JPS62290806A - Production of metallic flake - Google Patents
Production of metallic flakeInfo
- Publication number
- JPS62290806A JPS62290806A JP13193686A JP13193686A JPS62290806A JP S62290806 A JPS62290806 A JP S62290806A JP 13193686 A JP13193686 A JP 13193686A JP 13193686 A JP13193686 A JP 13193686A JP S62290806 A JPS62290806 A JP S62290806A
- Authority
- JP
- Japan
- Prior art keywords
- metal
- molten metal
- cylinder
- rotating cylinder
- pulverized
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 14
- 229910052751 metal Inorganic materials 0.000 claims abstract description 68
- 239000002184 metal Substances 0.000 claims abstract description 67
- 239000002826 coolant Substances 0.000 claims abstract description 6
- 150000002739 metals Chemical class 0.000 abstract description 3
- 238000010298 pulverizing process Methods 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 15
- 239000007789 gas Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000000956 alloy Substances 0.000 description 3
- 238000005096 rolling process Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000010301 surface-oxidation reaction Methods 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 1
- 101100165918 Caenorhabditis elegans cam-1 gene Proteins 0.000 description 1
- RGJOEKWQDUBAIZ-IBOSZNHHSA-N CoASH Chemical compound O[C@@H]1[C@H](OP(O)(O)=O)[C@@H](COP(O)(=O)OP(O)(=O)OCC(C)(C)[C@@H](O)C(=O)NCCC(=O)NCCS)O[C@H]1N1C2=NC=NC(N)=C2N=C1 RGJOEKWQDUBAIZ-IBOSZNHHSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/06—Making metallic powder or suspensions thereof using physical processes starting from liquid material
- B22F9/08—Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
- B22F2009/0804—Dispersion in or on liquid, other than with sieves
- B22F2009/0812—Pulverisation with a moving liquid coolant stream, by centrifugally rotating stream
Landscapes
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
& 発明の詳細な説明
〔産業上の利用分野〕
本発明は金属溶湯から大葉に金属フレークを製造するの
に適した金属フレークの製造方法〒ある。[Detailed Description of the Invention] & Detailed Description of the Invention [Industrial Application Field] The present invention provides a method for producing metal flakes suitable for producing large-sized metal flakes from molten metal.
従来、フレーク状の金属元素や合金(本発明〒はこれら
を単に金属と称する)を製造するには、例えば、金属イ
ンゴットを切削して得たIJ 、)iン状切削片、金属
を圧延して得た薄片、金属の溶湯を細流として回転円盤
上に落下して得た薄片等をスタンプミル、ゼールミル等
1厚さ数ミクロン、極数mmの薄片となし、これらをさ
らに細分化することによって細い金属フレークとしてい
る。Conventionally, in order to produce flaky metal elements or alloys (in the present invention, these are simply referred to as metals), for example, IJ obtained by cutting a metal ingot,) in-shaped cut pieces, or by rolling the metal. Thin flakes obtained by making molten metal fall onto a rotating disk as a trickle are made into thin flakes with a thickness of several microns or a few mm using stamp mills, Zeel mills, etc., and these are further divided into thin pieces. It is made of thin metal flakes.
これらの製造方法は工程数が多く複雑マあったの〒、本
発明者は先に、金属の溶湯を細管を通して落下し、落下
中の溶湯流に側面力)ら圧縮ガスρ)らノズルを噴射し
、細粉化され1こ浴湯を回転円盤に衝突させることによ
って1つの工程〒簡単に金属フレークを得ることに底功
した(特公昭53−16391号公報)。These manufacturing methods involved many steps and were complicated, but the inventor first developed a method in which molten metal was dropped through a thin tube, and compressed gas ρ) was injected into the falling molten metal flow through a nozzle. However, they succeeded in easily obtaining metal flakes in a single step by colliding the pulverized bath water against a rotating disk (Japanese Patent Publication No. 16391/1983).
