JP3284244B2 - Zirconium oxide powder and method for producing the same - Google Patents

Zirconium oxide powder and method for producing the same

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Publication number
JP3284244B2
JP3284244B2 JP15605791A JP15605791A JP3284244B2 JP 3284244 B2 JP3284244 B2 JP 3284244B2 JP 15605791 A JP15605791 A JP 15605791A JP 15605791 A JP15605791 A JP 15605791A JP 3284244 B2 JP3284244 B2 JP 3284244B2
Authority
JP
Japan
Prior art keywords
zirconium oxide
oxide powder
particles
powder
suspension
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP15605791A
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Japanese (ja)
Other versions
JPH04357115A (en
Inventor
英一 岩田
理治 大貝
信勝 大道
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tosoh Corp
Original Assignee
Tosoh Corp
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Priority to JP15605791A priority Critical patent/JP3284244B2/en
Priority to EP19920304892 priority patent/EP0517437B1/en
Priority to DE1992618495 priority patent/DE69218495T2/en
Priority to KR1019920009405A priority patent/KR100210762B1/en
Publication of JPH04357115A publication Critical patent/JPH04357115A/en
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は酸化ジルコニウム粉末に
関する。酸化ジルコニウム粉末は、通常他の粉末と混合
され、成形し、焼結することによって、各種の材料が製
造される。たとえば、固体電解質、圧電体、耐摩耗材、
研磨材等の製造に多量に使用されている。また、これに
イットリア、マグネシア、カルシア等の安定化剤を添加
したものは、安定化あるいは部分安定化ジルコニア焼結
体からなる構造材料等の製造に使用される。
The present invention relates to zirconium oxide powder. Zirconium oxide powder is usually mixed with other powders, molded, and sintered to produce various materials. For example, solid electrolytes, piezoelectrics, wear-resistant materials,
It is used in large quantities in the manufacture of abrasives and the like. Further, a material obtained by adding a stabilizer such as yttria, magnesia, and calcia to this is used for producing a structural material or the like made of a stabilized or partially stabilized zirconia sintered body.

【0002】本明細書中『一次粒子径』とは、透過型電
子顕微鏡又は光子相関法による粒度分布測定機器で測定
可能な粒子径1〜1000nm程度の粒子のことであ
り、『粒子径』とは、粒度分布測定装置等で測定される
体積基準分布の粒子径をいい、『平均粒子径』とは、い
わゆるメジアン径をいい、前記粒子径の累積分布が50
%に相当する粒子径をいう。また、本明細書中『水和ジ
ルコニア』とは、水酸化ジルコニウム、結晶性水和ジル
コニア、非結晶性水和ジルコニアなどと称されるものを
いう。
[0002] In the present specification, the term "primary particle size" refers to a particle having a particle size of about 1 to 1000 nm which can be measured by a transmission electron microscope or a particle size distribution measuring device by a photon correlation method. Refers to the particle size of the volume-based distribution measured by a particle size distribution measuring device or the like, and “average particle size” refers to a so-called median size, and the cumulative distribution of the particle size is 50%.
%. In this specification, the term “hydrated zirconia” refers to what is called zirconium hydroxide, crystalline hydrated zirconia, amorphous hydrated zirconia, or the like.

【0003】[0003]

【従来の技術】従来、酸化ジルコニウム粉末にイットリ
ア、マグネシア、カルシア等の安定化剤を添加したもの
を、成形後、焼結して、安定化あるいは部分安定化ジル
コニア焼結体からなる構造材料等が製造されている。前
記成形方法としては粉体を型に入れ、ピストン等で加圧
するプレス成形法や泥漿を鋳込型に流し込み、固化させ
る泥漿鋳込成形法が利用されている。
2. Description of the Related Art Conventionally, a material obtained by adding a stabilizer such as yttria, magnesia, and calcia to a powder of zirconium oxide, forming and sintering the resulting material to form a stabilized or partially stabilized zirconia sintered body. Are manufactured. As the molding method, a press molding method in which powder is put into a mold and pressurized with a piston or the like, or a slurry casting method in which slurry is poured into a casting mold and solidified is used.

