JPH0250964B2 - - Google Patents
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- Publication number
- JPH0250964B2 JPH0250964B2 JP59128939A JP12893984A JPH0250964B2 JP H0250964 B2 JPH0250964 B2 JP H0250964B2 JP 59128939 A JP59128939 A JP 59128939A JP 12893984 A JP12893984 A JP 12893984A JP H0250964 B2 JPH0250964 B2 JP H0250964B2
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- JP
- Japan
- Prior art keywords
- aqueous solution
- compound
- blowing air
- powder
- magnetic 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 - Lifetime
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- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Hard Magnetic Materials (AREA)
Description
〔産業上の利用分野〕
本発明は金属磁性粉末の製造法に係り、更に詳
しくは高密度記録に適した、保磁力(Hc)が700
〜1200 Oeの鉄を基とする金属磁性粉末の製造法
に関するものである。
〔従来の技術〕
現在使用されている磁気記録媒体は極めて多様
であり、用いられている磁性粉末に要求される特
性もそれぞれ異なつている。従来より磁気記録媒
体に使用されている強磁性粉末としてはγ―
Fe2O3、Coドープγ―Fe2O3、Fe3O4、Coドープ
Fe3O4、Fe3O4―γ―Fe2O3、CrO2等があるが、
これらの磁性粉末は保磁力、飽和磁束密度等に限
界があるため近年強磁性金属粉末(メタル粉)が
その保持力及び飽和磁束密度等の高さの故に注目
されている。
〔発明が解決しようとする問題点〕
これら金属磁性粉末の保磁力は通常1100〜1300
Oeの範囲にあり、その保持力の高さ故にメタル
対応以外のオーデイオ機器、ビデオ機器、デジタ
ル機器等には使用できないと云う欠点を有してい
る。
又、磁気記録は高密度化の方向にあり、高密度
の磁気記録を達成するためには磁性粉を更に微小
化する必要がある。しかし、従来の金属磁性粉末
は通常針状であり、その長軸長は1〜10μと高密
度化を達成するには不充分な大きさである。
そこでこの金属磁性粉末を微細化し高密度化を
達成せんとすると保磁力が更に高くなつてしまう
上に表面特性が低下するため分散性が悪くなり実
用的でなくなる。
〔問題点を解決するための手段〕
本発明者等は上記欠点を解消し、メタル対応以
外のオーデイオ機器、ビデオ機器、デジタル用機
器等にも使用可能で且つ高密度記録を達成し得る
金属磁性粉末を製造するため鋭意研究をし、本発
明を完成することができたのである。
金属磁性粉末の製造法としては従来から次の様
な方法が検討されて来た。
(1) 金属の有機酸塩(主としてシユウ酸塩)を熱
分解し、還元性気体で還元する方法。
(2) オキシ水酸化鉄、或いはこれに他の金属を含
有させたもの、或いは酸化鉄又はフエライト組
成酸化物を還元性気体で還元する方法。
(3) 強磁性金属合金を不活性ガス中で蒸発させる
方法。
(4) 金属カルボニ化合物を分解する方法。
(5) 水酸電解法によつて強磁性金属粉末を電析さ
せた後、Hgを分離する方法。
(6) 強磁性金属塩をその溶液中で水素化ホウ素ナ
トリウム、次亜リン酸ナトリウム等により湿式
還元する方法。
(7) 衝撃大電流を通じて放電爆発によつて強磁性
粉末を生じさせる方法。
これらの方法の中で、工業性、経済性を考慮し
た場合、特に(2)の方法が有望であり、本発明の金
属磁性粉末を製造する方法もこの製造法に属する
方法である。
即ち本発明は第1鉄塩溶液に炭酸ソーダを含む
水溶液を混合し、空気を吹き込み種結晶を析出さ
せ、更に苛性ソーダ水溶液を加えて空気を吹き込
むことによつて結晶を成長させたα―FeOOH
に、Si化合物及び/又はAl化合物を被着させた
後、水素気流中300〜600℃の温度で還元すること
を特徴とする金属磁性粉末の製法及び第1鉄塩溶
液に苛性ソーダを含む水溶液を混合し、空気を吹
き込み種結晶を析出させ、更に炭酸ソーダ水溶液
を加えて空気を吹き込むことによつて結晶を成長
させたα―FeOOHに、Si化合物及び/又はAl化
合物を被着させた後、水素気流中300〜600℃の温
度で還元することを特徴とする金属磁性粉末の製
法を提供するものである。
次に本発明の方法の好ましい実施態様を詳しく
述べると、先ず塩化第1鉄、硫酸第1鉄等の第1
鉄塩溶液に炭酸ソーダ又は苛性ソーダを添加し、
空気を吹き込んで種結晶を析出させ、次いで、炭
酸ソーダを使用した場合は苛性ソーダ、苛性ソー
ダを使用した場合には炭酸ソーダを添加して空気
を吹き込み結晶を成長させたα―FeOOHに、水
溶性Si化合物及び/又はAl化合物をSiO2及び/
又はAl2O3として0.05〜5wt%被着させる。被着
はSi化合物又はAl化合物と充分接触させるだけ
でも効果は認められるが、更に効果を上げるため
には懸濁後、上記水溶性のSi化合物又はAl化合
物がアルカリ性であるならば酸で、又逆にこれら
の化合物が酸性であればアルカリで全中和もしく
