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JPH0262481B2 - - Google Patents
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JPH0262481B2 - - Google Patents

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Publication number
JPH0262481B2
JPH0262481B2 JP16400885A JP16400885A JPH0262481B2 JP H0262481 B2 JPH0262481 B2 JP H0262481B2 JP 16400885 A JP16400885 A JP 16400885A JP 16400885 A JP16400885 A JP 16400885A JP H0262481 B2 JPH0262481 B2 JP H0262481B2
Authority
JP
Japan
Prior art keywords
metal
reaction
powder
hydrazine
particles
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
Application number
JP16400885A
Other languages
Japanese (ja)
Other versions
JPS6227310A (en
Inventor
Hirohisa Kajama
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.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
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 Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP16400885A priority Critical patent/JPS6227310A/en
Publication of JPS6227310A publication Critical patent/JPS6227310A/en
Publication of JPH0262481B2 publication Critical patent/JPH0262481B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/14Methods for preparing oxides or hydroxides in general
    • C01B13/36Methods for preparing oxides or hydroxides in general by precipitation reactions in aqueous solutions

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Compounds Of Iron (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は極めて微小な非針状を有する、例えば
四三酸化鉄、四三酸化コバルト、酸化マンガンな
どの金属酸化物粒子を簡単に効率よく製造する方
法に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention easily and efficiently produces extremely fine non-acicular metal oxide particles such as triiron tetroxide, tricobalt tetroxide, and manganese oxide. Relating to a method of manufacturing.

[従来技術およびその問題点] 一般に微小な金属酸化物粒子は顔料用、研磨材
用、電磁気材料用などとして有用である。例えば
三二酸化鉄は、0.1μm以下の微小粒子にすること
によつて、紫外線を通過させ難い特殊顔料として
の用途も生じ、その有用性が増加する。また、フ
エライトは一般に酸化鉄と他の金属酸化物もしく
は炭酸塩とを混合し、1000℃以上の高温で固体反
応により合成されるが、そのような固体反応を容
易に達成するために、原料として微小な酸化鉄が
望まれている。
[Prior art and its problems] In general, fine metal oxide particles are useful as pigments, abrasives, electromagnetic materials, and the like. For example, by making iron sesquioxide into fine particles of 0.1 μm or less, it can be used as a special pigment that does not easily transmit ultraviolet rays, increasing its usefulness. In addition, ferrite is generally synthesized by mixing iron oxide with other metal oxides or carbonates and performing a solid-state reaction at high temperatures of 1000°C or higher. Minute iron oxide is desired.

従来、微小な金属酸化物粒子の製造方法として
は、一般に(1)金属陽イオンを難溶の水酸化物、炭
酸塩、蓚酸塩などの形で沈殿させ、これを仮焼す
る方法、(2)金属アルコキシドを加水分解して得ら
れる沈殿物を仮焼する方法、(3)鉄酸化物として、
例えば特開昭58−20733号で提案されているよう
に、レピドクロサイトγ−FeOOHをオートクレ
ーブ中で攪拌しながら、200℃で30分間程度の水
熱処理をして微小なα型三二酸化鉄を得る方法な
どがある。
Conventionally, methods for producing fine metal oxide particles generally include (1) a method of precipitating metal cations in the form of hardly soluble hydroxide, carbonate, oxalate, etc., and calcining this; ) A method of calcining the precipitate obtained by hydrolyzing a metal alkoxide, (3) As an iron oxide,
For example, as proposed in JP-A-58-20733, lepidocrocite γ-FeOOH is hydrothermally treated at 200°C for about 30 minutes while stirring in an autoclave to form minute α-type iron sesquioxide. There are ways to get it.

