JPH0368922B2 - - Google Patents

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Publication number
JPH0368922B2
JPH0368922B2 JP60291329A JP29132985A JPH0368922B2 JP H0368922 B2 JPH0368922 B2 JP H0368922B2 JP 60291329 A JP60291329 A JP 60291329A JP 29132985 A JP29132985 A JP 29132985A JP H0368922 B2 JPH0368922 B2 JP H0368922B2
Authority
JP
Japan
Prior art keywords
powder
amorphous
molten metal
alloy
suction tube
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 - Lifetime
Application number
JP60291329A
Other languages
Japanese (ja)
Other versions
JPS61204305A (en
Inventor
Hiroshi Kumai
Tatsuhiko Noda
Tadashi Ichama
Takashi Sato
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.)
Nippon Kinzoku Co Ltd
Original Assignee
Nippon Kinzoku Co Ltd
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 Nippon Kinzoku Co Ltd filed Critical Nippon Kinzoku Co Ltd
Priority to JP29132985A priority Critical patent/JPS61204305A/en
Publication of JPS61204305A publication Critical patent/JPS61204305A/en
Publication of JPH0368922B2 publication Critical patent/JPH0368922B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は、流下する合金溶湯に高速液体を吹き
つけて非晶質合金粉末を製造する方法に関する。 〔従来技術〕 従来非晶質合金は、その形状により種々の方法
で製造されている。冷えば薄片の非晶質合金を製
造する場合、ガン法、ピストン・アンビル法、ト
ーシヨン・カタパルト法などが使用される。また
薄帯を連続的に製造する場合、遠心法、単ロール
法、双ロール法などが使用される。更に細線を製
造する場合、水流中紡糸法、回転液中紡糸法など
が使用されている。しかしこれらの方法で得られ
る非晶質合金は、形状が特定され、任意形状の部
品等を作製することが大変困難である。 これに対し複雑な形状の部品を製造する方法と
して、粉末をプレスなどを用いて圧粉成形する粉
末冶金法が知られている。また非晶質の合金粉末
を製造する方法として、スプレー法、キヤビテー
シヨン法、回転液中噴出法、アトマイズ法などが
知られている。 しかしこの方法は、冷却速度が十分でなく、細
かい粒子のものしか非晶質化せず、歩留りが悪い
とともに、非晶質化の程度も不均一である。しか
も得られた非晶質合金粉末の形状が球状あるいは
フレーク状であるため、圧粉成形しても粉末相互
のからみ合いが少なく、結合剤を用いなければ半
成素材、部品等を製作することができない。従つ
てこれらの方法で得られた粉末を工業的に粉末冶
金法に利用することは困難である。 本発明者は、この問題を解消すべく研究を重ね
た結果、以下の知見を得た。 溶湯を粉化して得られる粉末の形状は、溶湯流
に対する高速液体の剪断力などによつて決まる粉
化特性と、粉化後の凝固、冷却に至る過程とに大
きく影響される。とくに凝固、冷却に至るまでの
過程は、溶湯の物理的性質と溶接な関係があり、
冷却過程における粘性、表面張力などによつて粉
末の形状が影響を受ける。またこれら物理的性質
と冷却速度との相対的な諸因子が粉末の非晶質化
にも大きな影響を与える。 〔発明が解決しようとする技術的課題〕 本発明は、この知見にもとづいてなされたもの
で、溶湯粉化後の粉末が吸引されることにより粉
末周囲の蒸気膜を破壊し冷却速度を高め、このこ
とによつて圧粉成形が可能なほど不規則形状化さ
せるとともに完全に非晶質化した粉末を安定して
かつ効率よく得ることを目的とする。 〔技術的課題を解決する手段〕 すなわち、本発明は、非晶質化する合金の溶湯
を細孔から流下させる工程と、流下した溶湯に高
速液体を吹きつけて、溶湯を粉化するとともに急
冷凝固する工程と、溶湯を粉化する箇所の周囲に
吸引管を配置して20mmH2O乃至200mmH2Oの圧力
差で吸引する工程と、同吸引管の下方に粉末受け
体を配置して、凝固した非晶質粉末を、一旦この
粉末受け体に当てる工程と、同粉末受け体に当て
た後、非晶質粉末を液体を入れたタンクに落下さ
せる工程と、を具備して、粉末の全てが不規則形
状で非晶質単相からなり、かつ圧粉成形可能であ
る非晶質合金粉末を製造することを特徴とする。 以下本発明を図示する実施例を参照して説明す
る。図面は、非晶質合金の製造装置の一例を示
す。この装置は、噴霧タンク1上にルツボ2を配
置し、ルツボ2の下方に噴霧ノズル3、吸引管4
及び粉末受け体5を順に配置し、更に噴霧タンク
1に取付けたオーバーフーロー管6を排出タンク
7に接続している。 ルツボ2は、非晶質化する合金の溶湯を入れる
もので、下部に細孔を形成している。この合金と
しては、主として遷移金属元素に約15〜35原子%
の半金属元素(B、C、Si、P、Geなど)を加
えた非晶質合金型及び遷移金属−遷移金属系、遷
移金属−金属系、金属−金属系、金属−希土類系
の金属間化合物合金型などが挙げられる。 噴霧ノズル3は、水等の高速液体を噴出する例
えば環状リングノズルで、a点で高速液体の焦点
を結ぶようになつている。この高速液体の交角
は、噴霧ノズル開口径、高速液体の速さ、吸引管
4の径及び長さによつて異なるが30°〜100°が好
適である。また高速液体の速さは、噴霧圧Pに依
存し、80Kgf/cm2以上が望ましい。 更に吸引管4は、a点を囲うように設けられ、
オーバーフロー管6より上方に位置している。こ
の吸引管4は直径が小さい方が冷却速度を大きく
とれるが、あまり小さいと粉化後の粉末が吸引管
4の内壁に付着し、粉化の継続が困難になるた
め、その直径が噴霧ノズル開口部直径の0.2〜3.0
倍程度が好ましい。また長さは、あまり短いと吸
引効果が小さくなるため10cm以上とする必要があ
る。また形状は、どのような形状でもよいが、円
筒状のものが好ましい。更に粉霧タンク1の上チ
エンバ8と下チエンバ9の圧力差が20mmH2O〜
200mmH2O好ましくは40mmH2O〜200mmH2Oとな
るようにする。この理由は、圧力差が小さすぎる
と吸引効果が小さく初期の目的を達成できない
が、大きすぎると液体と粉末とが接触しにくくな
り所望の冷却速度が得られらなつて完全な非晶質
とすることが困難となるためである。 また粉末受け体5は、吸引管4の直下で、オー
バーフロー管6より上方に設ける。粉末受け体5
の構造は特に限定したものでなく、吸引管4と一
体となつたものでも分離したものでもよい。 〔発明の作用、効果〕 しかして本発明方法は、ルツボ2の細孔から溶
湯を流下し、流下する溶湯を噴霧ノズル3から噴
出する高速液体により粉化する。この時粉化した
合金粉末を、吸引管4の減圧作用で強制的に下方
に押し出す。このことにより高速液体が合金粉末
により強く作用して粉末を不規則化する。更に粉
末周囲に発生する蒸気膜を破壊して粉末の冷却速
度をも著しく上昇する。そして粉末を粉末受け体
5に当ててから噴霧タンク1又は排出タンク7で
捕捉し、その後付着流体の除去という工程を経
て、非晶質合金粉末を得る。この場合、一旦粉末
受け体5に当てるので噴霧タンク1内の水面のゆ
れを抑えて上下チヤンバ間の差圧変動を防ぎ、そ
の結果常に所望の圧力差を得ることができ粉末化
を安定しておこなうことができる。 〔実施例〕 次に本発明の実施例につき説明する。 実施例 1 Fe80原子%、P13原子%、C7原子%の組成の
合金5Kgを溶解し溶湯温度1400℃でノズルから流
下せしめた。この流下溶湯に噴霧圧力125Kg、流
量290/min、噴霧交角65°で水を噴出し、更に
吸引管で吸引し、粒子受け体に当てて非晶質合金
粉末(No.1)を得た。この場合、吸引管は、内径
50mmφ、長さ400mm、上下チエンバ間の差圧100mm
H2Oとした。 このようにして得られた非晶質合金粉末の粒度
分布を調べ、その結果第1表に示す。また比較の
ため吸引管、粉末受け体を用いず他の条件を同じ
として非晶質合金粉末(No.2)を製造し、その粒
度分布を調べた。その結果を第1表に併記する。
