JPS5948923B2 - Manufacturing method of metal fine powder - Google Patents
Manufacturing method of metal fine powderInfo
- Publication number
- JPS5948923B2 JPS5948923B2 JP4635077A JP4635077A JPS5948923B2 JP S5948923 B2 JPS5948923 B2 JP S5948923B2 JP 4635077 A JP4635077 A JP 4635077A JP 4635077 A JP4635077 A JP 4635077A JP S5948923 B2 JPS5948923 B2 JP S5948923B2
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- powder
- metal
- particle size
- metal powder
- 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.)
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- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Description
【発明の詳細な説明】
この発明は、粉状あるいは粒状の金属粉末からさらに微
細な粒度をもった金属微粉末を製造する方法に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing fine metal powder having finer particle size from powder or granular metal powder.
従来より金属粉末の製造法としては数多くの方法が知ら
れ、これらの方法のうちでも機械的粉砕法、溶湯粉化法
、還元法、および電解法などが一般的であり、特に溶融
金属から直接粉末を製造する溶湯粉化法は、固体状態の
金属を粉化する場合よりも比較的簡易に、しかも生成能
率よく粉砕することができることから、金属粉末の製造
に広く採用されている方法であるが、被粉砕物である溶
融金属に加えられる粉化時間が短かいために、微細粉末
を製造することがきわめて困難であるという欠点がある
。Many methods have been known for producing metal powders, and among these methods, mechanical crushing, molten metal pulverization, reduction, and electrolytic methods are common. The molten metal pulverization method for manufacturing powder is a method that is widely used for manufacturing metal powder because it is relatively easier and more efficient than pulverizing solid metals. However, it has the disadvantage that it is extremely difficult to produce fine powder because the pulverization time added to the molten metal to be crushed is short.
すなわち、現在、広く採用されている代表的溶湯粉化法
としては、
(a) 溶融金属を細孔より水中に滴下して凝固せし
めて粒化する滴下法(Shotting)、(b)
溶融金属を大気中で機械的に激しく攪拌しながら冷却凝
固させ、前記金属の酸化を利用して粒化する溶湯攪拌法
(Graining)、(C)溶融金属の細流を小孔か
ら流出させ、前記細流に圧縮ガス、水流ジェット、ある
いは遠心力を作用させて前記溶融金属を細かく飛散させ
ると同時に冷却凝固させて粉化する噴霧法
(Atomization)、
などの方法を上げることができる。That is, the typical methods of pulverizing molten metal that are currently widely adopted include (a) a dropping method (Shotting) in which molten metal is dropped into water through pores, solidified, and granulated; (b)
(C) A molten metal agitation method (graining) in which the molten metal is cooled and solidified while being mechanically stirred vigorously in the atmosphere, and is granulated by utilizing oxidation of the metal; Examples of methods include atomization, in which the molten metal is dispersed finely by applying a compressed gas, a water jet, or a centrifugal force to a trickle, and at the same time is cooled and solidified to become powder.
上記(a)方法によって得られる粉末は球形あるいは滴
状をした粗粒であり、粒径1mm以下の粉末を製造する
ことは困難である。The powder obtained by the above method (a) is coarse particles having a spherical or droplet shape, and it is difficult to produce powder with a particle size of 1 mm or less.
また上記(b)方法によって得られる粉末は、その表面
が酸化物で覆われた不定形あるいは滴状をした粗粒であ
って、粒度が粗く20〜100meshの粒度範囲のも
のが大部分を占めている。In addition, the powder obtained by the above method (b) is mostly coarse particles with amorphous or droplet-like shapes whose surfaces are covered with oxides, and whose particle size is coarse and in the range of 20 to 100 mesh. ing.
さらに上記(C)方法によって得られる粉末は製造条件
によって球状、適状などの種々の形状をもつと共に、数
10μm以上の広い粒度分布をもつが、その表面が酸化
されたり、噴霧媒体による冷却効果が大きいために雰囲
気ガスの巻込みが起ったり、溶湯中に溶解しているガス
の凝固時における放出が不充分になったりすることなど
から、粒子内に気孔が形成されることがしばしば発生し
ていた。Furthermore, the powder obtained by the above method (C) has various shapes such as spherical and spherical depending on the manufacturing conditions, and has a wide particle size distribution of several tens of micrometers or more, but the surface may be oxidized or the cooling effect of the spray medium may be affected. Pores often form within the particles due to the entrainment of atmospheric gas due to the large size of the molten metal, or insufficient release of gas dissolved in the molten metal during solidification. Was.
