JPH0764563B2 - Fine powder of crystalline zirconia and method for producing the same - Google Patents
Fine powder of crystalline zirconia and method for producing the sameInfo
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- JPH0764563B2 JPH0764563B2 JP60266830A JP26683085A JPH0764563B2 JP H0764563 B2 JPH0764563 B2 JP H0764563B2 JP 60266830 A JP60266830 A JP 60266830A JP 26683085 A JP26683085 A JP 26683085A JP H0764563 B2 JPH0764563 B2 JP H0764563B2
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- zirconia
- solution
- hydrogen peroxide
- monoclinic
- fine powder
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Description
【発明の詳細な説明】 本発明は、含まれるジルコニウムのほとんどが結晶子径
30〜100Åの単斜ジルコニアであり、その2次凝集粒子
の平均径が500Åを越えないことを特徴とする結晶質ジ
ルコニアの微粉末及びその製造方法に関する。ここでジ
ルコニアとは純粋なZrO2は勿論、一般に工業的にジルコ
ニアと呼ばれる程度の10%以下のHfO2、数%までのY
2O3、その他の安定化剤や不純物を含有するものを含む
広い意味でのジルコニアを指す。DETAILED DESCRIPTION OF THE INVENTION In the present invention, most of the zirconium contained is a crystallite size.
The present invention relates to a monoclinic zirconia powder having a particle size of 30 to 100 Å, wherein the average diameter of secondary agglomerated particles does not exceed 500 Å, and to a fine powder of crystalline zirconia and a method for producing the same. Here, zirconia is not only pure ZrO 2 but also HfO 2 of 10% or less, which is generally industrially called zirconia, and Y of up to several%.
It refers to zirconia in a broad sense, including those containing 2 O 3 , other stabilizers and impurities.
従来ジルコニウムの塩水溶液を水熱の加圧下で120〜300
℃で加熱処理することによりジルコニアのハイドロゾル
を得る方法は知られており(米国特許2,984,628)、ま
たジルコニウム塩水溶液を長時間煮沸することによりジ
ルコニア微粒子懸濁液が得られることも既知である〔エ
ー.クリアフィールド;インオーガニックケミストリー
第3巻146頁1964年、(A.Clearfield;Inorg.Chem.3,146
(1964)〕。Conventionally, zirconium salt aqueous solution is 120-300 under hydrothermal pressure.
A method for obtaining a hydrosol of zirconia by heat treatment at ℃ is known (US Pat. No. 2,984,628), and it is also known that a zirconia fine particle suspension can be obtained by boiling an aqueous zirconium salt solution for a long time [A. . Clearfield; Inorganic Chemistry, Vol. 3, pp. 146, 1964, (A.Clearfield; Inorg.Chem.3,146
(1964)].
しかしながら前者では高圧下高温度でかなり長時間を要
し、また後者は一層長大な熱処理時間が必要で、何れも
工業的な大量生産に適しない非能率のものであるばかり
か、この生成粒子の特性は十分のものとはいえず、特に
2次凝集粒子の大きさは通常1000Åを越え、特に前者で
は2次粒子の大きさが不均一であり、ほとんど工業的に
応用されなかった。However, the former requires a considerably long time under high pressure and high temperature, and the latter requires a longer heat treatment time, both of which are inefficient and not suitable for industrial mass production. The characteristics are not sufficient, and the size of the secondary agglomerated particles usually exceeds 1000Å, and the size of the secondary particles is not uniform especially in the former case, so that it has hardly been industrially applied.
本発明者は基礎的研究によってこのジルコニア微粒子の
生成反応の進行の程度を定量的に決定する方法を始めて
確立し、この方法によっ種々の条件下で多数の実験を繰
返した結果、遂に過酸化水素の反応促進効果と超微粒子
化効果を発見した。The present inventor established the method for quantitatively determining the extent of the progress of the formation reaction of the zirconia fine particles by the basic research, and as a result of repeating a large number of experiments under various conditions by this method, finally the peroxidation was finally performed. We have discovered the hydrogen reaction acceleration effect and ultrafine particle formation effect.
