JPS63129017A - Production of fine powdery zirconia - Google Patents
Production of fine powdery zirconiaInfo
- Publication number
- JPS63129017A JPS63129017A JP27739286A JP27739286A JPS63129017A JP S63129017 A JPS63129017 A JP S63129017A JP 27739286 A JP27739286 A JP 27739286A JP 27739286 A JP27739286 A JP 27739286A JP S63129017 A JPS63129017 A JP S63129017A
- Authority
- JP
- Japan
- Prior art keywords
- zro2
- fine
- stabilizer
- powder
- hydrate
- 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
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000000843 powder Substances 0.000 claims abstract description 26
- 239000000725 suspension Substances 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000001354 calcination Methods 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims abstract description 4
- 238000005406 washing Methods 0.000 claims abstract description 4
- 238000010298 pulverizing process Methods 0.000 claims abstract description 3
- 239000010419 fine particle Substances 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 3
- 150000003863 ammonium salts Chemical class 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims 1
- 239000011343 solid material Substances 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
- 239000003381 stabilizer Substances 0.000 abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 abstract description 7
- IVORCBKUUYGUOL-UHFFFAOYSA-N 1-ethynyl-2,4-dimethoxybenzene Chemical compound COC1=CC=C(C#C)C(OC)=C1 IVORCBKUUYGUOL-UHFFFAOYSA-N 0.000 abstract description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 abstract description 4
- 230000001376 precipitating effect Effects 0.000 abstract description 3
- 150000003754 zirconium Chemical class 0.000 abstract description 3
- 239000002244 precipitate Substances 0.000 abstract description 2
- 229910009253 Y(NO3)3 Inorganic materials 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 230000003301 hydrolyzing effect Effects 0.000 abstract 1
- BXJPTTGFESFXJU-UHFFFAOYSA-N yttrium(3+);trinitrate Chemical compound [Y+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O BXJPTTGFESFXJU-UHFFFAOYSA-N 0.000 abstract 1
- 238000000034 method Methods 0.000 description 10
- 238000000975 co-precipitation Methods 0.000 description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 5
- 239000003513 alkali Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 150000002500 ions Chemical class 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000006104 solid solution Substances 0.000 description 2
- 229910002076 stabilized zirconia Inorganic materials 0.000 description 2
- 229910001928 zirconium oxide Inorganic materials 0.000 description 2
- OBOSXEWFRARQPU-UHFFFAOYSA-N 2-n,2-n-dimethylpyridine-2,5-diamine Chemical compound CN(C)C1=CC=C(N)C=N1 OBOSXEWFRARQPU-UHFFFAOYSA-N 0.000 description 1
- NGDQQLAVJWUYSF-UHFFFAOYSA-N 4-methyl-2-phenyl-1,3-thiazole-5-sulfonyl chloride Chemical compound S1C(S(Cl)(=O)=O)=C(C)N=C1C1=CC=CC=C1 NGDQQLAVJWUYSF-UHFFFAOYSA-N 0.000 description 1
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- -1 oxygen ion Chemical class 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- DUNKXUFBGCUVQW-UHFFFAOYSA-J zirconium tetrachloride Chemical compound Cl[Zr](Cl)(Cl)Cl DUNKXUFBGCUVQW-UHFFFAOYSA-J 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、高強度高靭性の特性を有し、軸受、メカニカ
ルシール、治工具、刃物類、粉砕用メディア、内張材、
エンジン部品等の構造用セラミックスとして、またその
酸素イオン伝導性を利用して酸素センサー、酸素ポンプ
等の機能材料用セラミックスとしても利用されるジルコ
ニア焼結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 has characteristics of high strength and high toughness, and is applicable to bearings, mechanical seals, jigs and tools, cutlery, crushing media, lining materials,
The present invention relates to a method for producing raw material powder for zirconia sintered bodies, which are used as structural ceramics for engine parts and the like, and also as functional material ceramics for oxygen sensors, oxygen pumps, etc. by utilizing their oxygen ion conductivity.
[従来の技術]
従来、高強度高靭性のジルコニア(安定化ジルコニア)
の製造方法には、その安定化剤(Y2O2、CaO1M
g01CeO2等)の粉末を酸化ジルコニウムの粉末と
混合し、これを1000−1200℃の温度で仮焼して
から成形、焼結する方法が一般に採られている。[Conventional technology] Conventionally, high-strength, high-toughness zirconia (stabilized zirconia)
In the production method, stabilizers (Y2O2, CaO1M
Generally, a method is adopted in which powder of zirconium oxide (g01CeO2, etc.) is mixed with powder of zirconium oxide, and this is calcined at a temperature of 1000-1200°C, followed by shaping and sintering.
