JPS5919166B2 - Manufacturing method of metal magnetic powder - Google Patents
Manufacturing method of metal magnetic powderInfo
- Publication number
- JPS5919166B2 JPS5919166B2 JP55073014A JP7301480A JPS5919166B2 JP S5919166 B2 JPS5919166 B2 JP S5919166B2 JP 55073014 A JP55073014 A JP 55073014A JP 7301480 A JP7301480 A JP 7301480A JP S5919166 B2 JPS5919166 B2 JP S5919166B2
- Authority
- JP
- Japan
- Prior art keywords
- hydroxide
- particles
- magnetic powder
- iron
- powder
- 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
Links
Landscapes
- Hard Magnetic Materials (AREA)
- Paints Or Removers (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Magnetic Record Carriers (AREA)
Description
【発明の詳細な説明】
この発明は金属鉄を主体とする磁性粉末の製造方法に関
するものであわ、粒子の軸比や大きさの調整が可能で、
しかも熱処理工程における粒子の焼結や形崩れが抑制さ
れて緻密で優れた磁気特性を有する磁性粉末が得られる
上記製造方法を提供することを目的とする。[Detailed Description of the Invention] This invention relates to a method for producing magnetic powder mainly composed of metallic iron, which allows the axial ratio and size of the particles to be adjusted.
Moreover, it is an object of the present invention to provide the above-mentioned manufacturing method, which suppresses sintering and deformation of the particles during the heat treatment step, and obtains a magnetic powder that is dense and has excellent magnetic properties.
一般的に、金属鉄を主体とする磁性粉末は、Fe3o4
やγ−Fe2O3などの酸化鉄系磁性粉末に比較して保
磁力(Hc)などの磁性特性に優れる利点を有しており
、磁気テープを始めとす0る種々の磁気記録媒体用の記
録素子として脚光を浴びているが、通常は湿式反応工程
から裏山される針状粒子からなるα−オキシ水酸化鉄や
これを加熱脱水して得られるα−Fe2O3を原料とし
て加熱還元して製造されるため、粒子径や粒子のi5形
状などの性状は上記原料自体の性状に大きく依存し、ま
たこれらの性状によつて磁気特性ならびに磁気記録媒体
用としての適性が大きく左右される。Generally, magnetic powder mainly composed of metallic iron is Fe3o4
It has the advantage of superior magnetic properties such as coercive force (Hc) compared to iron oxide magnetic powders such as γ-Fe2O3 and γ-Fe2O3, and can be used as recording elements for various magnetic recording media such as magnetic tapes. However, it is usually produced by thermal reduction using α-iron oxyhydroxide, which is made up of acicular particles that are collected from the wet reaction process, and α-Fe2O3, which is obtained by heating and dehydrating it, as a raw material. Therefore, properties such as the particle diameter and i5 shape of the particles largely depend on the properties of the raw material itself, and these properties greatly influence the magnetic properties and suitability for magnetic recording media.
一方、熱処理工程すなわち上記の加熱還元時おn よび
α−Fe2O3を経る場合の加熱脱水時において、粒子
間の焼結、個々の粒子の部分的な溶融、脱水および脱酸
素による粒子の多孔化が起こヤ易く、粒度の不均一化や
粒子の針状形状および緻密性が損なわれることにより、
得られる金属鉄を主フ5体とする磁性粉末の磁気特性が
著しく低下する傾向がある。On the other hand, during the heat treatment process, that is, during the above-mentioned thermal reduction and thermal dehydration when passing through α-Fe2O3, sintering between particles, partial melting of individual particles, and porosity of the particles due to dehydration and deoxidation occur. This is likely to occur due to nonuniform particle size and loss of acicular shape and density of particles.
The magnetic properties of the obtained magnetic powder mainly composed of metallic iron tend to deteriorate significantly.
