JPH0441607A - Metal powder manufacturing method - Google Patents
Metal powder manufacturing methodInfo
- Publication number
- JPH0441607A JPH0441607A JP15042090A JP15042090A JPH0441607A JP H0441607 A JPH0441607 A JP H0441607A JP 15042090 A JP15042090 A JP 15042090A JP 15042090 A JP15042090 A JP 15042090A JP H0441607 A JPH0441607 A JP H0441607A
- Authority
- JP
- Japan
- Prior art keywords
- molten metal
- nozzle
- outer peripheral
- peripheral edge
- pressure gas
- 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.)
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- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
A4発明の目的
(1ン 産業上の利用分野
本発明は金属粉末の製造方法、特に、溶湯ノズルの下端
面に開口する流出口より溶湯を流出させ、また溶湯ノズ
ルの流出口近傍に配設された環状ガスノズルによる高圧
ガス流を、それが溶湯ノズルの下方で収斂するように円
錐シェル形に形成して、溶湯を高圧ガス流により切断す
ることによって粉末化する方法の改良に関する。Detailed Description of the Invention A4 Purpose of the Invention (1) Industrial Field of Application The present invention relates to a method for producing metal powder, and in particular, to a method for producing metal powder, in particular, a method for producing a molten metal powder through an outlet opening at the lower end face of a molten metal nozzle. A method of forming a high-pressure gas flow from an annular gas nozzle disposed near the outlet into a conical shell shape so that it converges below the molten metal nozzle, and cutting the molten metal with the high-pressure gas flow to powder it. Regarding improvements.
(2) 従来の技術
従来、この種製造方法としては、溶湯ノズルの流出口か
ら略柱状をなすように溶湯を流下させ、その溶湯に高圧
ガス流を衝突させて溶湯の粉末化を行う、といった方法
が知られている。(2) Conventional technology Conventionally, this type of manufacturing method involves making the molten metal flow down from the outlet of a molten metal nozzle in a substantially columnar shape, and colliding the molten metal with a high-pressure gas flow to turn the molten metal into powder. method is known.
(3)発明が解決しようとする課題
しかしながら、前記製造方法によると、高圧ガス流によ
って切断される粉末1個当りの溶湯量が多い上に、溶湯
に対する冷却作用が不十分であることに起因して粉末相
互の再接合を惹起し易く、その結果、金属粉末の粒度分
布が直径の大きい方へ偏るため微細な金属粉末を得るこ
とが難しい、という問題がある2
本発明は前記に鑑み、簡単な手段を採用することによっ
て微細な金属粉末を得ることのできる前記製造方法を提
供することを目的とする。(3) Problems to be Solved by the Invention However, according to the above manufacturing method, the amount of molten metal per powder cut by the high-pressure gas flow is large, and the cooling effect on the molten metal is insufficient. There is a problem in that it is difficult to obtain fine metal powder because the particle size distribution of the metal powder tends to be biased toward larger diameters. It is an object of the present invention to provide the above-mentioned manufacturing method capable of obtaining fine metal powder by employing suitable means.
B1発明の構成
(1) 課題を解決するための手段
本発明は、溶湯ノズルの下端面に開口する流出口より溶
湯を流出させ、また前記溶湯ノズルの流出口近傍に配設
された環状ガスノズルによる高圧ガス流を、それが前記
溶湯ノズルの下方で収斂するように円錐シェル形に形成
して、前記溶湯を前記高圧ガス流によ/9切断すること
によって粉末化するに当り、前記円錐シェル形高圧ガス
流を、それが前記溶湯ノズルの下端面外周縁に接触する
ように形成し、前記高圧ガス流が前記下端面外周縁を通
過することにより発生して前記流出口の溶湯を前記下端
面外周縁側に吸引する引圧p、と、前記溶湯ノズル内の
溶湯を前記流出口より流出させるための背圧1)l と
の関係を22≧p1に設定することによって、前記下端
面に添って流出する前記溶湯を前記下端面外周縁で前記
高圧ガス流により切断することを第1の特徴とする。B1 Structure of the Invention (1) Means for Solving the Problems The present invention provides a method for causing the molten metal to flow out from an outlet opening at the lower end face of a molten metal nozzle, and by an annular gas nozzle disposed near the outlet of the molten metal nozzle. forming a high-pressure gas stream in the shape of a conical shell so that it converges below the melt nozzle, and pulverizing the melt by cutting the melt by the high-pressure gas stream; A high-pressure gas flow is formed so that it contacts the outer circumferential edge of the lower end surface of the molten metal nozzle, and the high-pressure gas flow is generated by passing through the outer circumferential edge of the lower end surface, and the molten metal at the outlet is transferred to the lower end surface. By setting the relationship between the suction pressure p drawn toward the outer peripheral edge side and the back pressure 1)l for causing the molten metal in the molten metal nozzle to flow out from the outlet to 22≧p1, A first feature is that the flowing molten metal is cut at the outer peripheral edge of the lower end surface by the high pressure gas flow.
