JPH0216248B2 - - Google Patents
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- Publication number
- JPH0216248B2 JPH0216248B2 JP478484A JP478484A JPH0216248B2 JP H0216248 B2 JPH0216248 B2 JP H0216248B2 JP 478484 A JP478484 A JP 478484A JP 478484 A JP478484 A JP 478484A JP H0216248 B2 JPH0216248 B2 JP H0216248B2
- Authority
- JP
- Japan
- Prior art keywords
- barium ferrite
- barium
- ferrite powder
- temperature
- firing
- 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
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- Compounds Of Iron (AREA)
- Hard Magnetic Materials (AREA)
Description
【発明の詳細な説明】
本発明は、水熱合成法でマグネトプランバイト
型バリウムフエライト粉末を製造する方法の改良
に関するものである。
近年磁気記録の高密度化の要求に伴い、バリウ
ムフエライト(マグネトプランバイト型)を磁気
記録媒体として用いる垂直磁気記録方式の開発が
進められている。
垂直磁気記録方式に用いられるバリウムフエラ
イトとしては、保持力が適当な値(500〜1500e)
で、飽和磁化ができるだけ高く、粒子が小さく均
一で、粒子の凝集、焼結などがなく、分散性のよ
いものが望まれている。
従来バリウムフエライトの製造法としては、例
えば共沈法、フラツクス法、水熱合成法など種々
の方法が知られており、水熱合成法については、
例えば特公昭46−3545号公報、特開昭56−149328
号公報、特開昭56−160328号公報、特開昭58−
2224号公報などで提案されている。
水熱合成法によるバリウムフエライトは粒子の
凝集がなく比較的分散性はよいが、従来公知の方
法では粒径が大きなものしかできなかつたり、飽
和磁化が50emu/g程度かそれよりも低いものし
か得られなかつたり、またバリウムフエライトの
結晶化を進行させるために高温焼成が必要になつ
たり、さらには高温焼成するために粒子間の焼結
が生じ易くなつたりして分散性が悪くなつたりす
る難点がある。
本発明者らは、これらの実情に鑑み、粒径が小
さく、粒子の凝集、焼結などがなく、分散性のよ
い電磁特性のすぐれたバリウムフエライト粉末を
製造することを目的として研究を行つた結果、バ
リウムイオンと鉄イオンとの含有割合、アルカリ
添加量など特定の条件で水熱合成を行い、これに
塩化ナトリウムおよび塩酸を加えてPHを7〜10に
して乾燥した後、生成物を650〜850℃で焼成し、
焼成物を洗浄、乾燥することによつて上述の目的
を達成できるバリウムフエライト粉末が得られる
ことを知り、本発明に到つた。
本発明は、バリウム1グラム原子に対して鉄5
〜10グラム原子をイオンの状態で含む金属塩の水
溶液に、該金属塩の総量に対して1〜5倍当量の
アルカリを含む溶液を加え、140〜230℃に加熱保
持した後、塩化ナトリウムおよび塩酸を加えてPH
を7〜10に保持し、次いで乾燥して生成物を650
〜850℃で焼成した後、洗浄、乾燥することを特
徴とするバリウムフエライト粉末の製法に関する
ものである。
本発明によると、水熱合成時の加熱が一度でか
つ焼成操作を伴わない方法、例えば特公昭46−
3545号公報、特開昭56−149328号公報に記載の方
法による場合よりも特に高い飽和磁化を示すバリ
ウムフエライト粉末粒子が得られ、また特公昭46
−3545号公報に記載の方法による場合よりも粒径
の小さなものが得られる。また本発明によると、
特開昭56−160328号公報に記載の方法による場合
よりも粒子が焼結したりするのを防止するのが容
易である。
本発明において、バリウム1グラム原子に対し
て鉄5〜10グラム原子をイオンの状態で含む金属
塩の水溶液の調製は、一般に硝酸第二鉄、塩化第
二鉄、硝酸バリウム、塩化バリウムの如き水に可
溶性で比較的溶解度の高い金属塩をバリウムイオ
ンと鉄イオンとが前記範囲になるように水に溶解
させる方法で行われる。その際従来のバリウムフ
エライトに添加されている種々の元素、例えば
Co,Ni,Mn,Zn,Ca,Pb,Sr,Ti,In,Nb
などの水に可溶性の塩を若干添加してもよく、特
にCo,Ti,Mn,Caなどの添加は、磁気特性の
