JP3078626B2 - Method for producing raw material oxide for soft ferrite - Google Patents
Method for producing raw material oxide for soft ferriteInfo
- Publication number
- JP3078626B2 JP3078626B2 JP03293022A JP29302291A JP3078626B2 JP 3078626 B2 JP3078626 B2 JP 3078626B2 JP 03293022 A JP03293022 A JP 03293022A JP 29302291 A JP29302291 A JP 29302291A JP 3078626 B2 JP3078626 B2 JP 3078626B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- oxide
- chloride
- slurry
- mixed
- 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 - Fee Related
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01F—MAGNETS; INDUCTANCES; TRANSFORMERS; SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES
- H01F1/00—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties
- H01F1/01—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials
- H01F1/03—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity
- H01F1/12—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of soft-magnetic materials
- H01F1/34—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of soft-magnetic materials non-metallic substances, e.g. ferrites
- H01F1/36—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of soft-magnetic materials non-metallic substances, e.g. ferrites in the form of particles
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Power Engineering (AREA)
- Compounds Of Iron (AREA)
- Soft Magnetic Materials (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、ソフトフェライト(以
下フェライトと略記する)用原料酸化物の製造方法に関
する。The present invention relates to a method for producing a raw material oxide for soft ferrite (hereinafter abbreviated as ferrite).
【0002】[0002]
【従来の技術】フェライト製造工程は、通常、図4にM
n−Znフェライトの製造工程を示すように、マンガ
ン,ニッケル,マグネシウム,亜鉛等の個々の酸化物又
は加熱により酸化物に変化する炭酸塩等の化合物を所定
のモル比率で混合した後に、800〜1000℃の温度
で仮焼して原料酸化物とし、粉砕、造粒、焼成すること
により構成される。なお、添加物としてSiO2 ,Ca
CO3 等が、磁気特性の制御、焼成密度を上げる等のた
めに添加される。2. Description of the Related Art Usually, a ferrite manufacturing process is performed as shown in FIG.
As shown in the production process of n-Zn ferrite, after mixing individual oxides such as manganese, nickel, magnesium, and zinc or compounds such as carbonates that change into oxides by heating at a predetermined molar ratio, It is constituted by calcining at a temperature of 1000 ° C. to obtain a raw material oxide, and pulverizing, granulating and firing. It should be noted that SiO 2 , Ca
CO 3 or the like is added for controlling magnetic properties, increasing the firing density, and the like.
【0003】しかし、この方法においては次の問題点が
ある。 (1) 0.1〜1μmの粒径の原料を混合・分散させ
るために、フェライトの組成の均一混合性が不十分とな
り製品の磁気特性を劣化させる。 (2) 800〜1000℃という高温での仮焼工程を
経るために、コスト高になる。However, this method has the following problems. (1) Since a raw material having a particle size of 0.1 to 1 μm is mixed and dispersed, the uniform mixing of the ferrite composition becomes insufficient and the magnetic properties of the product deteriorate. (2) Since the calcination process is performed at a high temperature of 800 to 1000 ° C., the cost increases.
【0004】(3) 仮焼で原料酸化物が2〜10μm
と粒成長を起こし、次工程において1μm程度に粉砕す
る際に、粉砕に長時間を要するうえに、混入する不純物
による汚染や組成のずれが避けられない。 上記従来技術の問題点である上記(2)及び(3)を改
善する原料酸化物の製造方法として、図5に示すよう
に、フェライトを構成する亜鉛以外の金属元素の塩化物
混合水溶液を出発原料として、これを酸化焙焼する製造
方法が提案されている(特公昭63−17776号)。
しかしこの方法によっても、フェライトを構成する金属
元素のうち、亜鉛は塩化物の蒸気圧が高いので、塩化
鉄、塩化マンガン等と同時に焙焼すると揮発して逸散す
るので、同時に酸化焙焼することができず、そのため後
工程において別途酸化物の形態で混合する必要があっ
た。つまり、亜鉛成分については0.1〜1μmの粒径
の酸化物を後工程において混合しなければならず工程数
が多く、かつこれらの成分については原料酸化物の均一
混合性が十分でなく組成の不均一を招き、製品の磁気特
性を劣化させるという上記(1)の問題点は解決されて
いなかった。(3) The raw material oxide is 2 to 10 μm by calcination
When pulverizing to about 1 μm in the next step, it takes a long time to pulverize, and contamination and composition deviation due to impurities mixed inevitably cannot be avoided. As a method for producing a raw material oxide which improves the above-mentioned problems (2) and (3) of the prior art, as shown in FIG. 5, an aqueous chloride mixed solution of a metal element other than zinc constituting ferrite is started. As a raw material, a production method of oxidizing and roasting it has been proposed (Japanese Patent Publication No. 63-17776).
However, even with this method, among the metal elements constituting ferrite, zinc has a high vapor pressure of chloride, so that when it is roasted simultaneously with iron chloride, manganese chloride, etc., it volatilizes and escapes, so it is oxidized and roasted at the same time. Therefore, it was necessary to separately mix in the form of an oxide in a subsequent step. In other words, for the zinc component, an oxide having a particle size of 0.1 to 1 μm must be mixed in the subsequent steps, and the number of steps is large. However, the above-mentioned problem (1) of causing non-uniformity and deteriorating the magnetic properties of the product has not been solved.
