JPH0211704A - Method and apparatus for producing atomized powder - Google Patents

Method and apparatus for producing atomized powder

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Publication number
JPH0211704A
JPH0211704A JP16079688A JP16079688A JPH0211704A JP H0211704 A JPH0211704 A JP H0211704A JP 16079688 A JP16079688 A JP 16079688A JP 16079688 A JP16079688 A JP 16079688A JP H0211704 A JPH0211704 A JP H0211704A
Authority
JP
Japan
Prior art keywords
liquid
powder
atomizing
spray tank
liquid coolant
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
JP16079688A
Other languages
Japanese (ja)
Inventor
Toshio Watanabe
敏夫 渡辺
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP16079688A priority Critical patent/JPH0211704A/en
Publication of JPH0211704A publication Critical patent/JPH0211704A/en
Pending legal-status Critical Current

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  • Glanulating (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

PURPOSE:To eliminate water disturbance of liquid coolant caused by liquid jet for atomizing molten metal and to produce metal powder having narrow particle size distribution and uniform particle size at high yield by giving the liquid coolant in an atomizing vessel the horizontal rotating movement at the time of pulverizing by atomizing molten material of the metal, etc., with the liquid jet. CONSTITUTION:The metal, alloy or ceramic is melted in a melting furnace 1 and flowed down into the atomizing vessel 6 containing the liquid coolant 7 as molten material stream 3 from a bottom nozzle. By blowing the liquid jet 5 to the molten material stream 3 from the atomizing device 4, it is pulverized, and by blowing the liquid coolant 7 in the atomizing vessel 6, it is solidified to produce the powdery body of the metal or the ceramic. In this case, by injecting water to horizontal direction from a tangential blowing hole 25 against the liquid coolant 7 in the atomizing vessel 6, the horizontal rotating movement is given to the liquid coolant 7 to form vortex flow 51 and the liquid coolant 5 is collided to deep part at center of the vortex flow 51. The atomizing of the molten material stream 3 caused by the disturbance of the cooling water 7 with the liquid jet 5 does not become unstable, and the atomized powder of the metal or the ceramic having uniform particle size is obtd.

Description

【発明の詳細な説明】 [産業上の利用分野1 本発明は、アトマイズ粉体の製造方法およびその装置に
関し、金属粉またはセラミックス扮等を成形焼結させて
、種々の機械部品や製品を造るための原料微粉の製造技
術に関する。
[Detailed Description of the Invention] [Industrial Application Field 1] The present invention relates to a method of manufacturing atomized powder and an apparatus thereof, and is a method for manufacturing various mechanical parts and products by molding and sintering metal powder or ceramics. Regarding manufacturing technology of raw material fine powder.

[従来の技術] 第4図に従来のアトマイズ微粉製造技術の代表例を示す
[Prior Art] FIG. 4 shows a typical example of a conventional atomized fine powder manufacturing technology.

炉体1a、ストッパ1b、高周波加熱コイルlc、溶湯
ノズル1dからなる溶解炉l内に、金属またはセラミッ
クスの溶湯2を収納し、溶湯ノズルldから流下溶湯流
3を垂下させる。一方、水(またはその他の液体例えば
油)の噴霧装置4は、液の入口4a、円環状液ノズル4
b、=圧の均一化を図る円周タンク4Cを備え、噴霧液
(液ジェット)5を逆円錐状に噴射する。
A molten metal or ceramic 2 is stored in a melting furnace 1 consisting of a furnace body 1a, a stopper 1b, a high-frequency heating coil lc, and a molten metal nozzle 1d, and a falling molten metal stream 3 is suspended from the molten metal nozzle ld. On the other hand, the water (or other liquid such as oil) spraying device 4 includes a liquid inlet 4a, an annular liquid nozzle 4
b. A circumferential tank 4C is provided to equalize the pressure, and the spray liquid (liquid jet) 5 is sprayed in an inverted conical shape.

