JPS6396201A - Production of dustproof active metal powder - Google Patents

Production of dustproof active metal powder

Info

Publication number
JPS6396201A
JPS6396201A JP61243850A JP24385086A JPS6396201A JP S6396201 A JPS6396201 A JP S6396201A JP 61243850 A JP61243850 A JP 61243850A JP 24385086 A JP24385086 A JP 24385086A JP S6396201 A JPS6396201 A JP S6396201A
Authority
JP
Japan
Prior art keywords
active metal
powder
dust
raw material
weight
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.)
Granted
Application number
JP61243850A
Other languages
Japanese (ja)
Other versions
JPH07103401B2 (en
Inventor
Hiroshi Yamamoto
博 山本
Nobutsuka Takeno
竹野 伸束
Kunio Nomura
野村 邦雄
Shingo Ito
信吾 伊藤
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.)
Krosaki Harima Corp
Yahashi Kogyo KK
Original Assignee
Kurosaki Refractories Co Ltd
Yahashi Kogyo KK
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 Kurosaki Refractories Co Ltd, Yahashi Kogyo KK filed Critical Kurosaki Refractories Co Ltd
Priority to JP61243850A priority Critical patent/JPH07103401B2/en
Publication of JPS6396201A publication Critical patent/JPS6396201A/en
Publication of JPH07103401B2 publication Critical patent/JPH07103401B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Powder Metallurgy (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

PURPOSE:To produce active metal powder which is improved in dustproof and explosionproof characteristics by adding and mixing a specific amt. of granular polytetrafluoroethylene to and with raw material grains of an active metal in the stage of crushing and subjecting the mixture to dry pulverization to a specific grain size in an inert gaseous atmosphere. CONSTITUTION:The granular polytetrafluoroethylene is added and mixed at 0.005-0.1pt.wt. to and with 100pts.wt. raw material grain of the active metal formed to about <=15mm grain size in the stage of the crushing. The active metal includes Ca, Mg, Al, Si, Zr, Ti, Fe, etc. The mixture is then subjected to the dry pulverization continuously in the inert gaseous atmosphere so that >=50% thereof is <=100 mesh fine powder. The fine dustproof powder which is eliminated of the danger of dusting and exploding during handling is thereby obtd. without deteriorating the characteristics of the active metal powder.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は製鋼用脱酸剤、耐火物添加剤、塗料。[Detailed description of the invention] [Industrial application field] The present invention is a deoxidizing agent for steel manufacturing, a refractory additive, and a paint.

反応触媒、金属精錬1発熱剤、花火、溶接棒等広汎に利
用されているCa、 Mg+ A 1. !;+ + 
Zr、 TL Feあるいはそれらの合金のような活性
金属の粉末を、何等その特性を損なうことなく防塵性と
防爆発性を改善した状態で製造する方法に関する。
Ca, Mg+ A are widely used as reaction catalysts, metal refining exothermic agents, fireworks, welding rods, etc. 1. ! ;+ +
The present invention relates to a method for producing powders of active metals such as Zr, TL Fe or their alloys with improved dust and explosion resistance without any loss of their properties.

〔従来の技術〕[Conventional technology]

これらの活性金属の粉末の製造に際してはアトマイズ加
工とか、インペラ、スタンプ、ボールミル等の機械粉砕
によることが多いので、防塵と並行して防爆対策が極め
て重要である。
When manufacturing these active metal powders, atomization processing or mechanical pulverization using impellers, stamps, ball mills, etc. are often used, so explosion-proof measures are extremely important in addition to dust-proofing.

従来から採られているこのような酸化力の強い活性金属
粉末の処理に際しての防塵及び防爆対策は、油とかエチ
レングリコール等の液体と共に処理するとか、あるいは
これらの液体を処理粉末に充分に含浸させて行なうのが
一般的であった。
Conventional dust-proof and explosion-proof measures taken when processing active metal powders with strong oxidizing power include processing them with liquids such as oil or ethylene glycol, or sufficiently impregnating the treated powder with these liquids. It was common to do so.

しかし、使用目的によっては乾粉で使用したい場合があ
り、このための無粉塵化処理法として特公昭52−32
877号公報、特公昭55−24481号公報等に記載
されているように、活性金属粉末に粒状のポリテトラフ
ルオロエチレン(PTFE)樹脂を混合し処理する方法
がある。
However, depending on the purpose of use, there may be cases where it is desired to use dry powder, and for this purpose, a dust-free treatment method was developed using the
As described in Japanese Patent Publication No. 877 and Japanese Patent Publication No. 55-24481, there is a method in which active metal powder is mixed with granular polytetrafluoroethylene (PTFE) resin.