【0005】[0005]
【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解決し、塩化物を酸化焙焼して得られる酸
化物と酸化亜鉛とを、亜鉛の逸散を防止しながら一工程
で混合しようとするものである。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, and forms an oxide obtained by oxidizing and roasting chloride and zinc oxide while preventing the escape of zinc. It is intended to be mixed in the process.
【0006】[0006]
【課題を解決するための手段】本発明は、上記課題を解
決するために、酸化亜鉛又は加熱によって酸化亜鉛とな
る化合物に、ポリビニルアルコール、ポリビニルブチラ
ール、陰イオン性界面活性剤、水溶性有機防錆剤から選
ばれた非揮発性有機化合物水溶液を加えてスラリとし、
このスラリ(a)と、鉄の塩化物とマンガン,ニッケ
ル,マグネシウムよりなる群より選ばれた1種又は2種
以上の金属の塩化物との水溶液(b)とを、混合して酸
化焙焼することを特徴とするフェライト用原料酸化物の
製造方法を提供するもので、上記スラリ(a)と水溶液
(b)とを同時に酸化焙焼してもよい。In order to solve the above-mentioned problems, the present invention relates to a method of adding zinc oxide or a compound which becomes zinc oxide by heating to polyvinyl alcohol, polyvinyl butyral.
Tools, anionic surfactants, and water-soluble organic rust inhibitors
The aqueous solution of the non-volatile organic compound is added to form a slurry ,
The slurry (a) is mixed with an aqueous solution (b) of an iron chloride and a chloride of one or more metals selected from the group consisting of manganese, nickel, and magnesium, and oxidized and roasted. The present invention provides a method for producing a raw material oxide for ferrite, wherein the slurry (a) and the aqueous solution (b) may be simultaneously oxidized and roasted.
【0007】[0007]
【作用】本発明者らは、前記課題を解決し、低コストで
特性の優れたフェライトを製造することができる原料酸
化物の製造方法について鋭意研究を重ねた結果、本発明
を完成するに至った。亜鉛を含有するフェライト用原料
酸化物の製造において均一性を向上するには、主原料で
ある鉄の塩化物とマンガン、ニッケル、マグネシウム等
の塩化物のうちの1種以上とを含有する塩化物混合水溶
液と、酸化亜鉛又は炭酸亜鉛のような加熱によって酸化
亜鉛となる亜鉛源とを混合して酸化焙焼するか、又は塩
化物混合水溶液を酸化焙焼して酸化物を生成する過程に
おいて亜鉛源を均一混合させることが効果的な方法と考
えられる。The present inventors have solved the above-mentioned problems and conducted intensive studies on a method for producing a raw material oxide capable of producing ferrite having excellent characteristics at low cost. As a result, the present invention has been completed. Was. In order to improve the uniformity in the production of a raw material oxide for ferrite containing zinc, a chloride containing iron chloride, which is a main raw material, and at least one of chlorides such as manganese, nickel, magnesium, etc. A mixed aqueous solution and a zinc source that becomes zinc oxide by heating such as zinc oxide or zinc carbonate are mixed and oxidized and roasted, or a chloride mixed aqueous solution is oxidized and roasted to form an oxide in the process of forming an oxide. Uniform mixing of the sources is considered an effective method.
【0008】しかし、これらの亜鉛化合物は酸への溶解
度が高く容易に塩化物溶液に溶解したり、上記塩化物の
酸化焙焼により発生した塩酸ガスと反応して塩化亜鉛の
形態に変化してしまう。そのため酸化焙焼中に亜鉛は揮
発し組成のずれと不均一性を招いてしまう。以下、本発
明に至った基礎実験結果について述べる。However, these zinc compounds have a high solubility in an acid and are easily dissolved in a chloride solution, or react with hydrochloric acid gas generated by oxidizing and roasting of the chloride to change into a form of zinc chloride. I will. As a result, zinc is volatilized during oxidative roasting, resulting in a deviation in composition and inhomogeneity. Hereinafter, the results of basic experiments that led to the present invention will be described.
【0009】水1リットルに塩化第一鉄(FeCl2 ・
4H2O)712gと塩化マンガン(MnCl2 ・4H2
O)240gとを混合した塩化物混合水溶液5.0g
と、下記に示す試料1又は2とを混合し、それぞれ別の
石英坩堝に入れ、炉を所定の温度(600〜900℃)
に保持した後に、炉内に即座に挿入した。 試料1:酸化亜鉛0.1gと0.4gの水を混合したス
ラリ(懸濁液) 試料2:酸化亜鉛0.1gと40%濃度のPVA(ポリ
ビニールアルコール)水溶液0.4gを混合したスラリ 測定結果を図1に示した。試料2では試料1よりも亜鉛
成分の減少の割合が小さい。これは水溶性有機化合物で
あるPVAが酸化亜鉛粒子の周囲を取り囲み、酸化亜鉛
との塩化物との反応を防いだことが原因と考えられる。In one liter of water, ferrous chloride (FeCl 2.
4H 2 O) and manganese chloride (MnCl 2 .4H 2)
O) 5.0 g of an aqueous chloride mixture mixed with 240 g
And Sample 1 or 2 shown below are mixed and placed in separate quartz crucibles, and the furnace is heated to a predetermined temperature (600 to 900 ° C.).
