JPH1017909A - Production of metal powder - Google Patents

Production of metal powder

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Publication number
JPH1017909A
JPH1017909A JP17760796A JP17760796A JPH1017909A JP H1017909 A JPH1017909 A JP H1017909A JP 17760796 A JP17760796 A JP 17760796A JP 17760796 A JP17760796 A JP 17760796A JP H1017909 A JPH1017909 A JP H1017909A
Authority
JP
Japan
Prior art keywords
molten metal
metal powder
rotating body
metal
molten
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
JP17760796A
Other languages
Japanese (ja)
Inventor
Kazuo Matsui
一雄 松井
Takaaki Yasumura
隆明 安村
Yoshiteru Nakagawa
吉輝 中川
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.)
FDK Corp
Original Assignee
FDK 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 FDK Corp filed Critical FDK Corp
Priority to JP17760796A priority Critical patent/JPH1017909A/en
Publication of JPH1017909A publication Critical patent/JPH1017909A/en
Pending legal-status Critical Current

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  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce the size distribution of the obtained metal powder and to improve its yield by radialy forming plural projections on the surface of a rotary body on which molten metal is dropped and stopping the molten metal accumulated on a disk by the projected parts. SOLUTION: Molten metal continuously drops on the opening parts 7 of a rotary body 3 rotating at a high speed and is sprayed on the inside of a chamber by centrifugal force. The scattered misty molten metal is cooled and solidified in an atmosphere of an inert gas or the like and is formed into irregular shaped metal powder. At this time, the plural projecting parts 5 radialy extending to the outer circumferential side edge faces from the cinter side of the rotary body 3 are formed at equal intervals. In this way, the molten metal accumulated on the face of the rotary body 3 is stopped, and the further delay to the back side (the direction reverse to the rotating direction) is prevented. By this clogging and checking effect, the delay of the moving rate in the molten body is relaxed, and the difference in the moving rates between the upper and lower artscan be reduced. Thus, the releasing rate of the molten metal can be uniformized, and the size number in the metal powder cam be suppressed to a nallow low range 3.

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、粒径分布の狭い金
属粉末の製造を可能とする金属粉末の製造装置に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing a metal powder capable of producing a metal powder having a narrow particle size distribution.

【0002】[0002]

【従来の技術】従来より、この種の金属粉末の製造装置
としては、チャンバー内で溶融金属を高速回転(例えば
2000〜40000rpm)する円錐型またはV字型
の円板上に連続的に滴下し、回転時の遠心力により円板
上に溜まった溶融金属を飛散・凝固させるものが周知で
ある(実開昭58−45329号公報)。
2. Description of the Related Art Conventionally, as an apparatus for producing this kind of metal powder, a molten metal is continuously dropped on a conical or V-shaped disk which rotates at a high speed (for example, 2000 to 40000 rpm) in a chamber. A method of scattering and solidifying molten metal accumulated on a disk by a centrifugal force during rotation is well known (Japanese Utility Model Application Laid-Open No. 58-32929).

【0003】[0003]

【発明が解決しようとする課題】しかしながら、図6に
示すように、前記回転体3の溶融金属が滴下する側の面
がフラット形状であると、高速回転によって層状に溜ま
った溶融金属の高さ(厚み)方向に滑りが発生し、回転
体3と溶融金属との間で回転速度(移動速度)に差が生
じてしまう。
However, as shown in FIG. 6, if the surface of the rotating body 3 on which the molten metal is dropped is flat, the height of the molten metal accumulated in a layer by high-speed rotation is increased. Slip occurs in the (thickness) direction, and a difference occurs in the rotation speed (moving speed) between the rotating body 3 and the molten metal.

【0004】又、図7に示すように、前記溶融金属の移
動速度は溶融層の上部になる程遅くなり、このため、回
転体3からの放出スピードに差が生じて飛散する流体の
大きさがばらつき、得られる金属粉末の粒径が広範囲に
分布してしまう。
Further, as shown in FIG. 7, the moving speed of the molten metal becomes slower toward the upper part of the molten layer, so that there is a difference in the discharge speed from the rotating body 3 and the size of the scattered fluid is increased. And the particle size of the obtained metal powder is distributed over a wide range.

【0005】希望する粒径の金属粉末を得るためには、
後工程で作製された金属粉末を一旦メッシュ等で振るい
分けしなければならないが、このように粒径分布が広い
と金属粉末の歩留まりが悪くなる。
In order to obtain a metal powder having a desired particle size,
The metal powder produced in the subsequent process must be once sorted through a mesh or the like, but if the particle size distribution is wide as described above, the yield of the metal powder deteriorates.