(発明が解決しようとする問題点〕 但し、上記PTFE樹脂粉末を使用する従来技術は、何
れも粉砕が終了した微粉末を乾式又は湿式で防塵処理す
るものであり、次の問題点が指摘される。
(Problems to be Solved by the Invention) However, in all of the conventional techniques using the above-mentioned PTFE resin powder, the fine powder that has been pulverized is subjected to a dry or wet dustproof treatment, and the following problems have been pointed out. Ru.

(1)微粉を得る過程、特に粉砕時の粉塵爆発危険度が
大である。
(1) There is a high risk of dust explosion during the process of obtaining fine powder, especially during crushing.

(2)粉砕終了後の処理のため作業が煩雑になる。(2) The work becomes complicated due to processing after the crushing is completed.

+31  P T F Hの添加量を多くする必要があ
り、活性金属粉末そのものの特性に害を与えるおそれが
ある。
It is necessary to add a large amount of +31 P T F H, which may harm the properties of the active metal powder itself.

さらに効果が出る迄の取扱い中の粉塵爆発の危険度が大
である。
Furthermore, there is a high risk of dust explosion during handling until it becomes effective.

+4]  P T F E樹脂粉末の添加量を少なくす
るには、PTFHの分散効率を上げるために結局ン兄式
処理が必要となり、後工程として、真空乾燥が必要にな
りコスト高である。
+4] In order to reduce the amount of PTFE resin powder added, a double-breasted treatment is required in order to increase the dispersion efficiency of PTFH, and vacuum drying is required as a post-process, resulting in high cost.

本発明の目的は、上記活性金属粉末を乾式処理する防塵
処理に際しての問題点の解消にあり、比較的少量のPT
FBを使用して微粉製造の全工程に亘り、粉塵爆発を有
効に防止しつつ防塵処理を施す方法を提供することにあ
る。
The purpose of the present invention is to solve the problems in the dustproofing treatment of the above-mentioned active metal powder by dry processing.
It is an object of the present invention to provide a method of effectively preventing dust explosions and performing dustproof treatment over the entire process of producing fine powder using FB.

C問題点を解決するだめの手段〕 本発明は活性金属を粒径が粗砕した段階で、PTFE樹
脂粉末を添加して、乾式で粉砕と無粉塵化処理を同時に
行うことによって前記目的を達成したものである。
[Means for Solving Problem C] The present invention achieves the above object by adding PTFE resin powder at the stage where the active metal is crushed to a coarse particle size, and performing dry crushing and dust-free treatment at the same time. This is what I did.

即ち、防塵化可能な微粉化する段階迄の粉塵爆発の危険
性を下げるために、活性金属の粗砕原料にPTFE樹脂
粉末を混合し、更に、原料を粉砕しながら防塵化させる
手法で、PTFE樹脂粉末の添加量の削減を図り、粉砕
の進行と並行して、PTFEの作用を発現させることに
成功したものである。
That is, in order to reduce the risk of dust explosion up to the stage of pulverization that can be made dustproof, PTFE resin powder is mixed with the coarsely crushed active metal raw material, and the raw material is further made dustproof while being crushed. By reducing the amount of resin powder added, we succeeded in developing the effect of PTFE in parallel with the progress of pulverization.

さらに、本発明においては、PTFE樹脂粉末と共にス
テアリン酸のような固形脂肪酸あるいはそのケン化物を
同時に添加することによって、上記粗砕段階でPTFE
樹脂粉末を添加することによる活性金属そのものの特性
を同等劣化させることなく微粉化の過程での粉塵爆発を
防止しつつ防塵処理をするという効果に加えて、粉末の
粉砕機への付着及び粒子同志の凝集も少なくして粉末の
収率を上げることかできる。
Furthermore, in the present invention, by simultaneously adding a solid fatty acid such as stearic acid or a saponified product thereof together with the PTFE resin powder, PTFE can be removed at the coarse grinding stage.
In addition to the effect of preventing dust explosions during the pulverization process without deteriorating the properties of the active metal itself by adding resin powder, it also prevents the powder from adhering to the pulverizer and preventing particles from colliding with each other. It is also possible to increase the yield of powder by reducing agglomeration.

