JPS62119116A - Production of lepidocrocite - Google Patents

Production of lepidocrocite

Info

Publication number
JPS62119116A
JPS62119116A JP60201377A JP20137785A JPS62119116A JP S62119116 A JPS62119116 A JP S62119116A JP 60201377 A JP60201377 A JP 60201377A JP 20137785 A JP20137785 A JP 20137785A JP S62119116 A JPS62119116 A JP S62119116A
Authority
JP
Japan
Prior art keywords
soln
alkali
lepidocrocite
blowing
gas
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
Application number
JP60201377A
Other languages
Japanese (ja)
Other versions
JPH0329011B2 (en
Inventor
Norio Koike
紀夫 小池
Yoji Matsue
松江 洋司
Koji Shibuya
浩司 渋谷
Toshiko Suzuki
鈴木 寿子
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP60201377A priority Critical patent/JPS62119116A/en
Publication of JPS62119116A publication Critical patent/JPS62119116A/en
Publication of JPH0329011B2 publication Critical patent/JPH0329011B2/ja
Granted legal-status Critical Current

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

Abstract

PURPOSE:To obtain lepidocrocite suitable for the production of magnetic iron oxide powder for a magnetic recording medium by adding the alkali aq. soln. of the prescribed amount to a ferrous chloride aq. soln. and thereafter ageing the mixture under the specified conditions and blowing O2-contg. gas therein and furthermore adding the alkali soln. and also blowing O2-contg. gas therein. CONSTITUTION:The alkali aq. soln. such as caustic alkali and NH3 is added to a ferrous chloride aq. soln. in 0.4-0.7 times of theoretical amount necessary for the formation of ferrous hydroxide. Then while stirring this processing liquid in the nonoxidizing atmosphere such as inert gas atmosphere, it is aged by keeping it for 20-120min under the conditions of 6.0-9.0 pH value and 10-50 deg.C temp. Thereafter the seed crystal of gamma-FeOOH (lepidocrocite) is formed by blowing O2-contg. gas to the processing liquid after the maturation. gamma-FeOOH forming reaction is completely finished by adding the above-mentioned alkali aq. soln. to the above-mentioned matured liquid formed with the seed crystal and also blowing O2-contg. gas therein. Thereby lepidocrocite is obtained which is small in grain size distribution and has excellent properties having stably the required various grain sizes.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はレピッドクロサイト(γ−F’ e OOH)
の製造に係り、より詳細には、オーディオテープ、ビデ
オテープ、磁気カード等の磁気記録媒体用磁性酸化鉄粉
を製造する際に出発物質として好適なレピッドクロサイ
トの製造方法に関するものである。
[Detailed description of the invention] (Industrial application field) The present invention is directed to lepidocrocite (γ-F' e OOH)
More specifically, the present invention relates to a method for producing lepidocrocite, which is suitable as a starting material when producing magnetic iron oxide powder for magnetic recording media such as audio tapes, video tapes, and magnetic cards.

(従来の技術及び解決しようとする問題点)一般に、オ
ーディオテープ、ビデオテープ、磁気カート等の磁気記
録媒体用の磁性酸化鉄粉は。
(Prior Art and Problems to be Solved) Generally, magnetic iron oxide powder for magnetic recording media such as audio tapes, video tapes, magnetic carts, etc.

a−FeOOH(ゲータイト)又はY−FeOOH(レ
ピッドクロサイト)を出発物質とし、これに焼成(脱水
、焼きしめ)、還元及び酸化などの処理を順次に施して
針状のγ−Fe、o、(マクヘマイト)を得、或いはそ
の粒子表面にコバルト変成処理によってコバルト被着し
たCo−γ−Fe、0.を得ることにより、製造されて
いる。この場合、得られた磁性酸化鉄粉の磁気特性は上
記出発物質の性状に依存するため、磁気記録媒体に適し
た磁性酸化鉄粉末を得るには、優れた性状の出発物質を
使用する必要がある。
Using a-FeOOH (goethite) or Y-FeOOH (lepidocrocite) as a starting material, this is sequentially subjected to treatments such as calcination (dehydration, baking), reduction, and oxidation to produce acicular γ-Fe, o , (makuhemite), or Co-γ-Fe with cobalt deposited on the particle surface by cobalt modification treatment, 0. It is manufactured by obtaining In this case, the magnetic properties of the obtained magnetic iron oxide powder depend on the properties of the above-mentioned starting material, so in order to obtain magnetic iron oxide powder suitable for magnetic recording media, it is necessary to use a starting material with excellent properties. be.

