JPH07103402B2 - Method for producing dustproof active metal powder - Google Patents
Method for producing dustproof active metal powderInfo
- Publication number
- JPH07103402B2 JPH07103402B2 JP61243851A JP24385186A JPH07103402B2 JP H07103402 B2 JPH07103402 B2 JP H07103402B2 JP 61243851 A JP61243851 A JP 61243851A JP 24385186 A JP24385186 A JP 24385186A JP H07103402 B2 JPH07103402 B2 JP H07103402B2
- Authority
- JP
- Japan
- Prior art keywords
- active metal
- weight
- powder
- dustproof
- mesh
- 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
Links
- 239000000843 powder Substances 0.000 title claims description 31
- 229910052751 metal Inorganic materials 0.000 title claims description 20
- 239000002184 metal Substances 0.000 title claims description 20
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 19
- 239000002994 raw material Substances 0.000 claims description 13
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 11
- 239000002202 Polyethylene glycol Substances 0.000 claims description 11
- 229920001223 polyethylene glycol Polymers 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 9
- 238000010298 pulverizing process Methods 0.000 claims description 5
- 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
- 239000011261 inert gas Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims 1
- 239000000428 dust Substances 0.000 description 10
- 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
- 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
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910000861 Mg alloy Inorganic materials 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 229910052573 porcelain Inorganic materials 0.000 description 2
- 229910018134 Al-Mg Inorganic materials 0.000 description 1
- 229910018467 Al—Mg Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 150000002739 metals Chemical class 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
- 230000002265 prevention Effects 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
- 238000009628 steelmaking Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Powder Metallurgy (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
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,反応触
媒,金属精錬,発熱剤,花火,溶接棒等広汎に利用され
ているCa,Mg,Al,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。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is widely used in deoxidizing agents for steelmaking, refractory additives, paints, reaction catalysts, metal refining, exothermic agents, fireworks, welding rods and the like. The present invention relates to a method for producing a powder of an active metal such as Ca, Mg, Al, Si, Zr, Ti, Fe or their alloys in a state where dust resistance and explosion resistance are improved without impairing 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 producing powders of these active metals, atomization and mechanical crushing of impellers, stamps, ball mills, etc. are often used, so explosion-proof measures are extremely important in addition to dust prevention.
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。Dust-proof and explosion-proof measures for treating such active metal powders with strong oxidizing power, which have been conventionally taken, are to treat with a liquid such as oil or ethylene glycol, or to impregnate these liquids with the treated powder sufficiently. It was common practice.
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52−32877
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, it may be desirable to use it as a dry powder, and as a dust-free treatment method for this purpose, Japanese Patent Publication No.
As described in JP-B No. 55-24481, etc., there is a method in which a granular polytetrafluoroethylene (PTFE) resin is mixed with active metal powder and treated.
上記PTFEは金属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、その添加も粉砕
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-type dustproofing agent for metal powders, but it is expensive in itself, and since its addition is also added when pulverization is completed, it is dust in the process of obtaining fine powder. Explosion risk is high.
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
属の特性に何ら悪影響を与えることなく、しかも微粉化
工程での粉塵爆発の危険を回避できる防塵活性金属粉末
の製造方法に提供することにある。The object of the present invention is to find a dustproofing agent that is cheaper than the above-mentioned conventional dustproofing agent PTFE, and using the dustproofing agent does not have any adverse effect on the characteristics of the active metal, and yet dust in the micronization process is used. It is an object of the present invention to provide a method for producing a dustproof active metal powder capable of avoiding the danger of explosion.
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 trial and error, the present invention has found that the above-mentioned objects can be achieved by specifying the addition conditions of powdery-grain polyethylene glycol and polyethylene oxide, which are less expensive than PTFE.
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,P
TFE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何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 step of dedusting into fine particles, in the step of crushing the active metal, powdered granular polyethylene glycol or polyethylene oxide is added and mixed to this crushed active powder, and further, Dust-proof while crushing raw materials in an inert gas atmosphere.
It enables the use of inexpensive dustproofing agents in place of TFE, and succeeded in developing a dustproofing function in parallel with the progress of explosion-proof pulverization without adversely affecting the characteristics of the active metal with a small addition 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。As a matter of course, powdery particulate polyethylene glycol or polyethylene oxide as a dustproof agent can be used together 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。Further, in the present invention, by adding simultaneously a solid fatty acid such as stearic acid or a saponified product thereof together with polyethylene glycol or polyethylene oxide, in addition to the effect of addition of polyethylene glycol or polyethylene oxide in the above-mentioned crushing step, powder It is possible to increase the yield of the powder by reducing the adhesion of the powder to the crusher and the aggregation of the particles.
