JPH11302702A - Powder dryer - Google Patents

Powder dryer

Info

Publication number
JPH11302702A
JPH11302702A JP10112129A JP11212998A JPH11302702A JP H11302702 A JPH11302702 A JP H11302702A JP 10112129 A JP10112129 A JP 10112129A JP 11212998 A JP11212998 A JP 11212998A JP H11302702 A JPH11302702 A JP H11302702A
Authority
JP
Japan
Prior art keywords
powder
hot air
dryer
carrier
blown
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
JP10112129A
Other languages
Japanese (ja)
Inventor
Yasushi Yamamoto
裕史 山本
Isao Endo
功 遠藤
Hideo Koshimoto
秀生 越本
Isamu Otsuka
勇 大塚
Yoshimasa Okuno
良誠 奥野
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP10112129A priority Critical patent/JPH11302702A/en
Publication of JPH11302702A publication Critical patent/JPH11302702A/en
Pending legal-status Critical Current

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  • Powder Metallurgy (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently dry even the powder having relatively large specific gravity. SOLUTION: In a powder dryer for drying powder while floating by hot air by arranging the powder on a powder placing body 10 having many air holes and blowing the hot air from the under side of the powder placing body 10, a stirring means 21 for stirring the powder is disposed above the powder placing body 10. A hot air blowing port 14 for blowing the hot air from the under side of the powder placing body 10 toward the powder is disposed below the powder placing body 10 and a distributor for diffusing the hot air blown from the hot air blowing port 14 is disposed in the under side of the powder placing body 10.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、急冷凝固金属粉末
等の粉末を乾燥させるための粉末乾燥機に関する。
The present invention relates to a powder dryer for drying powder such as rapidly solidified metal powder.

【0002】[0002]

【従来の技術】例えば、冷却凝固金属粉末は、溶融金属
を噴出孔から微細に分断させて、冷却水と接触させる水
アトマイズ法により得られるが、上記方法で形成した冷
却凝固金属粉末は、水で濡れているため、脱水処理した
後に強制乾燥させる必要がある。
2. Description of the Related Art For example, a cooled and solidified metal powder is obtained by a water atomization method in which a molten metal is finely divided from an orifice and brought into contact with cooling water. Therefore, it is necessary to forcibly dry after dehydration treatment.

【0003】このため、従来では、脱水処理した急冷凝
固粉末を網上に配置し、網下から熱風を送風して急冷凝
固粉末を熱風で浮遊させながら強制乾燥させるようにし
たものがある(例えば特開平3−79705号公報)。
これは、棚式乾燥機等に比べて短時間で乾燥できるとい
う長所があり、比重の比較的軽い物質の乾燥には好適で
ある。
[0003] For this reason, conventionally, there is a type in which a rapidly solidified powder that has been dehydrated is placed on a net, hot air is blown from under the net, and the rapidly solidified powder is forcibly dried while floating with the hot air (eg, JP-A-3-79705).
This has an advantage that it can be dried in a shorter time than a shelf type dryer or the like, and is suitable for drying a substance having a relatively light specific gravity.

【0004】[0004]

【発明が解決しようとする課題】しかし、従来の粉末乾
燥機では、水アトマイズ法などで製造され濡れている金
属粉末を乾燥しようとした場合には、比重の大きい材
料では熱風で粉末が浮遊しにくい。熱風圧を上げた
り、熱風量を多くしても吹き抜けが発生するだけで、効
率のよい乾燥はできないという問題があった。従って、
例えば鉄粉末が濡れて凝集していると、内部で酸化が促
進されてしまい、高品質の粉末を得ることができなくな
った。
However, in a conventional powder dryer, when a wet metal powder produced by a water atomizing method or the like is to be dried, a powder having a large specific gravity floats due to hot air. Hateful. Even if the hot air pressure is increased or the amount of hot air is increased, there is a problem that only a blow-through occurs and efficient drying cannot be performed. Therefore,
For example, when the iron powder is wet and agglomerated, the oxidation is promoted inside, so that high quality powder cannot be obtained.

【0005】本発明は、上記問題点に鑑み、比重の比較
的重い粉末でも効率よく乾燥することができるようにし
たものである。
The present invention has been made in view of the above problems, and is intended to efficiently dry even a relatively heavy powder.

