JPH07291607A - Production of ceramic powder - Google Patents
Production of ceramic powderInfo
- Publication number
- JPH07291607A JPH07291607A JP8335394A JP8335394A JPH07291607A JP H07291607 A JPH07291607 A JP H07291607A JP 8335394 A JP8335394 A JP 8335394A JP 8335394 A JP8335394 A JP 8335394A JP H07291607 A JPH07291607 A JP H07291607A
- Authority
- JP
- Japan
- Prior art keywords
- group element
- tetravalent titanium
- alkaline earth
- titanium group
- ceramic powder
- 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
Links
- 239000000843 powder Substances 0.000 title claims abstract description 34
- 239000000919 ceramic Substances 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims description 25
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical group [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000010936 titanium Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims abstract description 20
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims abstract description 19
- 150000001342 alkaline earth metals Chemical class 0.000 claims abstract description 17
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims abstract description 6
- 238000000227 grinding Methods 0.000 claims abstract description 4
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 4
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 3
- 229910052735 hafnium Inorganic materials 0.000 claims abstract description 3
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 3
- 229910052718 tin Inorganic materials 0.000 claims abstract description 3
- 229910052788 barium Inorganic materials 0.000 claims abstract 2
- 229910052712 strontium Inorganic materials 0.000 claims abstract 2
- 238000006243 chemical reaction Methods 0.000 claims description 30
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 8
- -1 amine compound Chemical class 0.000 claims description 8
- 239000003518 caustics Substances 0.000 claims description 8
- 150000002484 inorganic compounds Chemical class 0.000 claims description 6
- 229910010272 inorganic material Inorganic materials 0.000 claims description 6
- 239000003513 alkali Substances 0.000 claims description 5
- 230000003301 hydrolyzing effect Effects 0.000 claims description 4
- 150000002902 organometallic compounds Chemical class 0.000 claims description 4
- 239000002270 dispersing agent Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 abstract description 6
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 abstract description 3
- 229910052726 zirconium Inorganic materials 0.000 abstract description 3
- 150000001875 compounds Chemical class 0.000 description 41
- 239000002131 composite material Substances 0.000 description 34
- 150000004703 alkoxides Chemical class 0.000 description 15
- 238000000034 method Methods 0.000 description 9
- 239000002243 precursor Substances 0.000 description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 229910001420 alkaline earth metal ion Inorganic materials 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 description 4
- 238000001027 hydrothermal synthesis Methods 0.000 description 4
- 238000010008 shearing Methods 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 238000002441 X-ray diffraction Methods 0.000 description 3
- 238000001354 calcination Methods 0.000 description 3
- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- QUSNBJAOOMFDIB-UHFFFAOYSA-N Ethylamine Chemical compound CCN QUSNBJAOOMFDIB-UHFFFAOYSA-N 0.000 description 2
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 2
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 239000011812 mixed powder Substances 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- RZXMPPFPUUCRFN-UHFFFAOYSA-N p-toluidine Chemical compound CC1=CC=C(N)C=C1 RZXMPPFPUUCRFN-UHFFFAOYSA-N 0.000 description 2
- 239000011164 primary particle Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229910015802 BaSr Inorganic materials 0.000 description 1
- BSBZZDSXEKBNSQ-UHFFFAOYSA-N CCCCO[Ti](OCCCC)OCCNCCO Chemical compound CCCCO[Ti](OCCCC)OCCNCCO BSBZZDSXEKBNSQ-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- AFBPFSWMIHJQDM-UHFFFAOYSA-N N-methyl-N-phenylamine Natural products CNC1=CC=CC=C1 AFBPFSWMIHJQDM-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 229910008651 TiZr Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 150000004982 aromatic amines Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- RCJVRSBWZCNNQT-UHFFFAOYSA-N dichloridooxygen Chemical compound ClOCl RCJVRSBWZCNNQT-UHFFFAOYSA-N 0.000 description 1
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- XXBDWLFCJWSEKW-UHFFFAOYSA-N dimethylbenzylamine Chemical compound CN(C)CC1=CC=CC=C1 XXBDWLFCJWSEKW-UHFFFAOYSA-N 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000003891 oxalate salts Chemical class 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000011163 secondary particle Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- JMXKSZRRTHPKDL-UHFFFAOYSA-N titanium ethoxide Chemical compound [Ti+4].CC[O-].CC[O-].CC[O-].CC[O-] JMXKSZRRTHPKDL-UHFFFAOYSA-N 0.000 description 1
- 231100000701 toxic element Toxicity 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、ABO3 型のペロブス
カイト構造のセラミックス粉体の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing ABO 3 type ceramic powder having a perovskite structure.
【0002】[0002]
【従来の技術】従来のABO3 型構造を有する複合ペロ
ブスカイト化合物粉体の製造方法としては、次のような
種々の方法が提案されている。2. Description of the Related Art The following various methods have been proposed as conventional methods for producing composite perovskite compound powder having an ABO 3 type structure.