したがつて、優れた磁性粉末を得るためには、前記のα
−オキシ水酸化鉄そのものを良好な性状のものとするこ
と、ならびに熱処理工程における10上記欠点を改善し
て原料のα−オキシ水酸化鉄の一 シャープな針状形状
と均一性を金属鉄を主体とする磁性粉末粒子に継承させ
る必要があるが、現状ではまだ十分に満足できる方法は
知られていない。Therefore, in order to obtain excellent magnetic powder, the above-mentioned α
- Making the iron oxyhydroxide itself have good properties, and improving the above 10 defects in the heat treatment process to improve the sharp acicular shape and uniformity of the raw material α-iron oxyhydroxide. There is a need to inherit this to the magnetic powder particles, but at present there is no known method that is fully satisfactory.
この発明者らは、上述の事情に照らし鋭意研究!5 を
重ねる過程で、α−オキシ水酸化鉄を生成させる反応、
すなわち第1鉄塩にアルカリを作用させる方法などによ
つて得られた水酸化第1鉄の懸濁液中に酸素含有ガスを
導入して酸化を行なう方法において、懸濁液をアルカリ
領域に維持して反応を行なえば、生成したα−オキシ水
酸化鉄もしくはこれを加熱脱水したα−Fe2O3を原
料として加熱還元して製造した金属鉄を主体とする磁性
粉末が非常に緻密な粒子となることを既に研明している
。The inventors conducted extensive research in light of the above circumstances! In the process of accumulating 5, a reaction that produces α-iron oxyhydroxide,
In other words, in a method of oxidizing ferrous hydroxide by introducing an oxygen-containing gas into a suspension of ferrous hydroxide obtained by applying an alkali to a ferrous salt, the suspension is maintained in an alkaline region. When the reaction is carried out, the magnetic powder mainly composed of metallic iron produced by thermal reduction using the generated α-iron oxyhydroxide or α-Fe2O3 obtained by heating and dehydrating it as a raw material becomes extremely dense particles. have already been refined.
この発明は、さらに継続する研究過程で、上記のα−オ
キシ水酸化鉄の生成反応をアルカリ領域で行なう反応に
おいて、水酸化第1鉄の懸濁液中に水酸化マグネシウム
、水酸化カルシウムより選ばれる少なくとも1種を存在
させ、かつ生成したα−オキシ酸化鉄もしくはこれを加
熱脱水した酸化鉄を気相中で加熱還元するに当たつて被
処理物の粒子表面にケイ素化合物を被着させて加熱脱水
または/および加熱還元を行なえば、存在させる水酸化
マグネシウム、水酸化カルシウムより選ばれる少なくと
も1種の量の加減によつて生成するα−オキシ水酸化鉄
ひいては最終的に得られる金属鉄を主体とする磁性粉末
の粒子の軸比や大きさを調整でき、しかも熱処理工程に
おける粒子の焼結や形崩れが抑制され、さらにアルカリ
領域の反応による既述した粒子の緻密性が維持されるこ
とを見い出して到達したものである。In the course of further research, this invention revealed that in the reaction for producing α-iron oxyhydroxide described above in an alkaline region, a metal selected from magnesium hydroxide and calcium hydroxide was added to a suspension of ferrous hydroxide. a silicon compound is deposited on the particle surface of the object to be treated when at least one of If thermal dehydration and/or thermal reduction is performed, α-iron oxyhydroxide produced by adjusting the amount of at least one selected from magnesium hydroxide and calcium hydroxide, and finally the metallic iron obtained. It is possible to adjust the axial ratio and size of the main magnetic powder particles, suppress the sintering and deformation of the particles during the heat treatment process, and maintain the already mentioned denseness of the particles due to the reaction in the alkaline region. This was achieved by discovering.
