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JPS61261217A - Production of magnetoplumbite-type ferrite powder - Google Patents

Production of magnetoplumbite-type ferrite powder

Info

Publication number
JPS61261217A
JPS61261217A JP60102689A JP10268985A JPS61261217A JP S61261217 A JPS61261217 A JP S61261217A JP 60102689 A JP60102689 A JP 60102689A JP 10268985 A JP10268985 A JP 10268985A JP S61261217 A JPS61261217 A JP S61261217A
Authority
JP
Japan
Prior art keywords
alkoxide
ferrite powder
magnetoplumbite
ferrous
type ferrite
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
JP60102689A
Other languages
Japanese (ja)
Inventor
Yoshiharu Ozaki
尾崎 義治
Mitsuyuki Wadasako
三志 和田迫
Yoshinori Shinohara
篠原 義典
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.)
Mitsubishi Mining and Cement Co Ltd
Original Assignee
Mitsubishi Mining and Cement Co Ltd
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 Mitsubishi Mining and Cement Co Ltd filed Critical Mitsubishi Mining and Cement Co Ltd
Priority to JP60102689A priority Critical patent/JPS61261217A/en
Publication of JPS61261217A publication Critical patent/JPS61261217A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To obtain the titled ferrite powder having fine particle size, uniform composition and high purity, by hydrolyzing a ferrous alkoxide and other bivalent metal alkoxide, oxidizing the product, and calcining the produced oxide. CONSTITUTION:A mixture of a ferrous alkoxide and alkoxide of one or more kinds of bivalent metals selected from Ba, Sr and Pb is hydrolyzed in nitrogen stream at 0-100 deg.C by dripping water to the mixture. The obtained hydrolysis product is oxidized by passing oxygen or an oxygen-containing gas through the suspension of the product. The oxidized product is separated and calcined at 700-1,000 deg.C to obtain the objective magnetoplumbite-type ferrite powder having an impurity content of <=0.1% and particle diameter of 0.06-0.3mum.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、第一鉄アルコキシドと2価金属のアルコキシ
ドを用いて液相反応によりマグネトプランバイト (l
agnetaplu層bite)型フェライト粉末を製
造する方法に関する。更に詳しくは、磁性材料として適
するマグネトプランバイト型フェライト粉末の製造方法
に関するものである。
Detailed Description of the Invention [Industrial Application Field] The present invention provides magnetoplumbite (l
The present invention relates to a method for producing agnetaplu layer (bite) type ferrite powder. More specifically, the present invention relates to a method for producing magnetoplumbite-type ferrite powder suitable as a magnetic material.

[従来の技術] 従来、マグネトプランバイト型フェライトのような鋭錐
状六方晶系のフェライト粉末は磁気特性に優れているた
め、磁性材料として利用できることが知られている。
[Prior Art] It has been known that ferrite powder having an acute pyramidal hexagonal system, such as magnetoplumbite ferrite, has excellent magnetic properties and can therefore be used as a magnetic material.

従来、この種の材料に利用されるマグネトプランバイト
型フェライト粉末の製造方法としては、一般に2価金属
の炭酸塩と酸化鉄を均一に混合してこの混合物を130
0℃以上の高温で仮焼して固相反応させた後、粉砕する
方法がある。
Conventionally, the method for producing magnetoplumbite-type ferrite powder used for this type of material is to uniformly mix divalent metal carbonate and iron oxide, and then process the mixture to 130%
There is a method of calcining at a high temperature of 0° C. or higher to cause a solid phase reaction, and then pulverizing.

[発明が解決しようとする問題点] 近年、電子部品に対し、より小型で高度な特性が要求さ
れるようになり、従ってそれに使用される原料粉末も、
従来に増して組成の均一性、高純度の微粒子であること
が必要になってきている。
[Problems to be solved by the invention] In recent years, electronic parts have been required to be smaller and have more advanced characteristics, and therefore the raw material powder used for them has also become smaller.
More than ever before, it has become necessary to have fine particles with uniform composition and high purity.

しかし、上記従来の方法により得られたマグネトプラン
バイト型フェライト粉末は、微視的に観察した場合に、
高温の仮焼により粒子径が大きくなり、また固相反応で
あるため組成が不均質になり、その特性を安定させるこ
とは困難であった。
However, when the magnetoplumbite-type ferrite powder obtained by the above conventional method is observed microscopically,
The particle size increases due to high-temperature calcination, and the composition becomes inhomogeneous due to the solid phase reaction, making it difficult to stabilize its properties.