向上および粒子径をコントロールするうえで好ま
しい。バリウムと鉄との原子比Fe/Baが5より
も小さくなるとマグネトプランバイト型バリウム
フエライトの生成量が少なく、六角板状の形状も
悪くなり、Fe/Baが10より大きくなるとα―
Fe2O3の生成があり、またバリウムフエライトの
粒径も大きく、磁気特性も劣つてくる。またバリ
ウムおよび鉄をイオンの状態で含む金属塩の水溶
液を調製する場合は、バリウム塩の濃度が30〜
150mmol/lの範囲になるようにするのが六角
板状の形状のよいバリウムフエライトを得るうえ
で望ましい。
バリウムおよび鉄をイオンの状態で含む金属塩
の水溶液は加温、好ましくは30〜90℃に加温し、
これにアルカリを含む溶液を加える。アルカリを
含む溶液の添加量は前記金属塩の総量に対して1
〜5倍当量になるようにする。アルカリの量が少
なすぎるとγ―Fe2O3の生成があり、また多すぎ
ると経済的でないので好ましくない。添加するア
ルカリを含む溶液のアルカリ成分としては、水酸
化ナトリウム、水酸化カリウムなどが好適であ
る。
本発明においてアルカリを含む溶液を加えた
後、まず140〜230℃、好ましくは150〜220℃に加
熱保持する。この加熱保持時間は0.5〜5時間程
度で十分であり、加熱保持によつて核となるバリ
ウムフエライトの結晶(沈殿物)が生成する。な
おこの結晶は化学組成的にはマグネトプランバイ
ト型のバリウムフエライトと同じ構造を有してい
るが、磁気特性は悪い。加熱保持温度が上記温度
より低いと核となる結晶の生成が十分でなく、ま
た高くしすぎると最終的に得られるバリウムフエ
ライトの粒径が大きくなるので適当でない。また
この加熱保持はアルカリを含む溶液添加後、上記
温度にまですみやかに昇温して行うのが望まし
く、加熱保持には一般にはオートクレーブが採用
される。
140〜230℃での加熱保持によつてバリウムフエ
ライトの微細な種晶となる沈殿物を生成させた
後、塩化ナトリウムおよび塩酸を加えて、PHを7
〜10に保持する。この塩化ナトリウムは上記沈殿
物に対し10〜80重量%、好ましくは20〜70重量%
添加するのが望ましい。添加量が少なすぎると焼
結しやすいので、望ましくなく、また多すぎると
経済的でない。
また塩酸は過剰のアルカリ分を中和するために
添加するもので、塩酸の希釈水溶液によつて、上
記スラリーのPHを7〜10に調節するように添加す
ることが好ましい。特に塩酸の水溶液は1〜5%
の濃度のものが望ましい。塩化ナトリウムと塩酸
の添加の順序は限定されないが塩化ナトリウムを
先に添加することが好ましい。
塩化ナトリウムおよび塩酸を添加することによ
つてPH7〜10にしたスラリーはろ過および洗浄を
せずになるべく早く乾燥する。この乾燥は水分の
除去が主目的であり、通常50〜200℃の温度で、
1〜20時間程度行うのが好ましい。乾燥方法とし
ては、一般に知られた方法が採用されるが、特に
ドラムドライヤーやスプレードライヤーによつて
迅速に乾燥することが好ましい。
乾燥によつて得られるバリウムフエライトの種
晶を含有する生成物(乾燥物)は、これを650〜
850℃、好ましくは700〜830℃の温度で焼成する。
焼成温度が低すぎると目的物を得るために長時間
を要したり、また得られたものの飽和磁化が低
い。また高すぎると粒子の成長が大きく、粒子径
の大きいものが得られる。焼成時間は1〜30時間
程度が適当であり、また焼成雰囲気は限定され
ず、焼成は空気雰囲気下で行なうことができる。
また焼成する場合、一度低温(650〜750℃)で焼
成し、さらに高温(750〜850℃)で焼成する2段
焼成が好ましい。
650〜850℃で焼成した焼成物(バリウムフエラ
イト)は、これを洗浄、乾燥する。洗浄は焼成物
中のアルカリ金属イオン、過剰の水酸化バリウム
など不純物を十分に除去できればどのような方法
で行つてもよい。洗浄液としては水や酢酸、硝
酸、塩酸などを用いることができる。十分に洗浄
した焼成物は次いで乾燥するが、乾燥方法は特に
制限されない。
乾燥によつて目的とする結晶状態のよい六角板
状のマグネトプランバイト型の粒径0.3μ以下の小
さい均一なバリウムフエライト粉末を得ることが
できる。またこのバリウムフエライト粉末は分散
性がよく、板状比は1/3〜1/10の範囲にあ
り、700〜12000eの保磁力および高い飽和磁化を
示す。更に、保磁力については、従来バリウムフ
エライトに添加されている前記した種種の元素
(例えば、Co,Ti等)を添加することにより自由
にコントロールすることができる。
実施例 1
内容3の四つ口フラスコに硝酸バリウム
〔Ba(NO3)2〕57.9g、硝酸第二鉄〔Fe(NO3)・
9H2O〕581.8g、硝酸コバルト〔Co(NO3)・
6H2O〕33.2g、四塩化チタン〔TiCl4〕24.1gお
よび水800mlを入れ、窒素ガス雰囲気下に撹拌し