上記の水酸化マグネシウム、水酸化カルシウムより選ば
れる少なくとも1種の具体例としては、水酸化マグネシ
ウムおよび水酸化カルシウムが好適であシ、これらが多
く存在するほど酸素含有ガスの導入によつて析出するα
−オキシ水酸化鉄粒子の軸比(長径/短径)が大きくな
b1粒径もやや小さくなる傾向があり、したがつてその
量の増減によつて最終的に得られる金属鉄を主体とする
磁性粉末の粒子の調整が可能となV1さらに析出するα
−オキシ水酸化鉄の粒子中ないし粒子表面にマグネシウ
ム、カルシウムより選ばれる少なくとも1種が存在する
ことによつて後の熱処理工程における粒子の焼結や形崩
れが抑制される。As specific examples of at least one selected from the above-mentioned magnesium hydroxide and calcium hydroxide, magnesium hydroxide and calcium hydroxide are preferable, and the more these are present, the more they will precipitate when oxygen-containing gas is introduced. α
-The axial ratio (major axis/minor axis) of iron oxyhydroxide particles tends to be large, and the b1 particle size also tends to become somewhat small. Therefore, by increasing or decreasing the amount, the final product is mainly metallic iron. V1 which allows adjustment of magnetic powder particles and α which further precipitates
- The presence of at least one member selected from magnesium and calcium in or on the surface of the iron oxyhydroxide particles suppresses sintering and deformation of the particles during the subsequent heat treatment step.
水酸化マグネシウム、水酸化カルシウムより選ばれる少
なくとも1種を水酸化第1鉄の懸濁液中に含有させる手
段としては、水酸化マグネシウム酸化カルシウムよシ選
ばれる少なくとも1種自体を添加する方法でもよいが、
通常は種々のマグネシウムカルシウムより選ばれる少な
くとも1種の水溶性塩を添加してPH調整によつて水酸
化物の沈殿を析出させる方法が採用される。後者の方法
の好適な具体例として、硫酸第1鉄などの第1鉄塩にア
ルカリを作用させて水酸化第1鉄のコロイド沈殿を析出
させる反応において、系内にアルカリ土類金属の水溶性
塩を加え、水酸化第1鉄と水酸化マグネシウム水酸化カ
ルシウムより選ばれる少なくとも1種の共沈物を生成さ
せる方法が挙げられ、このような方法によれば酸素含有
ガスを導入してα−オキシ水酸化鉄を析出させたとき、
マグネシウムカルシウムより選ばれる少なくとも1種が
主として析出粒子中に取り込まれるために他の方法よジ
も特に熱処理工程での前記効果に対する添加効率が良好
である。水酸化マグネシウム水酸化カルシウムより選ば
れる少なくとも1種の量は、アルカリ土類金属原子をM
eとしたとき、水酸化第1鉄に対してMe/Feの原子
比で0.001〜0.1となる量が好適であシ、過少で
は実質な効果が期待できず、過多では磁気特性面での悪
影響がある。The means for incorporating at least one selected from magnesium hydroxide and calcium hydroxide into the suspension of ferrous hydroxide may include a method of adding at least one selected from magnesium hydroxide and calcium oxide itself. but,
Usually, a method is adopted in which at least one water-soluble salt selected from various types of magnesium calcium is added and a hydroxide precipitate is precipitated by adjusting the pH. As a preferred specific example of the latter method, in a reaction in which a ferrous salt such as ferrous sulfate is reacted with an alkali to precipitate a colloidal precipitate of ferrous hydroxide, water-soluble alkaline earth metals are present in the system. A method of adding salt to produce at least one kind of coprecipitate selected from ferrous hydroxide, magnesium hydroxide and calcium hydroxide is mentioned. According to such a method, an oxygen-containing gas is introduced and α- When iron oxyhydroxide is precipitated,
Since at least one selected from magnesium and calcium is mainly incorporated into the precipitated particles, the addition efficiency for the above-mentioned effects is particularly good in the heat treatment process, even compared to other methods. The amount of at least one selected from magnesium hydroxide and calcium hydroxide is such that the alkaline earth metal atom is M
When e is the atomic ratio of Me/Fe to ferrous hydroxide, it is preferable that the amount is 0.001 to 0.1. If it is too little, no substantial effect can be expected, and if it is too much, the magnetic properties will deteriorate. There are negative side effects.