また製造中に不純物が混入し易く、磁性材料としての特
性が低下してしまう問題点があった。
Further, there is a problem that impurities are easily mixed in during manufacturing, and the properties as a magnetic material are deteriorated.

本発明の目的は、マグネトプランバイト型フェライト粉
末を比較的低温で、均一な組成にかつ高純度で微粒に製
造し得る製造方法を提供することにある。
An object of the present invention is to provide a method for producing magnetoplumbite-type ferrite powder with a uniform composition, high purity, and fine particles at a relatively low temperature.

[問題点を解決するための手段] 本発明は、第一鉄アルコキシドと第一鉄以外の他の2価
金属のアルコキシドを加水分解し、この加水分解生成物
を酸化した後、仮焼してマグネトプランバイト型フェラ
イト粉末を得る方法である。
[Means for solving the problems] The present invention involves hydrolyzing a ferrous alkoxide and an alkoxide of a divalent metal other than ferrous, oxidizing the hydrolyzed product, and then calcining the product. This is a method for obtaining magnetoplumbite type ferrite powder.

なお上記2価金属は、Ba、 Sr、 Pbの中から選
ばれたl又は2以上の金属がマグネトプランバイトを形
成するため好ましい、また上記アルコキシドの加水分解
は、上記アルコキシドが分解せず、かつ取扱いの容易な
0〜100℃の温度範囲で行われることが好ましい。更
に上記加水分解生成物の酸化は、加水分解生成物が分解
しない0〜200℃の温度範囲で行われることが好まし
い。
The divalent metal is preferably one or more metals selected from Ba, Sr, and Pb because they form magnetoplumbite, and the hydrolysis of the alkoxide is performed so that the alkoxide does not decompose and It is preferable to carry out the treatment in a temperature range of 0 to 100°C, which is easy to handle. Further, the oxidation of the hydrolyzed product is preferably carried out at a temperature range of 0 to 200°C at which the hydrolyzed product does not decompose.

なお本明細書では、「アルコキシド」とはアルコールの
OH基の水素原子を金属原子で置換した化合物をいう。
In this specification, "alkoxide" refers to a compound in which the hydrogen atom of the OH group of an alcohol is replaced with a metal atom.

本発明の出発原料は、第一鉄アルコキシドと2価金属の
アルコキシドである。この2価金属のアルコキシドは、
第一鉄以外の他の2価金属のアルコキシドである。 F
e以外の他の2価金属はマグネトプランバイトを形成す
るBa、 Sr、 Pbの中から選ばれたl又は2以上
の金属がよい、第一鉄アルコキシド及び第一鉄以外の他
の2価金属のアルコキシドの加水分解は、第一鉄アルコ
キシドと第一鉄以外の他の2価金属のアルコキシドとを
同時に加水分解させる。
The starting materials of the present invention are ferrous alkoxides and divalent metal alkoxides. This divalent metal alkoxide is
It is an alkoxide of a divalent metal other than ferrous iron. F
Other divalent metals other than e are preferably l or two or more metals selected from Ba, Sr, and Pb that form magnetoplumbite, ferrous alkoxide and other divalent metals other than ferrous iron. The hydrolysis of the alkoxide simultaneously hydrolyzes ferrous alkoxide and alkoxides of divalent metals other than ferrous.

この加水分解は、特に窒素気流中で行うことが第一鉄の
酸化を防止する上で好ましく、また溶液  (中に水を
直接追加することにより行うことができる他、加圧容器
から吹出す水蒸気流に接触させる方法でも行うことがで
きる。また加水分解のための反応温度は、加圧しない状
態では上記アルコキシドが分解せず、しかも取扱いの容
易な0〜100℃が好ましく、特に好ましくは25〜1
00℃である。加圧して行う場合或いは水蒸気流に接触
させる方法では100〜200℃が適当である。
This hydrolysis is preferably carried out in a nitrogen stream to prevent oxidation of ferrous iron, and it can also be carried out by directly adding water to the solution (water vapor blown out from a pressurized container). The reaction temperature for hydrolysis is preferably 0 to 100°C, and particularly preferably 25 to 100°C, since the alkoxide does not decompose in the absence of pressure and is easy to handle. 1
It is 00℃. In the case of applying pressure or contacting with a steam stream, a temperature of 100 to 200°C is appropriate.

上記加水分解生成物の酸化は、加水分解生成物の懸濁液
に酸素、又は酸素と他の気体とを含む気体、例えば空気
等を流通させることにより行う。
The above-mentioned oxidation of the hydrolysis product is carried out by passing oxygen or a gas containing oxygen and another gas, such as air, through the suspension of the hydrolysis product.

