JPS63222014A - Production of oxide fine powder of perovskite type - Google Patents
Production of oxide fine powder of perovskite typeInfo
- Publication number
- JPS63222014A JPS63222014A JP5529187A JP5529187A JPS63222014A JP S63222014 A JPS63222014 A JP S63222014A JP 5529187 A JP5529187 A JP 5529187A JP 5529187 A JP5529187 A JP 5529187A JP S63222014 A JPS63222014 A JP S63222014A
- Authority
- JP
- Japan
- Prior art keywords
- fine powder
- urea
- oxide fine
- perovskite type
- coprecipitated
- 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.)
- Granted
Links
- 239000000843 powder Substances 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000004202 carbamide Substances 0.000 claims abstract description 25
- 239000000243 solution Substances 0.000 claims abstract description 20
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 13
- 229910052745 lead Inorganic materials 0.000 claims abstract description 11
- 229910052726 zirconium Inorganic materials 0.000 claims abstract description 11
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 8
- 239000007864 aqueous solution Substances 0.000 claims abstract description 5
- 229910021645 metal ion Inorganic materials 0.000 claims description 7
- 238000000034 method Methods 0.000 abstract description 19
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 6
- 238000001354 calcination Methods 0.000 abstract description 5
- 238000007796 conventional method Methods 0.000 abstract description 5
- 229910021529 ammonia Inorganic materials 0.000 abstract description 3
- 238000000227 grinding Methods 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 abstract description 3
- 238000001035 drying Methods 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract 4
- 150000001455 metallic ions Chemical class 0.000 abstract 2
- 230000008030 elimination Effects 0.000 abstract 1
- 238000003379 elimination reaction Methods 0.000 abstract 1
- 150000004679 hydroxides Chemical class 0.000 abstract 1
- 239000000047 product Substances 0.000 description 12
- 238000000975 co-precipitation Methods 0.000 description 8
- 239000011259 mixed solution Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 239000010936 titanium Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 238000006386 neutralization reaction Methods 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- 238000010298 pulverizing process Methods 0.000 description 4
- 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 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910000000 metal hydroxide Inorganic materials 0.000 description 3
- 150000004692 metal hydroxides Chemical class 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- -1 ammonium ions Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- RLJMLMKIBZAXJO-UHFFFAOYSA-N lead nitrate Chemical compound [O-][N+](=O)O[Pb]O[N+]([O-])=O RLJMLMKIBZAXJO-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- UJVRJBAUJYZFIX-UHFFFAOYSA-N nitric acid;oxozirconium Chemical compound [Zr]=O.O[N+]([O-])=O.O[N+]([O-])=O UJVRJBAUJYZFIX-UHFFFAOYSA-N 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000011164 primary particle Substances 0.000 description 2
- 241001245789 Goodea atripinnis Species 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000004703 alkoxides Chemical class 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000011978 dissolution method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は尿素を用いた中和共沈法によるペロブスカイト
型酸化物微粉末の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing perovskite-type oxide fine powder by a neutralization coprecipitation method using urea.
ペロブスカイト型酸化物は一般にPbZrxTi1XO
!1として表わされる固溶体である。その粉末は強誘電
体、圧電体等の電気部材の原料として実用に供されてい
る。Perovskite oxides are generally PbZrxTi1XO
! It is a solid solution represented as 1. The powder is in practical use as a raw material for electrical components such as ferroelectrics and piezoelectrics.
用途上、より高い電気的特性(たとえば電気機械結合係
数)を要求されるため、該酸化物は高純度かつ平均粒子
径がサブミクロンのものが求められている。Since higher electrical properties (for example, electromechanical coupling coefficient) are required for the purpose of use, the oxide is required to have high purity and an average particle size of submicrons.
ペロブスカイト型酸化物粉末の製法は種々開発されてい
るが、製造コストが低く、かつ工程が簡単なアンモニア
中和共沈法(湿式法)が工業的に採用されている。Various methods for producing perovskite-type oxide powder have been developed, but the ammonia-neutralized coprecipitation method (wet method), which has a low production cost and a simple process, has been industrially adopted.