【0003】(a)複合ペロブスカイト化合物を構成す
る元素の炭酸塩あるいは酸化物粉体を混合した後、この
混合粉体を1000℃以上の温度で仮焼して目的の複合
ペロブスカイト化合物を得る方法。(A) A method of obtaining a target composite perovskite compound by mixing carbonate or oxide powders of the elements constituting the composite perovskite compound and then calcining the mixed powder at a temperature of 1000 ° C. or higher.
【0004】(b)蓚酸塩と複合ペロブスカイト化合物
を構成する元素の金属イオンを反応させて複合分子化合
物前駆体を生成した後、この複合分子化合物前駆体を仮
焼して目的の複合ペロブスカイト化合物を得る方法。(B) Oxalates are reacted with metal ions of the elements constituting the composite perovskite compound to form a composite molecular compound precursor, and then the composite molecular compound precursor is calcined to obtain the target composite perovskite compound. How to get.
【0005】(c)カテコールと複合ペロブスカイト化
合物を構成する元素の金属イオンを反応させて複合分子
化合物前駆体を生成した後、この複合分子化合物前駆体
を仮焼して目的の複合ペロブスカイト化合物を得る方
法。(C) After catechol and metal ions of the elements constituting the complex perovskite compound are reacted to form a complex molecular compound precursor, the complex molecular compound precursor is calcined to obtain the target complex perovskite compound. Method.
【0006】(d)複合ペロブスカイト化合物を構成す
る元素のアルコキシドを用いたゾル−ゲル反応による複
合ペロブスカイト化合物を得る方法。(D) A method for obtaining a composite perovskite compound by a sol-gel reaction using an alkoxide of an element constituting the composite perovskite compound.
【0007】(e)複合ペロブスカイト化合物を構成す
るアルカリ土類金属の水酸化物と4価のチタン族元素の
水酸化物あるいは酸化物ゾルを、高温・高圧・密閉下で
水熱反応させて目的の複合ペロブスカイト化合物を得る
方法。例えば、4価のチタン族元素がTiの場合の反応
は次式のようになる。(E) The purpose is to subject a hydroxide of an alkaline earth metal and a hydroxide or oxide sol of a tetravalent titanium group element constituting a composite perovskite compound to a hydrothermal reaction under high temperature, high pressure and sealing conditions. To obtain the composite perovskite compound of. For example, the reaction when the tetravalent titanium group element is Ti is as follows.
【0008】Me+2 + Ti(OH)6 -2 → Me
TiO3 + 3H2 O (但し、Me+2:アルカリ土類金属イオン) なお、本製造方法においては、4価のチタン族元素の水
酸化物あるいは酸化物ゾルのモル量に比べて過剰のモル
量のアルカリ土類金属の水酸化物を添加してTi(O
H)6 -2錯体を形成させて、このTi(OH)6 -2錯体
とアルカリ土類金属イオンとを反応させて反応収率を上
げている。そして反応終了後、余剰のアルカリ土類金属
イオンを純水で洗浄して除去する。Me +2 + Ti (OH) 6 -2 → Me
TiO 3 + 3H 2 O (provided that Me +2 is an alkaline earth metal ion) In the present production method, the molar amount of the tetravalent titanium group element hydroxide or oxide sol is larger than that of the tetravalent titanium group element hydroxide or oxide sol. Add an amount of alkaline earth metal hydroxide to make Ti (O
H) 6 -2 complex is formed and the Ti (OH) 6 -2 complex is reacted with an alkaline earth metal ion to increase the reaction yield. After the reaction is completed, excess alkaline earth metal ions are washed with pure water and removed.
【0009】[0009]
【発明が解決しようとする課題】しかしながら、上記製
造方法それぞれにおいて、以下に示すような問題点を有
していた。However, each of the above manufacturing methods has the following problems.
【0010】(a)の製造方法においては、複合ペロブ
スカイト化合物を構成する元素の酸化物あるいは炭酸塩
の粉体を混合するため、分子レベルで均一に分散させる
ことが不可能であった。また、混合粉体を1000℃以
上の高温で仮焼を行なって得た凝集体を剪断力の大きな
粉砕装置を用いて粉砕処理する必要があり、このときに
粉砕装置の内壁あるいはメディアの磨耗物が不純物とし
て複合ペロブスカイト化合物に混入した。In the production method of (a), since powders of oxides or carbonates of elements constituting the composite perovskite compound are mixed, it is impossible to disperse them uniformly at the molecular level. In addition, it is necessary to pulverize the agglomerates obtained by calcining the mixed powder at a high temperature of 1000 ° C. or higher using a pulverizer having a large shearing force. Was mixed as an impurity in the complex perovskite compound.
