JPS6396202A - Production of dustproof active metal powder - Google Patents
Production of dustproof active metal powderInfo
- Publication number
- JPS6396202A JPS6396202A JP61243851A JP24385186A JPS6396202A JP S6396202 A JPS6396202 A JP S6396202A JP 61243851 A JP61243851 A JP 61243851A JP 24385186 A JP24385186 A JP 24385186A JP S6396202 A JPS6396202 A JP S6396202A
- Authority
- JP
- Japan
- Prior art keywords
- active metal
- powder
- weight
- dust
- raw material
- 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
Links
- 239000000843 powder Substances 0.000 title claims abstract description 37
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 25
- 239000002184 metal Substances 0.000 title claims abstract description 25
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 21
- 239000002994 raw material Substances 0.000 claims abstract description 16
- 238000010298 pulverizing process Methods 0.000 claims abstract description 13
- 239000000203 mixture Substances 0.000 claims abstract 3
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 11
- 239000002202 Polyethylene glycol Substances 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 11
- 229920001223 polyethylene glycol Polymers 0.000 claims description 11
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 4
- 229930195729 fatty acid Natural products 0.000 claims description 4
- 239000000194 fatty acid Substances 0.000 claims description 4
- 150000004665 fatty acids Chemical class 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 3
- 239000011261 inert gas Substances 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 abstract description 7
- 230000002542 deteriorative effect Effects 0.000 abstract description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 abstract 2
- 238000010410 dusting Methods 0.000 abstract 1
- 239000000428 dust Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 238000004880 explosion Methods 0.000 description 6
- 229910045601 alloy Inorganic materials 0.000 description 5
- 239000000956 alloy Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 5
- 239000004810 polytetrafluoroethylene Substances 0.000 description 5
- 235000021355 Stearic acid Nutrition 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 4
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 4
- 239000008117 stearic acid Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 229910000861 Mg alloy Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052573 porcelain Inorganic materials 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011163 secondary particle Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Powder Metallurgy (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Abstract
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、?8接棒等広汎に
利用されているCa、Mg、A7. Si、Zr、Ti
、 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t員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。Reaction catalyst, metal refining 1 exothermic agent, fireworks,? 8 contact rod etc. are widely used such as Ca, Mg, A7. Si, Zr, Ti
The present invention relates to a method for producing active metal powders such as Fe or their alloys with improved dust and explosion resistance without compromising any of their properties.
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F!I!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 together with liquids such as oil and ethylene glycol, or treating these liquids with F! I! It was common practice to thoroughly impregnate the powder.
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持公開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 it as a dry powder.
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.
上記PTFEは全屈粉末の乾粉状防塵剤としては優れた
ものであるが、それ自体高価であると共に、その添加も
む)砕が終了したとき添加されるものであるので、微粉
を得る過程での粉塵爆発危険が大きい。The above-mentioned PTFE is excellent as a dry powder dustproofing agent, but it is expensive in itself, and it is added when the crushing is completed, so it is difficult to obtain the fine powder in the process of obtaining the fine powder. There is a high risk of dust explosion.
本発明の目的は、上記従来の防塵剤であるPTFEより
安価でありる防塵剤を見出し、その防塵剤を使用して活
性金属の特性に何ら想影響を与えることなく、しかも微
粉化工程での粉塵り3発の危険を回避できる防塵活性金
属粉末の製造方法を提供することにある。The purpose of the present invention is to find a dustproofing agent that is cheaper than PTFE, the conventional dustproofing agent, and to use this dustproofing agent to improve the properties of active metals without affecting the properties of active metals in the pulverization process. To provide a method for producing dust-proof active metal powder that can avoid the danger of three dust particles.
本発明は種々試行錯誤した結果、粉粒状ポリエチレング
リコール及びポリエチレンオキサイドがPTFEよりも
安価でありながら、その添加条件を特定することによっ
て上記目的が達成できることを見出した。As a result of various trials and errors, the present invention has found that while powdered polyethylene glycol and polyethylene oxide are cheaper than PTFE, the above object can be achieved by specifying the conditions for their addition.