【0006】[0006]

【課題を解決するための手段】この技術的課題を解決す
るための本発明の第1の技術的手段は、多数の通気孔を
有する粉末載せ体10上に粉末を配置し、粉末載せ体1
0の下から熱風を送風して粉末を熱風で浮遊させながら
乾燥させるようにした粉末乾燥機において、前記粉末載
せ体10の上方に、粉末を攪拌する攪拌手段21が設け
られている点にある。
A first technical means of the present invention for solving this technical problem is to arrange powder on a powder carrier 10 having a large number of ventilation holes, and to provide a powder carrier 1 having a plurality of air holes.
In a powder dryer in which hot air is blown from below and dried while floating the powder with hot air, a stirring means 21 for stirring the powder is provided above the powder placing body 10. .

【0007】本発明の第2の技術的手段は、粉末載せ体
10の下方に、粉末載せ体10の下から粉末に向けて熱
風を送風する熱風送風口14が設けられ、粉末載せ体1
0の下方に、熱風送風口14から送風される熱風を拡散
させる整流板16が設けられている点にある。
According to a second technical means of the present invention, a hot air blowing port 14 for blowing hot air from below the powder carrier 10 toward the powder is provided below the powder carrier 10, and the powder carrier 1 is provided.
The point below is that a rectifying plate 16 for diffusing the hot air blown from the hot air blowing port 14 is provided below the zero.

【0008】[0008]

【発明の実施の形態】以下、本発明の実施の形態を図を
参照して説明する。図1において、1は急冷凝固金属粉
末等の強制乾燥に使用される粉末乾燥機で、直方体形状
の支持台2と、支持台2上に載置した円筒状の乾燥機本
体3とを備える。乾燥機本体3の下端は底壁4により塞
がれ、乾燥機本体3の上端は天蓋5により塞がれ、乾燥
機本体3内は密閉状とされている。天蓋5は乾燥機本体
3の上端に着脱可能である。乾燥機本体3の上下方向中
途部に支持片6が内方突設されている。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, reference numeral 1 denotes a powder dryer used for forcibly drying rapidly solidified metal powder or the like, and includes a rectangular parallelepiped support base 2 and a cylindrical dryer main body 3 placed on the support base 2. The lower end of the dryer main body 3 is closed by a bottom wall 4, the upper end of the dryer main body 3 is closed by a canopy 5, and the inside of the dryer main body 3 is sealed. The canopy 5 is detachable from the upper end of the dryer main body 3. A support piece 6 is provided in a vertically intermediate portion of the dryer main body 3 so as to protrude inward.

【0009】9は粉末容器で、上端が開口した有底円筒
状に形成され、粉末容器9の底部は、乾燥の被処理物で
ある粉末が通過不能な網により構成されて、多数の通気
孔を有する粉末載せ体10とされている。この粉末容器
9は、天蓋5を取り外すことにより乾燥機本体3の上端
から乾燥機本体3内に挿入されて、乾燥機本体3内で支
持片6上に載置され、乾燥の被処理物である急冷凝固金
属粉末等の粉末を粉末容器9に収納して粉末載せ体10
上に配置するようになっている。
Reference numeral 9 denotes a powder container, which is formed in a cylindrical shape with a bottom having an open upper end. The bottom portion of the powder container 9 is constituted by a mesh through which the powder to be dried cannot pass, and has a large number of ventilation holes. And a powder carrier 10 having the following. The powder container 9 is inserted into the dryer main body 3 from the upper end of the dryer main body 3 by removing the canopy 5, is placed on the support piece 6 in the dryer main body 3, and is an object to be dried. A powder such as a rapidly solidified metal powder is stored in a powder container 9 and a powder carrier 10
It is designed to be placed on top.

【0010】13は一対の熱風供給管で、支持台2内に
配置され、各熱風供給管13の熱風送風口14側は底壁
4を貫通して乾燥機本体3内の下部に突出されている。
各熱風供給管13の下側端部に熱風供給ホースが接続さ
れるようになっており、一対の熱風供給管13により、
粉末容器9の粉末載せ体10の下からアルゴンガス又は
窒素ガス等の不活性ガスの熱風を粉末載せ体10上の粉
末に向けて送風するようになっている。
Reference numeral 13 denotes a pair of hot air supply pipes, which are disposed in the support base 2, and the hot air blowing port 14 side of each hot air supply pipe 13 penetrates through the bottom wall 4 and protrudes to the lower part in the dryer body 3. I have.
A hot air supply hose is connected to the lower end of each hot air supply pipe 13.
A hot air of an inert gas such as an argon gas or a nitrogen gas is blown from below the powder carrier 10 of the powder container 9 toward the powder on the powder carrier 10.