, And immediately inserted into the furnace. Sample 1: Slurry (suspension) in which 0.1 g of zinc oxide and 0.4 g of water were mixed Sample 2: Slurry in which 0.1 g of zinc oxide and 0.4 g of a 40% PVA (polyvinyl alcohol) aqueous solution were mixed The measurement results are shown in FIG. Sample 2 has a smaller rate of reduction of the zinc component than Sample 1. This is considered to be because PVA, which is a water-soluble organic compound, surrounded the zinc oxide particles and prevented the reaction of the zinc oxide with the chloride.
【0010】この結果、亜鉛源は非揮発性有機化合物の
水溶液によるスラリとして用いることにより、塩化物と
の反応が抑制され、その結果、亜鉛の減少を抑制するこ
とができ、酸化焙焼炉中にて鉄の塩化物とマンガン,ニ
ッケル,マグネシウムのうちの1種以上を含有する混合
塩化物水溶液と混合又は同時に焙焼し、フェライト原料
用酸化物を製造することが可能であることがわかり、塩
化物の酸化焙焼による酸化物の生成と酸化亜鉛の混合と
を、亜鉛の逸散を防止しながら一工程で行うことができ
る。As a result, by using the zinc source as a slurry with an aqueous solution of a non-volatile organic compound, the reaction with the chloride is suppressed, and as a result, the reduction of zinc can be suppressed. It is understood that it is possible to produce an oxide for ferrite raw material by mixing or simultaneously roasting with a mixed chloride aqueous solution containing one or more of manganese, nickel, and magnesium in the form of iron chloride. The generation of the oxide by the oxidative roasting of the chloride and the mixing of the zinc oxide can be performed in one step while preventing the escape of the zinc.
【0011】本発明に用いられる非揮発性有機化合物と
しては、ポリビニルアルコール(PVA)、ポリビニル
ブチラール(PVB)、陰イオン性界面活性剤、水溶性
有機防錆剤等が使用可能で、本発明に係るフェライトの
構成金属として用いられる亜鉛,マンガン,ニッケル,
マグネシウムは、パワーロス、透磁率、飽和磁化、保持
力等の磁性の制御の効果を得るために用いられるもの
で、Cu,Li,Coも低温焼結、磁気異方性の制御、
マイクロ波特性制御等の効果を得るために、これ等の塩
化物として塩化物の水溶液に添加することができる。As the non-volatile organic compound used in the present invention, polyvinyl alcohol (PVA), polyvinyl butyral (PVB), an anionic surfactant, a water-soluble organic rust inhibitor and the like can be used. Zinc, manganese, nickel, which are used as constituent metals of the ferrite,
Magnesium is used to obtain the effect of controlling magnetism such as power loss, magnetic permeability, saturation magnetization, and coercive force. Cu, Li, and Co are also sintered at a low temperature, control of magnetic anisotropy,
These chlorides can be added to an aqueous chloride solution in order to obtain effects such as control of microwave characteristics.
【0012】なお、本発明における酸化焙焼には噴霧焙
焼法が好適に用いられる。In the present invention, the spray roasting method is suitably used for the oxidative roasting.
【0013】[0013]
〔実施例1〕鋼板の塩酸酸洗廃液を100mリットル中
に15gの鉄を含有する濃度まで濃縮し、この濃縮液5
00リットルに金属マンガン25kgを投入し、80℃
に加熱して、金属マンガンを完全に溶解させた(液Aと
する)。[Example 1] A hydrochloric acid pickling waste liquid of a steel sheet was concentrated to a concentration containing 15 g of iron in 100 ml.
Put 25 kg of metallic manganese into 00 liter,
To completely dissolve the metal manganese (liquid A).
【0014】ZnOは、12.5kgを20重量%濃度
のPVA溶液に消泡剤とともに混合分散させた(液Bと
する)。図2に示したように、上記液Aをタンク3に液
Bをタンク2に貯蔵し、送液ポンプにて混合用タンク4
で液Aと液Bとを混合後、噴霧装置5を通じて噴霧ノズ
ル6より液滴7として、810℃に保持した噴霧焙焼炉
1の炉頂より噴霧した。この液滴7は酸化焙焼され、炉
底に酸化焙焼生成物(フェライト用原料酸化物)8を得
た。12.5 kg of ZnO was mixed and dispersed in a 20% by weight PVA solution together with an antifoaming agent (hereinafter referred to as liquid B). As shown in FIG. 2, the liquid A is stored in the tank 3 and the liquid B is stored in the tank 2.
After the liquid A and the liquid B were mixed with each other, the liquid was sprayed from a spray nozzle 6 through a spray device 5 as droplets 7 from the top of a spray roasting furnace 1 maintained at 810 ° C. The droplets 7 were oxidized and roasted, and an oxidized roasted product (raw material oxide for ferrite) 8 was obtained at the furnace bottom.
