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JPS62297216A - Production of fine particle of ba ferrite - Google Patents

Production of fine particle of ba ferrite

Info

Publication number
JPS62297216A
JPS62297216A JP61139648A JP13964886A JPS62297216A JP S62297216 A JPS62297216 A JP S62297216A JP 61139648 A JP61139648 A JP 61139648A JP 13964886 A JP13964886 A JP 13964886A JP S62297216 A JPS62297216 A JP S62297216A
Authority
JP
Japan
Prior art keywords
particles
ferrite
aqueous solution
precipitate
ions
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.)
Pending
Application number
JP61139648A
Other languages
Japanese (ja)
Inventor
Koichi Nushishiro
晃一 主代
Keizou Okuno
奥埜 計造
Izumi Hoshihara
星原 泉
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP61139648A priority Critical patent/JPS62297216A/en
Publication of JPS62297216A publication Critical patent/JPS62297216A/en
Pending legal-status Critical Current

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  • Compounds Of Iron (AREA)
  • Hard Magnetic Materials (AREA)

Abstract

PURPOSE:To obtain fine particles of Ba ferrite having very small particles and improved magnetic characteristics and powder characteristics free from sintering between particles, by obtaining coprecipitation from an aqueous solution containing both ions of Fe and Ba having a specific ratio of Fe/Ba, washing the coprecipitation with water, drying and calcining the coprecipitation with a specific flux. CONSTITUTION:Fine particles of Ba ferrite are obtained by the following method. Namely, (1) an aqueous solution containing Fe ion and Ba ion having a molar ratio of Fe/Ba of 10-13 is blended with an alkali aqueous solution and precipitate is obtained at pH >=10. (2) the precipitate is washed with water until the pH becomes 6-9 and dried. (3) the dried precipitate is incorporated with >=5wt% based on total amount of one or more of chloride or sulfate of Na or K and calcined at 600-1,200 deg.C.

Description

【発明の詳細な説明】 3、発明の詳細な説明 〈産業上の利用分野〉 本発明はBaフェライト微粒子の製造方法に関し、特に
電気機器等に組み込まれるゴムあるいはプラスチック磁
石などの永久磁石材料に用いられる磁性粉として適した
Baフェライト微粒子の製造方法に関する。
Detailed Description of the Invention 3. Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a method for producing Ba ferrite fine particles, particularly for use in permanent magnet materials such as rubber or plastic magnets incorporated into electrical equipment, etc. The present invention relates to a method for producing Ba ferrite fine particles suitable as magnetic powder.

〈従来技術とその問題点〉 ゴム、プラスチック磁石などに用いられる磁性粉に要求
される特性として、粉体特性及び磁気特性がよいことが
挙げられる。
<Prior art and its problems> Characteristics required of magnetic powder used in rubber, plastic magnets, etc. include good powder characteristics and magnetic characteristics.

すなわち粉体特性としては、樹脂との混練性がよいこと
、つまり粒径がほぼ単磁区(シングルドメイン)径で、
粒径が揃い、粒子間に焼結がなく樹脂中に粒子が分散し
やすいこと、また磁気特性としては、飽和磁化、保磁力
が大きいことが要求される。
In other words, the powder properties are that it has good kneadability with resin, that is, the particle size is approximately a single domain diameter,
It is required that the particle size be uniform, that there is no sintering between the particles, and that the particles are easily dispersed in the resin, and that the magnetic properties are high, such as saturation magnetization and coercive force.

ところで従来粒子間に焼結、融着等のない粒子を得る方
法としては、原料を焼成する際に融剤を添加する方法が
知られており、特公昭55−49030号の方法では融
剤成分として塩化バリウム、塩化ストロンチウムを用い
て焼成を行っている。しかしながらこれらの融剤は粒子
同士の接触による焼結、融着は防ぐが、融液相中のフェ
ライト成分がフェライト粒子に凝縮することによる粒子
の結晶成長を促進するので粒子を小さくし難い。
By the way, as a conventional method for obtaining particles without sintering, fusion, etc. between particles, there is a known method of adding a fluxing agent when firing raw materials. As a result, barium chloride and strontium chloride are used for firing. However, although these fluxes prevent sintering and fusion due to contact between particles, they promote crystal growth of the particles by condensing the ferrite component in the melt phase onto the ferrite particles, making it difficult to reduce the size of the particles.

