JPH06182194A - Device for producing stream of fine particle - Google Patents
Device for producing stream of fine particleInfo
- Publication number
- JPH06182194A JPH06182194A JP34176692A JP34176692A JPH06182194A JP H06182194 A JPH06182194 A JP H06182194A JP 34176692 A JP34176692 A JP 34176692A JP 34176692 A JP34176692 A JP 34176692A JP H06182194 A JPH06182194 A JP H06182194A
- Authority
- JP
- Japan
- Prior art keywords
- generation chamber
- gas
- fine particle
- fine particles
- chamber
- 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
Links
Landscapes
- Cyclones (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明はガス(気体)の流れに乗
って移動する微粒子の散乱する光を観測してガス流(流
速及び方向)を計測するレーザードップラー流速計やレ
ーザーライトシートに用いられる微粒子流発生装置に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is used for a laser Doppler velocimeter or a laser light sheet for measuring gas flow (flow velocity and direction) by observing scattered light of fine particles moving along with gas flow. And a particulate flow generator.
【0002】[0002]
【従来の技術】レーザードップラー流速計やレーザーラ
イトシートに用いられる微粒子(数μm〜100μm)
の発生装置としては粉流体容器に挿入された2重構造の
ダクトを有し、第1、第2ダクトの間にノズルを設ける
と共に第2ダクトの先端に吸引ノズルを設け、該第1ダ
クトに供給される圧縮空気の第2ダクトへの移動による
負圧により該吸引ノズルを介して前記粉体容器内の粉体
を吸引する粉体吸引手段(特開昭62−233738)
が公知である。2. Description of the Related Art Fine particles (several μm to 100 μm) used for laser Doppler velocimeter and laser light sheet
As a generator of the above, it has a double-structured duct inserted in a powder fluid container, a nozzle is provided between the first and second ducts, and a suction nozzle is provided at the tip of the second duct. Powder suction means for sucking the powder in the powder container through the suction nozzle by the negative pressure caused by the movement of the compressed air supplied to the second duct (JP-A-62-233738).
Is known.
【0003】[0003]
【発明が解決しようとする課題】しかし、上記装置にお
いては、負圧を利用して吸引ノズルから粒体を吸引する
ため、粒体を平らな面で吸引することはむずかしく、ノ
ズルに近い部分に凹部ができて、均一な微粒子流を長時
間発生することができない。又、公知例は粉体のレベル
の変化に対応させて吸引ノズルとの位置関係を制御する
ため、この制御技術が実際には大変むずかしく、装置も
複雑化して高価になる。However, in the above-mentioned device, since the particles are sucked from the suction nozzle by using the negative pressure, it is difficult to suck the particles on a flat surface, and the portion near the nozzle is difficult to suck. Since a concave portion is formed, a uniform fine particle flow cannot be generated for a long time. Further, in the known example, since the positional relationship with the suction nozzle is controlled according to the change of the powder level, this control technique is actually very difficult, and the apparatus becomes complicated and expensive.
【0004】本発明の目的は、均一な微粒子流を長時間
安定して発生させることのできる微粒子流発生装置を提
供することである。An object of the present invention is to provide a particle flow generator capable of stably generating a uniform particle flow for a long time.
【0005】[0005]
【課題を解決するための手段】本発明に係る微粒子流発
生装置の構成は次のとおりである。The structure of the particle flow generator according to the present invention is as follows.
【0006】微粒子流発生室を円筒状に形成すると共
に、この発生室内底部に微粒子を容れるように構成した
こと、前記発生室内に対する気体導入口を接線方向に取
り付けると共にこの気体導入口を発生室内上下方向に複
数箇所配置したこと、前記気体導入口に至る気体導入管
に夫々気体調節バルブを取り付けたこと、前記発生室の
上部に微粒子流導出管を取り付けたこと、を特徴とする
微粒子流発生装置。The fine particle flow generation chamber is formed in a cylindrical shape, and the fine particles are contained in the bottom of the generation chamber. The gas introduction port for the generation chamber is attached tangentially, and the gas introduction port is located above and below the generation chamber. A fine particle flow generator characterized in that it is arranged at a plurality of positions in the direction, a gas adjusting valve is attached to each of the gas introducing pipes reaching the gas introducing port, and a fine particle flow outlet pipe is attached to the upper part of the generating chamber. .
