JPH0421702A - Fine metal powder and its manufacturing method - Google Patents

Fine metal powder and its manufacturing method

Info

Publication number
JPH0421702A
JPH0421702A JP2127993A JP12799390A JPH0421702A JP H0421702 A JPH0421702 A JP H0421702A JP 2127993 A JP2127993 A JP 2127993A JP 12799390 A JP12799390 A JP 12799390A JP H0421702 A JPH0421702 A JP H0421702A
Authority
JP
Japan
Prior art keywords
metal powder
powder
phosphoric acid
metal
fine
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
JP2127993A
Other languages
Japanese (ja)
Other versions
JP2602979B2 (en
Inventor
Michitoshi Hirata
平田 道利
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.)
MATE Co Ltd
Original Assignee
MATE Co Ltd
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 MATE Co Ltd filed Critical MATE Co Ltd
Priority to JP2127993A priority Critical patent/JP2602979B2/en
Publication of JPH0421702A publication Critical patent/JPH0421702A/en
Application granted granted Critical
Publication of JP2602979B2 publication Critical patent/JP2602979B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01FMAGNETS; INDUCTANCES; TRANSFORMERS; SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES
    • H01F1/00Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties
    • H01F1/01Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials
    • H01F1/03Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity
    • H01F1/032Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of hard-magnetic materials
    • H01F1/04Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of hard-magnetic materials metals or alloys
    • H01F1/06Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of hard-magnetic materials metals or alloys in the form of particles, e.g. powder
    • H01F1/061Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of hard-magnetic materials metals or alloys in the form of particles, e.g. powder with a protective layer

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  • Engineering & Computer Science (AREA)
  • Power Engineering (AREA)
  • Powder Metallurgy (AREA)
  • Hard Magnetic Materials (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、プラスチック材料と一緒に混練し、成形して
所謂プラスチックマグネットを製造するための磁性粉末
或は、焼結コア製造用金属粉末等の各種用途に使用され
る金属微粉末及びこれの製法に関するものである。
Detailed Description of the Invention (Field of Industrial Application) The present invention is directed to magnetic powder for producing so-called plastic magnets by kneading with plastic materials and molding, or metal powder for producing sintered cores. The present invention relates to fine metal powders used for various purposes and methods for producing the same.

(背景技術) プラスチックマグネット用の磁性粉末、焼結コア用の金
属粉末などは、流動性の向上、成形品及び焼結晶の緻密
性向上及び磁場配向性の向上環の理由によって、その粒
度を可及的に小さくすることが望ましい。
(Background technology) The particle size of magnetic powder for plastic magnets, metal powder for sintered cores, etc. can be changed to improve fluidity, improve compactness of molded products and sintered crystals, and improve magnetic field orientation. It is desirable to make it as small as possible.

しかし、金属粉末は粒度か小さい程、表面積は粒度の2
乗に比例して増加し、酸化し易くなる。特に稀土類合金
磁石を製造するための磁性粉末は特にこの傾向が強い。
However, the smaller the particle size of metal powder, the smaller the surface area
It increases in proportion to the power of oxidation, making it easier to oxidize. This tendency is particularly strong in magnetic powders used to manufacture rare earth alloy magnets.

しかも金属を平均粒径が10ミクロン以下まで粉砕する
と、粒子中には1ミクロン以下の超微粒子が確率的に数
%混在しており、微粉砕によって極めて活性の強い新生
金属面が発生しているから、金属を微粉末化する過程で
は、金属の酸化の問題を避けることは出来ない。
Furthermore, when a metal is crushed to an average particle size of 10 microns or less, there is a probability that several percent of the particles are mixed with ultrafine particles of 1 micron or less, and as a result of pulverization, a new metal surface with extremely high activity is generated. Therefore, in the process of pulverizing metals, the problem of metal oxidation cannot be avoided.

5ミクロン以下の粒径にまで粉砕した場合、自然発火し
、燃えてしまう危険な状態となる。
If it is crushed to a particle size of 5 microns or less, it will spontaneously ignite and become a dangerous situation.

(従来の技術) 従来は金属粉末の耐熱性を向上するために、金属粉末の
表面に有機系物質の表面皮膜を形成していたが、この場
合、粉砕工程の後、金属粉砕装置から金属粉末を取り出
してから、金属粉末に被覆処理を行なっている。そのた
め、粉砕装置から金属粉末を取り出す際に、必然的に金
属粉末が大気に触れて自然発火する問題かあった。
(Prior art) Conventionally, in order to improve the heat resistance of metal powder, a surface film of an organic substance was formed on the surface of the metal powder, but in this case, after the pulverization process, the metal powder was After the metal powder is removed, the metal powder is coated. Therefore, when taking out the metal powder from the crusher, there was a problem that the metal powder inevitably came into contact with the atmosphere and spontaneously ignited.

出願人は以前、不活性雰囲気中で金属粒から微粉末を造
り、該金属微粉末を大気中へ取り出す前に、不活性雰囲
気下で燐酸エステル溶液を投入し、金属微粉末の表面に
燐酸エステル系の有機金属化合物の薄皮膜を形成する方
法を提案した(特開平1−234502)。この方法は
金属微粉末を金属粉砕装置から取り出さすに、金属粉砕
と粉体の被覆処理を不活性雰囲気中で行なったから、金
属微粉末の自然発火の問題は回避でき、5ミクロン以下
まで微粉末化できた。
Previously, the applicant made fine powder from metal particles in an inert atmosphere, and before taking out the fine metal powder into the atmosphere, put a phosphate ester solution in the inert atmosphere to coat the surface of the fine metal powder with phosphoric ester. proposed a method for forming a thin film of an organometallic compound (Japanese Unexamined Patent Publication No. 1-234502). This method avoids the problem of spontaneous ignition of fine metal powder because the metal crushing and powder coating treatment are carried out in an inert atmosphere before taking out the fine metal powder from the metal crushing equipment. I was able to turn it into

この微粉末は表面が燐酸エステル系の薄膜によって覆わ
れ、極めて美麗であるか、耐熱温度は高々300℃まで
であり、これ以上に温度を上げると薄膜は熱分解して下
地の金属微粉末の酸化が始まる問題があった。
The surface of this fine powder is covered with a thin film of phosphoric acid ester, which makes it extremely beautiful and has a heat resistance temperature of up to 300°C.If the temperature is raised above this temperature, the thin film will thermally decompose and the underlying metal fine powder will be destroyed. There was a problem with oxidation starting.