【0011】粉末容器9の粉末載せ体10の下方に、一
対の熱風供給管13の各熱風送風口14から送風される
熱風を拡散するように整流板16が設けられている。各
整流板16は熱風送風口14のすぐ上方を斜めに塞ぐよ
うに夫々配置されている。各整流板16は互いに逆方向
に傾斜されており、各熱風送風口14から送風される熱
風を粉末載せ体10の下で広く拡散して、熱風が粉末載
せ体10上の粉末側に直接送風されるのを防ぐと共に、
熱風を粉末載せ体10上の粉末側に全体に亘って略均等
に分散して、粉末側に送風するようになっている。
A rectifying plate 16 is provided below the powder carrier 10 of the powder container 9 so as to diffuse the hot air blown from the hot air blowing ports 14 of the pair of hot air supply pipes 13. Each of the flow regulating plates 16 is disposed so as to obliquely block a portion immediately above the hot air blowing port 14. Each current plate 16 is inclined in the opposite direction to each other, and the hot air blown from each hot air blowing port 14 is widely diffused below the powder carrier 10, and the hot air is blown directly to the powder side on the powder carrier 10. To prevent
The hot air is distributed substantially evenly over the powder side on the powder-carrying body 10 over the whole, and is sent to the powder side.

【0012】19は排気管で、天蓋5上に配置され、そ
の吸込口20側は天蓋5を貫通して乾燥機本体3内に導
入されている。熱風排気管19の上側端部に熱風排気ホ
ースが接続されるようになっており、前記一対の熱風供
給管13によって乾燥機本体3内に供給された不活性ガ
スの熱風を、排気管19によって外部に排出するように
なっている。
Reference numeral 19 denotes an exhaust pipe, which is disposed on the canopy 5 and whose suction port 20 side penetrates through the canopy 5 and is introduced into the main body 3 of the dryer. A hot air exhaust hose is connected to the upper end of the hot air exhaust pipe 19, and the hot air of the inert gas supplied into the dryer main body 3 by the pair of hot air supply pipes 13 is discharged by the exhaust pipe 19. It is designed to be discharged outside.

【0013】21は粉末を攪拌するための攪拌手段であ
る攪拌用のインペラーであり、インペラー21は回転軸
22の下端に放射状に取り付けられて、粉末載せ体10
の上方に配置されており、天蓋5上に取り付けたモータ
23により回転軸22廻りに回転駆動され、これにより
インペラー21は、粉末載せ体10上の粉末を攪拌する
ようになっている。
Reference numeral 21 denotes an impeller for stirring, which is a stirring means for stirring the powder. The impeller 21 is radially attached to a lower end of the rotating shaft 22 and has a powder loading member 10.
, And is rotated around a rotation shaft 22 by a motor 23 mounted on the canopy 5, whereby the impeller 21 agitates the powder on the powder carrier 10.

【0014】上記実施の形態によれば、急冷凝固金属粉
末等の粉末を乾燥させる場合、天蓋5を取り外して、乾
燥機本体3の上端から急冷凝固金属粉末を収納した粉末
容器9を乾燥機本体3に入れて、支持片6上に載せた
後、天蓋5を乾燥機本体3の上端に取り付け、熱風供給
管13によって乾燥機本体3内に熱風を供給すると共
に、モータ22によりインペラー21を回転駆動させ
る。
According to the above embodiment, when drying powder such as rapidly solidified metal powder, the canopy 5 is removed, and the powder container 9 containing the rapidly solidified metal powder is dried from the upper end of the main body 3 of the dryer. 3 and placed on the support piece 6, the canopy 5 is attached to the upper end of the dryer main body 3, hot air is supplied into the dryer main body 3 by the hot air supply pipe 13, and the impeller 21 is rotated by the motor 22. Drive.