PTFE樹脂粉末を添加する段階の粗砕活性金属原料粒
の粒径は15mm以下の場合が防爆効果上から最も効率
が良(,15m1以上の粗粒が多くなると100メノン
ユ以下の微粉末を得るには粉砕効率が悪過ぎる。好まし
い原料粒度としては選択する粉砕機にもよるが、インペ
ラ、スタンプ及びボールミル等の粉砕機では、3mm以
下のものが最も経済的である。
When the particle size of the crushed active metal raw material particles at the stage of adding PTFE resin powder is 15 mm or less, it is most efficient from the viewpoint of explosion protection (If there are many coarse particles of 15 m1 or more, it is difficult to obtain fine powder of 100 mm or less). The pulverization efficiency is too poor.The preferred raw material particle size depends on the pulverizer selected, but for pulverizers such as impellers, stamps, and ball mills, a particle size of 3 mm or less is most economical.

次に、PTFEの添加量であるが、粉砕a種、粉砕条件
で適正添加量が多少異なるが、粉砕金属原料に対し粒子
径が平均500μ程度のPTFE粉粒状物を、0、O1
〜0.1重量部程度添加する。0.01重里部以下では
、防塵効果が弱く、また0、1重量部以上になると付着
力が強くなり過ぎて排出及び分級が悪くなり、極端な場
合には不可能になる。
Next, regarding the amount of PTFE to be added, although the appropriate amount to be added differs slightly depending on the grinding type A and the grinding conditions, PTFE powder and granules with an average particle size of about 500μ are added to the pulverized metal raw material at 0, O1
Add approximately 0.1 part by weight. If the amount is less than 0.01 part by weight, the dust-proofing effect will be weak, and if it is more than 0.1 part by weight, the adhesion will be too strong, making discharge and classification difficult and, in extreme cases, impossible.

また、その改善のためにPTFEと井に添加される固形
脂肪酸乃至はそのケン化物、例えば、ステアリン酸を0
605〜0.5重量部添加した場合、PTFHの防塵効
果が同等阻害することなく、粉砕機への付着及び粒子同
志の凝集を有効に防止して処理粉末の収率を向上せしめ
ることができる。
In order to improve this, solid fatty acids or their saponified products, such as stearic acid, are added to PTFE and the well.
When 605 to 0.5 parts by weight is added, the dust-proofing effect of PTFH is not impaired to the same extent, and adhesion to the grinder and aggregation of particles among themselves can be effectively prevented and the yield of treated powder can be improved.

更に、粉砕条件であるが、前記先行技術の場合にはPT
FHのフィブリル化の有無が一つの必須条件になってい
るが、本発明法では、15買1以下の粗砕原料を連続乾
式粉砕して100メツシュ以下の微粉が50%以上得ら
れる程度の時間があれば防塵化には充分である。
Furthermore, regarding the crushing conditions, in the case of the prior art, PT
One of the essential conditions is the presence or absence of fibrillation of FH, but in the method of the present invention, the coarsely crushed raw material of 100 mesh or less is continuously dry-pulverized for a period of time such that at least 50% of the fine powder of 100 mesh or less can be obtained. It is sufficient for dust prevention.

但し、走査型電子顕微鏡による調査によっても防塵効果
が出た活性金属粉末車台体中では、)、≦加されたPT
FEは明確に識別できず、その防塵効果のメカニズムも
定かでない。
However, in the active metal powder vehicle chassis, which has been found to have a dust-proofing effect even when investigated using a scanning electron microscope,
FE cannot be clearly identified, and the mechanism of its dust-proofing effect is unclear.

PTFHによる防塵効果は、粉砕時間とPTFEの添加
量及び添加の時期とに関連があるが、この工程はあくま
で微粉を得ることが目的であって、ボールミル粉砕の場
合、粉砕のときの粉砕機の剪断力と粉砕時の温度を加味
してPTFE添加附及び時期、例えば、粉砕途中のガス
抜き時に添加する等、微粉化工程を阻害しないように、
微粉化のための各工程に合わせて調節することができる
The dust-proofing effect of PTFH is related to the grinding time and the amount and timing of addition of PTFE, but the purpose of this process is to obtain fine powder. The timing and timing of PTFE addition, taking into consideration the shearing force and temperature during pulverization, should be determined so as not to interfere with the pulverization process, for example, by adding it during degassing during pulverization.
It can be adjusted according to each process for pulverization.

分扱工f7に関してはその機構が付属された粉砕にでは
軍票であるが、未分級の被粉砕品の場合は目的粒度に応
じて分級すればよく、通常工業的には防塵処理品を20
0メソシュ程度迄篩網で分級可能である。この作業は無
粉塵化されているため環境も良く、且つ、安全に実施で
きる。
As for the sorter F7, it is a military standard for crushing that is attached to the mechanism, but in the case of unclassified products to be crushed, it is only necessary to classify them according to the target particle size, and normally industrially dust-proof treated products are
It is possible to classify with a sieve mesh down to about 0 mesh. Since this work is dust-free, it is environmentally friendly and can be carried out safely.

