JP2883522B2 - Method for producing rare earth oxide fine powder - Google Patents

Method for producing rare earth oxide fine powder

Info

Publication number
JP2883522B2
JP2883522B2 JP5218425A JP21842593A JP2883522B2 JP 2883522 B2 JP2883522 B2 JP 2883522B2 JP 5218425 A JP5218425 A JP 5218425A JP 21842593 A JP21842593 A JP 21842593A JP 2883522 B2 JP2883522 B2 JP 2883522B2
Authority
JP
Japan
Prior art keywords
rare earth
earth element
water
fine powder
surfactant
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
Application number
JP5218425A
Other languages
Japanese (ja)
Other versions
JPH0769624A (en
Inventor
正実 金吉
勇 藤岡
酒井  茂
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.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP5218425A priority Critical patent/JP2883522B2/en
Publication of JPH0769624A publication Critical patent/JPH0769624A/en
Application granted granted Critical
Publication of JP2883522B2 publication Critical patent/JP2883522B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

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、希土類元素焼結体の原
料および窒化硅素、窒化アルミニウム等のセラミックス
の焼結助剤として有用な凝集が無く分散性の良い希土類
元素酸化物微粉の製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a rare earth element oxide fine powder having no agglomeration and having good dispersibility useful as a raw material for a rare earth element sintered body and a sintering aid for ceramics such as silicon nitride and aluminum nitride. It is about.

【0002】[0002]

【従来の技術】従来、希土類元素酸化物の微粉は、希土
類元素の鉱酸塩水溶液に沈殿剤を添加して水不溶性の沈
殿を生成させ、これを濾別、水洗し、乾燥、焼成して製
造していた。しかし、乾燥、焼成時に凝集、凝結が起こ
り、焼成物は数mm程度の粒状物になってしまうため、焼
成後に解砕(多くの場合分散剤を用いる湿式粉砕をい
う)するが、解砕後でも凝集に起因する粗粒子が残って
おり、セラミックス原料としては好ましくないで解砕後
篩分け工程を必要とし、手間が掛かると共に、コスト高
と不純物混入の原因となる不利があった。
2. Description of the Related Art Conventionally, fine powders of rare earth element oxides are prepared by adding a precipitant to a rare earth element mineral salt aqueous solution to form a water-insoluble precipitate, which is separated by filtration, washed with water, dried and calcined. Had been manufactured. However, agglomeration and coagulation occur during drying and firing, and the fired material becomes granular matter of about several mm. Therefore, the material is crushed after firing (often wet grinding using a dispersant). However, coarse particles due to agglomeration remain, which is not preferable as a ceramic raw material, and requires a sieving step after crushing, which is troublesome, and has the disadvantages of high cost and impurity contamination.

【0003】[0003]

【発明が解決しようとする課題】本発明はかかる問題点
を解決したもので、焼成後に解砕を必要としない希土類
元素酸化物微粉の製造方法を提供しようとするものであ
る。
SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and an object of the present invention is to provide a method for producing a rare earth element oxide fine powder which does not require crushing after firing.

【0004】[0004]

【課題を解決するための手段】本発明者等は先の課題に
対して、希土類水不溶性塩類の晶出条件を検討した結
果、界面活性剤を共存させることにより乾燥、焼成時に
凝集がなく、解砕を必要としない希土類元素酸化物微粉
が得られることを見出し、諸条件を充分検討して、本発
明を完成させたもので、その要旨は、希土類元素の鉱酸
塩水溶液に、沈殿剤と共に界面活性剤を添加して希土類
元素の水不溶性塩を晶出させた後、または沈殿剤で希土
類元素の水不溶性塩を晶出させた後に界面活性剤を添加
混合した後、水不溶性塩を濾別し、必要に応じて水洗し
た後、焼成することを特徴とする希土類元素酸化物微粉
の製造方法にあり、希土類元素の水不溶性塩が希土類元
素蓚酸アンモニウム複塩NH4Re(C204)2・nH20 (ここにRe
は希土類元素、nは1以上である)、希土類元素水酸化
物または希土類元素炭酸塩である。
The present inventors have studied the crystallization conditions of the rare-earth water-insoluble salts with respect to the above-mentioned problems. As a result, by coexisting a surfactant, there is no aggregation during drying and firing, It has been found that a rare earth element oxide fine powder that does not require crushing can be obtained, and various conditions have been sufficiently studied to complete the present invention. The gist of the invention is that a rare earth element mineral salt aqueous solution is added with a precipitant. After adding a surfactant and crystallizing the water-insoluble salt of the rare earth element, or after crystallizing the water-insoluble salt of the rare earth element with the precipitant, adding and mixing the surfactant, the water-insoluble salt is removed. The method for producing a rare earth element oxide fine powder is characterized in that the rare earth element is finely filtered, washed with water as necessary, and then calcined, wherein the water-insoluble salt of the rare earth element is a rare earth element ammonium oxalate double salt NH 4 Re (C 20 4 ) 2・ nH 2 0 (here Re
Is a rare earth element, n is 1 or more), a rare earth element hydroxide or a rare earth element carbonate.