そのため出願人の前出の提案では表面に燐酸エステル系
の有機金属化合物の薄膜を形成した金属粉末を、更に2
00〜450℃に加熱することによって、薄膜を高温下
でも安定な燐酸系金属化合物の薄膜にする工程を付加し
た。これによって、薄膜中の有機成分が除かれ、その後
に僅かに露出する金属面は雰囲気中の酸素と結合し、粉
末粒子表面は燐酸系金属化合物が覆って、粉末の耐熱性
を向上した。しかし加熱工程を付加することによって、
製品はコスト高となる問題かあった。
Therefore, in the applicant's proposal mentioned above, a metal powder with a thin film of a phosphate ester-based organometallic compound formed on the surface is further added.
A step was added in which the thin film was made into a thin film of a phosphoric acid-based metal compound that was stable even at high temperatures by heating to 00 to 450°C. As a result, the organic components in the thin film were removed, and the slightly exposed metal surface was then combined with oxygen in the atmosphere, and the powder particle surface was covered with a phosphoric acid-based metal compound, improving the heat resistance of the powder. However, by adding a heating process,
There was a problem with the product's high cost.

しかも製品の粒子表面は、有機成分か除かれた燐酸系金
属化合物か覆っているとは言っても、これは有機金属化
合物の薄膜か、加熱処理によって変化して形成されたも
のであるから、−様ではなく、そのため耐酸化性は未だ
十分てはなかった。
Moreover, even though the particle surface of the product is covered with a phosphoric acid-based metal compound from which organic components have been removed, this is either a thin film of an organometallic compound or is formed by being changed by heat treatment. -, and therefore the oxidation resistance was still not sufficient.

(解決しようとする問題点) 金属微粉末を樹脂と混練して成形する場合、樹脂の溶融
温度よりも可成り高い温度(50〜100℃)の下で混
練される。混練機の局所では、混線中に高温を発生する
場合か屡々あるため、金属微粉末の薄膜は、経験的に4
00 ’C以上、好ましくは500 ’C以上の耐熱温
度を有している必要がある。
(Problems to be Solved) When fine metal powder is kneaded with a resin and molded, the kneading is carried out at a temperature considerably higher than the melting temperature of the resin (50 to 100°C). Since high temperatures are often generated locally in the kneading machine during cross-talk, it has been empirically shown that the thin film of fine metal powder has a temperature of 4.
It is necessary to have a heat resistance temperature of 00'C or higher, preferably 500'C or higher.

従来の多くの燐酸系、或いは他の有機系表面被覆金属微
粉末か300℃以上、特に500 ’C以上の高温に耐
えられなかった点は、上述の通り有機系化合物による薄
膜被覆層を主体としたからである。
Many conventional phosphoric acid-based or other organic surface-coated metal fine powders cannot withstand high temperatures of 300°C or higher, especially 500°C or higher, as mentioned above, because they are mainly made of thin film coating layers made of organic compounds. Because I did.

発明者は、金属微粉末の耐熱温度向上の研究を続けてい
る過程で、金属微粉末へ投入するための燐酸エステル溶
液は、燐酸とアルコールを調合して製造した時間的に新
らしいものを使用した場合は、金属微粉末は高い耐熱温
度を示すが、調合して数週間放置した燐酸エステル溶液
を使用した場合は、金属微粉末の耐熱温度は低下する傾
向かあることを知った。この原因を究明した結果、新ら
しい燐酸アルコール溶液の場合は、燐酸の大部分は未だ
エステル化せずにアルコール中で混合状態で存在してい
るからであることを見い出し、本発明を完成した。
In the process of continuing research on improving the heat resistance temperature of fine metal powder, the inventor used a phosphoric acid ester solution to be added to fine metal powder, which was a novel solution made by mixing phosphoric acid and alcohol. In this case, the fine metal powder has a high temperature resistance, but when a phosphate ester solution that has been prepared and left for several weeks is used, the temperature resistance of the fine metal powder tends to decrease. As a result of investigating the cause of this, it was discovered that in the case of a new phosphoric acid alcohol solution, most of the phosphoric acid was not yet esterified and existed in a mixed state in the alcohol, and the present invention was completed.

(目 的) 本発明は不活性雰囲気中での金属粉砕工程に引き続いて
、同し不活性不雰囲気中にて金属微粉末に対し表面被覆
処理工程を実施するだけで、500 ’C以上の耐熱温
度を有する金属微粉末及びそれの製法を提供することを
目的とYる。
(Purpose) The present invention provides heat resistance of 500'C or more by simply carrying out a surface coating treatment process on fine metal powder in the same inert atmosphere following a metal grinding process in an inert atmosphere. The purpose of the present invention is to provide a fine metal powder having a high temperature and a method for producing the same.

更に本発明は、有機溶剤を使用しなから、燐酸の有機化
を効果的に抑制し、且つ金属の粉砕過程で得られる極め
て活性の高い微粉末の新生表面と、燐酸化反応を起させ
て、耐酸化性に優れた金属微粉末を得る方法を提供する
ものである。
Furthermore, since the present invention does not use an organic solvent, it effectively suppresses the organic conversion of phosphoric acid, and causes a phosphorylation reaction with the new surface of the highly active fine powder obtained in the metal crushing process. , provides a method for obtaining fine metal powder with excellent oxidation resistance.