【0011】(b)の製造方法においては、蓚酸塩との
反応により得られた複合分子化合物前駆体を高温で仮焼
を行なった後の凝集体を、(a)と同様に、剪断力の大
きな粉砕装置を用いて粉砕処理する必要があり、このと
きに粉砕装置の内壁あるいはメディアの磨耗物が不純物
として複合ペロブスカイト化合物に混入した。また、複
合ペロブスカイトのAサイトを構成する元素間で、蓚酸
塩を形成する最適pHが互いに異なる場合があり、この
ようなときには目的の構成比率と異なる複合分子化合物
前駆体が形成されることがあった。さらに、得られた複
合分子化合物前駆体の水への溶解を抑えるため、大量の
エチルアルコール等の有機溶剤を添加する必要があり、
これにより濾過廃液中のBODが高くなった。In the production method of (b), the aggregate after the composite molecular compound precursor obtained by the reaction with the oxalate is calcined at high temperature is treated with shearing force in the same manner as in (a). It was necessary to carry out the pulverization process using a large pulverizer, and at this time, the abrasion material of the inner wall of the pulverizer or the media was mixed into the complex perovskite compound as an impurity. In addition, the optimum pH for forming oxalate may differ between the elements forming the A site of the composite perovskite, and in such a case, a composite molecular compound precursor having a different composition ratio than the target may be formed. It was Furthermore, in order to suppress dissolution of the obtained composite molecular compound precursor in water, it is necessary to add a large amount of an organic solvent such as ethyl alcohol.
This increased the BOD in the filtered waste liquid.
【0012】(c)の製造方法においても、カテコール
との反応により得られた複合分子化合物前駆体を高温で
仮焼を行なった後の凝集体を、(a)と同様に、剪断力
の大きな粉砕装置を用いて粉砕処理する必要があり、こ
のときに粉砕装置の内壁あるいはメディアの磨耗物が不
純物として複合ペロブスカイト化合物に混入した。Also in the production method of (c), the aggregate after the composite molecular compound precursor obtained by the reaction with catechol is calcined at high temperature has a large shearing force as in (a). It is necessary to perform a pulverization process using a pulverizer, and at this time, the abrasion material of the inner wall of the pulverizer or the media is mixed as an impurity in the complex perovskite compound.
【0013】(d)の製造方法においては、Tiのアル
コキシド例えばTi(OC3 H7 )4 は比較的安価であ
るが、複合ペロブスカイト化合物を構成する他の元素の
アルコキシドは非常に高価であって量産使用には適さな
かった。また、アルカリ土類金属イオンのアルコキシド
は一般的な有機溶剤に対して溶解度が小さく、複合ペロ
ブスカイト化合物を高濃度化して生産効率を上げること
が不可能であった。また、雰囲気コントロール可能な特
別な反応装置を必要とし、反応装置自体が高価なものと
なった。In the method (d), the alkoxide of Ti, such as Ti (OC 3 H 7 ) 4, is relatively inexpensive, but the alkoxides of other elements constituting the composite perovskite compound are very expensive. It was not suitable for mass production. Further, the alkoxide of an alkaline earth metal ion has a small solubility in a general organic solvent, and it has been impossible to increase the concentration of the complex perovskite compound and improve the production efficiency. Further, a special reaction device capable of controlling the atmosphere is required, and the reaction device itself becomes expensive.
【0014】(e)の製造方法においては、高圧に十分
耐える反応装置が必要なため設備費が高価となった。In the production method of (e), the equipment cost is high because a reactor which can withstand high pressure is required.
【0015】また、反応終了後に余剰のアルカリ土類金
属イオンを洗浄除去するとき、この余剰のアルカリ土類
金属イオンの一部が空気中の炭酸ガスと反応して難溶性
の炭酸塩となり、反応で得た複合ペロブスカイト化合物
粉体中に残る。このため、この炭酸塩を除去するために
弱い酸で処理すると、アルカリ土類金属の炭酸塩と共に
複合ペロブスカイト化合物粉体の一部も溶解して、目的
のモル比よりずれた複合ペロブスカイト化合物粉体とな
った。When the excess alkaline earth metal ions are removed by washing after completion of the reaction, a part of the excess alkaline earth metal ions reacts with carbon dioxide gas in the air to form a sparingly soluble carbonate, resulting in a reaction. It remains in the composite perovskite compound powder obtained in. Therefore, if a weak acid is used to remove the carbonate, a part of the complex perovskite compound powder is dissolved together with the alkaline earth metal carbonate, and the complex perovskite compound powder deviated from the target molar ratio. Became.
【0016】そこで、本発明の目的は、上記問題点を解
決して、粒径が小さく比表面積が大きくて易焼結性であ
って、均一に分散して組成ずれがない複合ペロブスカイ
ト構造を有するセラミックス粉体の製造方法を提供する
ことにある。Therefore, an object of the present invention is to solve the above problems and to have a composite perovskite structure which has a small particle size, a large specific surface area, is easily sinterable, and is uniformly dispersed and has no composition deviation. It is to provide a method for producing ceramic powder.
【0017】[0017]
【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ス粉体の製造方法は、一般式A
BO3 型(但し、Aはアルカリ土類金属元素でBa,S
r,Mg,Caのうちの少なくとも1種類以上、Bは4
価のチタン族元素でTi,Zr,Sn,Hfのうちの少
なくとも1種類以上)のペロブスカイト構造のセラミッ
クス粉体の製造において、アルカリ土類金属の水酸化物
の溶液と、該アルカリ土類金属と等モル量の4価のチタ
ン族元素の水酸化物あるいは酸化物ゾルのうちの少なく
とも1種類とを、容器内で粉砕メディアを攪拌させなが
ら加熱して反応させることを特徴とする。In order to achieve the above object, the method for producing a ceramic powder according to the present invention comprises a general formula A
BO 3 type (where A is an alkaline earth metal element, Ba, S
At least one of r, Mg, and Ca, and B is 4
In producing a ceramic powder having a perovskite structure of at least one of Ti, Zr, Sn, and Hf which is a valent titanium group element, a solution of an alkaline earth metal hydroxide and the alkaline earth metal It is characterized in that an equimolar amount of at least one kind of hydroxide or oxide sol of tetravalent titanium group element is reacted by heating while stirring the grinding media in the container.