【0015】生成物のX線回折定性分析を行ったとこ
ろ、生成酸化物はFe2 O3 とMn2O3 とスピネルで
あり、塩化物は認められなかった。化学分析により生成
酸化物のFe,Mn,Znの組成を求めた。組成はF
e,Mn,Znの合計が100重量%となるように求め
た。Fe,Mn,Znの組成ずれは表1に示した通りで
あり、組成のずれを生じることなくフェライト用原料酸
化物が得られていることがわかる。When the product was analyzed by X-ray diffraction qualitative analysis, the produced oxides were Fe 2 O 3 , Mn 2 O 3 and spinel, and no chloride was observed. The composition of Fe, Mn, and Zn of the produced oxide was determined by chemical analysis. The composition is F
It was determined that the sum of e, Mn, and Zn was 100% by weight. The compositional deviations of Fe, Mn, and Zn are as shown in Table 1, and it can be seen that the raw material oxide for ferrite was obtained without the compositional deviation.
【0016】この原料酸化物にSiO2 を0.01重量
%、CaCO3 を0.1重量%加え、純水を混ぜて混合
機(アトライタ)にて混合を行った。混合後にスラリを
乾燥し、この乾燥粉末にバインダとしてPVAを添加
し、造粒後、外径36mm、内径24mm、高さ10m
mのトロイダル形状に成形し、1340℃にて1%の酸
素を含む窒素雰囲気中で焼成した。The raw material oxide was added with 0.01% by weight of SiO 2 and 0.1% by weight of CaCO 3 , mixed with pure water, and mixed with a mixer (attritor). After mixing, the slurry was dried, PVA was added as a binder to the dried powder, and after granulation, the outer diameter was 36 mm, the inner diameter was 24 mm, and the height was 10 m.
m, and fired at 1340 ° C. in a nitrogen atmosphere containing 1% oxygen.
【0017】得られた焼結コアの磁気特性として、10
0kHz、0.2T、100℃のコアロスを測定したと
ころ、表2に示したように280mW/cm3 という良
好な磁気特性を得た。 〔実施例2〕Zn源として19.3kgのZnCO3 を
用いた他は実施例1と同様とした。The magnetic properties of the obtained sintered core are 10
When the core loss at 0 kHz, 0.2 T, and 100 ° C. was measured, good magnetic properties of 280 mW / cm 3 were obtained as shown in Table 2. Example 2 Example 1 was the same as Example 1 except that 19.3 kg of ZnCO 3 was used as a Zn source.
【0018】生成酸化物はFe2 O3 とMn2 O3 とス
ピネルであり塩化物は認められず、Fe,Mn,Znの
組成は表1に示した通りであり、組成のずれを生じるこ
となくフェライト用原料酸化物が得られていることがわ
かる。この原料酸化物を用い実施例1と同様にコアロス
を測定したところ、表2に示したように290mW/c
m2 という良好な磁気特性を得た。The oxides formed were Fe 2 O 3 , Mn 2 O 3 and spinel, and no chloride was observed. The composition of Fe, Mn and Zn was as shown in Table 1, and the composition was shifted. It can be seen that a raw material oxide for ferrite was obtained. The core loss was measured using this raw material oxide in the same manner as in Example 1, and as shown in Table 2, 290 mW / c
Good magnetic properties of m 2 were obtained.
【0019】〔実施例3〕図3に示したように、実施例
1にて作成した液A及び液Bをタンク3及びタンク2に
各々貯蔵し、噴霧装置5により、液Aは噴霧ノズル6A
より、液Bは噴霧ノズル6Bより、各々液滴7A、液滴
7Bとして810℃に保持した噴霧焙焼炉1の炉内に同
時に噴霧して酸化焙焼し、炉底に酸化焙焼生成物8Aを
得た。[Embodiment 3] As shown in FIG. 3, the liquid A and the liquid B prepared in the embodiment 1 are stored in the tank 3 and the tank 2, respectively.
The liquid B is sprayed simultaneously from the spray nozzle 6B into the furnace of the spray roasting furnace 1 kept at 810 ° C. as droplets 7A and 7B, respectively, and oxidized and roasted. 8A was obtained.
【0020】生成物のX線回折定性分析を行ったとこ
ろ、生成酸化物はFe2 O3 とMn2O3 とスピネルで
あり塩化物は認められず、Fe,Mn,Znの組成は表
1に示した通りであり、組成のずれを生じることなくフ
ェライト用原料酸化物が得られていることがわかる。こ
の原料酸化物を用い実施例1と同様にコアロスを測定し
たところ、表2に示したように280mW/cm3 とい
う良好な磁気特性を得た。When the product was analyzed by X-ray diffraction qualitative analysis, the resulting oxides were Fe 2 O 3 , Mn 2 O 3 and spinel, no chloride was observed, and the compositions of Fe, Mn and Zn were as shown in Table 1. It can be seen that the raw material oxide for ferrite was obtained without causing a composition shift. When core loss was measured using this raw material oxide in the same manner as in Example 1, good magnetic properties of 280 mW / cm 3 were obtained as shown in Table 2.
【0021】〔実施例4〕実施例1におけるPVAの替
わりにPVBを用いた他は実施例1と同様とした。生成
酸化物はFe2 O3 とMn2 O3 とスピネルであり、塩
化物は認められず、Fe,Mn,Znの組成ずれは表1
に示した通りであり、組成のずれを生じることなくフェ
ライト用原料酸化物が得られていることがわかる。Example 4 Example 1 was the same as Example 1 except that PVB was used instead of PVA. The oxides produced were Fe 2 O 3 , Mn 2 O 3 and spinel, no chloride was observed, and the compositional deviation of Fe, Mn, Zn was as shown in Table 1.