【0006】本発明の目的は、上記欠点を解消し、金属
粉末の粒径分布を改善(小さくする)して歩留まりの向
上を図った金属粉末の製造装置を提供することである。
An object of the present invention is to provide a metal powder manufacturing apparatus which solves the above-mentioned drawbacks and improves (reduces) the particle size distribution of the metal powder to improve the yield.

【0007】[0007]

【課題を解決するための手段】即ち、請求項1に記載の
本発明では、溶融金属(4)を高速回転する回転体
(3)上に滴下して金属粉末(8)を製造する金属粉末
の製造装置において、前記回転体(3)が円柱型又は円
錐型又はV字型の円板状であり、且つこの回転体(3)
の前記溶融金属(4)が滴下する側の面に、円板中央部
より外周側端面まで放射状に延びる複数本の突起部
(5)を中心部分を切り離して開放部(7)を設ける形
で形成したことを特徴とする。
According to the first aspect of the present invention, a metal powder is produced by dropping a molten metal (4) onto a rotating body (3) rotating at a high speed to produce a metal powder (8). In the manufacturing apparatus of (1), the rotating body (3) has a cylindrical, conical or V-shaped disk shape, and the rotating body (3)
A plurality of projections (5) extending radially from the central part of the disk to the outer peripheral end face are cut off from the central part of the surface on the side where the molten metal (4) is dropped to form an open part (7). It is characterized by having been formed.

【0008】又、請求項2に記載の本発明では、前記突
起部(5)の円板外周側の端面に高さ方向に曲面(R)
を設けたことを特徴とする。
According to the second aspect of the present invention, a curved surface (R) is formed on the end surface of the projection (5) on the outer peripheral side of the disk in the height direction.
Is provided.

【0009】更に、請求項3に記載の本発明では、前記
金属粉末(8)はアルカリ電池の負極用活物質として使
用する不定形状の亜鉛粉末であることを特徴とする。
Further, according to the present invention, the metal powder (8) is an irregular-shaped zinc powder used as an active material for a negative electrode of an alkaline battery.

【0010】[0010]

【発明の実施の形態】図1は本発明に係る金属粉末の製
造装置の概略構成を示す図である。
FIG. 1 is a diagram showing a schematic configuration of an apparatus for producing metal powder according to the present invention.

【0011】図中、1は密閉チャンバーであって、場合
により不活性ガスが導入される。前記チャンバー1の頂
部に金属を溶融するためのルツボ2が付設されており、
ルツボ2の底部に前記溶融金属4を滴下するノズル9が
設けられている。このノズル9の略真下に回転体3が配
設されている。又、8はチャンバー1の底部に蓄積した
金属粉末であって、10はこの金属粉末8を取り出すた
めの取出口である。
In FIG. 1, reference numeral 1 denotes a closed chamber to which an inert gas is introduced as the case may be. A crucible 2 for melting metal is provided at the top of the chamber 1,
A nozzle 9 for dropping the molten metal 4 is provided at the bottom of the crucible 2. The rotating body 3 is disposed substantially directly below the nozzle 9. Reference numeral 8 denotes metal powder accumulated at the bottom of the chamber 1, and reference numeral 10 denotes an outlet for taking out the metal powder 8.

【0012】図2は前記回転体3の外観斜視図である。
この回転体3は、外径が40mm程度の断面V字型の円
板で、その傾斜角は中心線に対して例えば約13゜〜2
0゜の範囲に設定されており、その材質は滴下される溶
融金属8の物性との関係より黒鉛等の耐火性の材料が使
用されている。
FIG. 2 is an external perspective view of the rotating body 3.
The rotating body 3 is a disk having an outer diameter of about 40 mm and a V-shaped cross section, and its inclination angle is, for example, about 13 ° to 2 ° with respect to the center line.
The angle is set in the range of 0 °, and a refractory material such as graphite is used for the material in view of the relationship with the physical properties of the molten metal 8 to be dropped.

【0013】又、前記回転体3軸部6に、この回転体3
を高速回転させるための回転装置(図示せず)が取り付
けられている。
Also, the rotating body 3 is provided on the rotating body 3 shaft 6.
A rotating device (not shown) for rotating at high speed is mounted.