その円錐用!!3.3の近傍で溶湯の流下流3は液の衝
突と冷却を受は粉末となる。液と粉末は混合して下方に
ほぼ円錐状に拡がる部分すなわち拡散ジェット5aを形
成し、噴霧槽6に落下する。噴霧槽6は液7を貯え、拡
散ジェット5aの衝撃緩和および冷却をする。拡散ジェ
ット5aの液はまだ相当の速度をもっており、雰囲気気
体7eも巻き込み、また、液7の表面を7a、7bのよ
うに大きく揺動させる。このとき液7の一部は大きな飛
沫7cや塊7dとなって上昇しく以下この現象を水暴れ
という)、これらが液ジェット5に当り、噴霧を不安定
にする。
For that cone! ! In the vicinity of 3.3, the molten metal downstream 3 is subjected to liquid collision and cooling, and becomes powder. The liquid and powder mix to form a downwardly expanding portion, ie, a diffusion jet 5a, which spreads out in a substantially conical shape, and falls into the spray tank 6. The spray tank 6 stores a liquid 7 and cushions the impact of the diffusion jet 5a and cools it. The liquid in the diffusion jet 5a still has a considerable speed, and the atmospheric gas 7e is also drawn in, causing the surface of the liquid 7 to swing greatly as shown at 7a and 7b. At this time, a part of the liquid 7 becomes large droplets 7c or lumps 7d and rises (hereinafter this phenomenon is referred to as water rampage), which hits the liquid jet 5 and makes the spray unstable.

結果として生成した粉の形が不整となり、大きさが狭い
粒度範囲に収斂せず広い分布となり、使用時に篩分けが
必要となり、液アトマイズによって均質な製品を得ると
いう意図に反して歩留りの低下を招いていた。
As a result, the shape of the resulting powder is irregular, the size does not converge into a narrow particle size range, but has a wide distribution, and sieving is required during use, which leads to a decrease in yield contrary to the intention of obtaining a homogeneous product by liquid atomization. I was invited.

この弊害の改善策として水暴れ防止のために。To prevent water damage as a remedy for this problem.

第5図または第6図に示すように液中に液の動きを妨げ
る障害物11.12をおき、ある程度の効果を収めてい
た。しかし、この障害物11.12は粉を含んだ液ジェ
ットの衝突により摩耗が激しく、またその取替には大き
な手間を必要とし、しかも水暴れを十分には押え切れな
い等、未だ不十分であった。
As shown in FIG. 5 or 6, obstacles 11 and 12 that impede the movement of the liquid were placed in the liquid, and some results were obtained. However, these obstacles 11 and 12 are subject to severe wear due to collisions with powder-containing liquid jets, require a great deal of effort to replace, and are still insufficient in that they are unable to sufficiently suppress water surges. there were.

[発明が解決しようとする課題] 水暴れの防止を図るには、液ジェットの衝撃による貯液
7の反動を起こさせないようにすることが最善策である
。このためには、例えば液ジェットが貯液7に衝突する
場合の液面との交差角を90度からできるだけ小さくし
、できれば貯液7の表面が液ジェットの方向と平行近く
になることが望ましい。さらに液ジェットで持ち込まれ
た雰囲気気体の気泡が貯液の上方に上がらず、下方に持
ち去られるようにすれば気泡による擾乱もなくなる。
[Problems to be Solved by the Invention] The best way to prevent water turbulence is to prevent the liquid storage 7 from reacting due to the impact of the liquid jet. For this purpose, for example, when the liquid jet collides with the liquid storage 7, the angle of intersection with the liquid surface should be made as small as possible from 90 degrees, and if possible, it is desirable that the surface of the liquid storage 7 be nearly parallel to the direction of the liquid jet. . Furthermore, if the bubbles of the atmospheric gas brought in by the liquid jet do not rise above the stored liquid and are carried away downward, disturbances caused by the bubbles can be eliminated.

本発明は、このようなノズルから流下する溶湯流に圧力
流体を衝突させて粉体を生成し、粉体を液体を貯えた噴
霧槽で冷却するアトマイズ粉体の製造技術において、水
暴れ減少を防止して、均一粒度のアトマイズ粉体を得る
ことを課題とする。
The present invention aims to reduce water turbulence in atomized powder production technology in which powder is produced by colliding a pressure fluid with a molten metal stream flowing down from such a nozzle, and the powder is cooled in a spray tank containing liquid. The objective is to prevent this problem and obtain atomized powder with uniform particle size.

〔課題を解決するための手段] 上記課題を解決するための本発明の技術手段は、噴霧槽
の液体に水平回転流を与え液面を窪ませ、その窪みに生
成した粉体を落下させることを特徴とするアトマイズ粉
体の製造方法である。
[Means for Solving the Problems] The technical means of the present invention for solving the above problems is to apply a horizontal rotational flow to the liquid in the spray tank to make the liquid surface depressed, and to cause the powder generated in the depression to fall. This is a method for producing atomized powder characterized by the following.