このようなことから、同一出願人は、先に特願昭51−
156469号(以下先行発明という)として、「溶融
あるいは半溶融状態の金属に、これに対して難固溶で、
しかもより高い溶融点をもった固体粉末を共存させ、前
記溶融あるいは半溶融状態の金属中に前記固体粉末が分
散均質化した状態を保持するように攪拌を加えながら冷
却凝固し、この結果得られた微細金属粉末から前記固体
粉末を分離することを特徴とする金属粉末の製造法。For this reason, the same applicant had previously filed a patent application filed in
No. 156469 (hereinafter referred to as the prior invention) states,
Moreover, a solid powder with a higher melting point is allowed to coexist, and the solid powder is cooled and solidified while stirring to maintain a homogeneous state in which the solid powder is dispersed in the molten or semi-molten metal. A method for producing metal powder, comprising separating the solid powder from fine metal powder.
」を出願し、確かに、この先行発明によって表面酸化や
気孔のない、数lQmeshから325mesh程度ま
での広い粒度分布(もちろん325mesh以下の粒度
の微粉末も含まれる)をもち、しかも球形あるいは不定
形の種々の形状をもった金属粉末を簡便に製造すること
ができたが、形状がそろい、数10μ程度のオーダーあ
るいはこれ以下の粒度をもった金属微粉末を安定して得
ることは困難であった。'', and it is true that this prior invention has no surface oxidation or pores, a wide particle size distribution from a few liters of mesh to about 325 mesh (of course, it also includes fine powder with a particle size of less than 325 mesh), and is spherical or irregularly shaped. Although it was possible to easily produce metal powders with various shapes, it was difficult to stably obtain fine metal powders with uniform shapes and particle sizes on the order of several tens of microns or smaller. Ta.
そこで、上述の既知の方法で製造された粒状あるいは粉
状の金属粉末や、削り粉および金属屑などの粒状あるい
は粉状の金属粉末などから、ボールミルなどを使用する
機械的粉砕法によって、上記のような金属微粉末を製造
することが行なわれているが、この機械的粉砕法によっ
て製造される金属微粉末は、その形状がリン片状、平板
状、あるいは皿状を呈し、形状および粒度のそろった金
属粉末を製造することはきわめて困難であり、しかも著
しく長い粉砕時間を必要とした。Therefore, from the granular or powdered metal powder produced by the above-mentioned known method, or the granular or powdered metal powder such as shavings and metal scraps, the above-mentioned However, the fine metal powder produced by this mechanical crushing method has a scale-like, plate-like, or dish-like shape, and the shape and particle size vary. Producing coherent metal powders was extremely difficult and required significantly longer milling times.