【0018】また、4価のチタン族元素の水酸化物は、
該4価のチタン族元素の水溶性の無機化合物を苛性アル
カリと反応させたもの、4価のチタン族元素の酸化物ゾ
ルは、該4価のチタン族元素の水溶性の無機化合物を加
水分解させたものおよび該4価のチタン族元素の有機金
属化合物を加水分解させたもののうち少なくとも1種
類、であることを特徴とする。Further, the hydroxide of the tetravalent titanium group element is
The water-soluble inorganic compound of the tetravalent titanium group element is reacted with caustic, and the oxide sol of the tetravalent titanium group element is obtained by hydrolyzing the water-soluble inorganic compound of the tetravalent titanium group element. And at least one of hydrolyzed organometallic compounds of the tetravalent titanium group element.
【0019】さらに、密閉容器内で60〜95℃の温度
に加熱して反応させることを特徴とする。Further, it is characterized in that the reaction is carried out by heating to a temperature of 60 to 95 ° C. in a closed container.
【0020】また、苛性アルカリあるいは有機アミン化
合物のうちの少なくとも1種類を、4価のチタン族元素
1モルに対して1〜4モル添加して反応させることを特
徴とする。Further, it is characterized in that at least one kind of caustic alkali or an organic amine compound is added in an amount of 1 to 4 mol per 1 mol of a tetravalent titanium group element and reacted.
【0021】そして、反応終了後、炭酸イオンおよび分
散剤を添加することを特徴とする。After the reaction, the carbonate ion and the dispersant are added.
【0022】[0022]
【作用】本発明においては、等モル量のアルカリ土類金
属の水酸化物と4価のチタン族元素の水酸化物あるいは
酸化物ゾルのうちの少なくとも1種類とを反応させる。
したがって、従来の水熱反応の場合のように、余剰のア
ルカリ土類金属元素を洗浄により除去してモル比の調整
を行なう必要性がない。In the present invention, an equimolar amount of a hydroxide of an alkaline earth metal is reacted with at least one of a hydroxide of a tetravalent titanium group element or an oxide sol.
Therefore, unlike the case of the conventional hydrothermal reaction, it is not necessary to remove the excess alkaline earth metal element by washing to adjust the molar ratio.
【0023】また、本発明では、粉砕メディアを攪拌さ
せながら反応させる。したがって、メディア同志の衝突
により衝突面に発生する剪断エネルギーによるメカノケ
ミカル作用で反応効率がアップする。さらに、本発明の
方法で生成する複合ペロブスカイト化合物粉体は結晶性
の酸化物であるので、非晶質の水酸化物ほど凝集性は強
くないものの同様に凝集する傾向を示すが、粉砕メディ
アの攪拌および分散剤の添加によりこの凝集を防ぐこと
ができる。Further, in the present invention, the pulverized media are reacted while being stirred. Therefore, the reaction efficiency is increased by the mechanochemical action due to the shearing energy generated on the collision surface by the collision of the media. Furthermore, since the composite perovskite compound powder produced by the method of the present invention is a crystalline oxide, it shows a tendency to agglomerate as well although it is not as cohesive as amorphous hydroxide, but it is This agglomeration can be prevented by stirring and adding a dispersant.
【0024】さらに、60〜95℃の温度で反応させる
ため、反応容器内の圧力は1atm以上になることはな
い。したがって、水熱反応を利用する製造方法の場合の
ように高耐圧の反応容器を必要とせず、反応装置が安価
となる。Further, since the reaction is carried out at a temperature of 60 to 95 ° C., the pressure in the reaction vessel never exceeds 1 atm. Therefore, unlike the case of the manufacturing method utilizing the hydrothermal reaction, a high-pressure resistant reaction container is not required, and the reactor becomes inexpensive.
【0025】また、密閉状態で空気中の炭酸ガスとの接
触を絶って反応させることにより、アルカリ土類金属元
素の不溶性炭酸塩の生成を防ぐことができる。Further, the formation of insoluble carbonate of an alkaline earth metal element can be prevented by causing the reaction with the carbon dioxide gas in the air in a closed state without contact.
【0026】また、本発明においては、アルカリ土類金
属元素の水酸化物の代わりに、苛性アルカリあるいは有
機アミン化合物を添加して、Ti(OH)6 -2錯体を形
成させる。したがって、反応終了後に有毒元素のBa+2
を回収して処理する必要がない。また、添加する苛性ア
ルカリや有機アミン化合物は安価なため、複合ペロブス
カイト化合物粉体の製造コストの低減化が図れる。In the present invention, instead of the hydroxide of the alkaline earth metal element, a caustic alkali or an organic amine compound is added to form a Ti (OH) 6 -2 complex. Therefore, after the reaction is completed, the toxic element Ba +2
Need not be collected and processed. Moreover, since the caustic alkali and the organic amine compound to be added are inexpensive, the production cost of the composite perovskite compound powder can be reduced.
