozzle structure - Google Patents

Nozzle structure

Info

Publication number
JP2547233Y2
JP2547233Y2 JP1991046892U JP4689291U JP2547233Y2 JP 2547233 Y2 JP2547233 Y2 JP 2547233Y2 JP 1991046892 U JP1991046892 U JP 1991046892U JP 4689291 U JP4689291 U JP 4689291U JP 2547233 Y2 JP2547233 Y2 JP 2547233Y2
Authority
JP
Japan
Prior art keywords
main
pipe
fluid
control fluid
sub
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 - Lifetime
Application number
JP1991046892U
Other languages
Japanese (ja)
Other versions
JPH04131451U (en
Inventor
剛 石川
Original Assignee
三井鉱山株式会社
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 三井鉱山株式会社 filed Critical 三井鉱山株式会社
Priority to JP1991046892U priority Critical patent/JP2547233Y2/en
Publication of JPH04131451U publication Critical patent/JPH04131451U/en
Application granted granted Critical
Publication of JP2547233Y2 publication Critical patent/JP2547233Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】この考案はノズル構造に関し、特
に、主流体の供給路に制御流体を螺旋状に噴射されるこ
とによって付着流を生じさせて負圧を発生させ、この負
圧によって主流体が螺旋状に供給されるようにし、この
時、主流体中の凝集粒子に剪断作用を生じさせて凝集粒
子を分散させるようにしたノズル構造に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a nozzle structure, in particular, a control fluid is spirally injected into a supply passage of a main fluid to generate an adhering flow to generate a negative pressure. The present invention relates to a nozzle structure in which a body is supplied in a spiral shape, and at this time, a shearing action is generated on aggregated particles in a main fluid to disperse the aggregated particles.

【0002】[0002]

【従来技術およびその問題点】一般に、供給路を流れる
主流体の内部に凝集粒子が位置している場合には、ノズ
ルを通過したのちに凝集粒子を分散する装置を設け、こ
の装置によって主流体中の凝集粒子を分散するようにし
てある。
2. Description of the Related Art In general, when agglomerated particles are located inside a main fluid flowing through a supply passage, a device for dispersing the agglomerated particles after passing through a nozzle is provided. Agglomerated particles inside are dispersed.

【0003】したがって、主流体中の凝集粒子を分散す
るための装置が必要であり、このこめに全体が大型にな
るとともに、全体が高価になってしまうという問題点を
有していた。
[0003] Therefore, an apparatus for dispersing aggregated particles in the main fluid is required, which has the problem that the whole becomes large and the whole becomes expensive.

【0004】この考案の目的は、主流体が流れる供給路
に制御流体を作用させることで、供給路中を主流体が螺
旋状に流れるようにし、この時、主流体中の凝集粒子を
分散させることのできるノズル構造を提供することにあ
る。
An object of the present invention is to cause a control fluid to act on a supply passage through which a main fluid flows, so that the main fluid flows spirally in the supply passage, and at this time, aggregate particles in the main fluid are dispersed. It is an object of the present invention to provide a nozzle structure.

【0005】[0005]

【問題点を解決するための手段】上記の目的を達成する
ためにこの考案は、連結部に向かって順次縮径するとと
もに、主流体が流入する副管と、該副管との連結部より
も内側の部位が最小径をなし、連結部から最小径の部位
に向かって順次縮径するとともに、最小径の部位よりも
内方に向かって順次拡径する主管とを具え、外周に設け
た制御流体供給部と連通するとともに、供給路に連通す
る複数の螺旋状の溝を前記連結部に設け、該溝から前記
主管の主流体の下流側内面に至る壁面をコアンダ効果を
生じさせる湾曲部に形成し、前記制御流体の供給時に前
記副管から凝集粒子を有する主流体を螺旋状に吸引する
とともに、剪断作用を施して分散することを特徴とする
ノズル構造を構成したものである。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention proposes that the diameter is gradually reduced toward the connecting portion.
In addition , from the sub-tube into which the main fluid flows, and the connection portion with the sub-tube
The part inside is also the minimum diameter, and the part with the minimum diameter from the connection part
And gradually reduce the diameter toward
A main pipe having a diameter gradually increasing inward, and a plurality of spiral grooves communicating with a control fluid supply section provided on an outer periphery and communicating with a supply path are provided in the connection section; A wall surface extending to the inner surface on the downstream side of the main fluid is formed in a curved portion that generates the Coanda effect, and is formed at the time of supply of the control fluid.
Spiral suction of the main fluid containing aggregated particles from the secondary pipe
In addition, a nozzle structure is characterized in that the nozzle structure is dispersed by applying a shearing action .