しかしながら、上記した如き従来法において
は、沈殿の生成時に粒子が微小であつても、粒径
が不揃いであつたり、その後の焼成工程で粒子の
二次成長が起こり易く粗大化したりして、所望の
微小な金属酸化物粒子が簡単に得られなかつた
り、また高温、加圧下の反応を必要するなど工業
的操作において工程が複雑であるなどの欠点を有
する。
However, in the conventional method as described above, even if the particles are microscopic when forming the precipitate, the particle size may be uneven, or the particles may easily undergo secondary growth in the subsequent firing process and become coarse. The disadvantages include that minute metal oxide particles cannot be easily obtained, and that the process is complicated in industrial operations, such as requiring reactions at high temperatures and under pressure.

[問題点を解決するための手段] 本発明者らは従来法における問題点を解決し、
微小な金属酸化物を簡便に得る方法について鋭意
研究を重ねた。その結果、金属ヒドラジン塩が過
酸化水素などの酸化剤で瞬時に酸化分解され、粒
度分布がシヤープである微小の金属酸化物粒子が
簡単に得られることを見出して、本発明を提供す
るに至つたものである。即ち、本発明は金属ヒド
ラジン塩を酸化分解することを特徴とする微小な
金属酸化物粒子の製造方法である。
[Means for solving the problems] The present inventors solved the problems in the conventional method,
We have conducted extensive research into ways to easily obtain minute metal oxides. As a result, they discovered that metal hydrazine salts can be instantaneously oxidized and decomposed with an oxidizing agent such as hydrogen peroxide, and that minute metal oxide particles with a sharp particle size distribution can be easily obtained, and have thus come to provide the present invention. It is ivy. That is, the present invention is a method for producing minute metal oxide particles, which is characterized by oxidatively decomposing a metal hydrazine salt.

本発明に用いる金属ヒドラジン塩の金属として
は、例えば鉄、コバルト、マンガン、ニツケル、
錫などである。かかる金属ヒドラジン塩は、一般
に対応する金属塩の少なくとも一種と、ヒドラジ
ンまたはヒドラジン化合物とを水溶液で反応させ
て得られる。したがつて、金属塩としては一般に
水溶性の金属化合物が好ましく、例えばFeCl2
CoCl2などの塩化物、FeSO4、MnSO4などの硫酸
塩、あるいは硝酸塩などが好適に用いられる。金
属塩とヒドラジンとの反応は公知であり、例えば
下記式の如く FeCl2+2N2H4→FeCl2(N2H42 CoCl2+2N2H4→CoCl2(N2H42 示される。
Examples of the metal of the metal hydrazine salt used in the present invention include iron, cobalt, manganese, nickel,
such as tin. Such metal hydrazine salts are generally obtained by reacting at least one corresponding metal salt with hydrazine or a hydrazine compound in an aqueous solution. Therefore, water-soluble metal compounds are generally preferred as metal salts, such as FeCl 2 ,
Chlorides such as CoCl 2 , sulfates such as FeSO 4 and MnSO 4 , or nitrates are preferably used. The reaction between metal salts and hydrazine is known, for example, as shown in the following formula: FeCl 2 +2N 2 H 4 →FeCl 2 (N 2 H 4 ) 2 CoCl 2 +2N 2 H 4 →CoCl 2 (N 2 H 4 ) 2 It will be done.

次に、本発明における金属ヒドラジン塩の酸化
分解反応は、該金属ヒドラジン塩の反応液を激し
く攪拌しながら酸化剤の添加によつて、良好に達
成される。したがつて、本発明においては金属ヒ
ドラジン塩の合成と該ヒドラジン塩の酸化分解と
を、同一の反応容器において連続して実施するこ
とが出来る。なお、酸化剤としては特に制限され
ないが、不純物の混入を防ぐという点から、過酸
化水素が好適であるが、そのほか亜硝酸塩、次亜
塩素酸塩、硝酸なども適用される。
Next, the oxidative decomposition reaction of the metal hydrazine salt in the present invention can be successfully achieved by adding an oxidizing agent while vigorously stirring the reaction solution of the metal hydrazine salt. Therefore, in the present invention, the synthesis of a metal hydrazine salt and the oxidative decomposition of the hydrazine salt can be carried out continuously in the same reaction vessel. The oxidizing agent is not particularly limited, but from the viewpoint of preventing contamination with impurities, hydrogen peroxide is preferred, but nitrites, hypochlorites, nitric acid, etc. are also applicable.

