JPS632893B2 - - Google Patents
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- Publication number
- JPS632893B2 JPS632893B2 JP53150737A JP15073778A JPS632893B2 JP S632893 B2 JPS632893 B2 JP S632893B2 JP 53150737 A JP53150737 A JP 53150737A JP 15073778 A JP15073778 A JP 15073778A JP S632893 B2 JPS632893 B2 JP S632893B2
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- JP
- Japan
- Prior art keywords
- rare earth
- lead
- aqueous solution
- sulfide
- compound
- 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.)
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- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
【発明の詳細な説明】
本発明は希土類化合物の製造方法に関するもの
である。詳しくは、鉛化合物の含有量が極めて少
い希土類化合物を製造する方法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing rare earth compounds. More specifically, the present invention relates to a method for producing a rare earth compound with an extremely low content of lead compounds.
希土類元素は、エレクトロニクスその他の分野
への用途が開けつつあるが、エレクトロニクス素
材の場合、特に不純物を含まないことが要求され
る。 Rare earth elements are increasingly being used in electronics and other fields, but in the case of electronics materials, they are particularly required to be free of impurities.
希土類化合物の分離、精製は、通常、液一液抽
出、イオン交換抽出などの方法によつて行われる
が、例えば、チオシアン型第4級アンモニウム塩
抽出溶媒を用いるイツトリウムの分離において
は、鉛はイツトリウムと類似の抽出挙動をとり、
分離が困難であるとか、また、抽出操作の際使用
する硝酸、塩酸、硫酸などの酸の中に含まれる鉛
化合物が混入することもあつて、鉛含有量の少い
希土類化合物を得ることは困難であつた。 Separation and purification of rare earth compounds is usually carried out by methods such as liquid-liquid extraction and ion exchange extraction. For example, in the separation of yttrium using a thiocyanate quaternary ammonium salt extraction solvent, lead is The extraction behavior is similar to that of
It is difficult to obtain rare earth compounds with low lead content because separation is difficult, and lead compounds contained in acids such as nitric acid, hydrochloric acid, and sulfuric acid used during extraction operations may be mixed in. It was difficult.
水溶液中の鉛化合物を除去する方法としては硫
化水素や硫化ナトリウムなどを用い、水溶液中の
鉛から硫化鉛を生成させて除去する方法が知られ
ているが、この方法によるときは、水溶液中の鉛
を1ppm程度以下とすることはできない。 A known method for removing lead compounds from an aqueous solution is to use hydrogen sulfide, sodium sulfide, etc. to generate lead sulfide from the lead in the aqueous solution. Lead cannot be reduced to less than about 1 ppm.
この方法を希土類化合物の水溶液に適用して
も、通常希土類化合物は0.1〜1.0モル/程度の
濃度の水溶液として取扱われることが多く、鉛の
量が水溶液中で1ppmであつても、この水溶液か
ら得られる希土類元素中には、鉛が濃縮されて
9ppm程度以上含まれることになり、前記用途の
ための希土類元素としては満足し得るものではな
い。 Even if this method is applied to an aqueous solution of a rare earth compound, the rare earth compound is usually treated as an aqueous solution with a concentration of about 0.1 to 1.0 mol/kg, and even if the amount of lead in the aqueous solution is 1 ppm, Lead is concentrated in the rare earth elements obtained.
The content is about 9 ppm or more, which is not satisfactory as a rare earth element for the above-mentioned purpose.
本発明者らは、鉛化合物の含有量の少い希土類
化合物を製造すべく、鋭意研究を重ねた結果、希
土類化合物の水溶液を硫化物の存在下、特定の処
理を行うことによつて、鉛化合物をほとんど完全
に除去することができることを知得して本発明を
完成した。 The inventors of the present invention have conducted extensive research to produce rare earth compounds with a low lead content. As a result, the inventors have found that by subjecting an aqueous solution of a rare earth compound to a specific treatment in the presence of sulfide, lead can be reduced. The present invention was completed based on the knowledge that the compound can be almost completely removed.
