JPS6183628A - Production of fine poder of oxides of metal containing nb - Google Patents

Production of fine poder of oxides of metal containing nb

Info

Publication number
JPS6183628A
JPS6183628A JP20332884A JP20332884A JPS6183628A JP S6183628 A JPS6183628 A JP S6183628A JP 20332884 A JP20332884 A JP 20332884A JP 20332884 A JP20332884 A JP 20332884A JP S6183628 A JPS6183628 A JP S6183628A
Authority
JP
Japan
Prior art keywords
powder
solution
oxalic acid
fine
thermal decomposition
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
JP20332884A
Other languages
Japanese (ja)
Inventor
Toichi Takagi
東一 高城
Kimitake Ametani
飴谷 公兵
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo 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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP20332884A priority Critical patent/JPS6183628A/en
Publication of JPS6183628A publication Critical patent/JPS6183628A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:A Nb solution acidified with oxalic acid is allowed to react with Mg and/or Mn and the resultant solution is thermally decomposed to give the titled fine particles of uniform size which has high purity, good dispersibility, uniform composition and reactivity. CONSTITUTION:A precipitate of niobium pentahydroxide and a powder of oxalic acid are mixed and dissolved in water and the resultant solution is allowed to react with Mg and/or Mn of 0.1-1mm particle sizes. Then, the reaction mixture is made into fine drops by spraying or atomizing and subjected to thermal decomposition in a short time in a reactor such as an electric furnace at 600-1,300 deg.C, further roasted, if the thermal decomposition is incomplete, to give the title fine powder.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はNb含有金属酸化物微粉末の製法、さらに詳し
くはNbのシュウ酸酸性溶液とMg及び/又はMnとを
反応させて得られた溶液を熱分解することにより高純度
で、しかも組成の均一なNb含有金属酸化物微粉末を製
造する方法に関する。
[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a method for producing Nb-containing metal oxide fine powder, more specifically, a method for producing Nb-containing metal oxide fine powder obtained by reacting an acidic solution of Nb with oxalic acid and Mg and/or Mn. The present invention relates to a method for producing Nb-containing metal oxide fine powder with high purity and uniform composition by thermally decomposing a solution.

(従来技術とその問題点) Nb含有金属酸化物粉末たとえば(Mgl/3Nb’/
3)02粉末、(Mn 731Jb ”/3)02粉末
などは、圧電材料、焦電材料、強誘電材料などのエレク
トロセラミックスを製造する場合の原料として重要であ
る。さらに説明すると、これらは圧電材料、強誘電材料
などとしてよく知られているPbT工03系、PbZr
O3系P’bTiO3−P″bZr03系材料などの第
2あるいは第3成分として加えられるP b(Mg1/
3Nb2/3)o3、Pb(Mn1/3Nb2/3 )
03などのIJK料として用いられる。
(Prior art and its problems) Nb-containing metal oxide powder, for example (Mgl/3Nb'/
3)02 powder, (Mn 731Jb ”/3)02 powder, etc. are important as raw materials for producing electroceramics such as piezoelectric materials, pyroelectric materials, and ferroelectric materials.To explain further, these are piezoelectric materials. , PbT 03 series, PbZr, which are well known as ferroelectric materials etc.
Pb(Mg1/
3Nb2/3)o3, Pb(Mn1/3Nb2/3)
It is used as an IJK material such as 03.

この際、Nb含有金属酸化物粉末は高純度で粒径が小さ
く、かつ均一で分散性、組成の均一性、反応性に優れた
ものが要求される。
At this time, the Nb-containing metal oxide powder is required to have high purity, small particle size, and uniformity and excellent dispersibility, compositional uniformity, and reactivity.