この発明では水酸化第1鉄の懸濁液中に空気などの酸素
含有ガスを導入してα−オキシ水酸化鉄を生成する反応
をアルカリ領域下で行なうが、上記懸濁液をアルカリ性
とする手段は種々存在する。In this invention, an oxygen-containing gas such as air is introduced into a suspension of ferrous hydroxide, and the reaction for producing α-iron oxyhydroxide is carried out in an alkaline region. There are various means.
たとえば、普通には硫酸第1鉄などの第1鉄塩の水溶液
と水酸化ナトリウムなどのアルカリ水溶液とを反応させ
て水酸化第1鉄を生成させる一般的な方法において過剰
量のアルカリを使用することによつて容易に行なえ、ま
た種々の方法によつて得られた水酸化第1鉄の懸濁液中
に後からアルカリを添加してもよい。いずれにおいても
酸素含有ガスの導入前のPHが11以上の高アルカリ領
域であればよく、このようなアルカリ領域での反応によ
つて最終的に得られる金属鉄を主体とする磁性粉末粒子
が緻密性に富むものとなる。生成したα−オキシ水酸化
鉄は、水洗および乾燥後、直接もしくは加熱脱水してα
−Fe,O3としたのち、還元性雰囲気中で加熱するこ
とにより、金属鉄を主体とする粉末となるが、この発明
では上記の加熱脱水または/および加熱還元に供tる被
処理物の粒子表面にケイ素化合物を被着させる。For example, an excess amount of alkali is used in a common process in which ferrous hydroxide is produced by reacting an aqueous solution of a ferrous salt, such as ferrous sulfate, with an aqueous alkaline solution, such as sodium hydroxide. In particular, the alkali can be easily carried out, and an alkali can be added afterwards to the suspension of ferrous hydroxide obtained by various methods. In either case, it is sufficient that the pH before introducing the oxygen-containing gas is in a highly alkaline region of 11 or higher, and the magnetic powder particles mainly composed of metallic iron that are finally obtained by the reaction in such an alkaline region are dense. It becomes rich in sexuality. The generated α-iron oxyhydroxide is washed with water and dried, and then dehydrated directly or by heating to form α-iron oxyhydroxide.
-Fe, O3 and then heated in a reducing atmosphere to obtain a powder mainly composed of metallic iron. A silicon compound is deposited on the surface.
上記ケイ素化合物としては、種々のケイ酸ナトリウム、
ケイ酸カリウムなどの無機ケイ酸塩、ならびに各種のシ
リコンオイルなどの有機ケイ素化合物を使用でき、これ
らは前記のアルカリ土類金属と相乗的に作用して熱処理
工程における粒子の焼結や形崩れを極めて効果的に抑制
する機能を持つている。The silicon compounds include various sodium silicates,
Inorganic silicates, such as potassium silicate, and organosilicon compounds, such as various silicone oils, can be used, and these act synergistically with the alkaline earth metals to prevent particle sintering and deformation during the heat treatment process. It has an extremely effective suppressing function.
ケイ素化合物による被着処理は、これらを溶解した液中
、たとえばケイ酸アルカリではアルカリ水溶液、シリ゛
コンオイルでは種々の有機溶媒に溶かした液中に被処理
物粉末を単に浸漬してその粒子表面に付着させてもよい
が、ケイ酸アルカリを使用する場合には上記浸漬状態下
で炭酸ガスを吹き込むか酸を添加して中昭し、ケイ酸ゾ
ルの形で粒子表面に沈着させる方法が推奨される。Adhesion treatment with silicon compounds is carried out by simply immersing the powder to be treated in a solution containing these compounds, such as an aqueous alkali solution for alkali silicates and various organic solvents for silicone oil. However, when using alkali silicate, it is recommended to blow carbon dioxide gas or add acid under the above immersion conditions and deposit it on the particle surface in the form of silicate sol. be done.