【0006】[0006]

【0007】[0007]

【作用】この考案は上記の手段を採用したことにより、
制御流体供給部に供給された制御流体は、複数の螺旋状
の溝を通って供給路内に流入することにより、制御流体
の噴流流れが螺旋状強制される。そして、制御流体が
主管の湾曲部の表面に付着流を形成すると、主管の内部
が負圧となり、副管からの主流体を吸引し、この場合、
吸引される主流体の流れは制御流体の流れに支配される
ので当然に螺旋状となる。したがって、主流体中の凝集
粒子は高速の螺旋気流中で剪断作用を受け、これにより
凝集粒子は分散されることになる。
[Function] This invention adopts the above-mentioned means,
Control fluid supplied to the control fluid supply, by flowing into the supply passage through a plurality of helical grooves, the jet flow of the control fluid is forced spirally. Then, when the control fluid forms an adherent flow on the surface of the curved portion of the main pipe, the inside of the main pipe becomes a negative pressure and sucks the main fluid from the sub-pipe.
Since the flow of the main fluid to be sucked is governed by the flow of the control fluid, it naturally has a spiral shape. Therefore, the agglomerated particles in the main fluid are subjected to shearing action in the high-speed spiral airflow, whereby the agglomerated particles are dispersed.

【0008】[0008]

【実施例】以下、図面に示すこの考案の実施例について
説明する。図1および図2にはこの考案によるノズル構
造が示されており、このノズル構造は、主管1と副管2
とから構成されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention shown in the drawings will be described below. FIGS. 1 and 2 show a nozzle structure according to the present invention, which comprises a main pipe 1 and a sub pipe 2.
It is composed of

【0009】前記主管1は、中央部に空所3を有する肉
厚をなし、端部に前記空所3を囲むように環状の溝4が
形成され、この溝4の外周側は段部4aに形成されると
ともに、前記溝4は端部の周面に設けられた制御流体の
流入口5に連通している。
The main pipe 1 has a thickness having a cavity 3 at the center, and an annular groove 4 is formed at the end so as to surround the cavity 3. An outer peripheral side of the groove 4 is a step 4a. The groove 4 communicates with a control fluid inlet 5 provided on the peripheral surface of the end.

【0010】そして、前記溝4と空所3との間で形成さ
れる端部は湾曲部6に形成され、一方、前記空所3は前
記湾曲部6に連なる端部が徐々に小径となる湾曲部7に
形成されるとともに、最小径部を介して内方が順次大径
に形成されている。
The end formed between the groove 4 and the cavity 3 is formed in a curved portion 6, while the end of the cavity 3 connected to the curved portion 6 gradually becomes smaller in diameter. In addition to being formed on the curved portion 7, the inner portion is sequentially formed with a larger diameter through the minimum diameter portion.

【0011】一方、前記副管2は、開口部に至るに従っ
て順次縮径する筒状をなすとともに、開口部8に径方向
に拡がるフランジ部9が形成され、このフランジ部9に
は前記開口部8を中心として所定の距離で囲むような突
出部10が一体に設けられ、また、前記開口部8の周縁
部の前記フランジ部9には所定の幅となっている環状の
突部11が設けられ、この突部11には、複数の溝12
が螺旋状に設けられている。
On the other hand, the auxiliary pipe 2 has a cylindrical shape whose diameter is gradually reduced as it reaches the opening, and a flange 9 is formed in the opening 8 so as to expand in the radial direction. A projection 10 surrounding the opening 8 at a predetermined distance is provided integrally, and an annular projection 11 having a predetermined width is provided on the flange 9 around the opening 8. The protrusion 11 has a plurality of grooves 12
Are provided spirally.