[Industrial Application Field] The present invention relates to a method for producing an amorphous alloy powder by spraying a high-speed liquid onto a flowing molten alloy. [Prior Art] Conventionally, amorphous alloys have been manufactured by various methods depending on their shape. When producing amorphous alloys that become flaky when cooled, the gun method, piston-anvil method, torsion-catapult method, etc. are used. In addition, when manufacturing ribbons continuously, a centrifugal method, a single roll method, a twin roll method, etc. are used. Furthermore, when producing fine wires, methods such as water spinning and rotating liquid spinning are used. However, the amorphous alloys obtained by these methods have a specific shape, and it is very difficult to manufacture parts with arbitrary shapes. On the other hand, a powder metallurgy method in which powder is compacted using a press or the like is known as a method for manufacturing parts with complex shapes. Also, known methods for producing amorphous alloy powder include a spray method, a cavitation method, an injection method in a rotating liquid, and an atomization method. However, in this method, the cooling rate is not sufficient, and only fine particles become amorphous, resulting in a poor yield and the degree of amorphization being non-uniform. Moreover, since the shape of the obtained amorphous alloy powder is spherical or flake-like, there is little entanglement between the powders even when compacted, and semi-finished materials, parts, etc. can be manufactured without using a binder. I can't. Therefore, it is difficult to industrially utilize powders obtained by these methods in powder metallurgy. The inventor of the present invention obtained the following knowledge as a result of repeated research to solve this problem. The shape of the powder obtained by pulverizing molten metal is greatly influenced by the pulverization characteristics determined by the shearing force of the high-speed liquid against the molten metal flow, and the processes leading to solidification and cooling after pulverization. In particular, the process from solidification to cooling is closely related to the physical properties of the molten metal and welding.
The shape of the powder is affected by viscosity, surface tension, etc. during the cooling process. Moreover, the relative factors between these physical properties and the cooling rate have a great influence on the amorphization of the powder. [Technical Problems to be Solved by the Invention] The present invention was made based on this knowledge, and the powder after molten metal powder is sucked to destroy the vapor film around the powder and increase the cooling rate. The purpose of this is to stably and efficiently obtain a powder that is irregularly shaped to the extent that it can be compacted and is completely amorphous. [Means for Solving Technical Problems] In other words, the present invention includes a step of causing a molten metal of an alloy that becomes amorphous to flow down through pores, and a process of blowing a high-speed liquid onto the flowing molten metal to powder the molten metal and rapidly cool it. A step of solidifying, a step of arranging a suction tube around the point where the molten metal is to be powdered and suctioning with a pressure difference of 20 mmH 2 O to 200 mmH 2 O, and a step of arranging a powder receiver below the suction tube, The process includes the steps of once applying the solidified amorphous powder to the powder receiver, and dropping the amorphous powder into a tank containing liquid after applying the solidified amorphous powder to the powder receiver. The present invention is characterized by producing an amorphous alloy powder that is entirely irregular in shape, consists of an amorphous single phase, and is compactable. The present invention will be described below with reference to illustrative embodiments. The drawing shows an example of an amorphous alloy manufacturing apparatus. In this device, a crucible 2 is arranged on a spray tank 1, and a spray nozzle 3 and a suction pipe 4 are installed below the crucible 2.
and a powder receiver 5 are arranged in this order, and an overflow pipe 6 attached to the spray tank 1 is connected to a discharge tank 7. The crucible 2 is used to hold a molten alloy to be amorphized, and has pores formed at the bottom thereof. This alloy mainly contains approximately 15 to 35 atomic percent of transition metal elements.
