JPH0367966B2 - - Google Patents
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- JPH0367966B2 JPH0367966B2 JP60203359A JP20335985A JPH0367966B2 JP H0367966 B2 JPH0367966 B2 JP H0367966B2 JP 60203359 A JP60203359 A JP 60203359A JP 20335985 A JP20335985 A JP 20335985A JP H0367966 B2 JPH0367966 B2 JP H0367966B2
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- perovskite
- oxygen
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Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ペロブスカイト型構造化合物(以
下、ペロブスカイトという)およびその固溶体の
原料粉末の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing a raw material powder of a perovskite structure compound (hereinafter referred to as perovskite) and a solid solution thereof.
ペロブスカイトおよびその固溶体は、圧電体、
誘電体、半導体、センサー、オプトエレクトロニ
クス材料等の機能性セラミツクスとして広範囲に
利用されている。最近はこの機能性セラミツクス
の高度化が進展し、その要請に対応できる易焼結
性、均一性、高嵩密度で、且つ低コストのペロブ
スカイトおよびその固溶体の原料粉末が多量に効
率的に製造できる技術の開発が要望されている。 Perovskites and their solid solutions are piezoelectric materials,
It is widely used as functional ceramics for dielectrics, semiconductors, sensors, optoelectronic materials, etc. Recently, the sophistication of functional ceramics has progressed, and raw material powders of perovskite and its solid solution that meet these demands can be produced efficiently in large quantities with easy sinterability, uniformity, high bulk density, and low cost. Development of technology is required.
従来、ペロブスカイトおよびその固溶体の原料
粉末の製造方法としては、乾式法と共沈法が知ら
れている。 Conventionally, dry methods and coprecipitation methods are known as methods for producing raw material powders of perovskites and solid solutions thereof.
乾式法は構成原料成分の化合物を乾式で混合
し、これを仮焼する方法である。しかし、この方
法では、均一組成の原料粉末が得難いため、優れ
た機能性を持つペロブスカイトおよびその固溶体
を得難いし、また焼結性も十分ではない。 The dry method is a method in which compounds of constituent raw materials are mixed in a dry method and then calcined. However, with this method, it is difficult to obtain a raw material powder with a uniform composition, so it is difficult to obtain a perovskite and its solid solution with excellent functionality, and the sinterability is also not sufficient.
共沈法はその構成成分のすべてを一緒にした混
合溶液を作り、これにアルカリ等の沈殿形成液を
添加して共沈させ、この共沈物を乾燥、仮焼させ
る方法である。 The coprecipitation method is a method in which a mixed solution is prepared by combining all of the constituent components, a precipitate-forming liquid such as an alkali is added to the mixed solution to cause coprecipitation, and this coprecipitate is dried and calcined.
この共沈法によると、均一性の優れた粉末が得
易いが、その均一性なるが故に、沈殿生成時、乾
燥時または仮焼時に粒子が凝結して二次粒子を形
成し、易焼結性になりにくい欠点があつた。 According to this coprecipitation method, it is easy to obtain powder with excellent uniformity, but because of its uniformity, the particles coagulate during precipitation, drying, or calcination to form secondary particles, making it easier to sinter. I had a flaw that made it difficult to become sexually sensitive.
また、共沈法では各成分の該沈殿形成液に対す
る沈殿形成能が同じでない場合は、例えば或成分
は100%沈殿を生成するが、他の成分は全部沈殿
を生成し得ないことが起り、所望組成となし難い
ことがある。 In addition, in the coprecipitation method, if the precipitate forming ability of each component in the precipitate forming liquid is not the same, for example, a certain component may form 100% precipitate, but other components may not be able to form any precipitate. It may be difficult to achieve the desired composition.