この発明は、上述のような観点から、既知の方法で製造
された粒状あるいは粉状の金属粉末や、削り粉および金
属屑などの粒状あるいは粉状の金属粉末から、形状およ
び粒度がそろい、しかも数10μ程度のオーダーあるい
はこれ以下の粒度をもった金属微粉末を簡便に短時間で
製造する方法を提供するもので、
(A) 既知の方法で製造された純金属や合金(以下
これらを総称して金属という)の粒(ショット)や粉末
、あるいは削り粉や金属屑など(以下これらを総称して
金属粉末という)と、(B) 溶融した上記金属粉末
に対して難固溶で、しかもより高い溶融点をもち、さら
に作業上および粉化上好ましい約IOへ〜10μmの範
囲内の平均粒径をもった、例えば、
(a) Al2O3、ZrO□、TiO2、Fe2O
4、アエロジル(商品名)、カオリナイトおよびCo0
・2A1203などの酸化物、
(b) B4C,ZrC,WClおよびTiCなとの
炭化物、
(c)Si3N4、BN、およびTiNなどの窒化物、
(d) Ti (CN)などの炭窒化物、およびTi
(CNO)などの炭窒酸化物、
(e) CdS、オヨヒXcdS−ycdSeナトノ
硫化物、
(f) Fe2B、 Ni2B、 NbB、およびA
lB2などのほう化物、
(g) カーボンフ゛ラック、および゛グラファイト
などの炭素、
など上記(a)〜(g)群のうちから上記金属粉末の種
類に応じて適宜選択した適当な固体粉末の1種または2
種以上とからなる、すなわち上記(A)項に示される適
切な金属粉末と上記(B)項に示される適切な固体粉末
とからなる混合粉末を容器内に装入し、
(C) つぎに上記混合粉末に、上記金属粉末と上記
固体粉末とが分散均質化した状態を保持するように攪拌
を加えながら、前記金属粉末が溶融あるいは半溶融する
温度に加熱し、なお、前記攪拌は、前記混合粉末の加熱
開始時から行なっても、あるいは前記金属粉末の溶融点
直下の温度に加熱された時点で開始してもよく、また前
記攪拌は、機械的あるいは電磁気的に回転あるいは振動
する攪拌翼や、前記の駆動力により容器を回転あるいは
振動させる方法などの公知の手段によって与えてやれば
よく、その攪拌程度も、いろいろな要因によって影響さ
れるために一般化することはできないが、例えば単板の
回転攪拌翼で攪拌する場合には、前記具には100r、
p、 m、以上の回転数を与えてやればよく、また容
器の振動による攪拌の場合には、前記容器に100回/
分以上の振動を与えてやれば充分であり、さらに前記加
熱溶解は、望ましくは溶融状態あるいは半溶融状態に加
熱される前記金属粉末、およびより微細化された金属微
粉末の酸化を防止するために非酸化雰囲気中で行なうの
がよく、
(D) ついで前記溶融あるいは半溶融状態の金属粉
末と前記固体粉末からなる混合粉末に、前記攪拌を続行
しながら冷却を施して、前記金属粉末を半溶融状態に保
持し、もってこの半溶融状態の金属粉末を前記固体粉末
により分断してより微細化し、この場合、前記固体粉末
の平均粒径は上記の通り10人〜10μmの範囲とする
のがよく、これは、その平均粒径が10人未満では取扱
いが難しく、作業性が損なわれるばかりでなく、経済的
入手が困難となり、一方10μmを越えた平均粒径にな
ると、金属粉末に対する効率的微粉化が困難になるとい
う理由にもとづくものであり、また前記冷却は前記金属
粉末の固相温度まで行なえば充分で、その冷却速度は粉
化を完全にするために0.1〜b
するのが好ましく、一方粉化終了後は別の容器に移し変
えることによって急冷させて粉末の凝集および焼結を妨
ぐことか望ましく、
(E) この結果形状のそろった200meshから
325mesh程度までの粒度分布(もちろん325m
esh以下の粒度の微粉末も存在する)をもった微細な
金属微粉末が形成されるから、これを適当な手段によっ
て前記固体粉末と分離し、(F) さらに、必要に応
じて、粒度分布範囲がより狭く、しかもより微細にして
形状のそろった金属微粉末を得るために上記(3)〜(
D)項に示される工程を繰り返し行なってもよく、
(Q なお、さらに上記(C)〜(F)項に示される工
程を、上記の先行発明における分離処理前の粉化された
金属粉末と固体粉末とからなる混合粉末に適用すること
によって、前記金属粉末を上記(E)項および(F)項
に示される金属微粉末に形成することもでき、この場合
必要に応じてさらに適量の固体粉末を前記混合粉末に添
加してもよく、
以上(A)〜0項からなることに特徴を有する。From the above-mentioned viewpoints, the present invention has been made to produce metal powders of uniform shape and particle size from granular or powdered metal powders produced by known methods, or granular or powdered metal powders such as shavings and metal scraps. It provides a method for easily and quickly producing fine metal powder with a particle size on the order of several tens of microns or smaller. (A) Pure metals and alloys produced by known methods (hereinafter collectively referred to as these) (B) particles (shot) or powder, shavings, metal scraps, etc. (hereinafter collectively referred to as metal powder); (a) Al2O3, ZrO□, TiO2, Fe2O with a higher melting point and with an average particle size in the range of about IO to 10 μm which is further preferred for working and powdering purposes;
4. Aerosil (product name), Kaolinite and Co0
・Oxides such as 2A1203, (b) Carbides such as B4C, ZrC, WCl and TiC, (c) Nitrides such as Si3N4, BN, and TiN,
(d) Carbonitrides such as Ti (CN), and Ti
(e) CdS, Oyohi XcdS-ycdSe nanosulfides, (f) Fe2B, Ni2B, NbB, and A
One type of suitable solid powder appropriately selected from the above groups (a) to (g) according to the type of metal powder, such as borides such as lB2, (g) carbon flakes, and carbon such as graphite. or 2