尚、この出願において、「金属」とは、強磁性合金例え
ばRCo s、RCO+7(RはSm、Pr、Ce、L
a等の稀土類元素)、Nd−Fe−B−Co系合金、ア
ルニコ合金、強磁性金属鉄、その他の金属及び合金を含
む。「燐酸Jとは、燐酸(H,PO,)のみでなく、無
機の燐基、金属燐酸化合物、その他の無機燐化合物を含
むものとする。
In this application, "metal" refers to ferromagnetic alloys such as RCos, RCO+7 (R is Sm, Pr, Ce, L
(rare earth elements such as a), Nd-Fe-B-Co alloys, alnico alloys, ferromagnetic metallic iron, and other metals and alloys. "Phosphoric acid J includes not only phosphoric acid (H, PO,) but also inorganic phosphorus groups, metal phosphoric acid compounds, and other inorganic phosphorus compounds.

「有機溶媒」とは、メタノール、エタノール、イソプロ
ピルアルコール等のアルコール類、その他有機基を有し
燐酸を分散させる溶媒を意味する。
"Organic solvent" means alcohols such as methanol, ethanol, isopropyl alcohol, and other solvents having an organic group and dispersing phosphoric acid.

(構 成) 本発明は、金属微粉末の粒体に対し、有機基を含まない
無機燐酸化合物の薄膜によって表面を一様に覆った金属
微粉末である。
(Structure) The present invention is a fine metal powder whose surface is uniformly covered with a thin film of an inorganic phosphoric acid compound containing no organic group.

更に本発明は、不活性雰囲気中で金属微粉末を作り、該
金属微粉末を大気中へ取り出す前に、不活性雰囲気中に
て、燐酸と有機溶媒との混合液であって有機燐酸化合物
か殆んと発生していない状態において、これを金属微粉
末へ接触させ、金属微粉末の破砕によって得られた活性
度の高い金属表面を無機燐酸金属化合物の薄膜によって
覆うことを特徴とする金属微粉末の製法である。
Further, in the present invention, a fine metal powder is produced in an inert atmosphere, and before the fine metal powder is taken out into the atmosphere, a mixture of phosphoric acid and an organic solvent, which is an organic phosphoric acid compound, is prepared in an inert atmosphere. A metal fine powder is brought into contact with fine metal powder in a state in which almost no generation occurs, and the highly active metal surface obtained by crushing the fine metal powder is covered with a thin film of an inorganic metal phosphate compound. This is a powder manufacturing method.

(作用効果) 本発明の金属微粉末は、無機の燐酸化合物によって表面
を一様に覆い、有機系の成分は含まないから、耐熱温度
は著しく向上し、平均的に500℃以上の高温に耐える
ことが出来た。
(Effects) The fine metal powder of the present invention uniformly covers the surface with an inorganic phosphoric acid compound and does not contain organic components, so its heat resistance is significantly improved, and it can withstand high temperatures of 500°C or more on average. I was able to do it.

更に本発明では金属微粉砕工程と被覆処理工程を同じ不
活性雰囲気中で実施され、しかも被覆処理は1回の工程
で、短時間に終了するから、製造コストは安価である利
点がある。
Further, in the present invention, the metal pulverization process and the coating process are carried out in the same inert atmosphere, and the coating process is completed in a short time in one process, so that the manufacturing cost is low.

尚、粉砕工程と被覆処理工程を分けて一連の不活性雰囲
気中で別々の装置で処理することも可能である。
Incidentally, it is also possible to separate the pulverizing step and the coating step and perform the processing in separate apparatuses in a series of inert atmospheres.

(実施例) 第1図は本発明方法の実施に用いる金属粉末の酸化防止
被覆処理装置を示している。
(Example) FIG. 1 shows an oxidation-preventing coating treatment apparatus for metal powder used in carrying out the method of the present invention.

実施例の装置は、金属粒を粉末化する粉砕装置を兼用し
ており、粉砕助剤として水を溶がさない水不溶性不活性
有機゛溶媒例えばトルエン、ヘキサン、ヘプタン等の炭
化水素系溶剤を使用し、該粉砕助剤中にて且つ不活性雰
囲気下で湿式粉砕を行ない、金属粒を粉末化した後、直
ちに被覆処理を行なうことか出来る。
The apparatus of the embodiment also serves as a pulverizer for pulverizing metal particles, and a water-insoluble inert organic solvent that does not dissolve water, such as a hydrocarbon solvent such as toluene, hexane, or heptane, is used as a pulverizing aid. The coating treatment can be carried out immediately after the metal particles are powdered by wet grinding in the grinding aid and under an inert atmosphere.

上面か開口した筒状攪拌槽(1)に気密に蓋板(13)
を被せ、攪拌槽内に攪拌体(2)を垂下配備している。
Airtightly attach a lid plate (13) to the cylindrical stirring tank (1) with its top open.
The agitation body (2) is placed in the agitation tank and suspended inside the agitation tank.

攪拌体(2)は蓋(13)の中央部を回転自由に且つ気
密に貫通した回転軸(21)に攪拌槽(1)内にて半径
方向に複数本の掻き棒(22)を突設して形成され、蓋
板(13)から外方へ突出した軸(21)上端に可変速
回転駆動装置(23)が連繋される。
The stirring body (2) has a plurality of scraping rods (22) protruding in the radial direction inside the stirring tank (1) on a rotating shaft (21) that freely and airtightly penetrates the center of the lid (13). A variable speed rotary drive device (23) is connected to the upper end of a shaft (21) that projects outward from the cover plate (13).

攪拌槽(1)は2重構造であり、内壁と外壁との間は冷
却水充填室(10)となっており、該室に冷却水供給口
(11)及び排出口(12)が接続されている。
The stirring tank (1) has a double structure, with a cooling water filling chamber (10) between the inner wall and the outer wall, and a cooling water supply port (11) and a discharge port (12) are connected to this chamber. ing.

又、蓋板(13)を貫通して不活性ガス供給管(4)、
及びカス圧力計(5)か接続されている。
In addition, an inert gas supply pipe (4) passes through the cover plate (13),
and a gas pressure gauge (5) are connected.