Amorphous alloys containing metalloid elements (B, C, Si, P, Ge, etc.) and intermetallic types such as transition metal-transition metal systems, transition metal-metal systems, metal-metal systems, and metal-rare earth systems Examples include compound alloy types. The spray nozzle 3 is, for example, an annular ring nozzle that spouts high-speed liquid such as water, and is designed to focus the high-speed liquid at point a. The intersection angle of this high-speed liquid varies depending on the aperture diameter of the spray nozzle, the speed of the high-speed liquid, and the diameter and length of the suction tube 4, but is preferably 30° to 100°. Further, the speed of the high-speed liquid depends on the spray pressure P, and is preferably 80 Kgf/cm 2 or more. Furthermore, the suction tube 4 is provided so as to surround point a,
It is located above the overflow pipe 6. The smaller the diameter of this suction tube 4, the faster the cooling rate can be achieved; however, if the diameter is too small, the powder after powdering will adhere to the inner wall of the suction tube 4, making it difficult to continue powdering. 0.2~3.0 of opening diameter
About double that is preferable. Also, the length needs to be at least 10 cm, as the suction effect will be reduced if it is too short. Further, the shape may be any shape, but a cylindrical shape is preferable. Furthermore, the pressure difference between the upper chamber 8 and lower chamber 9 of the powder mist tank 1 is 20 mmH 2 O ~
200mmH2O , preferably 40mmH2O to 200mmH2O . The reason for this is that if the pressure difference is too small, the suction effect will be small and the initial objective cannot be achieved, but if the pressure difference is too large, it will be difficult for the liquid and powder to come into contact with each other, making it impossible to obtain the desired cooling rate, resulting in complete amorphous formation. This is because it becomes difficult to do so. Further, the powder receiver 5 is provided directly below the suction pipe 4 and above the overflow pipe 6. Powder receiver 5
The structure is not particularly limited, and may be integrated with the suction tube 4 or separated. [Operations and Effects of the Invention] According to the method of the present invention, the molten metal flows down from the pores of the crucible 2, and the flowing molten metal is pulverized by the high-speed liquid jetted from the spray nozzle 3. At this time, the powdered alloy powder is forcibly pushed out downward by the vacuum action of the suction tube 4. This causes the high-speed liquid to act more strongly on the alloy powder, causing it to become disordered. Furthermore, the vapor film generated around the powder is destroyed and the cooling rate of the powder is significantly increased. Then, the powder is applied to the powder receiver 5 and then captured in the spray tank 1 or the discharge tank 7, followed by the removal of the adhering fluid to obtain an amorphous alloy powder. In this case, since the powder is once applied to the powder receiving body 5, the fluctuation of the water surface in the spray tank 1 is suppressed and the pressure difference between the upper and lower chambers is prevented.As a result, the desired pressure difference can always be obtained and powderization can be stabilized. It can be done. [Example] Next, an example of the present invention will be described. Example 1 5 kg of an alloy having a composition of 80 atomic % Fe, 13 atomic % P, and 7 atomic % C was melted and allowed to flow down from a nozzle at a molten metal temperature of 1400°C. Water was ejected onto this falling molten metal at a spray pressure of 125 kg, a flow rate of 290/min, and a spray intersection angle of 65°, which was further suctioned with a suction tube and applied to a particle receiver to obtain an amorphous alloy powder (No. 1). In this case, the suction tube has an inner diameter
50mmφ, length 400mm, differential pressure between upper and lower chambers 100mm
It was made into H2O . The particle size distribution of the amorphous alloy powder thus obtained was investigated, and the results are shown in Table 1. For comparison, an amorphous alloy powder (No. 2) was produced under the same conditions without using a suction tube or powder receiver, and its particle size distribution was investigated. The results are also listed in Table 1.