ながら約80℃に加温し、硝酸バリウムおよび硝酸
第二鉄を溶解させ、撹拌下に水酸化ナトリウム
〔NaOH〕218.3gを水400mlに溶解させた溶液を
徐々に滴下した。水酸化ナトリウム水溶液の滴下
によつて沈殿物が生成した。
沈殿物を含む溶液を撹拌下に80℃で10分間保持
し、オートクレーブに入れ、約1時間で200℃に
まで昇温し、1時間同温度に保持した後、スラリ
ーを2ビーカーに移し、これに塩化ナトリウム
364gを加え、さらに濃度5%の塩酸水溶液を
徐々に加えてスラリーのPHを約8にした。このよ
うにして得られたスラリーをドラムドライヤーに
て乾燥(濃縮乾固)した。
得られた乾燥物は、これを電気炉に入れ、空気
雰囲気下に800℃で10時間焼成した。この焼成物
を水によつて可溶物がなくなるまで洗浄した後ろ
過乾燥し、バリウムフエライト粉末を得た。この
バリウムフエライト粉末について透過型電子顕微
鏡(TEM)で粒子形状(粒径、厚さ)を測定し
た結果(粒子20個の平均値)および振動試料式磁
力計で磁気特性を測定した結果を第1表に示す。
また分散性をみるためにバリウムフエライト粉末
をバインダーおよび溶媒とボールミルでミーリン
グした後のインキを篩目が3μの篩でろ過したと
きのろ過率(インキ全量が篩を通過した場合をろ
過率100%とする)を測定した結果を第1表に示
す。
実施例 2
実施例1の焼成温度、時間800℃、10時間を750
℃、20時間にかえたほかは、実施例1と同様にし
てバリウムフエライト粉末を製造し、粒子形状、
磁気特性およびろ過率を測定した。その結果を第
1表に示す。
比較例 1
実施例1の硝酸第二鉄の使用量をかえて実施例
1のFe/Ba(原子比)を6から12にしたほかは、
実施例1と同様にしてバリウムフエライト粉末を
製造し、粒子形状、磁気特性およびろ過率を測定
した。その結果を第1表に示す。
比較例 2
実施例1の水酸化ナトリウムの使用量をかえて
実施例1の1.1倍当量(OH/NO3)から0.9倍当
量にかえたほかは、実施例1と同様にしてバリウ
ムフエライト粉末を製造し、粒子形状、磁気特性
およびろ過率を測定した。その結果を第1表に示
す。
比較例 3
実施例1の塩化ナトリウム添加および塩酸によ
るPH調節をせずに焼成したほかは、実施例1と同
様にしてバリウムフエライト粉末を製造し、粒子
形状、磁気特性およびろ過率を測定した。その結
果を第1表に示す。
比較例 4
実施例1の200℃での加熱保持を行わなかつた
ほかは、実施例1と同様にしてバリウムフエライ
ト粉末を製造し、粒子形状、磁気特性およびろ過
率を測定した。その結果を第1表に示す。
比較例 5
実施例1の200℃での加熱保持温度を130℃にか
えたほかは、実施例1と同様にしてバリウムフエ
ライト粉末を製造し、粒子形状、磁気特性および
ろ過率を測定した。その結果を第1表に示す。
比較例 6
実施例1の800℃での焼成温度を600℃にかえた
ほかは、実施例1と同様にしてバリウムフエライ
ト粉末を製造し、粒子形状、磁気特性およびろ過
率を測定した。その結果を第1表に示す。
比較例 7
実施例1の焼成温度800℃を900℃にかえたほか
は、実施例1と同様にしてバリウムフエライト粉
末を製造し、粒子形状、磁気特性およびろ過率を
測定した。その結果を第1表に示す。
比較例 8
実施例1の800℃での焼成を行わなかつたほか
は、実施例1と同様にしてバリウムフエライト粉
末を製造し、粒子形状、磁気特性およびろ過率を
測定した。その結果を第1表に示す。
実施例 3〜9
実施例1のFe/Ba(原子比)を6から8にかえ
た(実施例3)、OH/NO3を1.1から4にかえた
(実施例4)、加熱保持温度を200℃から180℃(実
施例5)および220℃(実施例6)にかえた、塩
化ナトリウムの添加量70重量%から50重量%(実
施例7)および20重量%(実施例8)にかえた、
焼成温度を800℃から750℃にかえた(実施例9)
ほかは、実施例1と同様にしてバリウムフエライ
ト粉末を製造し、粒子形状、磁気特性およびろ過
率を測定した。その結果を第1表に示す。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for producing magnetoplumbite-type barium ferrite powder by a hydrothermal synthesis method. In recent years, with the demand for higher density magnetic recording, development of perpendicular magnetic recording systems using barium ferrite (magnetoplumbite type) as a magnetic recording medium has been progressing. Barium ferrite used in perpendicular magnetic recording has an appropriate coercive force (500 to 1500e).