更に、ペロブスカイト機能材料には鉛とチタン
を同時に含むことが極めて多い。この様なものを
工業的に製造する場合、チタン原料として安価な
四塩化チタンを使用することが望ましい。しかし
これを共沈法に使用すると、四塩化チタン中の塩
素イオンが鉛と反応して白色沈殿を生成するた
め、使用し難い。この場合、四塩化チタンに代
え、オキシ硝酸チタン〔TiO(NO3)2〕を使用す
ればこの白色沈殿の生成を防ぐことができるが、
オキシ硝酸チタンは高価であるため工業生産とし
ては実用的でない。 Furthermore, perovskite functional materials very often contain lead and titanium at the same time. When producing such materials industrially, it is desirable to use inexpensive titanium tetrachloride as the titanium raw material. However, when this is used in the coprecipitation method, the chlorine ions in titanium tetrachloride react with lead to produce a white precipitate, making it difficult to use. In this case, the formation of this white precipitate can be prevented by using titanium oxynitrate [TiO(NO 3 ) 2 ] instead of titanium tetrachloride.
Titanium oxynitrate is expensive and therefore not practical for industrial production.
本発明は従来の共沈法における欠点をなくすこ
とができる方法、さらには、湿式法によつて、易
焼結性、均一性、低コスト、高嵩密度の四つの要
件を満足したペロブスカイトおよびその固溶体原
料粉末を効率よく製造することができる方法を提
供するにある。
The present invention uses a method that can eliminate the drawbacks of conventional coprecipitation methods, and furthermore, a perovskite that satisfies the four requirements of easy sinterability, uniformity, low cost, and high bulk density, and its perovskite. An object of the present invention is to provide a method for efficiently producing solid solution raw material powder.
本発明者らは前記目的を達成すべく鋭意研究の
結果、一般式ABO3(ただし、Aは酸素12配位金
属元素の1種または2種以上を、Bは酸素6配位
金属元素の1種または2種以上を示す。)で表わ
されるペロブスカイトおよびその固溶体の原料粉
末を湿式法で製造する際に、アミノ酸類の存在下
に、A成分とB成分の沈殿を遂次に生成させる
と、微粒子が高度に相互分散した均一粒子の沈殿
物が得られ、該沈殿物を仮焼して得られる原料粉
末は粒度分布が狭く、粒度が揃つた微粒子からな
つており、しかも組成が均一であり、極めて工業
的に有利に易焼結性ペロブスカイト原料粉末を製
造できることを知見し、本発明に到達した。
As a result of intensive research to achieve the above object, the present inventors found that the general formula ABO 3 (where A represents one or more of the 12-coordinated metal elements of oxygen, and B represents 1 of the 6-coordinated metal elements of oxygen) When producing a raw material powder of perovskite and its solid solution represented by (species or two or more species) by a wet method, precipitation of component A and component B is sequentially produced in the presence of amino acids. A precipitate of uniform particles in which fine particles are highly mutually dispersed is obtained, and the raw material powder obtained by calcining the precipitate has a narrow particle size distribution, consists of fine particles with uniform particle size, and has a uniform composition. It was discovered that easily sinterable perovskite raw material powder can be manufactured very industrially advantageously, and the present invention was achieved.
本発明は、一般式ABO3(ただし、Aは酸素12
配位金属元素の1種または2種以上を、Bは酸素
6配位金属元素の1種または2種以上を示す。)
で表わされるペロブスカイト型構造化合物(以下
ペロブスカイトという)およびその固溶体の原料
粉末を、A成分の金属元素を含んだ化合物の水溶
液と沈殿形成液とにより沈殿を生成させ、次いで
B成分の金属元素を含んだ化合物の水溶液と沈殿
形成液とにより沈殿を生成させるか、あるいはA
成分とB成分の沈殿の生成を前記と順序を代えて
生成させた後、沈殿物を仮焼することによつて製
造する際、前記各沈殿をアミノ酸類の存在下に生
成させることを特徴とする易焼結性ペロブスカイ
ト粉末の製造方法に関するものである。 The present invention is based on the general formula ABO 3 (where A is oxygen 12
B represents one or more types of coordination metal elements, and B represents one or more types of oxygen 6-coordination metal elements. )
A raw material powder of a perovskite-type structural compound (hereinafter referred to as perovskite) and its solid solution represented by the above is precipitated with an aqueous solution of a compound containing a metal element as an A component and a precipitation forming liquid, and then a precipitate is formed using a precipitate forming solution containing a metal element as an A component. A precipitate is generated by an aqueous solution of the compound and a precipitate forming solution, or
When the precipitates of the component and B component are produced in a different order from the above and then the precipitates are calcined, each of the precipitates is produced in the presence of amino acids. The present invention relates to a method for producing easily sinterable perovskite powder.