本発明は、前記溶湯ノズルとして、その流路の溶湯導入
側に前記背圧p、を減圧する絞りを備えたものを使用す
ることを第2の特徴とする。A second feature of the present invention is that the molten metal nozzle is provided with a restriction on the molten metal introduction side of the flow path for reducing the back pressure p.
(2)作 用
第1の特徴によれば、溶湯ノズルの下端面外周縁に存す
る溶湯が高圧ガス流により、その吸引作用で吸出されつ
\切断されるので、粉末1個当りの溶湯量が少なくなる
。(2) Effect According to the first feature, the molten metal existing on the outer periphery of the lower end surface of the molten metal nozzle is sucked out and cut by the suction action of the high-pressure gas flow, so the amount of molten metal per powder is reduced. It becomes less.
また、下端面外周縁に存する溶湯は、その蓋が少ない上
に、高圧ガス流の接触に伴い陵温される溶湯ノズルおよ
び高圧ガス流により冷却されるので、粉末化された後に
おける粉末相互の再接合の発生を回避することが可能で
ある。In addition, the molten metal existing on the outer periphery of the lower end surface has few lids, and is cooled by the molten metal nozzle and high-pressure gas flow, which heats the melt as it comes into contact with the high-pressure gas flow. It is possible to avoid the occurrence of rebonding.
このようにして、金属粉末の微細化が達成される。In this way, refinement of the metal powder is achieved.
第2の特徴によれば、溶湯に対する背圧p、の制御範囲
を拡張して、粉末製造作業の容易化を図ることが可能で
ある。According to the second feature, it is possible to expand the control range of the back pressure p on the molten metal, thereby facilitating powder manufacturing work.
(3)実施例
第1.第2図において、高圧Heガスアトマイズ法を実
施するための金属粉末用製造装置は、粉末製造部1と粉
未回収部2とを備え、粉末製造部1は上部の溶解チャン
バ3と下部の噴霧チャンバ4とよりなり、また粉末回収
8I!2は上部のサイクロン5と下部の回収ボット6と
よりなる。噴霧チャンバ4とサイクロン5とは導管7を
介しで接続される。(3) Example 1. In FIG. 2, the metal powder manufacturing apparatus for carrying out the high-pressure He gas atomization method includes a powder manufacturing section 1 and a powder unrecovered section 2, and the powder manufacturing section 1 has an upper melting chamber 3 and a lower spray chamber. 4 and more, powder collection 8I! 2 consists of an upper cyclone 5 and a lower collection bot 6. The spray chamber 4 and the cyclone 5 are connected via a conduit 7.
溶解チャンバ3内にるつぼ8が配設され、そのるつぼ8
の底壁に取付けられた溶湯ノズル9.が噴霧チ中ンバ4
内上部に位置する。溶湯ノズル91は上下方向に延びる
流路10を有し、その流入口11はるつぼ8内に向けて
開口し、また流出口12は溶湯ノズル9.の下端面13
に開口する。A crucible 8 is disposed within the melting chamber 3, and the crucible 8
Molten metal nozzle attached to the bottom wall of 9. is spraying inside 4
Located at the inner upper part. The molten metal nozzle 91 has a flow path 10 extending in the vertical direction, an inlet 11 of which opens into the crucible 8, and an outlet 12 of the molten metal nozzle 9. Lower end surface 13 of
Open to.
溶湯ノズル91の下部外周面に環状ガスノズル14が取
付けられ、そのガスノズル14にガス導入管15が接続
される。るつぼ8内にはス)7パ16が挿入され、その
ストツパ16により溶湯ノズル91の流入口11を閉鎖
し得るようになっている。An annular gas nozzle 14 is attached to the lower outer peripheral surface of the molten metal nozzle 91, and a gas introduction pipe 15 is connected to the gas nozzle 14. A stopper 16 is inserted into the crucible 8, and the stopper 16 can close the inlet 11 of the molten metal nozzle 91.
