JPS58109174A - Apparatus for separating and injecting particle - Google Patents

Apparatus for separating and injecting particle

Info

Publication number
JPS58109174A
JPS58109174A JP20875281A JP20875281A JPS58109174A JP S58109174 A JPS58109174 A JP S58109174A JP 20875281 A JP20875281 A JP 20875281A JP 20875281 A JP20875281 A JP 20875281A JP S58109174 A JPS58109174 A JP S58109174A
Authority
JP
Japan
Prior art keywords
particles
cylinder
circumferential side
separating
fixed
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
JP20875281A
Other languages
Japanese (ja)
Inventor
不可止 浦上
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 JP20875281A priority Critical patent/JPS58109174A/en
Publication of JPS58109174A publication Critical patent/JPS58109174A/en
Pending legal-status Critical Current

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  • Combined Means For Separation Of Solids (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、流体流に混入されて移送されている粒体を流
体流から分離しかつその流側流の外部へ前記粒体を排出
する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for separating particles being transported in a fluid stream from the fluid stream and discharging said particles out of the downstream stream.

従来、粒体を気体流又は液体流に混入して移送する時、
前記粒体を流体流から分離する装置としてサイクロン等
の大型の分離器を必要としていた。さらにその分離器の
外へ前1’i3粒体を排出する場合においてはロータリ
ーフィーダ等の気密式の排出機を必要としていた。しか
しそのロータリーフィーダも粒体のかみ込みによる作動
不良や摩耗による気密性不良など故障が多い欠点を有し
ている。
Conventionally, when transporting particles by mixing them into a gas or liquid stream,
A large separator such as a cyclone is required as a device to separate the particles from the fluid stream. Furthermore, when discharging the pre-1'i3 particles out of the separator, an airtight discharge machine such as a rotary feeder is required. However, the rotary feeder also has the drawback of frequent failures such as malfunction due to particle entrapment and poor airtightness due to wear.

本発明は、流体流から粒体を分離する機能とその流体流
の外部へ前記粒体を排出する機能を兼ね備えしかも非常
にコン1パクトで故障の少ない構造の粒体の分離、排出
装置を得ることを目的としている。
The present invention provides a particle separating and discharging device that has both the function of separating particles from a fluid stream and the function of discharging the particles to the outside of the fluid stream, and has a very compact structure and a structure with few failures. The purpose is to

本発明を実施例の図面にもとづいて説明すると、第1図
および第2図において、一方の側面が開口している円筒
状の分1111i1/は開口し、ていない他方の側面が
モーター2の軸に固定されている。分1ife/は円周
側面に多数個の、小孔l/を有し、又開口側面の端部の
全周にブラシ12を植設され、かつ又開口していない側
面はつば13を有している。
To explain the present invention based on drawings of embodiments, in FIGS. 1 and 2, a cylindrical portion 1111i1/ with one side open is open, and the other side is the shaft of the motor 2. is fixed. The minute 1ife/ has a large number of small holes l/ on the circumferential side, a brush 12 is planted around the entire circumference of the end of the open side, and the unopened side has a collar 13. ing.

固定1i!3はその円周側面にスリット状の粒体の射出
口3/を有している。固定筒3の一方の側面にはモータ
ー2が固定された側板グが装着されており、又他方の側
面には粒体が混入した流体が流入するいわゆる粒体の流
入管Sが装着されている。この粒体の流入管Sの固定W
J3と対面する部分は2重管構造となっており、粒体が
分離された後の流体が流出するいわゆる流体の流出管名
が粒体の流入管Sの内側にそう人されている。この流体
の流入管乙の開口面は分11!/の開口側面と対面して
おり、その開口面の端部にはブラシ12が密着している
。なおこのブラシ12は粒体が流体の流出管6中に流入
しない様にシール機能を有するものであるが同様の機能
を有するものがあればブラシでなくてもよい。
Fixed 1i! 3 has a slit-shaped particle injection port 3/ on its circumferential side. A side plate to which the motor 2 is fixed is attached to one side of the fixed cylinder 3, and a so-called granule inflow pipe S through which fluid mixed with granules flows is attached to the other side. . Fixing W of the inflow pipe S of this granule
The part facing J3 has a double pipe structure, and the name of the so-called fluid outflow pipe through which the fluid flows out after the granules are separated is written inside the inlet pipe S of the granules. The opening surface of this fluid inflow pipe B is 11! The brush 12 is in close contact with the end of the opening. Although this brush 12 has a sealing function to prevent particles from flowing into the fluid outflow pipe 6, it does not need to be a brush as long as it has a similar function.