この点、従来、レピッドクロサイト(γ−FeOOH)
を出発物質として/l)られる磁性酸化鉄粉末は、ゲー
タイト(α−F e O01−I )を出発物質とする
場合に比らべ、最終製品であるオーディオテープ、ビデ
オテープ等々の磁気記録媒体の磁気的配向性、分散性、
角形比、転写特性は優れているにも拘わらず、粒度分布
が大きいという問題があり、最終製品の特性(保磁力、
反転磁界強度分布等)に悪影響を及ぼすという欠点があ
った。
In this respect, conventionally, lepidocrocite (γ-FeOOH)
The magnetic iron oxide powder prepared using . magnetic orientation, dispersion,
Although the squareness ratio and transfer characteristics are excellent, there is a problem of large particle size distribution, and the properties of the final product (coercive force,
This has the disadvantage of having an adverse effect on the reversal magnetic field strength distribution, etc.).

ところで、上記出発物質のうちのレピッドクロサイトは
1通常、以下のような合成反応法で製造されている。
By the way, among the above starting materials, lepidocrocite is usually produced by the following synthetic reaction method.

まず、酸洗廃液等を利用して得られる塩化第一鉄(Fe
CQ□)水Ifj液に苛性アルカリ又はアンモニア等の
アルカリ水溶液を加えて中和する。この際。
First, ferrous chloride (Fe) obtained using pickling waste liquid etc.
CQ□) Add an alkaline aqueous solution such as caustic alkali or ammonia to the water Ifj liquid to neutralize it. On this occasion.

水酸基と鉄のモル比(OI−I/Fe)が約0.20〜
0.35となるようにアルカリ水溶液を混合する。
The molar ratio of hydroxyl group to iron (OI-I/Fe) is about 0.20~
An alkaline aqueous solution is mixed so that the concentration is 0.35.

次いで、これをMi含有ガス(空気又は酸素)で酸化し
てシート反応により種結晶をつくる。このときの反応温
度は約10〜25℃とする。シード反応が終了に近づく
と、反応液のP Hが低下し、アルカリ分が完全に消費
されて反応が終ると、P I−I値は約3.2〜3.8
となる。
Next, this is oxidized with a Mi-containing gas (air or oxygen) to produce seed crystals through a sheet reaction. The reaction temperature at this time is about 10-25°C. As the seed reaction approaches completion, the pH of the reaction solution decreases, and when the alkaline content is completely consumed and the reaction ends, the P I-I value will be approximately 3.2 to 3.8.
becomes.

その後、30〜50℃に昇温し、PH値が約3.5〜4
.5になるように酸素含有ガスを吹込むと共にアルカリ
水溶液を添加して成長反応を行う。
After that, the temperature is raised to 30-50℃, and the pH value is about 3.5-4.
.. A growth reaction is carried out by blowing in an oxygen-containing gas and adding an alkaline aqueous solution so that the concentration of the alkali becomes 5.5.

この成長反応が終了に近づくと、反応速度が遅くなり、
PH値が上!1する。P H値が約5.5になった時点
で反応の終了とし、針状のレピッドクロサイトを得る。
As this growth reaction approaches completion, the reaction rate slows down,
PH value is high! Do 1. The reaction is terminated when the pH value reaches approximately 5.5, and needle-like lepidocrocite is obtained.