すなわち本発明は、鉛化合物の含有量の少い希
土類化合物を、工業的に有利に製造することを目
的とするものであり、この目的は、不純物として
鉛化合物を含有する希土類化合物の水溶液に、硫
化水素、硫化アンモニウムまたは金属硫化物の存
在下、PH2〜7で、シユウ酸またはそのアンモニ
ウム塩を添加して、希土類化合物の一部を希土類
元素のシユウ酸塩として沈澱させ、生成した沈澱
を分離除去することによつて達成される。 That is, the purpose of the present invention is to industrially advantageously produce a rare earth compound with a small content of lead compounds, and this purpose is to add a rare earth compound containing a lead compound as an impurity to an aqueous solution of a rare earth compound containing a lead compound as an impurity. In the presence of hydrogen sulfide, ammonium sulfide, or metal sulfide, at pH 2 to 7, oxalic acid or its ammonium salt is added to precipitate a portion of the rare earth compound as the oxalate of the rare earth element, and the generated precipitate is separated. This is achieved by removing.
以下、本発明を詳細に説明する。 The present invention will be explained in detail below.
本発明でいう希土類化合物とは、原子番号が57
〜71の元素およびイツトリウム、スカンジウムを
包括する元素群の化合物を指すものである。 The rare earth compound referred to in the present invention has an atomic number of 57.
It refers to compounds of a group of elements including ~71 elements, yttrium, and scandium.
本発明で対象とする不純物として鉛化合物を含
有する希土類化合物の水溶液(以下含鉛希土水溶
液と略称する)は、希土類元素の硝酸塩、塩化
物、硫酸塩などの酸の塩の水溶液であり、不純物
として鉛化合物を含有するものである。希土類化
合物の濃度は0.01〜1.5モル〜程度、好ましく
は0.1〜1.0モル/から選ぶのがよい。 The aqueous solution of a rare earth compound containing a lead compound as an impurity targeted by the present invention (hereinafter referred to as a lead-containing rare earth aqueous solution) is an aqueous solution of an acid salt such as a nitrate, chloride, or sulfate of a rare earth element, It contains lead compounds as impurities. The concentration of the rare earth compound is preferably selected from about 0.01 to 1.5 mol, preferably from 0.1 to 1.0 mol.
硫化水素、硫化アンモニウムまたは金属硫化物
(以下単に硫化物と略称する)としては、硫化水
素、硫化アンモニウム、硫化ナトリウム、硫化カ
リウムのようなアルカリ金属の硫化物、硫化イツ
トリウム、硫化サマリウム、硫化セリウムのよう
な希土類元素の硫化物、その他鉛以外の各種金属
の硫化物があげられるが、希土類化合物中に異種
金属が混入することが不都合な場合には、硫化水
素、硫化アンモニウム、アルカリ金属の硫化物ま
たは希土類元素の硫化物を使用するのがよい。 Hydrogen sulfide, ammonium sulfide, or metal sulfides (hereinafter simply referred to as sulfides) include hydrogen sulfide, ammonium sulfide, alkali metal sulfides such as sodium sulfide, potassium sulfide, yttrium sulfide, samarium sulfide, and cerium sulfide. Examples include sulfides of rare earth elements, such as sulfides of various metals other than lead, but if it is inconvenient that different metals are mixed into rare earth compounds, hydrogen sulfide, ammonium sulfide, and sulfides of alkali metals are used. Alternatively, it is better to use sulfides of rare earth elements.
アルカリ金属は本発明の処理後、例えば希土類
化合物から希土類元素をシユウ酸塩として取得す
る方法を採用することによつて、希土類元素と分
離することができる。また、希土類元素の硫化物
を用いる場合は、含鉛希土水溶液中の希土類元素
と同種の元素を用いることによつて、異種金属の
混入を避けることができる。 After the treatment of the present invention, the alkali metal can be separated from the rare earth element, for example, by employing a method of obtaining the rare earth element as an oxalate from the rare earth compound. Furthermore, when using a sulfide of a rare earth element, mixing of different metals can be avoided by using the same type of element as the rare earth element in the lead-containing rare earth aqueous solution.