この方法は種々の扁品質の金属フレークを得ろことがマ
き、又この方法を実施した装置は騒音、振動が極めて少
ない等の種々の利点を有しているが、金属フレークを大
量に得ようとした場合に、その構造上装置の大型化が困
難であったり、又、例えば回転円盤な犬ぎくしてその半
径方向′IC細管を配列した構造にした場合には、細管
の位置により回転円盤の周速度が相異する等の製造条件
が異なる1こめに、金属粉の均一性が低下する等の問題
もあった。従って、同じ装置を多数必要とし、生産効率
ならびに設備費などの点において問題を抱えていた。This method makes it possible to obtain metal flakes of various flatness qualities, and the equipment that implements this method has various advantages such as extremely low noise and vibration, but it is possible to obtain metal flakes in large quantities. In this case, it is difficult to increase the size of the device due to its structure, or, for example, if the structure is such that the IC thin tubes are arranged in the radial direction of a rotating disk, the rotating disk In addition to the different manufacturing conditions such as different circumferential speeds, there were also problems such as a decrease in the uniformity of the metal powder. Therefore, a large number of the same devices are required, which poses problems in terms of production efficiency and equipment costs.
本発明は、上記問題点を解消するためになされたもので
あり、大量の金属フレークを短時間で製造することので
きろ極めて生産効率の良い金属フレークの製造方法を提
供することを目的とするもの1ある。The present invention has been made in order to solve the above-mentioned problems, and an object of the present invention is to provide a method for manufacturing metal flakes with extremely high production efficiency by which a large amount of metal flakes can be manufactured in a short time. There is one thing.
本発明のかかる目的は、内面を強制冷却されている回転
円筒の両方に設けられた複数の導管を通して金属の溶湯
を落下させ、落下中の各溶湯流に対して両面からノズル
より圧縮ガスを噴出し、溶湯流を細粉化しつつ回転円筒
の外壁に衝突させることを特徴とする金属フレークの製
造方法により達成することができる。The object of the present invention is to drop molten metal through a plurality of conduits provided on both sides of a rotating cylinder whose inner surface is forcibly cooled, and jet compressed gas from nozzles from both sides to each falling molten metal flow. However, this can be achieved by a method for manufacturing metal flakes, which is characterized in that the molten metal flow is made to collide with the outer wall of a rotating cylinder while being pulverized.
以下、本発明の方法を実施した装置について、ぶ付図百
f基づいて詳細に説明する。Hereinafter, an apparatus implementing the method of the present invention will be described in detail with reference to Figure 10F.
第1図廻示すように金8浴湯1を耐火容器2に入れ保温
しつつ適当なストレーナを用い、はぼ0.5〜5 m1
yIの導管を通して溶湯の細流を作る。As shown in Figure 1, put Kin 8 bath water 1 into a fireproof container 2 and use an appropriate strainer to keep it warm, and strain it to about 0.5 to 5 m1.
Create a trickle of molten metal through the yI conduit.
なお、本実施例においては、浴湯金属(金属およびその
合金)をP#に限定するものではないが、1400°C
以下の低融点のものが好適マある。In addition, in this example, the bath water metal (metal and its alloy) is not limited to P#, but at 1400°C
The following low melting points are preferred.
一方、導管6の下端付近において水平に設置したノズル
4を介して加圧ガスを噴射することにより、導管3から
流出した溶湯流を細粉化する。ここに使用する圧縮ガス
は例えば空気あるいは窒素、二酸fヒ炭素、アルゴン等
の非酸化性のガスを金属溶湯に、J:り適宜選択して使
用する。細粉化された金属溶湯は加圧ガス噴射方向前方
に設置された回転円筒5に衝突する。この回転円筒5は
図示されていないIIA動装置により回転軸6に設けら
れた例えばギア10等を介して回転され、且つこの回転
円筒5の内部には冷却媒が流れるようになされている。On the other hand, by injecting pressurized gas through a nozzle 4 installed horizontally near the lower end of the conduit 6, the molten metal flow flowing out from the conduit 3 is pulverized. The compressed gas used here is, for example, air or a non-oxidizing gas such as nitrogen, carbon dioxide, arsenic, or argon, which is appropriately selected and used for the molten metal. The pulverized molten metal collides with a rotating cylinder 5 installed forward in the direction of pressurized gas injection. This rotating cylinder 5 is rotated by an IIA moving device (not shown) via, for example, a gear 10 provided on a rotating shaft 6, and a cooling medium flows inside the rotating cylinder 5.
