JPS58110433A - Stabilizing method for needlelike magnetic metallic powder - Google Patents
Stabilizing method for needlelike magnetic metallic powderInfo
- Publication number
- JPS58110433A JPS58110433A JP56208533A JP20853381A JPS58110433A JP S58110433 A JPS58110433 A JP S58110433A JP 56208533 A JP56208533 A JP 56208533A JP 20853381 A JP20853381 A JP 20853381A JP S58110433 A JPS58110433 A JP S58110433A
- Authority
- JP
- Japan
- Prior art keywords
- metal powder
- mixture
- magnetic
- metallic powder
- air
- 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
Landscapes
- Compounds Of Iron (AREA)
- Hard Magnetic Materials (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は磁気テープ勢の磁気記録媒体に使用される針状
磁性金属粉の安定化処理法に係わる。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for stabilizing acicular magnetic metal powder used in magnetic recording media such as magnetic tape.
高出力及び高書度記鋒用の磁気記録媒体の磁性材料とし
ては、飽和磁化が大で、高抗磁力を有することも要求さ
れる。Magnetic materials for magnetic recording media for high output and high recording speed are also required to have high saturation magnetization and high coercive force.
このような磁性材料としては、一般に針状の磁性金属粉
が知られている。この針状磁性金属粉は、含水酸化鉄(
Pe00H)、酸化鉄、またはスパルト含有酸化鉄等を
加熱脱水、遺元処履して得る。そしてこのようにして得
た磁性金属粉は大気中での酸化、燃焼部に対す1化学的
安定性及び防錆性勢の耐腐蝕性を付与するためKその表
面Kml化膜、すなわち不働態酸化物膜を形成する表面
安定化の処理がなされる。Acicular magnetic metal powder is generally known as such a magnetic material. This acicular magnetic metal powder is made of hydrated iron oxide (
Pe00H), iron oxide, or spult-containing iron oxide, etc., are heated, dehydrated, and subjected to an aqueous treatment. The magnetic metal powder obtained in this way has a Kml film on its surface, that is, a passive oxidation film, in order to provide chemical stability against oxidation and combustion in the atmosphere and corrosion resistance with rust prevention properties. A surface stabilization treatment is performed to form a film.
このような釘状磁性金属粉の安定化処理法としての代表
的な方法としては、トルエン等の有機溶媒に磁性粉を浸
漬した後その有機溶媒を徐々に蒸発させ、その過程で磁
性粉の表面に酸化膜を形成する方法がある。ところが、
このような方法による場合、磁性金属粉の化学的安定性
はほぼ満足され、且つこの磁性金属粉の磁気媒体におけ
る磁性塗膜中での分散性及び配向性の点では満足し得る
ものであるが、その安定化処理すなわち酸化膜形成Kl
!する時間が長く、量産的でないという欠点がある。A typical method for stabilizing such nail-shaped magnetic metal powder is to immerse the magnetic powder in an organic solvent such as toluene and then gradually evaporate the organic solvent. There is a method of forming an oxide film. However,
When such a method is used, the chemical stability of the magnetic metal powder is almost satisfied, and the dispersibility and orientation of the magnetic metal powder in the magnetic coating film in the magnetic medium are satisfactory. , its stabilization treatment, that is, oxide film formation Kl
! The drawback is that it takes a long time to complete and is not suitable for mass production.
また、他の方法として磁性金属粉を有機溶媒中に懸濁し
、これKwR素を含むガス例えば空気を吹き込むことに
よって磁性金属粉の表面に酸化膜を形成するいわゆる液
相中酸化処理法がある。この方法による場合、短時間で
安全な酸化処理を行えるという点で工業的な利点を有す
る。ところがこの方法による場合、磁性金属粉の化学的
安定性及び耐腐蝕性に閤して充分満足できるものではな
く、さらに磁性粉の、磁気媒体における磁性塗膜中での
分散性及び配向性に劣り、このことは磁気媒体において
重大な欠点である。Another method is a so-called liquid phase oxidation treatment method in which magnetic metal powder is suspended in an organic solvent and a gas containing KwR elements, such as air, is blown into the suspension to form an oxide film on the surface of the magnetic metal powder. This method has an industrial advantage in that safe oxidation treatment can be performed in a short time. However, when using this method, the chemical stability and corrosion resistance of the magnetic metal powder are not fully satisfactory, and furthermore, the dispersibility and orientation of the magnetic powder in the magnetic coating film in the magnetic medium are poor. , this is a serious drawback in magnetic media.