【0027】さらに、本発明の方法で生成する複合ペロ
ブスカイト化合物の粉体は微細なため、幾分かは溶解し
てアルカリ土類金属元素イオンが溶出する。この溶出し
たアルカリ土類金属元素イオンに炭酸イオンを反応させ
て不溶性のアルカリ土類金属炭酸塩を生成させること
で、得られた複合ペロブスカイト化合物のモル比のずれ
を防止することができる。Further, since the powder of the complex perovskite compound produced by the method of the present invention is fine, some of it is dissolved and the alkaline earth metal element ions are eluted. By reacting the eluted alkaline earth metal element ions with carbonate ions to generate an insoluble alkaline earth metal carbonate salt, it is possible to prevent the deviation of the molar ratio of the obtained composite perovskite compound.
【0028】[0028]
【実施例】以下、本発明のセラミックス粉体の製造方法
について、その実施例を説明する。EXAMPLES Examples of the method for producing ceramic powder of the present invention will be described below.
【0029】まず、TiのアルコキシドであるTi(O
C3 H7 )4 の1.0モルをイソプロピルアルコール
(以下、IPAと称す)溶液中に溶解してアルコキシド
の1.0モル/L希釈溶液を調整した。次に、Ti量が
0.1モルになるようにこのアルコキシド希釈溶液を分
取してビーカーに移した。その後、分取したアルコキシ
ド希釈溶液にIPAを加えて約200ccとし、ホット
プレート上で45〜55℃に加温しながら10%の純水
を含むIPA溶液180ccをゆっくりと添加して加水
分解させた。加水分解後、アンモニア水を加えてpHを
9に調整してTiの酸化物ゾルを作製した。First, Ti (O) which is an alkoxide of Ti
1.0 mol of C 3 H 7 ) 4 was dissolved in an isopropyl alcohol (hereinafter referred to as IPA) solution to prepare a 1.0 mol / L diluted solution of alkoxide. Next, this diluted alkoxide solution was dispensed so that the amount of Ti would be 0.1 mol and transferred to a beaker. After that, IPA was added to the collected alkoxide diluted solution to make it about 200 cc, and 180 cc of IPA solution containing 10% pure water was slowly added to hydrolyze while heating to 45 to 55 ° C. on a hot plate. . After hydrolysis, the pH was adjusted to 9 by adding aqueous ammonia to prepare a Ti oxide sol.
【0030】同様に、ZrのアルコキシドであるZr
(OC4 H9 )4 を出発原料として、Zrの酸化物ゾル
を作製した。Similarly, Zr which is an alkoxide of Zr
Using (OC 4 H 9 ) 4 as a starting material, a Zr oxide sol was prepared.
【0031】また、TiおよびZrが各0.05モル量
になるようにそれぞれのアルコキド希釈溶液を分取して
ビーカーに移した。その後、分取したアルコキシド希釈
溶液にIPAを加えて約200ccとし、ホットプレー
ト上で45〜55℃に加温しながら10%の純粋を含む
IPA溶液180ccをゆっくりと添加して加水分解さ
せた。加水分解後、アンモニア水を加えてpHを9に調
節してTi・Zrの複合酸化物ゾルを作製した。Further, each alkoxide diluted solution was dispensed so that Ti and Zr were each 0.05 mol and transferred to a beaker. Then, IPA was added to the separated alkoxide diluted solution to make it about 200 cc, and 180 cc of IPA solution containing 10% of pure was slowly added thereto while heating at 45 to 55 ° C. on a hot plate for hydrolysis. After the hydrolysis, ammonia water was added to adjust the pH to 9 to prepare a Ti / Zr composite oxide sol.
【0032】次に、表1に示す組成比率となるように、
上記4価のチタン族元素の酸化物ゾル、アルカリ土類金
属元素の水酸化物、NaOHと純水500cc、直径2
mmのPSZ玉石500ccをウレタンを内貼した内容
積2000ccの反応容器に投入した。その後、PSZ
を高速攪拌するためのインペラ付き密閉蓋を反応容器に
セットし、この反応容器をオイルバス内に固定してPS
Zを高速攪拌しながら85℃で3時間反応させた。Next, so that the composition ratio shown in Table 1 is obtained,
Oxide sol of tetravalent titanium group element, hydroxide of alkaline earth metal element, NaOH and pure water 500 cc, diameter 2
500 cc of PSZ boulders of mm was put into a reaction container having an inner volume of 2000 cc with urethane stuck inside. Then PSZ
Set a sealed lid with an impeller for high-speed stirring in the reaction vessel, fix the reaction vessel in an oil bath, and
Z was reacted at 85 ° C. for 3 hours while stirring at high speed.
