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JP2668070B2 - Weightless powder classification method and apparatus - Google Patents
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JP2668070B2 - Weightless powder classification method and apparatus - Google Patents

Weightless powder classification method and apparatus

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Publication number
JP2668070B2
JP2668070B2 JP5343542A JP34354293A JP2668070B2 JP 2668070 B2 JP2668070 B2 JP 2668070B2 JP 5343542 A JP5343542 A JP 5343542A JP 34354293 A JP34354293 A JP 34354293A JP 2668070 B2 JP2668070 B2 JP 2668070B2
Authority
JP
Japan
Prior art keywords
powder
weightless
transfer tube
laminar flow
flow
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 - Fee Related
Application number
JP5343542A
Other languages
Japanese (ja)
Other versions
JPH07163906A (en
Inventor
香津雄 堤
友昭 高田
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.)
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo KK
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 Kawasaki Jukogyo KK filed Critical Kawasaki Jukogyo KK
Priority to JP5343542A priority Critical patent/JP2668070B2/en
Publication of JPH07163906A publication Critical patent/JPH07163906A/en
Application granted granted Critical
Publication of JP2668070B2 publication Critical patent/JP2668070B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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、粉体又は粉粒体(以
下、単に粉体という)を気流搬送して高精度の分級を行
う方法及び装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for carrying out a powder or a powder or granular material (hereinafter, simply referred to as a powder) by air flow for highly accurate classification.

【0002】[0002]

【従来の技術】従来の地球上の風力分級装置として、サ
イクロンやバーチャルインパクターが知られている(昭
和56年12月15日、日刊工業新聞社発行「粉体工学
用語辞典」第22頁、第118頁、第119頁参照)。
このサイクロンやバーチャルインパクターにおいては、
粉粒体を気流搬送し、気流の方向を変えて、大径粒子は
慣性力が大きいので気流のようには方向を変えず、小径
粒子は気流と同じような軌跡を描くことを利用して分級
する。なお、サイクロンでは、慣性力の上に遠心力が加
わり、大径粒子は分離されてサイクロン内の下部に移動
・落下する。
2. Description of the Related Art Cyclones and virtual impactors are known as conventional terrestrial wind classifiers (December 15, 1981, Nikkan Kogyo Shimbun, "Powder Engineering Glossary", p. 22, (See pages 118, 119).
In this cyclone and virtual impactor,
By transporting powdered particles in an air stream and changing the direction of the air stream, large particles have a large inertial force, so they do not change direction like air streams, but small particles use the same trajectory as the air stream. Classify. In the cyclone, centrifugal force is applied on top of the inertial force, and large-diameter particles are separated and move and fall to the lower part in the cyclone.

【0003】[0003]

【発明が解決しようとする課題】地球上には重力加速度
が存在するために、粉粒体を気流搬送するためには、粉
粒体が重力に抗して搬送される終端速度以上の気流の線
速度が必要となる。ところが、終端速度ではその気流自
体が乱流状態となり、粉粒体に乱れが生じて、粉粒体は
蛇行する。また、重力加速度の影響を受けて、気相中の
粉粒体は不安定な分布及び偏流が生じ、このため、分級
効率が低く、分級の精度が悪くなる。
Since gravitational acceleration exists on the earth, in order to convey a granular material in an air stream, an air flow at a speed equal to or higher than the terminal velocity at which the granular material is conveyed against gravity is required. Linear velocity is required. However, at the terminal velocity, the air flow itself becomes a turbulent state, causing turbulence in the granular material, and the granular material meanders. Further, under the influence of the gravitational acceleration, the powdery and granular materials in the gas phase have an unstable distribution and a drift, so that the classification efficiency is low and the classification accuracy is deteriorated.