この冷却媒を流す構造は、例えば回転円筒5を2重壁と
すると共に、中空に構成された回転軸6の一方から例え
ば水などの冷却媒を回転円筒5内に送り込み、一方の回
転@6から排出するような構造とすることが〒赦る。又
、回転円筒5の少なくとも表面は、溶湯噴霧金属と合金
化し難く、耐熱性を有しかつ衝突して扁平状となった金
属粉が容易に剥離する性質を有することが要求されるの
で、例えばセラミックスあるいはテフロン、シリコーン
、エポキシ等の熱硬化性樹脂〒焼付けした金属プレート
を用いることが好ましい。The structure for flowing this coolant is, for example, by making the rotating cylinder 5 double-walled, and by feeding a coolant such as water into the rotating cylinder 5 from one side of the hollow rotating shaft 6, so that one rotation @ 6 It is acceptable to have a structure that discharges water from the air. In addition, at least the surface of the rotating cylinder 5 is required to have properties that are difficult to alloy with the molten sprayed metal, have heat resistance, and allow metal powder that collides and becomes flat to be easily peeled off. It is preferable to use a metal plate baked with ceramics or a thermosetting resin such as Teflon, silicone, or epoxy.
上記のように強制冷却されている回転円筒5に’Jr突
した。M分化あるいは唄姑状の溶湯は、円筒表面上″I
″扁平化しつつ急冷固イヒされる。そして急冷固イヒし
た鱗片状の金属粉は円筒表面にa府することなく極めて
剥離し易い状態にあるの〒、回転円筒5の外周近傍に設
けた例えばドクタ7、ワイヤーブラシ8あるいはエアー
ブラシ(図示しない)等により極めて容易に掻き落とし
捕集することが〒きる。なお、円筒表面に付層した金属
粉ぼ、再び噴霧金属が衝突するまフには完全に落される
ように例えばワイヤーブラシ8等を二重、三重に設ける
ように考慮されている。又、上記各部材を収納したケー
シングには、ノズル4から噴出した圧縮ガスの圧力影響
を軽減するために、例えば強制吸引する吸引口9が設け
られている。The 'Jr' collided with the rotating cylinder 5 which was being forcibly cooled as described above. The M-differentiated or slender molten metal is ``I'' on the cylindrical surface.
The scaly metal powder that has been rapidly cooled and solidified is in a state where it is extremely easy to peel off without being stuck on the cylinder surface. 7. It can be scraped off and collected very easily with a wire brush 8 or an air brush (not shown). Note that the metal powder layered on the cylinder surface is completely removed from the muff where the sprayed metal collides with it again. For example, wire brushes 8, etc., are installed in double or triple layers so that the brushes 8 can be dropped into the air.In addition, the casing housing the above-mentioned components is designed to reduce the pressure effect of the compressed gas ejected from the nozzle 4. For this purpose, for example, a suction port 9 for forced suction is provided.
上記の導管3は回転円筒50回転軸線に沿って適宜間隔
マ複数配列され、ノズル4も導管3に対応して配設され
ている。従って、溶湯金属を流出する導管3を多くした
構成とすることマ、容易に金属粉の製造量を多くするこ
とが〒き、さらにまた大−!に製産にもかかわらず例え
ば金属粉の大きさが均一1品質の扁い金属粉を得ること
が〒きる。A plurality of the above-mentioned conduits 3 are arranged along the axis of rotation of the rotating cylinder 50 at appropriate intervals, and the nozzles 4 are also arranged corresponding to the conduits 3. Therefore, by increasing the number of conduits 3 through which the molten metal flows out, it is possible to easily increase the amount of metal powder produced, and it is also possible to increase the amount of metal powder produced. For example, it is possible to obtain flat metal powder with a uniform size and quality even though the metal powder is manufactured in different time periods.