しかし乍ら、上記方法では、前述の如く粒度分布が大き
いレピッドクロサイトしか得られず、良好な性状とは言
えず、更には平均粒度をコントロールすることが困難で
あるため、用途目的に適した任意の平均粒度を有するレ
ピッドクロサイトを提供できないという欠点があった。
However, as mentioned above, with the above method, only lepidocrocite with a large particle size distribution can be obtained, which cannot be said to have good properties, and furthermore, it is difficult to control the average particle size, so it is not suitable for the purpose of use. However, there was a drawback that lepidocrocite having an arbitrary average particle size could not be provided.

このため、磁性酸化鉄粉末の製造の出発物質としてはゲ
ータイト(α−Fe○○H)が多用されているのが現状
である。
For this reason, goethite (α-Fe○○H) is currently frequently used as a starting material for the production of magnetic iron oxide powder.

本発明は、前述の如く多くの利点を有するレピッドクロ
サイトにつき、上記従来技術の欠点を解消し、粒度分布
が小さく、かつ、要求される各種粒度を安定的に有する
優れた性状のレピッドクロサイトを製造する方法を提供
することを目的とするものである。
The present invention solves the drawbacks of the prior art and produces lepidocrocite, which has many advantages as described above, and has excellent properties such as a small particle size distribution and stably having various required particle sizes. The purpose of the present invention is to provide a method for producing docrosite.

(問題点を解決するための手段) 上記目的を達成するため、本発明では、塩化第一鉄水溶
液とアルカリ水溶液を混合するとレピッドクロサイト ス]−が生じるが、この結晶粒径の均一性をコントロー
ルすれば、以降の工程におけるレピッドクロサイトの種
結晶の生成及び成長に好結果をもたらすことを知見し、
そのためにシード反応前に該混合水溶液を特定条件にて
保持する熟成」工程を設けることを骨子とするものであ
る。
(Means for Solving the Problems) In order to achieve the above object, in the present invention, when a ferrous chloride aqueous solution and an alkali aqueous solution are mixed, lepidocrocytos]- is produced, but the uniformity of the crystal grain size is We found that controlling this will bring about good results in the production and growth of lepidocrocite seed crystals in the subsequent steps,
For this purpose, the key point is to provide a "ripening" step in which the mixed aqueous solution is maintained under specific conditions before the seed reaction.

以下に本発明を実施例に基づいて詳細に説明する。The present invention will be explained in detail below based on examples.

本発明における熟成工程は、塩化第一鉄水溶液にアルカ
リ水溶液を加える混合工程と、酸素含有ガスで酸化して
シード反応によりレピッドクロサイトの種結晶を生成さ
せるシード反応工程との間に行うもので、混合水溶液の
1−’ H値が6.0〜9.0. 温度が10〜50℃
の範囲内で 20〜120分間保持する。勿論、シート
反応ではないので、不活性ガス雰囲気等の非酸化性8囲
気中で行い、また撹拌しつつ行うことは云うまでもない
The aging process in the present invention is carried out between the mixing process of adding an alkaline aqueous solution to the ferrous chloride aqueous solution and the seeding reaction process of oxidizing with an oxygen-containing gas and generating seed crystals of lepidocrocite through a seed reaction. The 1-' H value of the mixed aqueous solution is 6.0 to 9.0. Temperature is 10-50℃
Hold within the range of 20 to 120 minutes. Of course, since this is not a sheet reaction, it goes without saying that it is carried out in a non-oxidizing atmosphere such as an inert gas atmosphere, and is carried out with stirring.

混合撹拌状態は1例えば、撹拌羽根の回転数200〜4
0Orpmとする程度で良い。
The mixing and stirring state is 1. For example, the rotation speed of the stirring blade is 200 to 4.
It is sufficient to set it to 0 rpm.