本発明はこのような賭欠点を改譬し、磁性金属粉の化学
的安定性を満足し、さらに磁気媒体の磁性塗膜中Ksi
−ける分散性及び配向性に優れ、さらkその安定化fi
llKおける磁性金属粉の乾燥過程での発熱発火がなく
、短時間に多量の磁性金属粉の表面酸化処理による安定
化処理な行うことがで参るようにした針状磁性金属粉の
安定化処理法を提供するものである。The present invention corrects such drawbacks, satisfies the chemical stability of magnetic metal powder, and furthermore satisfies the chemical stability of magnetic metal powder, and further improves the Ksi
- Excellent dispersibility and orientation, and its stabilization properties
A stabilization treatment method for acicular magnetic metal powder that does not generate heat and ignite during the drying process of magnetic metal powder in LLK, and allows stabilization treatment by surface oxidation treatment of a large amount of magnetic metal powder in a short time. It provides:
すなわち、本発明においては、液相中酸化丸環法におい
て有機溶媒中KS濁した金属粉の乾燥過程で有機**が
蒸発し、酸素含有ガスによって金属表面が酸化されると
會、酸化発熱が蓄熱しこれKよって金属粉の発火燃焼が
生じる仁と、そしくこの発火現象は、4IKII&通金
属粉が大量であるほど著しいことに対処して“、有機溶
媒中に懸濁した金属粉に酸素含有ガスを強制的に大量に
送風して、蓄熱する酸化発熱を強制的に放熱し、同時に
有機溶媒の蒸発速度を早め短時間に大量の針状磁性金属
粉に対する表面酸化による安定化処理を可能にするもの
である。すなわちこの本発明方V&においては金属粉の
乾燥過程に始めに有機#l!媒の蒸発に伴う吸熱過程が
あり、次に強制送jLKよる酸化熱の強制放熱過程があ
って、いずれにおいても金属粉の蓄熱、発火現象は回避
された。またこのようKして得た安定化処理のなされた
針状磁性金属粉の分散性及び配向性が満足できるもので
あることも確められた。すなわち、この分散性及び配向
性は金属粉の酸化物層の表両構造によって影響されるも
のであるが、本発明方法による場合、この点満足で赦る
ものであることが明らかとなった。That is, in the present invention, in the liquid phase oxidation round ring method, organic ** evaporates during the drying process of KS-turbid metal powder in an organic solvent, and when the metal surface is oxidized by an oxygen-containing gas, oxidation heat is generated. The metal powder accumulates heat and ignites and burns, and this ignition phenomenon becomes more pronounced as the amount of metal powder increases. By forcibly blowing a large amount of the contained gas, the accumulated oxidation heat is forcibly radiated, and at the same time, the evaporation rate of the organic solvent is increased, making it possible to stabilize a large amount of acicular magnetic metal powder by surface oxidation in a short time. In other words, in method V& of the present invention, in the drying process of metal powder, there is first an endothermic process accompanying the evaporation of the organic #l! medium, and then there is a forced heat dissipation process of oxidation heat by forced feed jLK. In both cases, heat accumulation and ignition phenomena of the metal powder were avoided.It was also confirmed that the dispersibility and orientation of the stabilized acicular magnetic metal powder obtained by K in this way were satisfactory. In other words, the dispersibility and orientation are influenced by the surface structure of the oxide layer of the metal powder, but in the case of the method of the present invention, this point is satisfied and can be tolerated. It became clear.