【0014】係る形状の回転体3は公知であるが、本実
施形態では、回転体3の溶融金属4が滴下する側の面
に、その中心側より外周側端面まで延びる高さ0.7〜
2mm程度の細長い角柱状の突起部5が放射状に、且つ
等間隔で4本形成されていることを特徴としている。
Although the rotating body 3 having such a shape is known, in the present embodiment, the height of the rotating body 3 extending from the center side to the outer peripheral side end surface on the surface of the rotating body 3 on which the molten metal 4 is dropped is 0.7 to 0.7 mm.
It is characterized in that four elongated prism-shaped projections 5 of about 2 mm are formed radially and at equal intervals.

【0015】この放射状突起部5の中心部分が夫々切り
離されて、前記ノズル9より溶融金属4を滴下する円状
の開放部7が形成されており、且つ図2(b) に示すよう
に、この突起部5の外周側の端面に高さ方向に曲面Rが
設けられている。
The central portion of each of the radial projections 5 is cut off to form a circular opening 7 into which the molten metal 4 is dropped from the nozzle 9, and as shown in FIG. A curved surface R is provided on an end surface on the outer peripheral side of the protrusion 5 in the height direction.

【0016】図3は前記ノズル9より滴下された溶融金
属4が回転体3より飛散する様子を示す図である。
FIG. 3 is a view showing how molten metal 4 dropped from the nozzle 9 scatters from the rotating body 3.

【0017】金属(例えば亜鉛又は亜鉛合金等)が前記
ルツボ2で溶融され、このルツボ2内の溶融金属4が底
部に設けられたノズル9より、その略真下に位置する回
転体3の開放部7部分にノズル9の孔径で決まる所定の
流量で連続的に滴下されていく。この時、回転体3はそ
の軸部6に連結された前記回転装置によって高速で回転
しており、滴下された溶融金属4はその粘性によって高
速回転するV字型円板の中心部より外周側に向けて層状
に溜まっていき、回転時の遠心力でその端面から順次チ
ャンバー1内に噴霧される。
A metal (for example, zinc or a zinc alloy) is melted in the crucible 2, and the molten metal 4 in the crucible 2 is opened from a nozzle 9 provided at the bottom of the crucible 2 by an opening of the rotating body 3 located almost directly below the nozzle 9. Drops are continuously dropped on the seven portions at a predetermined flow rate determined by the hole diameter of the nozzle 9. At this time, the rotating body 3 is rotating at a high speed by the rotating device connected to the shaft portion 6, and the molten metal 4 dropped from the central portion of the V-shaped disk which rotates at a high speed due to its viscosity is located on the outer peripheral side. And is sprayed into the chamber 1 sequentially from the end face by centrifugal force at the time of rotation.

【0018】チャンバー1内に飛散した霧状の溶融金属
4は、不活性ガス等の雰囲気中で冷却・凝固して不定形
状の金属粉末8となって前記チャンバー1の底部に蓄積
する。この場合、飛散した溶融金属4の粒子が冷えて凝
固する前にチャンバー1の内壁に衝突しないよう、前記
チャンバー1の大きさが設定されている。
The mist-like molten metal 4 scattered in the chamber 1 is cooled and solidified in an atmosphere of an inert gas or the like to form an irregularly shaped metal powder 8 and accumulates at the bottom of the chamber 1. In this case, the size of the chamber 1 is set so that the scattered molten metal particles 4 do not collide with the inner wall of the chamber 1 before cooling and solidifying.

【0019】ところで、高速回転する前記回転体3上の
溶融金属4は、その粘性による摩擦力で回転体3と共に
回転(移動)しているが、既述したように、高速回転時
の滑りによって、この溶融金属4(溶融体)の高さ方向
に回転速度(移動速度)の差が生じ、この速度差は上層
になる程大きくなっていく。
The molten metal 4 on the rotating body 3 that rotates at high speed rotates (moves) together with the rotating body 3 due to the frictional force due to its viscosity. A difference in rotational speed (moving speed) occurs in the height direction of the molten metal 4 (melt), and the difference in speed increases as the layer becomes higher.