上記硫化物を存在させるには、含鉛希土水溶液
と硫化物を混合するのみでよいが、鉛の含有量の
多い含鉛希土水溶液の場合は、過剰の硫化物を混
合して、固体の硫化鉛を生成させて分離除去した
ものを用いてもよい。 In order to make the above sulfides exist, it is sufficient to simply mix the lead-containing rare earth aqueous solution and the sulfide, but in the case of a lead-containing rare earth aqueous solution with a high lead content, it is necessary to mix excess sulfide and solidify it. It is also possible to use a product in which lead sulfide is generated and separated and removed.
存在させる硫化物の量は、含鉛希土水溶液中の
鉛に対し5〜200倍モル、好ましくは30〜150倍モ
ル程度とするのがよい。あまりに少いと本発明の
効果が期待できなくなる。逆に多いことは特に支
障はないが、多く用いたことによる特段の効果が
期待できるものではない。 The amount of sulfide to be present is preferably about 5 to 200 times, preferably about 30 to 150 times, the amount of lead in the lead-containing rare earth aqueous solution. If the amount is too small, the effects of the present invention cannot be expected. On the other hand, there is no particular problem in using too much, but no particular effect can be expected from using too much.
本発明の処理を行う際の含鉛希土水溶液のPHは
2〜7である必要があり、好ましくは5〜6.5程
度である。PHが2より低いと本発明の効果が小さ
く、実用的でなくなる。逆にPHが7より高いと、
希土類化合物が水酸化物となつて析出するように
なり、希土類化合物の損失が大きくなるので好ま
しくない。 The pH of the lead-containing rare earth aqueous solution used in the treatment of the present invention must be between 2 and 7, preferably between about 5 and 6.5. If the pH is lower than 2, the effect of the present invention will be small and will be impractical. On the other hand, if the pH is higher than 7,
This is not preferable because the rare earth compound becomes a hydroxide and precipitates, resulting in a large loss of the rare earth compound.
含鉛希土水溶液のPHを調整するには、アンモニ
ア、水酸化ナトリウム、水酸化カリウムなどを使
用することができる。 To adjust the pH of the lead-containing rare earth aqueous solution, ammonia, sodium hydroxide, potassium hydroxide, etc. can be used.
本発明においては、上記含鉛希土水溶液を硫化
物の存在下PH2〜7で、シユウ酸またはそのアン
モニウム塩を加えて、含鉛希土水溶液中の一部の
希土類化合物をシユウ酸塩として沈澱させる。か
くするときは、含鉛希土水溶液中の鉛化合物も共
に沈澱する。 In the present invention, some rare earth compounds in the lead-containing rare earth aqueous solution are precipitated as oxalates by adding oxalic acid or its ammonium salt to the lead-containing rare earth aqueous solution at pH 2 to 7 in the presence of sulfide. let When this is done, the lead compounds in the lead-containing rare earth aqueous solution are also precipitated.
シユウ酸またはそのアンモニウム塩は、固体の
まま加えてもよく、また水溶液として加えてもよ
い。またシユウ酸のアンモニウム塩としては、シ
ユウ酸アンモニウム、シユウ酸水素アンモニウム
の何れであつてもよい。 Oxalic acid or its ammonium salt may be added as a solid or as an aqueous solution. The ammonium salt of oxalic acid may be either ammonium oxalate or ammonium hydrogen oxalate.
シユウ酸またはそのアンモニウム塩の使用量
は、含鉛希土水溶液中の希土類化合物に対し、
0.05〜0.7倍モル、好ましくは0.1〜0.3倍モル使用
するのがよい。あまりに少いと本発明の効果が得
がたくなる。逆に多いことは、鉛化合物の除去の
上からは好ましいけれども、シユウ酸塩となつて
鉛化合物と共に沈澱する希土類元素が多くなるの
で得策ではない。 The amount of oxalic acid or its ammonium salt to be used is based on the rare earth compound in the lead-containing rare earth aqueous solution.