第1図は本発明による安定化処理法を実施する装置の一
例を示す、この例K>いては例えばステンレスよりなる
一応容器(1)内に安定化処理を施さんとする乾式還元
後の針状磁性金属粉を有機溶媒 中に浸漬した混合物
(2)を配置する。(3)はガス分散板で容器(1)の
例えば金属粉と有機溶媒の混合物(2)の下方より矢印
l及びbK示すように酸素を含むガスをガス分散板(3
)を通じて混合物(2)中に分散して強制的に送風する
。一方容器(1)の上方には金属フィルター(4)が配
置され、容器(1)の上方より矢印cK示すように排気
がなされ、tた容器(1)Kはフィルター(4)の目づ
まりを防止するN雪tIス或いは空気等の逆流用ガスの
供給口(5)を設ける。(6)はその調整弁例えば電気
弁を示す、このような装置によって酸素含有ガスが処理
すべき金属11に均一に送風されるようKする。このよ
うkし【処理すべぎ金属粉が容器(1)内において均一
に乾燥されるようKなされ、局部的に酸化発熱は蓄熱さ
れることがないようにされる。こζに有機溶媒への混合
物への混合金属粉の状態は、微粉末状態、ベレット状W
A′jtGいはあまり大きくない塊状勢いずれの状態を
もとり得る。FIG. 1 shows an example of an apparatus for carrying out the stabilization treatment method according to the present invention. A mixture (2) of magnetic metal powder immersed in an organic solvent is placed. (3) is a gas dispersion plate that distributes oxygen-containing gas from below the mixture (2) of metal powder and organic solvent in the container (1) as shown by arrows l and bK.
) and forcefully blow the air through the mixture (2). On the other hand, a metal filter (4) is placed above the container (1), and exhaust air is provided from above the container (1) as shown by the arrow cK.The container (1)K prevents the filter (4) from clogging. A supply port (5) for backflow gas such as nitrogen gas or air is provided. (6) indicates the regulating valve, for example, an electric valve, so that the oxygen-containing gas is uniformly blown onto the metal 11 to be treated by such a device. In this way, the metal powder to be treated is dried uniformly in the container (1), and heat generated by oxidation is prevented from being locally accumulated. The state of the mixed metal powder in the organic solvent is fine powder state, pellet shape W
A'jtG can take on any form of not-so-large clumps.
また金属粉を浸漬する有機溶媒としては、水との相溶性
の高い溶剤、或いは極性基を有する溶剤では空気中の水
分が徐kK溶は込み金属粉の酸化が促進され、その制御
が難しくなるのでこの有機溶媒としては水との相溶性が
低く、しか4&性基なもたない溶剤より選ばれることが
*tLい、このよ5な溶媒としては例えばペンタン、ヘ
キタン、ヘプタン、オタタン勢のメタン系縦化水1g或
いはベンゼン、トリコン、キシレン勢の芳香族炭化水素
等より選ばれる。In addition, if the organic solvent in which the metal powder is immersed is one that is highly compatible with water or has a polar group, moisture in the air will slowly penetrate into the metal powder and accelerate oxidation of the metal powder, making it difficult to control. Therefore, the organic solvent should be selected from solvents that have low compatibility with water and do not have any functional groups. Examples of such organic solvents include pentane, hexane, heptane, and methane of the Otatan group. It is selected from 1 g of verticalized water or aromatic hydrocarbons such as benzene, tricone, and xylene.
また酸素を含むガスとしては、酸素濃度が30重量−以
下の酸素を含有する不活性ガスの混合ガスが用いられる
ことが望首しく、このようなガスとしては空気が用いら
れ得るものであり、この場合、経済性に優れまたその酸
素濃度は最適の値を有している。尚、酸素Stが30重
量−を越える高11&となると金属粉の酸化反応が急激
となって、その酸化発熱によって発火の恐れが生じるか
或いは発火に至らすともこの急激な酸化のために金属粉
の磁気特性を著しく劣化させる仁とKなる。tた逆に酸
化濃度が極端に低い場合は、金meの表面酸化安定化処
理に要する時間が長時間になって工業的に望ましくない
状lIKなり、これらから駿素を含むガスとしては空気
が最適ガスである。Further, as the oxygen-containing gas, it is desirable to use a mixed gas of an inert gas containing oxygen with an oxygen concentration of 30% by weight or less, and air can be used as such a gas, In this case, it is economical and the oxygen concentration has an optimum value. Furthermore, when the oxygen St reaches a high level of 11& exceeding 30% by weight, the oxidation reaction of the metal powder becomes rapid, and there is a risk of ignition due to the heat generated by the oxidation. K and K significantly deteriorate the magnetic properties of the metal. On the other hand, if the oxidation concentration is extremely low, the time required for the surface oxidation stabilization treatment of gold metal becomes long, resulting in industrially undesirable lIK. It is the optimal gas.