【表】 次に本発明に係る粉末(No.1)のうち+100メ
ツシユ、−100〜+300メツシユ及び−350メツシユ
のものをX線回折して非晶質化しているか否かを
調べた。その結果を第2図イ(+100メツシユ)
及び同図ロ(−350メツシユ)に示す。また従来
の粉末(No.2)についても同様にX線回折して非
晶質化しているか否かを調べた。その結果を第3
図イ(+100メツシユ)及び同図ロ(−350メツシ
ユ)に示す。第2図及び第3図から本発明のもの
は、結晶質の回折パターンが見られず、ブロード
になつており、非晶質化していることがわかる。
なお−100〜+350メツシユについては、図示して
いないが、同様のX線回折により本発明のものが
非晶質化し、従来のものが結晶質であることがわ
かつた。 次に各非晶質合金粉末の非晶質化度を示差熱分
析により調べた。その結果を第2表に示す。
[Table] Next, among the powders according to the present invention (No. 1), those with +100 mesh, -100 to +300 mesh, and -350 mesh were subjected to X-ray diffraction to determine whether they had become amorphous or not. The result is shown in Figure 2 A (+100 meters)
and shown in the same figure (-350 mesh). Furthermore, the conventional powder (No. 2) was similarly subjected to X-ray diffraction to determine whether it had become amorphous. The result is the third
Shown in Figure A (+100 mesh) and Figure B (-350 mesh). From FIG. 2 and FIG. 3, it can be seen that in the case of the present invention, no crystalline diffraction pattern is observed, and the diffraction pattern is broad, indicating that the diffraction pattern is amorphous.
Although not shown, it was found by similar X-ray diffraction that the meshes of the present invention were amorphous, while the conventional meshes were crystalline. Next, the degree of amorphization of each amorphous alloy powder was investigated by differential thermal analysis. The results are shown in Table 2.