従来Nb含有金属酸(ヒ物粉末の製造方法としては、N
b、Mg、Muの酸化物、炭酸塩等の化合物粉末を秤量
α今後、仮焼し、さらに粉砕仮焼による固相反応を何度
も繰り返して製造するいわゆる固相法がある。この方法
では粉砕時に混入する不純物のために高純度の粉末の製
造が困難であった。また粉砕によって効率よ(製造でき
る粉末の粒径は、数廊程度が限界であり、しかもその粒
径も不均一となりやすく反応性に劣ること、さらに固相
法では組成の均一性の高い粉末を得ることは困難である
。これらの固相法の欠点を改良する方法として溶液な出
発原料として粉末な製造する共沈法が知られている。こ
の方法では出発溶液として硝酸溶液、塩酸溶液、硫酸溶
液などの無機酸を用いた場合には、得られる粉体中に残
留する硝酸塩、塩化物、硫酸塩などの無機アニオン不純
物が問題となる。この無機アニオン不純物?除去するた
めに出発溶液から沈殿生成後、ろ過洗浄工程な経るのが
一般的であるが特にMgは完全に沈殿生成させることは
非常に困難であり、ろ過洗浄工程で溶出し、目的組成と
することができない欠点があった。
Conventionally, Nb-containing metal acids (N
There is a so-called solid-phase method in which compound powders such as oxides, carbonates, etc. of Mg, Mu, etc. are weighed, calcined, and then solid-phase reaction by crushing and calcining is repeated many times. With this method, it was difficult to produce highly pure powder due to impurities mixed in during pulverization. In addition, pulverization increases efficiency (the particle size of powder that can be produced is limited to a few squares, and the particle size tends to be non-uniform, resulting in poor reactivity; furthermore, the solid phase method produces powder with a highly uniform composition). As a method to improve the disadvantages of these solid-phase methods, a coprecipitation method is known in which a powder is produced using a solution starting material.In this method, a nitric acid solution, a hydrochloric acid solution, or a sulfuric acid solution is used as a starting solution. When inorganic acids such as solutions are used, inorganic anion impurities such as nitrates, chlorides, and sulfates that remain in the resulting powder pose a problem.To remove these inorganic anion impurities, precipitation is performed from the starting solution. After production, it is common to undergo a filtration and washing process, but it is particularly difficult to completely precipitate Mg, which has the disadvantage that it is eluted during the filtration and washing process, making it impossible to obtain the desired composition.

また共沈法ではNbは水酸化物であり、Mgはシュウ酸
塩であるといったように生成する沈殿の性状が異なるた
めにどうしても沈殿が分離しゃすく組成の均一性に劣る
欠点があった。したがってろ過洗浄工程をなりシ、シか
も無機アニオン不純物が入らない手法としてシュウ酸等
の有機酸溶液の噴霧熱分解法などが考えられるが、IA
gのシュウ酸酸性溶液は低濃度の溶液しか調製できない
ため非常に高価であり工業的に使用できなかった。また
、低濃度の原液しか調↓できないため熱分解の効率も低
くエネルギーコストもかかるため実際的でなかった。
In addition, in the coprecipitation method, the properties of the precipitates produced are different, such as Nb being a hydroxide and Mg being an oxalate, so that the precipitates inevitably separate, resulting in poor composition uniformity. Therefore, spray pyrolysis of an organic acid solution such as oxalic acid can be considered as a method that does not introduce inorganic anion impurities during the filtration and cleaning process, but IA
Since the oxalic acid acidic solution of g can only be prepared at a low concentration, it is very expensive and cannot be used industrially. In addition, since only a low-concentration stock solution can be prepared, the thermal decomposition efficiency is low and energy costs are high, making it impractical.

またFb(Mg1/3Nb2/z )03固溶体の場合
、PbO。
In addition, in the case of Fb(Mg1/3Nb2/z)03 solid solution, PbO.

MgO、NbzO5の粉末を出発原料にしてPb(Mg
1/5Nb2/z )03固溶体を作る際には3 Pb
O−2Nb205や2 F’bO−Nb2057’、C
ト(7) 固溶体が、副生1、−CLまイPb(Mgl
/、Nb2/3)o33固溶を形成することが非常に困
難であった。
Pb(Mg
1/5Nb2/z)03 When making a solid solution, 3Pb
O-2Nb205 or 2F'bO-Nb2057', C
(7) The solid solution is a by-product 1, -CL, Pb (Mgl
/, Nb2/3) o33 It was very difficult to form a solid solution.