本発明によると、従来の共沈法における欠点を
解消することができる。 According to the present invention, the drawbacks of conventional coprecipitation methods can be overcome.
前記一般式ABO3のA成分の酸素12配位金属元
素として、例えば、Pb、Ba、Ca、Sr及びLa等
の稀土類元素が挙げられる。またB成分の酸素6
配位金属元素としては、例えば、Ti、Zr、Mg、
Sc、Hf、W、Nb、Ta、Cr、Mo、Mn、Fe、
Co、Ni、Zn、Cd、Al、Sn、As、Bi等が挙げら
れる。 Examples of the oxygen 12-coordination metal element of the A component of the general formula ABO 3 include rare earth elements such as Pb, Ba, Ca, Sr, and La. Also, the B component oxygen 6
Examples of coordination metal elements include Ti, Zr, Mg,
Sc, Hf, W, Nb, Ta, Cr, Mo, Mn, Fe,
Examples include Co, Ni, Zn, Cd, Al, Sn, As, Bi, etc.
ペロブスカイトおよびその固溶体の構成成分で
あるA成分、B成分の金属元素を含む化合物の水
溶液を調整するための成分化合物としては、特に
限定されないがそれらの水酸化物、炭酸塩、オキ
シ塩、硫酸塩、硝酸塩、塩化物等の無機塩、酢酸
塩、しゆう酸塩等の有機酸塩、酸化物などがあ
る。これらは一般に水溶液として使用される。水
に可溶でない場合には酸を添加して可溶させれば
よい。 Component compounds for preparing an aqueous solution of compounds containing metal elements of component A and component B, which are constituent components of perovskite and its solid solution, include, but are not particularly limited to, their hydroxides, carbonates, oxysalts, and sulfates. , inorganic salts such as nitrates and chlorides, organic acid salts such as acetates and oxalates, and oxides. These are generally used as aqueous solutions. If it is not soluble in water, an acid may be added to make it soluble.
本発明に使用するアミノ酸類としては、特に限
定されないが、例えば、H2NCnH2nCOOH(ただ
し、nは、1、2または3を示す。)で表わされ
るグリシン、γ−アミノ酪酸、β−アラニン等の
低級脂肪族アミノ酸が好適である。アミノ酸類の
使用量は、一般にはA成分の金属元素を含んだ化
合物とB成分の金属元素を含んだ化合物との合計
の全モル数に対して、0.01〜20、好ましくは0.1
〜15倍モルが適当である。 The amino acids used in the present invention are not particularly limited, but include, for example, glycine represented by H 2 NCnH 2 nCOOH (where n represents 1, 2 or 3), γ-aminobutyric acid, β-alanine Lower aliphatic amino acids such as are preferred. The amount of amino acids to be used is generally 0.01 to 20, preferably 0.1 to the total number of moles of the compound containing a metal element as component A and the compound containing a metal element as component B.
~15 times the molar amount is appropriate.
沈殿形成液としては、アンモニア、炭酸アンモ
ニウム、苛性アルカリ、しゆう酸等が挙げられ
る。 Examples of the precipitation forming liquid include ammonia, ammonium carbonate, caustic alkali, oxalic acid, and the like.