第3A図にも示すように、溶湯ノズル9.は、その下端
面13から下部外周面の所定位置までを先細りのテーパ
面17に形成される。ガスノズル14による高圧ガス流
gは、テーパ面16に沿った後、流出口12の中心延長
線上で収斂するように円錐シェル形に形成される。その
結果、高圧ガス流gは溶湯ノズル9.の下端面外周縁1
3aに接触することになる。As also shown in FIG. 3A, the molten metal nozzle 9. is formed into a tapered surface 17 from its lower end surface 13 to a predetermined position on the lower outer peripheral surface. The high-pressure gas flow g from the gas nozzle 14 is formed into a conical shell shape so as to converge on the central extension line of the outlet 12 after passing along the tapered surface 16 . As a result, the high pressure gas flow g flows through the molten metal nozzle 9. Lower end surface outer rim 1
3a will be contacted.
金属粉末の製造に当っては、第3A、第3B図に示すよ
うにるつぼ8内で溶湯mを調製し、その溶湯mを、それ
に背圧P+を作用させることによって溶湯ノズル9.の
流路10を通じ流出口12から流出させる。またガス導
入管15に高圧Heガスを供給し、そのHeガスをガス
ノズル14から噴射させることによって高圧ガス流gを
形成する。In producing metal powder, a molten metal m is prepared in a crucible 8 as shown in FIGS. 3A and 3B, and the molten metal m is passed through a molten metal nozzle 9 by applying a back pressure P+ to it. It is made to flow out from the outlet 12 through the flow path 10 . Further, high pressure He gas is supplied to the gas introduction pipe 15 and the He gas is injected from the gas nozzle 14 to form a high pressure gas flow g.
そして、高圧ガス流gが溶湯ノズル9.の下端面外周縁
13aを通過すると、高圧ガス流gの内側空rjIsは
減圧状態となって下端面13に沿う引圧Ptが発生し、
この引圧P、により流出口12の溶湯mが下端面外周縁
13a側に吸引される。Then, the high pressure gas flow g flows through the molten metal nozzle 9. When passing through the outer peripheral edge 13a of the lower end surface, the inner air space rjIs of the high-pressure gas flow g becomes depressurized, and a suction pressure Pt along the lower end surface 13 is generated.
This suction pressure P causes the molten metal m in the outlet 12 to be sucked toward the outer peripheral edge 13a of the lower end surface.
この場合、引圧p2と前圧p1との関係はpヨ≧P+に
設定されるので、溶湯mは流出口12より下端面13に
添ってその外周縁13aに向けて流出する。In this case, since the relationship between the suction pressure p2 and the front pressure p1 is set to pyo≧P+, the molten metal m flows out from the outlet 12 along the lower end surface 13 toward its outer peripheral edge 13a.
これにより、溶湯ノズル91の下端面外周縁13aに存
する溶湯mが高圧ガス流gにより、その吸引作用で吸出
されつ一切断されるので、粉末1個当りの溶湯量が少な
くなる。As a result, the molten metal m existing on the outer peripheral edge 13a of the lower end face of the molten metal nozzle 91 is sucked out by the suction action of the high-pressure gas flow g and is cut off, thereby reducing the amount of molten metal per powder.
また、下端面外周縁13aに存する溶湯mは、その量が
少ない上に、高圧ガス流gの接触に伴い降温される溶湯
ノズル91および高圧ガス流gにより冷却されるので、
粉末化された後における粉末相互の再接合の発生を回避
することが可能である。In addition, the amount of molten metal m existing on the outer peripheral edge 13a of the lower end surface is small, and it is cooled by the molten metal nozzle 91 and the high-pressure gas flow g, whose temperature is lowered by contact with the high-pressure gas flow g.
It is possible to avoid the occurrence of re-bonding of the powders after they have been pulverized.
このようにして、金属粉末Pmの微細化が達成される。In this way, refinement of the metal powder Pm is achieved.
第4図は溶湯ノズルの変形例を示し、その溶湯ノズル9
□は流路10の溶湯導入側に背圧P+を減圧する絞り1
8を備えている。FIG. 4 shows a modification of the molten metal nozzle, and the molten metal nozzle 9
□ is a throttle 1 that reduces the back pressure P+ on the molten metal introduction side of the flow path 10
It is equipped with 8.
このような溶湯ノズル9□を使用すると、溶湯mに対す
る背圧P1の制御範囲を拡張して、例えば、第4図鎖線
示のように絞り18よりも下流側において溶湯mを流路
10内周面に添わせながら流出させ、前記背圧p、と引
圧P2との関係を容易に成立させることにより粉末製造
作業の容易化を図ることが可能である。When such a molten metal nozzle 9□ is used, the control range of the back pressure P1 for the molten metal m can be expanded, and for example, the molten metal m can be directed to the inner periphery of the flow path 10 on the downstream side of the throttle 18 as shown by the chain line in FIG. By allowing the powder to flow out along the surface and easily establishing the relationship between the back pressure p and the suction pressure P2, it is possible to facilitate the powder manufacturing operation.