〔ナショナル・テクニカル・し?−ト第23巻第1号(
1977)、第95〜102頁「Na5ion&l T
echnical Report J Vow 23 
/161(1977)95〜102」参照〕 これはMgOやNb206の粉末の反応性、MgとN’
bの組成の均一性も関係しているものと考えられ、Pl
)(Mg1/5Nb2/s )03固溶体などが形成し
ゃすいNb含有酸化物粉体を提供することは本発明の目
的の1つである。
[National Technical Shi? - Volume 23, No. 1 (
1977), pp. 95-102 “Na5ion&lT
electrical report J Vow 23
/161 (1977) 95-102]] This is due to the reactivity of MgO and Nb206 powder, and the reactivity of Mg and N'
It is thought that the uniformity of the composition of b is also related, and Pl
)(Mg1/5Nb2/s)03 It is one of the objects of the present invention to provide a Nb-containing oxide powder that does not form a solid solution or the like.

(問題点を解決するための手段) 本発明者らは高濃度、安定なシュウ酸酸性混合れた粒径
の均一なNt+含有微粉末が製造できること?見出し本
発明に至った。すなわち、本発明はNbのシュウ酸酸性
溶液とMg及び/又まMnとを反応させて得られた溶液
を熱分解することを特徴とするN’b含有微粉末の製造
方法である。
(Means for Solving the Problems) The present inventors have found that it is possible to produce Nt+-containing fine powder with a uniform particle size and a stable oxalic acid mixture at a high concentration. Heading This invention has been achieved. That is, the present invention is a method for producing N'b-containing fine powder, which is characterized by thermally decomposing a solution obtained by reacting an acidic solution of Nb with oxalic acid and Mg and/or Mn.

以下さらに詳しく本発明を説明する。The present invention will be explained in more detail below.

本発明で用いるNbシュウ酸醋酸性溶液調製法としては
特に限定されないが本出願人がさきに提案した各槌金属
の水和物の沈澱とシュウ酸粉末と?混合した復水を添加
する特願昭59−156293号の手法などが挙げられ
る。金属のMg及び/又はMnの形態としては粉末状の
ものほど反応性がよく、短時間に反応が終了するが反応
に伴う発熱及び水素気体の発生が激しいため、その粒径
が0.1〜1朋稚度のものが好ましい。
The method for preparing the Nb oxalic acid solution used in the present invention is not particularly limited, but the method of preparing the Nb oxalic acid solution is the method of preparing the hydrate of each mallet metal and the oxalic acid powder as previously proposed by the present applicant. Examples include the method disclosed in Japanese Patent Application No. 156293/1983 in which mixed condensate is added. Regarding the form of the metal Mg and/or Mn, the more reactive it is in powder form, the reaction is completed in a short time, but the heat generation and generation of hydrogen gas associated with the reaction are intense, so the particle size is 0.1~ 1 friendliness level is preferable.

またMg及び/又はMnとNbのシュウ酸酸性溶液とを
反応させる方法としては、攪拌しながら混合する一般的
な手法でよく、反応温度についても特に限定されない。
Further, as a method for reacting Mg and/or Mn with an oxalic acid solution of Nb, a general method of mixing while stirring may be used, and the reaction temperature is not particularly limited.

なお反応の際に気体を発生するので注意を要する。熱分
解する方法としては、溶液を噴霧するなどして微細な液
滴状としこれを電気炉等で加熱された反応器あるいは可
燃性ガスなどの炎中に導入して熱交換させる方法が挙げ
られ、できるだけ短時間に熱分解する手法が好ましい。
Please note that gas is generated during the reaction, so care must be taken. Examples of thermal decomposition methods include spraying a solution into fine droplets, introducing the droplets into a reactor heated with an electric furnace, or into a flame of flammable gas for heat exchange. , a method of pyrolysis in as short a time as possible is preferred.

また、これらの手法では熱分解が不完全な場合には得ら
れた粉末をさらに仮焼する。加熱された反応器で熱分解
する場合の反応器温度は600〜1300°Cが好まし
い。温度6008C未満では熱を換が不完全であり、生
産効率も低い。また温度300℃こえると設備が高価な
ものとなり実用的でない。可燃性ガスなどの炎で熱分解
する場合には液滴が急熱及び急冷をうけるため微細な粉
末を得やすく好ましい。
Furthermore, if thermal decomposition is incomplete in these methods, the obtained powder is further calcined. In the case of thermal decomposition in a heated reactor, the reactor temperature is preferably 600 to 1300°C. At temperatures below 6008C, heat exchange is incomplete and production efficiency is low. Furthermore, if the temperature exceeds 300°C, the equipment becomes expensive and impractical. In the case of thermal decomposition using a flame such as a flammable gas, the droplets are rapidly heated and cooled, so it is easy to obtain a fine powder, which is preferable.