構成成分の沈殿を生成させるにあたつてはアミ
ノ酸類の存在下、沈殿形成液を撹拌しながら、沈
殿形成液に、各構成成分の水溶液を添加してもよ
く、その反対に添加してもよい。添加に際しては
液を十分に撹拌しながら行うことが好ましい。 To generate a precipitate of the constituent components, an aqueous solution of each constituent component may be added to the precipitate forming liquid while stirring the precipitate forming liquid in the presence of amino acids, or vice versa. good. It is preferable that the addition be carried out while sufficiently stirring the liquid.
また沈殿の生成に際し、例えば一つの成分の沈
殿を生成した後、陰イオンを除去するために水洗
した後、沈殿物を新しい水またはアルコール中に
分散して、さらにアミノ酸類の存在下、他成分の
水溶液と沈殿形成液を添加して沈殿を生成しても
よい。 In addition, when forming a precipitate, for example, after forming a precipitate of one component, washing with water to remove anions, dispersing the precipitate in fresh water or alcohol, and then dispersing the precipitate of another component in the presence of amino acids. A precipitate may be generated by adding an aqueous solution of and a precipitate forming liquid.
更にまたアミノ酸類の存在下にA成分またはB
成分の沈殿を生成した後、沈殿形成液の種類と濃
度を適当に選ぶことによつて、前記以外の金属元
素を含んだ化合物の沈殿を生成してもよい。 Furthermore, in the presence of amino acids, component A or component B
After the components are precipitated, compounds containing metal elements other than those mentioned above may be precipitated by appropriately selecting the type and concentration of the precipitate forming liquid.
またA成分、B成分のほかに、ペロブスカイト
の焼結性や特性を制御するための微量成分を添加
する場合はA成分、B成分の溶液を調整する際、
それらの微量成分を添加させてもよい。また、必
要に応じて前記したようにA成分およびB成分の
沈殿の生成を、多段にしてもよく、更に交互に沈
殿させてもよい。しかし各々の成分の沈殿を生成
させる際には、アミン酸類を存在させておくこと
が必要である。 In addition to A and B components, when adding trace components to control the sinterability and properties of perovskite, when preparing the solution of A and B components,
Minor amounts of these components may also be added. Further, if necessary, as described above, the precipitation of component A and component B may be formed in multiple stages, or may be caused to precipitate alternately. However, when forming a precipitate of each component, it is necessary to have an amine acid present.
前記方法により得られた沈殿物は通常の方法に
より洗浄、ろ別、乾燥した後、仮焼する。乾燥
は、大気圧下で行なつても減圧下で行なつてもよ
い。 The precipitate obtained by the above method is washed, filtered, dried, and then calcined by a conventional method. Drying may be carried out under atmospheric pressure or under reduced pressure.
仮焼温度としては、過度に低いと沈殿物の脱
水、熱分解が不十分であり、また過度に高いと粉
末が粗大化するので、通常、仮焼温度は300〜
1000℃の範囲が好適である。 If the calcination temperature is too low, dehydration and thermal decomposition of the precipitate will be insufficient, and if it is too high, the powder will become coarse, so the calcination temperature is usually 300-300℃.
A range of 1000°C is preferred.
以下に実施例および比較例を示し、さらに詳し
く本発明について説明する。
EXAMPLES The present invention will be explained in more detail by showing Examples and Comparative Examples below.