【0012】そして、前記主管1と副管2とを接続する
場合には、主管1の溝4の外周側に設けた段部4aに、
前記副管2のフランジ部9に設けた突出部10を位置さ
せ、また、前記主管1と副管2との間隔を保持するため
のシム13を主管1と副管2との間に位置させた状態
で、主管1と副管2とをボルト14で固定して、主管1
と副管2とを同芯に微細な間隔を隔てた状態とする。
When connecting the main pipe 1 and the sub pipe 2, a step 4 a provided on the outer peripheral side of the groove 4 of the main pipe 1
A protrusion 10 provided on the flange portion 9 of the sub pipe 2 is located, and a shim 13 for maintaining an interval between the main pipe 1 and the sub pipe 2 is positioned between the main pipe 1 and the sub pipe 2. In this state, the main pipe 1 and the sub pipe 2 are fixed with bolts 14 and the main pipe 1
And the sub-tube 2 are concentrically spaced at a fine interval.

【0013】すると、前記主管1の溝4と空所3との間
で形成される湾曲部6と、前記副管2の開口部8に設け
た突部11とは当接し、したがって、主管1の溝4の内
部と、主管1の空所3と副管2との内部、すなわち、供
給路とは前記副管2の開口部8に設けた突部11の複数
の螺旋状の溝12によって連通された状態となる。
Then, the curved portion 6 formed between the groove 4 of the main pipe 1 and the space 3 abuts on the projection 11 provided at the opening 8 of the sub pipe 2, and accordingly, the main pipe 1 The inside of the groove 4 and the inside of the space 3 of the main pipe 1 and the inside of the sub pipe 2, that is, the supply path is defined by a plurality of spiral grooves 12 of the projection 11 provided in the opening 8 of the sub pipe 2. The communication is established.

【0014】上記のように組立てた後に前記主管1の側
面に設けた流入口5を介して高圧ガスの制御流体Aを導
入すると、この制御流体Aは主管1の溝4に達して、こ
の溝4を空気だまりとして機能させ、前記副管2の突部
11に設けた複数の螺旋状の溝12を介して図2に示す
ように内部に噴射する。
When the control fluid A of high-pressure gas is introduced through the inflow port 5 provided on the side of the main pipe 1 after assembling as described above, the control fluid A reaches the groove 4 of the main pipe 1 and this groove 4 4 is made to function as an air pool, and is injected into the inside through a plurality of spiral grooves 12 provided in the projection 11 of the sub pipe 2 as shown in FIG.

【0015】この場合、前記複数の溝12が螺旋状に設
けられているので供給された制御流体Aの噴流流れを螺
旋状に強制することになる。
In this case, since the plurality of grooves 12 are provided spirally, the jet flow of the supplied control fluid A is spirally forced.

【0016】そして、高圧ガスである制御流体Aが螺旋
状となって主管1の湾曲部7の表面に付着流を形成し、
すなわち、コアンダ効果を生じることになる。すると前
記主管1の中心部が負圧となり、これにより2次ガスで
ある空気を副管2側から吸引することになる。この場
合、2次ガスは制御流体の流れに支配されるために当然
螺旋状となって前記主管1に流入することになる。
Then, the control fluid A, which is a high-pressure gas, spirals to form an adherent flow on the surface of the curved portion 7 of the main pipe 1,
That is, the Coanda effect occurs. Then, the central portion of the main pipe 1 becomes negative pressure, whereby air as a secondary gas is sucked from the sub pipe 2 side. In this case, since the secondary gas is governed by the flow of the control fluid, the secondary gas naturally flows into the main pipe 1 in a spiral shape.

【0017】したがって、前記副管2を2次ガス側にし
ておけば、2次ガス側である供給される主流体B中の凝
集粒子は高速の螺旋気流中で激しく剪断作用を受け、こ
れにより凝集粒子は分散されることになり、このことが
連続して行われることになる。
Therefore, if the auxiliary pipe 2 is set on the secondary gas side, the aggregated particles in the supplied main fluid B, which is on the secondary gas side, are severely sheared in the high-speed spiral airflow, whereby The agglomerated particles will be dispersed and this will be done continuously.