また、熱分解が不完全な場合に行なう仮焼の仮焼温度と
しては600〜1000°Cが好ましい。
Further, the calcination temperature for calcination to be carried out when thermal decomposition is incomplete is preferably 600 to 1000°C.

温度600°Cでは熱分解の効率が低く、温度1000
°Cをこえると粉末同志が焼結して固い凝集体となりや
す(粉末の特性を低下させるので好ましくない。また仮
焼時間は焼結による凝集体をつくらないために短かい方
が効率的でもある。
At a temperature of 600°C, the efficiency of thermal decomposition is low;
If the temperature exceeds °C, the powders tend to sinter and form hard aggregates (this is not preferable as it reduces the properties of the powder.Also, it is more efficient to shorten the calcination time to prevent the formation of aggregates due to sintering. be.

以下さらに実施例な挙げて説明する。Examples will be further described below.

〔実施例〕〔Example〕

実施例1 a) ニオブのシュウ酸溶液の製造 ニオブのフッ酸溶液にアンモニア水を加えて生成した水
酸化ニオブ沈殿を充分洗浄してフッ素濃度500 pp
m以下とした。得られた水酸化ニオブ沈殿な用いてニオ
ブのシュウ酸酸性溶液を調製した。この溶液を分析した
結果、ニオブ金属濃度Q、465 mol / l シ
:zつ酸濃度1.228 mol / 1であった。な
お分析法はそれぞれ誘起結合プラズマ分析法及び酸化還
元滴定法で行なった。
Example 1 a) Production of niobium in oxalic acid solution A niobium hydroxide precipitate produced by adding ammonia water to a niobium in hydrofluoric acid solution was thoroughly washed to give a fluorine concentration of 500 pp.
m or less. An acidic solution of niobium in oxalic acid was prepared using the obtained niobium hydroxide precipitate. As a result of analyzing this solution, the niobium metal concentration Q was 465 mol/l, and the citric acid concentration was 1.228 mol/1. The analytical methods used were inductively coupled plasma analysis and redox titration, respectively.

b) ニオブ含有金属酸化物の製造 Mg : Nbの原子比が1:2となるようにニオブの
シュウ酸酸性溶液に金属Mg粉末を攪拌しながら加え、
得られた溶液を温度1000°Cに保持した縦型の電気
炉中に噴霧して得られた粉末を、さらに温度900°C
で30分間仮焼して(Mg”/3Nb2/3 )02の
微粉末を得た。この粉末の電子顕微鏡(31!iM )
写真を第1図に示す。この粉末は粒径0.1μmN度で
粒径が均一で分散性のよい粉末であった。また粉末X線
回折ではMgNb2O,単相であった。発光分析及び炭
素分析の結果不純物はいずれも数ppm以下でほとんど
含まれておらず高純度のものであった。
b) Production of niobium-containing metal oxide Add metallic Mg powder to an acidic solution of niobium in oxalic acid with stirring so that the atomic ratio of Mg:Nb is 1:2,
The obtained solution was sprayed into a vertical electric furnace maintained at a temperature of 1000°C, and the resulting powder was further heated to a temperature of 900°C.
A fine powder of (Mg''/3Nb2/3)02 was obtained by calcination for 30 minutes.This powder was examined under an electron microscope (31!iM).
A photograph is shown in Figure 1. This powder had a particle size of 0.1 μm N degrees, was uniform in particle size, and had good dispersibility. Further, powder X-ray diffraction revealed that it was MgNb2O, a single phase. As a result of emission analysis and carbon analysis, impurities were found to be highly pure with almost no impurities being contained at a few ppm or less.

またこの粉末の反応性及び組成の均一性を評価するため
Pb (Mgl/5Nb2/、)O!3組成):−ナル
上5ニPb0を混合し、温度850℃で1時間仮焼して
得られた粉末をX線回折により測定したところPb(M
g1/3Nb”/3)o3単相であツタ。その粉末X線
回折図を第2図に示す。
In addition, in order to evaluate the reactivity and compositional uniformity of this powder, Pb (Mgl/5Nb2/,)O! 3 composition): - Pb (M
g1/3Nb''/3)o3 single phase ivy. Its powder X-ray diffraction pattern is shown in Figure 2.