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15mm以下の場合が防塵効果上から最も
効率が良く、15mm以上の粗粒が多くなると100メッシュ
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粉砕機では、8mm以下
のものが最も経済的である。In the step of crushing the active metal in the step of adding the dustproofing agent powder such as polyethylene glycol or polyethylene oxide, the particle diameter of 15 mm or less is the most efficient in terms of the dustproofing effect, and if the number of coarse particles of 15 mm or more increases 100 The crushing efficiency is too poor to obtain fine powders below the mesh. Although the preferable raw material particle size depends on the crusher selected, a crusher such as an impeller, a stamp or a ball mill is most economical when it has a diameter of 8 mm or less.
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。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。Next, the amount of the particulate dust-removing polyethylene glycol and / or polyethylene oxide added is 0.01% of the granular material with respect to 100 parts by weight of the crushed active metal raw material.
It may be used in an amount of up to 0.5 parts by weight, and the appropriate addition amount will vary depending on the crushing model and crushing conditions. Usually, if the amount is less than 0.01 parts by weight, the dustproof effect is weak, and if the amount is more than 0.1 parts by weight, the adhesion and cohesive force is too strong and the discharge and classification become poor 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何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。Further, in the case of adding 0.05 to 0.5 parts by weight of a solid fatty acid such as stearic acid or a saponified product thereof for improvement thereof, adhesion to a crusher and particles of the same particles are prevented without any inhibition of the dustproof effect of the dustproofing agent. It is possible to effectively prevent agglomeration and improve the yield of the treated powder.
更に、粉砕条件であるが本発明法では15mm以下の粗砕原
料を連続乾式粉砕して100メッシュ以下が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
防塵効果を有する活性金属の微粉を得ることができる。Further, although it is a crushing condition, in the method of the present invention, it is sufficient if there is a time such that 50% or more of 100 mesh or less is obtained by continuously dry crushing a coarsely crushed raw material of 15 mm or less, and thereby, a sufficient dustproof effect can be obtained. A fine powder of active metal can be obtained.
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
な活性金属粉末聚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 described below or its saponified product cannot be clearly identified in the active metal powder composite having a remarkable dustproofing effect, and its mechanism is not clear.
なお、防塵剤添加量及び時期との関連には特に限定はな
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。The relationship between the amount of dustproofing agent added and the timing is not particularly limited, and the time necessary 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、通常工業的には防塵処理品を200メ
ッ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。The classification process is not necessary with a crusher equipped with that mechanism, but in the case of unclassified crushed products, classification can be done according to the target particle size. It can be classified with a sieve screen. Since this work is dust-free, it has a good environment 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
れる凝集粗大二次粒子径が60メッシュ以下で、且つ、10
0メッシュ以下が98%以上から成るものである。The obtained dustproof powder has a single particle size of 60 mesh or less,
It exhibits a roundish granularity, and the aggregated coarse secondary particle diameter formed by weakly adhering them is 60 mesh or less, and 10
0 mesh or less consists of 98% or more.
実施例1. 純度99%以上のAlとMgを溶製して得た重量比でAl50.7−
Mg48.9%の自家製合金地金を小型ジョークラッシャーで
10mm径以下に粗砕し、粗砕原料を調整した。次に該Al−
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R150)10gを内容積14の磁性ポットミルに入れ
窒素ガスを装入して10時間乾式粉砕した。次いで得られ
た被粉砕物1.82kgを100メッシュ篩網で分級し、100メッ
シュ以下の粉末製品1.60kgを得た。比較流動試験Yに準
ずる測定で無粉塵性であった。Example 1. Al50.7-at a weight ratio obtained by melting Al and Mg having a purity of 99% or more.
Homemade alloy ingot of Mg 48.9% with a small jaw crusher
The material was roughly crushed to have a diameter of 10 mm or less to prepare a roughly crushed raw material. Next, the Al-
10g polyethylene oxide powder (trade name Alcox R150) manufactured by Meiwa Kasei Co., Ltd. as a dustproofing agent in 2kg of Mg alloy coarsely crushed raw material was placed in a magnetic pot mill with an internal volume of 14 and nitrogen gas was charged to dry it for 10 hours. Crushed. Next, 1.82 kg of the obtained pulverized product was classified with a 100 mesh sieve mesh to obtain 1.60 kg of a powder product having 100 mesh or less. No dust was observed according to the measurement according to the comparative flow test Y.