また、このガスの流量は、処理すべき金属粉の量によっ
て異らしめる必要があるが、この流量は金属粉の酸化発
熱が蓄熱しないような放熱に必要な流量に選定される。Further, the flow rate of this gas needs to be varied depending on the amount of metal powder to be treated, but this flow rate is selected to be a flow rate necessary for heat dissipation so that the heat generated by oxidation of the metal powder does not accumulate.
また1表面酸化処理の処理温度はso″C以下の室温程
度に遍ばれることが望鵞しい、すなわちこの処理温度が
極端に低い場合には金属粉が浸漬された有機5iIII
/)、ii発速度が遅くなり通ぎて、その金属粉の表面
酸化処理が長時間を要し、実用性に欠ける。一方、処理
温度があtり高くなると有機溶媒の蒸発速度が早くなり
過ぎ、゛金属粉に急激゛′な酸化反応が生じ、その酸化
熱による発火が生じたり、或いは発火KMらずとも急激
酸化のため金属粉の龜気特性を著しく劣化させる。これ
らのことがら蟻み、さらに’i金性及び経済性の上から
その処理th!縦は室温に選定されることが望ましい。In addition, it is highly desirable that the treatment temperature for the surface oxidation treatment be around room temperature below so''C.In other words, if this treatment temperature is extremely low, the metal powder is immersed in the organic 5iIII.
/), ii) The firing rate becomes too slow, and the surface oxidation treatment of the metal powder takes a long time, making it impractical. On the other hand, if the processing temperature is too high, the evaporation rate of the organic solvent becomes too fast, and a rapid oxidation reaction occurs in the metal powder, causing ignition due to the oxidation heat, or rapid oxidation even without ignition KM. Therefore, the air quality of the metal powder is significantly deteriorated. In addition to these considerations, it is also important to consider the process from the viewpoint of efficiency and economy! It is desirable that the vertical position be selected at room temperature.
そして、表面酸化処理の処理時間は、処理温度及び酸素
濃度に大きく作用されるが実用性から鑑みて5〜24時
間に選ばれるのがIIましい。The treatment time of the surface oxidation treatment is greatly affected by the treatment temperature and oxygen concentration, but from the viewpoint of practicality, it is preferably selected to be 5 to 24 hours.
また、本発明において使用対象とする釘状磁性金属粉に
は酸化安定化をいっそう高めるためK。Additionally, K is added to the nail-shaped magnetic metal powder used in the present invention in order to further enhance oxidation stabilization.
その還元処理前に、クロム、アル建ニウム、チタン等を
添加しておくことができる。さらにシンタリングの防止
のために予めシリコン油やV9ンカップリング剤で処理
しておくこともできる。Before the reduction treatment, chromium, aluminum, titanium, etc. can be added. Furthermore, in order to prevent sintering, it can be treated with silicone oil or a V9 coupling agent in advance.
次に本発明の実施例を挙げる。Next, examples of the present invention will be given.
実施例1
N&が10原子慢、別が5原子−含有する針状のα−F
BOsf、21/分の水1[量をもって3110”Cで
3時間還元した0次いで、その雰囲気を10011N8
雰囲気kW換し、この状態で富温壕で放冷した。そして
、この放冷後、還元された金属粉をトルエンに注入浸漬
して次いでこのトルエンの浸漬による混合物を、第1図
で説明した表面酸化処理のための反応容器0)内に配置
した。この場合、その混合物中の処理されるべき金属粉
は、約sog。Example 1 Acicular α-F containing 10 atoms of N& and 5 atoms of another
BOsf, 21/min water 1 [0 which was reduced at 3110''C for 3 hours, then the atmosphere was reduced to 10011N8
The atmosphere was changed to kW and left to cool in this condition in a Tomion trench. After cooling, the reduced metal powder was injected into toluene and immersed, and the mixture obtained by immersion in toluene was placed in the reaction vessel 0) for surface oxidation treatment described in FIG. In this case, the metal powder to be treated in the mixture is approximately sog.
トルエンが70gで全体の重量が120gであった。The total weight was 120 g with 70 g of toluene.