この製法はPb + Z r + T ]の各金属水酸
化物が水に難溶であることに着眼して開発されたもので
ある。すなわちPb、 Zr、 Tiの各金属イオンを
溶解させた混液にアンモニア水を滴下するか、逆にアン
モニア水に混液を滴下して混合溶液をpH6〜8にし、
Pb、 Zr、 Tiの各イオンを水酸化物として共沈
させ、得られた共沈物を濾過し、乾燥し、仮焼してはロ
ブスカイト型酸化物粉末を製造する方法である。This production method was developed based on the fact that metal hydroxides of Pb + Z r + T are poorly soluble in water. That is, ammonia water is dropped into a mixed solution in which each metal ion of Pb, Zr, and Ti is dissolved, or conversely, the mixed solution is dropped into ammonia water to make the mixed solution pH 6 to 8.
In this method, each ion of Pb, Zr, and Ti is coprecipitated as hydroxide, and the resulting coprecipitate is filtered, dried, and calcined to produce a robskite-type oxide powder.
前記アンモニア中和共沈法によって製造された酸化物粉
末の一次粒子は細かく、かつ組成的にも均一である。し
かしこの方法では沈澱形成段階で生成した各沈澱物が凝
集しながら共沈し、その乾燥物は非常に固い団塊となり
、仮焼後壕でその形状をとどめている。The primary particles of the oxide powder produced by the ammonia neutralization coprecipitation method are fine and uniform in composition. However, in this method, each precipitate produced in the precipitate formation stage coagulates and coprecipitates, and the dried material becomes a very hard lump that retains its shape in the trench after calcination.
そこで該中和共沈法では一般に乾燥後の乾燥物あるいは
仮焼後の仮焼物を耐摩耗性のライニング、媒体を整備し
た粉砕機を用いて粉砕して該酸化物の粉末を製造する。Therefore, in the neutralization coprecipitation method, the oxide powder is generally produced by pulverizing the dried material after drying or the calcined product after calcination using a pulverizer equipped with wear-resistant lining and media.
しかしながら、上記粉砕方法は機械的手段によるため、
平均粒子径はせいぜい数μm程度にしかならないこと、
および粉砕も長時間に及ぶため、ライニング等の摩耗に
よる不純物の混入が避けられないことが、従来の中和共
沈法の重大な欠点であった。However, since the above-mentioned pulverization method is based on mechanical means,
The average particle size is only a few μm at most;
A major drawback of the conventional neutralization coprecipitation method was that the grinding process also took a long time, so contamination with impurities due to wear of the lining etc. was unavoidable.
そこで、本発明者らはアンモニア中和共沈法を改良して
、粉砕工程を必要としないペロブスカイト型酸化物微粉
末の製造方法について研究した結果、アンモニアに替え
て尿素を採用することにより、従来法の欠点が解消でき
ることを見い出して本発明を完成した。Therefore, the present inventors improved the ammonia neutralization coprecipitation method and researched a method for producing perovskite-type oxide fine powder that does not require a pulverization process. The present invention was completed by discovering that the drawbacks of the method can be overcome.
すなわち本発明はPb 、 Zr 、 Tjの各金属イ
オンを含む硝酸溶液(以下単に「硝酸溶液」という)と
、前記金属イオンと反応し共沈させるに要する量以上の
尿素を溶解させた水溶液(以下「尿素溶液Jという)と
を混合後、加熱して尿素を分解させ、各金属イオンと反
応させて水酸化物とし共沈させ、得られた共沈物を謔過
し、乾燥し、仮焼してつくるペロブスカイト型酸化物の
製造方法を要旨とするものである。That is, the present invention uses a nitric acid solution (hereinafter simply referred to as "nitric acid solution") containing metal ions of Pb, Zr, and Tj, and an aqueous solution (hereinafter simply referred to as "nitric acid solution") in which urea is dissolved in an amount greater than the amount required to react with the metal ions and cause co-precipitation. After mixing with urea solution J), the urea is decomposed by heating, reacted with each metal ion to form a hydroxide, and co-precipitated.The resulting coprecipitate is filtered, dried, and calcined. The gist of this paper is a method for producing perovskite-type oxides.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明に用いる尿素は純度の高い市販品が用いられる。As the urea used in the present invention, a commercially available product with high purity is used.