また加熱脱水を経て加熱還元を行なう場合は、加熱脱水
または加熱還元のどちらかの工程の前処理として上記被
着処理を行なえばよいが、両工程の前処理として重複し
て行なつても差しつかえない。ケイ素化合物の被着量は
総量でSi/Feの原子比が0.001〜0.06の範
囲内となる量が好ましく、より少ないときは実質的な効
果が期待できず、より多い場合は磁気特性面での問題が
ある。加熱還元は、被還元物の上記種類と粒度などによ
つて最適条件が異なるが、通常は水素気流中で300〜
500℃の温度下で行なう。得られた金属鉄を主体とす
る粉末は、粒子表面ないし粒子内部にマグネシウムカル
シウムよ勺選ばれる少なくとも1種とケイ素とを含有す
るものであり、α−オキシ水酸化鉄のシヤープな針状形
状と均一性を継承しており、保磁力(Hc)や角型比(
σr/σs)などの磁気特性に優れたものである。In addition, when thermal reduction is performed after thermal dehydration, the above-mentioned adhesion treatment may be performed as a pretreatment for either the thermal dehydration or thermal reduction process, but it may be performed at the same time as a pretreatment for both processes. can not use. The total amount of silicon compound deposited is preferably such that the Si/Fe atomic ratio is within the range of 0.001 to 0.06; if it is less, no substantial effect can be expected, and if it is more than that, the magnetic There are problems with the characteristics. Optimum conditions for thermal reduction vary depending on the above-mentioned type and particle size of the material to be reduced, but usually 300~
It is carried out at a temperature of 500°C. The obtained powder mainly composed of metallic iron contains at least one selected from magnesium calcium and silicon on the particle surface or inside the particle, and has a sharp acicular shape of α-iron oxyhydroxide. Uniformity is inherited, and coercive force (Hc) and squareness ratio (
It has excellent magnetic properties such as σr/σs).
以下、この発明を実施例にて具体的に示す。This invention will be specifically illustrated in Examples below.
実施例 12007/t(7I)FesO4・7r0と
0.897/tのMgSO4・7H20を溶解した水溶
液1.5t中に、撹拌しつつ200t/TONaOH水
溶液1.5tを添加してFe(0H)2とMg(0H)
2の共沈物を含む懸濁液を得た。Example 12007/t(7I) Fe(0H)2 was added by adding 1.5t of a 200t/TONaOH aqueous solution with stirring into 1.5t of an aqueous solution in which FesO4.7r0 and 0.897/t MgSO4.7H20 were dissolved. and Mg(0H)
A suspension containing a coprecipitate of 2 was obtained.
この時、懸濁液のPHは12以上であつた。次いで液温
を40℃に加温し、液中に2t/分の割合で空気を8時
間吹き込み、α−FeOOHの針状粒子を析出させた。
得られたα−FeOOHを水洗、乾燥の後、その107
を採取して4f!/t濃度のNa4siO4水溶液0.
5t中に分散させ、CO2ガスを2t/分の割合で30
分間吹き込んで中和し、粒子表面にケイ酸ゾルが沈着し
たα−FeOOHを得た。このα−FeOOHを水洗、
乾燥後、その1tを採取して電気炉中で400℃の温度
下、H2ガス流量1t/分にて2時間還元し、マグネシ
ウムとケイ素を含有する金属鉄粉末を得た。この粉末の
平均長径は0.3μm1軸比は10であつた。実施例
2実施例1の方法において、MgSO4・7H20の溶
解量が3,55v/tである硫酸第1鉄一硫酸マグネシ
ウム混合水溶液1.5tを使用し、他の条件を全て実施
例1と同一にして、マグネシウムとケイ素とを含む金属
鉄粉末を得た。At this time, the pH of the suspension was 12 or higher. Next, the liquid temperature was raised to 40° C., and air was blown into the liquid at a rate of 2 t/min for 8 hours to precipitate needle-like particles of α-FeOOH.
