JPH07188963A - Method for recovering copper from waste copper electrolyte - Google Patents

Method for recovering copper from waste copper electrolyte

Info

Publication number
JPH07188963A
JPH07188963A JP33011693A JP33011693A JPH07188963A JP H07188963 A JPH07188963 A JP H07188963A JP 33011693 A JP33011693 A JP 33011693A JP 33011693 A JP33011693 A JP 33011693A JP H07188963 A JPH07188963 A JP H07188963A
Authority
JP
Japan
Prior art keywords
copper
sulfide
anode
cathode
electrolyte
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.)
Withdrawn
Application number
JP33011693A
Other languages
Japanese (ja)
Inventor
Iwao Iwasaki
巌 岩崎
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials Corp
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 Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP33011693A priority Critical patent/JPH07188963A/en
Publication of JPH07188963A publication Critical patent/JPH07188963A/en
Withdrawn legal-status Critical Current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

Landscapes

  • Electrolytic Production Of Metals (AREA)

Abstract

PURPOSE:To energy-savingly recover high-purity copper from a waste copper electrolyte. CONSTITUTION:The impurities such as Cu, As and Sb in a circulating electrolyte in the electrolytic refining of copper are recovered as the sulfide consisting essentially of copper sulfide by treating the electrolyte with hydrogen sulfide. An electrolytic cell 1 having an anode 4 and a cathode 6 and provided with an anode chamber 3 formed by partitioning the anode 4 at the center with a diaphragm 2 is used, and the recovered sulfide is agitated and anodized by using an aq. sulfuric acid soln. as the electrolyte to deposit pure copper on the cathode 6 which is 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】この発明は粗銅から高純度銅を電
解精製する際に発生する電解廃液から銅を回収する方法
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 recovering copper from electrolytic waste liquid generated when electrolytically refining high-purity copper from crude copper.

【0002】[0002]

【従来の技術】従来一般に、銅電解廃液から銅を回収す
る方法としては図2にフローシートで示される方法が知
られている。この従来方法は図2に示されるとおり電解
廃液を不溶性電極を用い陰極に銅を析出させ電解銅を転
炉や熔錬炉の原料として用いる一方、処理液は脱ニッケ
ル回収ののち硫酸として回収される方法が知られてい
る。
2. Description of the Related Art Conventionally, as a method for recovering copper from a copper electrolytic waste solution, a method shown by a flow sheet in FIG. 2 is known. According to this conventional method, as shown in FIG. 2, electrolytic waste liquid is used as a raw material for a converter or a smelting furnace by depositing copper on the cathode using an insoluble electrode, and the treatment liquid is recovered as sulfuric acid after recovery of nickel. It is known how to

【0003】[0003]

【発明が解決しようとする課題】近年、銅電解設備のの
大型化にともない上記電解廃液処理量も増大する傾向に
あり、上記従来方法において陰極に析出した銅は純度が
低いために転炉や熔錬炉などの原料として用いられるに
すぎず省エネルギー、歩止りの観点から必ずしも望まし
くないのが現状である。
In recent years, there has been a tendency for the amount of electrolytic waste liquid treated to increase with the increase in size of copper electrolysis equipment, and the copper deposited on the cathode in the above-mentioned conventional method has a low purity, so that it can At present, it is only used as a raw material for a smelting furnace or the like, and is not always desirable from the viewpoint of energy saving and yield.

【0004】[0004]

【課題を解決するための手段】そこで、本発明者ら上述
の観点から銅電解廃液から高純度銅を回収する研究を行
った結果図1にフローシートで示されるように銅電解廃
液を硫化水素で処理して液中のCuおよびAs、Sbな
どの不純物を硫化銅を主成分とする硫化物として回収
し、図2の概略縦断面図で示されるように陽極4と陰極
6が設置され、かつ、前記陽極を中央部にて隔膜2で仕
切られた陽極室3が形成された電解槽1を用い、前記回
収硫化物を前記陽極室にて電解液として硫酸水溶液を用
い攪拌処理しながら陽極電解処理すると例えばステンレ
ス鋼製の陰極には99.9%以上の高純度の銅が析出す
るという研究結果を得たのである。
Therefore, the inventors of the present invention conducted a study for recovering high-purity copper from a copper electrolysis waste liquid from the above viewpoints, and as a result, as shown in the flow sheet of FIG. And recover impurities such as Cu and As and Sb in the liquid as sulfides containing copper sulfide as a main component, and the anode 4 and the cathode 6 are installed as shown in the schematic longitudinal sectional view of FIG. In addition, while using the electrolytic cell 1 in which the anode chamber 3 in which the anode is partitioned by the diaphragm 2 at the central portion is formed, the recovered sulfide is stirred in the anode chamber using an aqueous sulfuric acid solution as an electrolytic solution, According to the research result, when electrolytic treatment is performed, for example, 99.9% or more of high-purity copper is deposited on a stainless steel cathode.