【0004】本発明は上記の点に鑑みなされたもので、
本発明の目的は、重力加速度による粉体の偏流及び乱流
域による粉体の蛇行流をなくすために、無重力下又は微
小重力下にて層流流体中に滞電粒子を乗せ、さらに電場
又は磁場をかけて粒体を精度良く分級する方法及び装置
を提供することにある。
[0004] The present invention has been made in view of the above points,
An object of the present invention is to put non-charged particles in a laminar fluid in zero gravity or under microgravity in order to eliminate the drift of the powder due to gravitational acceleration and the meandering flow of the powder due to a turbulent region, and further to apply an electric field or magnetic field. And to provide a method and an apparatus for accurately classifying the granules.

【0005】[0005]

【課題を解決するための手段及び作用】上記の目的を達
成するために、本発明の無重力粉体分級方法は、滞電粉
体を無重力下又は微小重力下にて層流で気流搬送し、こ
の層流に電場又は磁場をかけて粉体を分級することを特
徴としている。
In order to achieve the above object, a method for classifying weightless powder according to the present invention comprises the steps of: transporting a static-charged powder in a laminar flow under zero gravity or microgravity; An electric or magnetic field is applied to the laminar flow to classify the powder.

【0006】また、本発明の無重力分級装置は、無重力
室内に粉体気流搬送管を配置し、この粉体気流搬送管の
一端に滞電粉体供給手段及び送風機を接続し、この粉体
気流搬送管内の他端に粉体分級手段を設け、この粉体気
流搬送管の途中に電場付与手段又は磁場付与手段を配置
したことを特徴としている。
Further, in the weightless classification apparatus of the present invention, a powder airflow conveying pipe is arranged in a weightless chamber, and one end of the powder airflow conveying pipe is connected to an electrostatically charged powder supply means and a blower, and the powder airstream is connected. A powder classification means is provided at the other end in the transport pipe, and an electric field applying means or a magnetic field applying means is arranged in the middle of the powder air flow transport pipe.

【0007】無重力下又は微小重力下では、空塔速度の
低い層流で粉体を気流搬送することができる。層流で
は、粉体粒子は一直線に進むので、予め粉体を滞電させ
ておくか、又は粉体を滞電させつつ粉体気流搬送管(ダ
クト)内に流し、この粉体気流搬送管に電場又は磁場を
加えると、粉体の質量に反比例した加速度が生じ、これ
によって粉体は分級される。
Under zero gravity or microgravity, powder can be conveyed by laminar flow having a low superficial velocity. In the laminar flow, the powder particles travel in a straight line, so that the powder is charged beforehand, or the powder is charged while flowing into the powder flow carrier pipe (duct). When an electric or magnetic field is applied to the powder, an acceleration is generated that is inversely proportional to the mass of the powder, whereby the powder is classified.

【0008】[0008]

【実施例】以下、図面を参照して本発明の好適な実施例
を詳細に説明する。ただし、この実施例に記載されてい
る構成機器の形状、その相対配置などは、とくに特定的
な記載がない限りは、本発明の範囲をそれらのみに限定
する趣旨のものではなく、単なる説明例にすぎない。 実施例1 図1は本発明の無重力粉体分級装置の一実施例で、電場
をかける場合を示している。10は無重力室で、ロケッ
ト、落下塔、放物線を描いて飛行する航空機などであ
る。この無重力室10内に粉体気流搬送管12(ダク
ト)を配置し、この気流搬送管12の一端に滞電粉体供
給手段14及び送風機16を接続している。滞電粉体供
給手段14としては、例えば、下部に切り出し弁18を
備えた粉体貯槽20に、さらに高電圧印加手段22を設
けたものを挙げることができる。なお、粉体を層流で供
給しながら、気流搬送管12に高電圧をかけて粉体を滞
電させるように構成することも可能である。粉体を気流
搬送管12内に入れるために、例えば、送風機16から
分岐した気体を粉体貯槽20内に供給するようにする。
また、好ましい層流をつくるため、気体の入口から切り
出し弁18までの距離を、気流搬送管12の内径lの1
0倍前後とすることが好ましい。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below in detail with reference to the drawings. However, the shapes of the components described in this embodiment, the relative arrangement thereof, and the like are not intended to limit the scope of the present invention to them only, unless otherwise specified, and are merely illustrative examples. It's just Embodiment 1 FIG. 1 shows an embodiment of a weightless powder classifier according to the present invention, in which an electric field is applied. Reference numeral 10 denotes a weightless room, which is a rocket, a falling tower, an aircraft that draws a parabola and flies. A powder air transport tube 12 (duct) is arranged in the zero-gravity chamber 10, and one end of the air flow transport tube 12 is connected to a static electricity supply device 14 and a blower 16. Examples of the charged powder supply means 14 include a powder storage tank 20 provided with a cut-out valve 18 at a lower portion and further provided with a high voltage application means 22. It is also possible to supply the powder in a laminar flow while applying a high voltage to the air flow carrier pipe 12 so that the powder is charged. In order to put the powder into the air flow carrier pipe 12, for example, the gas branched from the blower 16 is supplied into the powder storage tank 20.
Further, in order to create a preferable laminar flow, the distance from the gas inlet to the cut-off valve 18 is set to 1 of the inner diameter l of the air flow carrier pipe 12.
It is preferred to be about 0 times.