また、特公昭57−21517号の方法では、Ba、 
Sr等のフェライト粒子粉末にNaCf1、BaCf1
2などの融剤を加えて焼成を行い、粒子形状の制御を行
っているが、原料として仮焼品を粉砕した粉末を用いて
いるため、焼成品の粒径は大きく、保磁力が3 KOe
程度と低い。
In addition, in the method of Japanese Patent Publication No. 57-21517, Ba,
NaCf1, BaCf1 in ferrite particle powder such as Sr
The particle shape is controlled by adding a flux such as 2 to control the particle shape, but since powder obtained by pulverizing the calcined product is used as the raw material, the particle size of the fired product is large and the coercive force is 3 KOe.
The degree is low.

〈発明の目的〉 本発明の目的は、電気機器の小型化に伴う永久磁石の小
型化、鯖密化、高性能化に対応するため、粒子が微小で
あり、粒子間に焼結がなく、粒径が揃っており、優れた
磁気特性を持ち、しかも樹脂との複合化の際優れた混練
性を有するHaミツエライト粒子の製造方法を提供する
ものである。
<Objective of the Invention> The object of the present invention is to respond to the miniaturization, density, and performance improvement of permanent magnets accompanying the miniaturization of electrical equipment, and in order to respond to the miniaturization, density, and performance improvement of permanent magnets, the particles are minute, there is no sintering between the particles, and The object of the present invention is to provide a method for producing Ha mitzerite particles having uniform particle sizes, excellent magnetic properties, and excellent kneading properties when compounded with a resin.

〈発明の構成〉 Baフェライトを製造する場合、一般的には炭酸バリウ
ム、酸化鉄の粉末を原料とし、これを混合した後反応さ
せる。しかし、この反応は酸化鉄粉末粒子の表面から内
部にバリウムイオンが拡散することによって起こるため
、生成したBaフェライト粒子は原理的に酸化鉄粒子よ
り小さくすることはできない。
<Structure of the Invention> When producing Ba ferrite, powders of barium carbonate and iron oxide are generally used as raw materials, which are mixed and then reacted. However, since this reaction occurs due to the diffusion of barium ions from the surface of the iron oxide powder particles into the interior, the generated Ba ferrite particles cannot be made smaller than the iron oxide particles in principle.

ところで水溶液中で、FeイオンとBaイオンを同時に
沈澱させた場合、沈澱物は非晶質状もしくは非常に微小
な粒子になっておりFeとBaがイオン単位で隣接し反
応のための拡散はわずかでよく、粒成長が進まないうち
に反応を完了できる。
By the way, when Fe ions and Ba ions are precipitated at the same time in an aqueous solution, the precipitate becomes amorphous or very small particles, and Fe and Ba are adjacent to each other in ion units, and diffusion for reaction is minimal. The reaction can be completed before grain growth progresses.

しかし、実際にこの沈澱物を用いて粒子を製造しようと
すると、粒子間の凝結が強くなるため、粒子が非常に焼
結しやすく、融着や結着を起こし、粒子をバラバラに出
来ない。そこで、この粒子間の焼結を妨ぐべく共沈物に
融剤を添加する。
However, when particles are actually produced using this precipitate, the coagulation between the particles becomes strong, so the particles are extremely susceptible to sintering, causing fusion and binding, making it impossible to separate the particles. Therefore, a fluxing agent is added to the coprecipitate to prevent sintering between particles.

なおその際用いる融剤としては、粒成長をおさえ反応を
促進するような特性を持つことが望ましい。
It is desirable that the flux used at this time has properties that suppress grain growth and promote the reaction.

以上のことを考慮し、融剤の選択及び種々の条件での製
造を行った結果本発明に至った。
In consideration of the above, the present invention was achieved as a result of selecting a flux and performing production under various conditions.

