JPH01230433A - Production of alumina-zirconia multiple powder - Google Patents
Production of alumina-zirconia multiple powderInfo
- Publication number
- JPH01230433A JPH01230433A JP63057143A JP5714388A JPH01230433A JP H01230433 A JPH01230433 A JP H01230433A JP 63057143 A JP63057143 A JP 63057143A JP 5714388 A JP5714388 A JP 5714388A JP H01230433 A JPH01230433 A JP H01230433A
- Authority
- JP
- Japan
- Prior art keywords
- alumina
- zirconia
- aqueous ammonia
- solution
- slurry
- 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 ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 239000000843 powder Substances 0.000 title claims abstract description 27
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000002245 particle Substances 0.000 claims abstract description 18
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 15
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000002002 slurry Substances 0.000 claims abstract description 12
- 239000012670 alkaline solution Substances 0.000 claims abstract description 9
- 239000000243 solution Substances 0.000 claims abstract description 9
- 238000001914 filtration Methods 0.000 claims abstract description 4
- 238000005406 washing Methods 0.000 claims abstract description 4
- 239000002131 composite material Substances 0.000 claims description 14
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims description 3
- 238000010298 pulverizing process Methods 0.000 claims 2
- 239000000725 suspension Substances 0.000 claims 1
- 239000002244 precipitate Substances 0.000 abstract description 10
- 239000012065 filter cake Substances 0.000 abstract description 3
- CMOAHYOGLLEOGO-UHFFFAOYSA-N oxozirconium;dihydrochloride Chemical compound Cl.Cl.[Zr]=O CMOAHYOGLLEOGO-UHFFFAOYSA-N 0.000 abstract description 3
- 150000002500 ions Chemical class 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract 3
- 150000003839 salts Chemical class 0.000 abstract 1
- 229910021512 zirconium (IV) hydroxide Inorganic materials 0.000 abstract 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 10
- 238000005452 bending Methods 0.000 description 6
- 239000010419 fine particle Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 5
- 239000012266 salt 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
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 150000003754 zirconium Chemical class 0.000 description 3
- FBOUIAKEJMZPQG-AWNIVKPZSA-N (1E)-1-(2,4-dichlorophenyl)-4,4-dimethyl-2-(1,2,4-triazol-1-yl)pent-1-en-3-ol Chemical compound C1=NC=NN1/C(C(O)C(C)(C)C)=C/C1=CC=C(Cl)C=C1Cl FBOUIAKEJMZPQG-AWNIVKPZSA-N 0.000 description 2
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 235000012501 ammonium carbonate Nutrition 0.000 description 2
- 239000001099 ammonium carbonate Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 235000019441 ethanol Nutrition 0.000 description 2
- 230000004580 weight loss Effects 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000006061 abrasive grain Substances 0.000 description 1
- 150000008043 acidic salts Chemical class 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- -1 chlorine ions Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- RCJVRSBWZCNNQT-UHFFFAOYSA-N dichloridooxygen Chemical compound ClOCl RCJVRSBWZCNNQT-UHFFFAOYSA-N 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G25/00—Compounds of zirconium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Compositions Of Oxide Ceramics (AREA)
- 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、アルミナ−ジルコニア複合粉体の製造方法に
関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for producing alumina-zirconia composite powder.