【0020】そこで、本発明では、図2に示すように回
転体3の中心側より外周側端面まで放射状に延びる4本
の突起部5を等間隔に形成した。係る構成であれば、回
転体3の面上に溜まった溶融金属4が前記突起部5によ
って塞き止められる形となり、それ以上後側(回転方向
と逆の方向)に遅れることは無くなる。このような塞き
止め効果によって、溶融体内の移動速度の遅れが緩和さ
れ、図4に示すように、従来例(図7参照)に比べて溶
融体の上下部での移動速度差を少なくできる。このた
め、溶融金属4の放出スピードが均一化されて作製され
る金属粉末8の粒径分布を狭い範囲に抑えることができ
る。
Therefore, in the present invention, as shown in FIG. 2, four protrusions 5 extending radially from the center side of the rotating body 3 to the outer peripheral end face are formed at equal intervals. With such a configuration, the molten metal 4 accumulated on the surface of the rotating body 3 is blocked by the protrusions 5, and there is no further delay behind (in the direction opposite to the rotation direction). Due to such a blocking effect, the delay of the moving speed in the melt is reduced, and as shown in FIG. 4, the difference in the moving speed between the upper and lower portions of the melt can be reduced as compared with the conventional example (see FIG. 7). . For this reason, the particle size distribution of the metal powder 8 produced by making the discharge speed of the molten metal 4 uniform can be suppressed to a narrow range.

【0021】又、図2(b) の部分拡大図に示すように、
前記突起部5の外周側端面に高さ方向にR加工を施すこ
とによって、溶融金属4がこの曲面Rの縁部に沿って均
等に分散されて、溶融体の飛散方向が回転体3の半径方
向に集中するようになり、作製される金属粉末8の粒径
分布はより向上する。
Also, as shown in the partially enlarged view of FIG.
By subjecting the outer peripheral end face of the projection 5 to R processing in the height direction, the molten metal 4 is evenly distributed along the edge of the curved surface R, and the scattering direction of the molten material is the radius of the rotating body 3. As a result, the particle size distribution of the produced metal powder 8 is further improved.

【0022】換言すれば、前記突起部5の外周側端面が
高さ方向にR加工されず直角形状であると、多くの溶融
金属4がこの角部分に集中し、そこから上下方向にラン
ダムに飛散してしまうため、相当量の溶融体粒子が凝固
する前にチャンバー1の内壁に衝突して大型粒径の粉体
を形成する。このため、金属粉体8の粒径分布が悪化す
る。
In other words, if the outer peripheral end surface of the protrusion 5 is not R-processed in the height direction and has a right-angled shape, a large amount of molten metal 4 is concentrated at this corner, and the molten metal 4 is randomly distributed vertically therefrom. Since the molten particles are scattered, the molten particles collide with the inner wall of the chamber 1 before solidifying to form a powder having a large particle diameter. For this reason, the particle size distribution of the metal powder 8 deteriorates.

【0023】以上、実施形態では、回転体3として断面
V字型のものを示したが、その形状は円柱型や円錐型で
あっても良い。又、前記回転体3に設けた突起部5は放
射状に配置されていれば、形状は上記実施形態に限定さ
れるものではなく、その本数も2本以上であれば、回転
体3の回転数や溶融される金属等に応じて適宜設定すれ
ば良い。
As described above, in the embodiment, the rotating body 3 has a V-shaped cross section, but the rotating body 3 may have a cylindrical or conical shape. The shape is not limited to the above embodiment as long as the protrusions 5 provided on the rotating body 3 are arranged radially, and the number of rotations of the rotating body 3 is not limited as long as the number is two or more. It may be set as appropriate according to the type of metal to be melted.

【0024】[0024]

【実施例】次に、本発明の金属粉末の製造装置と従来の
金属粉末の製造装置を用いて亜鉛粉末を作製し、粒径分
布の状態を調査した。
EXAMPLES Next, zinc powder was produced using the apparatus for producing metal powder of the present invention and a conventional apparatus for producing metal powder, and the state of particle size distribution was examined.

【0025】使用する回転体3は、円板の径は40m
m、形状は角度13゜の断面V字型とし、本発明の装置
の場合は、これに高さ2mmの突起部5を4本形成し
た。
The rotating body 3 used has a disk diameter of 40 m.
m, the shape was a V-shaped cross section at an angle of 13 °, and in the case of the device of the present invention, four protrusions 5 having a height of 2 mm were formed on the device.

【0026】又、遠心アトマイズ条件は、従来例、本発
明共に亜鉛溶融温度は約500℃、回転体3の回転数は
10000rpm、ノズル9の径は1.5Φmmとし
た。アトマイズ雰囲気は、酸素約21%(大気)とし
た。
The centrifugal atomization conditions for both the conventional example and the present invention were such that the zinc melting temperature was about 500 ° C., the number of revolutions of the rotating body 3 was 10,000 rpm, and the diameter of the nozzle 9 was 1.5 mm. The atomizing atmosphere was about 21% oxygen (atmosphere).