得られた防塵粉末はその単粒子径が60メッシュ以下で
、円味を帯びた粒状を呈し、それ等がポリテトラフルオ
ロエチレンの作用により弱(付着して形成される凝集粗
大二次粒子径が60メツシュ以下で、且つ、100メツ
シュ以下が98%以上から成るものである。
The obtained dust-proof powder has a single particle size of 60 mesh or less and a rounded granule shape, and these particles are weak due to the action of polytetrafluoroethylene (the size of aggregated coarse secondary particles formed by adhesion is The mesh is 60 or less, and 98% or more is 100 or less.

〔実施例〕〔Example〕

実施例1゜ 純度99%以上のAAとMgを溶製して得た重Y比でA
 150.3− Mg49.0の合金地金を小型ジョー
クラノンヤーで10軸以下に粗砕し、粗砕原ネ4を調整
した。次に、このAffi−ffg合金粗砕原料2kg
に、PTFE (三井デュポンフロロケミカル株式会社
製テフロンK)粒状物Logを内容積14βの磁器製ボ
ールミルに入れ、窒素ガスを装入して4時間乾式扮砕し
た。
Example 1 A with a weight Y ratio obtained by melting AA and Mg with a purity of 99% or more
An alloy ingot of 150.3-Mg49.0 was coarsely crushed into 10 or less pieces using a small jaw crane jar to prepare coarsely crushed raw material 4. Next, 2 kg of this Affi-ffg alloy coarse raw material
Next, PTFE (Teflon K manufactured by DuPont Mitsui Fluorochemical Co., Ltd.) granules Log were placed in a porcelain ball mill with an internal volume of 14β, nitrogen gas was introduced, and dry crushing was carried out for 4 hours.

この被粉砕物のボールミル内部からの排出星は1.6k
gであった。次いで、この排出物を100メツシュ篩網
で分級し、100メツシュ以下の製品収量は1.2kg
であった。製品はASTMによる比較流動試験Yに準す
る測定で無粉塵性であり、更に、得られたAJ−Mg合
金粉末は、走査型電子顕微鏡観察では粒子形状は円味を
帯びた粒状を呈していたが、フィブリル化したテフロン
には言うに及ばず、テフロンにも識別できなかった。
The discharge star from inside the ball mill of this material to be crushed is 1.6k
It was g. Next, this discharge was classified using a 100 mesh sieve, and the product yield of 100 mesh or less was 1.2 kg.
Met. The product was found to be dust-free when measured in accordance with ASTM Comparative Flow Test Y, and furthermore, the obtained AJ-Mg alloy powder had a rounded granular shape when observed with a scanning electron microscope. However, it could not be distinguished from Teflon, let alone fibrillated Teflon.

実施例2゜ PTFEと共に顆粒状ステアリン524gを加えた以外
は実施例1と同様にして処理した。
Example 2 The procedure of Example 1 was repeated except that 524 g of granular stearin was added together with PTFE.

粉砕後行た被粉砕物は1.96kgであり、また100
メツシュ篩網で分級した後の100メツシュ以下の製品
は1.9kgであった。実施例1と比較して収率の向上
が確認され、100メツシュ以下の製品中の粗粒子の存
在量は少なく、粉砕効率は優れていることが確認できた
。この製品は、実施例1の場合と同様に無粉塵性であり
、更に、得られたA7!−Mg合金粉末は、実施例1の
場合と同様に走査型電子顕微鏡観察で−は粒子形状は円
味を帯びた粒状を呈していたが、フィブリル化したテフ
ロンには言うに及ばず、テフロンK及びステアリン酸も
識別できなかった。
The material to be crushed after crushing was 1.96 kg, and 100 kg
After classification using a mesh sieve, the weight of products with a size of 100 mesh or less was 1.9 kg. It was confirmed that the yield was improved compared to Example 1, the amount of coarse particles present in the product of 100 mesh or less was small, and it was confirmed that the pulverization efficiency was excellent. This product is dust-free as in Example 1, and furthermore, the obtained A7! -The Mg alloy powder was observed under a scanning electron microscope in the same way as in Example 1, and the particle shape was rounded. and stearic acid could not be identified either.

比較例 実施例2と同様にして、テフロンKを除いた以外は同一
条件で粉砕した。
Comparative Example Grinding was carried out in the same manner as in Example 2 under the same conditions except that Teflon K was omitted.