すなわち、本実施例は回転円筒5の如き1つの回転体を
用した構成〒あるの〒、複数の導管3から排出された溶
湯は例えば該回転円筒50回転速度や冷却度合、ノズル
から円筒表面までの距離などが同一の条件下で処理され
るから〒ある。That is, this embodiment has a configuration using one rotating body such as the rotating cylinder 5, and the molten metal discharged from the plurality of conduits 3 is controlled by the rotational speed of the rotating cylinder 50, the degree of cooling, and the distance from the nozzle to the cylinder surface. There is 〒 because the distance etc. are processed under the same conditions.
上記実施例における導管3は0.5〜5 mm yi程
度の細管を用いたが、本発明の導管はこの範囲の比較的
細いものに限られるものfはなく、より太いものを用い
ることもできる。すなわち、例えば圧縮ガスのガス圧等
の諸条件によっては、太い導管を使用することも可能で
ある。Although a thin tube of about 0.5 to 5 mm yi was used as the conduit 3 in the above embodiment, the conduit of the present invention is not limited to a relatively thin tube within this range, and a thicker tube can also be used. . That is, depending on various conditions such as the gas pressure of the compressed gas, it is also possible to use a thick conduit.
又、上記実施例においては、導管6の数だけノズル4を
設置したが、本発明はこれに限られるもの〒はなく、例
えば、複数の導管6が配置された範囲(幅)を扁平な開
口を有した1つのノズルで賄うような構底!あってもよ
く、又1つの導管6に対して複数のノズルを適宜配置し
たような構底マあっても勿論よい。Further, in the above embodiment, the number of nozzles 4 is equal to the number of conduits 6, but the present invention is not limited to this. A structure that can be covered by one nozzle with Of course, it is also possible to have a bottom structure in which a plurality of nozzles are appropriately arranged for one conduit 6.
本発明の方法によって得られろ鱗片状金属粉の形状およ
び大きさは、溶湯流の温度および細さ、ノズルの形状お
よび高圧ガスの噴射速度、ノズルより回転円筒の表面ま
マの距離、回転円筒の回転速度および冷却度合および材
質により調整することがマき、金属粉末の酸化は噴霧ガ
スの選択および回転円盤の冷却度合により防止すること
が〒き、又、必要に応じて噴霧媒を用いることもフきる
。The shape and size of the scaly metal powder obtained by the method of the present invention are determined by the temperature and thinness of the molten metal flow, the shape of the nozzle and the injection speed of the high-pressure gas, the distance from the nozzle to the surface of the rotating cylinder, and the distance between the nozzle and the surface of the rotating cylinder. The oxidation of the metal powder can be prevented by selecting the atomizing gas and the degree of cooling of the rotating disk, and if necessary, using an atomizing medium. It can also be completed.
以上述べたように本廃明の方法によれば、適当な条件の
設定により金属溶湯から直接容易VC@片状金属粉を得
ることがマき、金属粉の厚さ、大きさの調節が容易マあ
るばかりか機械的操作、粉砕助剤を用いず溶湯から噴霧
固化までの時間が短いので噴霧媒の選択によって表面酸
化が少く、かつ不純物の少い高品質の金属粉を短時間に
効率よく多量に得ろことが!きる。しかも本発明は塗料
用、顔料用の銅粉、黄銅粉あるいはアルミ粉の製造にお
けるような切削、圧延、展延粉砕の工程を省くことが1
1%きるのマ、展延粉砕時に於ける騒音、振動等の公害
面の問題点を解消できる。As mentioned above, according to the proposed method, it is possible to easily obtain VC @ flaky metal powder directly from molten metal by setting appropriate conditions, and the thickness and size of the metal powder can be easily adjusted. Not only is it easy to use, but the time from molten metal to spray solidification is short without the use of mechanical operations or grinding aids, so by selecting a spray medium, you can efficiently produce high-quality metal powder with little surface oxidation and few impurities in a short time. You can get a lot of things! Wear. Moreover, the present invention eliminates the steps of cutting, rolling, and rolling and crushing that are used in the production of copper powder, brass powder, or aluminum powder for paints and pigments.