は部分中和させる方法を採るべきである。又α―
FeOOHの分散性を向上させるためにオレイン酸
ソーダ、アルギン酸ソーダ等の界面活性剤を用い
ることにより、更に効果を上げることができる。
尚、使用し得る水溶性Si化合物としてはケイ酸
ソーダ、シリカゾル、コロイダルシリカ等、Al
化合物としてはアルミナゾル、アルミン酸ソー
ダ、塩化アルミニウム、硫酸アルミニウム等を挙
げることができる。
以上の方法により製造したα―FeOOHを
過・洗浄・乾燥し、600℃を越えない温度、好ま
しくは500℃以下で水素気流中で還元をする。還
元温度については実用的な下限はないが、低温に
おいては反応が非常にゆつくり進むので反応時間
が長くなりすぎて好ましくなく、少なくとも300
℃以上で還元するのが適当である。
還元後、還元器を冷却して、例えば空気1%及
び窒素99%の混合ガスを還元器に導入し、徐々に
空気含有量を増し4〜5時間後に空気だけに切り
換え還元器から取り出す。以上の方法により本発
明の金属磁性粉末を製造することができる。
尚、本発明においては特にα―FeOOHの製造
を種結晶の生成及び結晶の成長の二段階で行うこ
とにより結晶の大きさ、形態を調節しているの
で、保磁力を特定範囲内にすると共に角形比
(σr/σs)を高水準に維持できる特徴を有してい
るのである。
〔実施例〕
以下実施例により本発明を詳しく説明する。
実施例及び比較例
0.5mol/のNa2CO3水溶液24及び0.5mol/
のFeCl2水溶液16を50の反応器に入れ40℃
まで昇温した後、空気を15/min吹込み、酸化
反応を行い、酸化率が25%に達した時点で
4mol/のNaOH水溶液2を加え、更に酸化
率100%まで行ない生成したα―FeOOHを別、
洗浄、乾燥した。これを試料1とした。
上記方法において酸化率50%、75%に達した時
点でNaOH水溶液を加えたものを試料2,3と
し、酸化率100%迄、即ちNaOHを加えずに行つ
たものを試料4とした。
次に1.0mol/のNaOH水溶液24及び
0.5mol/のFeCl2水溶液16を50の反応器に
入れ、40℃まで昇温した後、空気を15/min吹
き込み酸化反応を行い、酸化率25%に達した時点
で2mol/のNa2CO3水溶液2を加え、更にに
酸化反応を酸化率100%まで行い、生成したα―
FeOOHを別、洗浄、乾燥した。これを試料5
とした。
又、上記方法において酸化率50%、75%に達し
た時点でNa2CO3水溶液を加えたものを試料6,
7とし、酸化率100%迄、即ちNa2CO3を加えず
に行つたものを試料8とした。
以上の試料1〜8を各89g、6の水に懸濁
し、これに100g/(SiO2換算)ケイ酸ソーダ
水溶液を40ml加え、塩酸で中和後、過、洗浄し
150℃を超えない温度で乾燥した。この様にして
得られたα―FeOOH各50gを3/minの水素
気流中で420℃で6時間かけて還元した。
還元終了後、反応器を室温まで冷却し、空気1
%及び窒素99%の混合ガスを反応器に導入し、約
30分間隔で混合ガス中の空気量を段階的に増し、
5時間後に空気のみに切換え磁性粉を反応器から
取り出し、印加磁場10KOeで磁気特性を測定し
た。結果を第1表に示す。
[Industrial Application Field] The present invention relates to a method for producing metal magnetic powder, and more specifically, it relates to a method for producing metal magnetic powder, and more specifically, it is suitable for high-density recording and has a coercive force (Hc) of 700.
The present invention relates to a method for producing iron-based metal magnetic powders of ~1200 Oe. [Prior Art] The magnetic recording media currently in use are extremely diverse, and the characteristics required of the magnetic powder used are also different. The ferromagnetic powder conventionally used in magnetic recording media is γ-
Fe 2 O 3 , Co-doped γ-Fe 2 O 3 , Fe 3 O 4 , Co-doped
There are Fe 3 O 4 , Fe 3 O 4 -γ-Fe 2 O 3 , CrO 2 , etc.
Since these magnetic powders have limitations in coercive force, saturation magnetic flux density, etc., ferromagnetic metal powder (metal powder) has recently attracted attention due to its high coercive force, saturation magnetic flux density, etc. [Problem to be solved by the invention] The coercive force of these metal magnetic powders is usually 1100 to 1300.