また、この方法を実施するための本発明の装置は、高圧
液体により垂下溶湯流から粉体を製造する液アトマイズ
装置であって、粉体を冷却する液体を貯える噴霧槽の円
周接線方向に、この槽内の液体に水平回転流を与える液
体または気体吹込口を配設したことを特徴とするアトマ
イズ粉体の製造装置であり、また、噴霧槽内に液体を水
平回転させて液面を窪ませる回転翼を噴霧槽内に設けた
装置を用いることもできる。
Furthermore, the apparatus of the present invention for carrying out this method is a liquid atomization apparatus for producing powder from a dripping molten metal flow by means of a high-pressure liquid, and the apparatus is a liquid atomization apparatus that produces powder from a dripping molten metal flow using a high-pressure liquid. , is an atomized powder production device characterized by having a liquid or gas inlet that gives a horizontally rotating flow to the liquid in the tank, and also has a method for horizontally rotating the liquid in the spray tank to raise the liquid level. It is also possible to use a device in which a recessed rotor is provided within the spray tank.

[作用1 液噴霧槽内の液に水平回転を与えると渦流を生し、その
中央上部に液のない空間が構成され、粉体を生成した液
ジェットは渦流51の深いところで噴霧槽内の液に当る
[Effect 1: When horizontal rotation is applied to the liquid in the liquid spray tank, a vortex is created, and a liquid-free space is formed in the upper center of the vortex, and the liquid jet that has generated the powder is deep in the vortex 51 to form a vortex. corresponds to

このため液ジェットと噴霧槽内の液との耐衝突はなくな
り水暴れが解消される。
As a result, the collision resistance between the liquid jet and the liquid in the spray tank is eliminated, and water swell is eliminated.

従って、液ジェット噴霧が安定し、粒度範囲の狭い、形
状の整った粉体を得ることができる。
Therefore, liquid jet spraying is stable, and powder with a narrow particle size range and well-shaped powder can be obtained.

〔実施例〕〔Example〕

第1図〜第3図を参照して本発明の詳細な説明する。 The present invention will be described in detail with reference to FIGS. 1 to 3.

溶解炉lから流下した溶湯流3は円環状水噴霧装置4に
導かれ、逆円錐形液ジェット5によって粉化され、水と
共に拡散ジェット5aとなり、噴霧槽6に落下する。噴
霧槽6内に貯えられている貯液7は水平回転流を与えら
れてその液面に窪みを生じている。この窪みは、この実
施例ではポンプ21から電動バルブ22、分配円環23
、電動流量調整バルブ24、接線吹込口25を介して水
を送ることによって生成されている。
The molten metal stream 3 flowing down from the melting furnace 1 is led to an annular water spray device 4, is pulverized by an inverted conical liquid jet 5, becomes a diffusion jet 5a together with water, and falls into a spray tank 6. The liquid 7 stored in the spray tank 6 is given a horizontal rotational flow to form a depression in its liquid level. In this embodiment, this recess extends from the pump 21 to the electric valve 22 to the distribution ring 23.
, an electric flow control valve 24, and a tangential inlet 25.

第1図では2箇所ある吹込口25から接線状に吹込液が
噴霧槽6内に導き入れられるが、このため槽内の貯液は
第1図に示すように回転して渦を生じ、その中央上方に
は貯液のない空間が構成され、拡散ジェット5aは第2
図に示すように渦流包絡面51の深いところて貯液7に
当る。このため拡散ジェット5aと貯液7との直衝突は
なくなり水暴れは解消される。
In FIG. 1, the blown liquid is introduced tangentially into the spray tank 6 from the two injection ports 25, but as a result, the liquid stored in the tank rotates and creates a vortex as shown in FIG. A space with no liquid storage is formed above the center, and the diffusion jet 5a is connected to the second
As shown in the figure, the deep part of the vortex envelope surface 51 hits the liquid storage 7. Therefore, there is no direct collision between the diffusion jet 5a and the stored liquid 7, and the water surge is eliminated.