It is preferable to use 0.05 to 0.7 times the mole, preferably 0.1 to 0.3 times the mole. If it is too small, it will be difficult to obtain the effects of the present invention. On the contrary, although it is preferable to remove lead compounds, it is not a good idea to increase the amount of rare earth elements, which become oxalate and precipitate together with the lead compounds.
上記沈澱を生成させる際の温度は、常温以外の
温度を採用することもできるが、通常常温付近で
十分である。 Although a temperature other than room temperature can be adopted as the temperature for producing the above-mentioned precipitate, a temperature around room temperature is usually sufficient.
かくして、沈澱を生成させた後は、過などの
手段によつて、生成した沈澱を分離することによ
つて、鉛化合物の含有量が極めて少い希土類化合
物の水溶液が得られ、この水溶液にシユウ酸を加
えて希土類元素をシユウ酸塩として析出させる方
法、あるいはアンモニアを加えて希土類元素を水
酸化物として析出させる方法などによつて、鉛含
有量が2ppm程度以下の希土類化合物を得ること
ができる。 After the precipitate is formed, an aqueous solution of a rare earth compound with an extremely low content of lead compounds can be obtained by separating the precipitate by filtration or other means. A rare earth compound with a lead content of about 2 ppm or less can be obtained by adding an acid to precipitate the rare earth element as an oxalate, or adding ammonia to precipitate the rare earth element as a hydroxide. .
本発明は、粗希土類化合物の精製の任意の段階
で適用することができるが、抽出などの操作の際
使用される酸などからの鉛化合物の混入を考慮す
ると、本発明は、精製の最終段階、すなわち、希
土類化合物の水溶液から製品希土類化合物を取得
する直前に適用するのが好ましい。 The present invention can be applied at any stage of purification of crude rare earth compounds, but considering the contamination of lead compounds from acids used during operations such as extraction, the present invention can be applied to the final stage of purification. That is, it is preferable to apply it immediately before obtaining the rare earth compound product from the aqueous solution of the rare earth compound.
また、沈澱した鉛を含有する希土類元素のシユ
ウ酸塩は、鉛含有量が問題とならない用途に用い
てもよく、また、本発明の原料として使用するこ
ともできる。 Further, the rare earth element oxalate containing precipitated lead may be used in applications where the lead content is not a problem, and may also be used as a raw material in the present invention.
本発明方法によるときは、容易な操作で鉛化合
物含有量の極めて少い希土類化合物を製造するこ
とができるので、工業的価値が大きい。 The method of the present invention has great industrial value because rare earth compounds with extremely low lead compound content can be produced with easy operations.
以下、実施例によつて本発明を具体的に説明す
るが、本発明はその要旨をこえない限り以下の実
施例に限定されるものではない。 EXAMPLES The present invention will be specifically explained below with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist thereof.
なお、実施例中の鉛の含有量は原子吸光法によ
つて分析した値である。 In addition, the content of lead in the examples is a value analyzed by atomic absorption spectrometry.
実施例 1
Y2O3当り33ppmの鉛を含有する硝酸イツトリ
ウム〔Y(NO3)3〕の0.4モル/水溶液155mlに、
0.5%硫化ナトリウム水溶液2mlを添加し、アン
モニア水を用いてPHを6.5に調整した。この段階
では固体の析出は認められなかつた。Example 1 To 155 ml of a 0.4 mol/aqueous solution of yttrium nitrate [Y(NO 3 ) 3 ] containing 33 ppm lead per Y 2 O 3 ,
2 ml of 0.5% sodium sulfide aqueous solution was added, and the pH was adjusted to 6.5 using aqueous ammonia. No solid precipitation was observed at this stage.
この溶液に、固体のシユウ酸2.36gを加え、1
時間撹拌して沈澱を生成させた後、5Cの紙
(東洋紙(株)製)を用いて沈澱を別した。得ら
れた硝酸イツトリウム水溶液に硝酸を加えてPHを
0.4に調整した後、7%シユウ酸水溶液170mlを添
加して、イツトリウムをシユウ酸塩として析出さ
せた。 Add 2.36 g of solid oxalic acid to this solution and
After stirring for a period of time to form a precipitate, the precipitate was separated using 5C paper (manufactured by Toyo Paper Co., Ltd.). Add nitric acid to the obtained yttrium nitrate aqueous solution to adjust the pH.
After adjusting the concentration to 0.4, 170 ml of a 7% aqueous oxalic acid solution was added to precipitate yttrium as an oxalate salt.
このシユウ酸イツトリウムを焼成して得た酸化
イツトリウムの量は5.95g(収率85.2%)であり
鉛含有量は2.7ppmであつた。 The amount of yttrium oxide obtained by calcining this yttrium oxalate was 5.95 g (yield: 85.2%), and the lead content was 2.7 ppm.
なお、沈澱を焼成して得た酸化イツトリウムの
量は1.03g(ロス14.8%)であり鉛含有量は
200ppmであつた。 The amount of yttrium oxide obtained by calcining the precipitate was 1.03 g (loss 14.8%), and the lead content was
It was 200ppm.
実施例 2
酸化物の重量%でイツトリウム25.3%、エルビ
ウム6.6%、ホルミウム1.5%、ジスプロシウム
18.7%、ガドリニウム20.3%、サマリウム27.6%
の組成を有し、Pbを希土酸化物当り35ppm含有
する混合希土を硝酸に溶解し、0.4モル/の硝
酸希土水溶液を調整した。Example 2 Weight percent of oxides: yttrium 25.3%, erbium 6.6%, holmium 1.5%, dysprosium
18.7%, gadolinium 20.3%, samarium 27.6%
A mixed rare earth having the composition and containing 35 ppm of Pb per rare earth oxide was dissolved in nitric acid to prepare a 0.4 mol/aqueous rare earth nitrate solution.
この水溶液155mlを用いて、実施例と同一条件
で同様な操作を行なつた結果、Pb含有量が酸化
物当り2.3ppmである混合希土酸化物8.68gを得
た(収率88.6%)。 Using 155 ml of this aqueous solution, the same operation as in the example was carried out under the same conditions as in the example, and as a result, 8.68 g of mixed rare earth oxide having a Pb content of 2.3 ppm per oxide was obtained (yield: 88.6%).
なお、沈澱を焼成して、Pb含有量が220ppmで
ある混合希土酸化物1.12gを得た。(ロス11.4%) The precipitate was calcined to obtain 1.12 g of mixed rare earth oxide having a Pb content of 220 ppm. (Loss 11.4%)
Claims (1)
物の水溶液に、硫化水素、硫化アンモニウムまた
は金属硫化物の存在下、PH2〜7で、シユウ酸ま
たはそのアンモニウム塩を添加して、希土類化合
物の一部を希土類元素のシユウ酸塩として沈澱さ
せ、生成した沈澱を分離除去することを特徴とす
る希土類化合物の精製方法。1. Oxalic acid or its ammonium salt is added to an aqueous solution of a rare earth compound containing a lead compound as an impurity in the presence of hydrogen sulfide, ammonium sulfide, or metal sulfide at a pH of 2 to 7 to convert a portion of the rare earth compound into a rare earth compound. A method for purifying a rare earth compound, which comprises precipitating the element as an oxalate and separating and removing the generated precipitate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15073778A JPS5575920A (en) | 1978-12-06 | 1978-12-06 | Production of rare earth element compound |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15073778A JPS5575920A (en) | 1978-12-06 | 1978-12-06 | Production of rare earth element compound |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5575920A JPS5575920A (en) | 1980-06-07 |
| JPS632893B2 true JPS632893B2 (en) | 1988-01-21 |
Family
ID=15503302
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15073778A Granted JPS5575920A (en) | 1978-12-06 | 1978-12-06 | Production of rare earth element compound |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5575920A (en) |
-
1978
- 1978-12-06 JP JP15073778A patent/JPS5575920A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5575920A (en) | 1980-06-07 |
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