[go: up one dir, main page]

JP3668985B2 - Manufacturing method of ceramic powder - Google Patents

Manufacturing method of ceramic powder Download PDF

Info

Publication number
JP3668985B2
JP3668985B2 JP21476894A JP21476894A JP3668985B2 JP 3668985 B2 JP3668985 B2 JP 3668985B2 JP 21476894 A JP21476894 A JP 21476894A JP 21476894 A JP21476894 A JP 21476894A JP 3668985 B2 JP3668985 B2 JP 3668985B2
Authority
JP
Japan
Prior art keywords
powder
hydroxide
ceramic
ceramic powder
mixture slurry
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
Application number
JP21476894A
Other languages
Japanese (ja)
Other versions
JPH0873219A (en
Inventor
光俊 川本
幸生 浜地
国三郎 伴野
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.)
Murata Manufacturing Co Ltd
Original Assignee
Murata Manufacturing 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 Murata Manufacturing Co Ltd filed Critical Murata Manufacturing Co Ltd
Priority to JP21476894A priority Critical patent/JP3668985B2/en
Publication of JPH0873219A publication Critical patent/JPH0873219A/en
Application granted granted Critical
Publication of JP3668985B2 publication Critical patent/JP3668985B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Compositions Of Oxide Ceramics (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Ceramic Capacitors (AREA)