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、活性金属の粗砕段階で、この粗砕活
性粉末に粉粒状ポリエチレングリコールまたはポリエチ
レンオキサイドを添加混合し、更に、不活性ガス雰囲気
中で原料を粉砕しながら防塵化させるもので、高価な、
PTFHに代わる安価な防塵剤の使用を可能にし、少
ない添加量によって活性金属の特性に同等悪影響を与え
ることなく、防爆粉砕の進行と並行して、防塵作用を発
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 dust-proofed, granular polyethylene glycol or polyethylene oxide is added and mixed to the coarsely crushed active powder at the stage of coarsely crushing the active metal, and further, This is a method that makes the raw material dustproof while pulverizing it in an inert gas atmosphere.
This enables the use of an inexpensive dust-proofing agent in place of PTFH, and has succeeded in developing dust-proofing effects in parallel with the progress of explosion-proof crushing without having the same negative effect on the properties of active metals by adding a small amount. .
勿論、防塵剤としての粉粒状ポリエチレングリコールま
たはポリエチレンオキサイドは、それら同志の併用や他
の防塵剤との併用も可能である。Of course, granular polyethylene glycol or polyethylene oxide as dustproofing agents can be used in combination with each other or with other dustproofing agents.
さらに、本発明においては、ポリエチレングリコールあ
るいはポリエチレンオキサイド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、上記粗砕段階でポリエチレングリコール
あるいはポリエチレンオキサイドの添加の効果に加えて
、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ができる。Furthermore, in the present invention, by simultaneously adding solid fatty acids such as stearic acid or saponified products thereof together with polyethylene glycol or polyethylene oxide, in addition to the effect of adding polyethylene glycol or polyethylene oxide at the above-mentioned crushing stage, powder It is possible to increase the yield of powder by reducing adhesion to the grinder and agglomeration of particles among themselves.
ポリエチレングリコールあるいはポリエチレンオキサイ
ド等の防塵剤粉末を添加する段階の活性金属の粗砕段階
にある粒子の径は15+u以下の場合が防爆効果上から
最も効率が良<、15mm以上の粗粒が多くなると10
0メツシュ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↑5)砕機で
は、3mm以下のものが最も経済的である。In terms of explosion protection, it is most efficient if the diameter of the particles in the coarse crushing stage of the active metal at the stage of adding dustproof agent powder such as polyethylene glycol or polyethylene oxide is 15+U or less. 10
The pulverization efficiency is too low to obtain a fine powder with a mesh size of 0 or less. The preferred particle size of the raw material depends on the crusher selected, but for crushers such as impellers, stamps, and ball mills, a particle size of 3 mm or less is most economical.
次に、防塵剤である粉粒状のポリエチレングリコール及
び、または、ポリエチレンオキサイドの添加量であるが
、粗砕活性金属原料100重量部に対し粉粒状物を0.
01〜0.5重量部用いれば良く、粉砕機種、粉砕条件
で適正添加量が多少異なる。Next, regarding the amount of powdery polyethylene glycol and/or polyethylene oxide that is a dustproofing agent, 0.00% of the powdery and granular material is added to 100 parts by weight of the coarsely crushed active metal raw material.
It is sufficient to use 01 to 0.5 parts by weight, and the appropriate amount to be added varies somewhat depending on the type of grinding machine and grinding conditions.
通常、0.01重量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凝集力が強過ぎて排出及び
分級が悪くなるか不可能になる。Normally, if it is less than 0.01 part by weight, the dustproof effect is weak, and if it is less than 0.01 part by weight,
If the amount exceeds 1 part by weight, the adhesion and cohesive force will be so strong that discharge and classification will become difficult or impossible.
また、その改善のため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0.05〜0.5重量部添加
した場合、前記防塵剤の防塵効果を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 addition, if 0.05 to 0.5 parts by weight of a solid fatty acid such as stearic acid or its saponified product is added in order to improve the problem, the dust-proofing effect of the dust-proofing agent will not be affected and the adhesion to the crusher will be reduced. Furthermore, it is possible to effectively prevent particles from agglomerating together, thereby improving the yield of treated powder.