【表】 第2表から本発明方法で完全に非晶質化できる
ことがわかる。 また各非晶質合金粉末(No.1、No.2)の形状を
顕微鏡で調べ、その模式図を第4図イ(本発明粉
末)及び同図ロ(従来粉末)に示す。第4図から
本発明合金粉末が不規則形状となつていることが
わかる。 次に本発明に係る粉末(No.1)と従来の粉末
(No.2)との見掛密度(A.D.)と流動度(F.R.)
とを調べたその結果を第3表に示す。
Table 2 shows that complete amorphization can be achieved by the method of the present invention. In addition, the shape of each amorphous alloy powder (No. 1, No. 2) was examined using a microscope, and its schematic diagrams are shown in FIG. 4A (invention powder) and FIG. 4B (conventional powder). It can be seen from FIG. 4 that the alloy powder of the present invention has an irregular shape. Next, the apparent density (AD) and fluidity (FR) of the powder according to the present invention (No. 1) and the conventional powder (No. 2)
The results of the investigation are shown in Table 3.

【表】 上表から本発明粉末は、見掛密度が従来に比べ
著しく低く、流動度が悪いため、従来のものに比
べて著しく不規則であることがわかる。 実施例 2 鉄75原子%、Si10原子%、B15原子%の合金5
Kgを溶解し、実施例1と同様の条件で非晶質合金
粉末を作製した。その非晶質化度を第4表に示
す。
[Table] From the above table, it can be seen that the powder of the present invention has a significantly lower apparent density than the conventional powder, poor flowability, and is significantly irregular compared to the conventional powder. Example 2 Alloy 5 of 75 at% iron, 10 at% Si, and 15 at% B
Kg was dissolved and an amorphous alloy powder was produced under the same conditions as in Example 1. Table 4 shows the degree of amorphization.

【表】 実施例 3 鉄75原子%、Si15原子%、B10原子%の合金5
Kgを溶解し、実施例1と同様の条件で非晶質合金
粉末を作製した。その非晶質化度を第5表に示
す。
[Table] Example 3 Alloy 5 with 75 at% iron, 15 at% Si, and 10 at% B
Kg was dissolved and an amorphous alloy powder was produced under the same conditions as in Example 1. Table 5 shows the degree of amorphization.