It can be seen that the raw material oxide for ferrite was obtained without causing a composition shift.
【0022】この原料酸化物を用い実施例1と同様にコ
アロスを測定したところ、表2に示したように290m
W/cm3 という良好な磁気特性を得た。 〔実施例5〕ZnO12.5kgを純水を混ぜ、このス
ラリに分散剤として陰イオン性界面活性剤を1重量%濃
度になるように添加し、混合した(液Cとする)。Using this raw material oxide, the core loss was measured in the same manner as in Example 1, and as shown in Table 2, 290 m
Good magnetic properties of W / cm 3 were obtained. Example 5 12.5 kg of ZnO was mixed with pure water, and an anionic surfactant was added as a dispersant to this slurry to a concentration of 1% by weight, followed by mixing (hereinafter referred to as liquid C).
【0023】実施例1と同様の方法にて液Aと液Cを使
用して噴霧焙焼し、炉底に酸化焙焼生成物を得た。生成
酸化物はFe2 O3 とMn2 O3 とスピネルであり塩化
物は認められなかった。Fe,Mn,Znの組成は表1
に示した通りであり、組成のずれを生じることなくフェ
ライト用原料酸化物が得られていることがわかる。この
原料酸化物を用い実施例1と同様にコアを作製し、コア
ロスを測定したところ表2に示したように295mW/
cm3 という良好な磁気特性を得た。The liquid A and the liquid C were spray-roasted in the same manner as in Example 1 to obtain an oxidized roasted product on the furnace bottom. The generated oxides were Fe 2 O 3 , Mn 2 O 3 and spinel, and no chloride was observed. Table 1 shows the composition of Fe, Mn and Zn.
It can be seen that the raw material oxide for ferrite was obtained without causing a composition shift. Using this raw material oxide, a core was manufactured in the same manner as in Example 1, and the core loss was measured. As shown in Table 2, 295 mW /
Good magnetic properties of cm 3 were obtained.
【0024】〔実施例6〕ZnO12.5kgを純水を
混ぜ、このスラリに水溶性有機防錆剤を1重量%濃度に
なるように添加し、混合した(液Dとする)。実施例1
と同様の方法にて液Aと液Dを使用して噴霧焙焼し、炉
底に酸化焙焼生成物を得た。生成酸化物はFe2 O3 と
Mn2 O3 とスピネルであり、塩化物は認められなかっ
た。Fe,Mn,Znの組成は表1に示した通りであ
り、組成のずれを生じることなくフェライト用原料酸化
物が得られていることがわかる。Example 6 12.5 kg of ZnO was mixed with pure water, and a water-soluble organic rust inhibitor was added to this slurry to a concentration of 1% by weight and mixed (hereinafter referred to as a liquid D). Example 1
Using the liquid A and the liquid D, spray roasting was performed in the same manner as described above to obtain an oxidized roasted product at the furnace bottom. The generated oxides were Fe 2 O 3 , Mn 2 O 3 and spinel, and no chloride was observed. The compositions of Fe, Mn, and Zn are as shown in Table 1, and it can be seen that a raw material oxide for ferrite was obtained without causing a composition shift.
【0025】この原料酸化物を用い実施例1と同様にコ
アを作製し、コアロスを測定したところ表2に示したよ
うに285mW/cm3 という良好な磁気特性を得た。 〔実施例7〕鋼板の塩酸酸洗廃液を100mリットル中
に15gの鉄を含有する濃度まで濃縮し、この濃縮液4
80リットルに金属マンガン2.2kgと金属マグネシ
ウム9.5kgとを投入し、80℃に加熱して完全に溶
解させた(溶液Eとする)。Using this raw material oxide, a core was prepared in the same manner as in Example 1, and the core loss was measured. As shown in Table 2, good magnetic properties of 285 mW / cm 3 were obtained. [Example 7] A hydrochloric acid pickling waste liquid of a steel sheet was concentrated to a concentration containing 15 g of iron in 100 ml.
2.2 kg of metal manganese and 9.5 kg of metal magnesium were put into 80 liters, and heated to 80 ° C. to completely dissolve (solution E).
【0026】ZnO21.2kgを純水を混ぜ、このス
ラリに陰イオン界面活性剤を5重量%濃度になるように
添加し、混合した(液Fとする)。実施例1と同様の装
置にて液Eと液Fを使用して噴霧焙焼し、炉底に酸化焙
焼生成物を得た。生成酸化物はFe2 O3 とMn2 O3
とスピネルであり塩化物は認められず、Fe,Mn,M
g,Znの組成は表1に示した通りであり、組成のずれ
を生じることなくフェライト用原料酸化物が得られてい
ることがわかる。21.2 kg of ZnO was mixed with pure water, and an anionic surfactant was added to the slurry to a concentration of 5% by weight and mixed (hereinafter referred to as a liquid F). The liquid E and the liquid F were used for spray roasting in the same apparatus as in Example 1 to obtain an oxidized roasted product on the furnace bottom. The generated oxides were Fe 2 O 3 and Mn 2 O 3
And spinel without chloride, and Fe, Mn, M
The compositions of g and Zn are as shown in Table 1, and it can be seen that the raw material oxide for ferrite was obtained without causing a composition shift.