Oe range, and because of its high holding power, it has the disadvantage that it cannot be used in audio equipment, video equipment, digital equipment, etc. that are not compatible with metal. Furthermore, magnetic recording is trending toward higher density, and in order to achieve higher density magnetic recording, it is necessary to further miniaturize magnetic powder. However, conventional metal magnetic powders are usually needle-shaped and have a major axis length of 1 to 10 microns, which is insufficient to achieve high density. Therefore, if this metal magnetic powder is made finer and higher density is not achieved, the coercive force will further increase and the surface properties will deteriorate, resulting in poor dispersibility, making it impractical. [Means for Solving the Problems] The present inventors have solved the above-mentioned drawbacks, and have developed a metal magnetic material that can be used in audio equipment, video equipment, digital equipment, etc. other than those compatible with metal, and can achieve high-density recording. They conducted extensive research to produce powder and were able to complete the present invention. Conventionally, the following methods have been considered for producing metal magnetic powder. (1) A method of thermally decomposing metal organic acid salts (mainly oxalates) and reducing them with reducing gas. (2) A method of reducing iron oxyhydroxide, or iron oxyhydroxide containing other metals, or iron oxide or ferrite composition oxide with a reducing gas. (3) A method of vaporizing a ferromagnetic metal alloy in an inert gas. (4) A method for decomposing metal carbonic compounds. (5) A method in which Hg is separated after ferromagnetic metal powder is electrodeposited by hydroxyl electrolysis. (6) A method in which a ferromagnetic metal salt is wet-reduced in its solution using sodium borohydride, sodium hypophosphite, etc. (7) A method in which ferromagnetic powder is produced by discharge explosion through a large impact current. Among these methods, method (2) is particularly promising when considering industrial efficiency and economic efficiency, and the method for producing the metal magnetic powder of the present invention also belongs to this production method. That is, the present invention involves mixing an aqueous solution containing sodium carbonate with a ferrous salt solution, blowing air to precipitate seed crystals, and then adding an aqueous caustic soda solution and blowing air to grow crystals.