Description

【0001】
【産業上の利用分野】
本発明は、積層セラミックコンデンサの誘電体原料として有用な、ペロブスカイト型化合物からなるセラミック粉体の製造方法に関する。
【0002】
【従来の技術】
従来より、電子デバイスを構成するセラミック電子部品の小型高性能化を図るため、この電子部品の製造に用いられるセラミック材料の改良が行なわれてきている。
【0003】
そして、具体的に誘電体セラミック材料としては、粒径1μm以下、好ましくは0.5μm以下の均一で球形状のペロブスカイト型化合物からなるセラミック粉体の製造方法が研究されている。このような粒径のセラミック粉体は、粒径が小さいために表面エネルギ−が高くなり、粒径分布が均一で球状のために成形時の充填性がよくなって焼結性が著しく改善され、より低い温度で緻密強固なセラミックを得ることが期待できるものである。
【0004】
さらに、積層セラミックコンデンサの誘電体層の薄層化・多積層化を実現させるために、厚み10μm以下のセラミックグリ−ンシ−トが要求されているが、そのためにも、粒径1μm以下好ましくは0.5μm以下の均一で球形状のセラミック粉体が望まれている。
【0005】
ところで、従来より、ペロブスカイト型化合物からなるセラミック粉体、例えばチタン酸バリウム粉体の製造方法としては、炭酸バリウムと酸化チタンを1000℃以上の高温で仮焼して反応させてチタン酸バリウムを合成し、その後機械的に粉砕する方法(固相合成法)が知られている。
【0006】
また、その他、湿式合成法として、金属アルコキシド法、水酸化物法、水熱合成法等が知られている。
【0007】
【発明が解決しようとする課題】
しかしながら、固相合成法の場合、仮焼後のチタン酸バリウムが強く凝集しているため、機械的粉砕を行なっても粒径1μm以下の微細な粒子にするのは困難であった。また、その粒子形状は破砕物状になるため、これを任意の形状に成形して焼成した場合、焼結性に欠けるという問題点を有していた。さらに上述したように、積層セラミックコンデンサの誘電体層の薄層化・多積層化を実現させるためには、厚み10μm以下のセラミックグリ−ンシ−トを成形することが必要であるが、固相合成法で得られたチタン酸バリウム粉体を用いた場合、グリ−ンシ−トの密度が低下したり、あるいは、グリ−ンシ−トの厚みばらつきが大きくなったりするという不具合が生じていた。
【0008】
一方、湿式合成法によるペロブスカイト型化合物からなるセラミック粉体の製造であるが、金属アルコキシド法の場合、原料が高価で工業化には問題があった。
【0009】
水酸化物法については、原料も比較的安価であり、得られる粉体も焼結性が高いという点で注目されている。例えば、特開昭59−39726号公報においては、チタン塩の水溶液に塩化バリウム、硝酸バリウム等の水溶性バリウム塩を溶解させ、アルカリを加えてpHを13以上に調製して、沸点以下で加熱する方法が開示されている。しかしながら、この方法で得られるチタン酸バリウム粉体は、粒子径が0.02〜0.03μmと微細すぎるため、成形加工した場合の密度が低く、焼結時の収縮が大きくなるという問題があり、用途によっては好ましくない場合があった。
【0010】
また、特開昭60−90825号公報では、チタン酸と水酸化バリウムを多量の水の存在下で、沸点以下の温度で加熱する方法が開示されているが、この方法の場合、チタン酸をあらかじめ調製する工程が必要となるが、その際、例えばチタン酸をチタン化合物の水溶液の中和によって沈澱させた場合にはコロイド状となるため、洗浄および濾過が工業的に困難であるという問題を有していた。
【0011】
水熱合成法に関しては、積層セラミックコンデンサの薄層化・多積層化のために最適なチタン酸バリウム粉体を得ることができるとして、近年特に注目されている。たとえば、特開昭61−31345号公報では、Ba,Sr等のA群元素およびTi,Zr等のB群元素の水酸化物の所望のA/B比の混合物を水性媒体中で水熱反応させた後、水性媒体中に溶存するA群元素を水不溶性の形にして濾過、水洗、乾燥させる方法が開示されている。ところが、この場合、A群元素を水不溶性の形にするいわゆる不溶化剤の添加量を、製造ロット毎に決めなければならない煩雑さが生じてくる。つまり、水熱反応において、製造ロット毎に反応率にばらつきがあるため、そのたびごとに、濾液に溶存しているA群元素イオン濃度を分析し、その値に応じて不溶化剤の添加量を決定する必要があった。
【0012】
また、特開昭62−72525号公報では、四塩化チタンの水溶液に、バリウム等の炭酸塩、塩化物、硝酸塩のうち、いずれか1種類の化合物を溶解させ、水酸化ナトリウムまたは水酸化カリウムを加えて、オ−トクレ−ブ中で加熱する方法が開示されている。しかしながら、この方法を詳細に検討した結果、NaやK等のアルカリ金属不純物をどうしても除去することができず、例えば、合成されたチタン酸バリウム粉体中にNaやCa等が800〜1000ppm程度残存することが明らかとなった。
【0013】
そこで、本発明の目的は、粒径が0.5μm以下の均一で球形状の粒子であり、Aサイト元素とBサイト元素とのモル比が1.000±0.002の範囲にあり、結晶性が高く、かつ、アリカリ金属等の不純物が極めて少ない、ペロブスカイト型化合物からなるセラミック粉体の製造方法を提供することにある。
【0014】
【課題を解決するための手段】
上記目的を達成するため、本発明のセラミック粉体の製造方法は、Mg,Ca,Sr,BaおよびPbよりなる群から選ばれる少なくとも1種類の元素の水酸化物または塩化物と、Ti,Zr,HfおよびSnよりなる群から選ばれる少なくとも1種類の元素の水酸化物と、アルカリ性水溶液との混合物スラリ−を得る工程と、該混合物スラリ−を少なくとも2つの異なる温度で水熱反応させてペロブスカイト型化合物を得ることを特徴とする。
【0015】
【作用】
ABO3 型のペロブスカイト型化合物からなるセラミック粉体の製造において、Aサイト元素の水酸化物または塩化物とBサイト元素の水酸化物とを、OHイオンの存在下、2つの異なる温度で水熱反応させることにより、粒径が0.5μm以下の均一で球形状の粒子であり、A/Bモル比のずれがなく結晶性が高く、かつ、アルカリ金属不純物の残存量が大幅に減少したセラミック粉体が得られる。
【0016】
【実施例】
以下、本発明のセラミック粉体の製造方法について、その実施例を説明する。
(実施例1)
まず、混合物スラリーを作製した。即ち、0.1モルのTi(OC3 7 4 正確に秤量し、約30ccのイソプロピルアルコ−ルと共に、内容積約400ccのポリテトラフロロエチレン製ビ−カ−に投入した。次に、この溶液をウルトラディスパ−サ−にて撹拌しながら、0.6モルのNaOHを含有する水溶液約135ccを添加し、加水分解を行なった。その後、0.1モルのBaCl2を投入し混合物スラリーを得た。
【0017】
次に、この混合物スラリ−の入ったポリテトラフロロエチレン製ビ−カ−を、オ−トクレ−ブ装置に取り付けた。その後、温度120℃、圧力4kg/cm2の条件で、ポリテトラフロロエチレン製の撹拌棒で150rpmで撹拌させながら1時間水熱反応させた。次に、温度を200℃まで上昇させ、その状態で上述同様の方法で4時間水熱反応させた。反応終了後、水洗および濾過を繰り返した後、乾燥および解砕をへてBaTiO3 粉体を得た。
【0018】