この被粉砕物は実施例2同様ボールミルからほぼ全量に
相当する1、90kg排出したが、排出時の発塵は激し
かった。また実施例Iと同様にして分級して得た100
メツシュ以下の製品収量は1.55kgであったが、比
較流動試験では全く防塵性はなかった。
As in Example 2, 1.90 kg of the material to be crushed, which corresponds to almost the entire amount, was discharged from the ball mill, but a large amount of dust was generated during discharge. In addition, 100
The product yield below the mesh was 1.55 kg, but in the comparative flow test, there was no dust resistance at all.

〔発明の効果〕〔Effect of the invention〕

本発明法により乾式法で粗砕原料の粉砕と無粉塵化を同
一工程で処理することにより、PTFHの使用量を少な
くして活性金属粉末の特性を同等低下させることなく、
製造過程での粉塵爆発を完全に防止でき、しかも取扱い
中における粉塵爆発の危険性をなくした防塵微粉を得る
ことができる。
By using the method of the present invention to process the pulverization and dust-free processing of the coarsely crushed raw material in the same process using a dry method, the amount of PTFH used can be reduced and the properties of the active metal powder will not be deteriorated to the same extent.
It is possible to obtain dust-proof fine powder that can completely prevent dust explosions during the manufacturing process and eliminate the risk of dust explosions during handling.

Claims (1)

【特許請求の範囲】 1、粗砕段階の活性金属原料粒100重量部に粒状ポリ
テトラフルオロエチレン0.005〜0.1重量部を添
加混合して、不活性ガス雰囲気の下で100メッシュ以
下の微粉が50%以上得られる迄連続して乾式粉砕する
ことを特徴とする防塵性活性金属粉末の製造方法。 2、粗砕段階の活性金属原料粒100重量部に粒状ポリ
テトラフルオロエチレン0.005〜0.1重量部と固
形脂肪酸またはそのケン化物0.05〜0.5重量部と
を添加混合して、不活性ガス雰囲気の下で100メッシ
ュ以下の微粉が50%以上得られる迄連続して乾式粉砕
することを特徴とする防塵性活性金属粉末の製造方法。
[Claims] 1. Add and mix 0.005 to 0.1 part by weight of granular polytetrafluoroethylene to 100 parts by weight of active metal raw material grains at the coarse crushing stage, and mix the mixture to 100 mesh or less under an inert gas atmosphere. 1. A method for producing dust-proof active metal powder, which comprises continuously dry-pulverizing until 50% or more of fine powder is obtained. 2. Add and mix 0.005 to 0.1 parts by weight of granular polytetrafluoroethylene and 0.05 to 0.5 parts by weight of solid fatty acids or saponified products thereof to 100 parts by weight of active metal raw material particles at the coarse crushing stage. . A method for producing a dust-proof active metal powder, which comprises continuously dry-pulverizing the powder under an inert gas atmosphere until 50% or more of fine powder of 100 mesh or less is obtained.
JP61243850A 1986-10-13 1986-10-13 Method for producing dustproof active metal powder Expired - Lifetime JPH07103401B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61243850A JPH07103401B2 (en) 1986-10-13 1986-10-13 Method for producing dustproof active metal powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61243850A JPH07103401B2 (en) 1986-10-13 1986-10-13 Method for producing dustproof active metal powder

Publications (2)

Publication Number Publication Date
JPS6396201A true JPS6396201A (en) 1988-04-27
JPH07103401B2 JPH07103401B2 (en) 1995-11-08

Family

ID=17109881

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH07103401B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5338712A (en) * 1993-02-04 1994-08-16 Timmino Ltd. Production of non-explosive fine metallic powders
US5466310A (en) * 1991-02-19 1995-11-14 The Australian National University Production of metal and metalloid nitrides
WO1999028026A1 (en) * 1997-12-03 1999-06-10 Murakashi Lime Industry Co., Ltd. Dust prevention process for dust-generating powders
JP2006261526A (en) * 2005-03-18 2006-09-28 Tdk Corp Method of manufacturing rare-earth sintered magnet

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5466310A (en) * 1991-02-19 1995-11-14 The Australian National University Production of metal and metalloid nitrides
US5338712A (en) * 1993-02-04 1994-08-16 Timmino Ltd. Production of non-explosive fine metallic powders
WO1994017942A1 (en) * 1993-02-04 1994-08-18 Timminco Limited Production of non-explosive fine metallic powders
US5461012A (en) * 1993-02-04 1995-10-24 Timminco Ltd. Non-explosive fine metallic powder mixtures for making refractories
WO1999028026A1 (en) * 1997-12-03 1999-06-10 Murakashi Lime Industry Co., Ltd. Dust prevention process for dust-generating powders
JP2006261526A (en) * 2005-03-18 2006-09-28 Tdk Corp Method of manufacturing rare-earth sintered magnet

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