【0033】反応終了後、生成した複合ペロブスカイト
化合物に対してNa2 CO3 を2モル%、EDTAを
0.01wt%添加して30分間低速で攪拌した。その
後、反応容器をオイルバスより取り出し室温まで冷却し
た後、反応生成物を回収し純粋で洗浄してNa+ を除去
して複合ペロブスカイト化合物粉体を得た。After completion of the reaction, 2 mol% of Na 2 CO 3 and 0.01 wt% of EDTA were added to the produced composite perovskite compound, and the mixture was stirred at a low speed for 30 minutes. Then, the reaction container was taken out from the oil bath and cooled to room temperature, and then the reaction product was collected and washed with pure water to remove Na + to obtain a composite perovskite compound powder.
【0034】[0034]
【表1】 [Table 1]
【0035】次に、得られた複合ペロブスカイト化合物
のX線回折(XRD)分析、比表面積(SS)測定、モ
ル比の化学分析を行なった。その結果を表2に示す。ま
た、試料No.2の複合ペロブスカイト化合物を透過分
析電子顕微鏡を用いて3μmスポット径で10箇所ラン
ダムにモル比分析を行なった。その結果を表3に示す。Next, the obtained composite perovskite compound was subjected to X-ray diffraction (XRD) analysis, specific surface area (SS) measurement, and chemical analysis of molar ratio. The results are shown in Table 2. In addition, the sample No. Using the transmission analysis electron microscope, the composite perovskite compound of No. 2 was subjected to random molar ratio analysis at 10 spots with a spot diameter of 3 μm. The results are shown in Table 3.
【0036】[0036]
【表2】 [Table 2]
【0037】[0037]
【表3】 [Table 3]
【0038】表2に示す通り、XRD分析の結果、本発
明の製造方法で得た試料No.1〜3の複合ペロブスカ
イトは、それぞれBaTiO3 、(BaSr)TiO3
およびBa(TiZr)O3 の立方晶の単相になってい
る。またSS測定の結果、試料No.1〜3の粉体は約
40m2 /gと、従来の炭酸塩あるいは酸化物粉体の仮
焼、粉砕により得られた粉体の10倍以上の比表面積を
有し、本発明の方法で得られる複合ペロブスカイト化合
物は非常に微細な粉体であることを示している。なお、
SSの値から換算した粒径は3nmであり、XRDの回
折幅から計算した結晶粒径の4nmとほぼ一致してお
り、一次粒子イコール結晶粒子になっている。また、電
子顕微鏡観察の結果によると、数nmの一次粒子が集ま
って0.1〜0.3μmの二次粒子となっていることが
判明している。さらに、試料No.1〜3の複合ペロブ
スカイト化合物粉体のモル比を化学分析したところ、分
析誤差範囲内で仕込み量通りの化合物が得られている。As shown in Table 2, as a result of the XRD analysis, the sample No. obtained by the manufacturing method of the present invention was tested. The composite perovskites 1 to 3 are BaTiO 3 and (BaSr) TiO 3 respectively.
And a cubic single phase of Ba (TiZr) O 3 . As a result of the SS measurement, the sample No. The powders 1 to 3 have a specific surface area of about 40 m 2 / g, which is 10 times or more that of the powder obtained by calcination and pulverization of the conventional carbonate or oxide powder. The obtained composite perovskite compound is shown to be a very fine powder. In addition,
The particle size converted from the value of SS is 3 nm, which is almost the same as the crystal particle size of 4 nm calculated from the diffraction width of XRD, and the particles are primary particle equal crystal particles. Moreover, according to the result of electron microscope observation, it has been found that primary particles of several nm are aggregated to form secondary particles of 0.1 to 0.3 μm. Further, the sample No. A chemical analysis of the molar ratios of the composite perovskite compound powders 1 to 3 showed that the compounds as charged were obtained within the analytical error range.
【0039】また、表3に示す通り、試料No.2の複
合ペロブスカイト化合物粉体を透過分析電子顕微鏡によ
り3μmのスポット径で10箇所ランダムに分析した結
果も、仕込み量に近いモル比になっている。Further, as shown in Table 3, the sample No. The result of randomly analyzing the composite perovskite compound powder of No. 2 with a transmission analysis electron microscope at 10 spots with a spot diameter of 3 μm also shows a molar ratio close to the charged amount.
【0040】以上の結果より、本発明のセラミックス粉
体の製造方法により、仕込み通りの組成比で均一に分散
し、かつ比表面積が大きくて表面活性の高い複合ペロブ
スカイト粉体が得られている。From the above results, according to the method for producing a ceramic powder of the present invention, a composite perovskite powder which is uniformly dispersed at the composition ratio as charged and has a large specific surface area and high surface activity is obtained.
【0041】なお、上記実施例においては、4価のチタ
ン族元素の有機金属化合物であるTi(OC3 H7 )4
あるいはZr(OC4 H9 )4 を加水分解して得られた
酸化物ゾルをアルカリ土類金属の水酸化物と反応させて
いるが、本発明はこれのみに限定されるものではない。
即ち、4価のチタン族元素の水溶性の無機化合物を苛性
アルカリと反応させて得た水酸化物または加水分解させ
た酸化物ゾル、または4価のチタン族元素のアルコキシ
ド等の有機金属化合物を加水分解させた酸化物ゾルのう
ちの少なくとも1種類を適宜アルカリ土類金属の水酸化
物と反応させることができる。In the above embodiment, Ti (OC 3 H 7 ) 4 which is an organometallic compound of tetravalent titanium group element is used.
