JPH05247556A - Method for covering in from pb-sn-in alloy - Google Patents

Method for covering in from pb-sn-in alloy

Info

Publication number
JPH05247556A
JPH05247556A JP7876492A JP7876492A JPH05247556A JP H05247556 A JPH05247556 A JP H05247556A JP 7876492 A JP7876492 A JP 7876492A JP 7876492 A JP7876492 A JP 7876492A JP H05247556 A JPH05247556 A JP H05247556A
Authority
JP
Japan
Prior art keywords
dross
alloy
added
scrap
melt
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.)
Granted
Application number
JP7876492A
Other languages
Japanese (ja)
Other versions
JP3199184B2 (en
Inventor
Harutoshi Kubota
晴俊 窪田
Chiaki Minami
千秋 南
Shuji Hata
修二 畑
Kazuhiko Takei
和彦 武井
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.)
Sumitomo Metal Mining Co Ltd
Original Assignee
Sumitomo Metal Mining 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 Sumitomo Metal Mining Co Ltd filed Critical Sumitomo Metal Mining Co Ltd
Priority to JP7876492A priority Critical patent/JP3199184B2/en
Publication of JPH05247556A publication Critical patent/JPH05247556A/en
Application granted granted Critical
Publication of JP3199184B2 publication Critical patent/JP3199184B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

PURPOSE:To recover high-purity In from Pb-Sn-In alloy scrap at a high yield by adding ammonia chloride to the melt of the Pb-Sn-In alloy scrap and separating In as InCl dross. CONSTITUTION:The scrap of the Pb-Sn-In alloy is put into a graphite crucible and is melted in an electric furnace. While this scrap melt is maintained in a 350 to 500 deg.C range, NH4Cl is added at 0.1 to 1.0wt.% ratio to the melt and the melt is stirred. The In the molten scrap floats as dross on the surface of the molten alloy. This treatment is repeated and continued until the In content in the molten alloy decreases to a desired value or below and until the grater part of the In the molten alloy turns to the dross. Concd. hydrochloric acid and water are added to the resultant dross and the dross is stirred and dissolved. The hydrochloric acid liquid contg. the dissolved In is filtered and separated from the undissolved matter and an NaOH soln. is added thereto. The generated precipitate is removed and thereafter, Zn powder is added thereto to precipitate the high-purity In. This In is separated and recovered.

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、In含有物からのIn
の回収に関し、特にPbとSnとInとを主成分とする
Pb−Sn−In合金からのInの回収方法に関する。
The present invention relates to In from In-containing materials.
The present invention relates to a method for recovering In from a Pb-Sn-In alloy containing Pb, Sn, and In as main components.

【0002】[0002]

【従来の技術】Inは、主として亜鉛製錬における副産
物として産出され、例えば、Pb−Sn−In合金のよ
うに各種の合金材料として用いられている。前記Pb−
Sn−In合金は、低融点であるために、スパッタリン
グターゲットなどのボンディング用ろう材として広く使
用されている。
2. Description of the Related Art In is mainly produced as a by-product in zinc smelting, and is used as various alloy materials such as Pb-Sn-In alloy. Pb-
Since the Sn-In alloy has a low melting point, it is widely used as a brazing material for bonding such as a sputtering target.

【0003】ところで、Inは高価な金属であり、また
希少物質であること等から、Inを含む各種のスクラッ
プよりInを回収する方法が開発されている。
By the way, since In is an expensive metal and is a rare substance, a method for recovering In from various scraps containing In has been developed.