なお、保持時間は、20分未満ではグリーンラストの結
晶粒径の均一化の効果がなく、しかし、120分を超え
て保持しても上記効果がそれ以上期待できず、処理時間
の延長化をもたらすだけであるので、20〜120分間
の範囲内とし、好ましくは30分以上100分以内で保
持する。また、混合水溶液のP H値及び温度が上記範
囲外では、ゲータイトが発生したり、粒子の針状性が悪
化するので、比較的低温で弱酸もしくは弱アルカリの上
記範囲内で行う必要がある。
It should be noted that if the holding time is less than 20 minutes, there is no effect of making the grain size of green last uniform.However, if the holding time is held for more than 120 minutes, the above effect cannot be expected any longer, so it is necessary to extend the treatment time. The holding time is within the range of 20 to 120 minutes, preferably 30 minutes to 100 minutes. Furthermore, if the pH value and temperature of the mixed aqueous solution are outside the above range, goethite may be generated or the acicularity of the particles may deteriorate, so it is necessary to carry out the process at a relatively low temperature and with a weak acid or a weak alkali within the above range.

また、上記P I−I値、温度及び保持時間を適宜設定
することにより、グリーンラストの結晶粒径の大きさを
コントロールすることも可能であり、したがって、出発
原料の塩化第一鉄の溶液濃度等々の条件選定と相俟って
得られるレピッドクロサイトの平均粒度をコントロール
することができる。
In addition, by appropriately setting the P I-I value, temperature, and holding time, it is possible to control the crystal grain size of green last, and therefore, the solution concentration of ferrous chloride, which is the starting material, can be controlled. The average particle size of the lepidocrocite obtained can be controlled by selecting conditions such as the following.

本発明における熟成工程以外の工程は、従来と同様であ
り、特にそれらの条件は制限されない。
The steps other than the aging step in the present invention are the same as conventional ones, and the conditions are not particularly limited.

但し、塩化第一鉄を水酸化第一鉄にするのに要するアル
カリの理論量は、シード反応工程と成長工程とに分けて
添加するが、シード反応工程で添加する量は、ゲータイ
トの発生を防止し、針状性の優れたレピッドクロサイト
の粒子を得るため、上記理論量の0.4〜0.7倍とす
る必要がある。
However, the theoretical amount of alkali required to convert ferrous chloride to ferrous hydroxide is added separately in the seed reaction step and the growth step, but the amount added in the seed reaction step is determined to prevent the generation of goethite. In order to prevent this and obtain lepidocrocite particles with excellent acicularity, the amount needs to be 0.4 to 0.7 times the above theoretical amount.

(実施例) 人1j1− 濃度0.97モル/Qの塩化第一鉄水溶液25Qを窒素
ガス雰囲気に保った反応器内で撹拌しながら、濃度0.
71モル/12の水酸化すトリウム水溶液42Ωを添加
し、PH値7.6.温度13℃で60分間撹拌しつつ保
持して熟成させた。
(Example) Person 1j1- While stirring a ferrous chloride aqueous solution 25Q having a concentration of 0.97 mol/Q in a reactor maintained in a nitrogen gas atmosphere, the concentration was 0.97 mol/Q.
A 42Ω aqueous solution of 71 mol/12 thorium hydroxide was added, and the pH value was 7.6. The mixture was maintained at a temperature of 13°C for 60 minutes with stirring to ripen.

この熟成の後、5気圧(ゲージ圧)の空気を20Q/m
inの速度で吹き込んで酸化させ、シード反応を行った
。この間、液温は13℃にコントロールした。
After this aging, air at 5 atm (gauge pressure) is supplied at 20 Q/m.
A seed reaction was carried out by blowing at a rate of 0.25 in to oxidize. During this time, the liquid temperature was controlled at 13°C.

シード反応の終了をPH値の測定で確認した後(PII
=3.2)、空気の吹込みを止め、1.5気圧(ゲージ
圧)の窒素ガスを3Q/minの速度で吹き込み1反応
器内を不活性雰囲気にし、撹拌しつつ48℃に昇温した
After confirming the completion of the seed reaction by measuring the PH value (PII
=3.2), stop blowing air, blow nitrogen gas at 1.5 atm (gauge pressure) at a rate of 3 Q/min to create an inert atmosphere inside reactor 1, and raise the temperature to 48°C while stirring. did.