Therefore, it is desired that the saturation magnetization is as high as possible, the particles are small and uniform, there is no agglomeration or sintering of the particles, and the dispersibility is good. Conventionally, various methods are known for producing barium ferrite, such as coprecipitation method, flux method, and hydrothermal synthesis method.
For example, Japanese Patent Publication No. 46-3545, Japanese Patent Publication No. 56-149328
Publication No. 160328, Japanese Patent Application Publication No. 160328, Japanese Patent Application Publication No. 1982-
This is proposed in publications such as Publication No. 2224. Barium ferrite produced by hydrothermal synthesis has relatively good dispersibility without particle agglomeration, but conventionally known methods can only produce particles with large diameters or with a saturation magnetization of about 50 emu/g or lower. In other cases, high-temperature firing is required to advance the crystallization of barium ferrite, and furthermore, high-temperature firing tends to cause sintering between particles, resulting in poor dispersibility. There are some difficulties. In view of these circumstances, the present inventors conducted research with the aim of producing barium ferrite powder with small particle size, no particle agglomeration or sintering, good dispersibility, and excellent electromagnetic properties. As a result, hydrothermal synthesis was performed under specific conditions such as the content ratio of barium ions and iron ions and the amount of alkali added, and after adding sodium chloride and hydrochloric acid to adjust the pH to 7 to 10 and drying, the product was heated to 650 ml. Baked at ~850℃,
The inventors have discovered that a barium ferrite powder that can achieve the above-mentioned objectives can be obtained by washing and drying a fired product, and have thus arrived at the present invention. The present invention uses 5 iron for 1 gram atom of barium.