【0004】[0004]

【発明が解決しようとする課題】しかし、従来粉末に
は、依然問題がある。すなわち、プレス成形を行なう場
合のラミネーション(層状の組織を構成すること)など
の欠陥の発生、泥漿鋳込成形を行なう場合の着肉速度の
遅さ、石膏鋳込型の目詰まりなど、成形性の問題であ
る。このような問題が発生すると製品の密度や強度の低
下及び生産性の低下の原因となる。この成形性の悪さは
大型の製品を製造する場合や工業的に自動プレスにより
多量の製品を製造する場合に特に問題となる。本発明の
目的は前記問題点を改善した、成形性がよく、したがっ
て、高密度、高強度の焼結体を製造することのできる酸
化ジルコニウム粉末を提供することにある。
However, conventional powders still have problems. That is, moldability such as occurrence of defects such as lamination (composing a layered structure) when performing press molding, slow deposition speed when performing slurry casting, and clogging of a gypsum casting mold. Is a problem. When such a problem occurs, the density and strength of the product and the productivity are reduced. This poor formability is particularly problematic when large products are manufactured or when a large number of products are industrially manufactured by automatic pressing. An object of the present invention is to provide a zirconium oxide powder which has improved the above-mentioned problems, has good moldability, and can produce a high-density, high-strength sintered body.

【0005】[0005]

【課題を解決するための手段】本発明者らは鋭意検討し
た結果、BET比表面積が1〜10m/g、平均粒子
径が0.1〜1μm、及び累積分布において0.1μm
以下及び10μmを越える粒子の占める割合が5%以下
であることを特徴とする酸化ジルコニウム粉末が上記目
的を達成できることを見いだし、さらにその製造方法が
煮沸加水分解して得られる、結晶子径が5nm以下、一
次粒子径が50〜150nmの水和ジルコニア粒子懸濁
液を乾燥した後、仮焼することを特徴とすることを見い
だし発明を完成した。
The present inventors have conducted intensive studies and found that the BET specific surface area is 1 to 10 m 2 / g, the average particle size is 0.1 to 1 μm, and the cumulative distribution is 0.1 μm.
And zirconium oxide powder characterized in that the proportion of particles having a particle size exceeding 10 μm is 5% or less can achieve the above-mentioned object. Hereinafter, the inventors have found that a suspension of hydrated zirconia particles having a primary particle diameter of 50 to 150 nm is dried and then calcined, thereby completing the invention.

【0006】以下その詳細について説明する。本発明の
酸化ジルコニウム粉末はBET比表面積が1〜10m
/g、平均粒子径が0.1〜1μmであることを必須と
する。該範囲よりBET比表面積が大きい又は平均粒子
径が小さい場合は、例えば、泥漿鋳込成形を行う場合に
泥漿の粘度が高くなるために高濃度の泥漿を使用するこ
とが難しい、又は石膏の鋳型に入れたときに微粉末であ
るために石膏の細孔を塞ぐため着肉速度が遅い、さらに
はプレス成形を行う場合に粒子が小さ過ぎるために成形
圧力の伝達が悪い、又はラミネーションが発生しやすい
など、いずれにしても高密度の製品が得られ難いという
問題が生じやすい。他方、該範囲よりBET比表面積が
小さい又は平均粒子径が大きい場合は、すなわち酸化ジ
ルコニウム粉末の粒子が大きく粗い場合であり、高密度
高強度の焼結体を得ることが難しい。該範囲よりBET
比表面積のみが大きい又は平均粒子径のみが大きい場合
は、酸化ジルコニウム粉末が微細な粒子の強固に凝集し
たものであり、成形焼結によっても微細粒子間の細孔が
そのまま残りやすく、結果として高密度の焼結体が得ら
れにくい。
The details will be described below. The zirconium oxide powder of the present invention has a BET specific surface area of 1 to 10 m 2.
/ G, and an average particle diameter of 0.1 to 1 μm. When the BET specific surface area is larger or the average particle size is smaller than the above range, for example, it is difficult to use a high-concentration slurry due to an increase in the viscosity of the slurry when performing slurry casting, or a gypsum mold. When it is placed in a fine powder, the inlay speed is slow to block the gypsum pores, and furthermore, when performing press molding, the transmission of the molding pressure is poor because the particles are too small, or lamination occurs. In any case, it is difficult to obtain a high-density product. On the other hand, when the BET specific surface area is smaller than this range or the average particle size is larger, that is, when the zirconium oxide powder particles are large and coarse, it is difficult to obtain a sintered body with high density and high strength. BET from the range
When only the specific surface area is large or only the average particle diameter is large, the zirconium oxide powder is agglomerated firmly of fine particles, and pores between the fine particles are likely to remain as they are even after molding and sintering. It is difficult to obtain a sintered body having a high density.