上記装置の構成は、金属粒を粉末化する公知の湿式金属
粉砕装置と同様であって、攪拌槽(1)内に粉砕すべき
金属粒、直径5mm程度のスチールボール及びトルエン
、ベンセン、n−へキサン、これ等の1種又は2種以上
の混合液等の水不溶性有機溶媒を粉砕助剤として投入し
て施蓋する。不活性ガス供給管(4)からN2、Ar等
の不活性ガスを攪拌槽(1)内に充満させ、攪拌槽(1
)内を大気圧より少し高く維持して、外気の侵入を確実
に防止し、この状態にて攪拌体(2)を回転させる。
The configuration of the above-mentioned apparatus is similar to a known wet metal grinding apparatus for powdering metal particles, and a stirring tank (1) contains metal particles to be ground, steel balls with a diameter of about 5 mm, toluene, benzene, n- A water-insoluble organic solvent such as hexane or a mixture of one or more of these is added as a grinding aid and the mixture is covered. The stirring tank (1) is filled with an inert gas such as N2 or Ar from the inert gas supply pipe (4).
) is maintained a little higher than atmospheric pressure to reliably prevent outside air from entering, and in this state, the agitator (2) is rotated.

スチールボールと金属粒が衝突を繰り返し、金属粒が粉
砕される。
The steel ball and the metal particles repeatedly collide, and the metal particles are crushed.

この装置の特徴は、上記攪拌槽(1)内に被覆処理液の
供給管(61)を接続した点である。
A feature of this device is that a coating treatment liquid supply pipe (61) is connected to the stirring tank (1).

実施例では蓋板(13)を貫通して被覆処理液供給管(
61)を攪拌槽(1)内に挿入し、該供給管(61)に
処理液タンク(6)を接続している。
In the embodiment, a coating liquid supply pipe (
61) is inserted into the stirring tank (1), and the processing liquid tank (6) is connected to the supply pipe (61).

タンク(6)の上面開口には気密に蓋(62)が取付け
られ、更に、タンク(6)の上部に不活性ガス兜填管(
63)か橙緋六れ、タンク(6)の7寿而夫蓋との間の
気層部を常時不活性ガスにて充満し大気圧以上に維持し
、タンク(6)内への外気の流入を確実に防止している
A lid (62) is airtightly attached to the top opening of the tank (6), and an inert gas filling pipe (
63) The air layer between the tank (6) and the lid is constantly filled with inert gas to maintain it above atmospheric pressure, and outside air is allowed to flow into the tank (6). The inflow is reliably prevented.

又、攪拌槽(1)内の液の温度を計る液温計(7)が蓋
板(13)を貫通して配備されている。
Further, a liquid thermometer (7) for measuring the temperature of the liquid in the stirring tank (1) is provided through the lid plate (13).

表面処理液は、金属粒が所望粒径に粉砕され、被覆処理
を行なう直前の約10分以内に、別の容器中で、必要量
の燐酸にアルコール系溶剤を素早く、攪拌混合すること
により、燐酸のエステル化を可及的に抑え、これをタン
ク(6)へ移したものである。
The surface treatment solution is prepared by quickly stirring and mixing the necessary amount of phosphoric acid with an alcoholic solvent in a separate container within about 10 minutes just before the metal particles are crushed to the desired particle size and the coating is applied. The esterification of phosphoric acid was suppressed as much as possible and then transferred to the tank (6).

金属粉末の用途か、室温から200℃位の範囲で使用さ
れる程度であれば、エステル化が進んだ処理液によって
処理された金属微粉末でも、十分な耐酸化特性を示す。
If the metal powder is used in a temperature range from room temperature to about 200° C., even fine metal powder treated with a treatment liquid with advanced esterification exhibits sufficient oxidation resistance.

しかし200°C以上の高温で樹脂と混練され、成形さ
れる用途のためには、金属微粉末は、前述の燐酸エステ
ル化を避けた液で処理されて無機燐酸塩系薄膜で覆われ
たものを使用しなければならない。
However, for applications in which the fine metal powder is kneaded with resin and molded at high temperatures of 200°C or higher, it must be treated with a liquid that avoids phosphoric acid esterification and covered with an inorganic phosphate-based thin film. must be used.

金属粒が所望の粒径に粉砕された時点で、金属微粉末と
スチールボールとの攪拌を続けなから、被覆処理液を注
入バルブ(64)によってタンク(6)から供給管(6
1)を経て攪拌槽(1)中へ投入し、燐酸によって金属
微粉末の新生表面と反応させることにより、金属微粉末
表面に、燐酸金属化合物を主成分とする強固な無機燐酸
系の耐酸化薄膜を形成する。薄膜の形成反応は攪拌槽内
で攪拌しつつ行なわれているから、反応は2分以内の極
めて短時間で行なうのがよい。攪拌が長すぎると薄膜が
破壊されて金属の地肌が露われ、再び処理液と反応する
が、既に処理液中の燐酸は消費され、被覆処理液は不足
状態となる。
When the metal particles are pulverized to the desired particle size, without continuing stirring the fine metal powder and the steel balls, the coating solution is pumped from the tank (6) through the supply pipe (6) using the injection valve (64).
1) into a stirring tank (1) and react with the newly formed surface of the fine metal powder with phosphoric acid, so that the surface of the fine metal powder is coated with a strong inorganic phosphoric acid-based oxidation-resistant material whose main component is a phosphate metal compound. Forms a thin film. Since the thin film forming reaction is carried out in a stirring tank with stirring, the reaction is preferably carried out within a very short time of 2 minutes or less. If stirring is continued for too long, the thin film will be destroyed and the bare metal will be exposed and will react with the treatment liquid again, but the phosphoric acid in the treatment liquid will have already been consumed and the coating treatment liquid will become insufficient.

被覆処理液の投入量は後述する如く、金属微粉末の平均
粒径に応じて必要最小限度に厳密に決められているから
、被覆処理液か不足すると、処理液の薄膜の色も茶色味
を帯び、耐熱性が低下してくる。従って金属粉末と被覆
処理液との攪拌反応は、形成された薄膜を壊さない程度
に、短時間で終了する必要がある。
As will be explained later, the amount of coating solution to be fed is strictly determined to the minimum necessary amount according to the average particle size of the fine metal powder, so if there is a shortage of coating solution, the color of the thin film of the coating solution will turn brownish. heat resistance decreases. Therefore, the stirring reaction between the metal powder and the coating solution needs to be completed in a short time without damaging the formed thin film.