【0007】[0007]
【作用】発生室内の底部には粒径の整った微粒子が容れ
られ、気体導入管からは加圧気体例えば空気が発生室内
において上下複数箇所から導入される。導入された気体
は気体導入口が発生室内において接線方向に向けられて
いるため、接線方向に噴出し、発生室内に旋回流をつく
りながら圧力の低い発生室内上方に上昇し、この間に微
粒子をまき上げる。まき上げられた微粒子は気体中に混
入し、微粒子導出管を経由して発生室外に導き出され、
被測定室或いは器内等に送り込まれる。In the bottom of the generating chamber, fine particles having a uniform particle size are contained, and pressurized gas such as air is introduced from a plurality of upper and lower positions in the generating chamber through the gas introducing pipe. The introduced gas has its gas inlet directed tangentially in the generation chamber, so it is ejected in the tangential direction and rises above the generation chamber where the pressure is low while creating a swirling flow in the generation chamber. increase. The fine particles that have been thrown in are mixed in the gas, and are guided out of the generation chamber via the fine particle discharge pipe.
It is sent to the room to be measured or inside the container.
【0008】微粒子の混入量は発生室内に導入される気
体の流速により決まるので、この混入量を調節バルブを
調節することにより、発生室内に均一な施回流を安定し
てつくることができる。Since the mixing amount of the fine particles is determined by the flow velocity of the gas introduced into the generation chamber, by adjusting the mixing valve with a control valve, a uniform circulating flow can be stably formed in the generation chamber.
【0009】[0009]
【実施例】図1において、1は円筒状に形成された発生
室、2は発生室1内底部に容れられた微粒子、3は気体
導入管にして、この気体導入管3は分岐管4、4a、4
bで分岐され、発生室1内において、前記微粒子2より
も上部であって、接線方向に向けて形成され、かつ上下
に配置された気体導入口5、5a、5bに夫々接続され
ている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In FIG. 1, 1 is a cylindrical generating chamber, 2 is fine particles contained in the bottom of the generating chamber 1, 3 is a gas introducing pipe, and this gas introducing pipe 3 is a branch pipe 4. 4a, 4
It is branched at b and is connected to the gas introduction ports 5, 5a, 5b which are formed above the fine particles 2 in the tangential direction in the generation chamber 1 and are arranged vertically.
【0010】6は発生室1の上部中央から延長された制
御弁8付の微粒子流導出管にして、この先は被測定室に
継がれている。The reference numeral 6 designates a fine particle flow outlet pipe with a control valve 8 extending from the center of the upper portion of the generation chamber 1, and this tip is connected to the chamber to be measured.
【0011】7、7a、7bは分岐管4、4a、4bに
夫々取り付けられた調節弁である。Reference numerals 7, 7a and 7b are control valves attached to the branch pipes 4, 4a and 4b, respectively.
【0012】上記実施例において、気体導入管3から導
入された空気は、分岐管4、4a、4bから気体導入口
5、5a、5bを経由して発生室1内に噴出する。この
際、気体導入口5、5a、5bが発生室1内において接
線方向を向いているため、流体した気体は旋回流となっ
て発生室1内を旋回しながら上昇し、この間に微粒子を
まき上げる。まき上げられた微粒子は気体中に混入し、
導出管6から発生室1外に導き出される。この導き出さ
れる微粒子流において、微粒子の混入量を調節する場合
には、調節弁7、7a、7bを調節して気体導入口5、
5a、5bから発生室1内に導入される気体の量を調節
する。なお、上記実施例の場合、気体導入口は3ケ所で
あるが、2ケ所でも構わない。In the above embodiment, the air introduced from the gas introduction pipe 3 is jetted into the generation chamber 1 from the branch pipes 4, 4a, 4b via the gas introduction ports 5, 5a, 5b. At this time, since the gas inlets 5, 5a, 5b are oriented tangentially in the generation chamber 1, the fluidized gas becomes a swirling flow and rises while swirling in the generation chamber 1, and the fine particles are scattered during this period. increase. The fine particles that have been thrown in are mixed in the gas,
It is led out of the generation chamber 1 from the lead-out pipe 6. When adjusting the mixing amount of fine particles in the derived fine particle flow, the control valves 7, 7a, 7b are adjusted to adjust the gas introduction port 5,
The amount of gas introduced into the generation chamber 1 from 5a and 5b is adjusted. In addition, in the case of the above-mentioned embodiment, the gas introduction ports are provided at three places, but it may be provided at two places.
