JPH0353032A - Method for recovering samarium and cobalt from samarium-cobalt alloy scrap - Google Patents
Method for recovering samarium and cobalt from samarium-cobalt alloy scrapInfo
- Publication number
- JPH0353032A JPH0353032A JP1185930A JP18593089A JPH0353032A JP H0353032 A JPH0353032 A JP H0353032A JP 1185930 A JP1185930 A JP 1185930A JP 18593089 A JP18593089 A JP 18593089A JP H0353032 A JPH0353032 A JP H0353032A
- Authority
- JP
- Japan
- Prior art keywords
- samarium
- sulfuric acid
- cobalt
- aqueous solution
- alloy scrap
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明はサマリウム(SII1)一コバルト(co)焼
結合金磁石の製造時に発生するSrs − Co合金ス
クラノプからのS一およびCoの分離回収方法に関する
。[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a method for separating and recovering S- and Co from Srs-Co alloy scranop generated during the production of samarium (SII1)-cobalt (co) sintered alloy magnets. Regarding.
[従来の技術]
Ss − Co合金焼結磁石の製造工程から切削屑や不
良品等のスクラップが発生するが、これらのSm−Co
合金スクラップからSIIとCoをそれぞれ分離して回
収する方法として、Sa+ − Co合金スクラップを
塩酸、硝酸、硫酸等の絋酸に溶解し、蓚酸を添加してS
II1を蓚酸サマリウム沈殿として口過分離したのち、
口液に炭酸塩を添加してCoを炭酸コバルトとして回収
していた。しかしこの方法ではSmとCoを完全に分離
することが困難であった。すなわち、S一を完全に分離
するためには蓚酸を多量に添加しなければならず、この
際Coもまた蓚酸塩を形成してSII1の蓚酸塩と共沈
してしまうため純度の高いSmを回収できないのである
。[Prior art] Scraps such as cutting chips and defective products are generated in the manufacturing process of Ss-Co alloy sintered magnets, but these Sm-Co
As a method for separating and recovering SII and Co from alloy scrap, Sa+-Co alloy scrap is dissolved in oxalic acid such as hydrochloric acid, nitric acid, or sulfuric acid, and oxalic acid is added to dissolve SII.
After II1 was separated by filtration as samarium oxalate precipitate,
Co was recovered as cobalt carbonate by adding carbonate to the oral fluid. However, with this method, it was difficult to completely separate Sm and Co. That is, in order to completely separate S1, a large amount of oxalic acid must be added, and at this time, Co also forms oxalate and co-precipitates with the oxalate of SII1, so it is necessary to add highly pure Sm. It cannot be recovered.
[発明が解決しようとする課題〕
そこで本発明の目的は、上記問題点を解消し、簡便な処
理により高い回収率を達戒することのできるSm −
Go合金スクラップからのSmおよびCOO回収方法を
提供することである。[Problems to be Solved by the Invention] Therefore, the purpose of the present invention is to solve the above-mentioned problems and to obtain a Sm-
An object of the present invention is to provide a method for recovering Sm and COO from Go alloy scrap.
[課題を解決するための千段]
上記目的を達或するために、本発明方法はS+w −C
o合金スクラップを硫酸に溶解して硫酸水溶液とし、該
硫酸水溶液中のSmに対して概略当量以下の蓚酸を添加
してSsイオンの少量を該硫酸水溶液中に残すと共に析
出した蓚酸サマリウムを口過分離回収した後、口過液に
アルカリおよび/または炭酸化合物を添加して、析出し
たSmとCoの炭酸塩を含水析出物の形で分離し、該含
水析出物を硫酸で処理し、生戒した硫酸コバルト水溶液
を不溶解サマリウム複塩から口過分離回収する点に特徴
がある。[A thousand steps to solve the problem] In order to achieve the above object, the method of the present invention
o Alloy scrap is dissolved in sulfuric acid to make a sulfuric acid aqueous solution, and oxalic acid is added in an amount less than approximately equivalent to Sm in the sulfuric acid aqueous solution, leaving a small amount of Ss ions in the sulfuric acid aqueous solution, and precipitated samarium oxalate is filtered through the mouth. After separation and recovery, an alkali and/or carbonate compound is added to the oral filtrate to separate the precipitated carbonates of Sm and Co in the form of a hydrous precipitate, and the hydrous precipitate is treated with sulfuric acid to improve the quality of life. It is characterized by the fact that the aqueous cobalt sulfate solution obtained is separated and recovered from the undissolved samarium double salt.