なお、背圧p、の調節因子としては、前記絞り18の外
に、溶湯ノズル9..9.の内径、溶湯mの粘度等が挙
げられる。In addition to the throttle 18, the back pressure p is adjusted by the molten metal nozzle 9. .. 9. Examples include the inner diameter of m, the viscosity of the molten metal m, etc.
〔実施例]
下表は、第2図に示す溶湯ノズル9Iを用い、各種製造
条件の下でアルミニウム合金粉末を製造した場合を示す
。[Example] The table below shows the case where aluminum alloy powder was manufactured under various manufacturing conditions using the molten metal nozzle 9I shown in FIG. 2.
溶湯mは6重量%Cr、2重量%Zr、3重量%Feを
含有するアルミニウム合金溶湯、るつぼ8および溶湯ノ
ズル9Iの材質はグラファイト、るつぼ8への原料装入
量は約2kg、溶湯温度は1200°C,Heガス圧は
100kgf/dである。The molten metal m is an aluminum alloy molten metal containing 6% by weight Cr, 2% by weight Zr, and 3% by weight Fe, the material of the crucible 8 and the molten metal nozzle 9I is graphite, the amount of raw material charged into the crucible 8 is about 2 kg, and the molten metal temperature is The temperature was 1200°C and the He gas pressure was 100 kgf/d.
表において、本発明■〜■は前記製造法に則ったもので
あり、一方、従来例I〜■は、第3A図鎖線示のように
溶湯mを溶湯ノズル9Iの流出口12から略柱状に流下
させた場合に該当する。この場合、背圧p1の方が引圧
p:よりも大、即ちP+>Plに設定される。In the table, the present inventions 1 to 2 are based on the above-mentioned manufacturing method, while the conventional examples I to 2 are the ones in which the molten metal m is flowed into a substantially columnar shape from the outlet 12 of the molten metal nozzle 9I as shown by the chain line in FIG. 3A. This applies when the water is allowed to flow down. In this case, the back pressure p1 is set to be larger than the suction pressure p:, that is, P+>Pl.
第5図はアルミニウム合金粉末の粒度分布を示し、同図
(a)は表中の本発明■に、また同図(ロ)は表中の従
来例■にそれぞれ該当する。FIG. 5 shows the particle size distribution of aluminum alloy powder, and FIG. 5(a) corresponds to the present invention (■) in the table, and FIG. 5(b) corresponds to the conventional example (■) in the table.
前記表および第5図から明らかなように、本発明■〜■
によれば、アルミニウム合金粉末の粒度分布が粉末直径
の小さい方に偏っており、また平均直径も小さくなるこ
とが判る。As is clear from the above table and FIG. 5, the present inventions ■ to ■
According to , it can be seen that the particle size distribution of aluminum alloy powder is biased toward smaller powder diameters, and the average diameter is also smaller.
C1発明の効果
第(1)請求項記載の発明によれば、溶湯に作用する背
圧P+および引圧Pzを前記のように特定することによ
って微細な金属粉末を得ることができる。C1 Effect of the Invention According to the invention described in claim (1), fine metal powder can be obtained by specifying the back pressure P+ and suction pressure Pz acting on the molten metal as described above.
第(2)請求項記載の発明によれば、前記背圧p。According to the invention recited in claim (2), the back pressure p.
および引圧Pgの関係を容易に成立させて、微細な金属
粉末の製造能率を向上させることができる。and suction pressure Pg can be easily established to improve the production efficiency of fine metal powder.
第1図は金属粉末用製造装置の全体正面図、第2図は第
1図の要部縦断正面図、第3A図は溶湯ノズルを用いた
粉末製造法の説明図、第3B図は第3A図mb−mb線
断面図、第4図は18iJiノズルの変形例を示す縦断
正面図、第5図はアルミニウム合金粉末の粒度分布図で
ある。
と・・高圧ガス流、m・・・溶湯、Pl・・・背圧、p
2・・引圧、Pm・・・金属粉末、95.9z・・・溶
湯ノズル、10・・・流路、12・・・流出口、13・
・・下端面、13a・・・下端面外周縁、14・・・環
状ガスノズル、18・・・絞りFig. 1 is an overall front view of the metal powder manufacturing equipment, Fig. 2 is a longitudinal sectional front view of the main part of Fig. 1, Fig. 3A is an explanatory diagram of the powder manufacturing method using a molten metal nozzle, and Fig. 3B is a 3A 4 is a longitudinal sectional front view showing a modified example of the 18iJi nozzle, and FIG. 5 is a particle size distribution diagram of aluminum alloy powder. and...high pressure gas flow, m...molten metal, Pl...back pressure, p
2... Suction pressure, Pm... Metal powder, 95.9z... Molten metal nozzle, 10... Channel, 12... Outlet, 13...