本発明において、特に粒度分布がシヤープな金
属酸化物粒子を得るためには、金属ヒドラジン塩
の濃度を一般に15重量%以下、特に5〜10重量%
に調整した水溶液中で酸化分解することが好まし
い。即ち、金属ヒドラジン塩の酸化分解反応は極
めて瞬時に達成されるため、該金属ヒドラジン塩
の濃度が高すぎる場合には、反応が局所的とな
り、得られる金属酸化物の粒度分布が不揃いにな
る。金属ヒドラジン塩の濃度が5重量%より低い
場合にも反応は達成されるが、効率的でない。ま
た、反応温度が低すぎる場合には、反応がスムー
ズに達成されなくなり効率的でなく、結果として
微小で且つシヤープな粒度分布を有する金属酸物
粒子が得られにくくなる。したがつて、反応温度
は一般に20〜100℃、特に40〜90℃の範囲が好ま
しい。
In the present invention, in order to obtain metal oxide particles with a particularly sharp particle size distribution, the concentration of the metal hydrazine salt is generally 15% by weight or less, particularly 5 to 10% by weight.
It is preferable to carry out oxidative decomposition in an aqueous solution adjusted to That is, since the oxidative decomposition reaction of the metal hydrazine salt is accomplished very instantaneously, if the concentration of the metal hydrazine salt is too high, the reaction will be localized and the particle size distribution of the resulting metal oxide will be uneven. The reaction is also achieved when the concentration of metal hydrazine salt is lower than 5% by weight, but not efficiently. Furthermore, if the reaction temperature is too low, the reaction will not be achieved smoothly and will not be efficient, and as a result, it will be difficult to obtain metal oxide particles having a fine and sharp particle size distribution. Therefore, the reaction temperature is generally preferably in the range of 20 to 100°C, particularly 40 to 90°C.

本発明における金属ヒドラジン塩の酸化剤によ
る酸化分解は、例えば下記式 3FeCl2(N2H42+2H2O2→Fe3O4 +6NH4Cl+2H2+3N2 のように、速やかに反応が達成される。生成した
金属酸化物は反応液より常法により分離、水洗し
た後、乾燥することにより微小な粒子状粉末とし
て得られる。
In the present invention, the oxidative decomposition of the metal hydrazine salt by an oxidizing agent can quickly achieve the reaction as shown in the following formula: 3FeCl 2 (N 2 H 4 ) 2 +2H 2 O 2 →Fe 3 O 4 +6NH 4 Cl+2H 2 +3N 2 be done. The generated metal oxide is separated from the reaction solution by a conventional method, washed with water, and then dried to obtain a fine particulate powder.

[効果] 以上に説明したように、本発明は従来法に比べ
て焼成工程を必要としないため、粒子の粗大化も
なく、例えば0.05μm以下の極めて微小かつ粒度
分布がシヤープである、非針状でほぼ球状の金属
酸化物粒子を得ることが出来る。また、本発明は
加圧下での反応なども必要としないため、簡単な
工程および操作で、迅速に効率よく且つ安易に、
所望の微小な金属酸化物を得ることが出来、工業
的にも極めて有用である。
[Effects] As explained above, the present invention does not require a firing process compared to the conventional method, so there is no coarsening of particles, and non-needle particles with extremely small particles of, for example, 0.05 μm or less and a sharp particle size distribution, are produced. It is possible to obtain metal oxide particles having a shape and a substantially spherical shape. Furthermore, since the present invention does not require a reaction under pressure, it can be carried out quickly, efficiently, and easily with simple steps and operations.
Desired minute metal oxides can be obtained and are extremely useful industrially.