その後、窒素ガスに代えて、5気圧(ゲージ圧)の空気
を3Ω/minの速度で吹き込むと共に濃度1.6モル
/Qの水酸化ナトリウム水溶液を80ε/minの一定
速度で添加し、成長反応を行なった。
Thereafter, instead of nitrogen gas, air at 5 atm (gauge pressure) was blown at a rate of 3Ω/min, and a sodium hydroxide aqueous solution with a concentration of 1.6 mol/Q was added at a constant rate of 80ε/min to cause a growth reaction. I did it.

この成長反応はPH値が5.5に上昇した時点で終了し
た。
This growth reaction ended when the pH value rose to 5.5.

大漁狙1 濃度1.0モル/Qの塩化第一鉄水溶液25Qを窒素ガ
ス雰囲気に保った反応器内で撹拌しながら、濃度0.8
モル/Qのアンモニア水溶液41Qを添加し、PH値7
.5、温度13℃で60分間撹拌しつつ保持して熟成さ
せた。この熟成の後、5気圧(ゲージ圧)の空気を20
 Q / mibの速度で吹き込んで酸化させ、シード
反応を行った。この間、液温は13℃にコントロールし
た。
Big Catch Aim 1 While stirring 25Q of ferrous chloride aqueous solution with a concentration of 1.0 mol/Q in a reactor maintained in a nitrogen gas atmosphere,
Add mol/Q ammonia aqueous solution 41Q, pH value 7
.. 5. The mixture was maintained at a temperature of 13° C. for 60 minutes with stirring to ripen. After this aging, air at 5 atmospheres (gauge pressure) is added for 20 minutes.
A seed reaction was performed by blowing at a rate of Q/mib for oxidation. During this time, the liquid temperature was controlled at 13°C.

シード反応の終了をPH値の測定で確認した後(PH=
3.4)、空気の吹込みを止め、1.5気圧(ゲージ圧
)の窒素ガスを3Q7’+inの速度で吹き込み、反応
器内を不活性雰囲気にし、撹拌しつつ45℃に昇温した
After confirming the completion of the seed reaction by measuring the PH value (PH=
3.4) Stop blowing air, blow nitrogen gas at 1.5 atm (gauge pressure) at a rate of 3Q7'+in to create an inert atmosphere inside the reactor, and raise the temperature to 45°C while stirring. .

その後、窒素ガスに代えて、5気圧(ゲージ圧)の空気
を312/minの速度で吹き込むと共に濃度1.6モ
ル/Qの水酸化ナトリウム水溶液を80g/minの一
定速度で添加し、成長反応を行った。
Thereafter, instead of nitrogen gas, air at 5 atm (gauge pressure) was blown at a rate of 312/min, and an aqueous sodium hydroxide solution with a concentration of 1.6 mol/Q was added at a constant rate of 80 g/min to cause a growth reaction. I did it.

この成長反応はP H値が5.5に上昇した時点で終了
した。
This growth reaction was terminated when the pH value rose to 5.5.

え献上口。An offering mouth.

実施例1において、塩化第一鉄と水酸化ナトリウムとの
混合水溶液を、熟成させずに、直ちにシード反応工程に
供し、以降、同様の処理を行った。
In Example 1, the mixed aqueous solution of ferrous chloride and sodium hydroxide was immediately subjected to the seed reaction step without being aged, and the same treatment was performed thereafter.

比較例2 実施例2において、塩化第一鉄とアンモニアとの混合水
溶液を、熟成させずに、直ちにシード反応工程に供し、
以降、同様の処理を行った。
Comparative Example 2 In Example 2, the mixed aqueous solution of ferrous chloride and ammonia was immediately subjected to a seed reaction step without aging,
Thereafter, similar processing was performed.

以上の4例で得た各々のレピッドクロサイトについて、
電子顕微銀にて粒子の粒径を測定し1粒度分布を求めた
。その結果を第1表に示す。なお、粒度分布は針状のレ
ピッドクロサイト粒子の長軸方向の粒度分布における標
準偏差値で表わし、平均粒径は粒度分布の平均値で表わ
した。
Regarding each lepidochrosite obtained in the above four cases,
The particle size of the particles was measured using a silver electron microscope to obtain a particle size distribution. The results are shown in Table 1. The particle size distribution was expressed by the standard deviation value of the particle size distribution in the long axis direction of the acicular lepidocrocite particles, and the average particle size was expressed by the average value of the particle size distribution.