また1本実施例では、循環ポンプ21によって貯液に回
転を与え、貯液は噴霧槽底の排出口6aから連続的に排
出されるので、この流れによって渦流の窪みは下方へ延
長する。渦の形成する液面の渦流包絡面51の形状は吹
込口25からの吹込液の流入速度と排出口6aからの排
出量を規制する調節弁6bによって調節することができ
る。さらにこの下降液流のため、生成した粉末は直ちに
噴霧槽から排出されサイクロン31とカスケード式沈降
槽32および最終濾過装置33、液の冷却装置34で連
続自動集粉が可能となる。従って、従来は噴霧槽6内に
粉末を貯蔵して一定量毎にバンヂ処理を行っていたが、
これに比し噴霧槽の省力効果を図ることができる。
Furthermore, in this embodiment, the circulation pump 21 rotates the stored liquid and the stored liquid is continuously discharged from the outlet 6a at the bottom of the spray tank, so that this flow causes the vortex depression to extend downward. The shape of the vortex envelope surface 51 of the liquid surface formed by the vortex can be adjusted by a control valve 6b that regulates the inflow speed of the blown liquid from the inlet 25 and the amount of discharge from the outlet 6a. Further, due to this downward flow of liquid, the generated powder is immediately discharged from the spray tank, and continuous automatic powder collection is enabled by the cyclone 31, cascade settling tank 32, final filtration device 33, and liquid cooling device 34. Therefore, conventionally, powder was stored in the spray tank 6 and banding was performed every fixed amount.
In contrast, it is possible to achieve a labor-saving effect in the spray tank.

もちろん貯液の排出をこのように構成したり、液を循環
させることは本発明とは独立のものであり、気体または
回転翼等によって貯液に回転を勺えてもよく、これらの
手段は状況に応じて採用すれば良いものである。
Of course, configuring the discharge of the stored liquid in this way and circulating the liquid in this manner are independent of the present invention, and the storage liquid may be rotated by gas or rotary blades, etc., and these means may be used depending on the situation. It is advisable to adopt it according to the situation.

なお、この実施例の構成についても、類似の変化、応用
を妨げるものではない。例えば、噴霧槽6への液の接線
流入口25は、第1図に示した2箇所にとられれず、1
箇所でもよく、また4、6.8またはそれ以上と任意の
口数がとれることは言うまでもない。
It should be noted that the configuration of this embodiment does not preclude similar changes and applications. For example, the tangential inlet 25 for liquid into the spray tank 6 is not provided at two locations as shown in FIG.
It goes without saying that the number may be 4, 6.8 or more.

また第3図に示すように貯槽6への流入方向36も水平
(θ=0)のみならず、例えば上下方向入射角0を15
度とか20度とか任意の入射角とし、窪みの形状が急峻
になるようにすることもできる。
Furthermore, as shown in FIG.
It is also possible to set the incident angle to an arbitrary angle such as 20 degrees or 20 degrees, and make the shape of the depression steep.

また噴霧槽6の横断面形状は円形が望ましいが、必ずし
も円形にこだわることはなく、渦流をラッパ状の窪みに
形成できればよく、本発明の効果は何ら変わるものでは
ない。また、本発明は金属粉はもちろん、セラミックス
扮、ポリマー扮等の他の粉体に適用できる。
Further, although it is desirable that the cross-sectional shape of the spray tank 6 is circular, it does not necessarily have to be circular, and the effect of the present invention will not change in any way as long as the vortex can be formed into a trumpet-shaped depression. Further, the present invention can be applied not only to metal powder but also to other powders such as ceramic powder and polymer powder.

[発明の効果] 従来の噴霧槽内ては液ジェットによる液面叩きが行われ
る結果、大きな非定常的液揺動と上方飛び跳ね散乱を伴
う水暴れがあって、これを防止する種々の槽内陣書物構
造が提案されているが、何れも複雑で建設や掃除などを
含もメンテナンスが厄介で効果も完全ではなかった。
[Effect of the invention] As a result of the liquid surface being hit by a liquid jet in a conventional spray tank, there is a large unsteady liquid fluctuation and a water turbulence accompanied by upward splashing and scattering. Jinshomono structures have been proposed, but they are all complicated, require troublesome maintenance, including construction and cleaning, and are not completely effective.

本発明は槽内に構造物を置くことなく、ジェット流の緩
和と冷却を行うことができるので、構造物の隅部等に粉
体が滞留したり、凝固したりする心配もなく、旋回流に
より噴霧槽内壁への粉体の付着がなく、槽内清掃も容易
で、液の跳ね上げもないので、液ジェット噴霧は安定す
る。さらに粉体を含もスラリの連続排出処理、液の冷却
をクローズドシステムとして自動化することも容易にで
きる。
The present invention can moderate and cool the jet flow without placing any structure in the tank, so there is no need to worry about powder staying in the corners of the structure or solidifying, and the swirling flow This prevents powder from adhering to the inner wall of the spray tank, the tank interior is easy to clean, and there is no splashing of liquid, resulting in stable liquid jet spraying. Furthermore, continuous discharge of slurry containing powder and liquid cooling can be easily automated as a closed system.