[実施例] 以下、本発明の実施例を示すが、本発明はこれ
らの実施例に制限されるものではない。
[Examples] Examples of the present invention will be shown below, but the present invention is not limited to these Examples.

実施例 1 硫酸第1鉄(7水塩)30gを水に溶解した水溶
液600mlを50℃に加熱した後、飽水ヒドラジン
(N2H4・H2O)12gを攪拌しながら徐々に注加
することによつて、やや緑色を帯びた白色の沈殿
物が生成した。次いで、これを攪拌しながら過酸
化水素水(15重量%)10gを徐々に添加すること
によつて、ガスを発生しながら反応が進行し、沈
殿物は最後に黒色に変化した。生成した沈殿物を
水洗、濾過および乾燥して微小な粉末を得た。
Example 1 After heating 600 ml of an aqueous solution of 30 g of ferrous sulfate (heptahydrate) dissolved in water to 50°C, 12 g of saturated hydrazine (N 2 H 4 H 2 O) was gradually added while stirring. As a result, a slightly greenish white precipitate was formed. Next, while stirring, 10 g of hydrogen peroxide solution (15% by weight) was gradually added to proceed with the reaction while generating gas, and the precipitate finally turned black. The generated precipitate was washed with water, filtered and dried to obtain a fine powder.

上記で得た粉末は、X線回折によりFe3O4であ
ることを確認した。また、粉末の比表面積は、
BET法により測定した結果、74.4m2/gであつ
た。第1図に、この粉末の電子顕微鏡写真
(200000倍)を示す。この電子顕微鏡写真の観察
により、粉末の粒子は平均直径が0.02μmのほぼ
球形として認められる。
The powder obtained above was confirmed to be Fe 3 O 4 by X-ray diffraction. In addition, the specific surface area of the powder is
As a result of measurement by BET method, it was 74.4 m 2 /g. Figure 1 shows an electron micrograph (200,000x magnification) of this powder. Observation of this electron micrograph reveals that the powder particles are approximately spherical with an average diameter of 0.02 μm.

実施例 2 塩化マンガン(4水塩)30gを水600に溶解
し、80℃に加熱した後、攪拌しながら飽水ヒドラ
ジン12gを徐々注加することによつて、黄白色の
沈殿物が生成した。次いで、直ちに攪拌しなが
ら、これに過酸化水素水(15重量%)20gを徐々
に添加することによつて、黒褐色に変化した沈殿
物が生成した。生成した沈殿物を水洗、濾過およ
び乾燥して微小な粉末を得た。
Example 2 30 g of manganese chloride (tetrahydrate) was dissolved in 600° C. of water, heated to 80° C., and then 12 g of saturated hydrazine was gradually added while stirring to form a yellowish white precipitate. . Next, 20 g of hydrogen peroxide solution (15% by weight) was gradually added to the mixture while stirring immediately, thereby producing a precipitate that turned blackish brown in color. The generated precipitate was washed with water, filtered and dried to obtain a fine powder.

上記で得た粉末は、X線回折によりMn2O3
あることを確認した。また、粒子の平均直径は
0.04μmであり、BET法による比表面積の測定で
は、34.1m2/gであつた。
The powder obtained above was confirmed to be Mn 2 O 3 by X-ray diffraction. Also, the average diameter of the particles is
The specific surface area was 0.04 μm, and the specific surface area was 34.1 m 2 /g by BET method.