反応容器(1)中の混合物(2)の層高は約sasであ
った。The bed height of the mixture (2) in the reaction vessel (1) was approximately sas.
次にこの状態で反応容器(1)内に空気をその下方より
送風し、金属粉に対する表面酸化安定化処理を施した。Next, in this state, air was blown into the reaction vessel (1) from below to perform a surface oxidation stabilization treatment on the metal powder.
この処理は空気流量7慮/分とし、室温で24時間の処
IIKより(行った。向、仁の場合、この処理過1での
発熱は全くなかった。This treatment was carried out at room temperature for 24 hours at an air flow rate of 7 min/min. In the case of Mukai and Jin, no heat generation occurred during this treatment.
実施例2
実施例1で使用したとPIlltり金属粉を用意し、こ
れの約180 gをトルエン約230 i K注入浸漬
した混合物、すなわち約3sO厘の混合物を第111で
説明した反応容器(1)内に配し、反応容器(1)内に
その下方より空気を送風して金属粉の表面酸化安定化処
理を施した。この場合の反応容II(11中の混合物(
2)の層高は約20aaであった。そしてその安定化処
理は、空気流量71/分の送風によって室温で27時間
の処理によって行った。この場合においてもこの処理過
程での発熱は全くなかった。Example 2 The PIllt metal powder used in Example 1 was prepared, and about 180 g of it was injected and immersed in about 230 iK of toluene, and a mixture of about 3 sO was added to the reaction vessel (1 ), and air was blown into the reaction vessel (1) from below to perform surface oxidation stabilization treatment on the metal powder. In this case reaction volume II (mixture in 11 (
The layer height of 2) was about 20 aa. The stabilization treatment was carried out at room temperature for 27 hours by blowing air at a flow rate of 71/min. In this case as well, there was no heat generation at all during this treatment process.
実施例3
実施例1で使用したと同様の金属粉を用意し、これの約
1.0 kgをトルエン$1!JIJkgK注入浸漬し
た混合物、すなわち約2.6に@の混合物を第1図で説
明した反応容器(里)内に配し、反応容器(1)内に七
の下方より空気を送風して金属粉の表面酸化安定化処理
を施した。この場合の反応容器(1)中の混合物(2)
の層高は約4051であった。そしてその安定化処理は
、空気流量751/分の送風によって室温で24時間の
処理によって行った。仁の場合においてもこの処理過程
での発熱は全くなかった。Example 3 Prepare metal powder similar to that used in Example 1, and add about 1.0 kg of it to toluene for $1! The JIJkgK injected and immersed mixture, that is, the mixture of approximately 2.6% and 2%, was placed in the reaction vessel (ri) explained in Fig. 1, and air was blown into the reaction vessel (1) from below to remove the metal powder. surface oxidation stabilization treatment. The mixture (2) in the reaction vessel (1) in this case
The layer height was approximately 4,051 cm. The stabilization treatment was carried out at room temperature for 24 hours using an air flow rate of 751/min. Even in the case of keratin, there was no heat generation at all during this treatment process.
実施例4
Coが15Ji子嘔、Niが2m子−18i カ2 x
子−含有する釘状のα−F@g0gを、2慮/分の水嵩
流量をもつc480℃で3時間還元した。次いで、その
雰囲気を1001N11雰囲気に置換し、この状態で寵
温壕で放冷した。そして、この放冷後、還元された金属
粉をトルエンに注入浸漬して次いでこのトルエンの浸漬
による混合物を、第1図で説明した表面酸化処理のため
の反応容器(1)内に配置した。Example 4 Co is 15Ji, Ni is 2m and 18i.
The nail-shaped α-F@g0g containing fertilized particles was reduced for 3 hours at 480° C. with a water bulk flow rate of 2 min/min. Next, the atmosphere was replaced with a 1001N11 atmosphere, and in this state, it was allowed to cool in a temperature trench. After cooling, the reduced metal powder was injected into toluene and immersed, and the mixture obtained by immersion in toluene was placed in the reaction vessel (1) for surface oxidation treatment described in FIG. 1.