To an aqueous solution of a metal salt containing ~10 g atoms in the ionic state, a solution containing an alkali equivalent of 1 to 5 times the total amount of the metal salt was added, and after heating and holding at 140 to 230°C, sodium chloride and Add hydrochloric acid to adjust pH
is maintained at 7-10 and then dried to obtain a product at 650
The present invention relates to a method for producing barium ferrite powder, which is characterized by firing at ~850°C, followed by washing and drying. According to the present invention, a method in which heating during hydrothermal synthesis is performed only once and does not involve a calcination operation, for example,
Barium ferrite powder particles exhibiting particularly higher saturation magnetization than those obtained by the methods described in JP-A No. 3545 and JP-A-56-149328 were obtained;
It is possible to obtain smaller particles than in the method described in Japanese Patent No. 3545. Further, according to the present invention,
It is easier to prevent particles from sintering than in the method described in JP-A-56-160328. In the present invention, the preparation of an aqueous solution of a metal salt containing 5 to 10 gram atoms of iron in the form of ions per 1 gram atom of barium is generally carried out using water such as ferric nitrate, ferric chloride, barium nitrate, barium chloride, etc. This method is carried out by dissolving a relatively highly soluble metal salt in water so that barium ions and iron ions are in the above range. At that time, various elements added to conventional barium ferrite, such as
Co, Ni, Mn, Zn, Ca, Pb, Sr, Ti, In, Nb
A small amount of water-soluble salts such as Co, Ti, Mn, Ca, etc. may be added, and addition of Co, Ti, Mn, Ca, etc. is particularly preferable for improving magnetic properties and controlling particle size. When the atomic ratio Fe/Ba of barium and iron is smaller than 5, the amount of magnetoplumbite barium ferrite produced is small and the hexagonal plate-like shape becomes poor, and when Fe/Ba is larger than 10, α-
Fe 2 O 3 is generated, and the barium ferrite grain size is also large, resulting in poor magnetic properties. In addition, when preparing an aqueous solution of metal salts containing barium and iron in the ionic state, the concentration of barium salt should be
It is desirable to keep the content within the range of 150 mmol/l in order to obtain barium ferrite with a good hexagonal plate shape. An aqueous solution of a metal salt containing barium and iron in the ionic state is heated, preferably to 30 to 90°C,
Add a solution containing an alkali to this. The amount of the alkali-containing solution added is 1 to the total amount of the metal salt.
Make it ~5 times equivalent. If the amount of alkali is too small, γ-Fe 2 O 3 will be produced, and if it is too large, it is not economical, which is not preferable. As the alkali component of the alkali-containing solution to be added, sodium hydroxide, potassium hydroxide, etc. are suitable. In the present invention, after adding the alkali-containing solution, it is first heated and maintained at 140 to 230°C, preferably 150 to 220°C. A heating and holding time of about 0.5 to 5 hours is sufficient, and barium ferrite crystals (precipitates) as nuclei are formed by heating and holding. Although this crystal has the same chemical composition as magnetoplumbite-type barium ferrite, its magnetic properties are poor. If the heating and holding temperature is lower than the above temperature, the formation of core crystals will not be sufficient, and if it is too high, the grain size of the barium ferrite finally obtained will become large, which is not appropriate. Further, this heating and holding is preferably carried out by quickly raising the temperature to the above temperature after addition of the alkali-containing solution, and an autoclave is generally employed for heating and holding. After heating and holding at 140 to 230°C to generate a precipitate that will become fine seed crystals of barium ferrite, sodium chloride and hydrochloric acid are added to bring the pH to 7.
Hold at ~10. This sodium chloride is 10 to 80% by weight, preferably 20 to 70% by weight based on the above precipitate.
It is desirable to add If the amount added is too small, sintering tends to occur, which is undesirable, and if the amount is too large, it is uneconomical. Hydrochloric acid is added to neutralize excess alkaline content, and is preferably added to adjust the pH of the slurry to 7 to 10 using a dilute aqueous solution of hydrochloric acid. In particular, an aqueous solution of hydrochloric acid is 1 to 5%
It is desirable to have a concentration of . Although the order of addition of sodium chloride and hydrochloric acid is not limited, it is preferable to add sodium chloride first. The slurry, brought to a pH of 7-10 by adding sodium chloride and hydrochloric acid, is dried as quickly as possible without filtration and washing. The main purpose of this drying is to remove moisture, and it is usually at a temperature of 50 to 200 degrees Celsius.