【0027】前記条件にて作製された亜鉛粉末8をメッ
シュで振るい分けして総重量に対する各粒径群の重量比
(%)を測定し、その分布状況を図5に示した。
The zinc powder 8 produced under the above conditions was sifted through a mesh, and the weight ratio (%) of each particle size group to the total weight was measured. The distribution is shown in FIG.

【0028】図5によれば、破線で示す従来品では、粒
径分布が大粒側(粒径125μm以上)に広く分布し、
希望する粒径の亜鉛粉末を効率良く得ることは難しい。
これに対し、実線で示す本発明品では、大粒側が減少し
て希望する粒径125〜250μmの範囲に急峻なピー
クを持つ粒径分布が得られている。
According to FIG. 5, in the conventional product shown by the broken line, the particle size distribution is widely distributed on the large particle side (particle size of 125 μm or more).
It is difficult to efficiently obtain zinc powder having a desired particle size.
On the other hand, in the product of the present invention indicated by the solid line, the particle size distribution having a sharp peak in the desired particle size range of 125 to 250 μm due to a decrease in the large particle side is obtained.

【0029】以上のように、本発明の金属粉末の製造装
置では、回転体3の面上に放射状に突起部5を配置して
滴下された溶融金属4を塞き止め、層状に溜まった溶融
金属4の高さ方向の移動速度差を小さくすることによっ
て、飛散時の溶融体粒子の径を一定にすると共に前記突
起部5の外周側端面に高さ方向にR加工を施すことで、
溶融体粒子の飛散方向を安定させることが可能となる。
これらによって得られる金属粉末8の粒径分布が大幅に
向上するため、歩留まりの良い金属粉末の製造が可能と
なる。
As described above, in the apparatus for producing metal powder of the present invention, the protrusions 5 are arranged radially on the surface of the rotating body 3 to block the dropped molten metal 4 and to prevent the molten metal 4 accumulated in a layer form. By reducing the difference in the moving speed of the metal 4 in the height direction, the diameter of the melt particles at the time of scattering is kept constant, and the outer peripheral end face of the protrusion 5 is subjected to R processing in the height direction,
It is possible to stabilize the scattering direction of the melt particles.
Since the particle size distribution of the obtained metal powder 8 is greatly improved, it is possible to produce a metal powder with a high yield.

【0030】[0030]

【発明の効果】以上説明したように、請求項1に記載の
本発明によれば、溶融金属が滴下される側の回転体の面
上に複数本の突起部を放射状に形成したので、円板上に
溜まった溶融金属はこの突起部で塞き止められ、溶融体
の上下層の移動速度差を小さくする。このため、回転体
からの放出スピードが均一化されて、作製される金属粉
末の粒径分布を狭くすることが可能となる。
As described above, according to the first aspect of the present invention, since a plurality of projections are radially formed on the surface of the rotating body on which the molten metal is dropped, a circular shape is obtained. The molten metal accumulated on the plate is blocked by these projections, and reduces the difference in moving speed between the upper and lower layers of the molten material. For this reason, the discharge speed from the rotating body is made uniform, and the particle size distribution of the produced metal powder can be narrowed.

【0031】又、請求項2に記載の本発明によれば、前
記突起部の外周側端面に高さ方向に曲面を設けたので、
溶融体粒子の飛散方向が回転体の半径方向に集中するよ
うになり、作製される金属粉末の粒径分布はより向上す
る。
According to the second aspect of the present invention, since the projection has a curved surface in the height direction on the outer peripheral end surface,
The scattering direction of the melt particles is concentrated in the radial direction of the rotating body, and the particle size distribution of the produced metal powder is further improved.

【0032】更に、請求項3に記載の本発明によれば、
アルカリ電池の負極活物質に用いる不定形亜鉛粉末の製
造に本発明の金属粉末の製造装置を用いれば、粒径分布
も良好であるため歩留まりは良く、生産性が大幅に向上
する。
Further, according to the third aspect of the present invention,
If the apparatus for producing a metal powder of the present invention is used for producing the amorphous zinc powder used for the negative electrode active material of the alkaline battery, the particle size distribution is good, so that the yield is good and the productivity is greatly improved.

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

【図1】本発明に係る金属粉末の製造装置の概略構成を
示す図である。
FIG. 1 is a diagram showing a schematic configuration of an apparatus for producing metal powder according to the present invention.