上記の如く、被覆処理液と金属粉末の反応を短時間に完
成させた後、蓋板(13)を外して、ポンプにて金属粉
末液を装置外に取出し、速やかに粉砕助剤及び被覆処理
液の残液を脱液処理した後、防爆対策を施した乾燥装置
に入れて、大気中で常温又は使用有機溶媒の引火点より
低い70°C以下にて常圧又は減圧加熱乾燥して燐酸化
被覆処理が終了する。
As mentioned above, after the reaction between the coating treatment liquid and the metal powder is completed in a short time, the lid plate (13) is removed, the metal powder liquid is taken out of the apparatus by the pump, and the crushing aid and the coating treatment are immediately carried out. After removing the residual liquid, place it in a drying device with explosion-proof measures, and heat and dry it in the atmosphere at room temperature or at 70°C or lower, which is lower than the flash point of the organic solvent used, under normal pressure or reduced pressure to produce phosphoric acid. The coating process is completed.

尚、量産用大形装置の場合は、粉末の投入口を上蓋板に
設け、開閉可能な排出口をタンク(6)の底部外周に設
けて、ポンプ類により金属粉末及び被覆処理液を一緒に
投入及び排出を行なうことも可能である。
In the case of a large-scale device for mass production, an inlet for the powder is provided on the top cover plate, and an outlet that can be opened and closed is provided on the outer periphery of the bottom of the tank (6), so that the metal powder and coating solution can be mixed together using pumps. It is also possible to input and discharge the liquid.

本発明の処理方法では、金属粉体の表面に燐酸−金属層
を形成するまでは、金属粉末を大気に触れさせないため
、被覆処理すべき金属粉体の粒度か5ミクロン以下(例
えば1ミクロン)であっても、酸化による自然発火の問
題は生じず、粉体の粒度を可及的に小さく出来、粉体の
流動性も良好である。
In the treatment method of the present invention, the metal powder is not exposed to the atmosphere until the phosphoric acid-metal layer is formed on the surface of the metal powder, so the particle size of the metal powder to be coated is 5 microns or less (for example, 1 micron). However, the problem of spontaneous combustion due to oxidation does not occur, the particle size of the powder can be made as small as possible, and the fluidity of the powder is also good.

表面処理液が金属微粉末の活性面と反応して得られた薄
膜層は、多元合金の金属との燐酸化の仕方によって薄膜
の色は異なり、青紫色(耐熱温度500℃以上)或いは
灰黒色(耐熱温度600 ’C以上)を呈する緻密な無
機燐酸金属化合物、又は無機燐金属化合物によって形成
されている。
The color of the thin film layer obtained by the reaction of the surface treatment liquid with the active surface of the fine metal powder varies depending on the method of phosphorylation with the metal of the multi-component alloy, and is blue-purple (heat resistant temperature 500℃ or higher) or gray-black. It is formed from a dense inorganic phosphoric acid metal compound or an inorganic phosphorus metal compound exhibiting a heat resistance temperature of 600'C or more.

金属微粉末の工業的生産においては、操作し易さと経済
性のためには、金属微粉末の平均粒径に対して燐酸の量
を規定する必要かある。
In the industrial production of fine metal powders, for ease of operation and economy, it is necessary to specify the amount of phosphoric acid relative to the average particle size of the fine metal powders.

燐酸か金属微粉末に対して過剰であると、被覆処理後の
乾燥工程中で、処理液中の残留燐酸とアルコール系溶剤
か反応してエステル化か進み、これか接着作用を持って
、金属微粉末層か固化したり、取扱い中の容器に強固に
付着して、機器、容器の清掃に困難を来たす。従って処
理される金属微粉末の量と平均粒径に応して投入すべき
燐酸量を厳密に規定し、更にこの燐酸を溶解すべきアル
コール溶剤の量も、燐酸を均一分散させるために必要な
最小限度に制限することが重要である。
If phosphoric acid is in excess relative to the metal powder, the residual phosphoric acid in the treatment solution will react with the alcohol solvent during the drying process after coating, resulting in esterification, which will have an adhesive effect and cause the metal to A layer of fine powder may solidify or adhere firmly to containers being handled, making cleaning of equipment and containers difficult. Therefore, the amount of phosphoric acid to be added must be strictly defined according to the amount of fine metal powder to be treated and the average particle size, and the amount of alcohol solvent to dissolve this phosphoric acid must also be determined according to the amount necessary to uniformly disperse the phosphoric acid. It is important to limit it to a minimum.

一般に燐酸は、金属粉末の平均粒径10ミクロン前後で
、金属微粉末重量に対し、燐酸重量は0.1〜5.0%
の範囲で最良の耐酸化膜が得られる。金属微粉末が、粒
径1ミクロン以下の超微粉末に近づく程、燐酸重量割合
を増やし、50%に近づけるのがよい。
Generally, the average particle size of the metal powder is around 10 microns, and the weight of phosphoric acid is 0.1 to 5.0% based on the weight of the fine metal powder.
The best oxidation-resistant film can be obtained within this range. As the metal fine powder approaches ultrafine powder with a particle size of 1 micron or less, the phosphoric acid weight percentage should be increased to approach 50%.

これによって燐酸のエステル化に伴なうトラブルは回避
でき、乾燥上りではサラサラした極めて流動性が良い許
りでなく、単分子層に近い燐酸系金属化合物を金属微粉
末の表面に形成することに留めることが出来、磁気特性
を向上できる。
This avoids the troubles associated with esterification of phosphoric acid, and instead of having extremely smooth and fluid properties after drying, a phosphoric acid-based metal compound close to a monomolecular layer is formed on the surface of the fine metal powder. It can be held in place and the magnetic properties can be improved.