【0015】すると、一対の熱風供給管13の各熱風送
風口14から不活性ガスの熱風が送風され、送風された
熱風は整流板16により粉末載せ体10の下で広く拡散
され、粉末載せ体10上の粉末側に全体に亘って略均等
に分散されて粉末側に送風される。また、このとき、イ
ンペラー21は、粉末載せ体10上の粉末を攪拌して、
凝集していた粉末をほぐす。その結果、粉末載せ体10
上の粉末を全体に亘って熱風で均一に浮遊させながら短
時間で乾燥させ、表面の清浄な金属粉末が得られる。
Then, the hot air of the inert gas is blown from each hot air blowing port 14 of the pair of hot air supply pipes 13, and the blown hot air is widely diffused under the powder carrier 10 by the rectifying plate 16, so that the powder carrier is supplied. The powder 10 is distributed substantially evenly over the entire powder side and is blown toward the powder side. At this time, the impeller 21 stirs the powder on the powder placing body 10 to
Dissolve the agglomerated powder. As a result, the powder carrier 10
The above powder is dried in a short time while being uniformly floated by hot air throughout, to obtain a metal powder having a clean surface.

【0016】実験結果によれば、表1に示す乾燥条件
で、Fe−Si−B系水アトマイズ粉末を乾燥させた場
合、従来の粉末乾燥機では、金属粉末の酸素の含有量が
約500ppmであったものが、本発明の粉末乾燥機で
は、金属粉末の酸素の含有量が約100〜200ppm
になった。
According to the experimental results, when the Fe—Si—B-based water atomized powder was dried under the drying conditions shown in Table 1, with a conventional powder dryer, the oxygen content of the metal powder was about 500 ppm. However, in the powder dryer of the present invention, the oxygen content of the metal powder is about 100 to 200 ppm
Became.

【0017】[0017]

【表1】 [Table 1]

【0018】なお、前記実施の形態では、多数の通気孔
を有する粉末載せ体10を網により構成しているが、こ
れに代え、粉末載せ体10を細かい多数の通気孔を有す
るパンチングメタルや多数の通気孔を有する板材その他
により構成してもよい。また、前記実施の形態では、粉
末容器9の底部の粉末載せ体10のみを多数の通気孔を
有する網により構成し、粉末容器9の外周部を板部材に
より構成しているが、これに代え、粉末容器9の粉末載
せ体10及び外周部を網その他の多数の通気孔を有する
部材により構成するようにしてもよい。
In the above-described embodiment, the powder carrier 10 having a large number of air holes is formed of a net. Alternatively, the powder carrier 10 may be formed of a punching metal having a large number of fine air holes or a large number of holes. May be constituted by a plate material having the above-mentioned ventilation holes. Further, in the above embodiment, only the powder carrier 10 at the bottom of the powder container 9 is constituted by a net having a large number of vents, and the outer periphery of the powder container 9 is constituted by a plate member. Alternatively, the powder carrier 10 and the outer peripheral portion of the powder container 9 may be constituted by a net or other members having a large number of ventilation holes.

【0019】また、前記実施の形態では、粉末を攪拌す
る攪拌手段として、回転駆動されるインペラー21を使
用しているが、これに代え、粉末を攪拌する攪拌手段と
して、軸芯廻りに回転駆動されるロール体やスクリュー
等を使用してもよい。また、前記実施の形態では、粉末
に向けて送風する熱風として、アルゴンガス又は窒素ガ
ス等の不活性ガスの熱風を送風するようにしているが、
これに代えて、乾燥させる粉末の種類によっては他の種
類のガスの熱風を送風するようにしてもよいし、また空
気の熱風を送風するようにしてもよい。
Further, in the above-described embodiment, the impeller 21 which is driven to rotate is used as the stirring means for stirring the powder. However, instead of this, the stirring means for stirring the powder is used to rotate the impeller 21 around the axis. A roll or a screw may be used. Further, in the above embodiment, as the hot air to be blown toward the powder, a hot air of an inert gas such as an argon gas or a nitrogen gas is blown,
Instead of this, depending on the type of powder to be dried, hot air of another type of gas may be blown, or hot air of air may be blown.