It is possible to eliminate pollution problems such as noise and vibration during spreading and crushing with 1% grinding.
このように本発明の方法は表面積の大きな、表面ば化の
少ない活性度の高い金属粉を一工程で多tに製造マきる
から、金稿触媒および有機金属の製造分野においても極
めて有用な製法マある。As described above, the method of the present invention can produce a large amount of highly active metal powder with a large surface area and low surface oxidation in one step, making it an extremely useful manufacturing method in the field of manufacturing gold catalysts and organic metals. There is a ma.
第1図は本発明の方法を用いた装置の1冥施例の拡大概
略図、第2図は第1図に示す装置全体の概略側面図、第
6図は第1図に示す装置全体の概略平面図である。
1・・・金属溶湯、 2・・・耐火容器、 3・・・
導管、4・・・ノズル、 5・・・回転円筒、 6・・
・回転軸、7・・・ドクタ、 8・・・ワイヤーブラ
シ、9・・・吸引口、 10・・・ギア。
(ほか2名> ”” ニ
第 1 図FIG. 1 is an enlarged schematic diagram of one embodiment of the apparatus using the method of the present invention, FIG. 2 is a schematic side view of the entire apparatus shown in FIG. 1, and FIG. 6 is a schematic side view of the entire apparatus shown in FIG. 1. FIG. 1... Molten metal, 2... Fireproof container, 3...
Conduit, 4... Nozzle, 5... Rotating cylinder, 6...
・Rotating shaft, 7...Doctor, 8...Wire brush, 9...Suction port, 10...Gear. (2 other people> ”” d. Figure 1)
Claims (1)
れた複数の導管を通して金属の溶湯を落下させ、落下中
の各溶湯流に対して側面からノズルより圧縮ガスを噴出
し、溶湯流を細粉化しつつ回転円筒の外壁に衝突させる
ことを特徴とする金属フレークの製造方法。 2)回転円筒の内面が、該円筒の内壁に沿つて設けられ
た冷却媒通路に冷却媒を流すことによつて冷却される特
許請求の範囲第1項に記載の金属フレークの製造方法。[Claims] 1) Molten metal is dropped through a plurality of conduits installed on the side of a rotating cylinder whose inner surface is forcibly cooled, and compressed gas is applied to each falling molten metal flow from the side from a nozzle. A method for producing metal flakes, characterized in that the molten metal flow is pulverized and collided with the outer wall of a rotating cylinder. 2) The method for producing metal flakes according to claim 1, wherein the inner surface of the rotating cylinder is cooled by flowing a coolant through a coolant passage provided along the inner wall of the cylinder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13193686A JPS62290806A (en) | 1986-06-09 | 1986-06-09 | Production of metallic flake |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13193686A JPS62290806A (en) | 1986-06-09 | 1986-06-09 | Production of metallic flake |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62290806A true JPS62290806A (en) | 1987-12-17 |
Family
ID=15069676
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13193686A Pending JPS62290806A (en) | 1986-06-09 | 1986-06-09 | Production of metallic flake |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62290806A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6746509B2 (en) | 2002-09-11 | 2004-06-08 | Mitsui Mining & Smelting Company, Ltd. | Process for producing zinc or zinc alloy powder for battery |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5316391A (en) * | 1976-07-30 | 1978-02-15 | Fujitsu Ltd | Method and apparatus for growing single crystalline alumina at gaseous phase |
JPS5835563A (en) * | 1981-08-26 | 1983-03-02 | Canon Inc | Copying device |
-
1986
- 1986-06-09 JP JP13193686A patent/JPS62290806A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5316391A (en) * | 1976-07-30 | 1978-02-15 | Fujitsu Ltd | Method and apparatus for growing single crystalline alumina at gaseous phase |
JPS5835563A (en) * | 1981-08-26 | 1983-03-02 | Canon Inc | Copying device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6746509B2 (en) | 2002-09-11 | 2004-06-08 | Mitsui Mining & Smelting Company, Ltd. | Process for producing zinc or zinc alloy powder for battery |
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