実施例 3 硫酸第1鉄(7水塩)27gおよび硫酸コバルト
(7水塩)30gを水600mlに溶解し、これを加熱し
て70℃に昇温した後、撹拌しながら飽水ヒドラジ
ン13gを徐々に添加することによつて、灰白色の
沈殿物が生成した。次いで、90℃に昇温した後、
攪拌しながら過酸化水素水(15重量%)10gを注
加することによつて、黒色に変化した沈殿物が生
成した。生成した沈殿物を水洗、濾過および乾燥
して微小な粉末を得た。
Example 3 27 g of ferrous sulfate (7 hydrate) and 30 g of cobalt sulfate (7 hydrate) were dissolved in 600 ml of water, heated to 70°C, and then 13 g of saturated hydrazine was added with stirring. Upon gradual addition, an off-white precipitate formed. Then, after raising the temperature to 90℃,
By adding 10 g of hydrogen peroxide solution (15% by weight) while stirring, a black precipitate was formed. The generated precipitate was washed with water, filtered and dried to obtain a fine powder.

上記で得た粉末をX線回折による分析の結果、
ピークはFe3O4のピークを外れ鉄−コバルトの固
溶体の存在が示唆された。なお、粉末を蛍光X線
による分析の結果、コバルトの存在を確認した。
また、粉末の粒子の平均直径は0.02μmであり、
BET法による比表面積の測定では、80.7m2/g
であつた。
As a result of analyzing the powder obtained above by X-ray diffraction,
The peak deviated from the Fe 3 O 4 peak, suggesting the presence of an iron-cobalt solid solution. In addition, the presence of cobalt was confirmed as a result of analyzing the powder using fluorescent X-rays.
In addition, the average diameter of the powder particles is 0.02 μm,
When measuring the specific surface area using the BET method, it was 80.7m 2 /g.
It was hot.

実施例 4 酸化剤として過酸化水素水の代わりに亜硝酸ナ
トリウム水溶液(10重量%)を用いた以外は、実
施例1と同様の方法によつて、実施した結果、黒
色の微小粉末を得た。
Example 4 A fine black powder was obtained in the same manner as in Example 1, except that an aqueous sodium nitrite solution (10% by weight) was used as the oxidizing agent instead of aqueous hydrogen peroxide. .

上記の粉末は、X線回折によりFe3O4であるこ
とを確認し、また粒子の平均直径は0.025μmであ
り、BET法により比表面積54.6m2/gを測定し
た。
The above powder was confirmed to be Fe 3 O 4 by X-ray diffraction, and the average particle diameter was 0.025 μm, and the specific surface area was measured to be 54.6 m 2 /g by BET method.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、実施例1で得た粉末の形状を示す電
子顕微鏡写真(200000倍)である。
FIG. 1 is an electron micrograph (200,000 times magnification) showing the shape of the powder obtained in Example 1.

Claims (1)

【特許請求の範囲】[Claims] 1 金属ヒドラジン塩を酸化分解することを特徴
とする微小な金属酸化物粒子の製造方法。
1. A method for producing minute metal oxide particles, which comprises oxidatively decomposing a metal hydrazine salt.
JP16400885A 1985-07-26 1985-07-26 Method for producing minute metal oxide particles Granted JPS6227310A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16400885A JPS6227310A (en) 1985-07-26 1985-07-26 Method for producing minute metal oxide particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16400885A JPS6227310A (en) 1985-07-26 1985-07-26 Method for producing minute metal oxide particles

Publications (2)

Publication Number Publication Date
JPS6227310A JPS6227310A (en) 1987-02-05
JPH0262481B2 true JPH0262481B2 (en) 1990-12-25

Family

ID=15785013

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16400885A Granted JPS6227310A (en) 1985-07-26 1985-07-26 Method for producing minute metal oxide particles

Country Status (1)

Country Link
JP (1) JPS6227310A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19647037A1 (en) * 1996-11-14 1998-05-28 Degussa Spherical color pigments, process for their preparation and their use
GB9903519D0 (en) 1999-02-16 1999-04-07 Europ Economic Community Precipitation process
KR100688732B1 (en) * 2005-03-30 2007-03-02 에스케이 주식회사 Method for producing spherical manganese carbonate and product thereof

Also Published As

Publication number Publication date
JPS6227310A (en) 1987-02-05

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