尿素溶液をつくるときに配合される尿素量は製造される
にロブスカイト型酸化物1モルに対し、少なくとも6モ
ル以」二、好ましい配合量は6〜60モルである。6モ
ル未満では各金属イオンが全量共沈しない場合があり、
30モルを超えれば仮焼物中に尿素が残存する場合もあ
るので、仮焼時間を非常に長くしなければならないこと
があり、いずれも好丑しくない。The amount of urea added when preparing the urea solution is at least 6 mol or more, preferably 6 to 60 mol, per 1 mol of the lobskite type oxide to be produced. If the amount is less than 6 mol, the entire amount of each metal ion may not be coprecipitated.
If the amount exceeds 30 moles, urea may remain in the calcined product, which may require a very long calcining time, which is undesirable.
尿素を水に溶解する方法は、慣用の方法にしたがって尿
素溶液をつくる。To dissolve urea in water, a urea solution is prepared according to a conventional method.
次に硝酸溶液のつくり方を説明する。Next, we will explain how to make a nitric acid solution.
硝酸溶液をつくるにはPb、 Zr+ Tiの各金属原
子を含む化合物を濃硝酸に溶解させることによってつく
られる。溶解方法は慣用方法による。A nitric acid solution is prepared by dissolving a compound containing metal atoms of Pb and Zr+Ti in concentrated nitric acid. The dissolution method is a conventional method.
化合物としては硝酸塩、オキシ硝酸塩等の無機化合物の
ほか、金属アルコキシド、酢酸塩等の有機化合物などが
示される。一つの化合物に上記金属原子が2種以上含ま
れていることはさしつかえない。Examples of compounds include inorganic compounds such as nitrates and oxynitrates, as well as organic compounds such as metal alkoxides and acetates. It is acceptable for one compound to contain two or more of the above metal atoms.
化合物の配合割合はPb、 Zr、 Tiの各金属原子
比が仮焼したさいに所望のペロブスカイト型酸化物にな
るような割合にすればよく、本発明ではその比を特に限
定しない。The compounding ratio of the compound may be such that the atomic ratio of each metal of Pb, Zr, and Ti becomes a desired perovskite type oxide upon calcining, and the ratio is not particularly limited in the present invention.
次に共沈物のつくり方を説明する。Next, we will explain how to make a coprecipitate.
上記のようにしてつくられた硝酸溶液に尿素溶液を加え
、あるいはその逆に加え混液どする。Add the urea solution to the nitric acid solution prepared as described above, or vice versa, and mix.
このとき、Pb、 Zr、 Tiの沈澱生成を防ぐため
混液をpH2以下に保つことが重要である。ついで混液
を攪拌しながらその混液を加熱する。加熱によって尿素
が分解し、Pl:) + Zr 、T1の各金属イオン
と反応してそれぞれの金属水酸化物が生成し共沈する。At this time, it is important to maintain the pH of the mixed solution at 2 or less in order to prevent precipitation of Pb, Zr, and Ti. The mixture is then heated while stirring. Urea is decomposed by heating and reacts with each metal ion of Pl:) + Zr and T1 to generate respective metal hydroxides and co-precipitate.
混液の加熱温度は尿素が効率よく分解する温度であれば
よく、好ましいのは50〜105℃である。50℃未満
では分解反応が遅いため沈澱形成が遅く、逆に105℃
を超えると加熱中に尿素分解物がガスとなって揮散する
ので好ましくない。The heating temperature of the mixed liquid may be a temperature at which urea is efficiently decomposed, and is preferably 50 to 105°C. Below 50℃, the decomposition reaction is slow and precipitation formation is slow;
Exceeding this is not preferable because the urea decomposition products become gas and volatilize during heating.
混液中に生成した共沈物はE過され、乾燥される。得ら
れた乾燥物はほとんど一次粒子のフワフワした粉末状で
ある。The coprecipitate formed in the mixed solution is filtered and dried. The obtained dried product is mostly in the form of a fluffy powder of primary particles.
得られた乾燥物は500〜1ooo℃、空気中で仮焼す
れシj゛平均粒径がサブミクロンのペロブスカイト型酸
化物微粉末が得られる。The obtained dried product is calcined in air at 500 to 100°C to obtain a perovskite type oxide fine powder with an average particle size of submicron.