【0005】以下、本発明を詳細に説明する。本発明の
希土類元素酸化物微粉の製造方法の全工程は次のように
なる。原料として希土類元素酸化物を鉱酸に溶解して遊
離酸濃度 1.5モル/リットル以下、希土類元素濃度 0.1
〜 1.0モル/リットルに調整した溶液に、濃度1〜30重
量%で対希土類元素2〜 2.5倍モル量の蓚酸水溶液およ
び対蓚酸2〜4倍モル量の28重量%アンモニア水を撹拌
しながら混合する。鉱酸は塩酸、硝酸、硫酸等が例示さ
れるが、これらの内硝酸が好ましい。ここで溶液の添加
順序を特定する必要はない。また、アンモニウム蓚酸複
塩の生成は粉末X線回折により容易に確認できる。
Hereinafter, the present invention will be described in detail. All steps of the method for producing a rare earth element oxide fine powder of the present invention are as follows. As a raw material, a rare earth element oxide is dissolved in a mineral acid to obtain a free acid concentration of 1.5 mol / liter or less and a rare earth element concentration of 0.1 mol / L.
An aqueous solution of oxalic acid having a concentration of 1 to 30% by weight and an aqueous solution of oxalic acid having a concentration of 2 to 2.5 times the amount of a rare earth element and an aqueous solution having a concentration of 2 to 4 times the amount of oxalic acid and 28% by weight of ammonia water having a concentration of 1 to 30% by weight were mixed with the solution adjusted to 1.0 mol / L while stirring. I do. Examples of the mineral acid include hydrochloric acid, nitric acid, and sulfuric acid, and among these, nitric acid is preferable. Here, it is not necessary to specify the order of adding the solutions. Further, the formation of ammonium oxalate double salt can be easily confirmed by powder X-ray diffraction.

【0006】ここで本発明の最大の特徴は沈殿剤である
蓚酸アンモニウムまたは蓚酸とアンモニア水を添加する
のと同時に界面活性剤を添加し撹拌して、生成する希土
類元素蓚酸アンモニウム複塩の表面に界面活性剤を吸着
させて濾別し、必要に応じて水洗した後、乾燥、焼成す
る。或は、希土類元素蓚酸アンモニウム複塩の全量が晶
出した後、界面活性剤を添加し撹拌して生成した希土類
元素蓚酸アンモニウム複塩の表面に界面活性剤を吸着さ
せて濾別し、必要に応じて水洗した後、乾燥、焼成して
も良い。
The most important feature of the present invention is that a surfactant is added and stirred simultaneously with addition of ammonium oxalate or oxalic acid as a precipitant and aqueous ammonia to form a rare earth element ammonium oxalate double salt on the surface. The surfactant is adsorbed and separated by filtration, washed with water if necessary, dried and calcined. Alternatively, after the entire amount of the rare earth element ammonium oxalate double salt has been crystallized, the surfactant is added to the surface of the rare earth element ammonium oxalate double salt formed by stirring, and the surfactant is adsorbed and separated by filtration. After rinsing accordingly, drying and baking may be performed.