(C) Next, a mixed powder consisting of a suitable metal powder as shown in item (A) above and a suitable solid powder as shown in item (B) above is charged into a container; The mixed powder is heated to a temperature at which the metal powder melts or semi-melts while stirring the metal powder and the solid powder to maintain a dispersed and homogenized state. The stirring may be carried out from the beginning of heating the mixed powder, or may be started at the time when the mixed powder is heated to a temperature just below the melting point of the metal powder, and the stirring may be performed using a mechanically or electromagnetically rotating or vibrating stirring blade The agitation may be applied by known means such as rotating or vibrating the container using the driving force described above.The degree of agitation cannot be generalized because it is affected by various factors, but for example, When stirring with a rotating plate stirring blade, the ingredients are heated with 100r,
It is sufficient to apply a rotational speed of at least 100 m, or more, and in the case of stirring by vibration of the container, the rotation speed is applied to the container 100 times per minute.
It is sufficient to apply vibrations of 1 minute or more, and furthermore, the heating melting is preferably performed to prevent oxidation of the metal powder heated to a molten or semi-molten state and the finer metal powder. (D) Next, the mixed powder consisting of the molten or semi-molten metal powder and the solid powder is cooled while continuing the stirring to semi-oxidize the metal powder. The metal powder in a semi-molten state is held in a molten state, and the semi-molten metal powder is divided into fine particles by the solid powder, and in this case, the average particle size of the solid powder is preferably in the range of 10 to 10 μm as described above. Often, if the average particle size is less than 10 people, it will be difficult to handle, impair workability, and become difficult to obtain economically, while if the average particle size exceeds 10 μm, it will be difficult to handle the metal powder efficiently. This is based on the reason that pulverization becomes difficult, and it is sufficient to perform the cooling to the solidus temperature of the metal powder, and the cooling rate is 0.1 to b to complete pulverization. is preferable, and on the other hand, it is preferable to rapidly cool the powder by transferring it to another container after completion of powdering to prevent agglomeration and sintering of the powder. (Of course 325m
A fine metal powder with a particle size of less than esh is formed, and this is separated from the solid powder by an appropriate means, and (F) further, if necessary, the particle size distribution is In order to obtain fine metal powder with a narrower range and finer shape and uniform shape, the above (3) to (
The steps shown in section D) may be repeated; By applying the metal powder to a mixed powder consisting of a solid powder, the metal powder can be formed into the metal fine powder shown in the above items (E) and (F). In this case, if necessary, an appropriate amount of solid powder can be added. A powder may be added to the mixed powder, and is characterized in that it consists of the above items (A) to 0.
つぎに、この発明を実施例により説明する。Next, the present invention will be explained by examples.
実施例 1
実施に際しては、第1図に概略縦断面図で示されるよう
な装置を使用して行なった。Example 1 The experiment was carried out using an apparatus as shown in a schematic vertical cross-sectional view in FIG.
すなわち、純度99.99%AI塊: 550gを、電
気抵抗炉1内に垂直軸を中心に回転可能に設けた黒鉛る
つぽ2内に装入し、加熱溶融して温度680℃の溶融A
16を形成した。That is, 550 g of AI ingot with a purity of 99.99% was charged into a graphite crucible 2 which was rotatably provided around a vertical axis in an electric resistance furnace 1, and heated and melted to form a molten A at a temperature of 680°C.
16 was formed.