本発明でつくられた乾燥物や仮焼物が従来法のように団
塊にならず、フワフワした粉末状になる理由は不詳であ
るが、次のように推定することができる。The reason why the dried product or calcined product produced by the present invention does not form into lumps as in the conventional method but instead becomes a fluffy powder is not known, but it can be assumed as follows.
すなわち混液の加熱によって尿素が部分的に分解し、尿
素およびアンモニウムイオンとして存在し、混液なアル
カリ性にする一方、イオン状態のPb、 Zr、 Ti
の各金属はアルカリと反応してゲル(水酸化物)を生成
する。That is, by heating the mixed solution, urea partially decomposes and exists as urea and ammonium ions, making the mixed solution alkaline, while Pb, Zr, and Ti in the ionic state
Each metal reacts with an alkali to form a gel (hydroxide).
このゲル表面に尿素および/またはアンモニウムイオン
が吸着し、各ゲル相互に反発し、凝集せずに共沈堆積す
るために、その乾燥物も微細化されたフワフワした状態
になるものと思われる。It is thought that urea and/or ammonium ions are adsorbed on the gel surface, repelled from each other, and co-precipitated without agglomeration, resulting in the dried product becoming fine and fluffy.
市販のオキシ硝酸ジルコニウム水溶液、チタンイソプロ
ポキシドおよび無水硝酸鉛を用いてペロブスカイト型酸
化物微粉末を製造した。Perovskite-type oxide fine powder was manufactured using a commercially available aqueous zirconium oxynitrate solution, titanium isopropoxide, and anhydrous lead nitrate.
オキシ硝酸ジルコニウム水溶液52.5m/(ZrO0
6mol/7 )に濃硝酸ろOm7!を加えたのち、チ
タンイソプロポキシド44.4m/!(Tiろ32mo
1.//−)を滴下し、攪拌して透明な溶液にした。こ
の溶液に無水硝酸鉛101.0ii’を加え、溶解させ
、Pb 、 Zr 。Zirconium oxynitrate aqueous solution 52.5m/(ZrO0
6mol/7) with concentrated nitric acid filter Om7! After adding 44.4 m/! of titanium isopropoxide! (Tiro 32mo
1. //-) was added dropwise and stirred to give a clear solution. 101.0ii' of anhydrous lead nitrate was added to this solution and dissolved to form Pb and Zr.
T]の原子比が1 : 0.52 : 0.4.8の硝
酸溶液をつくつた。A nitric acid solution with an atomic ratio of 1:0.52:0.4.8 was prepared.
三方、表1に示す尿素量を1000mlの純水に溶解さ
せて尿素溶液をつくった。On the other hand, a urea solution was prepared by dissolving the amount of urea shown in Table 1 in 1000 ml of pure water.
それら尿素溶液に硝酸溶液を加えてそれぞれの混液をつ
くったところ、各混液ともほぼpH1,6であった。つ
いで、各混液を表1に示す条件で加熱して共沈させたが
、このとき各混液ともほぼpHは8であった。When a nitric acid solution was added to these urea solutions to prepare respective mixtures, the pH of each mixture was approximately 1.6. Next, each mixed liquid was heated under the conditions shown in Table 1 to cause coprecipitation, and at this time, the pH of each mixed liquid was approximately 8.
各混液を吸引濾過(P紙5C)に共沈物を分別し、70
℃、24時間乾燥した。得られた各乾燥物はフワフワし
た微粉末であった。Each mixed solution was suction filtered (P paper 5C) to separate the coprecipitate, and
It was dried at ℃ for 24 hours. Each dried product obtained was a fluffy fine powder.
各乾燥物は600℃、1時間(ただし、実施例8のみは
2時間)電気炉で仮焼してペロブスカイト型酸化物を製
造した。製造された各試料とも5417であり、微粉末
状態であった。Each dried product was calcined in an electric furnace at 600° C. for 1 hour (2 hours only for Example 8) to produce a perovskite-type oxide. Each of the manufactured samples had a particle size of 5417 and was in a fine powder state.