実施例 1
グリシン0.2モルと28重量%アンモニア水400ml
を水1に溶解してアンモニア−グリシン混合水
溶液を作成した。この溶液を撹拌しながら、硝酸
塩0.2モル、オキシ塩化ジルコニウム0.1モルを水
1中に溶解して作成したPb2+とZr4+の混合水
溶液を滴下して白色のPbとZrの水酸化物共沈殿
を生成させた。この沈殿スラリーを撹拌しながら
四塩化チタン0.1モルを300mlの水に溶解した溶液
を添加混合して、Pb、ZrおよびTiの水酸化物の
均密沈殿を作つた。この沈殿物を洗浄した後、乾
燥し、600℃で約2時間仮焼してPb(Zr0.5Ti0.5)
O3粉末を得た。この粉末をボールミルで粉砕し
た。Example 1 0.2 mol of glycine and 400 ml of 28% by weight ammonia water
was dissolved in water 1 to prepare an ammonia-glycine mixed aqueous solution. While stirring this solution, a mixed aqueous solution of Pb 2+ and Zr 4+ prepared by dissolving 0.2 mol of nitrate and 0.1 mol of zirconium oxychloride in 1 part of water was added dropwise to form white Pb and Zr hydroxides. A precipitate formed. A solution prepared by dissolving 0.1 mol of titanium tetrachloride in 300 ml of water was added and mixed to this precipitate slurry while stirring to form a homogeneous precipitate of hydroxides of Pb, Zr, and Ti. After washing this precipitate, it was dried and calcined at 600℃ for about 2 hours to form Pb(Zr 0.5 Ti 0.5 ).
Obtained O3 powder. This powder was ground in a ball mill.
この粉末を透過型電子顕微鏡により観察した結
果、平均粒子径は、0.16μmであり、その粒度分
布は、0.10〜0.20μmで非常に良く粒子が揃つて
いた。 As a result of observing this powder using a transmission electron microscope, the average particle diameter was 0.16 μm, and the particle size distribution was 0.10 to 0.20 μm, indicating that the particles were very well aligned.
この粉末を1t/cm2で成型し、鉛蒸気と酸素雰囲
気下、1100℃で約3時間焼結した結果、その密度
は7.97g/c.c.で殆んど理論密度に近かつた。 This powder was molded at 1 t/cm 2 and sintered at 1100° C. for about 3 hours in a lead vapor and oxygen atmosphere, resulting in a density of 7.97 g/cc, which is almost the theoretical density.
比較例 1
沈殿形成時にグリシンを共存させなかつた以外
は実施例1と同様な操作を行いPb(Zr0.5Ti0.5)O3
仮焼粉末を得た。Comparative Example 1 Pb(Zr 0.5 Ti 0.5 ) O 3 was produced in the same manner as in Example 1, except that glycine was not present during precipitate formation.
A calcined powder was obtained.
この粉末を走査型電子顕微鏡により形状観察し
たところ、平均粒子径(50個平均)は、0.3μmで
あり、その粒度分布は、0.10〜0.39μmであり実
施例1と比較して平均粒子径が大きく、粒度分布
も広かつた。 When the shape of this powder was observed using a scanning electron microscope, the average particle size (average of 50 particles) was 0.3 μm, and the particle size distribution was 0.10 to 0.39 μm. It was large and had a wide particle size distribution.
またこの粉末を1t/cm2で成型し、鉛蒸気と酸素
雰囲気下、1100℃で約3時間焼結した結果、その
密度は7.85g/c.c.で、実施例1と比較して低かつ
た。 Further, this powder was molded at 1 t/cm 2 and sintered at 1100° C. for about 3 hours in a lead vapor and oxygen atmosphere, resulting in a density of 7.85 g/cc, which was lower than that of Example 1.
実施例 2
実施例1においてグリシンの使用量0.2モルの
代りに1.0モルとした以外は実施例1と同様な操
作を行いPb(Zr0.5Ti0.5)O3仮焼粉末を得た。Example 2 A Pb(Zr 0.5 Ti 0.5 ) O 3 calcined powder was obtained by carrying out the same operation as in Example 1 except that the amount of glycine used in Example 1 was 1.0 mol instead of 0.2 mol.
この粉末を透過型電子顕微鏡により粒子観察し
たところ、平均粒子径(50個)は、0.15μmであ
り、その粒度分布は0.07〜0.19μmであつた。 Particle observation of this powder using a transmission electron microscope revealed that the average particle diameter (50 particles) was 0.15 μm, and the particle size distribution was 0.07 to 0.19 μm.
またこの粉末を1t/cm2で成型し、鉛蒸気と酸素
雰囲気下、1100℃で約3時間焼結した結果、その
密度は7.97であつた。 This powder was molded at 1 t/cm 2 and sintered at 1100° C. for about 3 hours in a lead vapor and oxygen atmosphere, resulting in a density of 7.97.