【0018】図3および図4はこの考案によるノズル構
造の他の実施例を示し、このものにあっては、前記実施
例に示すものが主流体の供給側である副管2の開口部8
の周縁部に突部11を設けて、この突部11に複数の溝
12を螺旋状に設けることで、主管1の湾曲部7の表面
に付着流を生じさせるようにしたが、この実施例に示す
ものにあっては、主管1の端部である湾曲部6に複数の
溝22を螺旋状に設けたものである。
FIGS. 3 and 4 show another embodiment of the nozzle structure according to the present invention. In this embodiment, the one shown in the above embodiment is the opening 8 of the sub pipe 2 which is the main fluid supply side.
A protrusion 11 is provided on the peripheral edge of the main pipe 1, and a plurality of grooves 12 are spirally provided on the protrusion 11, so that an adhesion flow is generated on the surface of the curved portion 7 of the main pipe 1. In the embodiment shown in FIG. 1, a plurality of grooves 22 are spirally provided in a curved portion 6 which is an end of the main pipe 1.

【0019】このように構成した場合であっても制御流
体Aが湾曲部6に設けた複数の螺旋状の溝22を介して
噴流となって流れ、主管1の湾曲部7の表面に付着流を
形成し、すなわち、コアンダ効果を生じることになる。
すると前記主管1の中心部が負圧となり、これにより2
次ガスである空気を副管2側から吸引することになる。
この場合、2次ガスは制御流体の流れに支配されるため
に当然螺旋状となって前記主管1に流入することにな
る。
Even in such a case, the control fluid A flows as a jet through the plurality of spiral grooves 22 provided in the curved portion 6 and adheres to the surface of the curved portion 7 of the main pipe 1. , That is, the Coanda effect occurs.
Then, a negative pressure is applied to the central portion of the main pipe 1, whereby
The air as the next gas is sucked from the auxiliary pipe 2 side.
In this case, since the secondary gas is governed by the flow of the control fluid, the secondary gas naturally flows into the main pipe 1 in a spiral shape.

【0020】そして、前記副管2を2次ガス側にしてお
けば、2次ガス側である供給される主流体B中の凝集粒
子は高速の螺旋気流中で激しく剪断作用を受け、これに
より凝集粒子は分散されることになり、このことが連続
して行われることになる。
If the auxiliary pipe 2 is set on the secondary gas side, the agglomerated particles in the supplied main fluid B on the secondary gas side are severely sheared in a high-speed helical airflow. The agglomerated particles will be dispersed and this will be done continuously.

【0021】[0021]

【考案の効果】この考案は前記のように構成したことに
より、高圧の制御流体が複数の螺旋状の溝を介して供給
路内に螺旋状に強制されて噴流として流れ、しかも、主
管の湾曲部に付着流が生じて主管の内部を負圧にするコ
アンダ効果が発生する。 したがって、コアンダ効果によ
って発生した負圧によって副管から凝集粒子を有する主
流体が螺旋状に吸引されるので、高速の螺旋気流によっ
て凝集粒子が剪断作用を受けて凝集粒子確実に分散さ
れることになる。
According to the present invention, as described above, the high-pressure control fluid is helically forced into the supply path through a plurality of spiral grooves and flows as a jet.
Adhesion flow is generated in the curved part of the pipe, and the pressure inside the main pipe becomes negative.
An under effect occurs. Therefore, due to the Coanda effect
Having agglomerated particles from the secondary pipe due to the negative pressure generated
Since the fluid is drawn in a spiral shape, the high-speed spiral airflow
As a result, the aggregated particles are subjected to the shearing action, and the aggregated particles are surely dispersed.

【0022】しかも、凝集粒子を有する主流体の吸引、
および凝集粒子の分散は高圧の制御流体を供給するだけ
で良いので全体の構造が非常に簡易であるとともに、全
体を安価に製造することができるという効果を有してい
る。
Moreover, suction of the main fluid having the aggregated particles,
In addition, since it is only necessary to supply the high-pressure control fluid to disperse the aggregated particles, the whole structure is very simple and the whole can be manufactured at low cost.

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

【図1】この考案によるノズル構造の実施例を示す概略
縦断面図である。
FIG. 1 is a schematic longitudinal sectional view showing an embodiment of a nozzle structure according to the present invention.