更に、粉砕条件であるが本発明法では15龍以下の粗砕
原料を連続乾式粉砕して100メツシュ以下が50%以
上得られる程度の時間があれば十分で、これによって、
充分に防塵効果ををする活性金属の微粉を得ることがで
きる。Furthermore, regarding the pulverization conditions, in the method of the present invention, it is sufficient to continuously dry-pulverize the coarsely crushed raw material of 15 ryu or less and obtain 50% or more of 100 mesh or less, and thereby,
It is possible to obtain active metal fine powder that has a sufficient dust-proofing effect.
しかしながら、走査型電子顕微鏡下では添加された防塵
剤及び後述の脂肪酸乃至そのケン化物が防塵効果の顕著
な活性金属粉末繋合体中では明確に識別できず、そのメ
カニズムも定かでない。However, under a scanning electron microscope, the added dustproofing agent and the fatty acid or its saponified product, which will be described later, cannot be clearly identified in the active metal powder aggregate, which has a remarkable dustproofing effect, and the mechanism thereof is also unclear.
なお、防塵剤添加量及び時期との関連は特に限定はなく
、防塵剤が全体に分散するに必要な時間があれば十分で
ある。Note that there is no particular limitation on the amount and timing of addition of the dustproofing agent, and it is sufficient that the time required for the dustproofing agent to be dispersed throughout is sufficient.
分級工程に関してはその機構が付属された粉砕機では不
要であるが、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、通常工業内には防塵処理品を200
メツ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。Regarding the classification process, it is not necessary to use a crusher that is equipped with the mechanism, but in the case of unclassified products to be crushed, it is sufficient to classify them according to the target particle size.
It is possible to classify with a sieve mesh down to the mesh level. 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、それ等が弱く付着して形成
されるWE集粗大二次粒子径が60メッシュ以下で、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, exhibits a rounded granular shape, and a WE aggregate coarse secondary particle size formed by weak adhesion of these particles, which is 60 mesh or less, and 98% or more of the mesh is 100 meshes or less.
実施例1゜
純度99%以上のAIとMgを?8製して得た重量比で
A150.1− Mg48.9%の自家製合金地金を小
型ショークラッシャーで1011径以下に粗砕し、粗砕
原料を調整した。次に該AAl−1I合金粗砕原料2k
trに、防塵剤として明和化成工業株式会社製のポリエ
チレンオキサイド粉粒物(商品名アルコックスR150
)10gを内容積1iの磁性ボットミルに入れ窒素ガス
を装入して10時間乾式粉砕した。次いで得られた被粉
砕物1.82kgを100メツシュ篩網で分級し、10
0メッシュ以下の粉末製品1 、60 kgを得た。比
較流動試験Yにtjl!する測定で無粉塵性であった。Example 1゜AI and Mg with a purity of 99% or more? A homemade alloy ingot with a weight ratio of 0.1% A1 and 48.9% Mg was crushed using a small show crusher to a diameter of 1011 mm or less to prepare a crushed raw material. Next, the AAl-1I alloy coarse raw material 2k
tr, polyethylene oxide powder manufactured by Meiwa Kasei Kogyo Co., Ltd. (trade name Alcox R150) was used as a dustproofing agent.
) was placed in a magnetic bot mill with an internal volume of 1i, nitrogen gas was charged, and dry pulverization was carried out for 10 hours. Next, 1.82 kg of the obtained material to be crushed was classified using a 100-mesh sieve, and
1.60 kg of a powder product of 0 mesh or less was obtained. Tjl for comparative flow test Y! It was found to be dust-free when measured.