実施例 3
実施例1においてグリシンの代りにβ−アラニ
ンを使用した以外は実施例1と同様な操作を行い
Pb(Zr0.5Ti0.5)O3仮焼粉末を得た。Example 3 The same procedure as in Example 1 was performed except that β-alanine was used instead of glycine in Example 1.
Pb(Zr 0.5 Ti 0.5 ) O 3 calcined powder was obtained.
この粉末を粒子観察したところ、平均粒子径は
0.17μmであつた。 When observing the particles of this powder, the average particle size was
It was 0.17 μm.
またこの粉末を1t/cm2で成型し、鉛蒸気と酸素
雰囲気下、1100℃で約3時間焼結したところ、そ
の密度は7.95g/c.c.で殆んど理論密度に近かつ
た。 When this powder was molded at 1 t/cm 2 and sintered at 1100° C. for about 3 hours in an atmosphere of lead vapor and oxygen, its density was 7.95 g/cc, almost the theoretical density.
実施例 4
硝酸鉛〔Pb(NO3)2〕60.28g、硝酸ランタン
〔La(NO3)3・6H2O〕7.79gを溶解した水溶液1
を、グリシン75gを含む2N−アンモニア水1
中に撹拌下に滴下して共沈物を作つた。この沈
殿物の分散した溶液を撹拌しつつ、グリシン15
g、オキシ塩化ジルコニウム(ZrOCl2・8H2O)
40.97gおよび四塩化チタン13.09gを水300c.c.に
溶解した水溶液を滴下して、鉛、ランタン、ジル
コニウム、チタンの水酸化物の均密沈殿を得た。
この沈殿をアンモニア水で洗浄し、ろ別、乾燥し
た。Example 4 Aqueous solution 1 in which 60.28 g of lead nitrate [Pb(NO 3 ) 2 ] and 7.79 g of lanthanum nitrate [La(NO 3 ) 3.6H 2 O] were dissolved.
1 of 2N ammonia water containing 75g of glycine
was added dropwise to the solution while stirring to form a coprecipitate. While stirring the dispersed solution of this precipitate, glycine 15
g, zirconium oxychloride (ZrOCl 2 8H 2 O)
An aqueous solution of 40.97 g of titanium tetrachloride and 13.09 g of titanium tetrachloride dissolved in 300 c.c. of water was added dropwise to obtain a homogeneous precipitate of hydroxides of lead, lanthanum, zirconium, and titanium.
This precipitate was washed with aqueous ammonia, filtered, and dried.
さらに、この乾燥粉末を750℃で約2時間熱処
理して、Pb0.91La0.09(Zr0.65Ti0.35)0.9775O3の組成
の粉末を得た。 Furthermore, this dry powder was heat-treated at 750° C. for about 2 hours to obtain a powder having a composition of Pb 0.91 La 0.09 (Zr 0.65 Ti 0.35 ) 0.9775 O 3 .
この粉末をエタノール存在下でボールミル処理
し、その一部分を走査型電子顕微鏡により粒子を
観察した結果、平均粒子径は0.095μmで、その粒
度分布は0.05〜0.140μmであり、ほぼ均一粒子径
を有していた。またX線回折法で組成変動を測定
した結果、変動が認められなかつた。 This powder was ball-milled in the presence of ethanol, and part of it was observed using a scanning electron microscope. As a result, the average particle size was 0.095 μm, and the particle size distribution was 0.05 to 0.140 μm, indicating that the particle size was almost uniform. Was. Further, as a result of measuring compositional fluctuations using X-ray diffraction, no fluctuations were observed.