上記のように構成された装置において、流体の流出管乙
に吸引プロワと連通されたホースjが接続され、又粒体
の流入管Sには先端に吸引ノズルが装着されたホース7
が接続されているものとすると、吸引プロワの作動によ
り吸引ノズルからホース7、粒体の流入管51分111
Q/の小孔ll、流体の流出管6、ホースgを通って吸
引プロワに至6大気流が発生する。そこで前記吸引ノズ
ルより大気と共に粒体を吸引させてやると、粒径が大き
くかつ重い粒体は回転する分Fi1mlの小孔//を通
過できず逆に分lit筒lによりはねとばされて固定筒
3の射出口3/より固定筒3の外へ射出されるものであ
る。なお固定lll3の内こうの圧力は大気圧以下であ
るので射出口3ノより大気が流入し粒体の射出を妨げる
ものであるが、回転する分離筒/により粒体が射出口3
ノを飛び出すのに十分な遠心力すなわち速度を付与され
れば問題はない。第3図は粒体に作用する遠心力を増大
させる為に分11筒/の円周側面の外側に羽根板/グを
設けたことを示している。上記のような工夫により粒体
に作用する遠心力が増大し粒体の速度が増加すると、固
定fI3の射出口31の開口面積を小さくしても単位時
間当りの粒体の射出量は変わらず、−万射出口31の開
口面積が小さくなったことにより射出口31から固定筒
3の内こうへ流入する大気の量が減少し、その減少した
分だけ前記吸引ノズルより吸引する欠配の量が増加する
ので粒体の移送量を増加させることができる。なお分離
筒lの小孔//の開口面積の増減と円周側面の周速度の
増減により分離筒lにより分離可能な粒体の粒度を任意
の粒度に設定することができるものである。
In the apparatus configured as described above, a hose j communicating with a suction blower is connected to the fluid outflow pipe B, and a hose 7 having a suction nozzle attached to the tip is connected to the granule inflow pipe S.
is connected, the operation of the suction blower causes the suction nozzle to flow through the hose 7 and the granule inflow pipe 51 minutes 111.
An atmospheric flow is generated through the small hole Q/, the fluid outflow pipe 6, and the hose g to the suction blower. Therefore, when the particles are sucked together with the air from the suction nozzle, the large and heavy particles cannot pass through the small hole of 1ml Fi due to rotation, and are instead blown away by the lit cylinder. The liquid is then injected out of the fixed cylinder 3 from the injection port 3/ of the fixed cylinder 3. Note that since the pressure inside the stationary 1ll3 is below atmospheric pressure, the atmosphere flows in from the injection port 3 and prevents the injection of the particles.
There is no problem as long as sufficient centrifugal force, or speed, is applied to make the object fly out. FIG. 3 shows that a vane plate/g is provided on the outside of the circumferential side of the cylinder in order to increase the centrifugal force acting on the grains. When the centrifugal force acting on the granules increases and the speed of the granules increases due to the above measures, the amount of granules injected per unit time remains the same even if the opening area of the injection port 31 of the fixed fI3 is reduced. , - Due to the reduction in the opening area of the injection port 31, the amount of air flowing from the injection port 31 into the inner wall of the fixed cylinder 3 is reduced, and the amount of air sucked from the suction nozzle is equal to the reduced amount. Since this increases, the amount of particles transferred can be increased. Note that the particle size of the particles that can be separated by the separation tube 1 can be set to an arbitrary particle size by increasing or decreasing the opening area of the small hole // of the separation tube 1 and by increasing or decreasing the circumferential speed of the circumferential side surface.