この場合、その混合物中の処理されるべt金属粉は、約
7051.)ルエンが1101で全体の重量が180
gであった0反応容器(1)中や混合物(2)の層高は
約8clIであった。次にこの状態で反応容器(1)内
に!2!気をその下方より送風し、金属粉に対する表面
酸化安定化処理を施した。この処理は空気流量71/分
とし1wi温で24時間の処理によって行った。内、こ
の場合、この処理遥1での発熱は全くなかった。In this case, the treated metal powder in the mixture is about 7051. ) Luene is 1101 and the total weight is 180
The bed height in the reaction vessel (1) and in the mixture (2) was about 8 clI. Next, in this state, enter the reaction container (1)! 2! Air was blown from below to perform surface oxidation stabilization treatment on the metal powder. This treatment was carried out at an air flow rate of 71/min and at 1wi temperature for 24 hours. Of these, in this case, there was no heat generation at all in this treatment Haruka 1.
さらに本発明と比較されるべ数比較例を挙げる。Furthermore, a comparative example of a power number comparison with the present invention will be given.
比較例1
実施例1で使用したと同様の金属粉を用意し、その50
厘をトルエンIt中に浸漬した混合物を攪拌しながらこ
の混合物に空気を417分の流量をもって吹き込んで室
温で9時間の駿化処理による表面安定化処理を行った。Comparative Example 1 The same metal powder as used in Example 1 was prepared, and 50
A surface stabilization treatment was carried out by blowing air into the mixture at a flow rate of 417 min at room temperature for 9 hours while stirring the mixture in which the toluene was immersed in toluene.
比較例2
実施例1で使用したと同様の金属粉を用意し、その約5
0gをトルエン約701gで浸漬した混合物的B!Og
を空気中においてそのトルエンを室温におい【蒸発させ
、約S日間風乾して表面酸化安定化処理を行った。Comparative Example 2 The same metal powder as used in Example 1 was prepared, and about 5
Mixture B where 0g is immersed in about 701g of toluene! Og
The toluene was evaporated in the air at room temperature, and the surface was oxidized and stabilized by air drying for about S days.
比較例3
実施例4で使用した金属粉約sOgをトルエン約II中
に浸漬した混食物vm拌しながら、この混合物に空気を
約41/分の流量をもって吹き込み室温で9時間の表面
酸化安定化処理を行った。Comparative Example 3 A mixed food in which about sOg of the metal powder used in Example 4 was immersed in about II toluene vm While stirring, air was blown into this mixture at a flow rate of about 41/min to stabilize the surface by oxidation at room temperature for 9 hours. processed.
これら本発明による実施例1〜4、さらに比較例1〜3
によって夫々安定化処理の施された金属粉の各特性すな
わち磁化量σ6、角形比胞、抗磁力Hc、金属粉の比表
面積、さらにこの金属粉によって構成された磁性層の配
向シー)!性、特に抗磁力Hc 、角形比H@、残留磁
束fi度Brの各−j定結果を第2図に示す、これKよ
り明らかなように1本発明方法によるときは頬時間の処
理で優れた特性が得られることがわかる。These Examples 1 to 4 according to the present invention, and further Comparative Examples 1 to 3
Characteristics of the metal powder that have been stabilized by: magnetization amount σ6, square ratio, coercive force Hc, specific surface area of the metal powder, and orientation sheet of the magnetic layer composed of this metal powder)! Figure 2 shows the -j constant results for coercive force Hc, squareness ratio H@, and residual magnetic flux degree Br. It can be seen that similar characteristics can be obtained.
また、本発明による処理がなされた磁性傘j4粉は、経
時変化が少なく安定性に優れていることが確められた。In addition, it was confirmed that the magnetic umbrella j4 powder treated according to the present invention has excellent stability with little change over time.
すなわち実施例1及び比較例2によって夫々処理した磁
性金属粉1gを、100111の蒸溜水圧浸し、その後
r別して取出し空気中で常温にて乾燥して錆の有無を目
視輌察したところ実施例1のそれは、錆が認められず、
磁化量σSは、147emu/Ifであったに比し、比
較例2のそれは、錆がrI7&察され、磁化量σ易は、
130emu/gに低下した。That is, 1 g of magnetic metal powder treated in Example 1 and Comparative Example 2 was immersed in 100111 distilled water under pressure, then separated, taken out, dried in air at room temperature, and visually inspected for the presence of rust. It has no rust,
The magnetization amount σS was 147 emu/If, whereas in Comparative Example 2, rust was detected, and the magnetization amount σI was 147 emu/If.