ついで前記溶融AIが670℃に冷却された時点で、攪
拌用モーター3によって回転されるアルミナでコーティ
ングしたステンレス製攪拌翼4を回転数: 250r、
pom、で回転させると共にるつは2をモーター5に
よって回転させることによって前記溶融A1に攪拌を加
えながら、平均粒径:0.5μmをもった固体状CdS
粉末:30gを添加し、かかるCdS粉末添加の溶融A
Iを0.1℃/min程度の冷却速度で凝固点温度(6
59℃)まで冷却し、前記凝固点温度に保持して半溶融
状態を維持しながら攪拌を続けることによって完全に粉
化させた後、約650℃まで冷却した(第1段粉化処理
)。Next, when the molten AI was cooled to 670° C., the alumina-coated stainless steel stirring blade 4 rotated by the stirring motor 3 was rotated at a rotation speed of 250 r.
solid CdS having an average particle size of 0.5 μm while stirring the molten A1 by rotating the melter 2 with a motor 5.
Powder: Add 30g and melt A of such CdS powder addition
I at a cooling rate of about 0.1°C/min to the freezing point temperature (6
The mixture was cooled to 59° C.), kept at the freezing point temperature, kept stirring while maintaining a semi-molten state, and completely powdered, and then cooled to about 650° C. (first stage powdering treatment).
ついで、この発明の方法にしたがって、この結果得られ
たAI粒粉末CdS粉末とからなる温度約650℃の混
合粉末に、攪拌を続行しながら、さらに前記固体粉末と
してのCdS粉末を20g添加した後、再び約1℃/m
inの加熱速度で温度665℃に加熱し、引続いて同様
に約0.1℃/minの冷却速度で凝固点温度まで冷却
し、前記凝固点温度に保持して半溶融状態を維持しなが
ら攪拌を続けることによってさらに微細に粉化させた(
第2段粉化処理)。Next, according to the method of the present invention, 20 g of CdS powder as the solid powder was added to the resulting mixed powder of AI granules and CdS powder at a temperature of about 650° C. while continuing stirring. , again about 1℃/m
The mixture was heated to a temperature of 665° C. at a heating rate of 1.5 in, and then similarly cooled to a freezing point temperature at a cooling rate of about 0.1° C./min, and stirred while maintaining the semi-molten state at the freezing point temperature. By continuing, it was further finely powdered (
2nd stage powdering process).
その後攪拌を行ないながら温度630℃まで冷却した後
、別の容器に移しかえて急冷した。Thereafter, the mixture was cooled to a temperature of 630° C. while stirring, and then transferred to another container and rapidly cooled.
なお、上記の溶解から粉化までの作業は、不活性ガス吹
付はノズル7からのArガスの吹付けによって形成され
た非酸化雰囲気中で行なった。Note that the above operations from melting to powdering were performed in a non-oxidizing atmosphere formed by spraying Ar gas from the nozzle 7 for inert gas spraying.
この結果Al微粉末にCdS粉末が付着した混合粉末が
得られたが、この混合粉末をアセトン中で超音波洗浄し
、Al微粉末と、OS粉末とに分離した。As a result, a mixed powder in which CdS powder was attached to Al fine powder was obtained, and this mixed powder was ultrasonically cleaned in acetone and separated into Al fine powder and OS powder.
この結果得られたAl微粉末は、はぼ球形の形状を有す
ると共に表面酸化程度はきわめて小さく、その粒度分布
も第2図に示されるような結果を示し、200mesh
以下のものが大部分を占める微細なものであった。The resulting Al fine powder has a spherical shape, the degree of surface oxidation is extremely small, and its particle size distribution is as shown in Figure 2.
The following were the most minor ones.
なお、第2図には比較の目的で上記実施例1における第
2段粉化処理前、すなわち第1段粉化処理完了時点での
粒度分布を合せて示した。For comparison purposes, FIG. 2 also shows the particle size distribution before the second-stage powdering treatment in Example 1, that is, at the time of completion of the first-stage powdering treatment.
図示されるように、第1段粉化処理後のAI粒粉末、こ
の発明の方法にしたがって第2段粉化処理を施すことに
よって前記AI粒粉末さ′らに一段と微細化されること
が明らかである。As shown in the figure, it is clear that the AI granule powder after the first stage pulverization treatment is further refined by performing the second stage pulverization treatment according to the method of the present invention. It is.