Alternatively, an oxide sol obtained by hydrolyzing Zr (OC 4 H 9 ) 4 is reacted with a hydroxide of an alkaline earth metal, but the present invention is not limited to this.
That is, a hydroxide obtained by reacting a water-soluble inorganic compound of a tetravalent titanium group element with caustic or a hydrolyzed oxide sol, or an organometallic compound such as an alkoxide of a tetravalent titanium group element is used. At least one of the hydrolyzed oxide sols can be appropriately reacted with a hydroxide of an alkaline earth metal.
【0042】そして、4価のチタン族元素の水溶性の無
機化合物としては、塩化物、オキシ塩化物、硝酸塩、硫
酸塩等を用いることができる。また、4価のチタン族の
有機金属化合物としては、チタンイソプロポキシド、チ
タンブトキシド、チタンエトキシド、ジブトキシ−ジト
リエタノールアミナトチタン、ジブトキシ(2−ヒドロ
キシエチルアミノエトキシ)チタン等のアルコキシドや
その他のTi有機化合物を用いることができる。また、
Ti以外の他の4価のチタン族元素についてもTiアル
コキシド等のTi有機化合物の場合と同様である。As the water-soluble inorganic compound of tetravalent titanium group element, chloride, oxychloride, nitrate, sulfate and the like can be used. Examples of the tetravalent titanium group organometallic compound include alkoxides such as titanium isopropoxide, titanium butoxide, titanium ethoxide, dibutoxy-ditriethanolaminatotitanium, and dibutoxy (2-hydroxyethylaminoethoxy) titanium, and other alkoxides. Ti organic compounds can be used. Also,
The same applies to other tetravalent titanium group elements other than Ti as in the case of Ti organic compounds such as Ti alkoxide.
【0043】また、上記実施例においては、NaOHを
添加してTi(OH)6 -2錯体を形成させているが、本
発明はこれのみに限定されるものではない。即ち、Na
OH以外にKOH,LiOH等の苛性アルカリやNH4
OH、あるいはメチルアミン、ジメチルアミン、トリメ
チルアミン、エチルアミン等の脂肪族アミン、o−,m
−,p−トルイジン、N,N−ジメチルベンジルアミン
等の芳香族アミンを適宜用いることができる。Further, in the above embodiment, NaOH is added to form the Ti (OH) 6 -2 complex, but the present invention is not limited to this. That is, Na
In addition to OH, caustic alkali such as KOH and LiOH and NH 4
OH or aliphatic amine such as methylamine, dimethylamine, trimethylamine, ethylamine, o-, m
Aromatic amines such as-, p-toluidine and N, N-dimethylbenzylamine can be used as appropriate.
【0044】また、上記実施例においては、反応終了後
Na2 CO3 を添加して微量ながらも溶解する複合ペロ
ブスカイト化合物を沈殿させているが、本発明はこれの
みに限定されるものではない。即ち、Na2 CO3 以外
に、K2 CO3 ,Li2 CO3 ,(NH4 )2 CO3 等
の炭酸塩を適宜用いることができる。Further, in the above-mentioned Examples, Na 2 CO 3 was added after completion of the reaction to precipitate the complex perovskite compound which was dissolved in a small amount, but the present invention is not limited to this. That is, in addition to Na 2 CO 3 , carbonates such as K 2 CO 3 , Li 2 CO 3 and (NH 4 ) 2 CO 3 can be used as appropriate.
【0045】[0045]
【発明の効果】以上の説明で明らかなように、本発明の
セラミックス粉体の製造方法は、等モル量のアルカリ土
類金属の水酸化物と4価のチタン族元素の水酸化物ある
いは酸化物ゾルのうちの少なくとも1種類とを粉砕メデ
ィアを攪拌しながら反応させて、反応と同時に生成物を
粉砕するものである。したがって、粒径が小さく比表面
積が大きくて易焼結性であって、均一に分散して組成ず
れがない複合ペロブスカイト構造を有するセラミックス
粉体を得ることができる。As is apparent from the above description, the method for producing a ceramic powder according to the present invention employs an equimolar amount of a hydroxide of an alkaline earth metal and a hydroxide or oxide of a tetravalent titanium group element. At least one of the product sol is reacted with the grinding media while stirring, and the product is ground simultaneously with the reaction. Therefore, it is possible to obtain a ceramic powder having a composite perovskite structure which has a small particle size, a large specific surface area, is easily sinterable, and is uniformly dispersed without compositional deviation.
【0046】また、密閉容器内で60〜95℃の温度で
反応させるため、反応容器内の圧力は1atm以上にな
ることはなく、水熱反応を利用する製造方法の場合のよ
うに高耐圧の反応容器を必要とせず、反応装置が安価と
なる。Further, since the reaction is carried out in the closed container at a temperature of 60 to 95 ° C., the pressure in the reaction container does not become 1 atm or more, and the high withstand pressure as in the case of the manufacturing method utilizing the hydrothermal reaction is obtained. The reactor is inexpensive because it does not require a reaction vessel.