すなわち本発明は、FeイオンとBaイオンとを含み、
このモル比(Fe/Ba)が10〜13である水溶液と
、アルカリ水溶液とを混合してpH10以上で沈澱物を
得、該沈澱物をそのpHが6〜9となるまで水洗した後
、Naあるいはにの塩化物または硫酸塩のうち1種ある
いは2種以上を全重量の5wt%以上加え、600℃〜
1200℃の温度で焼成することを特徴とするBaフェ
ライト微粒子の製造方法を提供する。
That is, the present invention includes Fe ions and Ba ions,
This aqueous solution with a molar ratio (Fe/Ba) of 10 to 13 is mixed with an alkaline aqueous solution to obtain a precipitate at a pH of 10 or higher, and after washing the precipitate with water until the pH becomes 6 to 9, Na Alternatively, one or more of chloride or sulfate of crab is added at least 5 wt% of the total weight, and heated to 600℃~
Provided is a method for producing Ba ferrite particles, which is characterized by firing at a temperature of 1200°C.

以下に本発明の詳細な説明する。The present invention will be explained in detail below.

本発明方法では、微小なりaフェライト粒を得るため、
原料としてFeとBaを含む水溶液からの共沈物を用い
る。
In the method of the present invention, in order to obtain minute ferrite grains,
A coprecipitate from an aqueous solution containing Fe and Ba is used as a raw material.

Fe原料は水可溶性の鉄塩であればいかなるものでもよ
いか、塩化第2鉄、硝酸第2鉄、硫酸第2鉄等を単独で
、あるいは混合して用いる。
The Fe raw material may be any water-soluble iron salt, and ferric chloride, ferric nitrate, ferric sulfate, etc. may be used alone or in combination.

Ba原料も水可溶性のBa塩であればいかなるものでも
よいが、塩化バリウム、硝酸バリウム等を単独で、ある
いは混合して用いる。
The Ba raw material may be any water-soluble Ba salt, and barium chloride, barium nitrate, etc. may be used alone or in combination.

水溶液中のFeイオンとBaイオンのモル比(Fe/B
a)は10〜13とする。ここでFe/Baが10未満
の場合には、 [laO・2 Fe2O,で示される非
磁性組成物が生成し、13を超える場合には、Fe2O
3などの非磁性組成物が生成し、ともに好ましい磁気特
性が得られない。
Molar ratio of Fe ions and Ba ions in aqueous solution (Fe/B
a) shall be 10-13. Here, when Fe/Ba is less than 10, a non-magnetic composition represented by [laO.2 Fe2O, is produced, and when it exceeds 13, Fe2O
Non-magnetic compositions such as No. 3 are produced, and neither of them can provide desirable magnetic properties.

次にこのFeイオンとBaイオンを所定量含む水溶液と
アルカリ水溶液とを混合し、pH10以上でFe、 B
aの共沈物を得る。アルカリ水溶液はいかなるものでも
よいが、水酸化ナトリウム、炭酸ナトリウム水溶液が好
ましい。
Next, an aqueous solution containing a predetermined amount of Fe ions and Ba ions is mixed with an alkaline aqueous solution, and at a pH of 10 or more, Fe, B
Obtain a coprecipitate of a. Any alkaline aqueous solution may be used, but sodium hydroxide and sodium carbonate aqueous solutions are preferred.

ここで沈澱物を生成する際pHが10未満の状態である
とFeとBaのイオンが十分沈澱せず、この場合にも組
成ずれを起こし好ましい磁気特性が得られない。
When the precipitate is produced, if the pH is less than 10, Fe and Ba ions will not be sufficiently precipitated, and in this case as well, a compositional deviation will occur, making it impossible to obtain desirable magnetic properties.

上記の共沈物からアルカリ成分を除去するため、p11
6〜9となるまで水洗を行い、乾燥したものを原料とす
る。ここで共沈物にアルカリ成分が残っていると、Ba
フェライトよりも非磁性の組成物のほうが、優先的に生
成することがあり、また酸性水溶液中は共沈物は溶解し
てしまうため、この場合も組成ずれを起こすことがあり
、Baミツエライト造ト好ましくない。
In order to remove alkaline components from the above coprecipitate, p11
Wash with water until it reaches 6 to 9, and use the dried material as raw material. If alkaline components remain in the coprecipitate, Ba
Non-magnetic compositions may be formed preferentially over ferrite, and since coprecipitates are dissolved in acidic aqueous solutions, composition deviations may occur in this case as well, and Bamitzerite production Undesirable.

次にこの原料と融剤を混合した後焼成し、水洗、乾燥を
行う。焼成の際、融剤を使用すると粒子間に焼結のない
粒径の揃フた粒子が得られる。
Next, this raw material and flux are mixed, then fired, washed with water, and dried. When a flux is used during firing, particles with a uniform diameter can be obtained without sintering between the particles.