実施例2゜
純度99%以上のA1.l!:r′1gを溶装して得た
重量比でAf50.7− Mg48.0%の自家製合金
地金を小型ショークラッシャーで101径以下に粗砕し
粗砕原料を調整した。次に、該AI Mg合金粗砕原
料2kgに、防塵剤として明和化成工業株式会社製のポ
リエチレンオキサイド粉粒物(商品名アルコックスR1
50)10g及び顆粒状ステアリン酸4gを内容積14
I2の磁製ポットミルに入れ、窒素ガスを装入して10
時間乾式粉砕した。Example 2 A1. with a purity of 99% or more. l! A homemade alloy ingot having a weight ratio of 50.7% Af and 48.0% Mg obtained by welding 1 g of :r' was crushed to a size of 101 diameter or less using a small show crusher to prepare a coarsely crushed raw material. Next, polyethylene oxide powder manufactured by Meiwa Kasei Kogyo Co., Ltd. (trade name Alcox R1) was added to 2 kg of the AI Mg alloy coarse raw material as a dustproofing agent.
50) 10g and 4g of granular stearic acid in an internal volume of 14
Place it in a I2 porcelain pot mill and charge nitrogen gas for 10 minutes.
Dry milled for an hour.
次いで、得られた被粉砕物1.90kgを100メツシ
ュ篩絹で分級し、100メツシュ以下の粉末製品を1.
80kg得た。得られた100メ・ノシェ以下の製品は
比較流動試験では無粉塵性であった。この収率は実施例
1の場合より向上したものであった。Next, 1.90 kg of the obtained material to be crushed was classified using a 100-mesh silk sieve, and powder products with a size of 100 mesh or less were classified by 1.90 kg.
I gained 80kg. The resulting product with a size of 100 meters or less was dust-free in a comparative flow test. This yield was improved over that of Example 1.
実施例3゜
実施例1と同じ自家製合金地金を同様に処理してIon
径以下に粗砕し、粗砕原料を調整した。次に、該At−
Mg合金粗砕原料2kgに、三洋化成工業株式会社分子
ff11200のポリエチレングリコール粉粒物Log
及び顆粒状ステアリン酸4gを内容積14eの磁製ポッ
トミルに入れ、窒素ガスを装入して4時間乾式粉砕した
。Example 3゜The same homemade alloy ingot as in Example 1 was treated in the same manner as Ion.
The raw material was coarsely crushed to a size smaller than the diameter, and a coarsely crushed raw material was prepared. Next, the At-
To 2 kg of Mg alloy coarse raw material, Sanyo Chemical Industries Co., Ltd. polyethylene glycol powder with molecular weight ff11200 was added.
and 4 g of granular stearic acid were placed in a porcelain pot mill with an internal volume of 14 e, and nitrogen gas was introduced into the pot mill for dry pulverization for 4 hours.
次いで、得られた被粉砕物1.90kgを100メッシ
ュ篩網で分級し、100メツシュ以下の製品を1.82
kg得た。比較流動試験Yに準する測定で無粉塵性であ
った。Next, 1.90 kg of the obtained material to be crushed was classified using a 100 mesh sieve, and products with a size of 100 mesh or less were classified by 1.82 kg.
I gained kg. It was found to be dust-free when measured according to Comparative Flow Test Y.
この収率は実施例1の場合より向上したものであった。This yield was improved over that of Example 1.
比較例
実施例3と同様にして、ポリエチレングリコールを除い
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 3 under the same conditions except that polyethylene glycol was removed.
この被粉砕物は実施例3同様ポツトミルからほぼ全量に
相当する1、91gを排出したが、排出時の発塵は激し
かった。実施例3と同様にして得た100メツシュ以下
の製品収量は1.65kgであったが、比較流動試験で
は全く防塵性はなかった。Similar to Example 3, 1.91 g of the crushed material, which corresponds to almost the entire amount, was discharged from the pot mill, but a large amount of dust was generated during discharge. The yield of a product of 100 mesh or less obtained in the same manner as in Example 3 was 1.65 kg, but in a comparative flow test, it had no dust resistance at all.
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、防塵剤の使用量を少なく
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am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e=W粉を得る
ことができる。By using the dry process of the present invention to process the pulverization and dust-free treatment of coarsely crushed raw materials in the same process, the amount of dust-proofing agent used can be reduced and the properties of the active metal powder can be maintained without deteriorating to the same extent as in the manufacturing process. It is possible to obtain e=W powder which can completely prevent dust explosion and eliminates the risk of dust explosion during handling.