実施例 2
内径20mmφの有底石英管内に、数mm程度の粒径を
有する純銅ショット (粒状純銅粉末) 100gと平
均粒径:20人のAl2O3粉末(商品名アエロジノル
)とを共に装入し、173気圧のArで封入した後、加
熱炉内に装入した。Example 2 Into a bottomed quartz tube with an inner diameter of 20 mmφ, 100 g of pure copper shot (granular pure copper powder) having a particle size of about several mm and Al2O3 powder (trade name: Aerodinol) with an average particle size of 20 people were charged together, After sealing with Ar at 173 atm, the tube was placed in a heating furnace.
なお前記石英管内面に突起を設けて攪拌が充分に行なえ
るようにした。Note that protrusions were provided on the inner surface of the quartz tube to ensure sufficient stirring.
ついで前記加熱炉内で前記石英管をほぼ水平に傾けた状
態で回転数20Or、pom、で回転しながら温度11
00℃に加熱して前記純銅粉末を半溶融状態にした後、
0.5℃/minの冷却速度で回転を続行しながら冷却
を行なった。Next, the quartz tube was tilted almost horizontally in the heating furnace and heated to a temperature of 11°C while rotating at a rotational speed of 20 or more pom.
After heating the pure copper powder to 00°C to a semi-molten state,
Cooling was performed while continuing rotation at a cooling rate of 0.5° C./min.
この結果得られた混合粉末をアセトン中で超音波洗浄し
て純銅粉末とA1゜03粉末とを分離したが、前記純銅
粉末においては、球形を示すものが多く、数10μm程
度の粒径をもったものが多く含まれていた。The resulting mixed powder was ultrasonically cleaned in acetone to separate the pure copper powder and the A1゜03 powder, but most of the pure copper powder was spherical and had a particle size of several tens of micrometers. It contained many things.
実施例 3
あらかじめ用意したCu−13,5%Sn合金の切削片
(削り粉) 100gと平均粒径:80人のカーボンブ
ラック10gとを実施例2で使用したと同じ石英管内に
装入し、同様にArで同圧封入した後、加熱炉内に垂直
状態で装入し、前記加熱炉内で前記石英管を150回/
minの割合で上下に振動させながら温度約1050℃
に加熱し、その後混合攪拌を加えながら温度800℃ま
で冷却し、ついで再び混合攪拌を続行しながら前記合金
の半溶融温度である900℃の温度に再加熱した後、温
度800℃まで冷却し、以後急冷した。Example 3 100 g of Cu-13.5% Sn alloy cutting pieces (shavings) prepared in advance and 10 g of carbon black of 80 people with an average particle size were charged into the same quartz tube as used in Example 2, Similarly, after being sealed with Ar at the same pressure, the quartz tube was charged vertically into a heating furnace, and the quartz tube was heated 150 times/year in the heating furnace.
The temperature is approximately 1050℃ while vibrating up and down at a rate of min.
, then cooled to a temperature of 800° C. while mixing and stirring, then reheated to a temperature of 900° C., which is the half-melting temperature of the alloy, while continuing mixing and stirring, and then cooled to a temperature of 800° C. It was then rapidly cooled down.
このように、この発明の方法にしたがって粉化処理を2
回繰り返し施すことによって得られた混合粉末を同様に
アセトンを使用して超音波洗浄したところ、大部分が粒
径数10μm以下を占める粒度分布をもち、はぼ球形に
近い形状を有する前記組成の合金粉末が得られた。In this way, according to the method of this invention, the powdering treatment is carried out in two steps.
When the mixed powder obtained by repeating the application several times was similarly subjected to ultrasonic cleaning using acetone, it was found that the above composition had a particle size distribution in which most of the particles had a diameter of several tens of micrometers or less, and had a shape close to a spherical shape. An alloy powder was obtained.