【0009】気流搬送管12内の他端には、粉体分級手
段24が設けられ、この気流搬送管12の途中に電場付
与手段26が配置される。粉体分級手段24としては、
例えば、多数の板をスリットが生じるように水平方向に
重ね合わせたものからなるフィルターなどが用いられ
る。28は電源である。
A powder classifying means 24 is provided at the other end of the air flow carrying tube 12, and an electric field applying means 26 is arranged in the middle of the air flow carrying tube 12. As the powder classification means 24,
For example, a filter formed by laminating a number of plates in a horizontal direction so as to form slits is used. 28 is a power supply.

【0010】今、気流搬送管12の内径をl〔m〕、滞
電粉体の速度をv〔m/s〕、滞電粉体1個の質量をm
〔kg〕、電圧をV〔ボルト〕とすると、 E=V/l〔V/m〕又は〔N/C〕 となる。時間t=0で、粉体の位置x=0、y=0、粉
体の加速度x″=0、y″=Eq/mである。したがっ
て、t秒後には、x′=v、y′=Eqt/m(Eq/
m〔m/s2〕)、x=vt、y=Eqt2/2mとなる。
なお、qは滞電粉体の電荷である。x=x*でt=x*
v、y=Eqx*2/2mv2、すなわち、集塵部AB面
ではEqx*2/2mv2の偏位がある。E、q、x*
v、は一定であるので、粉体の偏位は質量mに反比例
し、dp3に反比例する。なお、x*は流れの方向への電
界が存在している距離、dpは粒子の直径である。
Now, the inner diameter of the air flow carrier tube 12 is 1 [m], the velocity of the static charge powder is v [m / s], and the mass of one static charge powder is m.
[Kg] and the voltage as V [volt], E = V / l [V / m] or [N / C]. At time t = 0, the powder position x = 0, y = 0, and the powder acceleration x ″ = 0, y ″ = Eq / m. Therefore, after t seconds, x ′ = v, y ′ = Eqt / m (Eq /
m [m / s 2 ]), x = vt, y = Eqt 2 / 2m.
Here, q is the electric charge of the charged powder. x = x * and t = x * /
v, y = Eqx * 2 / 2mv 2, i.e., in the dust collecting section AB plane has excursion Eqx * 2 / 2mv 2. E, q, x * ,
Since v is constant, the deviation of the powder is inversely proportional to the mass m and inversely proportional to dp 3 . Note that x * is the distance in which the electric field exists in the flow direction, and dp is the diameter of the particle.

【0011】したがって、図1に示すように、気流搬送
管12の上側をプラス極とし、下側をマイナス極とする
と、滞電した粉体は質量に反比例した加速度が生じ、小
径粉体は下側へ大きく移動し、大径粉体は下側へ少し移
動する。これらの粉体を分級手段24(フィルター)で
分離することにより、粉体が分級される。
Therefore, as shown in FIG. 1, if the upper side of the air flow carrier tube 12 is a positive pole and the lower side is a negative pole, the powder that has been charged has an acceleration that is inversely proportional to the mass, and the powder that has a small diameter has a bottom. The large-sized powder moves a little to the lower side. These powders are separated by the classification means 24 (filter), whereby the powders are classified.