本発明の処理方法によって形成された金属微粉末の表面
皮膜は極めて薄く、しかも微量であるから、この金属微
粉末を加圧成形後、焼結する場合、本焼結後に得られる
焼結晶の諸特性に大きな影響を及ぼす虞れはない。
Since the surface film of the fine metal powder formed by the treatment method of the present invention is extremely thin and in a small amount, when this fine metal powder is pressure-molded and then sintered, various types of sintered crystals obtained after main sintering are required. There is no possibility that the characteristics will be significantly affected.

又、金属粒は微粉化できるから、焼結温度も従来温度よ
りも100〜200℃の低い温度で焼結可能になり、熱
エネルギーの節約及び焼結炉自体及び炉材の購入費の低
減及び使用機材の長寿命化が画れて多くの経済効果が期
待出来る。
In addition, since metal particles can be pulverized, sintering can be performed at a temperature 100 to 200°C lower than conventional temperatures, which saves thermal energy and reduces the purchase cost of the sintering furnace itself and furnace materials. Many economic benefits can be expected as the lifespan of the equipment used will be extended.

又、本発明の製法を用いることにより、従来の5ミクロ
ン以上の粒径を用いて製造していた稀土類磁石製品(焼
結型及び樹脂成形型とも)は、今後は1〜3ミクロンの
極微粉末を使用することが出来、成形性の向上はもとよ
り、得られる製品の諸特性の顕著な改良、更には製品の
外観の美麗化など極めて多くの効果をえることができる
Furthermore, by using the manufacturing method of the present invention, rare earth magnet products (both sintered molds and resin molded molds), which were conventionally manufactured using particle sizes of 5 microns or more, will now be manufactured using ultrafine particles of 1 to 3 microns. Powder can be used, and it is possible to obtain many effects such as not only improved moldability but also remarkable improvements in various properties of the resulting product, and furthermore, a beautiful appearance of the product.

尚、本発明の被覆処理法は金属の微粉末の被覆処理法と
して卓効が認められることは上述の通りであるが、一般
の金属材料で板材及び管材に対する被覆処理にも十分に
適用されるものである。
As mentioned above, the coating method of the present invention is highly effective as a coating method for fine metal powder, but it is also fully applicable to coating general metal materials such as plates and pipes. It is something.

(実験例) 以下の表において、試料1〜3は本発明方法によって製
造した金属微粉末である。
(Experimental Example) In the table below, Samples 1 to 3 are fine metal powders produced by the method of the present invention.

試料4〜7は比較例であって、被覆処理は粉砕完了後、
粉砕装置より粉末を取り出し、破砕媒体を脱液後、攪拌
装置に粉体を移し、被覆処理液を新たに投入して被覆処
理を行なったもの。
Samples 4 to 7 are comparative examples, and the coating treatment was performed after the completion of crushing.
The powder is taken out from the crushing device, the crushing media is removed, the powder is transferred to the stirring device, and a coating treatment liquid is added to perform the coating treatment.

(以下余白) 粉砕時間は、試料1〜3では、ボール量3 Kg。(Margin below) For samples 1 to 3, the grinding time was 3 kg for the amount of balls.

試料4〜7ではボール量2 Kgを用いた場合を示す。Samples 4 to 7 show cases where a ball amount of 2 kg is used.

酸化開始温度は、金属微粉末を徐々に加熱した際に、重
量が0.15%増加する重量変化のあった温度である。
The oxidation start temperature is the temperature at which the weight of the fine metal powder increases by 0.15% when the fine metal powder is gradually heated.

試料4の表面処理液は、燐酸とメタノールの混合液を1
週間放置したものである。
The surface treatment solution for sample 4 is a mixture of phosphoric acid and methanol.
It was left alone for a week.

試料5〜7の表面処理液は市販品であって、記号は何れ
も商品名であり、有機系溶液である。
The surface treatment solutions of Samples 5 to 7 are commercially available products, all symbols are trade names, and are organic solutions.

GAFACLM400:燐酸エステル系溶液(東邦化学
工業■製) ZISNET  BN−40:)リアジンチオール(三
協化成(御製) RMIOIA:  (信越化学工業側腹)この表によっ
て明らかなとおり、本発明の金属微粉末は、580℃又
は5900Cまでの高い耐熱性を示した。
GAFACLM400: Phosphate ester solution (manufactured by Toho Chemical Co., Ltd.) ZISNET BN-40:) Riazinethiol (manufactured by Sankyo Kasei Co., Ltd.) RMIOIA: (Shin-Etsu Chemical Co., Ltd. side) As is clear from this table, the metal fines of the present invention The powder showed high heat resistance up to 580°C or 5900C.

(試料1の製造例と測定法) 原子重量%てN d +2F e 78C04B6の組
成を有するNd系稀土類磁石合金原料粉末(ゼネラルモ
ータース社製rMQP−BJ平均粒径25μm)500
grを計量する。
(Manufacturing example and measurement method of sample 1) Nd-based rare earth magnet alloy raw material powder having a composition of N d +2F e 78C04B6 in atomic weight % (rMQP-BJ average particle size 25 μm manufactured by General Motors) 500
Weigh gr.

予め第1図の攪拌槽(1)内に鋼球3Kgと粉砕助剤と
して有機溶剤n−ヘキサン300grとトルエン100
grの混合溶液を投入した上で蓋板(13)をO−リン
グを介して固定密閉する。
In advance, 3 kg of steel balls, 300 gr of organic solvent n-hexane as a grinding aid, and 100 gr of toluene were placed in the stirring tank (1) shown in Figure 1.
After adding the mixed solution of gr, the lid plate (13) is fixed and sealed via an O-ring.

次に上記の原料粉末を原料投入口(8)から漏斗を用い
て投入し、この投入口を密閉してからN2ガス(純度9
99%以上)をガス供給管より流量217m1nで注入
、一方の排出口の止栓を開いて槽内の空気のパージを約
5分間行なう。
Next, the above raw material powder is introduced from the raw material inlet (8) using a funnel, this inlet is sealed, and N2 gas (purity 9
99% or more) was injected from the gas supply pipe at a flow rate of 217 m1n, and the stopcock of one outlet was opened to purge the air in the tank for about 5 minutes.