次に、得られたBaTiO3 粉体のX線回折(XRD)分析による結晶構造、電子顕微鏡(SEM)観察による粒子状態、蛍光X線分析によるBa/Tiモル比、並びに原子吸光分析およびイオンクロマト分析による不純物量の確認を行なった。その結果、得られたBaTiO3 粉体は、立方晶のペロブスカイト構造を有し、その粒子は粒径が0.2〜0.3μmの球形状で分散性がよく、Ba/Tiモル比は1.001と殆どずれがなかった。また、BaTiO3 粉体中の不純物量は、Naが140ppm、Clが20ppmと低い値を示した。
【0019】
一方、比較のために、上記実施例と同一の混合物スラリーを120℃、1時間の条件で水熱反応させた。その結果、得られたBaTiO3 粉体は、粒子径が0.1μm前後でBa/Tiモル比が1.002であったが、不純物としてのNa量が1400ppmと非常に多いものであった。
【0020】
また、同様に比較のために、上記実施例と同一の混合物スラリーを200℃、4時間の条件で水熱反応させた。その結果、得られたBaTiO3 粉体は、不純物としてのNa量は上記実施例と同レベルに減少したが、粒子径の均一性に欠けるとともに分散性の悪いものとなった。
【0021】
(実施例2)
まず、混合物スラリーを作製した。即ち、0.1モルのTi(OC3 7 4 正確に秤量し、約30ccのイソプロピルアルコールと共に、内容積約400ccのポリテトラフロロエチレン製ビ−カ−に投入した。次に、この溶液をウルトラディスパ−サ−にて撹拌しながら、0.6モルのNaOHを含有する水溶液約135ccを添加し、加水分解を行なった。その後、0.1モルのSrCl2を投入し混合物スラリーを得た。
【0022】
次に、この混合物スラリ−を、実施例1と同様にして水熱反応させてSrTiO3 粉体を得た。
【0023】
その後、得られたSrTiO3 粉体について、実施例1と同様に、その性状等の確認を行なった。その結果、得られたSrTiO3 粉体は、立方晶のペロブスカイト構造を有し、その粒子は粒径が0.1〜0.2μmの球形状で分散性がよく、Sr/Tiモル比は0.999と殆どずれがなかった。また、SrTiO3粉体中の不純物量は、Naが160ppm、Clが20ppmと低い値を示した。
【0024】
(実施例3)
まず、混合物スラリーを作製した。即ち、0.1モルのTi(OC3 7 4を正確に秤量し、約30ccのイソプロピルアルコールと共に、内容積約400ccのポリテトラフロロエチレン製ビ−カ−に投入した。次に、この溶液をウルトラディスパ−サ−にて撹拌しながら、0.6モルのNaOHを含有する水溶液約135ccを添加し、加水分解を行なった。その後、0.1モルのSr(OH)2 を投入し混合物スラリーを得た。
【0025】
次に、この混合物スラリ−を、実施例1と同様にして水熱反応させてSrTiO3 粉体を得た。
【0026】
その後、得られたSrTiO3 粉体について、実施例1と同様に、その性状等の確認を行なった。その結果、得られたSrTiO3 粉体は、立方晶のペロブスカイト構造を有し、その粒子は粒径が0.1〜0.2μmの球形状で分散性がよく、Sr/Tiモル比は1.001と殆どずれがなかった。また、SrTiO3粉体中の不純物量は、Naが150ppm、Clが20ppmと低い値を示した。
【0027】
以上、実施例に示す通り、ABO3 型のペロブスカイト型化合物からなるセラミック粉体の製造において、Aサイト元素の水酸化物または塩化物とBサイト元素の水酸化物とを、OHイオンの存在下で120℃、1時間の条件で水熱反応させた後、さらに引き続いて200℃、4時間の条件で水熱反応させることにより、従来残存Na量が1400ppmであったものを140〜160ppmまで大幅に減少させることができた。
【0028】
なお、本製造方法において、水熱反応後のA/Bのモル比ずれを防止するためには、混合物スラリー中のOH濃度はAおよびBの仕込み濃度の少なくとも4倍、好ましくは6倍以上が必要である。上記実施例においては、AおよびBの仕込み量0.1モルの6倍の0.6モルのNaOHを添加している。
【0029】
また、上記実施例においては、BaTiO3 粉体およびSrTiO3 粉体の製造方法について説明したが、本発明はこれのみに限定されるものではない。即ち、一般式ABO3 (但し、AはMg,Ca,Sr,BaおよびPbよりなる群から選ばれる少なくとも1種類、BはTi,Zr,HfおよびSnよりなる群のうちから選ばれる少なくとも1種類)で表されるペロブスカイト型化合物、例えば、CaTiO3 ,(Ba,Ca)TiO3 ,BaZrO3 ,Ba(Ti,Zr)O3 ,(Ba,Ca)(Ti,Zr)O3 ,PbTiO3 ,Ba(Ti,Sn)O3 、Ba(Ti,Hf)O3 等の製造においても同様の効果が得られる。
【0030】
【発明の効果】
以上の説明で明らかなように、本発明のセラミック粉体の製造方法は、ABO3 型のペロブスカイト型化合物におけるAサイト元素の水酸化物または塩化物とBサイト元素の水酸化物とを、OHイオンの存在下、2つの異なる温度で水熱反応させるものである。
【0031】
これによって、0.5μm以下の均一で球形状の粒子であり、Aサイト元素とBサイト元素とのモル比が1.000±0.002の範囲にあり、結晶性が高く、かつ、アリカリ金属等の不純物が極めて少ない、ペロブスカイト型化合物からなるセラミック粉体を得ることができる。
【0032】
したがって、このセラミック粉体を用いることにより、より薄層化・多積層化した積層セラミックコンデンサを製造することができる。
[0001]
[Industrial application fields]
The present invention relates to a method for producing a ceramic powder comprising a perovskite type compound that is useful as a dielectric material for a multilayer ceramic capacitor.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, ceramic materials used for manufacturing electronic components have been improved in order to reduce the size and performance of the ceramic electronic components constituting the electronic device.
[0003]
As a dielectric ceramic material, a method for producing a ceramic powder made of a uniform and spherical perovskite compound having a particle size of 1 μm or less, preferably 0.5 μm or less has been studied. Ceramic powder with such a particle size has high surface energy due to its small particle size, and has a uniform particle size distribution and spherical shape, which improves the filling property during molding and significantly improves the sinterability. It can be expected to obtain a dense and strong ceramic at a lower temperature.