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

第1図は本発明の実施例のアトマイズ装置の全体構成図
、第2図、第3図は渦流と液ジェットの接交部の説明図
、第4図は従来のアトマイズ装置の構造、機能の説明図
、第5図、第6図は従来の水暴れ防止装置の例を示す斜
視図である。 1・・・溶解炉      2−・−溶湯3・・−溶湯
流      4・・・液噴霧装置5−・・液ジェット
    6・−・噴霧槽7−・・貯液 51−・・渦流包絡面 11.12・・・水暴れ防止装置
Fig. 1 is an overall configuration diagram of an atomizing device according to an embodiment of the present invention, Figs. 2 and 3 are explanatory diagrams of the intersection of a vortex and a liquid jet, and Fig. 4 is an illustration of the structure and function of a conventional atomizing device. The explanatory drawings, FIG. 5, and FIG. 6 are perspective views showing examples of conventional water splash prevention devices. 1... Melting furnace 2-... Molten metal 3...- Molten metal flow 4... Liquid spray device 5-... Liquid jet 6... Spray tank 7-... Liquid storage 51-... Eddy current envelope surface 11 .12...Water rampage prevention device

Claims (1)

【特許請求の範囲】 1 ノズルから流下する溶湯流に圧力流体を衝突させて
粉体を生成し、該粉体を液体を貯えた噴霧槽で冷却する
アトマイズ粉体の製造に当り、 該噴霧槽内の液体に水平回転流を与えてそ の液面を窪ませ、生成した粉体を該窪みに落下させるこ
とを特徴とするアトマイズ粉体の製造方法。 2 高圧流体により垂下溶湯流から粉体を製造するアト
マイズ装置において、 該粉体を冷却する液体を貯える噴霧槽の円 周接線方向に、該噴霧槽内の液体に水平回転流を与える
液体または気体吹込口を配設したことを特徴とするアト
マイズ粉体の製造装 置。 3 噴霧槽内の貯留液体に水平回転を与えて液面を窪ま
せる回転翼を該噴霧槽内に設けたことを特徴とするアト
マイズ粉体の製造装置。
[Scope of Claims] 1. In the production of atomized powder, a powder is generated by colliding a molten metal stream flowing down from a nozzle with a pressure fluid, and the powder is cooled in a spray tank storing liquid, the spray tank A method for producing atomized powder, characterized by applying a horizontal rotational flow to the liquid in the container to make the liquid surface concave, and causing the generated powder to fall into the concavity. 2. In an atomization device that produces powder from a dripping molten metal flow using a high-pressure fluid, a liquid or gas that provides a horizontal rotational flow to the liquid in the spray tank in the tangential direction of the circumference of the spray tank that stores the liquid that cools the powder. An atomized powder manufacturing device characterized by being equipped with an inlet. 3. An atomized powder manufacturing apparatus characterized in that a rotary blade is provided in the spray tank to apply horizontal rotation to the liquid stored in the spray tank to make the liquid surface depressed.
JP16079688A 1988-06-30 1988-06-30 Method and apparatus for producing atomized powder Pending JPH0211704A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16079688A JPH0211704A (en) 1988-06-30 1988-06-30 Method and apparatus for producing atomized powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16079688A JPH0211704A (en) 1988-06-30 1988-06-30 Method and apparatus for producing atomized powder

Publications (1)

Publication Number Publication Date
JPH0211704A true JPH0211704A (en) 1990-01-16

Family

ID=15722640

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16079688A Pending JPH0211704A (en) 1988-06-30 1988-06-30 Method and apparatus for producing atomized powder

Country Status (1)

Country Link
JP (1) JPH0211704A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101947653A (en) * 2010-09-29 2011-01-19 株洲火炬工业炉有限责任公司 Device and method for preparing zinc powder and pulp
JP2012507633A (en) * 2008-11-04 2012-03-29 ユミコア・アクチエンゲゼルシャフト・ウント・コムパニー・コマンディットゲゼルシャフト Apparatus and method for granulating molten metal
JP2021161465A (en) * 2020-03-31 2021-10-11 Jfeスチール株式会社 Granular iron manufacturing apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012507633A (en) * 2008-11-04 2012-03-29 ユミコア・アクチエンゲゼルシャフト・ウント・コムパニー・コマンディットゲゼルシャフト Apparatus and method for granulating molten metal
CN101947653A (en) * 2010-09-29 2011-01-19 株洲火炬工业炉有限责任公司 Device and method for preparing zinc powder and pulp
JP2021161465A (en) * 2020-03-31 2021-10-11 Jfeスチール株式会社 Granular iron manufacturing apparatus

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