各酸化物微粉末の平均粒径は自然沈降式粒度測定機で調
べ、その結果を表1に併記した。また鉱物組成について
X線回折計で調べたところ全試料ともPbZr1)、5
2T同、4.803の単一鉱物であった。The average particle diameter of each oxide fine powder was determined using a natural sedimentation particle size analyzer, and the results are also listed in Table 1. In addition, when the mineral composition was examined using an X-ray diffractometer, all samples contained PbZr1), 5
2T was a single mineral of 4.803.
表 1
〔発明の効果〕
本発明は金属水酸化物の共沈物をつくるのに、尿素を採
用したので、仮焼物は従来法のように団塊にならず、ザ
ブミクロンの微粉末を粉砕工程を経ずして製造でき、そ
の分不純物の混入の少ないペロブスカイト型酸化物微粉
末か得られる。Table 1 [Effects of the Invention] Since the present invention employs urea to create a coprecipitate of metal hydroxide, the calcined product does not form lumps unlike the conventional method, and the fine powder of Zabumicron is not subjected to the pulverizing process. The perovskite-type oxide fine powder can be produced without any process, and the perovskite-type oxide fine powder with less impurities can be obtained.
Claims (1)
素を溶解させた水溶液とを混合し、加熱して共沈物を生
成させたのち、該共沈物を乾燥し、仮焼してつくること
を特徴とするペロブスカイト型酸化物微粉末の製造方法A nitric acid solution containing metal ions of Pb, Zr, and Ti and an aqueous solution in which urea is dissolved are mixed, heated to form a coprecipitate, and then the coprecipitate is dried and calcined. A method for producing perovskite-type oxide fine powder characterized by producing
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62055291A JP2547007B2 (en) | 1987-03-12 | 1987-03-12 | Method for producing perovskite type oxide fine powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62055291A JP2547007B2 (en) | 1987-03-12 | 1987-03-12 | Method for producing perovskite type oxide fine powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63222014A true JPS63222014A (en) | 1988-09-14 |
| JP2547007B2 JP2547007B2 (en) | 1996-10-23 |
Family
ID=12994476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62055291A Expired - Lifetime JP2547007B2 (en) | 1987-03-12 | 1987-03-12 | Method for producing perovskite type oxide fine powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2547007B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1990009350A1 (en) * | 1989-02-10 | 1990-08-23 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Zirconia sol, preparation thereof, slurry for use in the production of porous ceramic, and porous ceramic produced from said slurry |
| US5275759A (en) * | 1989-02-10 | 1994-01-04 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Zirconia sol, method for production thereof, porous ceramic-producing slurry, and porous ceramic product obtained by use thereof |
| EP1227139A1 (en) * | 2001-01-24 | 2002-07-31 | Max-Planck-Gesellschaft zur Förderung der Wissenschaften e.V. | Method of producing crystalline phosphor powders at low temperature |
| KR100527060B1 (en) * | 2001-04-06 | 2005-11-08 | (주)아해 | Preparation of Single and Multi-Component Oxide by Pyrophoric Synthesis Method |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61215218A (en) * | 1985-03-19 | 1986-09-25 | Agency Of Ind Science & Technol | Manufacturing method of functional oxide powder |
-
1987
- 1987-03-12 JP JP62055291A patent/JP2547007B2/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61215218A (en) * | 1985-03-19 | 1986-09-25 | Agency Of Ind Science & Technol | Manufacturing method of functional oxide powder |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1990009350A1 (en) * | 1989-02-10 | 1990-08-23 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Zirconia sol, preparation thereof, slurry for use in the production of porous ceramic, and porous ceramic produced from said slurry |
| US5275759A (en) * | 1989-02-10 | 1994-01-04 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Zirconia sol, method for production thereof, porous ceramic-producing slurry, and porous ceramic product obtained by use thereof |
| EP1227139A1 (en) * | 2001-01-24 | 2002-07-31 | Max-Planck-Gesellschaft zur Förderung der Wissenschaften e.V. | Method of producing crystalline phosphor powders at low temperature |
| KR100527060B1 (en) * | 2001-04-06 | 2005-11-08 | (주)아해 | Preparation of Single and Multi-Component Oxide by Pyrophoric Synthesis Method |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2547007B2 (en) | 1996-10-23 |
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