【0012】実施例2 本実施例は、図2及び図3に示すように、図1に示す装
置において、電場付与手段の代りに磁場付与手段30を
設けたものである。磁場付与手段30としては、例え
ば、2つの磁石32、34を気流搬送管12のまわりに
設置したものを挙げることができる。他の構成は、実施
例1の場合と同様である。
Embodiment 2 In this embodiment, as shown in FIGS. 2 and 3, the apparatus shown in FIG. 1 is provided with a magnetic field applying means 30 in place of the electric field applying means. As the magnetic field applying means 30, for example, one in which two magnets 32 and 34 are installed around the air flow carrier tube 12 can be mentioned. Other configurations are the same as those in the first embodiment.

【0013】今、滞電粉体の速度をv、質量をmとする
と、時間t=0で、粉体の位置x=0、y=0である。
そして、x′=v、y′=vqBt/m、x=vt、y
=vqBt2/2mとなる。なお、Bは磁束密度〔Wb/m
2〕を表わす。x=x*で、y=vqB/2m×(x*
v)2、ここで、v、q、B、x*は一定であるので、粉
体の加速度は質量mに反比例する。
Assuming now that the velocity of the non-charged powder is v and the mass is m, the time t = 0 and the powder position x = 0 and y = 0.
Then, x '= v, y' = vqBt / m, x = vt, y
= VqBt 2 / 2m. B is the magnetic flux density [Wb / m
2 ]. x = x * , y = vqB / 2mx × (x * /
v) 2 , where v, q, B, x * are constant, so the acceleration of the powder is inversely proportional to the mass m.

【0014】したがって、図2に示すように、気流搬送
管12のむこう側(紙面の裏面)からこちら側へ磁界を
加えると、滞電した粉体は質量に反比例した加速度で移
動し、小径粉体は下側へ大きく移動し、大径粉体は下側
へ小さく移動する。これらの粉体を分級手段24(フィ
ルター)に通し分級する。
Therefore, as shown in FIG. 2, when a magnetic field is applied from the other side (back side of the paper surface) of the air flow carrier tube 12 to this side, the accumulated powder moves at an acceleration inversely proportional to the mass and has a small diameter. The powder moves largely downward, and the large-diameter powder moves small downward. These powders are passed through a classification means 24 (filter) and classified.

【0015】[0015]

【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。 (1)無重力状態又は微小重力状態で粉体を層流で気流
搬送し分級するので、重力加速度による粉体の偏流及び
乱流域による粉体の蛇行流が生じることなく、精度の高
い分級を行うことができる。
As described above, the present invention has the following effects. (1) Since powders are conveyed in a laminar flow in a gravitational flow in a weightless state or in a microgravity state, classification is performed with high accuracy without causing uneven distribution of powder due to gravitational acceleration and meandering flow of powder due to turbulent flow regions. be able to.

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

【図1】本発明の無重力粉体分級装置の一実施例(電界
の場合)を示す概略構成図である。
FIG. 1 is a schematic configuration diagram showing one embodiment (in the case of an electric field) of a weightless powder classifier of the present invention.

【図2】本発明の装置の他の実施例(磁界の場合)を示
す概略構成図である。
FIG. 2 is a schematic configuration diagram showing another embodiment (in the case of a magnetic field) of the apparatus of the present invention.

【図3】図2における磁場付与手段まわりの平面図であ
る。
FIG. 3 is a plan view around a magnetic field applying unit in FIG. 2;

【符号の説明】[Explanation of symbols]

10 無重力室 12 粉体気流搬送管 14 滞電粉体供給手段 16 送風機 18 切り出し弁 20 粉体貯槽 22 高電圧印加手段 24 粉体分級手段 26 電場付与手段 28 電源 30 磁場付与手段 32 磁石 34 磁石 10 Zero Gravity Chamber 12 Powder Air Flow Conveying Pipe 14 Electrostatic Powder Supplying Means 16 Blower 18 Cutout Valve 20 Powder Storage Tank 22 High Voltage Applying Means 24 Powder Classifying Means 26 Electric Field Applying Means 28 Power Supply 30 Magnetic Field Applying Means 32 Magnets 34 Magnets