実施例 4
ステンレス鋼(SUS304)の切削片(削り粉)50
0gと平均粒径:8μmをもった窒化チタン粉末50g
とをアルミナルツボに装入し、このルツボを真空誘導炉
内に装入した。Example 4 Cutting pieces (shavings) of stainless steel (SUS304) 50
0g and average particle size: 8μm titanium nitride powder 50g
were charged into an aluminum crucible, and this crucible was placed into a vacuum induction furnace.
ついでアルミナ製攪拌翼を回転速度500r、 p、
m、で回転させて前記ステンレス鋼切削片を約1420
℃の温度に加熱して半溶融状態とした後、攪拌を続行し
ながら10℃/minの冷却速度で温度1380℃まで
冷却し、以後急冷した。Next, the alumina stirring blade was rotated at a rotation speed of 500 r, p,
m, to rotate the stainless steel cutting piece at about 1420 m.
The mixture was heated to a temperature of 1380° C. to a semi-molten state, and then cooled to a temperature of 1380° C. at a cooling rate of 10° C./min while continuing stirring, and then rapidly cooled.
アセトンによる超音波洗浄によって得られたステンレス
鋼粉末は、そのほとんどのものが数10μm程度の粒径
をもつ球状形状のものであった。Most of the stainless steel powder obtained by ultrasonic cleaning with acetone had a spherical shape with a particle size of about several tens of micrometers.
上述のように、この発明によれば、粉状あるいは粒状の
金属粉末から簡単な操作で、生産効率よく、しかも安い
コストで、気孔や表面酸化がなく、粒形や粒径がそろっ
たすぐれた特性を有する微細な金属微粉末を製造するこ
とができるのである。As described above, according to the present invention, powdery or granular metal powder can be easily produced, efficiently produced, at low cost, without pores or surface oxidation, and with uniform particle shape and size. This makes it possible to produce fine metal powder with specific properties.
第1図はこの発明の実施装置を示す概略縦断面図、第2
図はこの発明の方法によって得られた金属微粉末と比較
金属粉末との粒度分布を示すグラフである。
図面において、1・・・・・・電気抵抗炉、2・・・・
・・黒鉛るつぼ、3,5・・・・・・モーター、4・・
・・・・攪拌翼、6・・・・・・溶融金属、7・・・・
・・ノズル。Fig. 1 is a schematic vertical cross-sectional view showing an apparatus for implementing the present invention;
The figure is a graph showing the particle size distribution of a fine metal powder obtained by the method of the present invention and a comparative metal powder. In the drawings, 1... electric resistance furnace, 2...
...graphite crucible, 3,5...motor, 4...
... Stirring blade, 6... Molten metal, 7...
··nozzle.
Claims (1)
て難固溶で、かつより高い溶融点をもち、さらに10人
〜10μmの範囲内の平均粒径をもった固体粉末と、半
溶融状態に保持された金属粉末とからなる混合粉末に、
回転攪拌翼あるいは容器振動にて攪拌を加え、前記半溶
融状態の金属粉末を前記固体粉末にて分断してより微細
化することを特徴とする金属微粉末の製造法。1 In a non-oxidizing atmosphere, a solid powder that is difficult to dissolve in the metal powder to be refined, has a higher melting point, and has an average particle size within the range of 10 μm to 10 μm, and a semi-molten powder. A mixed powder consisting of a metal powder held in a state,
A method for producing fine metal powder, characterized in that the metal powder in a semi-molten state is divided into fine particles by the solid powder by stirring using a rotating stirring blade or vibration in a container.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4635077A JPS5948923B2 (en) | 1977-04-23 | 1977-04-23 | Manufacturing method of metal fine powder |
| US05/857,886 US4202686A (en) | 1976-12-27 | 1977-12-06 | Process for manufacturing fine powder of metal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4635077A JPS5948923B2 (en) | 1977-04-23 | 1977-04-23 | Manufacturing method of metal fine powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53131957A JPS53131957A (en) | 1978-11-17 |
| JPS5948923B2 true JPS5948923B2 (en) | 1984-11-29 |
Family
ID=12744687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4635077A Expired JPS5948923B2 (en) | 1976-12-27 | 1977-04-23 | Manufacturing method of metal fine powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5948923B2 (en) |
-
1977
- 1977-04-23 JP JP4635077A patent/JPS5948923B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53131957A (en) | 1978-11-17 |
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