N2ガス置換完了後、攪拌用モーターを始動し、回転数
205 rpmにて9分間湿式粉砕を行ない平均粒径1
1.7μmの微粉砕を得る。
After the N2 gas replacement was completed, the stirring motor was started and wet pulverization was performed for 9 minutes at a rotation speed of 205 rpm until the average particle size was 1.
A fine grind of 1.7 μm is obtained.

この微粉砕以前に燐酸溶液の調整を行なう。Before this fine pulverization, the phosphoric acid solution is adjusted.

即ちオルソ燐酸4grを計量し、メタノール40grに
溶解するためスターラーで約5分間攪拌して均一な燐酸
アルコール溶液を作製する。この表面処理液を処理液タ
ンク(6)に入れて、同じくN2置換を行なった上で、
上記の粉砕完了時に合せて、注入バルブ(64)を開い
てN2圧(16Kg/cm2)をかけなから数秒以内に
注入を完了する。一方攪拌棒の回転は粉砕に引続き同一
回転数(205rpm)で回転して処理液を攪拌分散さ
せ、30秒後回転を停止し、被覆処理を完了する。
That is, 4g of orthophosphoric acid is weighed and dissolved in 40g of methanol and stirred for about 5 minutes using a stirrer to prepare a uniform phosphoric acid alcohol solution. After putting this surface treatment liquid into the treatment liquid tank (6) and performing the same N2 substitution,
When the above-mentioned pulverization is completed, the injection valve (64) is opened to apply N2 pressure (16 kg/cm2), and the injection is completed within a few seconds. On the other hand, the stirring rod is rotated at the same rotation speed (205 rpm) following the crushing to stir and disperse the treatment liquid, and after 30 seconds, the rotation is stopped to complete the coating treatment.

次ぎに開蓋し、蓋板及び撹拌棒を一緒に槽外に取出して
から被覆処理済み微粉末、鋼球及び液体全部をステンレ
ス金網を取り付けた受は容器に投入し、先ず鋼球を金網
こと取り除いてから、受容器中に沈澱した微粉末を乾燥
用バットに移し、上澄液を除去した後、排気ファン付乾
燥器に装入、50〜70’Cで約3時間加熱乾燥すると
、黒紫色を呈する。Nd系稀土類磁石合金微粉末(試料
1)が得られる。
Next, open the lid, take out the lid plate and stirring rod together from the tank, and then put the coated fine powder, steel balls, and liquid into a container with a stainless steel wire mesh attached, and first put the steel balls in the wire mesh. After removing the powder, the fine powder precipitated in the receiver was transferred to a drying vat, and after removing the supernatant liquid, it was placed in a dryer equipped with an exhaust fan and dried by heating at 50 to 70'C for about 3 hours. Appears purple. Nd-based rare earth magnet alloy fine powder (Sample 1) is obtained.

なお、本実施例の条件では、鋼球、容器なとへの微粉末
の付着は少なく、また被覆処理済み微粉末同志の付着現
象は殆んと見られず、サラサラした極めて流動性の自好
な状態を示したへこの微粉末を30mg精密天秤で計量
し7、白金製カップに入れてから島津製作所製TG計に
かけて流量40 ml/ minの空気を流しながら室
温20℃から650℃まで5°C/minで加熱して試
料の重量変化を自動記録する。
Note that under the conditions of this example, there was little adhesion of the fine powder to the steel balls and containers, and there was almost no adhesion phenomenon of the coated fine powder to each other. Weighed 30 mg of the fine powder from the heel with a precision balance 7, put it in a platinum cup, put it into a Shimadzu TG meter, and heated it at a temperature of 5° from room temperature 20°C to 650°C while flowing air at a flow rate of 40 ml/min. The sample is heated at C/min and the change in weight of the sample is automatically recorded.

この記録データより0.15%の酸化増量を示す温度を
酸化開始温度と規定し、上記試料の場合は580 ’C
を示した。即ち本試料では大気中で580℃まで加熱さ
れても殆んと酸化されないことを示すものである。
Based on this recorded data, the temperature at which 0.15% of oxidation weight increases is defined as the oxidation start temperature, and in the case of the above sample, it is 580'C.
showed that. This shows that this sample is hardly oxidized even when heated to 580° C. in the atmosphere.

(試料2の製造例) 試料1.3〜7までか射出成形型プラマグコンバウント
用として、平均粒子径を11〜12μmに調整しである
か、試料2は圧縮成形用として14μm前後に調整する
ために、主な条件として粉砕時間を6分とし、表面処理
液も燐酸25g1メタノ一ル25grとした。その他の
操作手順は試料1と全く同しである。得られた被覆処理
済み微粉末(試料2)は黒紫色を呈し、耐酸什性↓、5
80’(’:f;−示1.て一滞動性t1白ご付着現象
も見られず、良好な結果か得られた。
(Manufacturing example of sample 2) For samples 1.3 to 7, the average particle diameter is adjusted to 11 to 12 μm for injection molding plastic mag combination, or for sample 2, the average particle size is adjusted to around 14 μm for compression molding. Therefore, the main conditions were that the grinding time was 6 minutes, and the surface treatment liquid was also 25g of phosphoric acid and 25g of methanol. Other operating procedures are exactly the same as Sample 1. The coated fine powder (sample 2) obtained had a blackish-purple color and had acid resistance of ↓, 5.
80'(':f;-1.1), no stagnation phenomenon was observed, and good results were obtained.

(試料4の製造例) 原料粉末は上記と同じで、試料重量250grとし、射
出成形用とし平均粒径を11〜12μmに抑えるため粉
砕時間を8分に調整した。
(Manufacturing Example of Sample 4) The raw material powder was the same as above, the sample weight was 250 gr, and the grinding time was adjusted to 8 minutes in order to suppress the average particle size to 11 to 12 μm for injection molding.