【図2】同、金属粉末の製造装置の回転体を示す図で、
(a) は外観斜視図、(b) は側面図及び部分拡大図、(c)
は平面図である。
FIG. 2 is a view showing a rotating body of the same metal powder manufacturing apparatus;
(a) is an external perspective view, (b) is a side view and a partially enlarged view, (c)
Is a plan view.

【図3】溶融金属が回転体より飛散する様子を示す図で
ある。
FIG. 3 is a view showing a state where molten metal is scattered from a rotating body.

【図4】同、金属粉末の製造装置の回転体上に溜まった
溶融金属の高さ方向の移動速度差を示す図である。
FIG. 4 is a view showing a difference in a moving speed in a height direction of molten metal accumulated on a rotating body of the metal powder manufacturing apparatus.

【図5】亜鉛粉末の粒径分布を示す図である。FIG. 5 is a diagram showing a particle size distribution of zinc powder.

【図6】従来の金属粉末の製造装置の回転体を示す図
で、(a) は外観斜視図、(b) は側面図である。
6A and 6B are views showing a rotating body of a conventional metal powder manufacturing apparatus, wherein FIG. 6A is an external perspective view and FIG. 6B is a side view.

【図7】同、金属粉末の製造装置の回転体上に溜まった
溶融金属の高さ方向の移動速度差を示す図である。
FIG. 7 is a view showing a difference in a moving speed in a height direction of the molten metal accumulated on a rotating body of the metal powder producing apparatus.

【符号の説明】[Explanation of symbols]

3 回転体 4 溶融金属(溶融亜鉛) 5 突起部 7 開放部 8 金属粉末(亜鉛粉末) R 曲面 3 Rotating Body 4 Molten Metal (Molten Zinc) 5 Projection 7 Open Section 8 Metal Powder (Zinc Powder) R Curved Surface

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 溶融金属(4)を高速回転する回転体
(3)上に滴下して金属粉末(8)を製造する金属粉末
の製造装置において、 前記回転体(3)が円柱型又は円錐型又はV字型の円板
状であり、 且つこの回転体(3)の前記溶融金属(4)が滴下する
側の面に、円板中央部より外周側端面まで放射状に延び
る複数本の突起部(5)を中心部分を切り離して開放部
(7)を設ける形で形成したことを特徴とする金属粉末
の製造装置。
1. A metal powder manufacturing apparatus for manufacturing a metal powder (8) by dropping a molten metal (4) onto a rotating body (3) rotating at high speed, wherein the rotating body (3) is cylindrical or conical. And a plurality of protrusions extending radially from the center of the disk to the outer peripheral end surface on the surface of the rotating body (3) on which the molten metal (4) is dropped. An apparatus for producing a metal powder, characterized in that the part (5) is formed by cutting off the central part and providing an open part (7).
【請求項2】 前記突起部(5)の円板外周側の端面に
高さ方向に曲面(R)を設けたことを特徴とする請求項
1に記載の金属粉末の製造装置。
2. The metal powder producing apparatus according to claim 1, wherein a curved surface (R) is provided in a height direction on an end surface of the protrusion (5) on the outer peripheral side of the disk.
【請求項3】 前記金属粉末(8)はアルカリ電池の負
極用活物質として使用する不定形状の亜鉛粉末であるこ
とを特徴とする請求項1又は請求項2に記載の金属粉末
の製造装置。
3. The apparatus for producing a metal powder according to claim 1, wherein the metal powder (8) is an irregular-shaped zinc powder used as an active material for a negative electrode of an alkaline battery.
JP17760796A 1996-07-08 1996-07-08 Production of metal powder Pending JPH1017909A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17760796A JPH1017909A (en) 1996-07-08 1996-07-08 Production of metal powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17760796A JPH1017909A (en) 1996-07-08 1996-07-08 Production of metal powder

Publications (1)

Publication Number Publication Date
JPH1017909A true JPH1017909A (en) 1998-01-20

Family

ID=16033965

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17760796A Pending JPH1017909A (en) 1996-07-08 1996-07-08 Production of metal powder

Country Status (1)

Country Link
JP (1) JPH1017909A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007287627A (en) * 2006-04-20 2007-11-01 Fdk Energy Co Ltd Alkaline dry cell

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007287627A (en) * 2006-04-20 2007-11-01 Fdk Energy Co Ltd Alkaline dry cell

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