(従来の技術)
アルミナにジルコニアを添加すれば、アルミナ焼結体の
靭性を強化することは知られている。このジルコニアの
添加の方法としては、従来アルミナ粉体とジルコニア粉
体とを混合する方法が行なわれていた。ところが、アル
ミナの粒−rにしても、ジルコニアの粒子にしても粒径
が0.5μrrt以下の微粒子になれば、表面活性が大
きく、凝集体を作りやすい。特゛にジルコニア粒子はこ
の性質が顕著である。このため、アルミナ微粒子、ジル
コニア微粒子を均一に分散するには、これらの粒子の凝
集したアルミナ、ジルコニアを攪拌して十分に解砕する
必要がある。ところが、こ九らの凝集物は、分散されに
くく、種々の攪拌機、粉砕機で解砕されているが、いま
だ十分とは耳えない状態である。一方、アルミナ−ジル
コニアの硬度を高めるため、ジルコニアの添加量を少な
くしたほうがよい。この場合、ジルコニアを更に細かく
、均一に分散する必要があり、この均一分散性が問われ
る。このように、アルミナ−ジルコニア焼結体の製造方
法において、微粉ジルコニアの均一分散性が技術上の問
題としてクローズアップされている。本発明者等はこれ
らの点に鑑み、先に特願昭62−223588号でアル
ミニウム塩、ジルコニウムJJ(,74、及び尿素の水
溶液の))Hを3〜5の範囲で、−に昇さぜ、水酸化ア
ルミニウム粒子の周囲に水酸化ジルコ1ニウ11を晶析
する方法を発明し、出願した。(Prior Art) It is known that adding zirconia to alumina strengthens the toughness of an alumina sintered body. The conventional method for adding zirconia has been to mix alumina powder and zirconia powder. However, whether it is alumina particles-r or zirconia particles, if they are fine particles with a particle size of 0.5 .mu.rrt or less, they have a high surface activity and are likely to form aggregates. This property is particularly remarkable for zirconia particles. Therefore, in order to uniformly disperse alumina fine particles and zirconia fine particles, it is necessary to stir and sufficiently crush the aggregated alumina and zirconia particles. However, these aggregates are difficult to disperse, and although various types of stirrers and crushers have been used to crush them, the results are still not satisfactory. On the other hand, in order to increase the hardness of alumina-zirconia, it is better to reduce the amount of zirconia added. In this case, it is necessary to disperse zirconia more finely and uniformly, and this uniform dispersibility is questioned. As described above, in the method of manufacturing an alumina-zirconia sintered body, the uniform dispersibility of fine zirconia powder has been highlighted as a technical problem. In view of these points, the present inventors previously proposed in Japanese Patent Application No. 62-223588 that the aluminum salt, zirconium JJ (,74, and in an aqueous solution of urea))H was raised to - in the range of 3 to 5. Recently, we invented and filed an application for a method for crystallizing zirco-1-niu-11 hydroxide around aluminum hydroxide particles.
(発明が解決しようとする問題点)
ところが、この方法によって出来たアルミナ−ジルコニ
ア複合粉体は、成形、焼成しても相対密度が90%程度
に過ぎず、強度においてもいまだ十分とは唐゛えなかっ
た。(Problems to be Solved by the Invention) However, the alumina-zirconia composite powder produced by this method has a relative density of only about 90% even after being molded and fired, and its strength is still far from sufficient. I couldn't.
(問題点を解決するための手段)
本発明は、この水酸化ジルコニウ11品析によるアルミ
ナ−ジルコニア複合粉体の製造方法を改善したものであ
る。また、本発明の[1的は、アルミナ中に微粉のジル
コニア粒子を均一・に分散し、高強度に成形、焼結ij
f能にし11するアルミナ−ジルコニア複合粉体の製造
方法を提供することである。(Means for Solving the Problems) The present invention improves the method for producing alumina-zirconia composite powder by analyzing 11 zirconium hydroxide products. In addition, the first object of the present invention is to uniformly and uniformly disperse fine zirconia particles in alumina, and to form and sinter them to a high strength.
It is an object of the present invention to provide a method for producing an alumina-zirconia composite powder that has high functional properties.
つまり、微粉砕17たアルミナ粉体をジルコニウム塩溶
液に分散し、該溶液中にアルカリ溶液を添加してPHを
6〜10のスラリーとなし、該スラリーをろ過しで、ろ
滓をアンモニア水で洗浄してなるアルミナ−ジルコニア
複合粉体の製造方法である。That is, finely pulverized alumina powder is dispersed in a zirconium salt solution, an alkaline solution is added to the solution to make a slurry with a pH of 6 to 10, the slurry is filtered, and the filter residue is diluted with aqueous ammonia. This is a method for producing alumina-zirconia composite powder obtained by washing.