A method for producing a metal magnetic powder characterized by depositing a Si compound and/or an Al compound and then reducing the powder at a temperature of 300 to 600°C in a hydrogen stream, and adding an aqueous solution containing caustic soda to a ferrous salt solution. After mixing and blowing air to precipitate seed crystals, and then adding an aqueous sodium carbonate solution and growing crystals by blowing air, a Si compound and/or an Al compound was deposited on the α-FeOOH. The present invention provides a method for producing metal magnetic powder, which is characterized by reducing the metal magnetic powder at a temperature of 300 to 600°C in a hydrogen stream. Next, a preferred embodiment of the method of the present invention will be described in detail. First, ferrous chloride, ferrous sulfate, etc.
Adding soda carbonate or caustic soda to the iron salt solution,
Seed crystals are precipitated by blowing air into the α-FeOOH, and then caustic soda is added if sodium carbonate is used, or soda carbonate is added if caustic soda is used, and air is blown into the α-FeOOH to grow crystals. compound and/or Al compound with SiO 2 and/or
Alternatively, 0.05 to 5 wt% of Al 2 O 3 is deposited. For adhesion, the effect can be seen just by sufficient contact with the Si compound or Al compound, but to further increase the effect, after suspending, if the water-soluble Si compound or Al compound is alkaline, use an acid or Conversely, if these compounds are acidic, a method of total or partial neutralization with an alkali should be adopted. Also α-
The effect can be further improved by using a surfactant such as sodium oleate or sodium alginate to improve the dispersibility of FeOOH. In addition, water-soluble Si compounds that can be used include sodium silicate, silica sol, colloidal silica, etc.
Examples of the compound include alumina sol, sodium aluminate, aluminum chloride, and aluminum sulfate. The α-FeOOH produced by the above method is filtered, washed and dried, and then reduced in a hydrogen stream at a temperature not exceeding 600°C, preferably 500°C or less. There is no practical lower limit for the reduction temperature, but at low temperatures the reaction proceeds very slowly and the reaction time becomes too long, which is undesirable.
It is appropriate to reduce at temperatures above ℃. After reduction, the reducer is cooled, and a mixed gas of, for example, 1% air and 99% nitrogen is introduced into the reducer, the air content is gradually increased, and after 4 to 5 hours, the gas is switched to only air and taken out from the reducer. The metal magnetic powder of the present invention can be produced by the method described above. In addition, in the present invention, the size and morphology of the crystals are controlled by manufacturing α-FeOOH in two steps: generation of seed crystals and growth of crystals, so that the coercive force is kept within a specific range and It has the characteristic that the squareness ratio (σ r /σ s ) can be maintained at a high level. [Example] The present invention will be explained in detail with reference to Examples below. Examples and Comparative Examples 0.5 mol/Na 2 CO 3 aqueous solution 24 and 0.5 mol/
Put an aqueous solution of FeCl2 into a reactor at 50 °C and 40 °C.
After raising the temperature to
Add 4 mol/NaOH aqueous solution 2, further oxidize until the oxidation rate reaches 100%, and separate the generated α-FeOOH.