... lower end surface, 13a ... lower end surface outer periphery, 14 ... annular gas nozzle, 18 ... aperture
Claims (2)
に開口する流出口(12)より溶湯(m)を流出させ、
また前記溶湯ノズル(9_1、9_2)の流出口(12
)近傍に配設された環状ガスノズル(14)による高圧
ガス流(g)を、それが前記溶湯ノズル(9_1、9_
2)の下方で収斂するように円錐シェル形に形成して、
前記溶湯(m)を前記高圧ガス流(g)により切断する
ことによって粉末化するに当り、前記円錐シェル形高圧
ガス流(g)を、それが前記溶湯ノズル(9_1、9_
2)の下端面外周縁(13a)に接触するように形成し
、前記高圧ガス流(g)が前記下端面外周縁(13a)
を通過することにより発生して前記流出口(12)の溶
湯(m)を前記下端面外周縁(13a)側に吸引する引
圧p_2と、前記溶湯ノズル(9_1、9_2)内の溶
湯(m)を前記流出口(12)より流出させるための背
圧p_1との関係をp_2≧p_1に設定することによ
って、前記下端面(13)に添って流出する前記溶湯(
m)を前記下端面外周縁(13a)で前記高圧ガス流(
g)により切断することを特徴とする金属粉末の製造方
法。(1) Lower end surface (13) of molten metal nozzle (9_1, 9_2)
Let the molten metal (m) flow out from the outlet (12) that opens at
In addition, the outlet (12) of the molten metal nozzle (9_1, 9_2)
) The annular gas nozzle (14) disposed near the molten metal nozzle (9_1, 9_
2) Formed into a conical shell shape so as to converge below,
In pulverizing the molten metal (m) by cutting it with the high-pressure gas stream (g), the conical shell-shaped high-pressure gas stream (g) is connected to the molten metal nozzle (9_1, 9_
2) is formed so as to contact the outer peripheral edge (13a) of the lower end surface, and the high pressure gas flow (g) is formed so as to contact the outer peripheral edge (13a) of the lower end surface.
suction pressure p_2 that is generated by passing the molten metal (m) at the outlet (12) and sucks the molten metal (m) toward the outer peripheral edge (13a) of the lower end face; By setting the relationship between the back pressure p_1 and the back pressure p_1 for causing the molten metal ( ) to flow out from the outlet (12) to be p_2≧p_1, the molten metal (
m) at the outer peripheral edge (13a) of the lower end surface of the high pressure gas flow (
A method for producing metal powder, which comprises cutting by g).
0)の溶湯導入側に前記背圧p_1を減圧する絞り(1
8)を備えたものを使用する、第(1)項記載の金属粉
末の製造方法。(2) As the molten metal nozzle (9_2), its flow path (1
0) on the molten metal introduction side to reduce the back pressure p_1.
8), the method for producing metal powder according to item (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15042090A JPH0441607A (en) | 1990-06-08 | 1990-06-08 | Metal powder manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15042090A JPH0441607A (en) | 1990-06-08 | 1990-06-08 | Metal powder manufacturing method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0441607A true JPH0441607A (en) | 1992-02-12 |
Family
ID=15496551
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15042090A Pending JPH0441607A (en) | 1990-06-08 | 1990-06-08 | Metal powder manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0441607A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04276005A (en) * | 1991-03-01 | 1992-10-01 | Kobe Steel Ltd | Production of fine metal powder |
| JPH0566027U (en) * | 1992-02-20 | 1993-08-31 | 帝国ピストンリング株式会社 | Molten metal nozzle for flat metal powder manufacturing equipment |
| JPH0688202A (en) * | 1992-06-18 | 1994-03-29 | General Electric Co <Ge> | Nozzle for atomizing molten metal and method for atomizing molten metal |
-
1990
- 1990-06-08 JP JP15042090A patent/JPH0441607A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04276005A (en) * | 1991-03-01 | 1992-10-01 | Kobe Steel Ltd | Production of fine metal powder |
| JPH0566027U (en) * | 1992-02-20 | 1993-08-31 | 帝国ピストンリング株式会社 | Molten metal nozzle for flat metal powder manufacturing equipment |
| JPH0688202A (en) * | 1992-06-18 | 1994-03-29 | General Electric Co <Ge> | Nozzle for atomizing molten metal and method for atomizing molten metal |
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