Claims (5)
土類金属元素でBa,Sr,Mg,Caのうちの少なく
とも1種類以上、Bは4価のチタン族元素でTi,Z
r,Sn,Hfのうちの少なくとも1種類以上)のペロ
ブスカイト構造のセラミックス粉体の製造において、 アルカリ土類金属の水酸化物の溶液と、該アルカリ土類
金属と等モル量の4価のチタン族元素の水酸化物あるい
は酸化物ゾルのうちの少なくとも1種類とを、容器内で
粉砕メディアを攪拌させながら加熱して反応させること
を特徴とするセラミックス粉体の製造方法。1. The general formula ABO 3 type (wherein A is an alkaline earth metal element and at least one or more of Ba, Sr, Mg, and Ca is used, and B is a tetravalent titanium group element, Ti or Z.
At least one of r, Sn, and Hf) in the production of ceramic powder having a perovskite structure, a solution of a hydroxide of an alkaline earth metal, and tetravalent titanium in an equimolar amount with the alkaline earth metal. A method for producing a ceramic powder, which comprises reacting at least one of a hydroxide of a group element or an oxide sol with stirring while heating a grinding medium in a container.
価のチタン族元素の水溶性の無機化合物を苛性アルカリ
と反応させたもの、4価のチタン族元素の酸化物ゾル
は、該4価のチタン族元素の水溶性の無機化合物を加水
分解させたものおよび該4価のチタン族元素の有機金属
化合物を加水分解させたもののうち少なくとも1種類、
であることを特徴とする請求項1記載のセラミックス粉
体の製造方法。2. The hydroxide of a tetravalent titanium group element is
A water-soluble inorganic compound of a tetravalent titanium group element is reacted with caustic, and an oxide sol of a tetravalent titanium group element is obtained by hydrolyzing the water-soluble inorganic compound of a tetravalent titanium group element. And at least one of those obtained by hydrolyzing the organometallic compound of the tetravalent titanium group element,
The method for producing a ceramic powder according to claim 1, wherein
して反応させることを特徴とする請求項1記載のセラミ
ックス粉体の製造方法。3. The method for producing a ceramic powder according to claim 1, wherein the reaction is carried out by heating to a temperature of 60 to 95 ° C. in a closed container.
のうちの少なくとも1種類を、4価のチタン族元素1モ
ルに対して1〜4モル添加して反応させることを特徴と
する請求項1記載のセラミックス粉体の製造方法。4. The ceramic according to claim 1, wherein 1 to 4 mol of at least one of caustic alkali and an organic amine compound is added to 1 mol of a tetravalent titanium group element and reacted. Powder manufacturing method.
添加することを特徴とする請求項1記載のセラミックス
粉体の製造方法。5. The method for producing a ceramic powder according to claim 1, wherein carbonate ions and a dispersant are added after the reaction is completed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8335394A JPH07291607A (en) | 1994-04-21 | 1994-04-21 | Production of ceramic powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8335394A JPH07291607A (en) | 1994-04-21 | 1994-04-21 | Production of ceramic powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH07291607A true JPH07291607A (en) | 1995-11-07 |
Family
ID=13800081
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8335394A Pending JPH07291607A (en) | 1994-04-21 | 1994-04-21 | Production of ceramic powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07291607A (en) |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000035811A1 (en) * | 1998-12-11 | 2000-06-22 | Showa Denko K.K. | Perovskite type composite oxide containing titanium |
| WO2003004416A1 (en) * | 2001-07-04 | 2003-01-16 | Showa Denko K. K. | Barium titanate and its production method |
| WO2004054931A1 (en) * | 2002-12-18 | 2004-07-01 | Showa Denko K. K. | Barium titanate and electronic parts using the material |
| WO2005005042A1 (en) * | 2003-04-29 | 2005-01-20 | Hrd Corp. | Perovskite-based catalyst, its preparation and its use for conversion of methane to ethylene |
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| JP2005306728A (en) * | 2004-03-25 | 2005-11-04 | Showa Denko Kk | Titanium-containing perovskite-type compound and manufacturing method therefor |
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-
1994
- 1994-04-21 JP JP8335394A patent/JPH07291607A/en active Pending
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| US7091154B2 (en) | 1999-05-26 | 2006-08-15 | Showa Denko Kabushiki Kaisha | Perovskite titanium-type composite oxide particle and production process thereof |
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| JP2005306728A (en) * | 2004-03-25 | 2005-11-04 | Showa Denko Kk | Titanium-containing perovskite-type compound and manufacturing method therefor |
| JP2006298677A (en) * | 2005-04-18 | 2006-11-02 | National Institute Of Advanced Industrial & Technology | Method for synthesizing ceramic powder |
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| US7648687B1 (en) | 2006-06-15 | 2010-01-19 | Eestor, Inc. | Method of purifying barium nitrate aqueous solution |
| US7993611B2 (en) * | 2006-08-02 | 2011-08-09 | Eestor, Inc. | Method of preparing ceramic powders using ammonium oxalate |
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