第1表 同表に示すところから明らかなように、得られたレピッ
ドクロサイトの粒度分布は、比較例に比べ、熟成工程を
有する本発明例の場合の方が遥かに小さく、均一であり
、優れた性状であることを表わしている。また、この、
熟成の効果はアルカリの種類(水酸化ナトリウム又はア
ンモニア)によらず同様に期待でき、更には平均粒径が
小さい場合(実施例1)でも大きい場合(実施例2)で
も、小さな粒度分布のものが得られる。
As is clear from Table 1, the particle size distribution of the obtained lepidocrocite is much smaller and more uniform in the case of the present invention example which has a ripening process compared to the comparative example. , indicating excellent properties. Also, this
The effect of aging can be expected to be the same regardless of the type of alkali (sodium hydroxide or ammonia), and even if the average particle size is small (Example 1) or large (Example 2), the effect of aging can be expected to be the same regardless of the type of alkali (sodium hydroxide or ammonia). is obtained.

(発明の効果) 以上詳述したように、本発明によれば、レピッドクロサ
イトの合成反応においてシード反応前に特定条件の熟成
工程を経るので、任意の平均粒径を有し、しかも粒度分
布が極めて小さい優れた性状の針状レピッドクロサイト
を安定して製造することができ、したがって、優れた特
性の磁性酸化鉄粉末の製造を可能にするものである。
(Effects of the Invention) As described in detail above, according to the present invention, in the synthesis reaction of lepidocrocite, an aging step under specific conditions is performed before the seed reaction, so that the lepidocrocite can have an arbitrary average particle size, and Acicular lepidocrocite with excellent properties and extremely small distribution can be stably produced, and therefore magnetic iron oxide powder with excellent properties can be produced.

Claims (1)

【特許請求の範囲】[Claims] 塩化第一鉄水溶液に苛性アルカリ、アンモニア等のアル
カリ水溶液を、該塩化第一鉄を水酸化第一鉄にするのに
要する理論量の0.4〜0.7倍加えた後、PH値6.
0〜9.0及び温度10〜50℃の条件のもとで20〜
120分間保持して熟成し、次いで酸素含有ガスを吹込
んでγ−FeOOHの種結晶を生成させ、更に上記アル
カリ水溶液を加えると共に酸素含有ガスを吹込んでγ−
FeOOH生成反応を完結させることを特徴とするレピ
ッドクロサイトの製造方法。
After adding an alkaline aqueous solution such as caustic alkali or ammonia to the ferrous chloride aqueous solution, the pH value is 6. ..
20 to 9.0 under the conditions of 0 to 9.0 and temperature 10 to 50°C
It was held for 120 minutes to ripen, then an oxygen-containing gas was blown in to generate γ-FeOOH seed crystals, and the alkali aqueous solution was added and an oxygen-containing gas was blown in to form γ-FeOOH.
A method for producing lepidocrocite, which comprises completing a FeOOH production reaction.
JP60201377A 1985-09-11 1985-09-11 Production of lepidocrocite Granted JPS62119116A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60201377A JPS62119116A (en) 1985-09-11 1985-09-11 Production of lepidocrocite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60201377A JPS62119116A (en) 1985-09-11 1985-09-11 Production of lepidocrocite

Publications (2)

Publication Number Publication Date
JPS62119116A true JPS62119116A (en) 1987-05-30
JPH0329011B2 JPH0329011B2 (en) 1991-04-22

Family

ID=16440062

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60201377A Granted JPS62119116A (en) 1985-09-11 1985-09-11 Production of lepidocrocite

Country Status (1)

Country Link
JP (1) JPS62119116A (en)

Also Published As

Publication number Publication date
JPH0329011B2 (en) 1991-04-22

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