【0007】また、本発明の酸化ジルコニウム粉末は、
累積分布において0.1μm以下及び10μmを越える
粒子の占める割合が5%以下であるであることを必須と
する。該累積分布における条件は、0.1μm以下及び
10μmを越える粒子の割合が1%以下であることが好
ましく、0.1μm以下及び5μmを越える粒子の割合
が1%以下であることがより好ましい。
Further, the zirconium oxide powder of the present invention comprises:
It is essential that the proportion of particles having a cumulative distribution of 0.1 μm or less and exceeding 10 μm is 5% or less. Regarding the condition of the cumulative distribution, the ratio of particles having a particle size of 0.1 μm or less and 10 μm or more is preferably 1% or less, and the ratio of particles having a particle size of 0.1 μm or less and 5 μm or more is more preferably 1% or less.

【0008】該累積分布における条件の範囲をはずれる
と粒子中の微細すぎる又は粗大すぎる粒子が多すぎるた
め良好な成形性を得ることができず結果として高性能の
製品を得ることが難しいためである。本発明における酸
化ジルコニウム粉末の製造方法は、先ず水和ジルコニア
懸濁液の濃度を、前記水和ジルコニア懸濁液中の水和ジ
ルコニアをZrOとして換算して、約10〜約200
0g/リットル、好ましくは該換算値で10〜100g
/リットルの範囲としたものを準備する。
If the cumulative distribution is out of the range of the conditions, there are too many fine or coarse particles in the particles, so that good moldability cannot be obtained, and as a result, it is difficult to obtain a high-performance product. . In the method for producing a zirconium oxide powder in the present invention, first, the concentration of the hydrated zirconia suspension is converted to about 10 to about 200 by converting the hydrated zirconia in the hydrated zirconia suspension into ZrO 2.
0 g / liter, preferably 10 to 100 g in terms of the converted value
Prepare in the range of 1 / liter.

【0009】前記水和ジルコニア懸濁液の濃度は乾燥条
件等により一義的ではない。本発明において水和ジルコ
ニア懸濁液は、水溶性ジルコニウム塩の加水分解法によ
るものを使用する。理由としては粉末特性の整った粒子
が得られやすいためである。前記水和ジルコニア懸濁液
は、オキシ塩化ジルコニウム水溶液の加水分解法による
ものが好ましい。前記水和ジルコニア懸濁液は、イット
リア、マグネシア、カルシア等の安定化剤を添加させた
もの、すなわち仮焼後に安定化あるいは部分安定化ジル
コニア粉末を生成するようにしたものであってもよい
が、その添加方法に制限はない。
The concentration of the hydrated zirconia suspension is not unique due to drying conditions and the like. In the present invention, the hydrated zirconia suspension is obtained by a method of hydrolyzing a water-soluble zirconium salt. The reason is that particles having powder characteristics are easily obtained. The hydrated zirconia suspension is preferably prepared by a hydrolysis method of an aqueous solution of zirconium oxychloride. The hydrated zirconia suspension may be a suspension to which a stabilizer such as yttria, magnesia, and calcia is added, that is, a suspension in which a stabilized or partially stabilized zirconia powder is formed after calcination. There is no limitation on the method of addition.

【0010】本発明において、水和ジルコニア懸濁液中
の水和ジルコニア粒子は結晶子径5nm以下、さらに、
一次粒子径50〜150nmのものを使用する。該水和
ジルコニア懸濁溶液を乾燥する。
In the present invention, the hydrated zirconia particles in the hydrated zirconia suspension have a crystallite diameter of 5 nm or less.
The particles having a primary particle diameter of 50 to 150 nm are used. The hydrated zirconia suspension is dried.