本発明において、ジル′:、lニウム溶液と(i、オキ
シ塩化ジルコニウム、塩化ジルコニラ11、硫酸ジルコ
ニラ11なと′の酸性塩溶液を八う。また、アルカリ溶
液としては、アンモニア水、炭酸アンーモニノ溶液、あ
るいはアンモニア水と炭酸アンモンの混合液を用いろ。In the present invention, a zil':, lium solution and an acidic salt solution of (i, zirconium oxychloride, zirconia chloride 11, zirconia sulfate 11, etc.) are used.Also, as the alkaline solution, ammonia water, an ammonium carbonate solution, etc. are used. Or use a mixture of aqueous ammonia and ammonium carbonate.
また、本発明において、アルカリ溶液を添加して1)1
1を6〜10にするその理由は、後述するように、l1
lrか6以1:であれば沈澱が一1分に微細化しないた
めであり、一方I’ IIか10以」−であればそれ以
−1−反応が進まず、アンモニア等のアルカリ溶液が無
駄になるからである。In addition, in the present invention, by adding an alkaline solution, 1) 1
The reason for changing 1 to 6 to 10 is that l1
If lr is 6 or more, this is because the precipitate does not become finer in 11 minutes, whereas if it is I' II or more than 10, the reaction does not proceed further, and an alkaline solution such as ammonia is Because it would be wasted.
(作用−)
ジルコニウム塩溶液の11’ I−Iは1−3で、酸性
である。このため、アルミナ粉体はジルコニウム塩溶液
の解こう作用により、凝集せず、微細なアルミナ粒(・
とじて溶液中に分散する。このアルミナ分1攻l容1皮
にアンモニア水等のアルカリ溶液を添加し、+Y 拌す
ると、■〕I■が一上昇し、4.5付近でアルミナ微粒
子の周囲に水酸化ジルコニウムが析出する。このとき、
水酸化ジルコニラ11はアルミナ微粒子を含み、水酸基
で連鎖状となった巨人分子で非゛常に粘性の高い沈澱と
なる。この連鎖状の沈澱にアルカリ溶液を虹に徐々に添
加し続け、I) I−Iを6〜10付近まで上昇させる
と、連鎖状の沈澱の水酸化ジルコニウムの水素結合が切
]し、攪拌することによって巨人沈澱がほぐれる。この
ようにして、水酸化ジルコニラ11の付着したアルミナ
粒子を分lid L f= i合液(アルミナ−ジルコ
ニア複合スラリー)が得られる。しかしながら、この時
点では、凝集性の強い水酸化ジルコニラ11は末だ残存
するので、ボー、ルミル粉砕、あるいは長時間攪拌する
ことが望ましい。ただし、この操作は後工程のろ渦形式
に、よって異なり、例えばフィルタープレス、遠心分離
を伴ったろ過等高密度のケーキがt1↑られる揚台はそ
の必要がない。このスラリーをろ過する。次に、ろ適役
のる滓をさらにアンモニア水で洗浄することにより、水
酸化ジルコニウムのf!集力はさらに弱めに)れる。こ
の時、等重点で凝集したアルミナ粒子も−・部分分散さ
れ、しかも沈澱内部に含まれる塩素イオンも迅速しこ効
率よくろ滓より洗浄除去される。(Function) 11' I-I of the zirconium salt solution is 1-3 and is acidic. Therefore, the alumina powder does not aggregate due to the peptizing action of the zirconium salt solution, and the fine alumina particles (
Seal and disperse in the solution. When an alkaline solution such as aqueous ammonia is added to one volume of this alumina and stirred at +Y, ■]I■ increases by one level, and zirconium hydroxide is precipitated around the alumina fine particles at around 4.5. At this time,
The hydroxide zirconia 11 contains alumina fine particles and is a giant molecule chained with hydroxyl groups, forming a very viscous precipitate. Continuing to gradually add an alkaline solution to this chain-like precipitate and raising I-I to around 6 to 10, the hydrogen bonds of zirconium hydroxide in the chain-like precipitate are broken] and stirred. This loosens the giant precipitate. In this way, the alumina particles to which the zirconia hydroxide 11 is attached are separated to obtain a liquid mixture (alumina-zirconia composite slurry). However, at this point, the highly cohesive zirconia hydroxide 11 still remains, so it is desirable to grind it by bowl, lumill, or stir it for a long time. However, this operation differs depending on the type of filtration and vortex used in the subsequent process, such as a filter press, filtration accompanied by centrifugation, etc., and there is no need for a platform on which a high-density cake can be produced at t1↑. Filter this slurry. Next, by further washing the slag with aqueous ammonia, f! concentration becomes even weaker). At this time, the alumina particles that have aggregated at equal points are also partially dispersed, and the chlorine ions contained within the precipitate are also quickly and efficiently washed away from the filter dregs.