【0005】この発明は、上記の研究結果にもとづいて
なされたものであって、銅電解精製における還流電解液
を硫化水素で処理して液中のCuおよびAs、Sbなど
の不純物を硫化銅を主成分とする硫化物として回収し、
陽極と陰極が設置され、かつ、前記陽極を中央部にて隔
膜で仕切られた陽極室が形成された電解槽を用いて前記
回収硫化物を前記陽極室にて電解液として硫酸水溶液を
用い攪拌処理しながら陽極電解処理して、陰極に純銅を
析出させこれを回収することを特徴とするものである。
The present invention has been made based on the above-mentioned research results. The reflux electrolytic solution in copper electrolytic refining is treated with hydrogen sulfide to remove impurities such as Cu and As and Sb from the solution into copper sulfide. Recovered as the main component sulfide,
An anode and a cathode are installed, and the recovered sulfide is stirred using an aqueous sulfuric acid solution as an electrolytic solution in the anode chamber using an electrolytic cell in which an anode chamber is formed by partitioning the anode in the center with a diaphragm. It is characterized in that anodic electrolytic treatment is carried out during the treatment to deposit pure copper on the cathode and recover it.

【0006】[0006]

【実施例】つぎに、この発明方法を実施例により具体的
に説明する。図1に示されるCu:50g/l含有の銅
電解廃液に、硫化水素を吹き込んで硫化銅を主成分とす
る硫化物を沈澱させ、この沈澱物をろ過・乾燥・粉砕し
て硫化物粉末としこの硫化物粉末を図3に示される電解
槽1の陽極室3に装入し、電解槽1の中にpH:2.5
の硫酸水溶液を満たし空気吹き込みパイプ5から空気を
吹き込んで陽極室3内を攪拌した状態で 電流密度:1,500A/m2(陽極表面基準)、 陽極室内粉末濃度:350g/l、 電解時間:8hr の条件で陽極処理を行なうことにより本発明の方法を実
施して、電解槽の側壁に沿って設けたステンレス鋼製の
陰極上に純銅を析出させ、Sを陽極室のスラリー中に残
留させた。
EXAMPLES Next, the method of the present invention will be specifically described by way of examples. Hydrogen sulfide was blown into a copper electrolysis waste liquid containing Cu: 50 g / l shown in FIG. 1 to precipitate a sulfide containing copper sulfide as a main component, and the precipitate was filtered, dried and pulverized to obtain a sulfide powder. This sulfide powder was loaded into the anode chamber 3 of the electrolytic cell 1 shown in FIG.
Of the sulfuric acid aqueous solution and blowing air from the air blowing pipe 5 to stir the inside of the anode chamber 3 Current density: 1,500 A / m 2 (anode surface standard), Powder concentration in the anode chamber: 350 g / l, Electrolysis time: The method of the present invention was carried out by anodizing under the condition of 8 hr to deposit pure copper on the stainless steel cathode provided along the side wall of the electrolytic cell, and to leave S in the slurry in the anode chamber. It was

【0007】また、比較の目的で上記電解廃液を鉛板の
陽極と銅板の陰極を用いて脱銅電解処理を行うことによ
り従来方法を実施して陰極上に電解銅を析出させた。
Further, for the purpose of comparison, the electrolytic waste solution was subjected to decopperization electrolytic treatment using a lead plate anode and a copper plate cathode to carry out a conventional method to deposit electrolytic copper on the cathode.

【0008】[0008]

【発明の効果】この結果本発明法により得られた純銅は
99.96%純度を持つのに対して従来方法で得られた
電解銅は99.1%の純度しか持たないものであった。
上述のように、この発明の方法によれば銅電解廃液から
99.9%以上の高純度の銅を回収することができ、銅
回収の省エネルギー化および歩止りに大いに寄与すると
ころ大である。
As a result, the pure copper obtained by the method of the present invention has a purity of 99.96%, while the electrolytic copper obtained by the conventional method has a purity of only 99.1%.
As described above, according to the method of the present invention, high-purity copper of 99.9% or more can be recovered from the copper electrolysis waste liquid, which greatly contributes to energy saving and yield of copper recovery.

【図面の簡単な説明】[Brief description of drawings]

【図1】 本発明の方法を示す工程図である。FIG. 1 is a process chart showing a method of the present invention.

【図2】 本発明の方法の実施装置を示す概略縦断面図
である。
FIG. 2 is a schematic vertical sectional view showing an apparatus for carrying out the method of the present invention.

【図3】 従来方法を示す工程図である。FIG. 3 is a process drawing showing a conventional method.

【符号の説明】[Explanation of symbols]

1.電解槽 2.隔膜 3.陽極室 4.陽極 5.空気吹き込みパイプ 6.陰極 1. Electrolysis tank 2. Diaphragm 3. Anode chamber 4. Anode 5. Air blowing pipe 6. cathode

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 銅電解精製における還流電解液を硫化水
素で処理して液中のCuおよびAs、Sbなどの不純物
を硫化銅を主成分とする硫化物として回収し、陽極と陰
極が設置され、かつ、前記陽極を中央部にて隔膜で仕切
られた陽極室が形成された電解槽を用いて前記回収硫化
物を前記陽極室にて電解液として硫酸水溶液を用い攪拌
処理しながら陽極電解処理して、陰極に純銅を析出させ
これを回収することを特徴とする銅電解廃液から銅を回
収する方法。
1. A reflux electrolytic solution in copper electrorefining is treated with hydrogen sulfide to recover impurities such as Cu and As and Sb in the solution as a sulfide containing copper sulfide as a main component, and an anode and a cathode are installed. In addition, using an electrolytic cell in which an anode chamber partitioned by a diaphragm in the center of the anode is formed, the recovered sulfide is anodically electrolyzed in the anode chamber while stirring using an aqueous sulfuric acid solution as an electrolytic solution. Then, a method of recovering copper from a copper electrolysis waste liquid, which comprises depositing pure copper on the cathode and recovering it.
JP33011693A 1993-12-27 1993-12-27 Method for recovering copper from waste copper electrolyte Withdrawn JPH07188963A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33011693A JPH07188963A (en) 1993-12-27 1993-12-27 Method for recovering copper from waste copper electrolyte

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33011693A JPH07188963A (en) 1993-12-27 1993-12-27 Method for recovering copper from waste copper electrolyte

Publications (1)

Publication Number Publication Date
JPH07188963A true JPH07188963A (en) 1995-07-25

Family

ID=18228982

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33011693A Withdrawn JPH07188963A (en) 1993-12-27 1993-12-27 Method for recovering copper from waste copper electrolyte

Country Status (1)

Country Link
JP (1) JPH07188963A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030064177A (en) * 2002-01-26 2003-07-31 대한민국(충남대학교) A method of preparing copper powder from waste etchant
CN102534657A (en) * 2012-02-17 2012-07-04 重庆重冶铜业有限公司 Method for treating waste electrolyte in process of producing cathode copper
KR101472464B1 (en) * 2013-08-27 2014-12-15 한국과학기술연구원 Method for Recovering Copper from Wastewater Comprising Copper

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030064177A (en) * 2002-01-26 2003-07-31 대한민국(충남대학교) A method of preparing copper powder from waste etchant
CN102534657A (en) * 2012-02-17 2012-07-04 重庆重冶铜业有限公司 Method for treating waste electrolyte in process of producing cathode copper
KR101472464B1 (en) * 2013-08-27 2014-12-15 한국과학기술연구원 Method for Recovering Copper from Wastewater Comprising Copper
CN104419833A (en) * 2013-08-27 2015-03-18 韩国科学技术研究院 Method for recovering copper from wastewater comprising copper

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A300 Withdrawal of application because of no request for examination

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Effective date: 20010306