After washing the obtained α-FeOOH with water and drying, its 107
Collect 4f! /t concentration of Na4siO4 aqueous solution 0.
CO2 gas is dispersed in 5t/min at a rate of 2t/min.
The particles were blown into the solution for neutralization to obtain α-FeOOH in which silicic acid sol was deposited on the particle surface. Wash this α-FeOOH with water,
After drying, 1 ton of the powder was collected and reduced in an electric furnace at a temperature of 400° C. at a H2 gas flow rate of 1 ton/min for 2 hours to obtain metallic iron powder containing magnesium and silicon. This powder had an average major axis of 0.3 μm and a uniaxial ratio of 10. Example
2 In the method of Example 1, 1.5 t of ferrous sulfate monomagnesium sulfate mixed aqueous solution having a dissolved amount of MgSO4.7H20 of 3.55 v/t was used, and all other conditions were the same as in Example 1. , a metallic iron powder containing magnesium and silicon was obtained.
この粉末の平均長径は0.4μm1軸比は12であつた
。実施例 3
実施例1の方法における硫酸第1鉄一硫酸マグネシウム
混合水溶液の代わりに、2007/tのFeSO4・7
H20と1.70v/tのCa(NO3)2・4H20
を溶解した水溶液1.5tを使用し、他の条件を全て実
施例1と同一にして、カルシウムとケイ素とを含む金属
鉄粉末を得た。This powder had an average major axis of 0.4 μm and a uniaxial ratio of 12. Example 3 Instead of the ferrous sulfate monomagnesium sulfate mixed aqueous solution in the method of Example 1, 2007/t FeSO4.7
H20 and 1.70v/t Ca(NO3)2・4H20
Metallic iron powder containing calcium and silicon was obtained using 1.5 t of an aqueous solution in which .
この粉末の平均長径は0.35μm1軸比は10であつ
た。実施例 42007/t濃度のNaOH水溶液1.
5t中に、攪拌しつつ2007/TOFeSO4・7H
20と1.7v/t(7)Ca(NO3)2・4H20
を溶解した水溶液1.5tを添加し、Fe(0H)2と
Ca(0H)2との共沈物を含む懸濁液を得た。This powder had an average major axis of 0.35 μm and a uniaxial ratio of 10. Example 4 NaOH aqueous solution with a concentration of 2007/t1.
2007/TOFeSO4・7H while stirring during 5t
20 and 1.7v/t(7)Ca(NO3)2・4H20
1.5 t of an aqueous solution in which Fe(0H)2 and Ca(0H)2 were dissolved was added to obtain a suspension containing a coprecipitate of Fe(0H)2 and Ca(0H)2.
この時、懸濁液のPHは12以上であつた。次いで液温
を20℃に維持しつつ1t/分の割合で空気を1時間吹
き゛込み、α−FeOOHの種晶を生成させ、さらに液
温を50℃に昇温して2t/分の割合で空気を10時間
吹き込んでα−FeOOHの針状粒子を析出させた。得
られたα−FeOOHを水洗、乾燥の後、その10tを
採取してマツフル炉中で、τ 600′Cの温度下、空
気を1.5t/分の割合で通して10時間の酸化を行つ
てα−Fe2O3とし≠らこのα−Fe2O3を47/
t濃度のMa4siO4水溶液0.5t中に分散させ、
0.1N−Hct水溶液を添加して液のPHが6.0と
なるまで中和し、フ粒子表面にケイ酸ゾルが沈着したα
−Fe2O3粒子を得た。このα−Ft2O3を水洗、
乾燥後、その1tを採取して電気炉中で450℃の温度
下、H2ガス流量1t/分にて2時間還元し、カルシウ
ムとケイ素とを含む金属鉄粉末を得た。この粉末の平均
長径は0.4μm1軸比は10であつた。比較例 1実
施例1の方法における硫酸第1鉄一硫酸マグネシウム混
合水溶液の代わシに、200p/tのFeSO4・7H
20のみを溶解した水溶液を使用し、他の条件を全て実
施例1と同一にして、ケイ素を含む金属鉄粉末を得た。At this time, the pH of the suspension was 12 or higher. Next, while maintaining the liquid temperature at 20°C, air was blown in at a rate of 1 t/min for 1 hour to generate α-FeOOH seed crystals, and then the liquid temperature was further raised to 50°C and air was blown at a rate of 2 t/min. Air was blown into the solution for 10 hours to precipitate acicular particles of α-FeOOH. After washing and drying the obtained α-FeOOH, 10 t of it was collected and oxidized in a Matsufuru furnace at a temperature of τ 600′C for 10 hours by passing air at a rate of 1.5 t/min. Let this α-Fe2O3 be 47/
Dispersed in 0.5 t of Ma4siO4 aqueous solution of t concentration,
A 0.1N-Hct aqueous solution was added to neutralize the solution until the pH reached 6.0, and silicic acid sol was deposited on the surface of the particles.