融剤として、Na、にの塩化物または硫酸塩を単独ある
いは二種以上混合して用いる。特に、これら融剤は水溶
性であるため水洗により除去が容易で、安価であるとい
う利点を持つ。融剤を単独又は二種以上を混合して用い
た場合、600℃から1200℃までの焼成温度範囲で
粒子間に焼結のない、粒径のよく揃った、磁気特性の優
れた粒子を得ることができる。ここで、600℃を下回
る温度で焼成した場合には、その温度が融剤の融点以下
で、融剤を添加する効果が望めない場合とフェライト化
反応が不十分である場合があり、また1200℃を上回
る温度で焼成した場合には粒成長が進み、粒径が大きく
なり、磁気特性も好ましくない。
As a fluxing agent, a chloride or sulfate of Na or Na is used alone or in combination of two or more. In particular, since these fluxes are water-soluble, they have the advantage of being easy to remove by washing with water and being inexpensive. When a flux is used alone or in combination of two or more, particles with excellent magnetic properties, with no sintering between particles and with well-uniformed particle sizes can be obtained in the firing temperature range from 600°C to 1200°C. be able to. Here, when firing at a temperature lower than 600°C, the temperature is below the melting point of the fluxing agent, and the effect of adding the fluxing agent may not be expected, or the ferrite reaction may be insufficient. When fired at a temperature higher than 0.degree. C., grain growth progresses, grain size increases, and magnetic properties are also unfavorable.

これに反し塩化バリウムを含む融剤を用いて焼成した場
合には、得られだ粒子は、粒径が大きく、あるいは反応
が不十分であるので磁気特性が好ましくない。またBa
SO4は水に難溶であるので水洗による除去ができない
On the other hand, when firing is performed using a flux containing barium chloride, the resulting particles have unfavorable magnetic properties because of their large particle size or insufficient reaction. Also Ba
Since SO4 is poorly soluble in water, it cannot be removed by washing with water.

融剤の混合割合については5wt%以上含まれると融剤
効果が認められる。好ましくは、5〜70wt%とする
Regarding the mixing ratio of the fluxing agent, a fluxing agent effect is recognized when it is contained in a proportion of 5 wt % or more. Preferably, it is 5 to 70 wt%.

〈実施例〉 以下に実施例について発明を具体的に説明する。<Example> The invention will be specifically described below with reference to Examples.

(実施例1) 塩化バリウム(Ba(:12 ・21120)15.2
5 g及び塩化第2鉄(FeCj!3  ・6H20)
202.75gを水1uに溶解し、水溶液とする。水酸
化ナトリウム(Na011)250.0 g及び炭酸ナ
トリウム(Na2 CO3) 62.5gを水22に溶
解した水溶液に、Ba、 Feを含む水溶液を攪拌しな
がら添加した。pH11で得られた沈澱物はデカンテー
ションによりpHが8以下になるまで水洗を行い、濾過
、乾燥した。
(Example 1) Barium chloride (Ba(:12 ・21120) 15.2
5 g and ferric chloride (FeCj!3 ・6H20)
Dissolve 202.75 g in 1 U of water to make an aqueous solution. An aqueous solution containing Ba and Fe was added to an aqueous solution of 250.0 g of sodium hydroxide (Na011) and 62.5 g of sodium carbonate (Na2 CO3) dissolved in 22 of water with stirring. The precipitate obtained at pH 11 was washed with water by decantation until the pH became 8 or less, filtered, and dried.

得られた沈澱物に塩化ナトリウム(NaCIl)を沈澱
物と融剤の比を重量比で1:1になるように添加、混合
し、電気炉中で1000℃で2時間焼成を行った後、温
水で水洗を行い乾燥を行った。
Sodium chloride (NaCIl) was added and mixed to the obtained precipitate so that the ratio of precipitate to flux was 1:1 by weight, and after baking at 1000 ° C. for 2 hours in an electric furnace, It was washed with warm water and dried.

こうして得られた粒子は粒子間に焼結のない粒径のそろ
ったBaフェライト微粒子であった。平均粒径及び磁気
特性は第1表に示す。
The particles thus obtained were Ba ferrite fine particles with uniform particle sizes and no sintering between the particles. The average particle size and magnetic properties are shown in Table 1.