そのため操作手順は試料1と同じであるが、表面処理液
としては予めオルソ燐酸を加熱して約18%脱水し、冷
却後メタノール溶液中に入れ、スターシーで30分間攪
拌溶解し、更にエステル化を進めるため1週間放置して
、原液(燐酸5%)を作製した。微粉砕直前に原液20
gを計量し、これをメタノール400grで稀釈し、ス
ターシーで約5分間攪拌後、処理液タンクに入れ、N2
置換を行なう。その他の操作手順は試料1と同じである
。得られた表面処理済み微粉末(試料4)は美麗な黄金
色を呈するが耐酸化性は320°Cまでであり、燐酸量
を増やしてもこの耐酸化温度は改善されず、付着現象が
増大し、取扱上からも良好な結果が得られない。
Therefore, the operating procedure is the same as sample 1, but as a surface treatment liquid, orthophosphoric acid is heated in advance to dehydrate it by about 18%, and after cooling, it is poured into a methanol solution, stirred and dissolved in Starcy for 30 minutes, and further esterified. In order to proceed with the process, a stock solution (5% phosphoric acid) was prepared by leaving it for one week. 20% of the stock solution just before pulverization
g, diluted with 400g of methanol, stirred with Starcy for about 5 minutes, put it into a processing liquid tank, and poured it with N2
Perform a replacement. Other operating procedures are the same as for sample 1. The obtained surface-treated fine powder (sample 4) exhibits a beautiful golden color, but its oxidation resistance is up to 320°C, and even if the amount of phosphoric acid is increased, this oxidation resistance temperature does not improve and the adhesion phenomenon increases. However, good results cannot be obtained from the handling point of view.

この傾向は他の比較例でも同じ傾向を示した。This tendency was also observed in other comparative examples.

即ち比較例5〜7は何れも有機系物質を含む薄膜を形成
するもので、表面処理液(特に主剤)の量を増しても、
上述のように耐熱性は向上せず、付着性のみで増大して
期待した効果は得られなかった。
That is, Comparative Examples 5 to 7 all form thin films containing organic substances, and even when the amount of surface treatment liquid (especially the main agent) is increased,
As mentioned above, the heat resistance did not improve, only the adhesion increased, and the expected effect was not obtained.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施に使用する被覆処理装置の正面図
である。 (1)・・・攪拌槽    (2)・・・攪拌体(4)
・・・不活性ガス供給管 (6)・・・処理液タンク
FIG. 1 is a front view of a coating processing apparatus used in carrying out the present invention. (1)... Stirring tank (2)... Stirring body (4)
... Inert gas supply pipe (6) ... Processing liquid tank

Claims (1)

【特許請求の範囲】 1 有機基を含まない無機燐酸化合物の薄膜によって表
面を一様に覆った金属微粉末。 2 不活性雰囲気中で金属粒を粉砕して金属微粉末を作
り、該金属微粉末を大気中へ取り出す前に、不活性雰囲
気中にて、燐酸と有機溶媒との混合液であって有機燐酸
化合物が殆んど発生していない状態において、これを金
属微粉末へ接触させ、金属粒の破砕によって得られた活
性度の高い金属表面を無機燐酸金属化合物の薄膜によっ
て覆うことを特徴とする金属微粉末の製法。
[Claims] 1. Fine metal powder whose surface is uniformly covered with a thin film of an inorganic phosphoric acid compound containing no organic groups. 2. Fine metal powder is produced by crushing metal particles in an inert atmosphere, and before the fine metal powder is taken out into the atmosphere, a mixture of phosphoric acid and an organic solvent is prepared, which is an organic phosphoric acid, in an inert atmosphere. A metal characterized by contacting fine metal powder in a state where almost no compound is generated, and covering the highly active metal surface obtained by crushing the metal particles with a thin film of an inorganic phosphate metal compound. Manufacturing method of fine powder.
JP2127993A 1990-05-16 1990-05-16 Production method of heat-resistant metal fine powder Expired - Fee Related JP2602979B2 (en)

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Related Child Applications (1)

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JP6317969A Division JPH07278602A (en) 1994-12-21 1994-12-21 High heat resistant metal fine powder

Publications (2)

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JPH0421702A true JPH0421702A (en) 1992-01-24
JP2602979B2 JP2602979B2 (en) 1997-04-23

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5658987A (en) * 1993-03-30 1997-08-19 Nippon Zeon Co., Ltd. Rubber composition
JP2009523907A (en) * 2006-01-12 2009-06-25 ヘガネス・コーポレーシヨン Metallurgical powder composition and method for producing solidified product produced therefrom

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3882545B2 (en) * 2000-11-13 2007-02-21 住友金属鉱山株式会社 High weather-resistant magnet powder and magnet using the same

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60154503A (en) * 1984-01-24 1985-08-14 Ube Ind Ltd Method for stabilizing magnetic metal powder
JPS63134602A (en) * 1986-03-29 1988-06-07 Shin Etsu Chem Co Ltd Fine metallic powder
JPH01234502A (en) * 1988-03-11 1989-09-19 Hirata Michitoshi Fine metal powder and production thereof
JPH0270003A (en) * 1988-07-01 1990-03-08 Tosoh Corp Method for treating ferromagnetic iron powder

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60154503A (en) * 1984-01-24 1985-08-14 Ube Ind Ltd Method for stabilizing magnetic metal powder
JPS63134602A (en) * 1986-03-29 1988-06-07 Shin Etsu Chem Co Ltd Fine metallic powder
JPH01234502A (en) * 1988-03-11 1989-09-19 Hirata Michitoshi Fine metal powder and production thereof
JPH0270003A (en) * 1988-07-01 1990-03-08 Tosoh Corp Method for treating ferromagnetic iron powder

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5658987A (en) * 1993-03-30 1997-08-19 Nippon Zeon Co., Ltd. Rubber composition
JP2009523907A (en) * 2006-01-12 2009-06-25 ヘガネス・コーポレーシヨン Metallurgical powder composition and method for producing solidified product produced therefrom
US8703046B2 (en) 2006-01-12 2014-04-22 Hoeganaes Corporation Methods for preparing metallurgical powder compositions and compacted articles made from the same

Also Published As

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