JPH0653948B2 - Treatment method of sulfuric acid acidic solution containing bismuth - Google Patents

Treatment method of sulfuric acid acidic solution containing bismuth

Info

Publication number
JPH0653948B2
JPH0653948B2 JP61098685A JP9868586A JPH0653948B2 JP H0653948 B2 JPH0653948 B2 JP H0653948B2 JP 61098685 A JP61098685 A JP 61098685A JP 9868586 A JP9868586 A JP 9868586A JP H0653948 B2 JPH0653948 B2 JP H0653948B2
Authority
JP
Japan
Prior art keywords
sulfuric acid
bismuth
solution containing
electrolytic solution
copper
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.)
Expired - Lifetime
Application number
JP61098685A
Other languages
Japanese (ja)
Other versions
JPS62256982A (en
Inventor
正治 石渡
鋭治 木村
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 JP61098685A priority Critical patent/JPH0653948B2/en
Publication of JPS62256982A publication Critical patent/JPS62256982A/en
Publication of JPH0653948B2 publication Critical patent/JPH0653948B2/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

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  • Water Treatment By Sorption (AREA)
  • Electrolytic Production Of Metals (AREA)

Description

【発明の詳細な説明】 (産業分野) 本発明は銅製錬の電解工程における電解液の硫酸酸性溶
液中に蓄積した不純物のうち、可溶性のビスマスを簡単
な操作で選択的に分離除去する方法に関するものであ
る。
TECHNICAL FIELD The present invention relates to a method for selectively separating and removing soluble bismuth from impurities accumulated in a sulfuric acid acidic solution of an electrolytic solution in an electrolytic step of copper smelting by a simple operation. It is a thing.

(従来技術とその問題点) 銅の電解精製においては、陽極としてのアノード中には
目的金属の銅以外に、金、銀、ニツケル、セレン、テル
ル、ビスマス、砒素、アンチモン等、数多くの金属が含
まれている。そのうち、一部は銅とともに溶出し、一定
濃度以上に蓄積すると、銅とともに析出し、電気銅の品
質を低下させる。そのため、これら溶出不純物を一定濃
度以下に保つため、電解液の浄液が必要となる。
(Prior art and its problems) In electrolytic refining of copper, many metals such as gold, silver, nickel, selenium, tellurium, bismuth, arsenic, and antimony are contained in the anode as the anode, in addition to the target metal copper. include. A part of them elutes with copper, and when they accumulate to a certain concentration or more, they precipitate with copper and deteriorate the quality of electrolytic copper. Therefore, in order to keep these eluted impurities below a certain concentration, it is necessary to purify the electrolytic solution.

従来、銅電解液中のビスマスを分離する方法としては、
銅電解液を鉛などよりなる不溶性陽極を使用して電解
し、脱銅スライムとして除去する脱銅電解法、銅電解液
に炭酸ナトリウムを添加する中和法、電解液中に硫化水
素ガスを吹き込んで硫化物沈殿として除去する硫化物沈
殿法、更には、上記アンチモン等不純物の蓄積した電解
液を濃縮して硫酸銅結晶を晶出せしめ共沈した上記不純
物とともに除去するタンパン製造法などがある。しかし
ながら、これらの方法では、いずれも除去すべき不純物
とともに、それよりはるかに多量の銅が随伴して除去さ
れるため、この銅を回収すべく銅製錬工程の前段に再投
入し、繰り返し処理するなど、不純物の系外除去という
目的からは満足のいくものではなかつた。
Conventionally, as a method for separating bismuth in a copper electrolyte,
A copper electrolytic solution is electrolyzed using an insoluble anode made of lead, etc., and is removed as decoppered slime, a copper removal electrolytic method is neutralized, sodium carbonate is added to the copper electrolytic solution, and hydrogen sulfide gas is blown into the electrolytic solution. There is also a sulfide precipitation method of removing as a sulfide precipitate by the above method, and a method of producing a tampan which removes together with the above-mentioned impurities by concentrating the electrolyte solution in which impurities such as antimony are accumulated to crystallize copper sulfate crystals. However, in each of these methods, a much larger amount of copper is removed together with the impurities to be removed. Therefore, in order to recover this copper, it is re-introduced into the preceding stage of the copper smelting step and repeatedly treated. However, it was not satisfactory for the purpose of removing impurities from the system.

その他の除去方法としては、特開昭55−107793
号公報に、砒素、アンチモン、ビスマスのうち、少くと
も砒素を含有する遊離硫酸700g/以下の硫酸酸性溶
液に塩基性硫酸アンチモンまたは塩基性硫酸ビスマスの
一方又は両者の混合物を添加混合し生成する沈殿を分離
することを特徴とする硫酸酸性溶液中の砒素、アンチモ
ン、ビスマスの除去法、が開示されているが、この方法
は浄液目的物と同種の物質を電解液中に一度に多量に溶
解させるため、操作を誤ると、逆に電解液中の上記不純
物濃度を増加させる危険性がある。
Other removal methods are disclosed in Japanese Patent Laid-Open No. 55-107793.
Precipitation produced by adding and mixing one or both of basic antimony sulfate and basic bismuth sulfate to a sulfuric acid acidic solution containing free sulfuric acid of at least 700 g / arsenic among arsenic, antimony and bismuth. A method for removing arsenic, antimony, and bismuth in a sulfuric acid acidic solution, which is characterized by separating the same, is disclosed, but this method dissolves a large amount of a substance of the same kind as the target substance for purification in the electrolytic solution at one time. Therefore, if the operation is mistaken, there is a danger that the concentration of the impurities in the electrolytic solution is increased.

(発明の目的) 本発明者らは上記の従来技術の問題点を解決し、銅電解
液中に含まれるビスマスを簡単な操作で分離、除去し、
該電解液中のビスマス濃度を低減せしめる硫酸酸性溶液
中のビスマスの除去法を提供すべく検討した結果、活性
炭を電解液と接触させることにより非常に容易に上記目
的を達成しうることを見出し、本発明に到達した。
(Purpose of the invention) The present inventors have solved the above-mentioned problems of the prior art, and separated and removed bismuth contained in the copper electrolytic solution by a simple operation,
As a result of studies to provide a method for removing bismuth in a sulfuric acid acidic solution that reduces the bismuth concentration in the electrolytic solution, it was found that the above object can be achieved very easily by contacting activated carbon with the electrolytic solution. The present invention has been reached.

(発明の構成) すなわち、本発明の要旨とするところは、ビスマスを含
有する硫酸酸性溶液に活性炭を接触させ、該ビスマスを
該活性炭に吸着せしめることを特徴とするビスマスを含
有する硫酸酸性溶液の処理法、にある。
(Structure of the invention) That is, the gist of the present invention is that a sulfuric acid acidic solution containing bismuth is characterized in that activated carbon is brought into contact with a sulfuric acid acidic solution containing bismuth to adsorb the bismuth to the activated carbon. The processing method is in.

本発明において、活性炭を銅電解液と接触させるには、
活性炭をカラムに充填して層状とし、この層を通液させ
る方法によつてもよく、また活性炭を槽中で電解液と撹
拌する方法でもよく、さらにこれら二方法を併用しても
よい。又活性炭と接触する電解液温度は通常の電解温度
の60℃でもよいが、活性炭による作用はビスマスの吸
着であるので液温は60℃以下が好ましい。
In the present invention, to bring the activated carbon into contact with the copper electrolyte,
A method may be used in which a column is filled with activated carbon to form a layer, and this layer is passed through. Alternatively, the activated carbon may be stirred with an electrolytic solution in a tank, or these two methods may be used in combination. The temperature of the electrolytic solution in contact with the activated carbon may be 60 ° C. which is a normal electrolysis temperature. However, the action of activated carbon is the adsorption of bismuth, so the temperature of the electrolytic solution is preferably 60 ° C. or lower.

次に、本発明を実施例によつて具体的に説明する。Next, the present invention will be specifically described with reference to examples.

以下の実施例は本発明の範囲を限定するものではない。The following examples do not limit the scope of the invention.

実施例1 Cu42g/,Ni15g/,As5.1g/,S
b480mg/,Bi93mg/,遊離硫酸210g/
の銅電解液200mlを300mlの活栓つきの三角フラ
スコに採り、それぞれの該三角フラスコに異なる活性炭
を20g添加し、24時間撹拌した。この撹拌処理は6
0℃の恒温槽中に浸漬して行なつた。処理後の電解液中
のビスマスの分析を行い、得られた結果は第1表に示
す。
Example 1 Cu 42 g /, Ni 15 g /, As 5.1 g /, S
b480mg /, Bi93mg /, free sulfuric acid 210g /
200 ml of the copper electrolytic solution of 1 was placed in a 300 ml Erlenmeyer flask with a stopcock, 20 g of different activated carbon was added to each Erlenmeyer flask, and the mixture was stirred for 24 hours. This stirring process is 6
The test piece was immersed in a constant temperature bath at 0 ° C. Bismuth in the electrolytic solution after the treatment was analyzed, and the obtained results are shown in Table 1.

実施例2 実施例1と同様の方法により、実施例1と同様な組成の
電解液を液温40℃,60℃,80℃と変化させ、ツル
ミコール製粉末活性炭を各々20g添加し、恒温槽中で
24時間撹拌し、処理後の電解液中のビスマスの分析値
を第2表に示す。
Example 2 By the same method as in Example 1, the electrolytic solution having the same composition as in Example 1 was changed to a liquid temperature of 40 ° C., 60 ° C., 80 ° C., 20 g of each of Tsurumi Coal powder activated carbon was added, and the mixture was placed in a constant temperature bath. Table 2 shows the analytical values of bismuth in the electrolytic solution after stirring for 24 hours.

以上の結果から明らかなように、本発明によつて、ビス
マスを簡便に他元素との選択性がよく分離することが可
能である。
As is clear from the above results, according to the present invention, it is possible to easily separate bismuth from other elements with good selectivity.

(発明の効果) 本発明は上記構成をとることによつて、次の効果を示
す。
(Effects of the Invention) The present invention having the above-described configuration exhibits the following effects.

(1)活性炭と電解液を接触するのみであるので従来の中
和法のように、遊離硫酸の消費、異種金属の液中への混
入がない。
(1) Since the activated carbon and the electrolytic solution are only brought into contact with each other, there is no consumption of free sulfuric acid and mixing of different metals into the solution unlike the conventional neutralization method.

(2)電解液の浄液対象がビスマスの場合、本発明により
ビスマスを除去した液は全量もしくは一部をそのまま電
解工程に送ることができ、丹パン製造工程や脱銅電解工
程の負荷を軽減できる。
(2) When the purification target of the electrolytic solution is bismuth, the solution from which bismuth has been removed according to the present invention can be sent to the electrolysis process as it is or in part, reducing the load of the Danpan manufacturing process and the decoppering electrolysis process. it can.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ビスマスを含有する硫酸酸性溶液に活性炭
を接触させ、該ビスマスを該活性炭に吸着せしめること
を特徴とするビスマスを含有する硫酸酸性溶液の処理
法。
1. A method for treating an acidic sulfuric acid solution containing bismuth, which comprises contacting activated carbon with an acidic sulfuric acid solution containing bismuth to adsorb the bismuth on the activated carbon.
JP61098685A 1986-04-28 1986-04-28 Treatment method of sulfuric acid acidic solution containing bismuth Expired - Lifetime JPH0653948B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61098685A JPH0653948B2 (en) 1986-04-28 1986-04-28 Treatment method of sulfuric acid acidic solution containing bismuth

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61098685A JPH0653948B2 (en) 1986-04-28 1986-04-28 Treatment method of sulfuric acid acidic solution containing bismuth

Publications (2)

Publication Number Publication Date
JPS62256982A JPS62256982A (en) 1987-11-09
JPH0653948B2 true JPH0653948B2 (en) 1994-07-20

Family

ID=14226361

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61098685A Expired - Lifetime JPH0653948B2 (en) 1986-04-28 1986-04-28 Treatment method of sulfuric acid acidic solution containing bismuth

Country Status (1)

Country Link
JP (1) JPH0653948B2 (en)

Also Published As

Publication number Publication date
JPS62256982A (en) 1987-11-09

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