[0004]
Further, in order to realize the thinning and multi-layering of the dielectric layers of the multilayer ceramic capacitor, a ceramic green sheet having a thickness of 10 μm or less is required. For this reason, the grain size is preferably 1 μm or less. A uniform and spherical ceramic powder of 0.5 μm or less is desired.
[0005]
By the way, conventionally, a ceramic powder made of a perovskite type compound, for example, a barium titanate powder, has been synthesized by calcining barium carbonate and titanium oxide at a high temperature of 1000 ° C. or more and reacting them. Then, a method of pulverizing mechanically (solid phase synthesis method) is known.
[0006]
In addition, metal alkoxide methods, hydroxide methods, hydrothermal synthesis methods, and the like are known as wet synthesis methods.
[0007]
[Problems to be solved by the invention]
However, in the case of the solid phase synthesis method, the barium titanate after calcination is strongly agglomerated, so it was difficult to obtain fine particles having a particle diameter of 1 μm or less even by mechanical pulverization. Moreover, since the particle shape becomes a crushed material shape, when it is molded into an arbitrary shape and fired, it has a problem that it lacks sinterability. Further, as described above, in order to realize thinning and multi-layering of the dielectric layers of the multilayer ceramic capacitor, it is necessary to form a ceramic green sheet having a thickness of 10 μm or less. When the barium titanate powder obtained by the synthesis method is used, there is a problem that the density of the green sheet is reduced or the thickness variation of the green sheet is increased.
[0008]
On the other hand, the production of ceramic powder made of a perovskite type compound by a wet synthesis method, but in the case of the metal alkoxide method, the raw material was expensive and there was a problem in industrialization.
[0009]
Regarding the hydroxide method, attention has been paid in that the raw materials are relatively inexpensive and the resulting powder has high sinterability. For example, in Japanese Patent Application Laid-Open No. 59-39726, a water-soluble barium salt such as barium chloride or barium nitrate is dissolved in an aqueous solution of titanium salt, and an alkali is added to adjust the pH to 13 or higher. A method is disclosed. However, since the barium titanate powder obtained by this method has a particle diameter of 0.02 to 0.03 μm which is too fine, there is a problem that the density when molded is low and the shrinkage during sintering is large. Depending on the application, it may not be preferable.
[0010]
Japanese Patent Laid-Open No. 60-90825 discloses a method of heating titanic acid and barium hydroxide in the presence of a large amount of water at a temperature below the boiling point. A step of preparing in advance is necessary. At this time, for example, when titanic acid is precipitated by neutralization of an aqueous solution of a titanium compound, it becomes a colloidal shape, so that it is difficult to wash and filter industrially. Had.
[0011]