ジルコニウム塩、例えば0.2モル/lの塩化ジルコニル水
溶液を還流冷却器付のフラスコ中で100時間程度煮沸し
続けると溶液中のジルコニウムはほぼ完全に単斜型のジ
ルコニア結晶となり、これは分離乾燥後、真空中400℃
の熱処理でもほとんど変化せずX線的に単斜型のみを示
す。またジルコニウム塩水溶液にアンモニア水を加え生
成する水酸化物の沈殿を減圧下で脱水し真空中で400℃
に熱処理したものはX線的に正方型のジルコニアに結晶
化している。従ってある時間加熱処理した反応過程にあ
る懸濁液にアンモニアを加え、得られる沈殿を注意深く
減圧下で乾燥し、真空中400℃に熱処理すれば単斜型ジ
ルコニアと正方型ジルコニアの混合物が得られ、その量
比はX線回折で容易に知ることができ、それは溶液中で
のジルコニアの生成反応の進行の程度を示す正確な尺度
となる。Zirconium salt, for example 0.2 mol / l zirconyl chloride aqueous solution continued boiling for 100 hours in a flask with a reflux condenser zirconium in the solution almost completely monoclinic zirconia crystals, which after separation and drying, 400 ° C in vacuum
There is almost no change even in the heat treatment of, and only a monoclinic type is shown in X-ray. Ammonia water is added to the aqueous zirconium salt solution to form a hydroxide precipitate, which is dehydrated under reduced pressure and vacuumed at 400 ° C.
The heat-treated product is crystallized into tetragonal zirconia by X-ray. Therefore, ammonia was added to the suspension in the reaction process which was heat-treated for a certain time, the precipitate obtained was carefully dried under reduced pressure, and heat-treated at 400 ° C in vacuum to obtain a mixture of monoclinic zirconia and tetragonal zirconia. , Its quantitative ratio can be easily known by X-ray diffraction, which is an accurate measure of the degree of progress of the zirconia formation reaction in the solution.
この方法による実験結果の比較は単に白濁の程度の比較
とは著しく異なる結果を与える。例えば0.2モル/l濃度
の塩化ジルコニル水溶液300ccを還流冷却器付のフラス
コ中で20時間程度煮沸し続けると、溶液は完全に白濁す
るが生成したジルコニア微粒子の量は全体のジルコニウ
ムの10%程度に過ぎないことが分かり、一方同じ0.2モ
ル/l濃度の塩化ジルコニル水溶液を、本発明方法により
予め陰イオン交換樹脂で、Cl-を一部OH-に変え溶液のpH
を2.0とし、さらに過酸化水素水(30%)10ccを加えて3
00ccとした溶液を同じフラスコ中で同じく20時間煮沸し
た場合には溶液は薄く乳濁した程度のゾルとなるのにジ
ルコニア微粒子の生成量は100%で生成反応が既に完了
していることを示す。これは本発明方法が加水分解によ
る結晶質ジルコニアの生成反応を顕著に促進させること
およびその生成物ジルコニアが極めて微細な超微粒子で
あることを示すものである。Comparison of the experimental results by this method gives significantly different results than comparison of the degree of cloudiness. For example, 300 cc of 0.2 mol / l concentration of zirconyl chloride aqueous solution is continuously boiled for about 20 hours in a flask equipped with a reflux condenser, but the solution becomes completely cloudy, but the amount of zirconia fine particles produced is about 10% of the total zirconium. On the other hand, the same 0.2 mol / l concentration of zirconyl chloride aqueous solution was previously prepared by the method of the present invention using an anion exchange resin to change Cl − to a part of OH − and the pH of the solution.
To 2.0, and then add 10cc of hydrogen peroxide solution (30%) to 3
When the solution of 00cc was boiled for 20 hours in the same flask, the solution became a thin and turbid sol, but the amount of zirconia fine particles produced was 100%, indicating that the production reaction was already completed. . This shows that the method of the present invention remarkably promotes the reaction of forming crystalline zirconia by hydrolysis and that the zirconia product is extremely fine ultrafine particles.