(実施例) 次に本発明の実施例を述べる。(Example) Next, examples of the present invention will be described.
実施例」
平均粒径0 、 C; 7z mのアルミナ粉体G O
Ogをジルコニア換算で33%のオキシ塩化シルコニウ
t1溶液800 m L中に混ぜ、容量1.00Ont
1のボールミルで攪拌する。このようにして出来たアル
ミナ粒子分散溶液中に5規定のアンモニア水を加える。Example” Alumina powder GO with average particle size 0, C; 7z m
Og was mixed in 800 mL of 33% silconium oxychloride t1 solution in terms of zirconia, and the volume was 1.00 Ont.
Stir with a ball mill. 5N aqueous ammonia is added to the alumina particle dispersion solution thus prepared.
このアンモニア水の添加にともない、最初白く嵩高で、
怪5 m m程度の巨人な沈澱物が生じる。更に、アン
モニア水を徐々に添加するとI) Hが上昇するにつれ
、この巨大な沈澱物はほぐれ、水酸化ジルコニウム−ア
ルミナ粒子を分散した白濁のアルミナ−ジルコニア複合
スラリーとなる。With the addition of this ammonia water, it initially becomes white and bulky.
A huge precipitate about 5 mm in diameter is formed. Furthermore, when aqueous ammonia is gradually added, as I) H increases, this huge precipitate is loosened to form a cloudy alumina-zirconia composite slurry in which zirconium hydroxide-alumina particles are dispersed.
この人ラリ−をボールミルで粉砕してN 05 Cろ紙
でろ過し、ろ滓をろ液中に塩素、イオンが検出されない
程度までアンモニア水(0,2〜5規定)で洗浄する。This human rally is ground in a ball mill, filtered through N 05 C filter paper, and the filter cake is washed with aqueous ammonia (0.2 to 5 normal) until no chlorine or ions are detected in the filtrate.
この後メチルアルコール、あるいはエチルアルコールな
どのアルコールで洗浄して、分11女性の優れた粉体を
tl)る。洗汀Iされたろ滓を1」0°Cで1時間乾燥
し、その後600℃で仮焼する。出来たアルミナ−ジル
コニア塊状体に水と分散剤を加え、ボットミルで16時
間分散し、更に1 m mの小径ボールを加えて1時間
サンドミルにて分散し、乾燥してアルミナ−ジルコニア
複合粉体を作る。Thereafter, it is washed with alcohol such as methyl alcohol or ethyl alcohol to obtain a fine powder of 11 minutes. The washed filter cake is dried at 1'0°C for 1 hour, and then calcined at 600°C. Water and a dispersant were added to the resulting alumina-zirconia aggregates, and the mixture was dispersed in a bot mill for 16 hours.Additionally, small diameter balls of 1 mm were added and dispersed in a sand mill for 1 hour, and dried to form an alumina-zirconia composite powder. make.
出来たアルミナ−ジルコニア複合粉体をスプレードライ
ヤーにて0 、7 m m以下、水分8%造粒する。次
に、63 X G :3 X 6 m lTIの金型に
充填し、300 k K / (冒T12でプレス成形
し、その後1,1300kg/cm2で冷間等方圧縮で
更に加圧し、1550℃で焼成した。出来た焼結体の曲
げ強度、プラス1〜による摩耗試験、ビッカース硬度は
次の通り。なお比較のため、市販のアルミナ粉体のみを
同様に成形・焼成したもの、及びアルミナ粉体とジルコ
ニア粉体とを成型・焼成したものの測定値も表示した。The resulting alumina-zirconia composite powder is granulated with a spray dryer to a size of 0.7 mm or less and a moisture content of 8%. Next, it was filled into a 63 x G: 3 x 6 m TI mold, press-molded at 300 kK/(T12), then further pressurized by cold isostatic compression at 1,1300 kg/cm2, and then heated to 1550°C. The bending strength, wear test using +1~, and Vickers hardness of the resulting sintered body are as follows.For comparison, commercially available alumina powder alone was molded and fired in the same way, and alumina powder Measured values of the molded and fired body and zirconia powder are also shown.
曲げ強度 プラスト ビッカース
摩耗試験 硬度
の1l−(、lil:減
(kF/cm2m r/kg
夫五町 6060 18.3 1690アルミ
4620 22 、4 .1760すのみ
アルミ /1640 19.9 1700すとジ
ルコニ
ア粉体
なお表中、曲げ強度は、J]5l11601の試験法に
よる]0ザンブルでの平均値を示し、プラス1−1!f
l耗試験は平均100μmのアルミナ砥粒を試験体上か
ら真l:に試験体面に対し、45℃の角度をもつ9 、
1. m mのノスルより吹き付LE l 、 Ok
g/ cm 2で2分間吹きイ」げた時の単位試験体重
量当りの重量減で示した。Bending strength Plast Vickers abrasion test Hardness 1l-(, lil: reduction (kF/cm2m r/kg Fugocho 6060 18.3 1690 aluminum
4620 22, 4. 1760 Sumi Aluminum /1640 19.9 1700 Sumi Zirconia Powder In the table, the bending strength is the average value based on the test method of J]5l11601], plus 1-1! f
In the wear test, alumina abrasive grains with an average diameter of 100 μm were placed on the specimen at an angle of 45° with respect to the surface of the specimen.
1. Sprayed from the nostle of mm LE l, OK
It is expressed as the weight loss per unit test weight when blowing at g/cm2 for 2 minutes.
実施例2
実施例」ど同様に処理して出来たアルミナ−ジルコニア
複合粉体を実施例1と同様に造粒、成形し、l525°
Cで焼成した。出来た焼結体の測定値は次の通り。Example 2 Alumina-zirconia composite powder prepared in the same manner as in Example 1 was granulated and molded in the same manner as in Example 1.
It was fired at C. The measured values of the completed sintered body are as follows.
曲げ強度64.30 k g / c rn 2 ブ
ラストによるtp耗重重量減15 、3 m g /
k g ビッカース硬度17実施例3
実施例]−においてアルミナ粉体の粒径を0.3μIn
にし、実施例1と同様に処理したアルミナ−ジルコニア
複合粉体を実施例1と同様に造粒、成形、焼成した1、
出来たガC結体の曲げ強度は6750kg/aK、プラ
ス1〜による摩耗重ノI上減16.:3mg/kg
ビッカース硬度1790
実施例4
実施例1において、ジルコニアを5%含有するようにオ
キシ塩化ジルコニウムを調整してアルミナ−ジルコニア
複合粉体を作り、実施例、[と同様に造粒、成形、焼成
した。出来た焼結体の曲げ強度は6(54Okg /
a+f、プラス1−によるJ’ff耗虫ril:減1B
、1mg/kg ビッカース硬度」680
(効果)
以」二のように本発明は、微粉砕したアルミナ粒子をジ
ルコニラ11塩溶液に分散し、1核溶液中にアンモニア
水等のアルカリ溶液を添加してI)F■を6〜10に+
、昇させるため、生成する水酸化ジルコニラ11の巨人
沈澱をほぐしてスラリーとなる。また、このスラリーを
ろ過してろ滓をアンモニア水にて洗浄するため、ジルコ
ニアの微粒子は凝集することなくアルミナ粒1間に均一
に分散される。Bending strength: 64.30 kg/crn 2 TP weight loss due to blasting: 15.3 m g/crn
kg Vickers hardness 17 Example 3 The particle size of alumina powder was 0.3μIn in
Alumina-zirconia composite powder treated in the same manner as in Example 1 was granulated, molded, and fired in the same manner as in Example 1.
The bending strength of the resulting Ga-C assembly is 6,750 kg/aK, plus 1 to 16. :3mg/kg
Vickers hardness: 1790 Example 4 In Example 1, zirconium oxychloride was adjusted to contain 5% zirconia to produce an alumina-zirconia composite powder, and granulated, molded, and fired in the same manner as in Example. The bending strength of the completed sintered body is 6 (54Okg/
J'ff ril by a+f, plus 1-: decrease 1B
, 1mg/kg Vickers hardness: 680 I) F■ from 6 to 10+
In order to raise the temperature, the giant precipitate of zirconia hydroxide 11 that is generated is loosened to form a slurry. Further, since this slurry is filtered and the filter residue is washed with ammonia water, the zirconia fine particles are uniformly dispersed between the alumina grains 1 without agglomeration.
このように本発明によると、微粉のアルミナ−ジルコニ
ア複合粉体ができ、これを成形、焼成すれば、比較的低
温ても焼結できる。しかも、焼結体中には、アルミナ粒
間に均一にジルコニア粉が分散し、焼結体中のアルミナ
粒の粒成長を抑制でき、強度の大きな焼結体を得ること
が出来る。さらに本発明はジルコニアの微粒子を均一・
に分散しているため、ジルコニアの配合ハ(が極めて少
ない場合も、ジルコニア添加による靭性強化が発揮され
、アルミナージルコニアの理想的な焼結体を得ることが
出来る。As described above, according to the present invention, a fine alumina-zirconia composite powder is produced, and if this is shaped and fired, it can be sintered even at a relatively low temperature. Moreover, the zirconia powder is uniformly dispersed between the alumina grains in the sintered body, suppressing the grain growth of the alumina grains in the sintered body, and making it possible to obtain a sintered body with high strength. Furthermore, the present invention enables fine zirconia particles to be uniformly and
Even when the zirconia content is extremely small, toughness is enhanced by the addition of zirconia, making it possible to obtain an ideal sintered body of alumina-zirconia.
Claims (1)
該溶液中にアンモニア水等のアルカリ溶液を添加してP
Hを6〜10のスラリーとなし、該スラリー中の懸濁物
を粉砕、あるいは粉砕せずにろ過し、ろ滓をアンモニア
水にて洗浄してなるアルミナ−ジルコニア複合粉体の製
造方法Finely ground alumina particles are dispersed in a zirconium solution,
Adding an alkaline solution such as aqueous ammonia to the solution
A method for producing an alumina-zirconia composite powder by preparing H into a slurry of 6 to 10, pulverizing the suspension in the slurry or filtering it without pulverizing, and washing the filter residue with aqueous ammonia.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63057143A JPH01230433A (en) | 1988-03-09 | 1988-03-09 | Production of alumina-zirconia multiple powder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63057143A JPH01230433A (en) | 1988-03-09 | 1988-03-09 | Production of alumina-zirconia multiple powder |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01230433A true JPH01230433A (en) | 1989-09-13 |
Family
ID=13047352
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63057143A Pending JPH01230433A (en) | 1988-03-09 | 1988-03-09 | Production of alumina-zirconia multiple powder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01230433A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0396988A2 (en) * | 1989-05-12 | 1990-11-14 | Bayer Ag | Aluminium oxide powder having improved processing properties and process for producing |
-
1988
- 1988-03-09 JP JP63057143A patent/JPH01230433A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0396988A2 (en) * | 1989-05-12 | 1990-11-14 | Bayer Ag | Aluminium oxide powder having improved processing properties and process for producing |
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