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 滞電粉体を無重力下又は微小重力下にて
層流で気流搬送し、この層流に電場をかけて粉体を分級
することを特徴とする無重力粉体分級方法。
1. A gravity-free powder classification method, characterized in that an electrostatically charged powder is conveyed in a laminar flow in a gravitational flow under zero gravity or microgravity, and an electric field is applied to the laminar flow to classify the powder.
【請求項2】 滞電粉体を無重力下又は微小重力下にて
層流で気流搬送し、この層流に磁場をかけて粉体を分級
することを特徴とする無重力粉体分級方法。
2. A weightless powder classification method, characterized in that an electrostatically charged powder is conveyed in a laminar flow in a gravitational flow under zero gravity or microgravity, and a magnetic field is applied to the laminar flow to classify the powder.
【請求項3】 無重力室内に粉体気流搬送管を配置し、
この粉体気流搬送管の一端に滞電粉体供給手段及び送風
機を接続し、この粉体気流搬送管内の他端に粉体分級手
段を設け、この粉体気流搬送管の途中に電場付与手段を
配置したことを特徴とする無重力粉体分級装置。
3. A powder air transport tube is disposed in a weightless chamber,
An electrostatically charged powder supply means and a blower are connected to one end of the powder airflow transfer tube, and a powder classification means is provided at the other end of the powder airflow transfer tube, and an electric field applying means is provided in the middle of the powder airflow transfer tube. A weightless powder classifier characterized by having a.
【請求項4】 無重力室内に粉体気流搬送管を配置し、
この粉体気流搬送管の一端に滞電粉体供給手段及び送風
機を接続し、この粉体気流搬送管内の他端に粉体分級手
段を設け、この粉体気流搬送管の途中に磁場付与手段を
配置したことを特徴とする無重力粉体分級装置。
4. A powder air flow transfer pipe is disposed in a weightless chamber,
An electrostatically charged powder supply means and a blower are connected to one end of the powder airflow transfer tube, and a powder classification means is provided at the other end of the powder airflow transfer tube, and a magnetic field applying means is provided in the middle of the powder airflow transfer tube. A weightless powder classifier characterized by having a.
JP5343542A 1993-12-15 1993-12-15 Weightless powder classification method and apparatus Expired - Fee Related JP2668070B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5343542A JP2668070B2 (en) 1993-12-15 1993-12-15 Weightless powder classification method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5343542A JP2668070B2 (en) 1993-12-15 1993-12-15 Weightless powder classification method and apparatus

Publications (2)

Publication Number Publication Date
JPH07163906A JPH07163906A (en) 1995-06-27
JP2668070B2 true JP2668070B2 (en) 1997-10-27

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ID=18362329

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JP5343542A Expired - Fee Related JP2668070B2 (en) 1993-12-15 1993-12-15 Weightless powder classification method and apparatus

Country Status (1)

Country Link
JP (1) JP2668070B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20040016593A (en) * 2002-08-19 2004-02-25 이종구 Manufacture method of yellow clay powder
JP5573546B2 (en) * 2009-10-22 2014-08-20 Jfeスチール株式会社 Ferromagnetic separator
CN105618261A (en) * 2016-03-24 2016-06-01 陈勇 Device for magnetite separation by blowing ore sand through strong breeze
CN105618253A (en) * 2016-03-24 2016-06-01 陈勇 Device for magnetite separation by impacting ore sand through paraboloid

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6328662B2 (en) 2013-01-15 2018-05-23 コーニンクレッカ フィリップス エヌ ヴェKoninklijke Philips N.V. Binaural audio processing

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6328662B2 (en) 2013-01-15 2018-05-23 コーニンクレッカ フィリップス エヌ ヴェKoninklijke Philips N.V. Binaural audio processing

Also Published As

Publication number Publication date
JPH07163906A (en) 1995-06-27

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