-Fe2O3 particles were obtained. Wash this α-Ft2O3 with water,
After drying, 1 ton of the powder was collected and reduced in an electric furnace at a temperature of 450° C. at a H2 gas flow rate of 1 ton/min for 2 hours to obtain metallic iron powder containing calcium and silicon. This powder had an average major axis of 0.4 μm and a uniaxial ratio of 10. Comparative Example 1 In place of the ferrous sulfate monomagnesium sulfate mixed aqueous solution in the method of Example 1, 200 p/t of FeSO4.7H was added.
Metallic iron powder containing silicon was obtained using an aqueous solution in which only 20 was dissolved and all other conditions were the same as in Example 1.
この粉末の平均長径は0.45μm1軸比は12であつ
た。比較例 2
実施例2の方法においてNa4siO4による処理を行
なわなかつた以外は、全て実施例2と同一条件として、
マグネシウムを含む金属鉄粉末を得た。This powder had an average major axis of 0.45 μm and a uniaxial ratio of 12. Comparative Example 2 All conditions were the same as in Example 2, except that the treatment with Na4siO4 was not performed in the method of Example 2,
A metallic iron powder containing magnesium was obtained.
この粉末の平均長径は0.35μm1軸比は10であつ
た。以上の実施例および比較例にて得られた金属鉄粉末
について、それぞれ飽和磁化(σs)、保磁力(Hc)
および角型比(σr/σs)を測定した結果を下表に示
す。This powder had an average major axis of 0.35 μm and a uniaxial ratio of 10. Saturation magnetization (σs) and coercive force (Hc) of the metallic iron powders obtained in the above examples and comparative examples, respectively.
The results of measuring the squareness ratio (σr/σs) are shown in the table below.
実施例および比較例の結果から明らかなように、この発
明の方法によれば、加熱還元などの熱処理工程での粒子
間の焼結や粒子の形崩れが効果的に抑制されて優れた磁
気特性を有する金属鉄を主体とする磁性粉末が得られ、
かつ水酸化マグネシウム、水酸化カルシウムよシ選ばれ
る少なくとも1種の使用量の増減によつて軸比と粒度を
調整できる。As is clear from the results of Examples and Comparative Examples, according to the method of the present invention, sintering between particles and deformation of particles during heat treatment steps such as thermal reduction are effectively suppressed, resulting in excellent magnetic properties. A magnetic powder mainly composed of metallic iron is obtained,
Moreover, the axial ratio and particle size can be adjusted by increasing or decreasing the amount of at least one selected from magnesium hydroxide and calcium hydroxide.