In recent years, the hydrothermal synthesis method has attracted particular attention because it can obtain an optimum barium titanate powder for thinning and multi-layering of multilayer ceramic capacitors. For example, in Japanese Patent Application Laid-Open No. 61-31345, a mixture of a group A element such as Ba and Sr and a hydroxide of a group B element such as Ti and Zr with a desired A / B ratio is subjected to a hydrothermal reaction in an aqueous medium. A method is disclosed in which the group A element dissolved in an aqueous medium is made into a water-insoluble form, filtered, washed and dried. However, in this case, there is a problem that the amount of so-called insolubilizing agent that makes the group A element water-insoluble must be determined for each production lot. That is, in the hydrothermal reaction, since the reaction rate varies from production lot to production lot, the concentration of group A element ions dissolved in the filtrate is analyzed each time, and the amount of insolubilizing agent added is determined according to the value. There was a need to decide.
[0012]
In JP-A-62-72525, any one compound of carbonate, chloride and nitrate such as barium is dissolved in an aqueous solution of titanium tetrachloride, and sodium hydroxide or potassium hydroxide is added. In addition, a method of heating in an autoclave is disclosed. However, as a result of examining this method in detail, alkali metal impurities such as Na and K cannot be removed. For example, about 800 to 1000 ppm of Na or Ca remains in the synthesized barium titanate powder. It became clear to do.
[0013]
Therefore, an object of the present invention is uniform and spherical particles having a particle size of 0.5 μm or less, the molar ratio of A site element to B site element is in the range of 1.000 ± 0.002, It is an object of the present invention to provide a method for producing a ceramic powder made of a perovskite type compound that has high properties and is extremely low in impurities such as ants.
[0014]
[Means for Solving the Problems]
In order to achieve the above object, a method for producing a ceramic powder according to the present invention includes a hydroxide or chloride of at least one element selected from the group consisting of Mg, Ca, Sr, Ba and Pb, and Ti, Zr. , Hf and Sn, a step of obtaining a slurry of a mixture of a hydroxide of at least one element selected from the group consisting of an alkaline aqueous solution and a hydrothermal reaction of the mixture slurry at at least two different temperatures to form a perovskite A type compound is obtained.
[0015]
[Action]
In the production of a ceramic powder composed of an ABO 3 type perovskite type compound, the A-site element hydroxide or chloride and the B-site element hydroxide are hydrothermally heated at two different temperatures in the presence of OH ions. Ceramics with uniform and spherical particles with a particle size of 0.5 μm or less, high crystallinity without deviation in A / B molar ratio, and greatly reduced residual amount of alkali metal impurities. A powder is obtained.
[0016]
【Example】
Hereinafter, the Example is demonstrated about the manufacturing method of the ceramic powder of this invention.
(Example 1)