酸化条件は、出発原料の種類及び組合わせ、又は目的物
質の種類によって異なる。
Oxidation conditions vary depending on the type and combination of starting materials or the type of target substance.

所定の酸化を終了した後は、加水分解生成物を遠心分離
又は濾過により加水分解液から分離し、必要により真空
乾燥等の乾燥を行い、700℃〜1000℃で仮焼する
ことにより微粒の粉末が得られる。
After completing the specified oxidation, the hydrolyzed product is separated from the hydrolyzed liquid by centrifugation or filtration, dried by vacuum drying if necessary, and calcined at 700°C to 1000°C to form fine powder. is obtained.

上記反応により得られた加水分解生成物及び700℃前
後で仮焼した粉末の構造をX線回折により調べると、加
水分解生成物は非晶質であり、仮焼した粉末は結晶質の
マグネトプランバイト型フェライト粉末で示される。こ
のマグネトプランバイト型フェライト粉末の粒径は電子
顕微鏡観察によると、700℃の仮焼テ0.08pm 
、 1000”C(7)仮焼で0.1〜0.3gmの微
粒子である。仮焼温度が高くなるほど粒成長により粒子
間に相互作用が生じて組成のバラツキが見られる傾向が
ある。
When the structure of the hydrolyzed product obtained by the above reaction and the powder calcined at around 700°C was examined by X-ray diffraction, it was found that the hydrolyzed product was amorphous, and the calcined powder was crystalline magnetopran. Indicated by bite-type ferrite powder. According to electron microscopy, the particle size of this magnetoplumbite-type ferrite powder was 0.08 pm when calcined at 700°C.
, 1000''C(7) calcined to produce fine particles of 0.1 to 0.3 gm.The higher the calcining temperature, the more interaction occurs between particles due to grain growth, and the composition tends to vary.

また得られたマグネトプランバイト型フェライト粉末は
、化学分析の結果1粒子ひとつひとつが調合した組成と
ほぼ一致する極めて均一な粒子であり、しかも不純物0
.1%以下の高純度の物質である。
Furthermore, chemical analysis of the obtained magnetoplumbite-type ferrite powder revealed that each particle was extremely uniform, with almost the same composition as the prepared one, and contained no impurities.
.. It is a highly pure substance of 1% or less.

[発明の効果] 以上述べたように、本発明によれば、第一鉄アルコキシ
ドと第一鉄以外の他の2価金属のアルコキシドを加水分
解し、この加水分解生成物を酸・化した後、仮焼してマ
グネトプランバイト型フェライト粉末を得ることにより
、微粒で組成が極めて均一なマグネトプランバイト型フ
ェライト粉末を高純度で製造することができる優れた効
果がある。
[Effects of the Invention] As described above, according to the present invention, after hydrolyzing a ferrous alkoxide and an alkoxide of a divalent metal other than ferrous and oxidizing the hydrolyzed product, By calcining to obtain magnetoplumbite-type ferrite powder, there is an excellent effect that magnetoplumbite-type ferrite powder with fine particles and extremely uniform composition can be manufactured with high purity.

[実施例] 次に本発明の具体的態様を示すために、本発明を実施例
によりさらに詳しく説明するが、以下に示す例はあくま
でも一例であって、これにより本発明の技術的範囲を限
定するものではない。
[Examples] Next, in order to show specific embodiments of the present invention, the present invention will be explained in more detail using Examples, but the examples shown below are merely examples, and do not limit the technical scope of the present invention. It's not something you do.

〈実施例1〉 無水FeCIt 1.OOgとBaC1z 0.14g
とを脱水したエタノール100mJl中に溶解し、更に
この溶液中に化学量論比の金属ナトリウム0.39gを
加え、70℃で1時間還流しながら反応させた。置換反
応が行われて、第一鉄エトキシドFe(OEt)2及び
バリウムエトキシドBa(OEt)2を得た。
<Example 1> Anhydrous FeCIt 1. OOg and BaC1z 0.14g
was dissolved in 100 mJl of dehydrated ethanol, and 0.39 g of stoichiometric sodium metal was added to this solution, followed by reaction at 70° C. for 1 hour under reflux. A substitution reaction was carried out to obtain ferrous ethoxide Fe(OEt)2 and barium ethoxide Ba(OEt)2.