【図2】図1に示すものの副管の開口部に設けた突部を
示す概略図である。
FIG. 2 is a schematic view showing a protrusion provided at an opening of a sub-tube shown in FIG.

【図3】この考案によるノズル構造の他の実施例の主管
を示す概略図である。
FIG. 3 is a schematic view showing a main pipe of another embodiment of the nozzle structure according to the present invention.

【図4】図3の概略縦断面図である。FIG. 4 is a schematic longitudinal sectional view of FIG.

【符号の説明】[Explanation of symbols]

1……主管 2……副管 3……空所 4……溝 4a……段部 5……流入口 6、7……湾曲部 8……開口部 9……フランジ部 10……突出部 11……突部 12、22……溝 13……シム 14……ボルト A……制御流体 B……主流体 DESCRIPTION OF SYMBOLS 1 ... Main pipe 2 ... Sub pipe 3 ... Vacancy 4 ... Groove 4a ... Step part 5 ... Inflow port 6, 7 ... Curved part 8 ... Opening part 9 ... Flange part 10 ... Projection part 11: Projection 12, 22: Groove 13: Shim 14: Bolt A: Control fluid B: Main fluid

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 連結部に向かって順次縮径するととも
に、主流体が流入する副管と、該副管との連結部よりも
内側の部位が最小径をなし、連結部から最小径の部位に
向かって順次縮径するとともに、最小径の部位よりも内
方に向かって順次拡径する主管とを具え、外周に設けた
制御流体供給部と連通するとともに、供給路に連通する
複数の螺旋状の溝を前記連結部に設け、該溝から前記主
管の主流体の下流側内面に至る壁面をコアンダ効果を生
じさせる湾曲部に形成し、前記制御流体の供給時に前記
副管から凝集粒子を有する主流体を螺旋状に吸引すると
ともに、剪断作用を施して分散することを特徴とするノ
ズル構造。
1. The method according to claim 1, wherein the diameter is sequentially reduced toward the connecting portion.
And a connecting portion between the sub-tube into which the main fluid flows and the sub-tube.
The inner part forms the minimum diameter, from the connecting part to the part with the minimum diameter
The diameter gradually decreases toward the inside, and
A main pipe that sequentially increases in diameter toward the direction, communicates with a control fluid supply section provided on the outer periphery, and provides a plurality of spiral grooves communicating with the supply path in the connection section, and from the groove, A wall surface reaching the inner surface on the downstream side of the main fluid is formed in a curved portion that causes a Coanda effect, and the supply of the control fluid is performed when the control fluid is supplied.
When the main fluid with aggregated particles is sucked in spiral form from the secondary pipe
Both have a nozzle structure characterized by dispersing by applying a shearing action .
JP1991046892U 1991-05-24 1991-05-24 Nozzle structure Expired - Lifetime JP2547233Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991046892U JP2547233Y2 (en) 1991-05-24 1991-05-24 Nozzle structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991046892U JP2547233Y2 (en) 1991-05-24 1991-05-24 Nozzle structure

Publications (2)

Publication Number Publication Date
JPH04131451U JPH04131451U (en) 1992-12-03
JP2547233Y2 true JP2547233Y2 (en) 1997-09-10

Family

ID=31926228

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991046892U Expired - Lifetime JP2547233Y2 (en) 1991-05-24 1991-05-24 Nozzle structure

Country Status (1)

Country Link
JP (1) JP2547233Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011110512A (en) * 2009-11-27 2011-06-09 Ricoh Co Ltd Powder dispersion device, classification apparatus, classification method, and method for manufacturing toner

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999033598A1 (en) * 1997-12-25 1999-07-08 Fukuda Metal Foil & Powder Co., Ltd. Method of producing metal powder

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01123012A (en) * 1987-11-09 1989-05-16 Kawasaki Steel Corp Nozzle for manufacturing fine powder

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011110512A (en) * 2009-11-27 2011-06-09 Ricoh Co Ltd Powder dispersion device, classification apparatus, classification method, and method for manufacturing toner

Also Published As

Publication number Publication date
JPH04131451U (en) 1992-12-03

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