【0013】[0013]
【発明の効果】本発明は以上のように、発生室内底部に
微粒子を容れ、この発生室内上下において気体の旋回流
を発生させることにより、内部の微粒子をまき上げて均
一な微粒子流を長時間安定して発生させることができ
る。又、本発明は発生室内に気体の導入口を接線方向に
向けて設けるという手段だけで旋回流を発生させるの
で、発生装置の構造は極めてシンプルとなり小型化が可
能であると共に、安価に提供できる。又、発生室内上下
方向に複数の気体導入口を設け、この気体導入口から噴
出する気体の量を調節弁で調節することにより、施回流
を調節して任意の密度の微粒子流を安定的に発生させる
ことができる。INDUSTRIAL APPLICABILITY As described above, according to the present invention, the fine particles are contained in the bottom of the generation chamber, and the swirling flow of gas is generated above and below the generation chamber to raise the fine particles inside and to generate a uniform fine particle flow for a long time. It can be generated stably. Further, according to the present invention, since the swirling flow is generated only by providing the gas inlet in the generation chamber in the tangential direction, the structure of the generator is extremely simple and can be downsized, and can be provided at low cost. . In addition, by providing a plurality of gas inlets in the vertical direction of the generation chamber and adjusting the amount of gas ejected from the gas inlets with a control valve, the swirling flow is adjusted to stabilize a fine particle flow of any density. Can be generated.
【図1】本発明に係る発生装置の斜視図。FIG. 1 is a perspective view of a generator according to the present invention.
【図2】気体導入口の位置関係を示す発生室の断面図。FIG. 2 is a sectional view of a generation chamber showing a positional relationship of gas inlets.
【符号の説明】 1 発生室 2 微粒子 3 気体導入管 4、4a、4b 分岐管 5、5a、5b 気体導入口 6 微粒子流導出管 7、7a、7b 調節弁 8 制御弁[Explanation of Codes] 1 Generation chamber 2 Fine particles 3 Gas introduction pipe 4, 4a, 4b Branch pipe 5, 5a, 5b Gas introduction port 6 Fine particle flow discharge pipe 7, 7a, 7b Control valve 8 Control valve
Claims (1)
に、この発生室内底部に微粒子を容れるように構成した
こと、 前記発生室内に対する気体導入口を接線方向に取り付け
ると共にこの気体導入口を発生室内上下方向に複数箇所
配置したこと、 前記気体導入口に至る気体導入管に夫々気体調節バルブ
を取り付けたこと、 前記発生室の上部に微粒子流導出管を取り付けたこと、 を特徴とする微粒子流発生装置。1. A fine particle flow generation chamber is formed in a cylindrical shape and fine particles are contained in the bottom of the generation chamber, and a gas introduction port for the generation chamber is attached tangentially and the gas introduction port is generated. The fine particle flow is characterized in that a plurality of locations are arranged in the vertical direction of the room, a gas regulating valve is attached to each of the gas introduction pipes reaching the gas introduction port, and a fine particle flow outlet pipe is attached to the upper part of the generation chamber. Generator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34176692A JPH06182194A (en) | 1992-12-22 | 1992-12-22 | Device for producing stream of fine particle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34176692A JPH06182194A (en) | 1992-12-22 | 1992-12-22 | Device for producing stream of fine particle |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06182194A true JPH06182194A (en) | 1994-07-05 |
Family
ID=18348600
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP34176692A Pending JPH06182194A (en) | 1992-12-22 | 1992-12-22 | Device for producing stream of fine particle |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06182194A (en) |
-
1992
- 1992-12-22 JP JP34176692A patent/JPH06182194A/en active Pending
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