こうして得たFe(OEt)2及びBa(OEt)zに
脱炭酸した100m lの蒸留水を少量ずつ滴下して、
窒素気流中で加水分解したところ、沈殿物が生成した。
100 ml of decarboxylated distilled water was added dropwise to the thus obtained Fe(OEt)2 and Ba(OEt)z,
Hydrolysis in a nitrogen stream produced a precipitate.

この沈殿物の生じた懸濁溶液を70℃にしたまま、この
懸濁溶液に200m JL /winの流量で2時間空
気を流し、沈殿物の空気酸化を行った。この空気酸化し
た沈殿物を濾過により加水分解液から分離洗浄した後、
70℃で1時間乾燥して粉末を得た。
While the temperature of the suspended solution containing the precipitate was kept at 70° C., air was passed through the suspended solution at a flow rate of 200 m JL/win for 2 hours to perform air oxidation of the precipitate. After separating and washing this air-oxidized precipitate from the hydrolyzate by filtration,
It was dried at 70°C for 1 hour to obtain a powder.

得られた粉末の構造をX線回折により調べたところ、乾
燥した粉末は非晶質であり、 700℃の仮焼によりB
aFetz OIIで示されるマグネトプランバイト型
フェライト粉末であった。
When the structure of the obtained powder was examined by X-ray diffraction, it was found that the dried powder was amorphous, and B
It was a magnetoplumbite type ferrite powder designated as aFetz OII.

〈実施例2〉 無水FeCl21.00gと5rCh O,10gとを
脱水したエタノール100m i中に溶解し、更にこの
溶液中に化学量論比の金属ナトリウム0.39gを加え
、70℃で1時間還流しながら反応させた。置換反応が
行われて、第一鉄エトキシドFe(OEt) 2及びス
トロンチウムエトキシド5r(OEt)2を得た。
<Example 2> 1.00 g of anhydrous FeCl and 10 g of 5rCh O were dissolved in 100 m i of dehydrated ethanol, and 0.39 g of metallic sodium in a stoichiometric ratio was added to this solution, and the mixture was refluxed at 70°C for 1 hour. I reacted while doing so. A substitution reaction was carried out to yield ferrous ethoxide Fe(OEt) 2 and strontium ethoxide 5r(OEt) 2 .

こうして得たFe(OEt)2及び5r(OEthを実
施例1と同様に加水分解したところ、沈殿物が生成した
。この沈殿物を実施例1と同様に空気酸化した。この空
気酸化した沈殿物を濾過により加水分解液から分離洗浄
した後、70℃で1時間乾燥して粉末を得た。
When the thus obtained Fe(OEt)2 and 5r(OEth) were hydrolyzed in the same manner as in Example 1, a precipitate was generated.This precipitate was air oxidized in the same manner as in Example 1.This air oxidized precipitate It was separated and washed from the hydrolyzate by filtration, and then dried at 70°C for 1 hour to obtain a powder.

得られた粉末の構造をX線回折により調べたところ、乾
燥した粉末は非晶質であり、700℃の仮焼により5r
Fet* Otsで示されるマグネトプランバイト型フ
ェライト粉末であった。
When the structure of the obtained powder was investigated by X-ray diffraction, it was found that the dried powder was amorphous, and that it was
It was a magnetoplumbite type ferrite powder indicated by Fet*Ots.

〈実施例3〉 無水FeC1z 1.00gとPb(CHsCOO)z
O,11gとを脱水したエタノール100m l中に溶
解し、更にこの溶液中に化学量論比の金属ナトリウム0
.39gを加え、70℃で1時間還流しながら反応させ
た。置換反応が行われて、第一鉄エトキシドFe(OE
t)z及び鉛エトキシドPb(OEt)2を得た。
<Example 3> Anhydrous FeC1z 1.00g and Pb(CHsCOO)z
In addition, a stoichiometric ratio of metallic sodium was dissolved in 100 ml of dehydrated ethanol.
.. 39 g was added, and the mixture was reacted under reflux at 70° C. for 1 hour. A substitution reaction is carried out to form ferrous ethoxide Fe (OE
t)z and lead ethoxide Pb(OEt)2 were obtained.

こうして得たFe(OEt)z及びPb(OEt)tを
実施例1と同様に加水分解したところ、沈殿物が生成し
た。この沈殿物を実施例1と同様に空気酸化した。この
空気酸化した沈殿物を濾過により加水分解液から分離洗
浄した後、70℃で1時間乾燥して粉末を得た。
When Fe(OEt)z and Pb(OEt)t thus obtained were hydrolyzed in the same manner as in Example 1, a precipitate was generated. This precipitate was air oxidized in the same manner as in Example 1. This air-oxidized precipitate was separated and washed from the hydrolyzate by filtration, and then dried at 70° C. for 1 hour to obtain a powder.