【0027】この原料酸化物にSiO2 を0.1重量
%、CaCO3 を0.35重量%加え、純水を混ぜて混
合機にて混合を行った。混合後にスラリを乾燥し、この
乾燥粉にバインダとしてPVAを添加し、造粒後、外形
36mm,内径24mm,高さ10mmのトロイダル形
状に成形し、1290℃にて空気中で焼成した。得られ
たコアの磁気特性として、15.75kHz,0.1
T,100℃のコアロスを測定したところ、表2に示す
ように110mW/cm3 という良好な磁気特性を得
た。To this raw material oxide, 0.1% by weight of SiO 2 and 0.35% by weight of CaCO 3 were added, mixed with pure water, and mixed by a mixer. After mixing, the slurry was dried, and PVA was added as a binder to the dried powder. After granulation, the slurry was formed into a toroidal shape having an outer diameter of 36 mm, an inner diameter of 24 mm, and a height of 10 mm, and was fired at 1290 ° C. in air. The magnetic properties of the obtained core were 15.75 kHz, 0.1
When the core loss at T and 100 ° C. was measured, good magnetic characteristics of 110 mW / cm 3 were obtained as shown in Table 2.
【0028】〔実施例8〕鋼板の塩酸酸洗廃液を100
mリットル中に15gの鉄を含有する濃度まで濃縮し、
この濃縮液450リットルに金属マンガン2.0kgと
金属ニッケル25.0kgと金属マグネシウム2.0k
gとを投入し、80℃に加熱して完全に溶解させた(液
Gとする)。[Embodiment 8] A hydrochloric acid pickling waste liquid of a steel sheet was
concentrated to a concentration containing 15 g of iron in ml,
2.0 kg of metallic manganese, 25.0 kg of metallic nickel and 2.0 k of metallic magnesium were added to 450 liters of this concentrated liquid.
g) and heated to 80 ° C. to completely dissolve (hereinafter referred to as liquid G).
【0029】ZnO5.0kgを純水を混ぜ、このスラ
リに陰イオン界面活性剤を5重量%濃度になるように添
加し、混合した(液Hとする)。実施例1と同様の装置
にて液Gと液Hを使用して噴霧焙焼し、炉底に酸化焙焼
生成物を得た。生成酸化物はFe2 O3 とスピネルであ
り塩化物は認められず、Fe,Mn,Mg,Znの組成
は表1に示した通りであり、組成のずれを生じることな
くフェライト用原料酸化物が得られていることがわか
る。5.0 kg of ZnO was mixed with pure water, and an anionic surfactant was added to the slurry so as to have a concentration of 5% by weight and mixed (hereinafter referred to as liquid H). Using the same apparatus as in Example 1, the liquid G and the liquid H were used for spray roasting to obtain an oxidized roasted product on the furnace bottom. The generated oxides were Fe 2 O 3 and spinel, and no chloride was observed. The composition of Fe, Mn, Mg, and Zn was as shown in Table 1. It can be seen that is obtained.
【0030】この原料酸化物にSiO2 を2.0重量
%、Bi2 O3 を0.05重量%加え、純水を混ぜて混
合機にて混合を行った。混合後にスラリを乾燥し、この
乾燥粉にバインダとしてPVAを添加し、造粒後、外形
36mm,内径24mm,高さ10mmのトロイダル形
状に成形し、1200℃にて空気中で焼成した。得られ
たコアの磁気特性として、1MHzと40MHzにおい
て5mOe,25℃の初透磁率を測定したところ、表3
に示すように各々50,48という良好な磁気特性を得
た。To this raw material oxide, 2.0% by weight of SiO 2 and 0.05% by weight of Bi 2 O 3 were added, mixed with pure water, and mixed by a mixer. After mixing, the slurry was dried, and PVA was added as a binder to the dried powder. After granulation, the slurry was formed into a toroidal shape having an outer diameter of 36 mm, an inner diameter of 24 mm, and a height of 10 mm, and was fired at 1200 ° C. in air. The magnetic permeability of the obtained core was measured at 5 MHz and 25 ° C. at 1 MHz and 40 MHz.
As shown in Table 2, good magnetic properties of 50 and 48 were obtained.
【0031】〔比較例1〕PVAを用いなかった他は実
施例1と同様とした。生成酸化物はFe2 O3 とMn2
O3 とスピネルであり、塩化物は認められなかったが、
Fe,Mn,Znの組成ずれは表1に示した通りであ
り、亜鉛の組成が大幅に減少し、相対的に鉄とマンガン
の組成が増加している。Comparative Example 1 The procedure of Example 1 was repeated except that PVA was not used. The oxides produced were Fe 2 O 3 and Mn 2
O 3 and spinel, no chloride was found,
The composition deviations of Fe, Mn, and Zn are as shown in Table 1. The composition of zinc is greatly reduced, and the compositions of iron and manganese are relatively increased.
【0032】この原料酸化物に実施例1の組成と同じに
なるように酸化亜鉛を加えた後、実施例1と同様にコア
を作製しコアロスを測定したところ、表2に示したよう
に900mW/cm3 という高いコアロスとなった。After zinc oxide was added to this raw material oxide so as to have the same composition as in Example 1, a core was prepared and the core loss was measured in the same manner as in Example 1. As shown in Table 2, 900 mW was obtained. / Cm 3 as high as core loss.