【0020】[0020]

【発明の効果】本発明によれば、攪拌手段により粉末を
攪拌して、凝集していた粉末をほぐすことができ、比重
の比較的重い粉末でも短時間で効率よく乾燥させること
ができる。
According to the present invention, the agglomerated powder can be loosened by stirring the powder with the stirring means, and even a relatively heavy powder can be efficiently dried in a short time.

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

【図1】本発明の一実施の形態を示す側断面図である。FIG. 1 is a side sectional view showing an embodiment of the present invention.

【図2】同正面図である。FIG. 2 is a front view of the same.

【図3】同平面図である。FIG. 3 is a plan view of the same.

【符号の説明】[Explanation of symbols]

10 網 14 熱風送風口 21 インペラー(攪拌手段) 10 net 14 hot air blowing port 21 impeller (stirring means)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大塚 勇 兵庫県尼崎市浜1丁目1番1号 株式会社 クボタ技術開発研究所内 (72)発明者 奥野 良誠 兵庫県尼崎市浜1丁目1番1号 株式会社 クボタ技術開発研究所内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Isamu Otsuka 1-1-1, Hama, Amagasaki-shi, Hyogo Prefecture Inside Kubota R & D Laboratories Co., Ltd. (72) Inventor Yoshimasa Okuno 1-1-1, Hama, Amagasaki-shi, Hyogo Stock Company Kubota Technology Development Laboratory

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 多数の通気孔を有する粉末載せ体(1
0)上に粉末を配置し、粉末載せ体(10)の下から熱
風を送風して粉末を熱風で浮遊させながら乾燥させるよ
うにした粉末乾燥機において、 前記粉末載せ体(10)の上方に、粉末を攪拌する攪拌
手段(21)が設けられていることを特徴とする粉末乾
燥機。
1. A powder carrier (1) having a large number of air holes.
0) In a powder dryer in which powder is placed on the upper surface and hot air is blown from under the powder carrier (10) to dry the powder while floating with the hot air, the powder is placed above the powder carrier (10). And a stirring means (21) for stirring the powder.
【請求項2】 粉末載せ体(10)の下方に、粉末載せ
体(10)の下から粉末に向けて熱風を送風する熱風送
風口(14)が設けられ、粉末載せ体(10)の下方
に、熱風送風口(14)から送風される熱風を拡散させ
る整流板(16)が設けられていることを特徴とする請
求項1に記載の粉末乾燥機。
2. A hot air blowing port (14) for blowing hot air from below the powder carrier (10) toward the powder is provided below the powder carrier (10), and below the powder carrier (10). 2. The powder dryer according to claim 1, further comprising a rectifying plate (16) for diffusing hot air blown from the hot air blowing port (14). 3.
JP10112129A 1998-04-22 1998-04-22 Powder dryer Pending JPH11302702A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10112129A JPH11302702A (en) 1998-04-22 1998-04-22 Powder dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10112129A JPH11302702A (en) 1998-04-22 1998-04-22 Powder dryer

Publications (1)

Publication Number Publication Date
JPH11302702A true JPH11302702A (en) 1999-11-02

Family

ID=14578932

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10112129A Pending JPH11302702A (en) 1998-04-22 1998-04-22 Powder dryer

Country Status (1)

Country Link
JP (1) JPH11302702A (en)

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JP2007217600A (en) * 2006-02-17 2007-08-30 Mitsui Eng & Shipbuild Co Ltd Gas hydrate manufacturing apparatus and method
JP2010013736A (en) * 2009-10-05 2010-01-21 Fujitsu Ltd Powder preparation method and apparatus
CN114633960A (en) * 2022-05-23 2022-06-17 西安宝德九土新材料有限公司 Metal powder processing apparatus is used in metallurgical production of big height-diameter ratio tungsten alloy powder

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005290460A (en) * 2004-03-31 2005-10-20 Fujitsu Ltd Powder adjustment method and apparatus
JP2007217600A (en) * 2006-02-17 2007-08-30 Mitsui Eng & Shipbuild Co Ltd Gas hydrate manufacturing apparatus and method
JP2010013736A (en) * 2009-10-05 2010-01-21 Fujitsu Ltd Powder preparation method and apparatus
CN114633960A (en) * 2022-05-23 2022-06-17 西安宝德九土新材料有限公司 Metal powder processing apparatus is used in metallurgical production of big height-diameter ratio tungsten alloy powder

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