【0007】界面活性剤としては陽イオン性、陰イオン
性、非イオン性のいずれも使用することができるが、そ
の中でも特に陽イオン性の界面活性剤が効果的であり、
アセタミン24(花王(株)製商品名、アルキルアミン塩
系陽イオン性)、エマールAD-25R(花王(株)製商品
名、アルキル硫酸エステル塩系イオン性)、ノニポー
ル140 (三洋化成工業(株)製商品名、ポリオキシエチ
レン系非イオン性)等が例示される。添加量は界面活性
剤純分で全液量1リットル当たり0.01〜10g 、好ましくは0.
05〜5g が良い。0.01g/L 未満では添加効果が発現せ
ず、10g/L を越えてもより一層の効果は望めず不経済で
ある。濾別は常法によれば良く、水洗は必要に応じて実
施すれば良い。洗浄を終了した該希土類元素蓚酸複塩は
必要に応じて乾燥した後焼成する。焼成温度および時間
も重要な要因で、蓚酸複塩を完全に酸化物に交換するた
めには 800〜 1,000℃で1〜4時間とするのが良い。こ
のようにして得られる焼成物である希土類元素酸化物は
サラサラした流動性の良い粉末になり、解砕を必要とせ
ず、希土類元素酸化物焼結体の原料、窒化ケイ素、窒化
アルミニウム等の焼結助剤として取扱い上極めて有用で
ある。
As the surfactant, any of cationic, anionic and nonionic surfactants can be used. Among them, cationic surfactants are particularly effective.
Acetamine 24 (trade name, manufactured by Kao Corporation, alkylamine salt-based cationic), Emar AD-25R (trade name, manufactured by Kao Corporation, alkyl sulfate salt-based anionic ), Nonipol 140 (Sanyo Chemical Industries, Ltd.) (Trade name, polyoxyethylene-based nonionic), and the like. The addition amount is 0.01 to 10 g per liter of the total amount of the pure surfactant, preferably 0.1 g.
05 to 5g is good. If the amount is less than 0.01 g / L, the effect of addition is not exhibited, and if it exceeds 10 g / L, no further effect can be expected and it is uneconomical. The filtration may be performed by a conventional method, and the washing may be performed as needed. The washed rare earth element oxalate double salt is dried and fired if necessary. The firing temperature and time are also important factors, and it is preferable to set the temperature at 800 to 1,000 ° C. for 1 to 4 hours in order to completely replace the double oxalate with the oxide. The fired product of the rare-earth element oxide thus obtained is a smooth and fluid powder having no need to be crushed, and is used as a raw material for a rare-earth-element oxide sintered body, such as silicon nitride and aluminum nitride. It is extremely useful in handling as a binder.

【0008】[0008]

【作用】沈殿剤として蓚酸アンモニウムまたは蓚酸とア
ンモニア水を使用した場合に添加する界面活性剤の作用
は、界面活性剤が希土類元素蓚酸複塩の沈殿粒子の表面
に吸着し、乾燥段階での複塩同士の付着を防ぐことにあ
ると考えられる。希土類元素微粉の前躯体としては、希
土類元素アンモニウム複塩の他に、水酸化物、炭酸塩等
が用いられるが、これらについても界面活性剤の添加効
果は認められるが、アンモニウム蓚酸複塩の場合に効果
は最も顕著である。本発明における希土類元素の適用範
囲はYを含むLa、Ce、Pr、Nd、Sm、Eu、Gd、Tb、Dy、Ho、Er、Tm、Yb
およびLuから成る群から選択される1種または2種以上
の混合希土類元素酸化物である。
[Function] When ammonium oxalate or oxalic acid and ammonia water are used as the precipitant, the action of the surfactant added is such that the surfactant is adsorbed on the surface of the precipitated particles of the rare earth element oxalate double salt, and the surfactant is added in the drying stage. It is considered to be to prevent the adhesion of salts. As the precursor of the rare earth element fine powder, in addition to the rare earth element ammonium double salt, hydroxides, carbonates, etc. are used. The effect is most pronounced. The applicable range of the rare earth element in the present invention is La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb containing Y.
And one or more mixed rare earth element oxides selected from the group consisting of and Lu.