【0011】前記該水和ジルコニア懸濁溶液の乾燥は噴
霧乾燥するのが好ましい。噴霧乾燥以外の乾燥方法、例
えば、静置乾燥の場合では、該乾燥粉末がブロック状と
なり均一に仮焼による熱処理を行うのが難しく、均一に
するためには乾燥後に粉砕工程が必要となり、エネルギ
ー的に損失が大きい。前記乾燥の温度は通常用いられる
温度でよく、好ましくは50〜250℃の温度で乾燥す
るのがよく、100〜200℃がより好ましい。前記乾
燥を行う前に有機化合物、または表面処理剤等を生成す
る水和ジルコニア乾燥粉末の粉体特性を制御するために
添加してもよい。
[0011] The hydrated zirconia suspension is preferably spray-dried. In the case of a drying method other than spray drying, for example, in the case of static drying, the dried powder becomes block-shaped, and it is difficult to perform heat treatment by calcining uniformly. The loss is large. The drying temperature may be a commonly used temperature, preferably 50 to 250 ° C, and more preferably 100 to 200 ° C. Before the drying, an organic compound or a surface treating agent may be added to control the powder characteristics of the hydrated zirconia dry powder.

【0012】前記有機化合物は、好ましくはアルコール
類、エステル類、界面活性剤などを使用する。とくに、
炭素数1〜10のアルコール類がよい。該有機化合物の
添加量は、前記水和ジルコニア懸濁液に有機化合物を含
有Zrに対して0.01〜10mol%の範囲が好まし
く、該含有Zrに対して0.01〜1mol%の範囲が
より好ましい。さらに、該乾燥を行いやすくするために
必要ならば、該乾燥前に該水和ジルコニア懸濁溶液の粘
度調整を行う。該粘度調整は該水和ジルコニア懸濁溶液
の粘度が50〜5000cP程度になるようにするのが
好ましい。前記粘度調整は酸、またはアルカリによって
pH調整を行うか、凝集剤、界面活性剤、有機高分子等
を添加すればよい。
As the organic compound, alcohols, esters, surfactants and the like are preferably used. In particular,
Alcohols having 1 to 10 carbon atoms are preferred. The amount of the organic compound to be added is preferably in the range of 0.01 to 10 mol% based on the Zr containing the organic compound in the hydrated zirconia suspension, and is preferably in the range of 0.01 to 1 mol% based on the Zr. More preferred. Further, if necessary to facilitate the drying, the viscosity of the hydrated zirconia suspension is adjusted before the drying. The viscosity is preferably adjusted so that the viscosity of the hydrated zirconia suspension solution is about 50 to 5000 cP. The viscosity may be adjusted with an acid or an alkali, or a coagulant, a surfactant, an organic polymer, or the like may be added.

【0013】該水和ジルコニア乾燥粉末は軽装嵩密度
1.0〜2.0g/cmであることが好ましい。該嵩
密度は1.2〜1.8g/cm3であることがより好ま
しく、1.3〜1.5g/cmであることがさらに好
ましい。前記水和ジルコニア乾燥粉末の含有水分量は1
5%以下であることが好ましく、10%以下がより好ま
しい。
The hydrated hydrated zirconia powder preferably has a light bulk density of 1.0 to 2.0 g / cm 3 . The bulk density is more preferably from 1.2 to 1.8 g / cm 3 , even more preferably from 1.3 to 1.5 g / cm 3 . The water content of the hydrated zirconia dry powder is 1
It is preferably at most 5%, more preferably at most 10%.

【0014】さらに、仮焼後の粉体特性を制御するため
に必要ならば、NaCl,NaOH等のアルカリ金属塩
又は苛性アルカリを添加してもよい。本発明において、
仮焼前の前記乾燥粉末中の塩素原子含有量がZrO
対してClとして、1〜20重量%あるのが好ましい。
該水和ジルコニア乾燥粉末を仮焼する。仮焼は酸素雰囲
気中無加圧等の、通常の方法で行えばよい。
Further, if necessary for controlling the powder characteristics after calcination, an alkali metal salt such as NaCl or NaOH or a caustic alkali may be added. In the present invention,
As Cl chlorine atom content of the dry powder of the calcined before the relative ZrO 2, there is preferably 1 to 20 wt%.
The dried hydrated zirconia powder is calcined. The calcination may be performed by a normal method such as no pressurization in an oxygen atmosphere.