[作 用]
第l図に本発明方法の手順を示す.
本発明方法に適用しうるStrr − Co合金スクラ
ップはSs − Co合金焼結磁石を製造する際に発生
する切削屑や割れた不良品等を挙げることができ、特に
限定されるものではないが、ランタン(La)、セリウ
ム(Ce)、プラセオジウム(Pr)等の希土類元素お
よび鉄(Fe)やニッケル(Ni)を不純物として含ん
でも差し支えない。該Ss − Co合金スクラップを
硫酸に溶解するに当り、該Sm − Co合金スクラッ
プを溶解することができればよく、該硫酸濃度は特に限
定されない。必要があれば、不溶解残渣を口過分離する
ことができる。[Operation] Figure 1 shows the procedure of the method of the present invention. Strr-Co alloy scrap that can be applied to the method of the present invention includes cutting waste generated during manufacturing Ss-Co alloy sintered magnets, cracked defective products, etc., and is not particularly limited. Rare earth elements such as lanthanum (La), cerium (Ce), and praseodymium (Pr), as well as iron (Fe) and nickel (Ni) may be included as impurities. When dissolving the Ss-Co alloy scrap in sulfuric acid, the sulfuric acid concentration is not particularly limited as long as the Sm-Co alloy scrap can be dissolved. If necessary, undissolved residue can be separated by filtration.
該硫酸水溶液中のS一に対して概略当量以下の蓚酸を添
加することが必要であるが、該硫酸水溶液中にS−をイ
オンの状態で少量残すことが重要である.もしも該硫酸
水溶液中のS一に対して当量を越える蓚酸を添加すると
、該Sllの全量を蓚酸サマリウムとして析出させるだ
けでな<、coも蓚酸コバルトとして共析させることと
なり蓚酸サマリウムの純度を低下させることとなり不都
合である。析出した蓚酸サマリウムをロ過分離回収した
後、口過液にアルカリおよび/または炭酸化合物を添加
するのであるが、該アルカリとしては特に制限されず、
水酸化ナトリウム、水酸化カリウム等のものを挙げるこ
とができ、該炭酸化合物もまた、炭酸ナトリウム、炭酸
水素ナトリウム、炭酸カリウム、炭酸水素カリウム、炭
酸アンモニウム等を挙げることができ、上記の化合物を
単独あるいは混合して用いればよい。該アルカリおよび
該炭酸化合物は水溶液状態でも粉末でも差し支えなく使
用することができる。該アルカリおよび/または該炭酸
化合物を該口過液に添加することにより硫酸水溶液を中
和して硫酸ナトリウムを形戒させるのであるが同時に該
アルカリおよび該炭酸化合物を使用しても、別々に使用
しても差し支えない。上記SLlとCoの炭酸塩析出物
を該口過液中から分離するに際し、含水状態で分離する
ことが必要である.該含水析出物として分離する方法と
しては常用の方法であればよいが特にフィルタープレス
法が好適である。Although it is necessary to add approximately an equivalent amount or less of oxalic acid to S- in the sulfuric acid aqueous solution, it is important to leave a small amount of S- in the ion state in the sulfuric acid aqueous solution. If oxalic acid is added in excess of an amount equivalent to S in the sulfuric acid aqueous solution, not only will the entire amount of S be precipitated as samarium oxalate, but also co will be eutectoid as cobalt oxalate, reducing the purity of samarium oxalate. This is inconvenient. After the precipitated samarium oxalate is separated and recovered by filtration, an alkali and/or carbonate compound is added to the filtrate, but the alkali is not particularly limited.
Examples of the carbonate compound include sodium hydroxide, potassium hydroxide, etc., and examples of the carbonate compound include sodium carbonate, sodium hydrogen carbonate, potassium carbonate, potassium hydrogen carbonate, ammonium carbonate, etc. Alternatively, they may be used in combination. The alkali and the carbonate compound can be used in the form of an aqueous solution or a powder. By adding the alkali and/or the carbonate compound to the oral fluid, the sulfuric acid aqueous solution is neutralized and the sodium sulfate is eliminated, but the alkali and the carbonate compound can be used at the same time or separately. It's okay to do that. When separating the SL1 and Co carbonate precipitates from the mouth filtrate, it is necessary to separate them in a water-containing state. Any conventional method may be used to separate the water-containing precipitate, but a filter press method is particularly suitable.
該含水析出物は固形でもスラリー状態でも差し支えない
が、重要なことは、該含水析出物を水洗して該含水析出
物中の水分および該水分に溶解している硫酸ナトリウム
を除去してはならず、含水率が70重量%程度あること
が好ましい。該含水析出物を硫酸で処理するに際し、該
含水析出物中のCo沈殿物のみを溶解しなければならず
、Coが50g/1以上となるように溶解するのが良く
、用いる硫酸濃度は70重量%のものが好適である。The water-containing precipitate may be in a solid or slurry state, but the important thing is that the water-containing precipitate must not be washed with water to remove the water in the water-containing precipitate and the sodium sulfate dissolved in the water. First, it is preferable that the water content is about 70% by weight. When treating the water-containing precipitate with sulfuric acid, it is necessary to dissolve only the Co precipitate in the water-containing precipitate, and it is preferable to dissolve Co so that it is 50 g/1 or more, and the sulfuric acid concentration used is 70 g/1 or more. % by weight is preferred.
上記硫酸処理では、該含水析出物中のSI1沈殿物が硫
酸塩に変化すると同時に該含水中の硫酸ナトリウムと直
ちに結合し(SIlt(SO*)i ’ NazSo4
’ 811zO)なる不溶性の複塩を形成し沈殿物とな
る。従って該含水析出物を硫酸で処理した硫酸コバルト
水溶液から該不溶性Sll複塩をロ遇分離することがで
き、S一を含まない硫酸コバルトを回収し得る.[実施
例]
第1表に戒分の分析値を示す湿式粉砕したSs −Co
合金スクラフプ40kgを8 0 g/lのHzSOn
700lを加えて蒸気を吹き込みつつ加温溶解をして7
60Ilの硫酸水溶液を得た.スクラップ中に含まれる
Pr, Nd, CeはS+mと同じ希土類であり蓚酸
に対し反応性が高いので、これらを合計し、この合計に
対して、蓚酸反応率90%とみなし、1.0当量の蓚酸
と添加し、蓚酸塩を析出させ口過分離した。In the above sulfuric acid treatment, the SI1 precipitate in the water-containing precipitate changes into sulfate and at the same time immediately combines with the sodium sulfate in the water-containing precipitate (SIlt(SO*)i' NazSo4
'811zO) forms an insoluble double salt and becomes a precipitate. Therefore, the insoluble Sll double salt can be thoroughly separated from the cobalt sulfate aqueous solution obtained by treating the water-containing precipitate with sulfuric acid, and cobalt sulfate containing no S1 can be recovered. [Example] Wet-pulverized Ss-Co whose analytical values are shown in Table 1
Alloy Scrap 40kg to 80 g/l HzSOn
Add 700 liters and melt by heating while blowing steam.
60 Il of sulfuric acid aqueous solution was obtained. Pr, Nd, and Ce contained in the scrap are rare earth elements like S+m and have high reactivity to oxalic acid. Oxalic acid was added, and oxalate was precipitated and separated by filtration.
炉液中のSsの濃度は1.2 2 g/l, Coの濃
度は22g/lであった。この口液にカ性ソーダを添加
しpH4.0とし、次に炭酸ナトリウム20kgを添加
し、更にカ性ソーダを加えてpH10以上とした。The concentration of Ss in the furnace liquid was 1.2 2 g/l, and the concentration of Co was 22 g/l. Caustic soda was added to this mouth liquid to adjust the pH to 4.0, then 20 kg of sodium carbonate was added, and further caustic soda was added to adjust the pH to 10 or more.
生じた沈殿物をフィルタープレスでロ過したところ、6
7重量%の含水率の析出物を得た。口液中のsi濃度は
0.01g/l未満であった。上記含水析出物をタンク
中にて70重量%硫酸501および水を加え溶解した。When the resulting precipitate was filtered through a filter press, 6
A precipitate with a water content of 7% by weight was obtained. The si concentration in the oral fluid was less than 0.01 g/l. The above water-containing precipitate was dissolved in a tank by adding 70% by weight sulfuric acid 501 and water.
この硫酸水溶液をデンバー口過器で口過したところ硫酸
コバルト(Co64g/1〉水溶液2601と、分離し
た硫酸サマリウム・硫酸ナトリウム複塩(乾燥重量5.
9 kg)を回収した。When this sulfuric acid aqueous solution was passed through a Denver filter, a cobalt sulfate (Co64 g/1) aqueous solution 2601 and a separated samarium sulfate/sodium sulfate double salt (dry weight 5.
9 kg) were collected.
硫酸コバルト水溶液中のSsは0.16g/i!であっ
た。Ss in cobalt sulfate aqueous solution is 0.16g/i! Met.
第 1 表
上記処理により、SIl1はスクラソプ中に存在した量
に対して硫酸コバルト水溶液中に約0.6重量%存在す
るのみで、極めて低いものであった。Table 1 As a result of the above treatment, the amount of SIl1 present in the cobalt sulfate aqueous solution was only about 0.6% by weight compared to the amount present in the scrubber, which was extremely low.
[発明の効果]
本発明方法を実施することにより、簡便な処理で、かつ
高回収率でSLII− Co合金スクラップからSa+
とCoをそれぞれ分離回収することができ、その効果は
大である.[Effects of the Invention] By carrying out the method of the present invention, Sa+ can be recovered from SLII-Co alloy scrap with simple processing and high recovery rate.
It is possible to separate and recover Co and Co, respectively, and the effect is great.
第1図は本発明方法の手順を示す図である。 特許出順人 住友金属鉱山株式会社 FIG. 1 is a diagram showing the procedure of the method of the present invention. Patent issuer: Sumitomo Metal Mining Co., Ltd.
Claims (1)
硫酸水溶液とし、該硫酸水溶液中のサマリウムに対して
概略当量以下の蓚酸を添加してサマリウムイオンの少量
を該硫酸水溶液中に残すと共に析出した蓚酸サマリウム
をロ過分離回収した後、ロ過液にアルカリおよび/また
は炭酸化合物を添加して、析出したサマリウムとコバル
トの炭酸塩を含水析出物の形で分離し、該含水析出物を
硫酸で処理し、生成した硫酸コバルト水溶液を不溶解サ
マリウム複塩からロ過分離回収することを特徴とするサ
マリウム−コバルト合金スクラップからのサマリウムお
よびコバルトの回収方法。Samarium-cobalt alloy scrap is dissolved in sulfuric acid to make a sulfuric acid aqueous solution, and oxalic acid is added in an amount less than approximately equivalent to the samarium in the sulfuric acid aqueous solution, leaving a small amount of samarium ions in the sulfuric acid aqueous solution and precipitated samarium oxalate. After filtration separation and recovery, add an alkali and/or carbonate compound to the filtrate to separate precipitated samarium and cobalt carbonates in the form of a hydrous precipitate, and treat the hydrous precipitate with sulfuric acid, 1. A method for recovering samarium and cobalt from samarium-cobalt alloy scrap, which comprises recovering the generated cobalt sulfate aqueous solution from undissolved samarium double salt by filtration separation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1185930A JPH0353032A (en) | 1989-07-20 | 1989-07-20 | Method for recovering samarium and cobalt from samarium-cobalt alloy scrap |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1185930A JPH0353032A (en) | 1989-07-20 | 1989-07-20 | Method for recovering samarium and cobalt from samarium-cobalt alloy scrap |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0353032A true JPH0353032A (en) | 1991-03-07 |
Family
ID=16179367
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1185930A Pending JPH0353032A (en) | 1989-07-20 | 1989-07-20 | Method for recovering samarium and cobalt from samarium-cobalt alloy scrap |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0353032A (en) |
-
1989
- 1989-07-20 JP JP1185930A patent/JPH0353032A/en active Pending
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