It is preferable to carry out the treatment for about 1 to 20 hours. As the drying method, generally known methods are employed, but it is particularly preferable to dry quickly using a drum dryer or a spray dryer. The product (dried product) containing barium ferrite seed crystals obtained by drying is 650~
Calcinate at a temperature of 850°C, preferably 700-830°C.
If the firing temperature is too low, it may take a long time to obtain the desired product, or the obtained product may have low saturation magnetization. On the other hand, if the temperature is too high, the growth of particles will be large and particles with large diameters will be obtained. The firing time is suitably about 1 to 30 hours, and the firing atmosphere is not limited, and the firing can be performed in an air atmosphere.
Further, when firing, two-stage firing is preferred, in which firing is performed once at a low temperature (650 to 750°C) and then fired at a higher temperature (750 to 850°C). The fired product (barium ferrite) fired at 650-850°C is washed and dried. The cleaning may be carried out by any method as long as impurities such as alkali metal ions and excess barium hydroxide in the fired product can be sufficiently removed. As the cleaning liquid, water, acetic acid, nitric acid, hydrochloric acid, etc. can be used. The baked product that has been sufficiently washed is then dried, but the drying method is not particularly limited. By drying, it is possible to obtain the desired small, uniform barium ferrite powder having a hexagonal plate-like magnetoplumbite type particle size of 0.3 μm or less and having a good crystalline state. Moreover, this barium ferrite powder has good dispersibility, has a plate ratio in the range of 1/3 to 1/10, and exhibits a coercive force of 700 to 12,000 e and high saturation magnetization. Furthermore, the coercive force can be freely controlled by adding the various elements described above (eg, Co, Ti, etc.) that are conventionally added to barium ferrite. Example 1 57.9 g of barium nitrate [Ba(NO 3 ) 2 ] and ferric nitrate [Fe(NO 3 ).
9H 2 O〕581.8g, cobalt nitrate〔Co(NO 3 )・
Add 33.2 g of 6H 2 O, 24.1 g of titanium tetrachloride [TiCl 4 ], and 800 ml of water, and heat to approximately 80°C while stirring in a nitrogen gas atmosphere to dissolve barium nitrate and ferric nitrate, and stir. A solution of 218.3 g of sodium hydroxide (NaOH) dissolved in 400 ml of water was gradually added dropwise to the bottom. A precipitate was formed by dropping the aqueous sodium hydroxide solution. The solution containing the precipitate was kept under stirring at 80°C for 10 minutes, then placed in an autoclave, and the temperature was raised to 200°C in about 1 hour, kept at the same temperature for 1 hour, and the slurry was transferred to 2 beakers. Sodium chloride
364 g of the slurry was added thereto, and then a 5% aqueous hydrochloric acid solution was gradually added to bring the pH of the slurry to about 8. The slurry thus obtained was dried (concentrated to dryness) using a drum dryer. The obtained dried product was placed in an electric furnace and fired at 800° C. for 10 hours in an air atmosphere. This calcined product was washed with water until all soluble materials were removed, and then overdried to obtain barium ferrite powder. The results of measuring the particle shape (particle size, thickness) of this barium ferrite powder using a transmission electron microscope (TEM) (average value of 20 particles) and the magnetic properties using a vibrating sample magnetometer are shown in the first table. Shown in the table.
In addition, to examine the dispersibility, the filtration rate when the ink after milling the barium ferrite powder with the binder and solvent in a ball mill was filtered through a sieve with a sieve size of 3μ (the filtration rate is 100% when the entire amount of ink passes through the sieve). The results of the measurements are shown in Table 1. Example 2 The firing temperature and time of Example 1 were 800℃ and 750℃ for 10 hours.