【0015】仮焼工程における昇温速度は1分間に2℃
以下が好ましい。該仮焼温度700℃以下の領域では1
分間に1℃以下が好ましく、0.5℃以下がより好まし
い。さらに、該仮焼温度が700℃を越えた領域では、
該昇温速度は1分間に2℃以下が好ましい。前記仮焼温
度は900〜1300℃が好ましく、1000〜120
0℃がより好ましい。前記仮焼温度での保持時間は1時
間以上が好ましく、2時間以上がより好ましい。生成し
た酸化ジルコニウム粉末を必要に応じて洗浄、解砕した
後、必要ならば粉砕する。
The heating rate in the calcination step is 2 ° C./min.
The following is preferred. In the region where the calcination temperature is 700 ° C. or less, 1
The temperature is preferably 1 ° C. or less per minute, more preferably 0.5 ° C. or less. Further, in a region where the calcination temperature exceeds 700 ° C.,
The heating rate is preferably 2 ° C. or less per minute. The calcination temperature is preferably 900 to 1300 ° C.,
0 ° C. is more preferred. The holding time at the calcining temperature is preferably 1 hour or more, and more preferably 2 hours or more. The generated zirconium oxide powder is washed and crushed as necessary, and then crushed if necessary.

【0016】洗浄はジルコニウム及び安定化用化合物以
外のアルカリ金属原子及び金属原子等の不純物原子を酸
化物に換算した値が含有ZrをZrOに換算した値に
対して、好ましくは2000ppm以下、より好ましく
は1000ppm以下、さらに好ましくは600ppm
以下になるまで洗浄するのがよい。解砕は弱く凝集した
粗大粒子の凝集を解くために行う。粉砕は通常の方法、
媒体ミル、振動ミル、及びでボールミル等で粉砕するこ
とが好ましい。前記解砕後、好ましくは前記該酸化ジル
コニウム懸濁液を噴霧乾燥する。
In the cleaning, the value obtained by converting impurity atoms such as alkali metal atoms and metal atoms other than zirconium and the stabilizing compound into oxides is preferably 2,000 ppm or less, more preferably not more than 2000 ppm with respect to the value obtained by converting contained Zr to ZrO 2. Preferably 1000 ppm or less, more preferably 600 ppm
It is good to wash until the following. The disintegration is performed to disintegrate the weakly aggregated coarse particles. Grinding is the usual method,
It is preferable to pulverize with a medium mill, a vibration mill, a ball mill or the like. After the crushing, preferably, the zirconium oxide suspension is spray-dried.

【0017】[0017]

【発明の効果】本発明の酸化ジルコニウム粉末は、工業
的にも良好な成形性を示し、該成形体を焼結することに
より密度、強度等の点で従来のものよりも高性能で高信
頼性の酸化ジルコニウム焼結体を得ることのできる酸化
ジルコニウム粒子である。
Industrial Applicability The zirconium oxide powder of the present invention exhibits industrially good formability and, by sintering the formed body, has higher performance and higher reliability than conventional ones in terms of density, strength, etc. Zirconium oxide particles from which a sintered zirconium oxide sintered body can be obtained.

【0018】[0018]

【実施例】【Example】

実施例1 Yと換算して3mol%(Y換算値とZr
換算値との合計に対する。以下、同じ)となるYC
を含む、ZrO換算濃度50g/リットルのオキ
シ塩化ジルコニウム水溶液を煮沸加水分解した後、該Z
rO換算濃度が300g/リットルになるまで濃縮し
て、平均1次粒子径が100nmであり(光子相関法に
よる粒度分布測定器による)、結晶子径が4nmである
水和ジルコニア粒子の懸濁液を得た。該溶液をスプレー
ドライヤーにより噴霧乾燥した。得られた乾燥粒子は球
状であり、その軽装嵩密度は1.25g/cmであっ
た。該乾燥粉末を仮焼した。仮焼は500℃までは昇温
速度1℃/min.で、その後1050℃までは昇温速
度1.5℃/min.で昇温し、1050℃で2時間保
持して、酸化ジルコニウム粉末を得た。得られた粉末を
使用して泥漿鋳込成形及びプレス成形を行ったところ、
良好の成形性を示した。
3 mol% in terms of Example 1 Y 2 O 3 (Y 2 O 3 in terms of value and Zr
O 2 in terms of value to the sum of the. The same applies to the following)
including l 3, after boiling hydrolyzing zirconium oxychloride aqueous solution of ZrO 2 concentration in terms 50 g / liter, the Z
Concentration was performed until the concentration in terms of rO 2 became 300 g / liter, and a suspension of hydrated zirconia particles having an average primary particle diameter of 100 nm (by a particle size distribution analyzer using a photon correlation method) and a crystallite diameter of 4 nm. A liquid was obtained. The solution was spray-dried with a spray drier. The obtained dried particles were spherical and had a light bulk density of 1.25 g / cm 3 . The dried powder was calcined. Calcination is performed at a heating rate of 1 ° C./min. After that, the temperature was raised at a rate of 1.5 ° C./min. And kept at 1050 ° C. for 2 hours to obtain zirconium oxide powder. When the slurry was cast and press-molded using the obtained powder,
Good moldability was exhibited.