It decreased to 130 emu/g.
第1図は本発明による安定化処理法をli!施する装置
の一例の路線的構成図、第!図は安定化処理の施された
各磁性金属粉の特性測定結果のIIj図である。
(1)は反応容器、(2)は磁性金属粉の有機*m混合
物である。FIG. 1 shows the stabilization treatment method according to the present invention! A schematic diagram of an example of the equipment used for this purpose, Part 1! The figure is a IIj diagram of the characteristic measurement results of each magnetic metal powder subjected to stabilization treatment. (1) is a reaction vessel, and (2) is an organic*m mixture of magnetic metal powder.
Claims (1)
合物に酸素を含むガスを送風して上記有機溶媒を強制的
に蒸発させて上記磁性金属粉の表面に酸化膜を形成する
ことを特徴とする針状磁性金属粉の安定化処理法。A gas containing oxygen is blown through a mixture of dry-reduced acicular magnetic metal powder mixed in an organic solvent to forcibly evaporate the organic solvent to form an oxide film on the surface of the magnetic metal powder. Characteristic stabilization treatment method for acicular magnetic metal powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56208533A JPS58110433A (en) | 1981-12-23 | 1981-12-23 | Stabilizing method for needlelike magnetic metallic powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56208533A JPS58110433A (en) | 1981-12-23 | 1981-12-23 | Stabilizing method for needlelike magnetic metallic powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58110433A true JPS58110433A (en) | 1983-07-01 |
| JPH0261419B2 JPH0261419B2 (en) | 1990-12-20 |
Family
ID=16557758
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56208533A Granted JPS58110433A (en) | 1981-12-23 | 1981-12-23 | Stabilizing method for needlelike magnetic metallic powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58110433A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6076105A (en) * | 1983-10-01 | 1985-04-30 | Taiyo Yuden Co Ltd | Iron family nitride magnetic powder |
-
1981
- 1981-12-23 JP JP56208533A patent/JPS58110433A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6076105A (en) * | 1983-10-01 | 1985-04-30 | Taiyo Yuden Co Ltd | Iron family nitride magnetic powder |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0261419B2 (en) | 1990-12-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4318735A (en) | Process for preparing magnetic particles with metallic region therein, and magnetic particles prepared by the process | |
| US4618542A (en) | Magnetic thin film | |
| US4073977A (en) | Stabilization of pyrophoric metal powders with alkylene oxide polymers | |
| EP0305069B1 (en) | A process for producing a ferromagnetic metal powder having an oxidized coating | |
| JPS60128202A (en) | Production of magnetic metallic powder | |
| JPS62112702A (en) | Production of ferromagnetic metallic powder having oxide film | |
| JPH0261419B2 (en) | ||
| US2352316A (en) | Method of producing shaped bodies from powdery ferrous material | |
| GB2058845A (en) | Method of producing fine metal particles | |
| JPS6126702A (en) | Production of magnetic metallic powder | |
| JPS63199803A (en) | Production of ferromagnetic metal powder having oxide film | |
| JPH08153613A (en) | Method for stabilizing metallic magnetic powder | |
| JPS63153201A (en) | Production of metallic iron particle powder or magnetic alloy powder essentially consisting of iron | |
| JPH0310682B2 (en) | ||
| JP2898679B2 (en) | Stabilization method for metal with active surface | |
| JPS61216306A (en) | Magnetic metal powder and manufacture thereof | |
| JPS5916904A (en) | Processing method protecting metal powder from oxidation | |
| JPH0219161B2 (en) | ||
| JPS62112703A (en) | Production of ferromagnetic metallic powder having oxide film | |
| RU2179498C1 (en) | Iron powder heat treatment method | |
| JPH03253505A (en) | Production of ferromagnetic metal powder | |
| JPS6016808A (en) | Magnetic material containing iron carbide | |
| JPS62197324A (en) | Production of feromagnetic iron oxide powder | |
| JPH01241801A (en) | Manufacture of ferromagnetic iron powder | |
| JPH01147003A (en) | Method for stabilizing ferromagnetic iron powder |