実施例2 Mn : Nbの原子比が1=2となるように実施例1
で得られたNbのシュウ酸酸性溶液に金属Mn粉末な加
えた以外は実施例1と同様に行なった。その結果は実施
例1と同様の特性をもった(Mn1/2Nb2//、)
02微粉末が得られた。
Example 2 Example 1 so that the atomic ratio of Mn:Nb was 1=2.
Example 1 was carried out in the same manner as in Example 1, except that metallic Mn powder was added to the oxalic acid acidic Nb solution obtained in . The results had the same characteristics as Example 1 (Mn1/2Nb2//,)
02 fine powder was obtained.

実施例3 Mg : Nb : Mnの原子比が4:8:1となる
ように実施例1で得られたNbのシュウ酸酸性溶液に金
属Mg金属Mnを加えた以外は実施例1と同様に行なっ
た。その結果は、実施例1と同様の特性?もった微粉末
が得られた。
Example 3 Same as Example 1 except that metal Mg and metal Mn were added to the oxalic acid acid solution of Nb obtained in Example 1 so that the atomic ratio of Mg:Nb:Mn was 4:8:1. I did it. Are the results similar to those in Example 1? A fine powder was obtained.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、高純度で、粒径が小さくかつ均一であ
り、分散性、組成の均一性、反応性に優れたNb含有微
粉末を効率的にしかも安価に製造することができる。
According to the present invention, it is possible to efficiently and inexpensively produce Nb-containing fine powder that is highly pure, has a small and uniform particle size, and has excellent dispersibility, compositional uniformity, and reactivity.

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

第1図及び第2図はそれぞれ実施例1で得られた粉末の
粒子構造な示すSKM写真及びX線回折図である。 特許出願人 電気化学工業株式会社 14−2−P−鵬州
FIGS. 1 and 2 are an SKM photograph and an X-ray diffraction diagram showing the particle structure of the powder obtained in Example 1, respectively. Patent applicant Denki Kagaku Kogyo Co., Ltd. 14-2-P-Pengzhou

Claims (1)

【特許請求の範囲】[Claims] Nbのシユウ酸酸性溶液とMg及び/又はMnとを反応
させて得られた溶液を熱分解することを特徴とするNb
含有金属酸化物微粉末の製法。
Nb characterized by thermally decomposing a solution obtained by reacting an oxalic acid acidic solution of Nb with Mg and/or Mn
Method for producing fine metal oxide powder.
JP20332884A 1984-09-28 1984-09-28 Production of fine poder of oxides of metal containing nb Pending JPS6183628A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20332884A JPS6183628A (en) 1984-09-28 1984-09-28 Production of fine poder of oxides of metal containing nb

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20332884A JPS6183628A (en) 1984-09-28 1984-09-28 Production of fine poder of oxides of metal containing nb

Publications (1)

Publication Number Publication Date
JPS6183628A true JPS6183628A (en) 1986-04-28

Family

ID=16472188

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20332884A Pending JPS6183628A (en) 1984-09-28 1984-09-28 Production of fine poder of oxides of metal containing nb

Country Status (1)

Country Link
JP (1) JPS6183628A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5109067A (en) * 1987-05-30 1992-04-28 Korea Chemical Co., Ltd. Process for the preparation of the modified resin and epoxy resin composition containing the modified resin for use in semiconductor encapsulation
US5366718A (en) * 1992-11-10 1994-11-22 Mizusawa Industrial Chemicals Ltd. Process for producing columbite-type niobate and process for producing perovskite-type compound therefrom
JP2012522720A (en) * 2009-04-06 2012-09-27 セルポテック エイエス Method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5109067A (en) * 1987-05-30 1992-04-28 Korea Chemical Co., Ltd. Process for the preparation of the modified resin and epoxy resin composition containing the modified resin for use in semiconductor encapsulation
US5366718A (en) * 1992-11-10 1994-11-22 Mizusawa Industrial Chemicals Ltd. Process for producing columbite-type niobate and process for producing perovskite-type compound therefrom
JP2012522720A (en) * 2009-04-06 2012-09-27 セルポテック エイエス Method
US8936731B2 (en) 2009-04-06 2015-01-20 Cerpotech As Process for the manufacture of ferroelectric materials

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