【0019】実施例2 仮焼条件を500℃までは昇温速度1℃/min.で、
その後950℃までは昇温速度1.5℃/min.で昇
温し、950℃で2時間保持した以外は実施例1と同一
条件で行った。
Example 2 The calcination conditions were up to 500 ° C. at a rate of 1 ° C./min. so,
Thereafter, until 950 ° C., the temperature was raised at a rate of 1.5 ° C./min. , And kept at 950 ° C. for 2 hours under the same conditions as in Example 1.

【0020】実施例3 仮焼条件を500℃までは昇温速度1℃/min.で、
その後1250℃までは昇温速度1.5℃/min.で
昇温し、1250℃で2時間保持した以外は実施例1と
同一条件で行った。
Example 3 The calcination conditions were up to 500 ° C. at a rate of 1 ° C./min. so,
Thereafter, the temperature was raised to 1250 ° C. at a rate of 1.5 ° C./min. , And maintained at 1250 ° C. for 2 hours under the same conditions as in Example 1.

【0021】比較例1 Yと換算して3mol%(Y換算値とZr
換算値との合計に対する。以下、同じ)となるYC
を含む、オキシ塩化ジルコニウム水溶液を煮沸加水
分解した後、濃縮して、平均1次粒子径が140nmで
あり(光子相関法による粒度分布測定器による)、結晶
子径が6nmである水和ジルコニア粒子の懸濁液を得
た。該溶液を乾燥した後実施例1と同一の条件で仮焼し
て、酸化ジルコニウム粉末を得た。得られた粉末を使用
して泥漿鋳込成形を行なったところ、石膏鋳込型が目詰
まりして良好な成形体を得ることができなかった。
[0021] 3 mol% in terms of Comparative Example 1 Y 2 O 3 (Y 2 O 3 in terms of value and Zr
O 2 in terms of value to the sum of the. The same applies to the following)
including l 3, after boiling hydrolyzing zirconium oxychloride aqueous solution, and concentrated to an average primary particle diameter of 140 nm (according to particle size distribution measuring apparatus according to photon correlation spectroscopy), hydrated crystallite size of 6nm A suspension of zirconia particles was obtained. After the solution was dried, it was calcined under the same conditions as in Example 1 to obtain a zirconium oxide powder. When slurry casting was performed using the obtained powder, the gypsum casting mold was clogged and a good molded product could not be obtained.

【0022】比較例2 煮沸加水分解した後、濃縮して、平均1次粒子径が10
nmであり(光子相関法による粒度分布測定器によ
る)、非晶質の水和ジルコニア粒子の懸濁液を得た。該
溶液を乾燥した後実施例1と同一の条件で仮焼して、酸
化ジルコニウム粉末を得た。実施例及び比較例で得られ
た粉末の粉体特性を表1に示した。実施例及び比較例で
得られた酸化ジルコニウム粉末について、圧力700K
g/cmで57mm×34mm×約5mmに成形し
た。成形後1500℃で2時間焼成することにより、焼
結体を得た。焼結体密度をアルキメデス法により測定し
た後、得られた焼結体から、3mm×4mm×約40m
mの試験片を切り出し、JIS1601に規定された方
法により常温3点曲げ強度を測定した。30試料の平均
の結果を表2に示した。
Comparative Example 2 After boiling hydrolysis, the mixture was concentrated and the average primary particle diameter was 10%.
nm (by a photon correlation particle size analyzer) to give a suspension of amorphous hydrated zirconia particles. After the solution was dried, it was calcined under the same conditions as in Example 1 to obtain a zirconium oxide powder. Table 1 shows the powder properties of the powders obtained in the examples and the comparative examples. The zirconium oxide powders obtained in Examples and Comparative Examples were subjected to a pressure of 700K.
It was molded to 57 mm × 34 mm × about 5 mm at g / cm 2 . By firing at 1500 ° C. for 2 hours after molding, a sintered body was obtained. After measuring the sintered body density by the Archimedes method, from the obtained sintered body, 3 mm × 4 mm × about 40 m
m test piece was cut out, and the room temperature three-point bending strength was measured by the method specified in JIS1601. Table 2 shows the average results of the 30 samples.