(実施例2) 融剤として塩化カリウム(にcIL)を用い、焼成を8
00℃で行ったことの他は実施例1と同様とした。
(Example 2) Using potassium chloride (cIL) as a flux, calcination was carried out for 8
The procedure was the same as in Example 1 except that the temperature was 00°C.

(実施例3) 融剤として硫酸ナトリウム(Na2 S04 )を用い
た他は実施例1と同様とした。
(Example 3) The same procedure as Example 1 was carried out except that sodium sulfate (Na2S04) was used as a fluxing agent.

(実施例4) 融剤として塩化ナトリウム(NaC1)と硫酸ナトリウ
ム(Na2504 )の等モル比である混合物を用い、
焼成を700℃で行ったことの他は実施例1と同様とし
た。
(Example 4) Using a mixture of sodium chloride (NaC1) and sodium sulfate (Na2504) in an equimolar ratio as a flux,
The procedure was the same as in Example 1 except that the firing was performed at 700°C.

(実施例5) 融剤として塩化ナトリウム(Nal、u) と塩化カリ
ウム(にcR,)と硫酸ナトリウム(Na2 S04 
)の等モア1/ l十−Pふ乙10介物をY■し1.怖
[ルを600℃で行ったことの他は、実施例1と同様と
した。
(Example 5) Sodium chloride (Nal, u), potassium chloride (nicR,) and sodium sulfate (Na2S04) were used as fluxing agents.
)'s equal moa 1/l 10-P 10 pieces Y■ 1. The procedure was the same as in Example 1, except that the heating was carried out at 600°C.

(実施例6) 塩化バリウム16.65 g及び塩化第2鉄202.7
5gを用いて沈澱物を得、融剤として、Na2 S04
を用い、焼成を900℃で行ったことの他は実施例1と
同様とした。
(Example 6) Barium chloride 16.65 g and ferric chloride 202.7 g
5 g was used to obtain a precipitate, and Na2S04 was used as a fluxing agent.
The procedure was the same as in Example 1 except that the firing was performed at 900°C.

(比較例1) 融剤として、硫酸ナトリウ(Na2 S04 )を用い
、焼成を1300℃で行ったことの他は実施例1と同様
とした。
(Comparative Example 1) The procedure was the same as in Example 1 except that sodium sulfate (Na2 S04) was used as a flux and the firing was performed at 1300°C.

(比較例2) 炭酸バリウム(Ba CO3)粉末lO,14g及び酸
化鉄(a−Fe203)粉末52.05 gを混合した
ものを用い、こわに塩化ナトリウム(NaCρ)を原料
と融剤の比を重量比で1=1になるように添加、混合し
、電気炉中で1000℃で2時間焼成を行った後、温水
で水洗を行い乾燥を行った。
(Comparative Example 2) A mixture of 14 g of barium carbonate (Ba CO3) powder and 52.05 g of iron oxide (a-Fe203) powder was used, and the ratio of raw material and flux was adjusted by adding sodium chloride (NaCρ) to the mixture. They were added and mixed at a weight ratio of 1=1, fired in an electric furnace at 1000°C for 2 hours, washed with warm water, and dried.

(比較例3) 融剤として塩化カリウム(にCu)を用いた他は比較例
2と同様とした。
(Comparative Example 3) The same procedure as Comparative Example 2 was carried out except that potassium chloride (Cu) was used as a fluxing agent.

(比較例4) 焼成を1100℃で行ったことの他は実施例6と同様で
ある。
(Comparative Example 4) Same as Example 6 except that the firing was performed at 1100°C.

(比較例5) 融剤として塩化ナトリウム(NaCl2)と塩化バリウ
ム(BaCl2. )の等モル比である混合物を用いた
他は実施例4と同様とした。
(Comparative Example 5) The same procedure as in Example 4 was carried out except that a mixture of sodium chloride (NaCl2) and barium chloride (BaCl2.) in an equimolar ratio was used as a flux.

実施例および比較例で得られた粒子の平均粒径及び磁気
特性を第1表に示す。
Table 1 shows the average particle diameter and magnetic properties of the particles obtained in Examples and Comparative Examples.