【0009】[0009]

【実施例】以下、本発明の実施態様を実施例を挙げて具
体的に説明するが、本発明はこれらに限定されるもので
はない。 (実施例1)酸化イットリウムを硝酸に溶解し、イット
リウム濃度0.7mol/L、遊離酸濃度0.3mol/Lの硝酸イット
リウム溶液を調整しておく。別に5Lビーカーに純水
2,900ml、蓚酸二水和物 214g及び28重量%アンモニア
水 268mlを仕込んで撹拌し、蓚酸アンモニウム水溶液を
調整する。次いでこの蓚酸アンモニウム溶液に、撹拌回
転数280rpmで撹拌しながら、液温15〜20℃に保って、先
に調整した硝酸イットリウム溶液 1,160mlを3分間で加
えて晶出させ、5分間撹拌を続けた後、アセタミン24
(花王(株)製陽イオン性界面活性剤商品名)を 4.5g
加えた。更に10分間撹拌を続けた後、ブフナー漏斗で濾
別し、純粋 4,500mlをふりかけ洗浄した。得られたケー
キを石英容器に移し、電気炉に入れて2時間かけて 900
℃まで昇温し、更に1時間 900℃に保って焼成した後放
冷した。焼成物を目開き 425μmのステンレス製の篩に
かけたところ、3分以内に全量が通過し、89.0gのサラ
サラした流動性の良い粉末が得られた。この粉末の粒度
分布をレーザー回折法(マイクロトラック)にて測定し
たところ 0.9μm以下に全体の50重量%、 2.3μm以下
に全体の90重量%が含まれ、 5.0μmを越える粗粒子は
検出されなかった。
EXAMPLES Hereinafter, embodiments of the present invention will be described specifically with reference to Examples, but the present invention is not limited thereto. (Example 1) Yttrium oxide is dissolved in nitric acid to prepare an yttrium nitrate solution having a yttrium concentration of 0.7 mol / L and a free acid concentration of 0.3 mol / L. Separately, pure water in a 5L beaker
2,900 ml, 214 g of oxalic acid dihydrate and 268 ml of 28% by weight ammonia water are charged and stirred to prepare an ammonium oxalate aqueous solution. Then, to this ammonium oxalate solution, while stirring at a stirring rotation speed of 280 rpm, the solution temperature was maintained at 15 to 20 ° C., 1,160 ml of the previously adjusted yttrium nitrate solution was added in 3 minutes to crystallize, and stirring was continued for 5 minutes. After that, acetamine 24
4.5 g of Kao Corporation's brand name of cationic surfactant
added. After stirring was further continued for 10 minutes, the mixture was filtered with a Buchner funnel and sprinkled with 4,500 ml of pure water for washing. The resulting cake was transferred to a quartz container and placed in an electric furnace for 2 hours.
The temperature was raised to 900.degree. C., and calcined at 900.degree. When the fired product was passed through a stainless steel sieve having an opening of 425 μm, the whole amount passed within 3 minutes, and 89.0 g of a smooth and flowable powder was obtained. When the particle size distribution of this powder was measured by laser diffraction method (Microtrac), 0.9% or less contained 50% by weight and 2.3% or less contained 90% by weight, and coarse particles exceeding 5.0μm were detected. Did not.

【0010】(実施例2)酸化エルビウムを出発原料と
して、実施例1と同じ条件でエルビウム蓚酸アンモニウ
ム複塩のケーキを得た。得られたケーキを実施例1と同
様に焼成、篩分けしたところ、3分以内に全量が通過
し、151.9gのサラサラした流動性の良い粉末が得られ
た。この粉末の粒度分布をレーザー回折法にて測定した
ところ 1.1μm以下に全体の50重量%、 2.6μm以下に
全体の重量90重量%が含まれ、 5.0μmを越える粗粒子
は検出されなかった。
Example 2 Using erbium oxide as a starting material, a cake of erbium ammonium oxalate double salt was obtained under the same conditions as in Example 1. When the obtained cake was baked and sieved in the same manner as in Example 1, the whole amount passed within 3 minutes, and 151.9 g of a smooth and flowable powder was obtained. When the particle size distribution of this powder was measured by a laser diffraction method, 1.1% or less contained 50% by weight of the whole, and 2.6% or less contained 90% by weight of the whole, and coarse particles exceeding 5.0m were not detected.

【0011】(実施例3)酸化イットリウムを出発原料
として、アセタミン24の代わりにエマールAD-25R(花王
(株)製陰イオン性界面活性剤商品名)を4.5g添加する
ことの他は実施例1と同じ条件でイットリウム蓚酸アン
モニウム複塩のケーキを得た。得られたケーキを実施例
1と同様に焼成、篩分けしたところ、3分以内に全量が
通過し、89.1g のサラサラした流動性の良い粉末が得ら
れた。この粉末の粒度分布をレーザー回折法にて測定し
たところ 1.1μm以下に全体の50重量%、 2.7μm以下
に全体の重量90重量%が含まれ、 5.0μmを越える粗粒
子は検出されなかった。
Example 3 Example 4 was repeated except that 4.5 g of Emal AD-25R (trade name of an anionic surfactant manufactured by Kao Corporation) was added instead of acetamine 24 using yttrium oxide as a starting material. Under the same conditions as in 1, a cake of double yttrium ammonium oxalate was obtained. When the obtained cake was baked and sieved in the same manner as in Example 1, the whole amount passed within 3 minutes, and 89.1 g of a smooth and flowable powder was obtained. When the particle size distribution of this powder was measured by a laser diffraction method, 1.1% or less contained 50% by weight of the whole and 2.7μm or less contained 90% by weight of the whole, and coarse particles exceeding 5.0μm were not detected.

【0012】(実施例4)酸化イットリウムを出発原料
として、アセタミン24の代わりにノニポール140(三洋
化成工業(株)製非イオン性界面活性剤商品名)を4.5g
添加することの他は実施例1と同じ条件でイットリウム
蓚酸アンモニウム複塩のケーキを得た。得られたケーキ
を実施例1と同様に焼成、篩分けしたところ、5分以内
に全量が通過し、89.0g のサラサラした流動性の良い粉
末が得られた。この粉末の粒度分布をレーザー回折法に
て測定したところ 1.0μm以下に全体の50重量%、 2.8
μm以下に全体の重量90重量%が含まれ、 5.0μmを越
える粗粒子は検出されなかった。
Example 4 Using yttrium oxide as a starting material, 4.5 g of Nonipol 140 (trade name of a nonionic surfactant manufactured by Sanyo Chemical Industries, Ltd.) instead of acetamine 24
A cake of ammonium yttrium oxalate double salt was obtained under the same conditions as in Example 1 except for the addition. When the obtained cake was baked and sieved in the same manner as in Example 1, the whole amount passed within 5 minutes, and 89.0 g of a smooth and flowable powder was obtained. The particle size distribution of this powder was measured by a laser diffraction method.
90% by weight of the total weight was contained below μm, and coarse particles exceeding 5.0 μm were not detected.

【0013】(実施例5)酸化イットリウムを出発原料
として、硝酸イットリウム溶液の蓚酸アンモニウム溶液
への添加に先立ってアセタミン24 4.5gを蓚酸アンモニ
ウム溶液に加えておき、沈殿生成後には界面活性剤を添
加しないことの他は実施例1と同じ条件でイットリウム
蓚酸アンモニウム複塩のケーキを得た。得られたケーキ
を実施例1と同様に焼成、篩分けしたところ、3分以内
に全量が通過し、88.8g のサラサラした流動性の良い粉
末が得られた。この粉末の粒度分布をレーザー回折法に
て測定したところ 0.8μm以下に全体の50重量%、 2.2
μm以下に全体の重量90重量%が含まれ、 5.0μmを越
える粗粒子は検出されなかった。
(Example 5) Using yttrium oxide as a starting material, acetamine 24 (4.5 g) was added to an ammonium oxalate solution before adding the yttrium nitrate solution to the ammonium oxalate solution, and a surfactant was added after precipitation. A cake of ammonium yttrium oxalate double salt was obtained under the same conditions as in Example 1 except that this was not performed. When the obtained cake was baked and sieved in the same manner as in Example 1, the whole amount passed within 3 minutes, and 88.8 g of a smooth and flowable powder was obtained. The particle size distribution of this powder was measured by a laser diffraction method.
90% by weight of the total weight was contained below μm, and coarse particles exceeding 5.0 μm were not detected.

【0014】(比較例1)実施例1と同じ条件で、イッ
トリウム蓚酸アンモニウム複塩の沈殿を生成させた。15
分間撹拌を続けた後、界面活性剤を添加することなくブ
フナー漏斗で濾別した。得られたケーキを実施例1と同
様に焼成、篩分けしたところ、60分までに75.7gが目開
き 425μmの篩を通過したが、なお12.9gが篩上に残っ
ており、篩を通過したものも肉眼で見える粗粒子で構成
されていた。 425μm篩を通過した粉末の粒度分布をレ
ーザー回折法にて測定したところ 3.2μm以下に全体の
50重量%、13.6μm以下に全体の90重量%が含まれ、10
μmを越える粒子は全体の22.5重量%もあり、用途によ
っては解砕、再篩分けを必要とするものであった。
Comparative Example 1 A precipitate of ammonium yttrium oxalate double salt was formed under the same conditions as in Example 1. Fifteen
After stirring for minutes, the mixture was filtered off on a Buchner funnel without adding a surfactant. The obtained cake was calcined and sieved in the same manner as in Example 1. By 60 minutes, 75.7 g passed through a sieve having an opening of 425 μm, but 12.9 g still remained on the sieve and passed through the sieve. The object was also composed of coarse particles visible to the naked eye. The particle size distribution of the powder passing through a 425 μm sieve was measured by laser diffraction method.
50% by weight, 13.6μm or less contains 90% by weight of the whole, 10%
Particles exceeding μm accounted for 22.5% by weight of the whole, and required crushing and re-sieving for some applications.

【0015】(比較例2)比較例1と同じ条件で、酸化
エルビウムからエルビウム蓚酸アンモニウム複塩のケー
キを得た。得られたケーキを実施例1と同様に焼成、篩
分けしたところ、60分までに 124.8gが篩を通過した
が、なお22.8gが篩上に残っており、篩を通過したもの
も肉眼で見える粗粒子で構成されていた。 425μm篩を
通過した粉末の粒度分布をレーザー回折法にて測定した
ところ 3.9μm以下に全体の50重量%、13.7μm以下に
全体の90重量%が含まれ、10μmを越える粒子は全体の
16.4重量%であった。
Comparative Example 2 Under the same conditions as in Comparative Example 1, a cake of erbium ammonium oxalate double salt was obtained from erbium oxide. When the obtained cake was baked and sieved in the same manner as in Example 1, 124.8 g passed through the sieve by 60 minutes, but 22.8 g still remained on the sieve. It consisted of visible coarse particles. The particle size distribution of the powder that passed through the 425 μm sieve was measured by laser diffraction method. 3.9 μm or less contained 50 wt% of the whole, 13.7 μm or less contained 90 wt% of the whole, and particles exceeding 10 μm
16.4% by weight.

【0016】[0016]

【発明の効果】本発明によれば、希土類元素焼結体の原
料およびセラミックスの焼成助剤として有用な凝集が無
く分散性の良い流動性に優れた希土類元素酸化物微粉を
簡便な工程で低コストで製造でき、産業上その利用価値
は極めて高い。
According to the present invention, a rare earth element oxide fine powder having no agglomeration and excellent dispersibility and excellent fluidity useful as a raw material for a rare earth element sintered body and a firing aid for ceramics can be reduced in a simple process. It can be manufactured at low cost, and its industrial value is extremely high.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平4−238813(JP,A) 特開 昭64−14142(JP,A) (58)調査した分野(Int.Cl.6,DB名) C01F 17/00 C04B 35/42 - 35/49 ────────────────────────────────────────────────── ─── Continuation of front page (56) References JP-A-4-238813 (JP, A) JP-A-64-14142 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C01F 17/00 C04B 35/42-35/49

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】希土類元素の鉱酸塩水溶液に、沈殿剤と共
に界面活性剤を添加して希土類元素の水不溶性塩を晶出
させた後、または沈殿剤で希土類元素の水不溶性塩を晶
出させた後に界面活性剤を添加混合した後、水不溶性塩
を濾別し、必要に応じて水洗した後、焼成することを特
徴とする希土類元素酸化物微粉の製造方法。
1. A water-insoluble salt of a rare earth element is crystallized by adding a surfactant together with a precipitant to an aqueous solution of a mineral salt of a rare earth element to crystallize a water-insoluble salt of the rare earth element. A method for producing a rare earth element oxide fine powder, which comprises adding a surfactant, mixing the resulting mixture, filtering out a water-insoluble salt, washing with water if necessary, and calcining.
【請求項2】希土類元素の水不溶性塩が希土類元素蓚酸
アンモニウム複塩NH4Re(C204)2・nH20 (ここにReは希土
類元素、nは1以上である)、希土類元素水酸化物また
は希土類元素炭酸塩である請求項1に記載の希土類元素
酸化物微粉の製造方法。
2. A water-insoluble salt of a rare earth element is a rare earth element ammonium oxalate double salt NH 4 Re (C 2 O 4 ) 2 .nH 2 0 (where Re is a rare earth element and n is 1 or more), a rare earth element The method for producing a rare earth element oxide fine powder according to claim 1, which is a hydroxide or a rare earth element carbonate.
JP5218425A 1993-09-02 1993-09-02 Method for producing rare earth oxide fine powder Expired - Lifetime JP2883522B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5218425A JP2883522B2 (en) 1993-09-02 1993-09-02 Method for producing rare earth oxide fine powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5218425A JP2883522B2 (en) 1993-09-02 1993-09-02 Method for producing rare earth oxide fine powder

Publications (2)

Publication Number Publication Date
JPH0769624A JPH0769624A (en) 1995-03-14
JP2883522B2 true JP2883522B2 (en) 1999-04-19

Family

ID=16719716

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5218425A Expired - Lifetime JP2883522B2 (en) 1993-09-02 1993-09-02 Method for producing rare earth oxide fine powder

Country Status (1)

Country Link
JP (1) JP2883522B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103482673A (en) * 2013-10-12 2014-01-01 瑞科稀土冶金及功能材料国家工程研究中心有限公司 Preparation method of rare earth hydroxide
CN104556191A (en) * 2013-10-18 2015-04-29 乔占印 Rare-earth polymeric aluminum barium chloride and production technology thereof
CN104211106B (en) * 2014-09-01 2016-08-24 赣州鑫隆康稀土有限公司 A kind of carbonated rare earth preparation method not producing ammonia nitrogen waste water

Also Published As

Publication number Publication date
JPH0769624A (en) 1995-03-14

Similar Documents

Publication Publication Date Title
US5938837A (en) Cerium oxide ultrafine particles and method for preparing the same
KR950003421B1 (en) Method for the production of mixed ammonium rare earth oxalates and their application to the production of rare earth oxides
KR101158985B1 (en) Process for producing perovskite compound powder
US5284809A (en) Method for the preparation of α-aluminum oxide powder
JP2868176B2 (en) Method for producing rare earth element oxide powder
JP2883522B2 (en) Method for producing rare earth oxide fine powder
JP2735157B2 (en) Method for producing ultrafine powder with suppressed aggregation
KR20010046015A (en) Manufacturig method of alumina powder
JP3877922B2 (en) Method for producing rare earth compound
JPH04310516A (en) Production of rare earth element oxide
JP3394071B2 (en) Method for producing rare earth oxide fine powder
JP3216160B2 (en) Method for producing perovskite-type composite oxide powder
JPH06127940A (en) Production of fine powder of rate earth element oxides
JP2790951B2 (en) Method for producing plate-like alumina particles
JPH07277710A (en) Production of perovskite-type multiple oxide powder
JP3350332B2 (en) Method for producing aggregated rare earth hydroxide
JPH0826833A (en) Production of ceramic raw material
JP2004083350A (en) Method for manufacturing rare earth oxide fine powder having 100 nm or less primary particle size, and rare earth oxide fine powder
JP2966724B2 (en) Method for producing rare earth hydroxide and spherical particles of rare earth oxide
JPH07109118A (en) Production of rare earth element oxide
JP3300576B2 (en) Method for producing spherical rare earth oxide
JPH1179742A (en) Production of yttria/gadolinia/europia coprecipitated single-dispersed spherical particles and yttria/gadolinia/ europia coprecipitated single-dispersed spherical particles obtained by same
JP2001270714A (en) Method for producing yag fine powder
JP3280689B2 (en) Method for producing round rare earth oxide
JP2786052B2 (en) Method for producing rare earth element oxide particles

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080205

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090205

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090205

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100205

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110205

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110205

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120205

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120205

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130205

Year of fee payment: 14

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140205

Year of fee payment: 15