しかし、この方法では粉末同士の混合であるため均一な
混合を得にくく、焼結に1600℃以」二の高い温度を
必要とし、またその焼結体中での安定化剤の分布も不均
一になり易く、本来の特性を十分に発現できない嫌があ
った。However, since this method involves mixing powders, it is difficult to obtain uniform mixing, sintering requires a high temperature of 1,600°C or higher, and the distribution of the stabilizer in the sintered body is also uneven. There was a problem that the original characteristics could not be fully expressed.
一方、かかる従来の製法に代るものとして、近年、共沈
法と呼ばれる原料粉末の合成が行われている。この方法
は、酸化塩化ジルコニウム等の水溶性ジルコニウム塩と
、塩化イツトリウム等の安定化剤の水溶性塩とを所定量
それぞれ水に混合溶解し、これにアンモニア等のアルカ
リを加えてジルコニウム水酸化物と安定化剤の水酸化物
との混合物を共沈させ、この共沈物を濾過洗浄して乾燥
した後、仮焼、粉砕して粉末とするものである。On the other hand, as an alternative to such conventional production methods, synthesis of raw material powders called a coprecipitation method has recently been carried out. In this method, a water-soluble zirconium salt such as oxidized zirconium chloride and a water-soluble salt of a stabilizer such as yttrium chloride are mixed and dissolved in water, and an alkali such as ammonia is added to the mixture to form zirconium hydroxide. A mixture of hydroxide and a stabilizer is co-precipitated, and this coprecipitate is filtered, washed, dried, calcined, and ground to form a powder.
そして、この方法によれば、粉末同士の混合による場合
に比較して、著しく焼結性の改善された易焼結性の粉末
が得られるものとなっている。According to this method, an easily sinterable powder with significantly improved sinterability can be obtained compared to the case where powders are mixed together.
[発明が解決しようとする問題点]
しかし乍ら、上記共沈法によると、ジルコニウム水酸化
物と安定化剤の水酸化物とに、共沈時におけるpH等の
条件によって沈澱生成速度に差を生じるため、理想的な
均一共沈物を生成することは事実上困難で、多少の不均
一性を残すことは否めない。また、その乾燥、仮焼の段
階で、共沈水酸化物が固い凝集を生じ易く、易焼結性の
ものとする上で必要な均一微細な大きさの粉末を作り難
い欠点がある。[Problems to be Solved by the Invention] However, according to the above coprecipitation method, there is a difference in the rate of precipitation between zirconium hydroxide and the stabilizer hydroxide depending on conditions such as pH during coprecipitation. Therefore, it is practically difficult to produce an ideal homogeneous coprecipitate, and it is undeniable that some heterogeneity remains. In addition, during the drying and calcining stages, the coprecipitated hydroxide tends to form hard agglomerates, making it difficult to form powders of uniform and fine size necessary for easy sintering.
本発明は、このような問題点に鑑み、ジルコニア焼結体
に供する一層優れた易焼結性の原料粉末を得る目的で、
より均一に安定化剤を固溶しかつ容易に微細化できるジ
ルコニア微粉末の製造方法を新たに提供しようとするも
のである。In view of these problems, the present invention aims to obtain a raw material powder with even better sinterability for use in zirconia sintered bodies.
The present invention aims to provide a new method for producing fine zirconia powder that can more uniformly dissolve a stabilizer in solid solution and can be easily refined.
[問題点を解決するための手段]
本発明は、このような目的を達成するために、以下のよ
うな手段を採る。すなわち、水和ジルコニア微粒子の懸
濁液に、安定化剤のイオン(Y3−。[Means for Solving the Problems] In order to achieve the above object, the present invention takes the following means. That is, stabilizer ions (Y3-) are added to the suspension of hydrated zirconia fine particles.
Ca2+、Mg2+、Ce”)の一種又は二種以上を添
加混合して溶解させる。次いで、これにアンモニア水又
はアンモニウム塩の水溶液を単独又は混合して加えて、
前記安定化剤を水酸化物又は不溶性の炭酸塩として沈澱
させると同時に、前記水和ジルコニア微粒子を軟凝集さ
せる。しかる後、これらを均一に混合して沈降される固
形物を懸濁液から濾過、水洗して分離し、さらに乾燥、
仮焼、粉砕の工程を経て安定化剤を均一に固溶したジル
コニア微粉末を得るようにする。One or more of Ca2+, Mg2+, Ce") is added and mixed and dissolved. Next, aqueous ammonia or an aqueous solution of ammonium salts is added alone or in combination,
At the same time as the stabilizer is precipitated as a hydroxide or insoluble carbonate, the hydrated zirconia fine particles are soft aggregated. After that, these are mixed uniformly, and the precipitated solids are separated from the suspension by filtration, washing with water, and further drying.