【表】 実施例 4 鉄80原子%、ボロン20原子%の合金4.0Kgを溶
解し、溶湯温度1400℃、噴霧圧力100Kg/cm2、水
の流量250/min、噴霧交角40度、吸引管は内
径40mmφ、長さ500mm、上下チエンバーの圧力差
70mmH2Oで粉末を作製した。その非晶質化度を
第6表に示す。
[Table] Example 4 4.0 kg of an alloy containing 80 atomic% iron and 20 atomic% boron was melted, the molten metal temperature was 1400℃, the spray pressure was 100kg/cm 2 , the flow rate of water was 250/min, the spray intersection angle was 40 degrees, and the suction pipe was Inner diameter 40mmφ, length 500mm, pressure difference between upper and lower chambers
A powder was prepared at 70 mm H 2 O. The degree of amorphization is shown in Table 6.

【表】 実施例 5 鉄40原子%、ニツケル40原子%、ボロン20原子
%の合金5.0Kgを溶解し、溶湯温度1400℃、噴霧
圧力110Kg/cm2、水の流量260/min、噴霧交角
50度、吸引管は内径50mmφ、長さ500mm、上下チ
エンバーの圧力差85mmH2Oで粉末を作製した。
その非晶質化度を第7表に示す。
[Table] Example 5 5.0 kg of an alloy of 40 at% iron, 40 at% nickel, and 20 at% boron was melted, molten metal temperature 1400℃, spray pressure 110Kg/cm 2 , water flow rate 260/min, spray intersection angle.
Powder was prepared at 50 degrees, the suction tube had an inner diameter of 50 mmφ, a length of 500 mm, and a pressure difference between the upper and lower chambers of 85 mmH 2 O.
Table 7 shows the degree of amorphization.

【表】 実施例 6 鉄68原子%、クロム10原子%、モリブデン2原
子%、リン13原子%、炭素7原子%の合金5.0Kg
を溶解し、溶湯温度1400℃、噴霧圧力120Kg/cm2、
水の流量270/min、噴霧交角68度、吸引管は
内径50mmφ、長さ450mm、上下チエンバーの圧力
差100mmH2Oで粉末を作製した。その非晶質化度
を第8表に示す。
[Table] Example 6 Alloy 5.0Kg of 68 at% iron, 10 at% chromium, 2 at% molybdenum, 13 at% phosphorus, and 7 at% carbon
melted, molten metal temperature 1400℃, spray pressure 120Kg/cm 2 ,
Powder was produced at a water flow rate of 270/min, a spray intersection angle of 68 degrees, a suction tube with an inner diameter of 50 mmφ and a length of 450 mm, and a pressure difference between the upper and lower chambers of 100 mmH 2 O. Table 8 shows the degree of amorphization.

【表】 以上説明したように本発明によれば、吸引管を
設置して冷却速度を上昇させることにより、完全
に非晶質化された合金粉末を得ることができると
ともに、合金粉末を不規則形状化させることがで
きる。このため、この合金粉末を結合剤を用いる
ことなく、圧粉成形、ロール間での成形、押出し
成形などができ、例えば複雑な形状の磁性材料、
高耐食性材料など従来の非晶質合金では作ること
ができなかつた新しい用途に使用できる顕著な効
果を奏する。又粉末受け体を設けることにより安
定した粉末を製造することができる。しかも従来
装置に吸引管、粉末受け体を設けるという簡単な
構造で効率よく製造できる。 なお本発明方法は、超急冷合金粉末の作製に利
用することもできる。
[Table] As explained above, according to the present invention, by increasing the cooling rate by installing a suction tube, it is possible to obtain a completely amorphous alloy powder, and also to make the alloy powder irregular. It can be shaped. Therefore, this alloy powder can be compacted, formed between rolls, extruded, etc. without using a binder.
It has remarkable effects and can be used in new applications that cannot be made with conventional amorphous alloys, such as highly corrosion-resistant materials. Further, by providing a powder receiver, stable powder can be produced. Moreover, it can be manufactured efficiently with a simple structure in which a suction tube and a powder receiver are provided in a conventional device. Note that the method of the present invention can also be used for producing ultra-quenched alloy powder.