上記は大気流による粒体の吸引移送時に粒体を大気流か
ら分離しかつ大気流の外へ射出する本発明の一実施例を
述べたものであるが、本発明は大気流による粒体の圧送
時に粒体を大気流から分離しかつ大気流の外へ射出する
手段として用いてもよい。さらに本発明は大気以外の気
体や液体と粒体の混合流から粒体を分離しその流体の流
れの外へその分離した粒体を射出する手段として利用し
うるものである。
The above describes an embodiment of the present invention in which the particles are separated from the atmospheric flow and injected out of the atmospheric flow when the particles are suctioned and transferred by the atmospheric flow. It may also be used as a means of separating the particles from the atmospheric flow and ejecting it out of the atmospheric flow during pumping. Furthermore, the present invention can be used as a means for separating particles from a mixed flow of particles and gas or liquid other than the atmosphere and injecting the separated particles out of the fluid flow.

本発明は上記のように流体流から粒体を分離する機能と
その流体流の外部へ前記粒体を排出する機能を兼ね備え
て非常にコンパクトであり、しかも構造が簡単で故障が
少ないので可搬式の粒体の分離、射出装置として最適で
ある。
As described above, the present invention has both the function of separating particles from a fluid stream and the function of discharging the particles to the outside of the fluid stream, and is very compact.Moreover, the structure is simple, there are few failures, and it is portable. Ideal for separating and injecting granules.

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

第1図は本発明の一実施例の縦断面図、第2図は分@筒
および固定筒の実施態様を示す斜視図、第3図は分lI
l簡の別の実施態様を示す斜視図である。 特許出願人 浦 上 不可止 31 第3図 411−
FIG. 1 is a longitudinal cross-sectional view of an embodiment of the present invention, FIG. 2 is a perspective view showing an embodiment of a portion tube and a fixed tube, and FIG.
FIG. 7 is a perspective view showing another embodiment of the 1-sheet. Patent Applicant: Urakami Noki 31 Figure 3 411-

Claims (1)

【特許請求の範囲】 1、円周側面に多数個の孔またはスリットを有する筒状
の回転分Ill箇と、前記回転分ll箇を収納し円周側
面に粒体の射出口を有する筒状の固定筒と、前記回転分
層筒と固定筒の間の空間と連通された粒体の流入管と、
前記回転分II筒の内こうと連通された粒体が分離、除
去された後の流体の流出管とを備えたことを特徴とする
粒体の分離、射出装置。 2、回転分S筒の円周側面の外側に羽根板が固定された
ことを特徴とする特許請求の範囲第1項記載の装置。
[Scope of Claims] 1. A cylindrical rotation part Ill having a large number of holes or slits on its circumferential side, and a cylindrical shape housing the rotation parts and having a particle injection port on its circumferential side. a fixed cylinder; a granule inflow pipe communicating with the space between the rotating layer separating cylinder and the fixed cylinder;
A granule separation and injection device characterized by comprising an outlet pipe for fluid after the granules are separated and removed, communicating with the inner cavity of the rotational portion II cylinder. 2. The device according to claim 1, characterized in that a vane plate is fixed to the outside of the circumferential side of the rotation S cylinder.
JP20875281A 1981-12-23 1981-12-23 Apparatus for separating and injecting particle Pending JPS58109174A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20875281A JPS58109174A (en) 1981-12-23 1981-12-23 Apparatus for separating and injecting particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20875281A JPS58109174A (en) 1981-12-23 1981-12-23 Apparatus for separating and injecting particle

Publications (1)

Publication Number Publication Date
JPS58109174A true JPS58109174A (en) 1983-06-29

Family

ID=16561489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20875281A Pending JPS58109174A (en) 1981-12-23 1981-12-23 Apparatus for separating and injecting particle

Country Status (1)

Country Link
JP (1) JPS58109174A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003504176A (en) * 1999-07-14 2003-02-04 アストラゼネカ・アクチエボラーグ Filter device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5594614A (en) * 1979-01-12 1980-07-18 Taisei Corp Separating and removing device for foreign matter in fluid

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5594614A (en) * 1979-01-12 1980-07-18 Taisei Corp Separating and removing device for foreign matter in fluid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003504176A (en) * 1999-07-14 2003-02-04 アストラゼネカ・アクチエボラーグ Filter device

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