【0033】[0033]
【表1】 ─────────────────────────────────── 酸化焙焼生成物 分析結果(重量%) Fe Mn Mg Ni Zn 実施例1 68.5 22.5 9.0 実施例2 68.6 22.6 8.8 実施例3 68.5 22.8 8.7 実施例4 68.4 22.7 8.9 実施例5 68.6 22.3 9.1 実施例6 68.8 22.3 8.9 実施例7 71.5 2.2 9.4 16.9 実施例8 67.2 2.0 2.2 24.6 4.0 比較例1 74.9 24.8 0.3 ───────────────────────────────────[Table 1] 酸化 Oxidation roasting products analysis results (% by weight) FeMnMgNiNiZn Example 1 68.5 22.5 9.0 Example 2 68.6 22.6 8.8 Example 3 68.5 22.8 8.7 Example 4 68.4 22.7 8.9 Example 5 68.6 22.3 9.1 Example 6 68.8 22.3 8.9 Example 7 71.5 2.2 9.4 16.9 Example 8 67.2 0 2.2 24.6 4.0 Comparative Example 1 74.9 24.8 0.3 ───────
【0034】[0034]
【表2】 ────────────────────────────── コアロス(mW/cm3 ) 実施例1 280 実施例2 290 実施例3 280 実施例4 290 実施例5 295 実施例6 285 実施例7 110 比較例1 900 ──────────────────────────────2 Core loss (mW / cm 3 ) Example 1 280 Example 2 290 Example 3 280 Example 4 290 Example 5 295 Example 6 285 Example 7 110 Comparative Example 1 900 ───
【0035】[0035]
【表3】 ────────────────────────────── 初透磁率 1MHz 40MHz 実施例8 50 48 ────────────────────────────── 実施例1〜8と比較例1より、本発明によれば、亜鉛の
組成ずれを伴うことなく成分の均一分散性の良好なフェ
ライト用原料酸化物を、酸化焙焼後の酸化亜鉛の混合工
程を要することなく製造することが可能となり、その結
果、磁気特性の良好な製品を製造することが可能になっ
た。[Table 3] Initial magnetic permeability 1 MHz 40 MHz Example 8 50 48よ り From Examples 1 to 8 and Comparative Example 1, according to the present invention, the components were obtained without accompanying the compositional deviation of zinc. It is possible to produce a ferrite raw material oxide with good uniform dispersibility without the need for a mixing step of zinc oxide after oxidizing and roasting, and as a result, it is possible to produce a product with good magnetic properties Became.
【0036】[0036]
【発明の効果】本発明により、フェライトを構成する金
属の塩化物の酸化焙焼工程で亜鉛を逸散することなく亜
鉛源を混入することが可能となり、酸化焙焼後の別工程
にて亜鉛を酸化物の形態にて混合する必要がなく、仮焼
工程が省略され低コストで均一分散性が向上し、その結
果、焼結コアの磁気特性が向上したフェライト用原料酸
化物の製造が可能になった。According to the present invention, it is possible to mix a zinc source without escaping zinc in the oxidizing and roasting step of chloride of a metal constituting ferrite, and to separate zinc in a separate step after oxidizing and roasting. Does not need to be mixed in the form of an oxide, the calcination step is omitted, uniform dispersion is improved at low cost, and as a result, it is possible to produce a raw material oxide for ferrite with improved magnetic properties of the sintered core Became.
【図面の簡単な説明】[Brief description of the drawings]
【図1】基礎実験における炉内温度と残留したZnOと
の関係を示すグラフである。FIG. 1 is a graph showing a relationship between a furnace temperature and residual ZnO in a basic experiment.
【図2】実施例1、2、4、5、6、7、8及び比較例
1における酸化焙焼炉の模式図である。FIG. 2 is a schematic diagram of an oxidation roasting furnace in Examples 1, 2, 4, 5, 6, 7, 8 and Comparative Example 1.
【図3】実施例3における酸化焙焼炉の模式図である。FIG. 3 is a schematic view of an oxidation roasting furnace according to a third embodiment.
【図4】従来方法による工程のブロック図である。FIG. 4 is a block diagram of a process according to a conventional method.
【図5】他の従来方法による工程のブロック図である。FIG. 5 is a block diagram of a process according to another conventional method.
1 噴霧焙焼炉 2,3 貯蔵タンク 4 混合用タンク 5 噴霧装置 6,6A,6B 噴霧ノズル 7,7A,7B 噴霧された液滴 8,8A 炉底から得た生成酸化物 DESCRIPTION OF SYMBOLS 1 Spray roasting furnace 2, 3 Storage tank 4 Mixing tank 5 Spray device 6, 6A, 6B Spray nozzle 7, 7A, 7B Sprayed droplet 8, 8A Oxide produced from furnace bottom
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C01G 49/00 H01F 1/34 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int. Cl. 7 , DB name) C01G 49/00 H01F 1/34
Claims (2)
る化合物に、ポリビニルアルコール、ポリビニルブチラ
ール、陰イオン性界面活性剤、水溶性有機防錆剤から選
ばれた非揮発性有機化合物水溶液を混合してスラリと
し、該スラリと、鉄の塩化物とマンガン,ニッケル,マ
グネシウムよりなる群より選ばれた1種又は2種以上の
金属の塩化物との水溶液とを、混合して酸化焙焼するこ
とを特徴とするソフトフェライト用原料酸化物の製造方
法。1. A method for producing zinc oxide or a compound which becomes zinc oxide by heating , comprising polyvinyl alcohol and polyvinyl butyral.