得られた粉末の構造をX線回折により調べたところ、乾
燥した粉末は非晶質であり、700℃の仮焼によりPb
Fetz Otsで示されるマグネトプランバイト型フ
ェライト粉末であった。
When the structure of the obtained powder was investigated by X-ray diffraction, it was found that the dried powder was amorphous and that Pb
It was a magnetoplumbite type ferrite powder shown by Fetz Ots.

実施例1〜3で得られた粉末を電子顕微鏡により、それ
ぞれの粒径を測定したところ、いずれも加水分解生成物
は0.005〜0.011L鵬であり、 700℃の仮
焼で0.0B〜0.08#Lmの六角板状の微粒子であ
り、 1000℃の仮焼で0.1−0.3.層の六角板
状の微粒子であることが観察された。更に化学分析を行
った結果、各微粒子の組成は調合した組成と一致し、し
かも不純物が0.1%以下の高純度の物質であった。
When the particle size of each of the powders obtained in Examples 1 to 3 was measured using an electron microscope, the hydrolyzed product was 0.005 to 0.011 L, and the particle diameter was 0.005 to 0.011 when calcined at 700°C. It is a hexagonal plate-shaped fine particle of 0B to 0.08 #Lm, and has a particle size of 0.1 to 0.3 when calcined at 1000°C. It was observed that the particles were hexagonal plate-shaped particles. Further chemical analysis revealed that the composition of each fine particle matched the prepared composition and was a highly pure substance with impurities of 0.1% or less.

特許出願人  三菱鉱業セメント株式会社代理人  弁
理士  須 1)正 義ツ、。
Patent applicant Mitsubishi Mining Cement Co., Ltd. Representative Patent attorney Su 1) Masayoshi.

(外2名)′(2 others)'

Claims (2)

【特許請求の範囲】[Claims] (1)第一鉄アルコキシドと第一鉄以外の他の2価金属
のアルコキシドを加水分解し、この加水分解生成物を酸
化した後、仮焼してマグネトプランバイト型フェライト
粉末を得るマグネトプランバイト型フェライト粉末の製
造方法。
(1) Hydrolyzing ferrous alkoxide and alkoxides of divalent metals other than ferrous, oxidizing the hydrolysis product, and then calcining to obtain magnetoplumbite-type ferrite powder. Method for manufacturing type ferrite powder.
(2)2価金属のアルコキシドは、Ba、Sr、Pbの
中から選ばれた1又は2以上の金属である特許請求の範
囲第1項に記載のマグネトプランバイト型フェライト粉
末の製造方法。
(2) The method for producing magnetoplumbite-type ferrite powder according to claim 1, wherein the divalent metal alkoxide is one or more metals selected from Ba, Sr, and Pb.
JP60102689A 1985-05-16 1985-05-16 Production of magnetoplumbite-type ferrite powder Pending JPS61261217A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60102689A JPS61261217A (en) 1985-05-16 1985-05-16 Production of magnetoplumbite-type ferrite powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60102689A JPS61261217A (en) 1985-05-16 1985-05-16 Production of magnetoplumbite-type ferrite powder

Publications (1)

Publication Number Publication Date
JPS61261217A true JPS61261217A (en) 1986-11-19

Family

ID=14334213

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60102689A Pending JPS61261217A (en) 1985-05-16 1985-05-16 Production of magnetoplumbite-type ferrite powder

Country Status (1)

Country Link
JP (1) JPS61261217A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63210031A (en) * 1987-02-27 1988-08-31 Tdk Corp Ferrite powder and magnetic recording medium

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6054924A (en) * 1983-09-02 1985-03-29 Sentan Kako Kikai Gijutsu Shinko Kyokai Production of manganese ferrite
JPS6054925A (en) * 1983-09-02 1985-03-29 Sentan Kako Kikai Gijutsu Shinko Kyokai Production of magnetopumbite type ferrite

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6054924A (en) * 1983-09-02 1985-03-29 Sentan Kako Kikai Gijutsu Shinko Kyokai Production of manganese ferrite
JPS6054925A (en) * 1983-09-02 1985-03-29 Sentan Kako Kikai Gijutsu Shinko Kyokai Production of magnetopumbite type ferrite

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63210031A (en) * 1987-02-27 1988-08-31 Tdk Corp Ferrite powder and magnetic recording medium

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