Through the steps of calcining and pulverization, fine zirconia powder in which the stabilizer is uniformly dissolved is obtained.
本発明で用いる水和ジルコニア微粒子の懸濁液は、ジル
コニウム塩の水溶液の加水分解若しくは水酸化ジルコニ
ウムの加熱熟成等により得ることができる。The suspension of hydrated zirconia fine particles used in the present invention can be obtained by hydrolysis of an aqueous solution of a zirconium salt, heat aging of zirconium hydroxide, or the like.
また、この懸濁ゾルに対する( Y 3+’)等の安定
化剤イオンの添加方法には、それらの塩化物、硝酸塩等
の水溶性塩の添加あるいはそれらの酸化物を硝酸等の酸
に溶解した溶液の混合、などの手段によることができる
。In addition, methods for adding stabilizer ions such as (Y 3+') to this suspended sol include the addition of water-soluble salts such as chlorides and nitrates, or dissolving these oxides in acids such as nitric acid. This can be done by means such as mixing solutions.
さらに、安定化剤の沈澱生成の手段としては、Y3+、
Ce4+の場合には、アンモニア等のアルカリ添加によ
る水酸化物としての固形化が一般的であるが、Ca 2
+、M g ”十に場合については、アルカリと炭酸ア
ンモニウム等の炭酸塩との混合水溶液の添加によるCa
C0z等の不溶性炭酸塩の生成によるのが望ましい。Furthermore, as a means of precipitating the stabilizer, Y3+,
In the case of Ce4+, it is common to solidify it as a hydroxide by adding an alkali such as ammonia, but Ca2+
+, M g "In the case of 10, Ca by addition of a mixed aqueous solution of alkali and carbonate such as ammonium carbonate.
Preferably, this is through the formation of an insoluble carbonate such as C0z.
なお、以降の濾過、水洗等の処理工程については、従前
の共沈法の場合と同様である。Note that the subsequent treatment steps such as filtration and water washing are the same as in the case of the conventional coprecipitation method.
[作用]
このように水和ジルコニア微粒子の懸濁液中に所望の安
定化剤イオンを溶解させた液を、アルカリ等の沈澱剤を
加えて処理するようにしたものでは、Zr”+と安定化
剤イオンの混合溶液からアルカリ添加で両者の水酸化物
を共沈させるようにした今までの共沈法では得られない
、ジルコニアと安定化剤と極めて均一に混合した共沈固
形物を得ることができる。その理由は、あらかじめ水和
ジルコニア粒子が液中に均一に分散している中で安定化
剤の沈澱を生じさせることにより、極めて均一なジルコ
ニアと安定化剤の混合共沈物が得られるものである。ま
た、こうして得られた共沈物は水酸化物の場合と異なり
、乾燥仮焼時における凝集が強固にならず、極めてほぐ
しやすく微粉になり易いものである。[Function] In this way, when a suspension of hydrated zirconia fine particles in which a desired stabilizer ion is dissolved is treated by adding a precipitant such as an alkali, Zr"+ is stabilized. By adding alkali to a mixed solution of stabilizer ions, both hydroxides are co-precipitated.A coprecipitated solid product is obtained in which zirconia and stabilizer are mixed extremely uniformly, which cannot be obtained by conventional coprecipitation methods. The reason for this is that by precipitating the stabilizer while the hydrated zirconia particles are uniformly dispersed in the liquid, an extremely uniform co-precipitate of zirconia and the stabilizer can be created. Furthermore, unlike the case of hydroxide, the coprecipitate thus obtained does not aggregate strongly during drying and calcining, and is extremely easy to loosen and become fine powder.
[実施例]
一例としてイツトリアを安定化剤として含むジルコニア
微粉末の製造方法と、この原料粉末及び該粉末を用いた
ジルコニア焼結体の特性を、下記に詳述する。[Example] As an example, a method for producing fine zirconia powder containing ittria as a stabilizer, and characteristics of this raw material powder and a zirconia sintered body using the powder will be described in detail below.