Claims (1)
リエチレングリコール及び、またはポリエチレンオキサ
イドの防塵剤を0.01〜0.5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重量部に粉粒状ポ
リエチレングリコール及び、またはポリエチレンオキサ
イドの防塵剤を0.01〜0.5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 0.01 to 0.5 parts by weight of a dustproofing agent of granular polyethylene glycol and/or polyethylene oxide to 100 parts by weight of active metal raw material grains at the coarse crushing stage to form an inert powder. A method for producing a dust-proof active metal powder, which comprises continuously dry-pulverizing the powder in a gas atmosphere until at least 50% of the powder has a particle size of 100 mesh or less. 2. Add 0.01 to 0.5 parts by weight of a dustproofing agent of granular polyethylene glycol and/or polyethylene oxide to 100 parts by weight of active metal raw material particles at the coarse crushing stage, and 0.05 to 0.5 parts by weight of a solid fatty acid or its saponified product. 1. A method for producing a dust-proof active metal powder, which comprises adding and mixing parts by weight and dry-pulverizing continuously under an inert gas atmosphere until 50% or more of fine powder of 100 mesh or less is obtained.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61243851A JPH07103402B2 (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 |
---|---|---|---|
JP61243851A JPH07103402B2 (en) | 1986-10-13 | 1986-10-13 | Method for producing dustproof active metal powder |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6396202A true JPS6396202A (en) | 1988-04-27 |
JPH07103402B2 JPH07103402B2 (en) | 1995-11-08 |
Family
ID=17109897
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61243851A Expired - Lifetime JPH07103402B2 (en) | 1986-10-13 | 1986-10-13 | Method for producing dustproof active metal powder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07103402B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0480319A (en) * | 1990-07-20 | 1992-03-13 | Parker Netsushiyori Kogyo Kk | Heating medium agent for heat treatment |
-
1986
- 1986-10-13 JP JP61243851A patent/JPH07103402B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0480319A (en) * | 1990-07-20 | 1992-03-13 | Parker Netsushiyori Kogyo Kk | Heating medium agent for heat treatment |
Also Published As
Publication number | Publication date |
---|---|
JPH07103402B2 (en) | 1995-11-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0311369A1 (en) | Method for the production of a composite metal powder and the powder produced thereby | |
NL8500654A (en) | PROCESS FOR PREPARING NUCLEAR FUEL GRANULES. | |
US3090567A (en) | Size reduction of metal particles | |
US3918933A (en) | Nickel-lanthanum alloy produced by a reduction-diffusion process | |
US5902373A (en) | Sponge-iron powder | |
JPS6396202A (en) | Production of dustproof active metal powder | |
JPS62501081A (en) | Processing methods for refining metals and alloys | |
US3591349A (en) | High carbon tool steels by powder metallurgy | |
KR101854068B1 (en) | Process for producing ru-containing corrosion-resistant titanium alloy | |
JPS6396201A (en) | Production of dustproof active metal powder | |
US3389990A (en) | Manganese nitride | |
US3963482A (en) | Large size aluminum particle containing aluminum oxide therein | |
US4543197A (en) | Process for producing magnetic metallic oxide | |
US3737301A (en) | Process for producing iron-molybdenum alloy powder metal | |
US3988146A (en) | Process for producing large particle size aluminum pigments by working and welding smaller particles | |
JPS61238901A (en) | Ferromagnetic powder | |
JPH0224881B2 (en) | ||
JPH03111527A (en) | Manufacture of silicon carbide-containing alloy | |
JPS6199638A (en) | Manufacture of iron powder from pig iron-containing slag | |
JPH07278612A (en) | Method for crushing sponge titanium | |
JPS5879829A (en) | Preparation of iron disulfide | |
JPS5935971B2 (en) | How to process sintered ore | |
SU1101463A1 (en) | Batch for producing manganese agglomerate | |
JPS6136046B2 (en) | ||
JPS5873731A (en) | Regenerating method of magnet material containing rare earth |