本発明は上記のように、ジルコニア生成反応の促進、高
効率化による工業生産上の利点と、生成単斜ジルコニア
の超微粒子性に基づく特性上の利点によって経済的価値
の著しく高いものであるが、これはすべて製造において
過酸化水素を出発ジルコニウム塩水溶液に加えることに
起因する。As described above, the present invention has an extremely high economic value due to the advantages of industrial production by promoting the zirconia formation reaction and increasing the efficiency, and the advantages of the characteristics of the produced monoclinic zirconia based on the ultrafine particles. This is all due to the addition of hydrogen peroxide to the starting aqueous zirconium salt solution during manufacture.
即ち、本発明は含まれるジルコニウムのほとんどが結晶
子30〜100Åの単斜ジルコニアであり、その2次凝集粒
子が容易に分離しない強固なもので、その凝集粒子の平
均径が500Åを越えないことを特徴とする結晶質ジルコ
ニアの微粉末に関する。更に、その製造方法としては、
濃度0.05〜2.0モル/lのジルコニウムの塩水溶液に、過
酸化水素または過酸化水素を生成する化合物を加え、こ
の容液を80〜300℃に加熱処理して水溶液中でジルコニ
アを単斜型に結晶化させ結晶質ジルコニアのコロイドゾ
ルを得、このゾルに塩基を加え凝集沈降させ、凝集沈降
物を分離後、極性有機溶媒で水分を置換し乾燥すること
で結晶質ジルコニアの微粉末を得ることを特徴とし、ま
た濃度0.05〜2.0モル/lのジルコニウムの塩水溶液をpH1
〜3に調製するとともに、過酸化水素または過酸化水素
を生成する化合物を加え、この溶液を80〜300℃に加熱
処理して水溶液中でジルコニアを単斜型に結晶化させ、
結晶質ジルコニアのコロイドゾルを得、このゾルに塩基
を加え凝集沈降させ、凝集沈降物を分離後、極性有機溶
媒で水分を置換し乾燥することで結晶質ジルコニアの微
粉末を得ることを特徴とする。That is, most of the zirconium contained in the present invention is monoclinic zirconia having a crystallite of 30 to 100Å, the secondary agglomerated particles are strong and do not easily separate, and the average diameter of the agglomerated particles does not exceed 500Å. And a fine powder of crystalline zirconia. Furthermore, as its manufacturing method,
Hydrogen peroxide or a compound that produces hydrogen peroxide is added to a zirconium salt aqueous solution having a concentration of 0.05 to 2.0 mol / l, and this solution is heat-treated at 80 to 300 ° C to form zirconia into a monoclinic type in the aqueous solution. A crystalline zirconia colloidal sol is obtained by crystallization, a base is added to this sol to cause coagulation and sedimentation, and the coagulated sediment is separated, followed by replacing the water with a polar organic solvent and drying to obtain crystalline zirconia fine powder. The zirconium salt aqueous solution with a concentration of 0.05 to 2.0 mol / l has a pH of 1
~ 3 while adding hydrogen peroxide or a compound that produces hydrogen peroxide, the solution is heat treated at 80 ~ 300 ℃ to crystallize zirconia into a monoclinic form in an aqueous solution,
A crystalline zirconia colloidal sol is obtained, a base is added to the sol to cause coagulation and sedimentation, the coagulated sediment is separated, and then water is replaced with a polar organic solvent to be dried to obtain a fine powder of crystalline zirconia. .
本発明方法においてジルコニウム塩溶液の濃度は0.05モ
ル/l以下では効率が低すぎ、2.0モル/l以上では操作が
極めて困難となり、0.05〜2.0モル/l内が実際的な濃度
範囲であり0.2〜1.0モル/lがより好ましい濃度範囲であ
る。ジルコニウムの塩水溶液をpH1〜3に調製すること
により、以下に述べるが加水分解反応がpHを調製しない
時と比較して更に促進される効果がある。In the method of the present invention, the concentration of the zirconium salt solution is too low at 0.05 mol / l or less, the operation becomes extremely difficult at 2.0 mol / l or more, and the practical concentration range of 0.05 to 2.0 mol / l is 0.2 to 1.0 mol / l is a more preferable concentration range. By adjusting the pH of the zirconium salt aqueous solution to 1 to 3, the hydrolysis reaction is further promoted as compared with the case where the pH is not adjusted, as described below.
加水分解による結晶質ジルコニア生成のさらに詳細な進
行状況を種々な条件に対し比較して第1図に示す。A more detailed progress of the formation of crystalline zirconia by hydrolysis is shown in FIG. 1 in comparison with various conditions.
第1図は0.2モル/lの濃度の塩化ジルコニル水溶液300cc
を還流冷却器付フラスコ中で煮沸し続けた場合の時間的
変化を示し、横軸は煮沸時間、縦軸は溶液中の全ジルコ
ニウム量に対する生成単斜ジルコニア微粒子の量のモル
比である。Figure 1 shows 300cc of 0.2 mol / l zirconyl chloride aqueous solution.
Shows the change over time when boiling was continued in a flask with a reflux condenser, the horizontal axis represents the boiling time, and the vertical axis represents the molar ratio of the amount of monoclinic zirconia fine particles produced to the total amount of zirconium in the solution.
この分析方法は先に述べた方法で行った。また図中各曲
線に付された数字は出発時(煮沸前)の溶液の条件を示
し、陰イオン交換樹脂で調製された溶液のpH値および過
酸化水素水(31%)の添加量(cc)である。This analysis method was performed by the method described above. The numbers attached to each curve in the figure indicate the conditions of the solution at the time of starting (before boiling). The pH value of the solution prepared with anion exchange resin and the amount of hydrogen peroxide solution (31%) added (cc ).
図から明らかなように、従来の方法(図の黒丸)の単に
塩化ジルコニニル水溶液を加熱処理だけする場合には、
ジルコニア微粒子の生成反応を完了させるのに60時間の
長時間の連続煮沸が必要となるが、本発明方法(図の白
丸)である過酸化水素添加(0.2M,H2O2−10)によって
顕著な反応促進効果が認められ、さらにpHを陰イオン交
換樹脂で2.0とし、且つ過酸化水素を添加することによ
って(0.2M,pH2,H2O2−10)生成反応完了までの時間は
約1/3程度に短縮されることが分かる。As is clear from the figure, when the conventional method (black circle in the figure) simply heat-treats the zirconinyl chloride aqueous solution,
A continuous boiling for 60 hours for a long time is required to complete the reaction of forming the zirconia fine particles, but by the method of the present invention (white circles in the figure), hydrogen peroxide addition (0.2 M, H 2 O 2 -10) is used. observed remarkable reaction promotion effect, further with a pH of 2.0 with an anion exchange resin, and (0.2M, pH2, H 2 O 2 -10) by the addition of hydrogen peroxide time to produce the reaction completion about You can see that it is shortened to about 1/3.
次ぎに示す表は第1図と同様の実験において添加する過
酸化水素の量と20時間煮沸後の単斜結晶ジルコニア微粒
子生成量を比較したものであり少量の過酸化水素添加で
も既に明瞭な反応促進効果が認められるが、溶液中ジル
コニウムのモル数に対して等モル比(1:1)の過酸化水
素の添加の場合に最大の促進効果が現れ、約1/2モル比
以上が実際的であることを示す。また溶液中に過酸化水
素を生成する過酸化ソーダ、過酸化マグネシウム等も過
酸化水素と同様の促進効果を与える。The following table compares the amount of hydrogen peroxide added in the same experiment as in Fig. 1 and the amount of monoclinic crystal zirconia fine particles produced after boiling for 20 hours. Although an accelerating effect is observed, the maximum accelerating effect appears when hydrogen peroxide is added at an equimolar ratio (1: 1) to the number of moles of zirconium in the solution. Is shown. Further, sodium peroxide, magnesium peroxide, and the like that generate hydrogen peroxide in the solution also have the same promoting effect as hydrogen peroxide.
さらに第2図は塩化ジルコニルの濃度の高い場合での本
発明の効果を示したので、溶液のpH調製にアンモニア水
を加えた例である。第1図と同様、図中に溶液300ccに
対するアンモニア水(28%)の溶液(cc)を示した。水
溶液中の塩化ジルコニルの濃度が高くなると本発明の効
果は一層顕著であり、単に溶液を煮沸しただけでは0.5
モル/lでは40時間以上で始めて僅かにジルコニアが生成
し始め、0.8モル/l以上の濃度のものではジルコニアは
全く生成しないが、過酸化水素とアンモニアの添加によ
って高濃度溶液からでも比較的短時間に単斜結晶ジルコ
ニア超微粒子が生成する。図は溶液中に含有するジルコ
ニウム量と生成結晶化するジルコニアのモル比であるか
ら、高濃度のものが如何に高能率となるかが分る。 Further, FIG. 2 shows the effect of the present invention when the concentration of zirconyl chloride is high, and is an example in which aqueous ammonia is added to adjust the pH of the solution. Similar to FIG. 1, a solution (cc) of ammonia water (28%) to 300 cc of the solution is shown in the figure. The effect of the present invention is more remarkable when the concentration of zirconyl chloride in the aqueous solution is high, and it is 0.5 when the solution is simply boiled.
At mol / l, zirconia started to form slightly after 40 hours, and at a concentration of 0.8 mol / l or higher, zirconia did not form at all, but the addition of hydrogen peroxide and ammonia resulted in a relatively short time even from a high-concentration solution. Monoclinic crystal zirconia ultrafine particles are generated in time. The figure shows the molar ratio between the amount of zirconium contained in the solution and the zirconia that is formed and crystallized, so it can be seen how high the concentration of zirconia is.
本発明方法における加熱処理は必ずしも煮沸を要しな
い。本発明は100℃以下でも効果がありまた加圧雰囲気
下の高温処理でも同様の効果を示す。この実際的な処理
温度範囲は生成速度および装置などから80〜300℃であ
る。第3図は100℃以上での本発明の効果を示すもの
で、0.2モル/lの塩化ジルコニル溶液を水蒸気加圧下で1
30℃に保持した結果である。この場合にも予め過酸化水
素を添加後1時間煮沸した透明液は無添加溶液に比べ倍
以上の生成速度を示す。The heat treatment in the method of the present invention does not necessarily require boiling. The present invention is effective even at a temperature of 100 ° C. or lower, and exhibits similar effects even at high temperature treatment under a pressurized atmosphere. This practical processing temperature range is 80 to 300 ° C depending on the production rate and equipment. FIG. 3 shows the effect of the present invention at 100 ° C. or higher, in which a 0.2 mol / l zirconyl chloride solution was used under steam pressurization.
This is the result of holding at 30 ° C. In this case as well, the transparent liquid which had been boiled for 1 hour after the addition of hydrogen peroxide had a production rate more than double that of the non-added solution.
本発明により生成する単斜結晶ジルコニア超微粒子は粉
末X線回折のピークの半値幅から求めた結晶子径がすべ
て30〜100Åで、唯単に溶液を煮沸処理または低温で水
熱処理した場合とほとんど同じであるが、電子顕微鏡観
察によればその2次凝集粒子の大きさには顕著な差異が
ある。すなわち通常はジルコニア生成反応の完了時に2
次凝集粒子の径は1000Å以上となりこれは容易に分割さ
れない強固な結合をなすが、本発明方法による2次凝集
粒子は反応完了時でも500Å以下の径のものである。The monoclinic crystal zirconia ultrafine particles produced according to the present invention have crystallite diameters of all 30 to 100Å obtained from the half width of the peak of powder X-ray diffraction, which is almost the same as when the solution is simply boiled or hydrothermally treated at a low temperature. However, there is a marked difference in the size of the secondary agglomerated particles according to the electron microscope observation. That is, usually 2 at the completion of the zirconia formation reaction.
The diameter of the secondary agglomerated particles is 1000 Å or more, which is a strong bond that is not easily divided, but the secondary agglomerated particles according to the method of the present invention have a diameter of 500 Å or less even when the reaction is completed.
本発明で過酸化水素の作用の本質は必ずしも明らかでは
ないが、生成するジルコニアの2次凝集粒子の微細化に
は不可欠であり、従って過酸化水素は結晶成長よりもむ
しろ結晶核生成に効果があると考えられる。Although the essence of the action of hydrogen peroxide in the present invention is not always clear, it is indispensable for refining the secondary agglomerated particles of zirconia to be produced, and therefore hydrogen peroxide is effective for crystal nucleation rather than crystal growth. It is believed that there is.
またアンモニア等によるpH調製は2次凝集微粒子の微細
化に直接的に役立たないから核生成よりもむしろ結晶成
長促進に効果があると考えられる。何れにしても、本発
明方法は単斜結晶ジルコニア微粒子の生成を高効率化
し、生成物を超微細化する。すなわち、単斜結晶ジルコ
ニア超微粒子の工業的大量生産を可能にするとともに、
超微粒子化によってその応用製品を高品位化するもので
ある。Further, it is considered that the pH adjustment with ammonia or the like does not directly contribute to the miniaturization of the secondary agglomerated fine particles, so that it is effective in promoting crystal growth rather than nucleation. In any case, the method of the present invention makes the production of monoclinic zirconia fine particles highly efficient and makes the product ultrafine. That is, while enabling industrial mass production of monoclinic crystal zirconia ultrafine particles,
By applying ultrafine particles, the quality of the applied products will be improved.
本発明方法で得たゾルにアンモニア等の塩基を加え懸濁
粒子を凝集沈降させ、分離後アルコール、アセトン等の
極性溶媒で水分を置換し乾燥すれば、結晶質ジルコニア
の孤立した超微粒子からなる微粉末が得られるが、これ
は従来得られた如何なるジルコニア粉末よりも易焼結性
であり、特異である。例えばこの粉末成形物は1100℃の
低温ではほとんど理論密度の単斜結晶のみからなる高純
度ジルコニア焼結体を与える。これは従来ホットプレス
あるいは水熱下の特殊な方法でしか得られていないもの
である。また本発明方法のゾルより得られる粉末は2次
凝集粒子が極めて超微細なため、他の粉末との混合性に
優れ、ジルコン酸鉛の製造等固体反応用原料として使用
すれば接触面積の増大の結果著しく高反応性、低温焼結
性であり、その他のセラミック用添加剤として最も高分
散性であり、微量の均一な添加が可能となる。When a base such as ammonia is added to the sol obtained by the method of the present invention, suspended particles are aggregated and precipitated, and after separation, water is replaced with a polar solvent such as alcohol and acetone and dried to form isolated ultrafine particles of crystalline zirconia. A fine powder is obtained, which is more sinterable and unique than any previously obtained zirconia powder. For example, this powder compact gives a high-purity zirconia sintered body consisting of only monoclinic crystals of almost theoretical density at a low temperature of 1100 ° C. This is conventionally obtained only by a hot press or a special method under hydrothermal conditions. In addition, the powder obtained from the sol of the method of the present invention has extremely fine secondary agglomerated particles, and therefore has excellent miscibility with other powders, and when used as a raw material for solid reaction such as the production of lead zirconate, the contact area increases. As a result, it has extremely high reactivity and low-temperature sinterability, has the highest dispersibility as other additives for ceramics, and enables a small amount of uniform addition.
第1図、第2図、第3図および表は本発明方法が従来法
に比べて、結晶質ジルコニア微粒子の生成速度、効率が
非常に優れていることが示す実施例であるが、更に以下
に本発明の結晶質ジルコニアの微粉末について具体的な
実施例を示す。FIGS. 1, 2, 3 and Table are examples showing that the method of the present invention is much superior in production rate and efficiency of crystalline zirconia fine particles to the conventional method. Specific examples of the crystalline zirconia fine powder of the present invention are shown in FIG.
実施例1 特級試薬塩化ジルコニル(ZrOCl28H2O)97gを蒸留水約300
ccに溶解して約1.0モル/lの溶液とし、これに過酸化水
素水(31%)を90cc加えて攪拌し、さらにアンモニア水
(28%)30ccを徐々に加え、この溶液を還流冷却器付フ
ラスコ中で50時間煮沸して半透明乳濁のゾルを得た。こ
のゾルにアンモニア水を加えると懸濁粒子は凝集沈降す
るので、デカンテーションし、水をアセトンで置換し、
濾過、乾燥させた。この粉末の1次粒子の結晶子径は粉
末X線回折の半価幅から計算すれば44Åの超微細なもの
であり、また光学顕微鏡および電子顕微鏡の観察によれ
ば、比較的おおきな凝集粒子は単に物理的な付着に近い
壊れ易いものであり、強固な2次凝集粒子の大きさは50
0Å以下でかつ、粒径がほぼ均一であることが認められ
る。この粉末は乾燥したものをそのまま金型中2t/cm2
の成形圧で直径16mmの円板に成形後空気中で1100℃に1
時間焼成しただけで、理論密度の96%のかさ密度の単斜
結晶のみからなる高純度緻密な多結晶体を与えた。Example 1 97 g of a special grade reagent zirconyl chloride (ZrOCl 2 8H 2 O) was distilled in about 300 parts.
Dissolve it in cc to make a solution of about 1.0 mol / l, add 90 cc of hydrogen peroxide solution (31%) and stir it, then gradually add 30 cc of ammonia water (28%), and add this solution to a reflux condenser. It was boiled for 50 hours in an attached flask to obtain a semitransparent emulsion sol. When ammonia water is added to this sol, suspended particles aggregate and settle, so decant and replace water with acetone.
It was filtered and dried. The crystallite size of the primary particles of this powder is 44 Å as calculated from the half-width of powder X-ray diffraction, and according to the observation with an optical microscope and an electron microscope, a relatively large agglomerated particle is found. The size of the strong secondary agglomerated particles is 50 because it is a fragile material that is close to physical adhesion.
It is recognized that the particle size is 0 Å or less and the particle size is almost uniform. This powder is a dried product as it is in the mold 2t / cm 2
After molding into a disc with a diameter of 16 mm by the molding pressure of 1 at 1100 ℃ in air
Only by firing for a long time, a highly pure and dense polycrystal composed of monoclinic crystals with a bulk density of 96% of the theoretical density was obtained.
第1図は本発明方法と従来方法における煮沸時間と単斜
ZrO2の生成率の変化を示す。 第2図はジルコニウム塩濃度を変えた時の本発明方法と
従来方法における煮沸時間と単斜ZrO2の生成率の変化を
示す。 第3図は水熱下での本発明方法と従来方法における煮沸
時間と単斜ZrO2の生成率の変化を示す。何れも白丸が本
発明方法で黒丸が従来方法である。FIG. 1 shows the boiling time and monoclinicity in the method of the present invention and the conventional method.
The change in the production rate of ZrO 2 is shown. FIG. 2 shows changes in boiling time and monoclinic ZrO 2 production rate in the method of the present invention and the conventional method when the zirconium salt concentration was changed. FIG. 3 shows changes in boiling time and monoclinic ZrO 2 production rate in the method of the present invention and the conventional method under hydrothermal conditions. In both cases, the white circles are the method of the present invention and the black circles are the conventional methods.
Claims (3)
径30〜100Åの単斜ジルコニアであり、その2次凝集粒
子が容易に分離しない強固なもので、その凝集粒子の平
均径が500Åを越えないことを特徴とする結晶質ジルコ
ニアの微粉末。1. Most of the zirconium contained is monoclinic zirconia having a crystallite size of 30 to 100Å, the secondary agglomerated particles are strong and do not easily separate, and the average diameter of the agglomerated particles does not exceed 500Å. A fine powder of crystalline zirconia characterized by the above.
水溶液に、過酸化水素または過酸化水素を生成する化合
物を加え、この溶液を80〜300℃に加熱処理して水溶液
中でジルコニアを単斜型に結晶化させ、結晶質ジルコニ
アのコロイドゾルを得、このゾルに塩基を加え凝集沈降
させ、凝集沈降物を分離後、極性有機溶媒で水分を置換
し乾燥することを特徴とする結晶質ジルコニアの微粉末
の製造方法。2. Zirconia is added to an aqueous solution of zirconium salt having a concentration of 0.05 to 2.0 mol / l by adding hydrogen peroxide or a compound that produces hydrogen peroxide to the solution and heat-treating the solution at 80 to 300 ° C. Monoclinic crystallization to obtain a crystalline zirconia colloidal sol, a base is added to this sol to cause coagulation and sedimentation, the coagulated sediment is separated, and then water is replaced with a polar organic solvent for drying. Method for producing fine powder of zirconia.
る特許請求の範囲第2項記載の結晶質ジルコニア微粉末
の製造方法。3. The method for producing fine crystalline zirconia powder according to claim 2, wherein the pH of the zirconium salt aqueous solution is 1 to 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60266830A JPH0764563B2 (en) | 1985-11-27 | 1985-11-27 | Fine powder of crystalline zirconia and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60266830A JPH0764563B2 (en) | 1985-11-27 | 1985-11-27 | Fine powder of crystalline zirconia and method for producing the same |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17769481A Division JPS5879818A (en) | 1981-11-05 | 1981-11-05 | Colloidal sol, fine powder of crystalline zirconia and preparation thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61141620A JPS61141620A (en) | 1986-06-28 |
| JPH0764563B2 true JPH0764563B2 (en) | 1995-07-12 |
Family
ID=17436242
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60266830A Expired - Lifetime JPH0764563B2 (en) | 1985-11-27 | 1985-11-27 | Fine powder of crystalline zirconia and method for producing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0764563B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2204573B (en) * | 1987-03-31 | 1991-03-27 | Shinagawa Refractories Co | Spinning solution for producing zirconia fibers. |
| JPS63242926A (en) * | 1987-03-31 | 1988-10-07 | Shinagawa Refract Co Ltd | Zirconium-containing aqueous solution and production thereof |
| AU3505400A (en) | 1999-10-28 | 2001-05-08 | 3M Innovative Properties Company | Dental materials with nano-sized silica particles |
| ES2190300B1 (en) * | 2000-02-04 | 2004-11-16 | Consejo Superior De Investigaciones Cientificas | PROCEDURE FOR OBTAINING NANOMETRIC POWDER OF CIRCONIOUS OXIDE WITH MODIFICATION OF ITS SPECIFIC SURFACE AND STABLE TETRAGONAL STRUCTURE. |
| US7393882B2 (en) | 2002-01-31 | 2008-07-01 | 3M Innovative Properties Company | Dental pastes, dental articles, and methods |
| JP5034314B2 (en) * | 2006-05-19 | 2012-09-26 | 住友大阪セメント株式会社 | High refractive index transparent particle manufacturing method, high refractive index transparent particle, high refractive index transparent composite, and light emitting device |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5615442A (en) * | 1979-07-18 | 1981-02-14 | Tsudakoma Ind Co Ltd | Fluid injection method of weft yarn |
-
1985
- 1985-11-27 JP JP60266830A patent/JPH0764563B2/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| 日本化学会誌、1976〔3〕村瀬、加藤、P.425−430 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61141620A (en) | 1986-06-28 |
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