また、実施例2及び比較例2で得られたロaフェライト
粒子の走査型電子顕微鏡写真をそれぞれ、第1図及び第
2図に示す。
Further, scanning electron micrographs of the loa ferrite particles obtained in Example 2 and Comparative Example 2 are shown in FIGS. 1 and 2, respectively.

〈発明の効果〉 本発明方法により、得られた粒子は、走査型電子顕微鏡
観察の結果粒子間に焼結がなく粒径がよく揃い、飽和磁
化が55 emu/g以上で保持力が5000 0e以
上と、ゴム、プラスチック磁石用Baフェライト磁性粉
として優れた特性を持つ微粒子である。
<Effects of the Invention> As a result of scanning electron microscope observation, the particles obtained by the method of the present invention have a well-uniformed particle size with no sintering between the particles, a saturation magnetization of 55 emu/g or more, and a coercive force of 5000 0e. In summary, the fine particles have excellent properties as Ba ferrite magnetic powder for rubber and plastic magnets.

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

図面は全て結晶構造を示す図面代用写真である。 第1図および第2図は、それぞれ実施例2および比較例
2で得られたBaフェライト粒子の走査型電子顕微鏡写
真(6000倍)である。 特許出願人  川崎製鉄株式会社 代理人 弁理士  渡 辺 望 捻 回   弁理士   石  井  陽  −第  1 
 図 第21A
All drawings are photographs substituted for drawings showing the crystal structure. FIG. 1 and FIG. 2 are scanning electron micrographs (6000x magnification) of Ba ferrite particles obtained in Example 2 and Comparative Example 2, respectively. Patent applicant Kawasaki Steel Co., Ltd. agent Patent attorney Nozomi Watanabe Nejiri Patent attorney Yo Ishii - No. 1
Figure 21A

Claims (1)

【特許請求の範囲】[Claims] (1)FeイオンとBaイオンとを含み、このモル比(
Fe/Ba)が10〜13である水溶液と、アルカリ水
溶液とを混合してpH10以上で沈澱物を得、該沈澱物
をそのpHが6〜9となるまで水洗した後、Naあるい
はにの塩化物または硫酸塩のうち1種あるいは2種以上
を全重量の5wt%以上加え、600℃〜1200℃の
温度で焼成することを特徴とするBaフェライト微粒子
の製造方法。
(1) Contains Fe ions and Ba ions, and this molar ratio (
An aqueous solution with Fe/Ba) of 10 to 13 is mixed with an alkaline aqueous solution to obtain a precipitate at a pH of 10 or higher, and the precipitate is washed with water until the pH becomes 6 to 9, followed by chlorination of Na or Ni. 1. A method for producing Ba ferrite fine particles, which comprises adding one or more of Ba ferrite particles or sulfates in an amount of 5 wt% or more based on the total weight, and firing at a temperature of 600°C to 1200°C.
JP61139648A 1986-06-16 1986-06-16 Production of fine particle of ba ferrite Pending JPS62297216A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61139648A JPS62297216A (en) 1986-06-16 1986-06-16 Production of fine particle of ba ferrite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61139648A JPS62297216A (en) 1986-06-16 1986-06-16 Production of fine particle of ba ferrite

Publications (1)

Publication Number Publication Date
JPS62297216A true JPS62297216A (en) 1987-12-24

Family

ID=15250165

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61139648A Pending JPS62297216A (en) 1986-06-16 1986-06-16 Production of fine particle of ba ferrite

Country Status (1)

Country Link
JP (1) JPS62297216A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5378384A (en) * 1991-09-19 1995-01-03 Minnesota Mining And Manufacturing Company Process of making hexagonal magnetic ferrite pigment for high density magnetic recording applications
US5616414A (en) * 1993-12-28 1997-04-01 Imation Corp. Hexagonal magnetic ferrite pigment for high density magnetic recording applications

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5378384A (en) * 1991-09-19 1995-01-03 Minnesota Mining And Manufacturing Company Process of making hexagonal magnetic ferrite pigment for high density magnetic recording applications
US5626956A (en) * 1991-09-19 1997-05-06 Imation Corp. Hexagonal magnetic ferrite pigment for high density magnetic recording applications
US5616414A (en) * 1993-12-28 1997-04-01 Imation Corp. Hexagonal magnetic ferrite pigment for high density magnetic recording applications

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