液中に1モルの水和ジルコニア微粒子(平均粒子径=−
1μm)を含む懸濁液1gに硝酸イツトリウムを0゜0
6モル加え溶解混合させた後、撹拌しなから1:1アン
モニア水を液のpHが8〜9となるまで加えて固形物を
沈降させ、これを洗浄、濾過脱水した。1 mol of hydrated zirconia fine particles (average particle size = -
Add yttrium nitrate to 1 g of suspension containing 1 μm).
After adding 6 mol and dissolving and mixing, 1:1 ammonia water was added without stirring until the pH of the liquid became 8 to 9 to precipitate the solid, which was washed, filtered and dehydrated.
この含水ケーキを150℃で24hr乾燥したところ乾
燥物は指先で容易にほぐれる塊状物となった。これを0
.1mm以下に解砕し、電気炉中で800°C,lhr
仮焼した後、ポットミルで粉砕した。When this water-containing cake was dried at 150° C. for 24 hours, the dried product became a lump that could be easily loosened with fingertips. Set this to 0
.. Crush it to 1mm or less and heat it in an electric furnace at 800°C for lhr.
After calcining, it was ground in a pot mill.
得られたジルコニア微粉末の性状を第1表に示す。Table 1 shows the properties of the obtained zirconia fine powder.
第1表
次いで、この粉末を用いてφ20Xt2+nmのペレッ
ト状成形体を金型プレス(プレス圧98MPa)で作成
し、1300〜1500℃で焼成した。得られた焼結体
の密度(g/cm3)を、従来の共沈法で得られた粉末
を用いたものと比較して第2表に示す。Table 1 Next, using this powder, a pellet-like molded body having a diameter of 20×t2+nm was produced using a mold press (pressing pressure of 98 MPa), and fired at 1300 to 1500°C. The density (g/cm3) of the obtained sintered body is shown in Table 2 in comparison with that using powder obtained by a conventional coprecipitation method.
第2表
[発明の効果]
以」−のように、本発明の製造方法によると、ファイン
セラミック用安定化ジルコニアの原料粉末として、安定
化剤をより均一に固溶した微細な易焼結性に優れるもの
が得られる。したがって、この粉末を用いれば、緻密で
均一組成を有する高品質のジルコニア焼結体をより低い
焼結温度により筒中かつ確実に提供することができる。Table 2 [Effects of the Invention] As shown in the following, according to the production method of the present invention, as a raw material powder of stabilized zirconia for fine ceramics, fine, easily sinterable powder with a more uniform solid solution of the stabilizer can be obtained. You can get something that is excellent. Therefore, by using this powder, a high quality zirconia sintered body having a dense and uniform composition can be reliably provided in a cylinder at a lower sintering temperature.
Claims (1)
a^2^+、Mg^2^+、Ce^4^+を含む化合物
の一種又は二種以上を溶解させ、これにアンモニア水又
はアンモニウム塩の水溶液を単独又は混合して加えて固
形物を沈降させ、該固形物を濾過、水洗、仮焼、粉砕す
ることを特徴とするジルコニア微粉末の製造方法。Each of Y^3^+ and C was added to the suspension of hydrated zirconia fine particles.
One or more compounds containing a^2^+, Mg^2^+, and Ce^4^+ are dissolved, and ammonia water or an aqueous solution of ammonium salts is added alone or in combination to form a solid substance. A method for producing fine zirconia powder, which comprises settling, filtering, washing with water, calcining, and pulverizing the solid material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27739286A JPS63129017A (en) | 1986-11-19 | 1986-11-19 | Production of fine powdery zirconia |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27739286A JPS63129017A (en) | 1986-11-19 | 1986-11-19 | Production of fine powdery zirconia |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63129017A true JPS63129017A (en) | 1988-06-01 |
Family
ID=17582898
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27739286A Pending JPS63129017A (en) | 1986-11-19 | 1986-11-19 | Production of fine powdery zirconia |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63129017A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007142116A1 (en) | 2006-06-05 | 2007-12-13 | Nissan Chemical Industries, Ltd. | Method for producing metal oxide particle |
JP2008019621A (en) * | 2006-07-12 | 2008-01-31 | Asahi Kasei Homes Kk | Preassembled reinforcing bar temporarily erecting jig, and method of connecting preassembled reinforcing bar |
-
1986
- 1986-11-19 JP JP27739286A patent/JPS63129017A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007142116A1 (en) | 2006-06-05 | 2007-12-13 | Nissan Chemical Industries, Ltd. | Method for producing metal oxide particle |
JP2008019621A (en) * | 2006-07-12 | 2008-01-31 | Asahi Kasei Homes Kk | Preassembled reinforcing bar temporarily erecting jig, and method of connecting preassembled reinforcing bar |
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