Tools, anionic surfactants, and water-soluble organic rust inhibitors
Mix the separated non-volatile organic compound aqueous solution to form a slurry .
The slurry is mixed with an aqueous solution of iron chloride and one or more metal chlorides selected from the group consisting of manganese, nickel, and magnesium, and oxidized and roasted. Of producing a raw material oxide for soft ferrite.
る化合物に、ポリビニルアルコール、ポリビニルブチラ
ール、陰イオン性界面活性剤、水溶性有機防錆剤から選
ばれた非揮発性有機化合物水溶液を加えてスラリとし、
該スラリと、鉄の塩化物とマンガン,ニッケル,マグネ
シウムよりなる群より選ばれた1種又は2種以上の金属
の塩化物との水溶液とを、同時に酸化焙焼することを特
徴とするソフトフェライト用原料酸化物の製造方法。2. Polyvinyl alcohol or polyvinyl butyral is used as a zinc oxide or a compound which becomes zinc oxide by heating.
Tools, anionic surfactants, and water-soluble organic rust inhibitors
The aqueous solution of the non-volatile organic compound is added to form a slurry ,
A soft ferrite comprising simultaneously oxidizing and roasting the slurry and an aqueous solution of an iron chloride and a chloride of one or more metals selected from the group consisting of manganese, nickel and magnesium. Production method of raw material oxide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03293022A JP3078626B2 (en) | 1991-04-12 | 1991-11-08 | Method for producing raw material oxide for soft ferrite |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8000491 | 1991-04-12 | ||
| JP3-80004 | 1991-04-12 | ||
| JP03293022A JP3078626B2 (en) | 1991-04-12 | 1991-11-08 | Method for producing raw material oxide for soft ferrite |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0570145A JPH0570145A (en) | 1993-03-23 |
| JP3078626B2 true JP3078626B2 (en) | 2000-08-21 |
Family
ID=26421034
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP03293022A Expired - Fee Related JP3078626B2 (en) | 1991-04-12 | 1991-11-08 | Method for producing raw material oxide for soft ferrite |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3078626B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110993309B (en) * | 2019-12-24 | 2022-03-04 | 横店集团东磁股份有限公司 | Method for preparing slurry by using ferrite green sheets |
| CN116459740A (en) * | 2023-03-10 | 2023-07-21 | 华友新能源科技(衢州)有限公司 | A roasting furnace and a system for preparing lithium oxide precursors |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2849207B2 (en) | 1990-11-30 | 1999-01-20 | 川崎製鉄株式会社 | Method for producing raw material oxide for soft ferrite |
-
1991
- 1991-11-08 JP JP03293022A patent/JP3078626B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2849207B2 (en) | 1990-11-30 | 1999-01-20 | 川崎製鉄株式会社 | Method for producing raw material oxide for soft ferrite |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0570145A (en) | 1993-03-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR100733158B1 (en) | The method of manufacturing Ferrite raw material powder and Ferrite magnet by spray thermo decomposing method | |
| US4751070A (en) | Low temperature synthesis | |
| JP3157080B2 (en) | Manufacturing method of ferrite material | |
| US4372865A (en) | Carbonate/hydroxide coprecipitation process | |
| KR100564982B1 (en) | Method for manufacturing highly-crystallized double oxide powder | |
| US4808327A (en) | Compositions of particulate magnetic oxides with a defect spinel structure, preparation thereof and application thereof | |
| EP0462344B1 (en) | Method for producing composite oxides for use ad starting materials for ferrites | |
| JP6759855B2 (en) | Method for manufacturing rare earth-iron-nitrogen alloy powder | |
| JP3078626B2 (en) | Method for producing raw material oxide for soft ferrite | |
| US3766642A (en) | Process for preparing a ductile metal ferrite | |
| US4472369A (en) | Process for producing ferrites | |
| US4062922A (en) | Process for preparing strontium ferrites | |
| JP3032098B2 (en) | Soft ferrite raw material powder and method and apparatus for producing the same | |
| US3884823A (en) | Ceramic permanent magnet | |
| JP2010270379A (en) | Method for producing rare earth-iron-nitrogen based magnet powder | |
| WO1994019283A1 (en) | Soft ferrite raw material powder and sintered body thereof, and method for producing the same | |
| GB2050330A (en) | Process for producing hydrated iron oxide having silicon and phosphorus components | |
| JPH04219321A (en) | Zinc raw material for soft ferrite and production of oxide raw material for soft ferrite using the same | |
| JP2846147B2 (en) | Method for producing raw material oxide for soft ferrite | |
| JP2849207B2 (en) | Method for producing raw material oxide for soft ferrite | |
| JP4306389B2 (en) | Method for producing alloy powder | |
| JPH01305826A (en) | Production of laminar barium ferrite fine powder | |
| US3830743A (en) | Ceramic permanent magnet | |
| JP2852151B2 (en) | Method for producing raw material oxide for soft ferrite | |
| EP0684209B1 (en) | Production of magnetic oxide powder |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20000606 |
|
| LAPS | Cancellation because of no payment of annual fees |