【0004】従来よりIn含有原料からのInの回収方
法としては各種の方法が提案されている。湿式法では、
例えば、(1)In含有原料を硫酸で溶解し、水酸化ア
ルカリで中和し、生成した沈澱を硫酸で再溶解し、得た
溶液にZn粉末等の還元剤を添加し、粗Inを得、これ
を精製する方法や、(2)In含有原料を硫酸で溶解し
て得た溶液に硫化剤を添加し、生成した沈澱を除去し、
得た溶液を中和して得た沈澱を塩酸で溶解し、得た溶液
に再度硫化剤を添加し、生成した硫化物を分離した後の
溶液のpHを調整し、Zn粉末等を添加して得た粗In
を精製する方法がある。乾式法では、In含有原料を塩
化剤と混合し、加熱してInを塩化物として揮発させ、
回収する方法がある。
Conventionally, various methods have been proposed as a method of recovering In from an In-containing raw material. In the wet method,
For example, (1) In-containing raw material is dissolved with sulfuric acid, neutralized with alkali hydroxide, the formed precipitate is redissolved with sulfuric acid, and a reducing agent such as Zn powder is added to the obtained solution to obtain crude In. , A method for purifying it, or (2) adding a sulfiding agent to a solution obtained by dissolving an In-containing raw material with sulfuric acid to remove the formed precipitate,
The precipitate obtained by neutralizing the obtained solution was dissolved with hydrochloric acid, the sulfiding agent was added again to the obtained solution, the pH of the solution after separating the produced sulfide was adjusted, and Zn powder and the like were added. Crude In obtained
There is a method of purifying. In the dry method, an In-containing raw material is mixed with a chlorinating agent and heated to volatilize In as a chloride,
There is a way to collect it.

【0005】上記Pb−Sn−In合金においても、そ
の使用量の拡大と共にスクラップが増加するので、該ス
クラップからのInの回収、再利用が注目されてきてい
る。
In the above Pb-Sn-In alloy as well, since the amount of scrap increases with the increase in the amount used, the recovery and reuse of In from the scrap has been drawing attention.

【0006】合金の再利用という観点では、Pb−Sn
−In合金スクラップを再溶解などのように簡単に処理
できることがもっとも望まれる。しかしながら、このよ
うなPb−Sn−In合金スクラップは、不純物を含ん
でいるので、再溶解し組成比を調整するだけでは再利用
可能なPb−Sn−In合金を得ることができないのが
一般的である。よって、Inを選択的に回収し、生成し
て得た高純度InメタルをPb−Sn合金に添加するこ
とがInの再利用として最適といえる。
From the viewpoint of alloy reuse, Pb-Sn
It is most desirable to be able to easily process the In alloy scrap such as remelting. However, since such a Pb-Sn-In alloy scrap contains impurities, it is generally impossible to obtain a reusable Pb-Sn-In alloy only by remelting and adjusting the composition ratio. Is. Therefore, it can be said that it is optimum for reuse of In to selectively collect In and add the high-purity In metal obtained by the generation to the Pb-Sn alloy.

【0007】さらに、上記湿式法は比較的煩雑であり、
該湿式法を本発明の対象たるPb−Sn−In合金に適
用すると、溶解時に硫酸や塩酸を用いるため、硫酸鉛や
塩化鉛といった沈澱を原料表面に形成して原料を不溶解
化する問題点がある。また、乾式法を適用すると、In
ばかりでなくPbまでもが塩化物として揮発する問題点
がある。
Further, the wet method is relatively complicated,
When the wet method is applied to the Pb-Sn-In alloy which is the object of the present invention, sulfuric acid or hydrochloric acid is used during melting, so that a precipitate such as lead sulfate or lead chloride is formed on the surface of the raw material to make the raw material insoluble. There is. When the dry method is applied, In
Not only Pb but also volatilize as chlorides.

【0008】[0008]

【発明が解決しようとする課題】本発明の目的は、Pb
−Sn−In合金スクラップよりInを分離回収する方
法の提供にある。
The object of the present invention is to provide Pb
-Providing a method for separating and recovering In from Sn-In alloy scrap.

【0009】[0009]

【課題を解決するための手段】上記課題を解決する本発
明の方法は、Pb−Sn−In合金を加熱溶解して合金
融体を形成し、該合金融体の温度を350〜500℃に
維持しつつ、該合金融体に塩化アンモニウムを反応さ
せ、該合金融体中のInをドロスとして分離回収するこ
とを特徴とする。
According to the method of the present invention for solving the above problems, a Pb-Sn-In alloy is heated and melted to form a joint financial body, and the temperature of the joint financial body is adjusted to 350 to 500 ° C. It is characterized by reacting ammonium chloride with the financial instrument while maintaining it, and separating and collecting In in the financial instrument as dross.

【0010】また、前記合金融体の重量の0.1〜1.
0%の塩化アンモニウムを該合金融体に添加し、生成し
たドロスを分離することを、前記合金融体中のInの品
位が所望の値以下になるまで繰り返すことを特徴とす
る。
In addition, 0.1 to 1.
The method is characterized in that 0% ammonium chloride is added to the financial instrument, and the dross produced is separated until the In grade in the financial instrument falls below a desired value.

【0011】[0011]

【作用】本発明の方法は合金構成元素であるPb、S
n、Inと塩素との親和力の差を利用するものである。
すなわち、InはPbやSnと比べて親和力が大きいた
め、Pb−Sn−In合金の融体に塩素を作用させると
InClとなり、ドロスとして分離し融体表面に浮上す
る。
According to the method of the present invention, Pb and S which are alloy constituent elements are used.
This utilizes the difference in affinity between n, In and chlorine.
That is, since In has a greater affinity than Pb and Sn, when chlorine acts on the melt of the Pb-Sn-In alloy, it becomes InCl, which is separated as dross and floats on the surface of the melt.

【0012】塩素源として塩化アンモニウムを使用する
のは、塩化アンモニウムは350〜450℃で分解する
からであり、かつ分解生成物のアンモニアは揮発し、融
体中に蓄積されないからである。
Ammonium chloride is used as the chlorine source because ammonium chloride decomposes at 350 to 450 ° C. and the decomposition product, ammonia, volatilizes and does not accumulate in the melt.

【0013】融体温度を350〜500℃とするのは3
50℃未満では融体の流動性が低く、塩化アンモニウム
とInとの接触、反応が不十分となるからであり、50
0℃を越えると、ドロスとメタルとの分離性が低下し、
InClが揮発損失が大きくなるためである。
It is 3 that the melt temperature is 350 to 500 ° C.
This is because if the temperature is lower than 50 ° C., the fluidity of the melt is low and the contact and reaction between ammonium chloride and In become insufficient.
If the temperature exceeds 0 ° C, the separability between dross and metal will decrease,
This is because InCl has a large volatilization loss.

【0014】塩化アンモニウムの添加量をメタルの重量
の0.1%〜1.0%とするのは、0.1%未満である
と、発生するドロス量が少なく、生産性が低下するから
であり、1.0%を越えると、発生ドロス量が増加し、
ドロス中のIn品位が低下し、次工程でのドロスよりの
Inの回収工程での効率が低下するからである。
The amount of ammonium chloride added is set to 0.1% to 1.0% of the weight of metal because if it is less than 0.1%, the amount of dross generated is small and the productivity is lowered. Yes, if it exceeds 1.0%, the amount of generated dross increases,
This is because the In quality in the dross is lowered and the efficiency in the In recovery process from the dross in the next step is lowered.

【0015】融体中のIn品位が低下してきた場合、得
られるドロス中のIn品位が低下する場合が生じる。こ
の場合には、該ドロスを新規なPb−Sn−In合金融
体に添加してIn品位の高いドロスとすることができ
る。この場合、繰り返すドロス量が融体重量の0.1〜
1.0%であれば新規に塩化アンモニウムを添加する必
要はない。
When the In grade in the melt is lowered, the In grade in the obtained dross may be lowered. In this case, the dross can be added to a new Pb-Sn-In compound financial body to form a dros with a high In quality. In this case, the amount of repeating dross is 0.1 to 10% by weight of the melt.
If it is 1.0%, it is not necessary to newly add ammonium chloride.

【0016】なお、次工程のドロスよりのInの回収で
の効率を考慮すると、ドロス中のIn品位は一般に20
%以上とすることが好ましい。このために、Inのドロ
ス化は、一度に行うより、繰り返し方式を採用したほう
が好ましい。
Considering the efficiency of recovering In from the dross in the next step, the In quality in the dross is generally 20.
% Or more is preferable. For this reason, it is preferable to adopt a repeating method for converting In to dross at once.

【0017】ドロスよりのInの回収は通常の方法によ
り可能であり、例えば過剰の塩酸に溶解し、アルカリに
よりpHを1程度に調整し、Pbと微量のSnとを沈澱
させ、分離して得た溶液にZn粉末等の還元剤を添加
し、Inを析出させる。このようにして得たIn粉をカ
セイソーダと混合し、溶解してInインゴットを得る。
このようにして得たInは、純度が高く、そのまま合金
用添加剤として使用できる。
In can be recovered from the dross by an ordinary method, for example, by dissolving in excess hydrochloric acid, adjusting the pH to about 1 with an alkali, precipitating Pb and a trace amount of Sn, and separating them. A reducing agent such as Zn powder is added to the solution to precipitate In. The In powder thus obtained is mixed with caustic soda and dissolved to obtain an In ingot.
The In thus obtained has a high purity and can be used as it is as an additive for alloys.

【0018】[0018]

【実施例】次に、本発明の実施例について述べるEXAMPLES Next, examples of the present invention will be described.

【0019】[0019]

【実施例1】In10.7%、Sn54%、残部が実質
的にPbからなる合金スクラップ250kgを黒鉛坩堝
に装入し、黒鉛坩堝を電気炉内に入れ、400℃で加熱
溶解した。
Example 1 250 kg of alloy scrap consisting of In of 10.7%, Sn of 54% and the balance substantially of Pb was charged into a graphite crucible, and the graphite crucible was put into an electric furnace and heated and melted at 400 ° C.

【0020】前記スクラップが完全に溶解したことを確
認してから、塩化アンモニウム1.5kgを添加し、十
分に撹はんし、その後静置した。約1時間半後、表面に
形成されたドロスを柄杓ですくい除去した。そして、こ
の撹はん−静置−除去の操作を24回行った。偶数回ご
とに得られたドロスの量とInとSnとPbとの品位、
合金融体のInとSnとPbとの品位を調べ、その結果
を表1に示した。
After confirming that the scrap was completely dissolved, 1.5 kg of ammonium chloride was added, stirred thoroughly, and then allowed to stand. After about one and a half hours, the dross formed on the surface was removed by scooping with a ladle. Then, this stirring-stationary-removal operation was performed 24 times. The amount of dross obtained every even number of times and the quality of In, Sn and Pb,
The grades of In, Sn, and Pb of the joint financial body were examined, and the results are shown in Table 1.

【0021】表1より、回を追うごとにドロス中のIn
品位は低下するものの、14回目までのドロスのIn品
位は20%以上になっている。また、合金融体中のIn
品位を1%以下とするためには22回の繰り返しが必要
であることがわかる。
From Table 1, it can be seen that In
Although the quality deteriorates, the In quality of dross up to the 14th time is 20% or more. In addition, In
It can be seen that 22 times of repetition are necessary to reduce the quality to 1% or less.

【0022】次に、得られたドロスの16〜24回目の
ドロスを用いて以下の試験を行った。すなわち、Sn4
3%、In8.5%、残部がPbからなる合金を400
℃に加熱して溶解し、16回目のドロスを投入し、十分
に撹はんし、1.5時間静置した後、ドロスをすくいと
った。次いで、17回目のドロスを投入し、十分に撹は
んし、1.5時間静置した後、ドロスをすくいとった。
これを24回目のドロスまで繰り返した。得られた各偶
数回目のドロスと合金融体との分析値と発生ドロス量を
表2に示した。
Next, the following tests were carried out using the dross obtained 16th to 24th times. That is, Sn4
400% alloy containing 3%, In8.5% and the balance Pb
The mixture was heated to 0 ° C. to dissolve it, the 16th dross was added, the mixture was thoroughly stirred, and allowed to stand for 1.5 hours, and then the dross was scooped. Then, the 17th dross was added, thoroughly stirred and allowed to stand for 1.5 hours, and then the dross was scooped.
This was repeated until the 24th dross. Table 2 shows the analysis values and the amount of generated dross of the obtained even-numbered dross and the financial institutions.

【0023】表2より、低In品位のドロスを繰り返す
ことにより、高いIn品位のドロスが簡単に得ることが
可能であり、かつ確実に合金融体中のIn品位を低下さ
せうることがわかる。
From Table 2, it can be seen that by repeating the dross having a low In quality, it is possible to easily obtain the dross having a high In quality and surely reduce the In quality in the financial instrument.

【0024】[0024]

【表1】 [Table 1]

【0025】[0025]

【表2】 [Table 2]

【0026】[0026]

【実施例2】実施例1における1回目から4回目までの
ドロスを混合して得たドロス1.5kgに濃塩酸50l
と水とを添加し、室温で撹はんして溶解した。次いで、
未溶解物をろ過分離して146lのろ液を得た。このろ
液に20%の苛性ソーダ溶液を添加し、pHを1.5に
調節した。生成した沈澱を分離除去し、得た液に純度9
9.2%(金属Znの純度97.3%)の亜鉛粉末を撹
はんしつつ1当量添加してInを析出させた。得られた
In粉と0.4kgのNaOHとをステンレスボートに
入れ加熱溶解し、6.7kgの純度99.6%のインジ
ウムインゴットを得た。
Example 2 1.5 kg of dross obtained by mixing the dross from the first time to the fourth time in Example 1 was added to 50 l of concentrated hydrochloric acid.
And water were added and dissolved by stirring at room temperature. Then
The undissolved substance was separated by filtration to obtain 146 l of filtrate. A 20% caustic soda solution was added to the filtrate to adjust the pH to 1.5. The formed precipitate was separated and removed, and the obtained solution was purified to a purity of 9
1 equivalent of zinc powder of 9.2% (purity of metal Zn 97.3%) was added with stirring to precipitate In. The obtained In powder and 0.4 kg of NaOH were put into a stainless steel boat and melted by heating to obtain 6.7 kg of indium ingot having a purity of 99.6%.

【0027】[0027]

【発明の効果】以上示したように、本発明の方法によれ
ば、容易にかつ確実にPb−Sn−In合金スクラップ
よりInをドロスとして分離でき、得られたドロスより
高純度のInを容易に得ることができる。
As described above, according to the method of the present invention, In can be separated easily and reliably from the Pb-Sn-In alloy scrap as dross, and In having a higher purity than the obtained dross can be easily obtained. Can be obtained.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 Pb−Sn−In合金を加熱溶解して合
金融体を形成し、該合金融体の温度を350〜500℃
に維持しつつ、該合金融体に塩化アンモニウムを反応さ
せ、該合金融体中のInをドロスとして分離回収するこ
とを特徴とするPb−Sn−In合金からのInの回収
方法。
1. A Pb-Sn-In alloy is heated and melted to form a combined financial body, and the temperature of the combined financial body is 350 to 500.degree.
A method for recovering In from a Pb-Sn-In alloy, characterized in that ammonium chloride is allowed to react with the financial instrument while maintaining the above, and In in the financial instrument is separated and recovered as dross.
【請求項2】 前記合金融体の重量の0.1〜1.0%
の塩化アンモニウムを該合金融体に添加し、生成したド
ロスを分離することを、前記合金融体中のInの品位が
所望の値以下になるまで繰り返すことを特徴とする請求
項1に記載のPb−Sn−In合金からのInの回収方
法。
2. 0.1 to 1.0% of the weight of the financial institution
2. The method according to claim 1, wherein the ammonium chloride is added to the financial instrument and the dross formed is separated until the In grade in the financial instrument falls below a desired value. A method for recovering In from a Pb-Sn-In alloy.
JP7876492A 1992-03-02 1992-03-02 Method for recovering In from Pb-Sn-In alloy Expired - Lifetime JP3199184B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7876492A JP3199184B2 (en) 1992-03-02 1992-03-02 Method for recovering In from Pb-Sn-In alloy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7876492A JP3199184B2 (en) 1992-03-02 1992-03-02 Method for recovering In from Pb-Sn-In alloy

Publications (2)

Publication Number Publication Date
JPH05247556A true JPH05247556A (en) 1993-09-24
JP3199184B2 JP3199184B2 (en) 2001-08-13

Family

ID=13670973

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7876492A Expired - Lifetime JP3199184B2 (en) 1992-03-02 1992-03-02 Method for recovering In from Pb-Sn-In alloy

Country Status (1)

Country Link
JP (1) JP3199184B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5543031A (en) * 1994-08-19 1996-08-06 Nippon Mining & Metals Co., Ltd. Method for recovering indium by electrowinning and apparatus therefor
JP2012246532A (en) * 2011-05-27 2012-12-13 Panasonic Corp Metal processing method
WO2016111571A1 (en) * 2015-01-08 2016-07-14 주식회사 화류테크 Method for collecting indium and tin using industrial waste

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5543031A (en) * 1994-08-19 1996-08-06 Nippon Mining & Metals Co., Ltd. Method for recovering indium by electrowinning and apparatus therefor
JP2012246532A (en) * 2011-05-27 2012-12-13 Panasonic Corp Metal processing method
WO2016111571A1 (en) * 2015-01-08 2016-07-14 주식회사 화류테크 Method for collecting indium and tin using industrial waste

Also Published As

Publication number Publication date
JP3199184B2 (en) 2001-08-13

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