JPH0651568B2 - Method for producing fine zirconium oxide powder - Google Patents
Method for producing fine zirconium oxide powderInfo
- Publication number
- JPH0651568B2 JPH0651568B2 JP60267277A JP26727785A JPH0651568B2 JP H0651568 B2 JPH0651568 B2 JP H0651568B2 JP 60267277 A JP60267277 A JP 60267277A JP 26727785 A JP26727785 A JP 26727785A JP H0651568 B2 JPH0651568 B2 JP H0651568B2
- Authority
- JP
- Japan
- Prior art keywords
- zirconium
- hydrogen peroxide
- zirconium oxide
- powder
- aqueous solution
- 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 - Lifetime
Links
- 239000000843 powder Substances 0.000 title claims description 27
- 238000004519 manufacturing process Methods 0.000 title claims description 16
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 title claims description 14
- 229910001928 zirconium oxide Inorganic materials 0.000 title claims description 14
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 48
- 239000007864 aqueous solution Substances 0.000 claims description 17
- 150000003839 salts Chemical class 0.000 claims description 11
- 229910052751 metal Inorganic materials 0.000 claims description 10
- GBNDTYKAOXLLID-UHFFFAOYSA-N zirconium(4+) ion Chemical compound [Zr+4] GBNDTYKAOXLLID-UHFFFAOYSA-N 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 150000003754 zirconium Chemical class 0.000 claims description 6
- 229910052791 calcium Inorganic materials 0.000 claims description 4
- 239000011575 calcium Substances 0.000 claims description 4
- 229910052749 magnesium Inorganic materials 0.000 claims description 4
- 239000011777 magnesium Substances 0.000 claims description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 3
- 238000000034 method Methods 0.000 description 24
- 239000002245 particle Substances 0.000 description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 9
- 239000007788 liquid Substances 0.000 description 8
- 239000003381 stabilizer Substances 0.000 description 8
- 239000006185 dispersion Substances 0.000 description 7
- 239000002994 raw material Substances 0.000 description 6
- 229910052726 zirconium Inorganic materials 0.000 description 6
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 5
- 239000002002 slurry Substances 0.000 description 5
- 239000000919 ceramic Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- IVORCBKUUYGUOL-UHFFFAOYSA-N 1-ethynyl-2,4-dimethoxybenzene Chemical compound COC1=CC=C(C#C)C(OC)=C1 IVORCBKUUYGUOL-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 238000001354 calcination Methods 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- CMOAHYOGLLEOGO-UHFFFAOYSA-N oxozirconium;dihydrochloride Chemical compound Cl.Cl.[Zr]=O CMOAHYOGLLEOGO-UHFFFAOYSA-N 0.000 description 3
- 239000011164 primary particle Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- 239000011882 ultra-fine particle Substances 0.000 description 3
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical compound [Cu+2].C1=CC(C(=C2C=CC([N-]2)=C(C=2C=CC=CC=2)C=2C=CC(N=2)=C(C=2C=CC=CC=2)C2=CC=C3[N-]2)C=2C=CC=CC=2)=NC1=C3C1=CC=CC=C1 RKTYLMNFRDHKIL-UHFFFAOYSA-N 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000005728 strengthening Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229910052727 yttrium Inorganic materials 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 229910020630 Co Ni Inorganic materials 0.000 description 1
- 229910002440 Co–Ni Inorganic materials 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-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