Claims (1)
懸濁液中に酸素含有ガスを導入してα−オキシ水酸化鉄
を生成させ、このα−オキシ水酸化鉄もしくはこれを加
熱脱水した酸化鉄を気相中で加熱還元して金属鉄を主体
とする磁性粉末を製造するに当たり、上記懸濁液中にマ
グネシウムおよびカルシウムから選ばれる少なくとも1
種の水酸化物を含有させ、かつ前記の加熱脱水および加
熱還元の少なくとも1つの工程の前処理として前記αオ
キシ水酸化鉄もしくは酸化鉄の粒子表面にケイ素化合物
を被着させる工程を含むことを特徴とする金属磁性粉末
の製造方法。1. Introducing an oxygen-containing gas into an alkaline suspension of ferrous hydroxide adjusted to pH 11 or higher to produce α-iron oxyhydroxide, or iron oxide obtained by heating and dehydrating this α-iron oxyhydroxide. At least one member selected from magnesium and calcium is added to the suspension to produce a magnetic powder mainly composed of metallic iron by thermal reduction in a gas phase.
containing a seed hydroxide, and including a step of depositing a silicon compound on the surface of the α-oxyiron hydroxide or iron oxide particles as a pretreatment for at least one of the steps of the thermal dehydration and thermal reduction. Characteristic method for producing metal magnetic powder.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55073014A JPS5919166B2 (en) | 1980-05-30 | 1980-05-30 | Manufacturing method of metal magnetic powder |
| DE8181104141T DE3167164D1 (en) | 1980-05-30 | 1981-05-29 | Process for preparing ferromagnetic particles comprising metallic iron |
| EP81104141A EP0041257B1 (en) | 1980-05-30 | 1981-05-29 | Process for preparing ferromagnetic particles comprising metallic iron |
| US06/516,432 US4456475A (en) | 1980-05-30 | 1983-07-25 | Process for preparing ferromagnetic particles comprising metallic iron |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55073014A JPS5919166B2 (en) | 1980-05-30 | 1980-05-30 | Manufacturing method of metal magnetic powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56169708A JPS56169708A (en) | 1981-12-26 |
| JPS5919166B2 true JPS5919166B2 (en) | 1984-05-02 |
Family
ID=13506048
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55073014A Expired JPS5919166B2 (en) | 1980-05-30 | 1980-05-30 | Manufacturing method of metal magnetic powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5919166B2 (en) |
-
1980
- 1980-05-30 JP JP55073014A patent/JPS5919166B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56169708A (en) | 1981-12-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4456475A (en) | Process for preparing ferromagnetic particles comprising metallic iron | |
| JPS5919163B2 (en) | Method for producing magnetic metal powder | |
| JPS5919169B2 (en) | Manufacturing method of metal magnetic powder | |
| JPS6217364B2 (en) | ||
| JPS5919166B2 (en) | Manufacturing method of metal magnetic powder | |
| JPS5919165B2 (en) | Manufacturing method of metal magnetic powder | |
| JPS6122604A (en) | Magnetic metal powder and manufacture thereof | |
| JPS5919168B2 (en) | Manufacturing method of metal magnetic powder | |
| JPS58161705A (en) | Production of magnetic metallic powder | |
| JPH0420241B2 (en) | ||
| JPS5919167B2 (en) | Manufacturing method of metal magnetic powder | |
| JPH0237403B2 (en) | ||
| JPS5932523B2 (en) | Manufacturing method of metal magnetic powder | |
| JPS58161723A (en) | Production of magnetic metallic powder | |
| JPH0343325B2 (en) | ||
| JPS6132259B2 (en) | ||
| JPS5877505A (en) | Production of metallic magnetic powder | |
| JPS63140005A (en) | Production of fine ferromagnetic metal particle powder | |
| JPS59172209A (en) | Metal magnetic powder and manufacture thereof | |
| JPS61160905A (en) | Magnetic metal powder | |
| JPS6092446A (en) | Magnetic body of metallic iron containing cobalt atom | |
| JPS59159904A (en) | Metallic magnetic powder and its production | |
| JPS59162205A (en) | Metallic magnetic powder and its manufacture | |
| JPS62156208A (en) | Ferromagnetic metallic powder | |
| JPS58126905A (en) | Production of magnetic metal powder consisting of iron or essentially of iron |