実施例2. 純度99%以上のAlとMgを溶製して得た重量比でAl50.7−
Mg48.0%の自家製合金地金を小型ジョークラッシャーで
10mm径以下に粗砕し粗砕原料を調整した。次に、該Al−
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R150)10g及び顆粒状ステアリン酸4gを内容積14
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. Al50.7-at a weight ratio obtained by melting Al and Mg having a purity of 99% or more.
Homemade alloy ingot of Mg48.0% with a small jaw crusher
The material was roughly crushed to a diameter of 10 mm or less to prepare a roughly crushed raw material. Next, the Al-
2 kg of Mg alloy coarsely crushed raw material, 10 g of polyethylene oxide powder (trade name Alcox R150) manufactured by Meiwa Kasei Kogyo Co., Ltd. and 4 g of granular stearic acid as an anti-dust agent in the internal volume 14
It was put into a porcelain pot mill, and nitrogen gas was charged, followed by dry pulverization for 10 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メッシュ以下の粉末製品を1.80kg得た。得
られた100メッシュ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。Then, 1.90 kg of the obtained pulverized material was classified by a 100 mesh sieve mesh to obtain 1.80 kg of a powder product having 100 mesh or less. The obtained product of 100 mesh or less was dust-free in the comparative flow test. This yield was higher than in the case 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10mm径
以下に粗砕し、粗砕原料を調整した。次に、該Al−Mg合
金粗砕原料2kgに、三洋化成工業株式会社分子量1200の
ポリエチレングリコール粉粒物10g及び顆粒状ステアリ
ン酸4gを内容積14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 home-made alloy ingot as in Example 1 was treated in the same manner and was crushed to a diameter of 10 mm or less to prepare a crushed raw material. Next, 2 g of the Al-Mg alloy coarsely crushed raw material was charged with 10 g of polyethylene glycol powder having a molecular weight of 1200 and 4 g of granular stearic acid in a porcelain pot mill with an internal volume of 14 and charged with nitrogen gas. And pulverized 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メッシュ以下の製品を1.82kg得た。比較流
動試験Yに準ずる測定で無粉塵性であった。Next, 1.90 kg of the obtained pulverized product was classified with a 100 mesh screen to obtain 1.82 kg of a product having 100 mesh or less. No dust was observed according to the measurement according to the 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 higher than in the case 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 As in Example 3, grinding was performed under the same conditions except that polyethylene glycol was removed.
この被粉砕物は実施例3同様ポッ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メッシュ以下の製品
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。1.91 g of this pulverized product was discharged from the pot mill in the same manner as in Example 3, corresponding to almost the entire amount, but the dust generation during discharge was severe. The product yield of 100 mesh or less obtained in the same manner as in Example 3 was 1.65 kg, but there was no dustproof property in the comparative flow test.
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何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
における防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 processing the crushing and dedusting of the coarsely crushed raw material in the same process by the method of the present invention, the amount of the dustproofing agent used is reduced and the characteristics of the active metal powder are not lowered at all. It is possible to obtain dust-proof fine powder which can completely prevent dust explosion and eliminate the risk of dust-proof explosion during handling.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 伊藤 信吾 岐阜県本巣郡巣南町古橋289の1 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Shingo Ito 1 289, Furuhashi, Sunan-cho, Motosu-gun, Gifu Prefecture
Claims (2)
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5
0%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。1. A 0.01 to 0.5 part by weight of a dustproof agent of powdered polyethylene glycol and / or polyethylene oxide is added to and mixed with 100 parts by weight of the active metal raw material particles at the crushing stage, and 100 mesh under an inert gas atmosphere. The following fine powder is 5
A method for producing a dustproof active metal powder, which comprises continuously dry pulverizing until 0% or more is obtained.
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。2. To 100 parts by weight of the active metal raw material particles in the crushing stage, 0.01 to 0.5 parts by weight of a particulate polyethylene glycol and / or polyethylene oxide dustproofing agent and 0.05 to 0.5 parts by weight of a solid fatty acid or a saponified product thereof are added. Mix
50% of fine powder of 100 mesh or less under inert gas atmosphere
A method for producing a dustproof active metal powder, which comprises continuously dry pulverizing until the above 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 JPS6396202A (en) | 1988-04-27 |
| JPH07103402B2 true 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) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0480319A (en) * | 1990-07-20 | 1992-03-13 | Parker Netsushiyori Kogyo Kk | Preparation for heat treatment heat medium |
-
1986
- 1986-10-13 JP JP61243851A patent/JPH07103402B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6396202A (en) | 1988-04-27 |
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