Barium ferrite powder was produced in the same manner as in Example 1, except that the temperature was changed to ℃ for 20 hours, and the particle shape and
The magnetic properties and filtration rate were measured. The results are shown in Table 1. Comparative Example 1 Except that the amount of ferric nitrate used in Example 1 was changed and the Fe/Ba (atomic ratio) in Example 1 was changed from 6 to 12,
Barium ferrite powder was produced in the same manner as in Example 1, and the particle shape, magnetic properties, and filtration rate were measured. The results are shown in Table 1. Comparative Example 2 Barium ferrite powder was prepared in the same manner as in Example 1, except that the amount of sodium hydroxide used in Example 1 was changed from 1.1 times equivalent (OH/NO 3 ) to 0.9 times equivalent in Example 1. The particle shape, magnetic properties and filtration rate were measured. The results are shown in Table 1. Comparative Example 3 Barium ferrite powder was produced in the same manner as in Example 1, except that it was fired without adding sodium chloride or adjusting the pH with hydrochloric acid, and the particle shape, magnetic properties, and filtration rate were measured. The results are shown in Table 1. Comparative Example 4 Barium ferrite powder was produced in the same manner as in Example 1, except that the heating and holding at 200°C as in Example 1 was not carried out, and the particle shape, magnetic properties, and filtration rate were measured. The results are shown in Table 1. Comparative Example 5 Barium ferrite powder was produced in the same manner as in Example 1, except that the heating and holding temperature at 200°C in Example 1 was changed to 130°C, and the particle shape, magnetic properties, and filtration rate were measured. The results are shown in Table 1. Comparative Example 6 Barium ferrite powder was produced in the same manner as in Example 1, except that the firing temperature of 800°C in Example 1 was changed to 600°C, and the particle shape, magnetic properties, and filtration rate were measured. The results are shown in Table 1. Comparative Example 7 Barium ferrite powder was produced in the same manner as in Example 1, except that the firing temperature of 800°C in Example 1 was changed to 900°C, and the particle shape, magnetic properties, and filtration rate were measured. The results are shown in Table 1. Comparative Example 8 Barium ferrite powder was produced in the same manner as in Example 1, except that the firing at 800°C as in Example 1 was not performed, and the particle shape, magnetic properties, and filtration rate were measured. The results are shown in Table 1. Examples 3 to 9 Fe/Ba (atomic ratio) in Example 1 was changed from 6 to 8 (Example 3), OH/NO 3 was changed from 1.1 to 4 (Example 4), and the heating holding temperature was changed. The temperature was changed from 200°C to 180°C (Example 5) and 220°C (Example 6), and the amount of sodium chloride added was changed from 70% by weight to 50% by weight (Example 7) and 20% by weight (Example 8). Ta,
Firing temperature was changed from 800°C to 750°C (Example 9)
Otherwise, barium ferrite powder was produced in the same manner as in Example 1, and the particle shape, magnetic properties, and filtration rate were measured. The results are shown in Table 1. 【table】
Claims (1)
ム原子をイオンの状態で含む金属塩の水溶液に、
該金属塩の総量に対して1〜5倍当量のアルカリ
を含む溶液を加え、140〜230℃に加熱保持した
後、塩化ナトリウムおよび塩酸を加えてPHを7〜
10に保持し、次いで乾燥して生成物を650〜850℃
で焼成した後、洗浄、乾燥することを特徴とする
バリウムフエライト粉末の製法。1. In an aqueous solution of a metal salt containing 5 to 10 g atoms of iron in the form of ions per 1 g atom of barium,
Add a solution containing an alkali equivalent of 1 to 5 times the total amount of the metal salts, heat and maintain at 140 to 230°C, and then add sodium chloride and hydrochloric acid to bring the pH to 7 to 7.
10 and then dry the product at 650-850℃
A method for producing barium ferrite powder, which is characterized by firing, washing and drying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP478484A JPS60151224A (en) | 1984-01-17 | 1984-01-17 | Manufacture of barium ferrite powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP478484A JPS60151224A (en) | 1984-01-17 | 1984-01-17 | Manufacture of barium ferrite powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60151224A JPS60151224A (en) | 1985-08-09 |
| JPH0216248B2 true JPH0216248B2 (en) | 1990-04-16 |
Family
ID=11593430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP478484A Granted JPS60151224A (en) | 1984-01-17 | 1984-01-17 | Manufacture of barium ferrite powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60151224A (en) |
-
1984
- 1984-01-17 JP JP478484A patent/JPS60151224A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60151224A (en) | 1985-08-09 |
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