Washed and dried. This was designated as sample 1. Samples 2 and 3 were obtained by adding NaOH aqueous solution when the oxidation rate reached 50% and 75% in the above method, and Sample 4 was carried out until the oxidation rate reached 100%, that is, without adding NaOH. Next, 1.0 mol/NaOH aqueous solution 24 and
A 0.5 mol/FeCl 2 aqueous solution 16 was placed in a 50°C reactor, heated to 40°C, air was blown at 15/min to perform an oxidation reaction, and when the oxidation rate reached 25%, 2 mol/Na 2 CO 3Aqueous solution 2 was added, and the oxidation reaction was further carried out to an oxidation rate of 100%, resulting in α-
The FeOOH was separated, washed, and dried. Sample 5
And so. In addition, in the above method, when the oxidation rate reached 50% and 75%, Na 2 CO 3 aqueous solution was added to sample 6,
Sample 8 was obtained by increasing the oxidation rate to 100%, that is, without adding Na 2 CO 3 . Samples 1 to 8 above were suspended in 89 g each in 6 portions of water, 40 ml of 100 g/(SiO 2 equivalent) aqueous sodium silicate solution was added, neutralized with hydrochloric acid, filtered, and washed.
Dry at a temperature not exceeding 150°C. Each 50 g of α-FeOOH thus obtained was reduced at 420° C. for 6 hours in a hydrogen flow of 3/min. After the reduction is complete, the reactor is cooled to room temperature and air 1
% and 99% nitrogen into the reactor, approximately
Gradually increase the amount of air in the mixed gas at 30 minute intervals.
After 5 hours, the atmosphere was switched to air only, the magnetic powder was taken out from the reactor, and its magnetic properties were measured with an applied magnetic field of 10 KOe. The results are shown in Table 1.
本発明の方法によれば、保磁力が700〜1200Oe
の範囲であり、角形比も高水準の高密度記録に適
した金属磁性粉末を容易に得ることができる。
According to the method of the present invention, the coercive force is 700 to 1200 Oe.
It is possible to easily obtain a metal magnetic powder suitable for high-density recording with a high squareness ratio.
Claims (1)
合し、空気を吹き込み種結晶を析出させ、更に苛
性ソーダ水溶液を加えて空気を吹き込むことによ
つて結晶を成長させたα―FeOOHに、Si化合物
及び/又はAl化合物を被着させた後、水素気流
中300〜600℃の温度で還元することを特徴とする
金属磁性粉末の製法。 2 第1鉄塩溶液に苛性ソーダを含む水溶液を混
合し、空気を吹き込み種結晶を析出させ、更に炭
酸ソーダ水溶液を加えて空気を吹き込むことによ
つて結晶を成長させたα―FeOOHに、Si化合物
及び/又はAl化合物を被着させた後、水素気流
中300〜600℃の温度で還元することを特徴とする
金属磁性粉末の製法。[Claims] 1. α which is prepared by mixing an aqueous solution containing soda carbonate with a ferrous salt solution, blowing air to precipitate seed crystals, and then adding a caustic soda aqueous solution and blowing air to grow crystals. - A method for producing metal magnetic powder, which is characterized by depositing a Si compound and/or an Al compound on FeOOH and then reducing it in a hydrogen stream at a temperature of 300 to 600°C. 2. Mixing an aqueous solution containing caustic soda with a ferrous salt solution, blowing air to precipitate seed crystals, and then adding a sodium carbonate aqueous solution and blowing air to grow crystals. and/or a method for producing metal magnetic powder, which comprises depositing an Al compound and then reducing the powder at a temperature of 300 to 600°C in a hydrogen stream.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59128939A JPS619506A (en) | 1984-06-22 | 1984-06-22 | Manufacture of magnetic metallic powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59128939A JPS619506A (en) | 1984-06-22 | 1984-06-22 | Manufacture of magnetic metallic powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS619506A JPS619506A (en) | 1986-01-17 |
| JPH0250964B2 true JPH0250964B2 (en) | 1990-11-06 |
Family
ID=14997141
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59128939A Granted JPS619506A (en) | 1984-06-22 | 1984-06-22 | Manufacture of magnetic metallic powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS619506A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6367704A (en) * | 1986-09-09 | 1988-03-26 | Nissan Chem Ind Ltd | Manufacture of highly dispersive magnetic iron powder |
-
1984
- 1984-06-22 JP JP59128939A patent/JPS619506A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS619506A (en) | 1986-01-17 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |