JP2890830B2 - Purification method of scandium oxide - Google Patents

Purification method of scandium oxide

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Publication number
JP2890830B2
JP2890830B2 JP2325747A JP32574790A JP2890830B2 JP 2890830 B2 JP2890830 B2 JP 2890830B2 JP 2325747 A JP2325747 A JP 2325747A JP 32574790 A JP32574790 A JP 32574790A JP 2890830 B2 JP2890830 B2 JP 2890830B2
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Japan
Prior art keywords
scandium
precipitate
solution
added
impurity metal
Prior art date
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JP2325747A
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Japanese (ja)
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JPH04198017A (en
Inventor
博 海野
英臣 斎藤
正治 石渡
悦治 木村
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Mitsubishi Materials Corp
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Mitsubishi Materials Corp
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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、酸化スカンジウムに含まれる不純物金属
(Fe、Al、Sn、Zr、Ti、Pb、Ca、Cu、Zn、Thの1種また
は2種以上を云う)を分離する酸化スカンジウムの精製
方法に関する。スカンジウム(Sc)は工業的に利用でき
る原料鉱石が殆どなく、工業的にはウラン浸出液、チタ
ン(Ti)スラグ、スズ(Sn)スラグ等から分離回収して
いる。ところが、上記原料中には前述の金属が含まれて
おり、スカンジウムを回収するにはこれらの金属を分離
する必要がある。本発明は分離効果が良く、回収効率の
高い酸化スカンジウムの精製方法を提供する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to one or two types of impurity metals (Fe, Al, Sn, Zr, Ti, Pb, Ca, Cu, Zn, Th) contained in scandium oxide. (See more than one species). Scandium (Sc) has almost no raw material ore that can be used industrially, and is industrially separated and recovered from uranium leachate, titanium (Ti) slag, tin (Sn) slag, and the like. However, the above-mentioned metals are contained in the above-mentioned raw materials, and it is necessary to separate these metals in order to recover scandium. The present invention provides a method for purifying scandium oxide having a good separation effect and high recovery efficiency.

[従来技術の問題点] スカンジウムイオンと共に前述の不純物金属イオンを
含有する水溶液から、上記不純物金属を分離する方法と
しては、従来、次の方法が知られている。
[Problems of the Prior Art] As a method for separating the impurity metal from an aqueous solution containing the above-mentioned impurity metal ion together with scandium ion, the following method has been conventionally known.

(イ)上記溶液にアンモニアまたは苛性ソーダ等のアル
カリを添加し、pH3〜4付近で加水分解させてAl,Sn,Zr,
Ti等の水酸化物を沈殿させる方法。
(A) Add an alkali such as ammonia or caustic soda to the above solution and hydrolyze it at around pH 3-4 to make Al, Sn, Zr,
A method of precipitating a hydroxide such as Ti.

(ロ)上記溶液に塩酸、硝酸酸性溶液とし、イオン交換
によってZr,Ti,Hf,Thを吸着時に分離する方法。
(B) A method in which hydrochloric acid and nitric acid are added to the above solution, and Zr, Ti, Hf, and Th are separated at the time of adsorption by ion exchange.

(ハ)上記溶液を塩酸、硝酸酸性溶液とし、上記(ロ)
とは異なるイオン交換樹脂を用い、イオン交換の吸着時
および溶離時に分離する方法。
(C) The above solution is made into an acidic solution of hydrochloric acid and nitric acid, and
Separation at the time of adsorption and elution of ion exchange using a different ion exchange resin.

(ニ)上記溶液を塩酸、硝酸酸性溶液とし、溶媒抽出に
よってZr,Ti,Hf,Thを分離する方法。
(D) A method in which the above solution is converted into an acidic solution of hydrochloric acid and nitric acid, and Zr, Ti, Hf, and Th are separated by solvent extraction.

(ホ)上記溶液を塩酸、硝酸酸性溶液とし、上記(ニ)
とは異なる溶媒を用い、溶媒抽出により分離する方法。
(E) The above solution is made into an acid solution of hydrochloric acid and nitric acid, and
Separation by solvent extraction using a different solvent.

ところが、上記各方法には各々次のような問題があ
る。例えば、上記(イ)〜(ホ)の各方法は、単独では
上記不純物金属を同時に分離できず、(イ)と(ロ)、
(イ)または(ハ)と(ニ)、(ホ)のように上記方法
を組み合わせて分離精製を行っており、スカンジウムか
ら上記不純物金属を同時に分離する有効な方法は知られ
ていなかった。
However, each of the above methods has the following problems. For example, each of the above methods (a) to (e) cannot separate the impurity metal alone at the same time, and the methods (a) and (b)
As described in (a) or (c), (d) and (e), the above methods are combined for separation and purification, and no effective method for simultaneously separating the impurity metal from scandium has been known.

[問題解決の知見] 本発明者等は、スカンジウムと上記不純物金属との沈
殿分離法による分離を試み、錯化剤を用いればpH9.5程
度のアルカリ性領域で、スカンジウムは錯体を形成する
が上記不純物金属は錯体を形成しないことに注目し、ア
ルカリ性溶液中でスカンジウムの錯体を形成させてこれ
を該アルカリ溶液に溶解させ、上記不純物金属の沈殿を
分離すれば、効果的かつ容易にスカンジウムと上記不純
物金属とを分離できることを見い出した。
[Knowledge of Problem Solving] The present inventors have attempted to separate scandium from the impurity metal by a precipitation separation method. When a complexing agent is used, scandium forms a complex in an alkaline region of about pH 9.5. Focusing on the fact that the impurity metal does not form a complex, a complex of scandium is formed in an alkaline solution, which is dissolved in the alkaline solution, and the precipitate of the impurity metal is separated effectively and easily. It has been found that it can be separated from impurity metals.

[発明の構成] 本発明は、上記不純物金属を含有する酸化スカンジウ
ムについて、以下の構成からなる精製方法を提供するも
のである。
[Constitution of the Invention] The present invention provides a method for purifying scandium oxide containing the above-mentioned impurity metal, having the following constitution.

(1)不純物金属(Fe、Al、Sn、Zr、Ti、Pb、Ca、Cu、
Zn、Thの1種または2種以上を云う)を含有する酸化ス
カンジウムを、塩酸または硝酸を用いてpH2以下で溶解
し、この溶解液に炭酸塩以外のアルカリを加えてpHを3
以上に調整してスカンジウムおよび不純物金属を水酸化
物として沈殿させ、この沈澱を含む溶液に炭酸塩化合物
を加えることによりアルカリ性下でスカンジウム錯体を
形成させて再溶解し、残留した不純物金属の沈澱を濾別
分離した後に、スカンジウム酸化物を回収することを特
徴とする酸化スカンジウムの精製方法。
(1) Impurity metals (Fe, Al, Sn, Zr, Ti, Pb, Ca, Cu,
Scandium oxide containing one or more of Zn and Th) is dissolved at a pH of 2 or less using hydrochloric acid or nitric acid, and an alkali other than carbonate is added to the solution to adjust the pH to 3 or less.
The scandium and the impurity metal were precipitated as hydroxides by adjusting as described above, and a carbonate compound was added to the solution containing the precipitate to form a scandium complex under alkalinity and redissolved, thereby precipitating the remaining impurity metal. A method for purifying scandium oxide, comprising recovering scandium oxide after separation by filtration.

(2)上記不純物金属の沈澱を濾別分離した後に、その
濾液に塩酸または硝酸を加えた後に蓚酸または蓚酸塩化
合物を添加して蓚酸スカンジウムを沈殿させ、この沈殿
を濾過回収し、焙焼してスカンジウム酸化物を回収する
請求項1の精製方法。
(2) After separating the precipitate of the impurity metal by filtration, hydrochloric acid or nitric acid is added to the filtrate, and then oxalic acid or an oxalate compound is added to precipitate scandium oxalate. The precipitate is collected by filtration and roasted. The purification method according to claim 1, wherein the scandium oxide is recovered by heating.

(3)炭酸塩化合物による錯体の形成を60℃以下で行う
請求項1または2の方法。
(3) The method according to claim 1 or 2, wherein the complex is formed by the carbonate compound at a temperature of 60 ° C or lower.

[発明の具体的な説明] 本発明の方法は、不純物金属を含有する酸化スカンジ
ウムの精製方法に関するものである。本精製方法におい
て、不純物金属とは、Fe、Al、Sn、Zr、Ti、Pb、Ca、C
u、Zn、Thの1種または2種以上を云う。以下、上記不
純物金属を含有する酸化スカンジウムの精製方法を具体
的に説明する。
[Detailed Description of the Invention] The method of the present invention relates to a method for purifying scandium oxide containing an impurity metal. In the present purification method, the impurity metals are Fe, Al, Sn, Zr, Ti, Pb, Ca, C
It refers to one or more of u, Zn, and Th. Hereinafter, a method for purifying scandium oxide containing the impurity metal will be specifically described.

上記不純物金属を含有する酸化スカンジウムを、加熱
しつつ塩酸または硝酸を用い、pH2以下で溶解する。液
のpHが2を超えると酸化スカンジウムの未溶解物が残る
ので好ましくない。該溶液にアンモニア水や苛性ソーダ
等のアルカリ物質を加え、pH3以上に調整してスカンジ
ウムおよび不純物金属の水酸化物沈殿を生成させる。液
のpHが3未満では水酸化スカンジウムの沈澱生成が十分
ではない。なお、液のpHが7を超えるとアルカリの消費
が多くなる。
The scandium oxide containing the impurity metal is dissolved at a pH of 2 or less using hydrochloric acid or nitric acid while heating. If the pH of the solution exceeds 2, undissolved scandium oxide remains, which is not preferable. An alkaline substance such as aqueous ammonia or caustic soda is added to the solution, and the pH is adjusted to 3 or more to form hydroxide precipitates of scandium and impurity metals. When the pH of the solution is less than 3, precipitation of scandium hydroxide is not sufficient. When the pH of the solution exceeds 7, the consumption of alkali increases.

これらスカンジウムおよび不純物金属の水酸化物沈澱
を含む溶液に、スカンジウム沈殿物の錯化剤として炭酸
塩化合物を加える。この炭酸塩化合物を加えることによ
りアルカリ性下でスカンジウム沈殿物は錯体を形成して
液中に再度溶解する。一方、上記不純物金属の水酸化物
沈澱または炭酸塩沈澱として残留する。従って、これを
濾過して上記沈殿物を分離することにより、スカンジウ
ムと上記不純物金属を分離することができる。
A carbonate compound as a complexing agent for the scandium precipitate is added to the solution containing the hydroxide precipitate of the scandium and the impurity metal. By adding this carbonate compound, the scandium precipitate forms a complex under alkalinity and dissolves again in the liquid. On the other hand, the impurity metal remains as a hydroxide precipitate or a carbonate precipitate. Therefore, by filtering this and separating the precipitate, scandium and the impurity metal can be separated.

錯化剤としては炭酸ナトリウム、炭酸カリウム、炭酸
アンモニウム等を用いるいことができる。後述の実施例
に示すように、これらの炭酸塩化合物を添加することに
より溶液はアルカリ性を示し、スカンジウム沈殿が錯化
して溶解する。この錯化剤は粉末あるいは溶液として添
加する。なお、液量を増加させないためには粉末で添加
するのが好ましい。また、これら錯化剤である炭酸塩化
合物を添加する際、液温は低温ほど好ましく、60℃以下
が適当であり、好ましくは室温で実施するのがよい。液
温がこれより高いと、スカンジウムの錯体生成能力が弱
まり、スカンジウムが一部沈澱のまま残るので好ましく
ない。
As a complexing agent, sodium carbonate, potassium carbonate, ammonium carbonate and the like can be used. As shown in Examples described later, the solution becomes alkaline by adding these carbonate compounds, and the scandium precipitate is complexed and dissolved. This complexing agent is added as a powder or a solution. In order to prevent the liquid volume from increasing, it is preferable to add the powder. In addition, when adding the carbonate compound as a complexing agent, the liquid temperature is preferably as low as possible, suitably at 60 ° C. or lower, and more preferably at room temperature. If the liquid temperature is higher than this, scandium complex formation ability is weakened, and part of scandium remains as a precipitate, which is not preferable.

以上のようにして上記不純物金属を分離したスカンジ
ウムを蓚酸塩沈澱として回収する。具体的には、固液分
離したスカンジウム溶液に塩酸または硝酸を加えてpHを
2程度ないし実施例1〜3に示すように0.8にし、これ
に蓚酸または蓚酸塩化合物を添加してスカンジウムを蓚
酸塩に転じて沈澱させる。この沈澱を濾過して回収す
る。なお、添加する蓚酸化合物としては蓚酸アンモニウ
ムが不純物を混入させない上で好ましい。
The scandium from which the impurity metal has been separated as described above is recovered as an oxalate precipitate. Specifically, hydrochloric acid or nitric acid is added to the solid-liquid separated scandium solution to adjust the pH to about 2 to 0.8 as shown in Examples 1 to 3, and oxalic acid or an oxalate compound is added thereto to convert the scandium to oxalate. Turn to precipitate. The precipitate is collected by filtration. As the oxalic acid compound to be added, ammonium oxalate is preferable since impurities are not mixed.

[実施例および比較例] 以下、本発明を実施例によって具体的に示す。Examples and Comparative Examples Hereinafter, the present invention will be specifically described with reference to Examples.

実施例1 表1に示す不純物を含有するpH0.8のスカンジウ塩酸
酸性溶液145mlに、市販特級アンモニア水16mlを加えてp
Hを6.5とした。これによりスカンジウムと上記不純物の
水酸化物沈澱を生成させた。この沈澱を含む溶液に炭酸
アンモニウム25gを粉末のまま添加して10分間撹拌し
た。このときの液のpHは10.4であった。これを濾過して
不純物を分離し、298mlの濾洗液を得た。これに市販特
級塩酸30mlを加えて液のpHを1.0に調整した。その後、
試薬特級蓚酸13gを粉末のまま添加して5分間攪拌し、
蓚酸スカンジウム沈澱を生成させた。この沈澱を濾過し
て得た蓚酸スカンジウムを700℃で焙焼し精製酸化スカ
ンジウム2.8gを得た。これを分析に供した。この分析結
果を表1に示した。表示する結果から、全ての不純物金
属が除去され精製されていることがわかる。なお、スカ
ンジウムの回収率は85%であった。
Example 1 To 145 ml of a scandium hydrochloride acid solution of pH 0.8 containing impurities shown in Table 1, 16 ml of commercially available special grade ammonia water was added, and p
H was set to 6.5. This produced a hydroxide precipitate of scandium and the above impurities. To the solution containing the precipitate, 25 g of ammonium carbonate was added as a powder, and the mixture was stirred for 10 minutes. The pH of the solution at this time was 10.4. This was filtered to separate impurities, and 298 ml of a filtrate was obtained. To this was added 30 ml of commercially available special grade hydrochloric acid to adjust the pH of the solution to 1.0. afterwards,
13g of reagent grade oxalic acid was added as powder and stirred for 5 minutes,
A scandium oxalate precipitate formed. Scandium oxalate obtained by filtering this precipitate was roasted at 700 ° C. to obtain 2.8 g of purified scandium oxide. This was subjected to analysis. The results of this analysis are shown in Table 1. The results show that all impurity metals have been removed and purified. The recovery rate of scandium was 85%.

実施例2 表2に示す不純物を含有するpH1.5のスカンジウム硝
酸酸性溶液(Sc濃度:21.45mg/l)100mlに、市販特級ア
ンモニア水11mlを加えてpH8.8とした。これによりスカ
ンジウムと上記不純物の水酸化物沈澱を生成させた。こ
の沈澱を含む溶液に炭酸ナトリウム200g/lの溶液100ml
を添加して10分間撹拌した。このときの液のpHは10.2で
あった。これを濾過し不純物を分離して318mlの濾洗液
を得た。これに市販特級硝酸35mlを加えて液のpHを0.8
に調整した。その後、試薬特級蓚酸アンモニウム16gを
粉末のまま添加して5分間撹拌し、蓚酸スカンジウム沈
澱を生成させた。これを濾過して得た蓚酸スカンジウム
を700℃で焙焼して精製酸化スカンジウム2.83gを得た。
これを分析に供した。この分析結果を表2に示した。表
示する結果から、全ての不純物金属が除去され精製され
ていることがわかる。なお、スカンジウムの回収率は86
%であった。
Example 2 To 100 ml of a scandium nitrate acid solution (Sc concentration: 21.45 mg / l) containing impurities shown in Table 2 and having a pH of 1.5, 11 ml of commercially available special grade ammonia water was added to adjust the pH to 8.8. This produced a hydroxide precipitate of scandium and the above impurities. 100 ml of a solution of 200 g / l sodium carbonate in the solution containing this precipitate
Was added and stirred for 10 minutes. At this time, the pH of the solution was 10.2. This was filtered to separate impurities to obtain 318 ml of a washing solution. To this was added 35 ml of commercially available special grade nitric acid to adjust the pH of the solution to 0.8.
Was adjusted. Thereafter, 16 g of a reagent grade ammonium oxalate was added as it was and stirred for 5 minutes to produce a scandium oxalate precipitate. This was filtered and the scandium oxalate obtained was roasted at 700 ° C. to obtain 2.83 g of purified scandium oxide.
This was subjected to analysis. The results of this analysis are shown in Table 2. The results show that all impurity metals have been removed and purified. The recovery rate of scandium was 86
%Met.

実施例3 表2に示す不純物を含有するpH1.5のスカンジウム硝
酸酸性溶液100mlに、市販特級アンモニア水11mlを加え
てpH8.8とした。これによりスカンジウムと上記不純物
の水酸化物沈澱を生成させた。この沈澱を含む溶液に炭
酸水素ナトリウム200g/lの溶液80mlを添加して10分間撹
拌した。このときの液のpHは8.1であった。これを濾過
し不純物を分離して257mlの濾洗液を得た。これに市販
特級硝酸32mlを加えて液のpHを0.8に調整した。その
後、試薬特級蓚酸アンモニウム16gを粉末のまま添加し
て5分間撹拌し、蓚酸スカンジウム沈澱を生成させた。
以後、実施例2と同様にして精製酸化スカンジウム3.03
gを得た。この分析結果を表3に示した。表示する結果
から、全ての不純物金属が除去され精製されていること
がわかる。なお、スカンジウムの回収率は92%であっ
た。
Example 3 To 100 ml of a scandium nitrate acid solution of pH 1.5 containing impurities shown in Table 2, 11 ml of commercially available special grade ammonia water was added to adjust the pH to 8.8. This produced a hydroxide precipitate of scandium and the above impurities. To the solution containing the precipitate, 80 ml of a solution of 200 g / l of sodium bicarbonate was added and stirred for 10 minutes. The pH of the solution at this time was 8.1. This was filtered and impurities were separated to obtain 257 ml of a filtrate. To this was added 32 ml of commercially available special grade nitric acid to adjust the pH of the solution to 0.8. Thereafter, 16 g of a reagent grade ammonium oxalate was added as it was and stirred for 5 minutes to produce a scandium oxalate precipitate.
Thereafter, in the same manner as in Example 2, purified scandium oxide 3.03
g was obtained. The results of the analysis are shown in Table 3. The results show that all impurity metals have been removed and purified. The recovery rate of scandium was 92%.

比較例 表2に示す不純物を含有するpH1.5のスカンジウム硝
酸酸性溶液100mlに、試薬特級蓚酸13gを粉末のまま添加
して5分間撹拌し、蓚酸スカンジウム沈澱を生成させ
た。以後、実施例2と同様にして精製酸化スカンジウム
3.1gを得た。この分析結果を表4に示した。表示する結
果から、一部の不純物金属に対して精製効果が得られる
が、実施例1〜3に比較して不純物量が格段に多く、精
製効果が大幅に低い。
Comparative Example To 100 ml of a scandium nitric acid acidic solution having a pH of 1.5 and containing impurities shown in Table 2, 13 g of reagent grade oxalic acid was added as it was, and stirred for 5 minutes to form a scandium oxalate precipitate. Thereafter, in the same manner as in Example 2, the purified scandium oxide was used.
3.1 g was obtained. The results of this analysis are shown in Table 4. From the results shown, a refining effect can be obtained for some impurity metals, but the refining effect is much lower than in Examples 1 to 3, and the refining effect is significantly lower.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 木村 悦治 埼玉県大宮市北袋町1丁目297番地 三 菱金属株式会社中央研究所内 (58)調査した分野(Int.Cl.6,DB名) C01F 17/00 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Etsuji Kimura 1-297 Kitabukuro-cho, Omiya-shi, Saitama Mitsui Kinzoku Co., Ltd. Central Research Laboratory (58) Field surveyed (Int.Cl. 6 , DB name) C01F 17 / 00

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】不純物金属(Fe、Al、Sn、Zr、Ti、Pb、C
a、Cu、Zn、Thの1種または2種以上を云う)を含有す
る酸化スカンジウムを、塩酸または硝酸を用いてpH2以
下で溶解し、この溶解液に炭酸塩以外のアルカリを加え
てpHを3以上に調整してスカンジウムおよび不純物金属
を水酸化物として沈殿させ、この沈澱を含む溶液に炭酸
塩化合物を加えることによりアルカリ性下でスカンジウ
ム錯体を形成させて再溶解し、残留した不純物金属の沈
澱を濾別分離した後に、スカンジウム酸化物を回収する
ことを特徴とする酸化スカンジウムの精製方法。
1. An impurity metal (Fe, Al, Sn, Zr, Ti, Pb, C
a, Cu, Zn, or Th) is dissolved in hydrochloric acid or nitric acid at a pH of 2 or less using hydrochloric acid or nitric acid, and an alkali other than carbonate is added to the solution to adjust the pH. By adjusting the amount to 3 or more, scandium and the impurity metal are precipitated as hydroxides, and a carbonate compound is added to the solution containing the precipitate to form a scandium complex under alkalinity and redissolved to precipitate the remaining impurity metal. A method for purifying scandium oxide, comprising collecting scandium oxide after separating by filtration.
【請求項2】上記不純物金属の沈澱を濾別分離した後
に、その濾液に塩酸または硝酸を加えた後に蓚酸または
蓚酸塩化合物を添加して蓚酸スカンジウムを沈殿させ、
この沈殿を濾過回収し、焙焼してスカンジウム酸化物を
回収する請求項1の精製方法。
2. The precipitate of the impurity metal is separated by filtration, and then hydrochloric acid or nitric acid is added to the filtrate, followed by adding oxalic acid or an oxalate compound to precipitate scandium oxalate.
The purification method according to claim 1, wherein the precipitate is collected by filtration and roasted to recover the scandium oxide.
【請求項3】炭酸塩化合物による錯体の形成を60℃以下
で行う請求項1または2の方法。
3. The method according to claim 1, wherein the complex is formed by the carbonate compound at a temperature of 60 ° C. or lower.
JP2325747A 1990-11-29 1990-11-29 Purification method of scandium oxide Expired - Fee Related JP2890830B2 (en)

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Application Number Priority Date Filing Date Title
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JP2890830B2 true JP2890830B2 (en) 1999-05-17

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102676830A (en) * 2011-03-08 2012-09-19 龙颖 Method for extracting scandium oxide from tungsten steel slag
AU2015310078A1 (en) * 2014-08-26 2017-02-02 Ishihara Sangyo Kaisha, Ltd. Method for separating scandium
US11142809B2 (en) 2015-02-10 2021-10-12 Scandium International Mining Corp. Systems and processes for recovering scandium values from laterite ores
JP6583445B2 (en) * 2018-01-25 2019-10-02 住友金属鉱山株式会社 Method for producing high purity scandium oxide
KR102178440B1 (en) * 2018-12-18 2020-11-13 주식회사 포스코 Method for recovering scandium
CN112320832A (en) * 2020-10-23 2021-02-05 荆门市格林美新材料有限公司 Method for purifying and refining high-purity scandium oxide from scandium hydroxide intermediate product

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