First, a mixture slurry was prepared. That is, 0.1 mol of Ti (OC 3 H 7 ) 4 was accurately weighed and put into a polytetrafluoroethylene beaker having an internal volume of about 400 cc together with about 30 cc of isopropyl alcohol. Next, while this solution was stirred with an ultradisperser, about 135 cc of an aqueous solution containing 0.6 mol of NaOH was added for hydrolysis. Thereafter, 0.1 mol of BaCl 2 was added to obtain a mixture slurry.
[0017]
Next, the polytetrafluoroethylene beaker containing the mixture slurry was attached to an autoclave apparatus. Then, hydrothermal reaction was carried out for 1 hour while stirring at 150 rpm with a stirring rod made of polytetrafluoroethylene under the conditions of a temperature of 120 ° C. and a pressure of 4 kg / cm 2 . Next, the temperature was raised to 200 ° C., and a hydrothermal reaction was carried out for 4 hours in the same manner as described above. After completion of the reaction, washing with water and filtration were repeated, followed by drying and crushing to obtain BaTiO 3 powder.
[0018]
Next, crystal structure of the obtained BaTiO 3 powder by X-ray diffraction (XRD) analysis, particle state by electron microscope (SEM) observation, Ba / Ti molar ratio by X-ray fluorescence analysis, atomic absorption analysis and ion chromatography The amount of impurities was confirmed by analysis. As a result, the obtained BaTiO 3 powder has a cubic perovskite structure, and the particles are spherical with a particle size of 0.2 to 0.3 μm and have good dispersibility, and the Ba / Ti molar ratio is 1. There was almost no deviation from 0.001. Further, the amount of impurities in the BaTiO 3 powder was as low as 140 ppm for Na and 20 ppm for Cl.
[0019]
On the other hand, for comparison, the same mixture slurry as the above example was hydrothermally reacted at 120 ° C. for 1 hour. As a result, the obtained BaTiO 3 powder had a particle size of around 0.1 μm and a Ba / Ti molar ratio of 1.002, but the amount of Na as an impurity was very high at 1400 ppm.
[0020]
Similarly, for comparison, the same mixture slurry as in the above example was hydrothermally reacted at 200 ° C. for 4 hours. As a result, the amount of Na as an impurity was reduced to the same level as in the above examples, but the resulting BaTiO 3 powder was not uniform in particle diameter and poor in dispersibility.
[0021]
(Example 2)
First, a mixture slurry was prepared. That is, 0.1 mol of Ti (OC 3 H 7 ) 4 was accurately weighed and introduced into a polytetrafluoroethylene beaker having an internal volume of about 400 cc together with about 30 cc of isopropyl alcohol. Next, while this solution was stirred with an ultradisperser, about 135 cc of an aqueous solution containing 0.6 mol of NaOH was added for hydrolysis. Thereafter, 0.1 mol of SrCl 2 was added to obtain a mixture slurry.
[0022]
Next, this mixture slurry was subjected to a hydrothermal reaction in the same manner as in Example 1 to obtain SrTiO 3 powder.
[0023]
Thereafter, the properties and the like of the obtained SrTiO 3 powder were confirmed in the same manner as in Example 1. As a result, the obtained SrTiO 3 powder has a cubic perovskite structure, the particles have a spherical shape with a particle size of 0.1 to 0.2 μm and good dispersibility, and the Sr / Ti molar ratio is 0. There was almost no deviation from 999. Moreover, the amount of impurities in the SrTiO 3 powder was as low as 160 ppm for Na and 20 ppm for Cl.
[0024]
(Example 3)