【0023】 表 1 粉体特性 平均粒子径 BET比表面積 累積分布(%) (μm) (m/g) ≦0.1μm >10μm >5μm 実施例1 0.8 6.2 0.6 0 0.6 実施例2 0.5 9.3 0.9 0 1.0 実施例3 0.7 5.6 0.4 0.5 0.9 比較例1 0.8 15.2 6.5 0 0.5 比較例2 1.5 7.7 1.2 3.2 8.1 表 2 焼結体密度及び常温3点曲げ強度 焼結体密度 常温3点曲げ強度 (g/cm3 (kgf/mm 実施例1 6.09 125.7 実施例2 6.05 120.1 実施例3 6.07 122.3 比較例1 6.05 115.8 比較例2 5.89 99.5Table 1 Powder properties Average particle size BET specific surface area Cumulative distribution (%)(Μm) (m 2 /g)≦0.1 μm> 10 μm> 5 μm Example 1 0.8 6.2 0.6 0 0.6 Example 2 0.5 9.3 0.9 0 1.0 Example 3 0.7 5.6 0.4 0.5 0.9 Comparative Example 1 0.8 15.2 6.5 0 0.5 Comparative Example 2 1.5 7.7 1.2 3.2 8.1 Table 2 Sintered Body Density and Room Temperature Three-Point Bending Strength Sintered Body Density Room temperature 3-point bending strength (G / cm3) (kgf / mm 2)  Example 1 6.09 125.7 Example 2 6.05 120.1 Example 3 6.07 122.3 Comparative Example 1 6.05 115.8 Comparative Example 2 5.89 99.5

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C01G 25/02 C04B 35/48 CA(STN)──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int. Cl. 7 , DB name) C01G 25/02 C04B 35/48 CA (STN)

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】BET比表面積が1〜10m/g、平均
粒子径が0.1〜1μm、及び累積分布において0.1
μm以下及び10μmを越える粒子の占める割合が5%
以下であることを特徴とする酸化ジルコニウム粉末。
1. A BET specific surface area of 1 to 10 m 2 / g, an average particle diameter of 0.1 to 1 μm, and a cumulative distribution of 0.1 to 1 m 2 / g.
5% or less of particles less than μm and more than 10 μm
A zirconium oxide powder characterized by the following.
【請求項2】煮沸加水分解して得られる、結晶子径が5
nm以下、一次粒子径が50〜150nmの水和ジルコ
ニア粒子懸濁液を乾燥した後、仮焼することを特徴とす
る特許請求の範囲第1項記載の酸化ジルコニウム粉末の
製造方法。
2. A crystallite having a crystallite diameter of 5 obtained by boiling hydrolysis.
The method for producing a zirconium oxide powder according to claim 1, wherein a suspension of the hydrated zirconia particles having a primary particle diameter of 50 to 150 nm or less is dried and calcined.
JP15605791A 1991-05-31 1991-05-31 Zirconium oxide powder and method for producing the same Expired - Fee Related JP3284244B2 (en)

Priority Applications (4)

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JP15605791A JP3284244B2 (en) 1991-05-31 1991-05-31 Zirconium oxide powder and method for producing the same
EP19920304892 EP0517437B1 (en) 1991-05-31 1992-05-29 Zirconium oxide powder and a method of making thereof
DE1992618495 DE69218495T2 (en) 1991-05-31 1992-05-29 Zirconium oxide powder and process for its manufacture
KR1019920009405A KR100210762B1 (en) 1991-05-31 1992-05-30 Zirconium oxide powder and a method of making thereof

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