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

第1図は本発明方法に係る非晶質合金粉末の製
造装置の一例を示す説明図、第2図イ及び同図ロ
は本発明合金粉末のX線回折結果を示す図、第3
図イ及び同図ロは従来合金粉末のX線回折結果を
示す図、第4図イは本発明合金粉末の模式図、同
図ロは従来合金粉末の模式図である。 1……噴霧タンク、2……ルツボ、3……噴霧
ノズル、4……吸引管、5……粉末受け体、6…
…オーバーフロー管、7……排出タンク。
FIG. 1 is an explanatory diagram showing an example of an apparatus for manufacturing amorphous alloy powder according to the method of the present invention, FIGS. 2A and 2B are diagrams showing X-ray diffraction results of the alloy powder of the present invention,
Figures 4A and 4B are diagrams showing the X-ray diffraction results of the conventional alloy powder, Figure 4A is a schematic diagram of the alloy powder of the present invention, and Figure 4B is a schematic diagram of the conventional alloy powder. 1... Spray tank, 2... Crucible, 3... Spray nozzle, 4... Suction pipe, 5... Powder receiver, 6...
...overflow pipe, 7...discharge tank.

Claims (1)

【特許請求の範囲】 1 非晶質化する合金の溶湯を細孔から流下させ
る工程と、 流下した溶湯に高速液体を吹きつけて、溶湯を
粉化するとともに急冷凝固する工程と、 溶湯を粉化する箇所の周囲に吸引管を配置して
20mmH2O乃至200mmH2Oの圧力差で吸引する工程
と、 同吸引管の下方に粉末受け体を配置して、凝固
した非晶質粉末を、一旦この粉末受け体に当てる
工程と、 同粉末受け体に当てた後、非晶質粉末を液体を
入れたタンクに落下させる工程と、を具備して、 粉末の全てが不規則形状で非晶質単相からな
り、かつ圧粉成形可能である非晶質合金粉末を製
造する方法。
[Scope of Claims] 1. A step in which a molten metal of an alloy that becomes amorphous is allowed to flow down through pores, a step in which a high-speed liquid is sprayed onto the flowing down molten metal to pulverize the molten metal and rapidly solidify it, and a step in which the molten metal is rapidly solidified into powder. Place a suction tube around the area where
A step of suctioning with a pressure difference of 20mmH 2 O to 200mmH 2 O, a step of arranging a powder receiver below the suction tube and once applying the solidified amorphous powder to this powder receiver, After applying it to a receiver, the amorphous powder is dropped into a tank containing a liquid. A method of producing an amorphous alloy powder.
JP29132985A 1985-12-24 1985-12-24 Production of amorphous alloy powder Granted JPS61204305A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29132985A JPS61204305A (en) 1985-12-24 1985-12-24 Production of amorphous alloy powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29132985A JPS61204305A (en) 1985-12-24 1985-12-24 Production of amorphous alloy powder

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP13138183A Division JPS6024302A (en) 1983-07-19 1983-07-19 Production of amorphous alloy powder

Publications (2)

Publication Number Publication Date
JPS61204305A JPS61204305A (en) 1986-09-10
JPH0368922B2 true JPH0368922B2 (en) 1991-10-30

Family

ID=17767500

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29132985A Granted JPS61204305A (en) 1985-12-24 1985-12-24 Production of amorphous alloy powder

Country Status (1)

Country Link
JP (1) JPS61204305A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4778355B2 (en) 2006-04-25 2011-09-21 セイコーエプソン株式会社 Metal powder production equipment
WO2019111951A1 (en) 2017-12-07 2019-06-13 Jfeスチール株式会社 Method for producing atomized metal powder

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2806716C3 (en) * 1978-02-14 1985-08-29 Mannesmann AG, 4000 Düsseldorf Process for making iron powder

Also Published As

Publication number Publication date
JPS61204305A (en) 1986-09-10

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