First, a mixture slurry was prepared. That is, 0.1 mol of Ti (OC 3 H 7 ) 4 was accurately weighed and introduced into a polytetrafluoroethylene beaker having an internal volume of about 400 cc together with about 30 cc of isopropyl alcohol. Next, while this solution was stirred with an ultradisperser, about 135 cc of an aqueous solution containing 0.6 mol of NaOH was added for hydrolysis. Thereafter, 0.1 mol of Sr (OH) 2 was added to obtain a mixture slurry.
[0025]
Next, this mixture slurry was subjected to a hydrothermal reaction in the same manner as in Example 1 to obtain SrTiO 3 powder.
[0026]
Thereafter, the properties and the like of the obtained SrTiO 3 powder were confirmed in the same manner as in Example 1. As a result, the obtained SrTiO 3 powder has a cubic perovskite structure, and the particles are spherical with a particle size of 0.1 to 0.2 μm and have good dispersibility, and the Sr / Ti molar ratio is 1 There was almost no deviation from 0.001. Moreover, the amount of impurities in the SrTiO 3 powder was as low as 150 ppm for Na and 20 ppm for Cl.
[0027]
As described above, in the production of the ceramic powder composed of the ABO 3 type perovskite type compound, the hydroxide or chloride of the A site element and the hydroxide of the B site element are produced in the presence of OH ions. Hydrothermal reaction at 120 ° C. for 1 hour at 200 ° C., followed by further hydrothermal reaction at 200 ° C. for 4 hours to greatly increase the residual Na content from 1400 ppm to 140-160 ppm. Could be reduced.
[0028]
In this production method, the OH concentration in the mixture slurry is at least 4 times, preferably 6 times or more of the charged concentrations of A and B, in order to prevent the A / B molar ratio shift after the hydrothermal reaction. is necessary. In the above embodiment, 0.6 mol of NaOH, which is 6 times the amount of 0.1 mol of A and B, is added.
[0029]
In the above embodiment has been described manufacturing method of the BaTiO 3 powder and SrTiO 3 powder, the present invention is not limited only thereto. That is, the general formula ABO 3 (where A is at least one selected from the group consisting of Mg, Ca, Sr, Ba and Pb, and B is at least one selected from the group consisting of Ti, Zr, Hf and Sn) ), For example, CaTiO 3 , (Ba, Ca) TiO 3 , BaZrO 3 , Ba (Ti, Zr) O 3 , (Ba, Ca) (Ti, Zr) O 3 , PbTiO 3 , Similar effects can be obtained in the production of Ba (Ti, Sn) O 3 , Ba (Ti, Hf) O 3, and the like.
[0030]
【The invention's effect】
As is apparent from the above description, the method for producing a ceramic powder of the present invention comprises a hydroxide or chloride of an A site element and a hydroxide of a B site element in an ABO 3 type perovskite compound. Hydrothermal reaction is carried out at two different temperatures in the presence of ions.
[0031]
Accordingly, the particles are uniform and spherical particles of 0.5 μm or less, the molar ratio of the A site element to the B site element is in the range of 1.000 ± 0.002, the crystallinity is high, and the ant pottery metal Thus, a ceramic powder made of a perovskite type compound with very little impurities such as can be obtained.
[0032]
Therefore, by using this ceramic powder, it is possible to manufacture a monolithic ceramic capacitor having a thinner and multi-layered structure.