この粉末を1.5t/cm2で成型し、酸素ガスと鉛蒸
気の混合雰囲気下で常圧1100℃で40時間焼結し
た。これにより密度は7.80であり、透過率75%
(1mm厚さ)の透光性PLZTが得られた。 This powder was molded at 1.5 t/cm 2 and sintered at normal pressure of 1100° C. for 40 hours in a mixed atmosphere of oxygen gas and lead vapor. This gives a density of 7.80 and a transmittance of 75%
(1 mm thickness) translucent PLZT was obtained.
本発明の方法により沈殿を生成させる際、アミ
ノ酸類の存在下に逐次に沈殿を生成させると、微
粒子で均一粒子が高度に相互分散した状態の沈殿
物が得られる結果、仮焼時に凝結を起しにくく、
易焼結性の粒度分布が狭い均一な微粒子からなる
粉末を再現性良く製造することができる。
When a precipitate is generated by the method of the present invention, if the precipitate is sequentially generated in the presence of amino acids, a precipitate in which fine and uniform particles are highly interdispersed is obtained, resulting in coagulation during calcination. difficult to do,
Powder consisting of uniform fine particles with a narrow particle size distribution that is easily sinterable can be produced with good reproducibility.
また本プロセスでは各相が高度に相互分散して
おり、従つてこのものを仮焼したものは十分な均
一性が達成される。さらにプロセスが簡単である
ことに由来して、再現性良く低コストで易焼結性
の粉末が得られる等の優れた効果を有する。 In addition, in this process, each phase is highly mutually dispersed, so that the calcined material achieves sufficient uniformity. Further, since the process is simple, it has excellent effects such as being able to obtain easily sinterable powder with good reproducibility and at low cost.
Claims (1)
元素の1種または2種以上を、Bは酸素6配位金
属元素の1種または2種以上を示す。)で表わさ
れるペロブスカイト型構造化合物(以下ペロブス
カイトという)およびその固溶体の原料粉末を、
A成分の金属元素を含んだ化合物の水溶液と沈殿
形成液とにより沈殿を生成させ、次いでB成分の
金属元素を含んだ化合物の水溶液と沈殿形成液と
により沈殿を生成させるか、あるいはA成分とB
成分の沈殿の生成を前記と順序を代えて生成させ
た後、沈殿物を仮焼することによつて製造する
際、前記各沈殿をアミノ酸類の存在下に生成させ
ることを特徴とする易焼結性ペロブスカイト粉末
の製造方法。1 Perovskite structure represented by the general formula ABO 3 (where A represents one or more 12-coordinated metal elements of oxygen, and B represents one or more 6-coordinated metal elements of oxygen). The raw material powder of the compound (hereinafter referred to as perovskite) and its solid solution is
A precipitate is generated by an aqueous solution of a compound containing a metal element of component A and a precipitate forming liquid, and then a precipitate is generated by an aqueous solution of a compound containing a metal element of component B and a precipitate forming liquid, or B
An easy-to-sinter method characterized in that each of the precipitates is produced in the presence of amino acids when the precipitates of the components are produced in a different order from the above and then the precipitates are calcined. A method for producing crystalline perovskite powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60203359A JPS6265907A (en) | 1985-09-17 | 1985-09-17 | Method for producing easily sinterable perovskite powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60203359A JPS6265907A (en) | 1985-09-17 | 1985-09-17 | Method for producing easily sinterable perovskite powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6265907A JPS6265907A (en) | 1987-03-25 |
| JPH0367966B2 true JPH0367966B2 (en) | 1991-10-24 |
Family
ID=16472723
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60203359A Granted JPS6265907A (en) | 1985-09-17 | 1985-09-17 | Method for producing easily sinterable perovskite powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6265907A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63319214A (en) * | 1987-06-23 | 1988-12-27 | Ube Ind Ltd | Powder for capacitor materials |
| JP5541670B2 (en) * | 2009-11-18 | 2014-07-09 | 日本電信電話株式会社 | Lithium air secondary battery and method for producing lithium air secondary battery |
-
1985
- 1985-09-17 JP JP60203359A patent/JPS6265907A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6265907A (en) | 1987-03-25 |
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