- 229910052769 Ytterbium Inorganic materials 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000004703 alkoxides Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 229910052863 mullite Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 150000003014 phosphoric acid esters Chemical class 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- SIXSYDAISGFNSX-UHFFFAOYSA-N scandium atom Chemical compound [Sc] SIXSYDAISGFNSX-UHFFFAOYSA-N 0.000 description 1
- 239000007784 solid electrolyte Substances 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- NAWDYIZEMPQZHO-UHFFFAOYSA-N ytterbium Chemical compound [Yb] NAWDYIZEMPQZHO-UHFFFAOYSA-N 0.000 description 1
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 description 1
- PCMOZDDGXKIOLL-UHFFFAOYSA-K yttrium chloride Chemical compound [Cl-].[Cl-].[Cl-].[Y+3] PCMOZDDGXKIOLL-UHFFFAOYSA-K 0.000 description 1
- -1 zirconium ions Chemical class 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明は、酸化ジルコニウムに、マグネシウム、カルシ
ウム及び3価以上の原子価を有する金属元素から選ばれ
た少なくとも1種の金属成分を固溶させてなる酸化ジル
コニウム系微粉末の製法に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial field of application> The present invention is to solid-dissolve zirconium oxide with at least one metal component selected from magnesium, calcium and metal elements having a valence of 3 or more. And a method for producing a zirconium oxide fine powder comprising
酸化ジルコニウム系微粉末は、自動車排ガス用や溶鉱炉
用の酸素センサーとするための固体電解質として、ある
いはAl2O3,Si3N4,SiC,MgO・Al2O3(スピネル)、3Al2
O3・2SiO2(ムライト)等のセラミック、Co-Ni系合金等
の金属に微細な正方晶型ZrO2粒子を分散させてなる高強
度かつ高靱性の分散強化セラミック、又は分散強化合金
などのセラミック原料として使用されている。Zirconium fine oxide powder, as a solid electrolyte for oxygen sensor for automotive exhaust gas for and blast furnaces, or Al 2 O 3, Si 3 N 4, SiC, MgO · Al 2 O 3 ( spinel), 3Al 2
For example, high strength and high toughness dispersion strengthened ceramics or dispersion strengthened alloys made by dispersing fine tetragonal ZrO 2 particles in a ceramic such as O 3・ 2SiO 2 (mullite) or a metal such as Co-Ni alloy Used as a ceramic raw material.
酸化ジルコニウム系粉末は、1次粒子の粒径が数百Å以
下の超微結晶であり、且つ強固な2次凝集粒子を形成し
ていないことが強く望まれているが、従来このような結
晶性超微粒子を生成させるのに多大な時間を要したり、
高価な原料若しくは装置を用いなければならなかつたり
するので、その製造コストが高く、需要の拡大が阻まれ
ている。It is strongly desired that the zirconium oxide-based powder is an ultrafine crystal having a primary particle size of several hundred Å or less and that it does not form strong secondary agglomerated particles. Takes a lot of time to generate the ultrafine particles of
Since expensive raw materials or equipment have to be used, the production cost is high and the expansion of demand is hindered.
<従来技術と問題点> 酸化ジルコニウム系微粉末の一般的な製法は、水溶性ジ
ルコニウム塩の水溶液とCa,Mg及びYなどの3価以上の
原子価を有する金属元素(安定化剤という)の少なくと
も1種を酸化物または塩などの可溶性化合物の形で加え
て溶解した水溶液との混合溶液を、アンモニア水等のア
ルカリで難溶性の水酸化物などとして沈殿させ、水洗・
乾燥後数百℃で仮焼熱分解するものである。しかし、こ
の方法では出発原料の塩が残り、また粗大で粒度分布の
広い2次凝集粒子しか得られず、機械的摩砕が不可欠で
あり、高純度を保つことが困難である。<Prior art and problems> A general method for producing a fine zirconium oxide powder is an aqueous solution of a water-soluble zirconium salt and a metal element having a valence of 3 or more such as Ca, Mg and Y (referred to as a stabilizer). A mixed solution with an aqueous solution in which at least one kind is added in the form of a soluble compound such as an oxide or a salt and dissolved is precipitated as a sparingly soluble hydroxide in an alkali such as ammonia water, and washed with water.
After drying, it undergoes calcination and thermal decomposition at several hundreds of degrees Celsius. However, in this method, the salt of the starting material remains, and only coarse secondary coagulated particles having a wide particle size distribution are obtained, mechanical grinding is essential, and it is difficult to maintain high purity.
近年前記製造方法の欠点である乾燥時並びに仮焼熱分解
時における粒子の粗大化と強固な2次凝集粒子の形成を
回避する方法等がいろいろ提案されている。たとえば、
ジルコニウム塩と安定化剤の塩との混合水溶液から得ら
れた沈殿スラリーを還流下100時間位煮沸してコロイ
ドゾルとした後、ベンゼン、シクロヘキサン、n−オク
チルアルコール等の有機溶媒を加え、加熱蒸留により脱
水、乾燥させ、得られたジルコニウム水酸化物の微粒子
を加熱分解する方法がある。(特開昭56-145118号公
報)。しかし、この方法は、前記説明からも明らかなよ
うに製造に長時間を要し、しかも有機溶媒を使用するた
め製造コストが高いので用途は限定されたものになつて
いる。In recent years, various methods have been proposed for avoiding coarsening of particles and formation of strong secondary agglomerated particles at the time of drying and at the time of calcination pyrolysis, which are disadvantages of the above-mentioned production method. For example,
A precipitation slurry obtained from a mixed aqueous solution of a zirconium salt and a stabilizer salt is boiled under reflux for about 100 hours to form a colloidal sol, and then an organic solvent such as benzene, cyclohexane, n-octyl alcohol is added, and the mixture is heated and distilled by heating. There is a method of dehydrating and drying, and thermally decomposing the obtained fine particles of zirconium hydroxide. (JP-A-56-145118). However, as is clear from the above description, this method requires a long time for production, and since the production cost is high because an organic solvent is used, its use is limited.
また、ジルコニウムと安定化剤の混合アルコキシド溶液
の加水分解によつて生成する非晶質ゾルを乾燥、仮焼す
る方法があるが、若干の粒子凝集は不可避であり、しか
も原料コストが著しく高い。Further, there is a method of drying and calcination of an amorphous sol produced by hydrolysis of a mixed alkoxide solution of zirconium and a stabilizer, but some agglomeration of particles is unavoidable and the raw material cost is extremely high.
さらには、結晶性の微粒子を溶液中で生成させる方法と
して、ジルコニウム塩と安定化剤の塩との混合水溶液を
常圧又は水熱加圧条件下で加熱処理する方法がある。常
圧法としては、ジルコニウム塩と安定化剤の塩との混合
水溶液(水酸化ジルコニウム沈殿が生成しないpH<2.0
の領域)に過酸化水素水を添加し、温度80〜300℃
に加熱処理する方法(特開昭58−79818号公報)
がある。Furthermore, as a method of producing crystalline fine particles in a solution, there is a method of heat-treating a mixed aqueous solution of a zirconium salt and a stabilizer salt under atmospheric pressure or hydrothermal pressure. As the atmospheric pressure method, a mixed aqueous solution of zirconium salt and a stabilizer salt (pH <2.0 at which zirconium hydroxide precipitates are not formed)
Hydrogen peroxide solution is added to the temperature range of 80 to 300 ° C.
Method of heat-treating (JP-A-58-79818)
There is.
しかし、この方法も実用的なZrO2微粒子の量を得るため
には数日間を要する。また、水熱加圧法は圧力容器を用
いるため設備コストが高く、実用的な方法ではない。However, this method also requires several days to obtain a practical amount of ZrO 2 particles. Further, the hydrothermal pressurization method is not a practical method because the equipment cost is high because a pressure vessel is used.
<問題点を解決するための手段> 本出願人は、前記公知の酸化ジルコニウム系粉末の製造
法の欠点を解消すべく、種々研究を重ねた結果、水酸化
ジルコニウムはpH12以上のアルカリ水溶液中で過酸化
水素と錯体を形成し溶解すること、またこのアルカリ水
溶液を加熱処理すると配位子の過酸化水素が徐々に分解
・脱離し、結晶のZrO2超微結晶粒子が存在しなくとも従
来法の結晶性酸化ジルコニウムの常圧析出法に比較して
短時間で結晶質ZrO2超微粒子が生成するという知見によ
り、すでに特願昭60−111179号にて結晶質酸化
ジルコニウム微粉末の製法を提出しているが、本発明
は、その技術を安定化剤を含む酸化ジルコニウム系粉末
の製法に適用しようとするものである。<Means for Solving Problems> The present applicant has conducted various studies in order to solve the drawbacks of the known method for producing a zirconium oxide-based powder, and as a result, zirconium hydroxide was found to be contained in an alkaline aqueous solution having a pH of 12 or more. When forming a complex with hydrogen peroxide and dissolving it, and heat-treating this alkaline aqueous solution, hydrogen peroxide of the ligand is gradually decomposed and desorbed, and the conventional method is used even if crystalline ZrO 2 ultrafine crystal particles do not exist. Based on the finding that crystalline ZrO 2 ultrafine particles are formed in a shorter time than the atmospheric pressure precipitation method of crystalline zirconium oxide, the method for producing crystalline zirconium oxide fine powder is already submitted in Japanese Patent Application No. 60-111179. However, the present invention intends to apply the technique to a method for producing a zirconium oxide-based powder containing a stabilizer.
すなわち、本発明は、マグネシウム、カルシウム及び3
価以上の原子価を有する金属元素から選ばれた少なくと
も1種の金属の塩とジルコニウムの塩とを含む水溶液を
pH12以上のアルカリ水溶液中で過酸化水素と反応させ
て水溶性のジルコニウムイオンの過酸化水素錯体を形成
させた後、温度80〜200℃で加熱処理することを特
徴とする酸化ジルコニウム系微粉末の製法である。That is, the present invention relates to magnesium, calcium and 3
An aqueous solution containing a salt of at least one metal selected from metal elements having a valence of at least one and a salt of zirconium
After reacting with hydrogen peroxide in an alkaline aqueous solution having a pH of 12 or more to form a water-soluble zirconium ion hydrogen peroxide complex, heat treatment is performed at a temperature of 80 to 200 ° C. It is a manufacturing method.
以下さらに本発明を詳しく説明する。The present invention will be described in more detail below.
本発明に用いる出発原料の塩としては、たとえば塩酸
塩、硝酸塩、硫酸塩、酢酸塩などがあげられる。3価以
上の原子価を有する金属元素としては、イツトリウム、
セリウム、イツテルビウム、スカンジウムなどがあげら
れる。また、安定化剤の量は、ZrO2に対して、MgOとCaO
については3〜15モル%、Y2O3などは2〜15モル%
の範囲が適切である。Examples of the salt of the starting material used in the present invention include hydrochloride, nitrate, sulfate, acetate and the like. As the metal element having a valence of 3 or more, yttrium,
Examples include cerium, ytterbium, and scandium. In addition, the amount of stabilizer is MgO and CaO with respect to ZrO 2 .
About 3 to 15 mol% and Y 2 O 3 etc. about 2 to 15 mol%.
Is appropriate.
次に、ジルコニウムの塩と安定化剤の塩を含んでなる混
合水溶液にアルカリ剤と過酸化水素を添加し、pH12以
上のアルカリ水溶液中で過酸化水素と反応させて水溶性
のジルコニウムイオンの過酸化水素錯体を形成させる。
アルカリ剤と過酸化水素の添加順序は分割添加などどの
ような方法であつてもよい。反応温度は、通常、常温で
行われる。混合水溶液中の金属成分濃度としては、特別
な制限はないが、実用上の見地から0.1〜1.0モル/程
度が適切である。Next, an alkaline agent and hydrogen peroxide are added to a mixed aqueous solution containing a zirconium salt and a stabilizer salt, and the mixture is reacted with hydrogen peroxide in an alkaline aqueous solution having a pH of 12 or more to dissolve the water-soluble zirconium ion. Form a hydrogen oxide complex.
The alkaline agent and hydrogen peroxide may be added in any order such as divided addition. The reaction temperature is usually room temperature. The metal component concentration in the mixed aqueous solution is not particularly limited, but from a practical point of view, it is suitable to be about 0.1 to 1.0 mol / min.
アルカリ剤としては、アンモニア水、NaOH,KOH等のい
ずれでもよいが、ジルコニウムイオンの過酸化水素錯体
となつて溶解し始める水素イオン濃度pH=12以上を容
易に達成できるもので、しかも酸化ジルコニウム系微粉
末を生成するに際し加熱処理を施すため揮発性でないも
のが望ましい。なお、この場合において、アルカリ濃度
を高めてたとえばpH≧13.5にすると、ジルコニウムイ
オンの過酸化水素錯体の分解、脱離速度が著しく遅くな
るので結晶性と分散性にすぐれた酸化ジルコニウム系微
粉末を製造することができる。しかも、溶質によるモル
沸点上昇効果も大きくとれるので、次の処理である過酸
化水素錯体の熱処理温度を高くすることができ、結晶性
と分散性をさらに向上させることができる。従つて、本
発明においては、アルカリ濃度を高めることは好ましい
ことである。As the alkaline agent, any of ammonia water, NaOH, KOH, etc. may be used, but it can easily achieve a hydrogen ion concentration of pH = 12 or more which starts to dissolve when it becomes a hydrogen peroxide complex of zirconium ion, and it is a zirconium oxide type. Since it is subjected to a heat treatment when producing a fine powder, it is desirable that it is not volatile. In this case, if the alkali concentration is increased to, for example, pH ≧ 13.5, the decomposition and desorption rate of the hydrogen peroxide complex of zirconium ion will be significantly slowed down, so that the zirconium oxide fine particles having excellent crystallinity and dispersibility will be obtained. A powder can be produced. Moreover, since the effect of increasing the molar boiling point by the solute can be taken large, the heat treatment temperature of the hydrogen peroxide complex which is the next treatment can be raised, and the crystallinity and dispersibility can be further improved. Therefore, in the present invention, it is preferable to increase the alkali concentration.
過酸化水素としては、過酸化水素水を用いるのが望まし
く、その添加量は、水溶性ジルコニウムイオンの過酸化
水素錯体を形成するために溶液中のジルコニウム量の当
モル以上とするのがよい。As the hydrogen peroxide, it is desirable to use hydrogen peroxide solution, and the addition amount thereof is preferably equal to or more than the equimolar amount of zirconium in the solution in order to form a hydrogen peroxide complex of water-soluble zirconium ions.
以上のようにして得られた過酸化水素錯体を次いで加熱
処理する。加熱処理温度としては、80〜200℃好ま
しくは90〜140℃である。80℃未満では、粉末の
析出に長大な時間を要し経済的にも実際的でなく、一
方、200℃をこえると反応時間は短縮されるが、装置
等固定設備費用が高くなるだけでなく生成粉末が粗大で
粒度が不均一となる。反応槽は、反応の均一性を高め得
られる粉末の均一化を図るために充分な攪拌を行なうこ
とが望ましい。尚、100℃を越える温度領域で製造す
る場合には、従来技術で述べたように水熱加圧の可能な
圧力容器(オートクレーブなど)を使用する。本発明の
方法では、温度条件が200℃以下で処理することが可
能であり、加圧条件下で製造する場合に使用する圧力容
器の材質、耐圧などの面で従来に比較して低価格な設備
で製造が可能である。The hydrogen peroxide complex obtained as described above is then heat treated. The heat treatment temperature is 80 to 200 ° C, preferably 90 to 140 ° C. If the temperature is lower than 80 ° C, it takes a long time to deposit the powder and it is not economically practical. On the other hand, if the temperature exceeds 200 ° C, the reaction time is shortened, but not only the fixed equipment cost such as equipment is increased. The produced powder is coarse and the particle size is not uniform. It is desirable that the reaction tank is sufficiently agitated in order to enhance the homogeneity of the reaction and to homogenize the obtained powder. When manufacturing in a temperature range exceeding 100 ° C., a pressure vessel (autoclave or the like) capable of hydrothermal pressurization is used as described in the prior art. In the method of the present invention, it is possible to process at a temperature condition of 200 ° C. or less, and the cost is lower than that of the conventional one in terms of the material of the pressure vessel used when manufacturing under pressure conditions, the pressure resistance and the like. It can be manufactured with equipment.
<実施例> 以下、実施例、比較例をあげてさらに説明する。<Examples> Hereinafter, examples and comparative examples will be further described.
実施例1 オキシ塩化ジルコニウム(ZrOCl2・8H2O)80gと、塩
化イツトリウム(YCl3・6H2O)6gを純水300mに
溶解し、これに水酸化ナトリウム水溶液(濃度0.5モル
/リツトル)を加え、攪拌しながら市販の過酸化水素濃
度31重量%の過酸化水素水70mを加えた。次い
で、濃度8モル/リットルの水酸化ナトリウム水溶液2
00mを加えて攪拌したところ、水溶性のジルコニウ
ムイオンの過酸化水素錯体を含む淡黄色の液体が得られ
た。この液体のpHを堀場製作所製のpHメーター(型式:
F−8L)を用いて測定した結果、pH12.8であっ
た。Example 1 zirconium oxychloride (ZrOCl 2 · 8H 2 O) 80g, chloride yttrium (YCl 3 · 6H 2 O) 6g was dissolved in pure water 300 meters, this aqueous solution of sodium hydroxide (concentration: 0.5 mol / liters) In addition, 70 m of commercially available hydrogen peroxide solution having a hydrogen peroxide concentration of 31% by weight was added with stirring. Then, an aqueous solution of sodium hydroxide having a concentration of 8 mol / liter 2
When 00 m was added and stirred, a pale yellow liquid containing a water-soluble zirconium ion hydrogen peroxide complex was obtained. The pH of this liquid is measured by Horiba's pH meter (model:
As a result of measurement using F-8L), the pH was 12.8.
これを還流下、温度95℃で3時間加熱処理して乳濁状
のスラリーを得た。これを純水にて洗浄ろ過した後温度
100℃で5時間乾燥した。得られた乾燥物をX線回折
した結果、正方晶系の酸化ジルコニウム微粉末であつ
た。This was heated under reflux at a temperature of 95 ° C. for 3 hours to obtain an emulsion slurry. This was washed with pure water, filtered, and dried at a temperature of 100 ° C. for 5 hours. As a result of X-ray diffraction of the obtained dried product, it was found to be tetragonal zirconium oxide fine powder.
この微粉末1gをリン酸エステル系の分散剤(商品名
「Emphos PS−21A」)を適量添加してなるエチルア
ルコール50mに加え市販の超音波洗浄器にて30分
間分散処理を施した。その分散状態を透過型電子顕微鏡
で観察した結果、1次粒子は200Å前後の超微粒子
で、大部分の粒子は0.1μm前後の集合体を形成してお
り、非常に分散性がよいものであつた。1 g of this fine powder was added to 50 m of ethyl alcohol prepared by adding an appropriate amount of a phosphoric acid ester-based dispersant (trade name "Emphos PS-21A") and subjected to a dispersion treatment for 30 minutes by a commercially available ultrasonic cleaner. As a result of observing the dispersion state with a transmission electron microscope, the primary particles are ultrafine particles of about 200 Å, and most of the particles form aggregates of about 0.1 μm, which shows that they have very good dispersibility. It was
比較例1 過酸化水素水を添加しない以外は実施例1と同様にして
反応させたところ、粘稠なスラリー沈殿粒子を含むが得
られた。この液体のpHを実施例1と同じ測定法で測定し
た結果、pH12.6であった。そのスラリーを還流下、
温度95℃で約10時間加熱処理した。その処理物を純
水にて洗浄濾過した後、温度100℃の熱風下5時間乾
燥させた。Comparative Example 1 When the reaction was carried out in the same manner as in Example 1 except that hydrogen peroxide solution was not added, viscous slurry containing precipitate particles was obtained. The pH of this liquid was measured by the same measuring method as in Example 1, and as a result, it was pH 12.6. Under reflux of the slurry,
Heat treatment was performed at a temperature of 95 ° C. for about 10 hours. The treated product was washed with pure water, filtered, and dried under hot air at a temperature of 100 ° C. for 5 hours.
得られた乾燥物をX線回折した結果、非晶質の粉末であ
つた。また、この粉末を実施例1と同様の方法で透過型
電子顕微鏡で観察したところ、1〜10μmの凝集粒子
であつた。As a result of X-ray diffraction of the obtained dried product, it was found to be an amorphous powder. When this powder was observed with a transmission electron microscope in the same manner as in Example 1, it was found to be aggregated particles of 1 to 10 μm.
実施例2 オキシ塩化ジルコニウム(ZrOCl2・8H2O)80gと塩化
マグネシウム(MgCl2・6H2O)5gを用いて実施例1と同
じ操作で水溶性のジルコニウムイオンの過酸化水素錯体
を含む淡黄色の液体を得た。この液体のpHを実施例1と
同じ測定法で測定した結果、pH12.7であった。以下
実施例1と同じ操作で微粉末を得た。得られた粉末特性
は実施例1同様に分散性の良好なものであつた。Example 2 Using 80 g of zirconium oxychloride (ZrOCl 2 .8H 2 O) and 5 g of magnesium chloride (MgCl 2 .6H 2 O), the same procedure as in Example 1 was repeated to obtain a water-soluble zirconium ion hydrogen peroxide complex. A yellow liquid was obtained. The pH of this liquid was measured by the same measuring method as in Example 1, and as a result, it was pH 12.7. Fine powder was obtained by the same procedure as in Example 1 below. The powder properties obtained were good in dispersibility as in Example 1.
実施例3 オキシ塩化ジルコニウム(ZrOCl2・8H2O)80gと炭酸
カルシウム2gを用いて実施例1と同じ操作で水溶性の
ジルコニウムイオンの過酸化水素錯体を含む淡黄色の液
体を得た。この液体のpHを実施例1と同じ測定法で測定
した結果、pH12.8であった。以下実施例1と同じ操
作で微粉末を得た。得られた粉末特性は実施例1同様に
分散性の良好なものであつた。Example 3 80 g of zirconium oxychloride (ZrOCl 2 .8H 2 O) and 2 g of calcium carbonate were used to obtain a pale yellow liquid containing a water-soluble zirconium ion hydrogen peroxide complex by the same procedure as in Example 1. The pH of this liquid was measured by the same measuring method as in Example 1, and as a result, it was pH 12.8. Fine powder was obtained by the same procedure as in Example 1 below. The powder properties obtained were good in dispersibility as in Example 1.
実施例4 実施例1の水溶性のジルコニウムイオンの過酸化水素錯
体を含む淡黄色の液体をオートクレーブ(高圧化学社
製)を用いて攪拌下140℃に保持しながら、2時間加熱
処理して酸化ジルコニウムの生成反応を進め乳濁状のス
ラリーを得た。これを純水にて洗浄濾過した後、温度10
0℃で5時間乾燥した。得られた粉末の特性は実施例1
と同様に分散性の良好なものであった。Example 4 The pale yellow liquid containing the hydrogen peroxide complex of the water-soluble zirconium ion of Example 1 was subjected to heat treatment for 2 hours while being kept at 140 ° C. under stirring using an autoclave (manufactured by High Pressure Chemical Co., Ltd.) for oxidation. The zirconium formation reaction was advanced to obtain an emulsion slurry. After washing and filtering with pure water,
It was dried at 0 ° C. for 5 hours. The characteristics of the obtained powder are shown in Example 1.
Similar to the above, the dispersibility was good.
<発明の効果> (1)本発明のように過酸化水素を作用させることによ
り、従来の常圧下又は水熱加圧下における加熱処理法と
比較して短時間(3時間以内)で粉末を製造することが
できる。<Effects of the Invention> (1) By reacting hydrogen peroxide as in the present invention, a powder is produced in a shorter time (within 3 hours) as compared with the conventional heat treatment method under normal pressure or under hydrothermal pressure. can do.
(2)本発明の製法は、極めて単純な単位操作から構成さ
れ、しかも、短時間で高収率が得られるため工業的大量
生産が可能であり、その経済的価値は著しく高い。すな
わち、原料塩水溶液、過酸化水素水、アルカリ剤を混合
し、加熱処理を施せばよい。また、1モル/以上の濃
厚溶液の処理も可能である。さらには、同一容器内です
べての操作を行なえばよく大量の処理が可能である。(2) The production method of the present invention comprises an extremely simple unit operation, and since a high yield can be obtained in a short time, industrial mass production is possible, and its economic value is extremely high. That is, the raw material salt aqueous solution, the hydrogen peroxide solution, and the alkaline agent may be mixed and heat-treated. It is also possible to treat a concentrated solution of 1 mol / or more. Furthermore, it is sufficient to perform all operations in the same container, and a large amount of processing can be performed.
(3)本発明の製法によつて得られた酸化ジルコニウム系
微粉末は、粒度が均一で、洗浄・脱水後加熱により乾燥
しても実質的に凝集のない1次粒子からなり、優れた分
散性と混合性を有する。従つて、分散強化セラミックス
及び分散強化合金用原料粉末として、さらには、高密度
焼結体製造用原料粉末として特に有用である。(3) The zirconium oxide-based fine powder obtained by the production method of the present invention has a uniform particle size and is composed of primary particles that do not substantially agglomerate even when dried by heating after washing / dehydrating, and have excellent dispersion. It has both sex and miscibility. Therefore, it is particularly useful as a raw material powder for dispersion strengthening ceramics and dispersion strengthening alloys, and further as a raw material powder for producing a high density sintered body.
フロントページの続き (72)発明者 嶋田 ▲禎▼之 新潟県西頚城郡青海町大字青海2209番地 電気化学工業株式会社青海工場内 審査官 中田 とし子 (56)参考文献 特開 昭59−35029(JP,A) 特開 昭58−79818(JP,A)Front page continuation (72) Inventor Shimada ▲ Sadayuki No. 2209 Aomi, Aomi-cho, Nishikubiki-gun, Niigata Prefecture Tokiko Nakata, Examiner, Aomi Plant, Denki Kagaku Kogyo Co., Ltd. (56) Reference JP-A-59-35029 A) JP-A-58-79818 (JP, A)
Claims (1)
原子価を有する金属元素から選ばれた少なくとも1種の
金属の塩とジルコニウムの塩とを含む水溶液に過酸化水
素を加え、PH12以上のアルカリ水溶液中で反応させて
水溶性のジルコニウムイオンの過酸化水素錯体を形成さ
せた後、温度80〜200℃で加熱処理することを特徴
とする酸化ジルコニウム系微粉末の製法。1. An alkaline aqueous solution having a pH of 12 or more by adding hydrogen peroxide to an aqueous solution containing a salt of at least one metal selected from magnesium, calcium and a metal element having a valence of 3 or more and a zirconium salt. A method for producing a zirconium oxide-based fine powder, which comprises reacting in water to form a water-soluble zirconium ion hydrogen peroxide complex and then heat-treating at a temperature of 80 to 200 ° C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60267277A JPH0651568B2 (en) | 1985-11-29 | 1985-11-29 | Method for producing fine zirconium oxide powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60267277A JPH0651568B2 (en) | 1985-11-29 | 1985-11-29 | Method for producing fine zirconium oxide powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62128924A JPS62128924A (en) | 1987-06-11 |
| JPH0651568B2 true JPH0651568B2 (en) | 1994-07-06 |
Family
ID=17442599
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60267277A Expired - Lifetime JPH0651568B2 (en) | 1985-11-29 | 1985-11-29 | Method for producing fine zirconium oxide powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0651568B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62212224A (en) * | 1986-03-14 | 1987-09-18 | Taiyo Yuden Co Ltd | Production of zirconia solid solution crystal fine powder |
| JP3250243B2 (en) * | 1991-12-24 | 2002-01-28 | 日産化学工業株式会社 | Method for producing zirconia-based sol |
| 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 |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5879818A (en) * | 1981-11-05 | 1983-05-13 | Etsuro Kato | Colloidal sol, fine powder of crystalline zirconia and preparation thereof |
| JPS5935029A (en) * | 1982-08-20 | 1984-02-25 | Etsuro Kato | Manufacturing method of zirconia fine powder |
-
1985
- 1985-11-29 JP JP60267277A patent/JPH0651568B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62128924A (en) | 1987-06-11 |
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