Claims (1)

Mg,Ca,Sr,BaおよびPbよりなる群から選ばれる少なくとも1種類の元素の水酸化物または塩化物と、Ti,Zr,HfおよびSnよりなる群から選ばれる少なくとも1種類の元素の水酸化物と、アルカリ性水溶液との混合物スラリ−を得る工程と、該混合物スラリ−を少なくとも2つの異なる温度で水熱反応させてペロブスカイト型化合物を得ることを特徴とするセラミック粉体の製造方法。Hydroxide or chloride of at least one element selected from the group consisting of Mg, Ca, Sr, Ba and Pb and hydroxylation of at least one element selected from the group consisting of Ti, Zr, Hf and Sn A process for obtaining a mixture slurry of a product and an alkaline aqueous solution, and a hydrothermal reaction of the mixture slurry at at least two different temperatures to obtain a perovskite type compound.
JP21476894A 1994-09-08 1994-09-08 Manufacturing method of ceramic powder Expired - Fee Related JP3668985B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21476894A JP3668985B2 (en) 1994-09-08 1994-09-08 Manufacturing method of ceramic powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21476894A JP3668985B2 (en) 1994-09-08 1994-09-08 Manufacturing method of ceramic powder

Publications (2)

Publication Number Publication Date
JPH0873219A JPH0873219A (en) 1996-03-19
JP3668985B2 true JP3668985B2 (en) 2005-07-06

Family

ID=16661221

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21476894A Expired - Fee Related JP3668985B2 (en) 1994-09-08 1994-09-08 Manufacturing method of ceramic powder

Country Status (1)

Country Link
JP (1) JP3668985B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003004415A1 (en) * 2001-07-04 2003-01-16 Toho Titanium Co., Ltd. Barium titanate powder and method for production thereof
JP4626207B2 (en) * 2004-07-28 2011-02-02 Tdk株式会社 Method for producing barium titanate powder
KR101158953B1 (en) 2005-02-25 2012-06-21 사까이가가꾸고오교가부시끼가이샤 Method for producing composition
JP4967599B2 (en) * 2006-10-23 2012-07-04 Tdk株式会社 Barium titanate powder, dielectric ceramic composition and electronic component
WO2015152237A1 (en) * 2014-03-31 2015-10-08 戸田工業株式会社 Strontium titanate fine particle powder and method for producing same

Also Published As

Publication number Publication date
JPH0873219A (en) 1996-03-19

Similar Documents

Publication Publication Date Title
EP0641740B1 (en) Process for the synthesis of crystalline ceramic powders of perovskite compounds
US4520004A (en) Method of manufacturing metal titanate fine powder
US4677083A (en) Method for manufacturing dielectric fine powder of Ba1-x Srx TiO3
US5445806A (en) Process for preparing fine powder of perovskite-type compound
US7556792B2 (en) Method for preparing perovskite complex oxide powder of formula ABO3
KR101625156B1 (en) Process of preparing titanates
US7001585B2 (en) Method of making barium titanate
US8715614B2 (en) High-gravity reactive precipitation process for the preparation of barium titanate powders
US4810484A (en) Method for manufacturing fine lead titanate powders
JPH0339018B2 (en)
JP3319807B2 (en) Perovskite-type compound fine particle powder and method for producing the same
JP3772354B2 (en) Manufacturing method of ceramic powder
JP3668985B2 (en) Manufacturing method of ceramic powder
JP3838523B2 (en) Method for producing the composition
EP0104002B1 (en) Methods of manufacturing metal titanate fine powders
KR102190834B1 (en) Method for producing barium titanate powder
JPH0339014B2 (en)
JPH0246531B2 (en)
EP1860069B1 (en) Method for producing composition
KR100647247B1 (en) Synthesis method of barium titanate powder by solvent thermal method
KR100290247B1 (en) Method for manufacturing barium titanate and perovskite type composite oxide
JPH0339015B2 (en)
EP0163739A1 (en) Process for preparing fine particles of ba (zrx ti 1-x)o3-solid solution
KR20060102928A (en) Method for producing barium titanate powder
JPH01122907A (en) Production of perovskite oxide powder

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040409

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040629

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050322

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050404

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090422

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090422

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100422

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110422

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees