JPS60500453A - Method for adding thioureas to electrolytic solutions useful for copper smelting - Google Patents

Method for adding thioureas to electrolytic solutions useful for copper smelting

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Publication number
JPS60500453A
JPS60500453A JP58501347A JP50134783A JPS60500453A JP S60500453 A JPS60500453 A JP S60500453A JP 58501347 A JP58501347 A JP 58501347A JP 50134783 A JP50134783 A JP 50134783A JP S60500453 A JPS60500453 A JP S60500453A
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thioureas
copper
concentration
electrolyte
refining
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JPS6230271B2 (en
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ゴツフマン,マーチン
ジヨーダン,トーマス・エル
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アサ−コ・インコ−ポレ−テッド
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/12Electrolytic production, recovery or refining of metals by electrolysis of solutions of copper

Abstract

Method for electrolytically refining copper involving precise control of the thiourea concentrations in the copper sulfate, sulfuric acid solution used in the refining whereby improvements are obtained in tankhouse current efficiencies and the quality of the refined copper deposited on the cathodes. Sufficient thiourea is added to the electrolyte feed so that at least above trace quantities are measured in the electrolyte outflow.

Description

【発明の詳細な説明】 銅精錬用に有用な電解溶液にチオ尿素類の添加方法背景技術 本発明は銅の電解精錬、より詳細には銅の精錬に際し電解液中に有効なチオ尿素 類濃度を常に維持するための方法に関する。[Detailed description of the invention] Background technology for adding thioureas to electrolytic solutions useful for copper refining The present invention relates to the electrolytic refining of copper, and more specifically, to the electrolytic refining of copper. The present invention relates to a method for constantly maintaining the concentration of substances.

伝統的に銅は、電流が不純な銅の鋳造陽極とめつきされた実質的に純粋な銅析出 物を有する陰極(陽極および陰極双方とも適切な電解液に浸漬されている)の間 を伝達される方法で精製されている。当技術分野で一般に受け入れられている電 解液は硫酸銅および硫酸の水溶液である。この精錬法では、まず不純な陽極泥が 電解液に済解し、次いで鋼イオン(Cu ” )を近くの陰極に伝達し、ここで 銅がほとんど純粋な金属Cu”として析出する。一定期間ののち希望する厚さの 銅が陰極上に析出し、そこでこれらは取出され、のちに数種の常用される製品の 形状に鋳造するために6融される。Traditionally copper is a substantially pure copper deposit plated with an impure copper cast anode. between the cathode (both anode and cathode are immersed in a suitable electrolyte) with It has been purified in a manner that conveys it. Generally accepted in the art The solution is an aqueous solution of copper sulfate and sulfuric acid. In this refining method, impure anodic mud is first into the electrolyte and then transfer the steel ions (Cu '') to the nearby cathode, where they are Copper is deposited as almost pure metal Cu''. After a certain period of time, the desired thickness is deposited. Copper deposits on the cathode, where they are extracted and later used in several commonly used products. 6 melted to cast into shape.

この操作に際して幾つかの問題が生じ、結果的にこれらが広範な研究の課題とな った。エネルギー費は上昇し続けるので、電解精錬における電流効率を増大させ ることの重要性は主要な要件となった。大規模な近代的な銅電M精錬所において 電流効率が1チ変化す乞と銅容量が実質的に増大し、あるいは生産1単位当たり の電気量を減少させることができる。さらに、電流効率を犠牲にすることなくよ り高いタンクハウス電流密度で操作することが望まし〜・。このような改良によ れば、銅および幾つかの望ましい副生物たとえば銀かより大量にかつより速かに 2 回収され、また交代作業の必要性も低下するので労務費が低下するであろう。Several problems arise in this operation, which have resulted in the subject of extensive research. It was. As energy costs continue to rise, increasing current efficiency in electrolytic refining is essential. The importance of ensuring safety became a key requirement. In a large modern copper and metal smelter If the current efficiency changes by 1 inch, the copper capacity increases substantially, or per unit of production. The amount of electricity can be reduced. In addition, the current efficiency can be improved without sacrificing current efficiency. It is desirable to operate at a higher tankhouse current density. Such improvements the copper and some desirable by-products, such as silver, in larger quantities and more rapidly. 2 Labor costs will be lower because of increased recovery and less need for shift work.

各種添加剤、たとえば米国特許第2,660,555号おXび第3.389.0 64号明細書に記載されたものが、陰極上に沈積した銅の品質改良に役立った。Various additives, such as U.S. Patent Nos. 2,660,555 and 3.389.0. No. 64 was used to improve the quality of the copper deposited on the cathode.

特にグルーであるアビトン(Avitone)とチオ尿素の組合せ(以下1チオ 尿素類1とは純粋なまたは商業用のチオ尿素、ならびにチオ尿素基金含む大部分 の有機化合物、たとえば米国特許第3,389.064号明細書に記載されたも のを表わすものと解される)全添加すると、むらのない密な、かつ均一な陰極銅 析出物の生成が促進されることが認められた。この徨の添加物全使用しない場合 、陰極上に析出する銅は1小塊(aadule)“ 全形成しやすく、これは不 規則な樹状に生長し、操作中にしばしば有害な短絡を生じる。また陰極における 溝状の生長である大きな“縦じわ(5triation ) ’が電解液中に存 在する不純物を捕捉する可能性があシ、これは特に不純物濃度(殊にチオ尿素濃 度と考えられている)が電解液中で不都合な水準にまで上昇した場合に危険であ る。In particular, the combination of glue Avitone and thiourea (hereinafter referred to as 1 thiourea) Ureas 1 are pure or commercial thioureas, as well as most thioureas, including thiourea foundations. organic compounds such as those described in U.S. Pat. No. 3,389.064. (understood as representing the It was observed that the formation of precipitates was promoted. If you do not use any of these additives , the copper deposited on the cathode tends to form a single adule. It grows in a regular dendritic pattern and often causes harmful short circuits during operation. Also at the cathode Large “vertical wrinkles” (5triations), which are groove-like growths, exist in the electrolyte. There is a possibility of trapping existing impurities, especially at impurity concentrations (particularly thiourea concentrations). dangerous if the electrolyte (considered to be Ru.

添加物の使用により生じた問題は、精錬用タンクハウス中の最適操作濃度全速や かにかつ適確に定めなければならないこと、まためっき操作中にいかにして電流 効率金高めるかということであった。米国特許第3,389.064号明細書で は電解液中における記載された添加物の化学は明らかにさルておらず、むしろ添 加剤は電解精錬操作中に使いつくされてしまうであろうと推定している。しかし タンクハウス精錬金含めていかなる大規模の商業的操作においても、効果的な操 作に変数の数に依存するであろう。従って系全最大操作条件下に一定の状態で稼 動させ続けるためには、系内の決定的パラメーターを速やかにかつ適確に測定し く旧式な試行錯誤による再調整にたよることなく)、かつ銅の精錬全行うべき添 加物濃度範囲全定める方法全見出すことが望ましい。The problems caused by the use of additives are the optimum operating concentration in the smelting tank house and the It must be determined precisely and accurately, and how the current The idea was to increase efficiency. In U.S. Patent No. 3,389.064 does not clarify the chemistry of the listed additives in the electrolyte, but rather It is estimated that the additive will be used up during the electrolytic refining operation. but In any large-scale commercial operation, including tankhouse refining, effective operation is essential. The production will depend on the number of variables. Therefore, the system operates under constant conditions under the overall maximum operating conditions. To keep the system running, critical parameters within the system must be measured quickly and accurately. (without resorting to old-fashioned trial-and-error readjustments) It is desirable to find a method for determining the entire additive concentration range.

発明の目的 従って本発明の利点は、銅の電解精錬に用いられる改良法が提供されることであ る。Purpose of invention Therefore, an advantage of the present invention is that it provides an improved method for use in the electrolytic refining of copper. Ru.

本発明の他の利点は、電流効率を高め、従って操簗費および労働硬性を少なくす る改良された銅の電解精錬法が提供されることである。Another advantage of the invention is that it increases current efficiency and thus reduces cane handling costs and labor intensity. An improved copper electrolytic refining method is provided.

本発明の他の利点は、゛電解夜中の柚々の濃度のチオ尿素類が陰極析出した銅の 品質にどのような影響全厚えるかが判定されることである。Another advantage of the present invention is that thioureas at a concentration similar to that of the cathodically deposited copper during the electrolytic process are It is to be determined what effect the total thickness will have on the quality.

発明の要約 これらおよび他の本発男の利点は、硫酸および硫酸鋼、ならびに少重量の添加剤 (そのうち1種はチオ尿素類である)を官有する銅精錬用電解液全調製し、該電 解液がめつきに際して、流入液流および流出液流の導通手段全経由する電解液の 流入液流♂よび流出液流の双方全備えた適切な容器手段中に存在し;チオ尿素類 の流出液流中濃度全会なくとも痕跡濃度以上の値、すなわち少なくとも測定可能 な量に維持するのに十分な量のチオ尿素を流入液流に添加し、その際流出液流中 の最大許容濃度はそれ以上では陰極析出した銅への混入が有意となる値、すなわ ちそれ以上では電解液中に存在する不純物が析出した銅の品質に物質的影響を与 える値であり、そして銅全容器手段中で電解精錬する間、以上全会なくとも周期 的に反復することよりなる、銅の電解精錬のだめの改良された方法によって達成 される。Summary of the invention These and other advantages of Honka Dan are made from sulfuric acid and sulfuric acid steel, as well as low weight additives. (one of which is thioureas) was prepared completely, and the electrolyte solution for copper refining containing When the electrolyte is plated, the electrolyte passes through all the inflow and outflow conduction means. in suitable container means with both an inlet stream and an effluent stream; thioureas; The concentration in the effluent stream should be at least as high as the trace concentration, i.e. at least measurable. Sufficient thiourea is added to the influent stream to maintain a The maximum permissible concentration of Above this point, impurities present in the electrolyte will have a physical effect on the quality of the deposited copper. and during electrolytic refining in a copper vessel means at least a period of Achieved by an improved method of electrolytic refining of copper, consisting of repeated be done.

図面の簡単な説明 M1図A、Bは電解槽中に陽極と陰極全電気的に交互に配置した2棟の別法の概 観全示す。Brief description of the drawing M1 diagrams A and B show the outline of an alternative method in which the anode and cathode are placed alternately in an electrolytic cell. Full view.

第2図はタンクハウスが単一セクションからなる銅電解液循環サイクルを示す。Figure 2 shows a copper electrolyte circulation cycle in which the tank house consists of a single section.

発明の詳細な記述 今日製造されるすべての銅のうち約95%は採掘された鉱石の状態から最終製品 への加工中に電解により精製されると推定される。電解精錬はまず陽極から不純 な銅を化学的に溶出し、次いで溶出した銅全天質的に純粋な形で陰極上に選択的 にめつさする方法である。従ってこの棟の方法は2つの目的に役立つ。detailed description of the invention Approximately 95% of all copper produced today goes from mined ore to the final product. It is estimated that it is purified by electrolysis during processing. Electrolytic refining first removes impurities from the anode. The copper is chemically eluted and then the eluted copper is selectively deposited in its qualitatively pure form onto the cathode. This is a way of looking at it. This method of building therefore serves two purposes.

すなわちこれは銅の電気的特性および機械的特性に有害な不純物全実質的に除去 し、また価値のある不純物11から分離し、これ全経済的に実用性がある場合に は副生物として回収できるか、さもなければ廃棄する。i.e. it virtually eliminates all impurities that are detrimental to the electrical and mechanical properties of copper. and separated from valuable impurities11, if this is economically practical. can be recovered as a by-product or otherwise disposed of.

今日工業的タンクハウスで行われている電解精錬はほとんど例外なく“多11ま たは0平行”基金用いて行われており、この場合、各電解槽中の陽極および陰極 は電気的に平行な配列で間に挿入されている。図IAおよびIBには、陽極−陰 極および槽の結線全配置する2槙の別法が示されている。各実施態様において個 々の槽中の陽極2A、2Bはすべである電位で活性化され、一方すべての陰極4 A、4Bはこれよりも低い第2の電位にある。各陽極2A、、2Bはすべての陽 極が実質的に均一な速度で溶解するように、2種の陰極4A、4Bの間に配置さ れる。The electrolytic refining that takes place today in industrial tankhouses is almost without exception In this case, the anode and cathode in each electrolytic cell are are inserted between them in an electrically parallel arrangement. Figures IA and IB show anode-cathode Two alternative methods of arranging the pole and cell connections are shown. In each embodiment, The anodes 2A, 2B in each bath are all activated at a potential, while all the cathodes 4 A and 4B are at a second potential lower than this. Each anode 2A, 2B placed between the two cathodes 4A, 4B such that the poles dissolve at a substantially uniform rate. It will be done.

各種は電気的に順次接萩されてセクション全形成し、一般に約20〜45個の検 力・らなる各でクションは留錬タンクハウスの分離した別個の部分(モジュール )全構成し、これは電極の挿入および取出し、檜の底部からの陽極残量の洗浄な どの操作ならびに維持!務のために他のセクションから電気的および化学的に分 離されていてもよい。Each species is electrically grafted in sequence to form a complete section, typically about 20 to 45 specimens. In each case, the power and ramifications are separated and distinct parts (modules) of the ruren tank house. ) This includes inserting and removing the electrode, and cleaning the remaining amount of anode from the bottom of the cypress. Which operation as well as maintenance! electrically and chemically separated from other sections for They may be separated.

近接する各種は順次ぞの隣凄員子と接続しており、各槽中の陰極はすべて隣接す る槽中の陽極と直接に接続している。すなわち同一電位にある。Each type of adjacent tank is connected to its adjacent member in turn, and all cathodes in each tank are connected to each adjacent member. It is directly connected to the anode in the tank. That is, they are at the same potential.

今日鋼の精錬V(用いられる電解液は鋼40〜50 g/e、および硫酸175 〜225g/L ならびに少駿の不純′吻(王としてニッケル、ヒ素、鉄および アンチモン)の水溶液である。Today's steel refining V (the electrolyte used is 40-50 g/e of steel and 175 ~225g/L and Shaojun's impurity (nickel, arsenic, iron and antimony).

スチームヒーターが浴夜全精錬漕の入口において約60〜65℃の温度に保ち、 電解液が銅の処理中に槽金循環するのに伴ってその温度は出口において約55〜 60℃に低下する。槽の内および外に2ける電解液の流速あるいは循環によって 一般的な大型の工業用の漕はその電解液全5〜6時間毎に1回再循環させる。こ のような循環は幾つかの理由から必須である。その1つは溶解した不純物金瘤外 へ輸送すること、および電極の表面における均−fL鋼イオン#度を保証するこ とである。A steam heater maintains the temperature at approximately 60 to 65 degrees Celsius at the entrance of the entire bathhouse refining tank. As the electrolyte circulates during copper processing, its temperature at the outlet ranges from about 55 to The temperature drops to 60°C. Depending on the flow rate or circulation of the electrolyte in and out of the cell A typical large industrial tank recirculates its electrolyte once every 5 to 6 hours. child Such a cycle is essential for several reasons. One of them is dissolved impurities outside the gold knob. transport to the surface of the electrode and ensure a uniform -fL steel ion density at the surface of the electrode. That is.

電解液は、性能全改善するためにこれに添加される数棟の1添加剤′全含む。こ れらの添加剤が電解液に混入さ7’1.、tい場6 合、最終的なめつきされた銅析出物は柔らかくなるがまたは粗結晶質の析出物と なるであろう。陰極上の銅“小塊“の生長(しばしばこれらが近接する陽極に接 触するまで生長し、従って短絡音生じる)が促進され、これらを@シ除くために 付加的な人力全必要とし、またタンクハウス電流効it低下させるでるろう。今 日稽錬所で用いられる一般的添加物は骨にかわ、カゼイン氷解物、スル丁ン化し た本部繊維たとえばゴーラック(goulac )、ビンダレン(bindar ene)およびリグノン(l ignon)、ならびに石油りカー(petra 上eum 1iquor)、特に7アビトyA”として昶られているものである 。精錬電位の最適化にきわめて重要であることが認められているこの種の添加物 の一つは、チオ尿素を制御された量使用することである。ここで用いられるチオ 尿素類とは、チオ尿素核−rfLわち全含む有機化合物子べて、特に商業的に純 粋なまたは商業用のチオ尿素全意味する。The electrolyte contains several additives that are added to it to improve its overall performance. child These additives are mixed into the electrolyte 7'1. ,t field 6 In this case, the final plated copper deposit will be soft or coarsely crystalline. It will be. Growth of copper “nodules” on the cathode (often when these touch the adjacent anode) grow to the touch, thus producing a short circuit sound), and in order to eliminate these It would require additional manpower and also reduce tank house current efficiency. now Common additives used at Nikkei Renjo include bone glue, casein melt, and sultinized Motobu fibers such as goulac, bindar ene) and lignon, and petroleum oil (petra) 7 abitoyA" . Additives of this type have been recognized as being of vital importance in optimizing the refining potential. One is to use controlled amounts of thiourea. Thio used here Ureas are all organic compounds containing the thiourea nucleus -rfL, especially those that are commercially pure. All means stylish or commercial thiourea.

しかし含まれるチオ尿素の量が少ないため(通常は電解質の兜)また特に電解液 中におけるこれらの濃度を測定することが困難なため、i@精錬叡中におけるチ オ尿素の挙動は実質的に未知である。特に、タンクハウス操作中にチオ尿素が消 費される速度、凍にの濃度水準のチオ尿素が析出した銅陰極に与える影響、およ び電解液中の不純物濃度が上昇することによる影響はきわめて興味深い。工業界 では伝統的に、小塊および縦じゎの生長を制御する様式%電流効率の改善、なら びに陰極上に析出した銅の品質において、きわめて非科学的に操作されてきた。However, due to the small amount of thiourea it contains (usually in the electrolyte) and especially in the electrolyte Because it is difficult to measure these concentrations in The behavior of urea is virtually unknown. In particular, thiourea is depleted during tankhouse operation. The rate at which thiourea is consumed, the effect that thiourea has on the deposited copper cathode at a concentration level of The effects of increasing the impurity concentration in the electrolyte and electrolyte are of great interest. industry Traditionally, if the method of controlling the growth of nodules and vertical stripes is to improve the % current efficiency, then The quality of the copper deposited on the cathode has been very unscientifically manipulated.

従ってこれら種々の現象をよシ良く理解し、かつ制卸する方法全考案することが 工業界の目標であった。Therefore, it is important to understand these various phenomena better and devise ways to control them. This was the goal of industry.

このよう左方法が見出された。82図を見ることによpその広い実施態様が最も 良く理解される。ごルはタンクハウス精錬が単一セクションからなる概略工程図 でちる。ミキサータンク2は精錬工程用のチオ尿素類の供給源として、また他の 数棟の添加剤および添加物である塩類の供提源として用いられる。チオ尿素類は 用いられるシステムのi面々の型に応じて連続的に、または定期的にN解夜に添 加することができる。タンク2のチオ尿素類は管その他の適切な流通手段4を経 由し、流通調節器6全通過して、ここで管8の電解液の主循環に加わる。この様 式で添加されるチオ尿素類の量を調節することにより、管8中のチオ尿素類の流 入液流中濃度は一般に約8oo〜2500ppb、最も一般的には約1500〜 2000 ppbに保持される。This is how the left method was discovered. By looking at Figure 82, its widest embodiment is the most well understood. A schematic process diagram of tank house refining consisting of a single section. Dechiru. Mixer tank 2 serves as a source of thioureas for the refining process and also for other purposes. It is used as a source of additives and additive salts. Thioureas are Continuously or periodically depending on the type of system used can be added. The thioureas in tank 2 are passed through pipes or other suitable distribution means 4. It then passes through the flow regulator 6, where it joins the main circulation of the electrolyte in the tube 8. Like this The flow of thioureas in tube 8 can be adjusted by adjusting the amount of thioureas added with the formula Concentrations in the incoming stream generally range from about 8oo to 2500 ppb, most commonly from about 1500 to Maintained at 2000 ppb.

しかし流入液流中濃度は各タンクハウス部分からのチオ尿素類の流出液流中濃度 が少なくとも痕跡濃度で、すなわち少なくとも測定可能な、量、好ましくは少な くとも約100 ppb存在するような範囲になければならない。意外にも、適 切であると考えられていたよりも高い水推のチオ尿素類全流入液流中に用いて有 害な結果を生じないことが見出された。特に5000 ppb程度のチオ尿素類 全流入液流中に用いて満足すべき結果が得られた。これは全く予想外であった。However, the concentration in the influent stream is the concentration of thioureas in the effluent stream from each tank house part. in at least a trace concentration, i.e. at least a measurable amount, preferably a small It should be in a range such that at least about 100 ppb is present. Surprisingly, suitable It is possible to use thioureas in the total influent stream at a higher water pressure than was thought to be necessary. It has been found that there are no harmful consequences. Especially about 5000 ppb of thioureas Satisfactory results were obtained using the entire influent stream. This was completely unexpected.

このような高水準のチオ尿素類(は特にチオ尿素類中に存在するイオウが混入す ることにより析出した銅陰極に損傷を与んると考えられていたからでるる。These high levels of thioureas (particularly due to the contamination of sulfur present in thioureas) This was because it was believed that this would damage the deposited copper cathode.

しかしこのように憂い水準で操作することにより経済的利点その他の利点は得ら れない。However, there are no economic or other benefits to be gained by operating at such alarming levels. Not possible.

第2図を参照すると、次いで電解液+ま多数の漕12に分割さルたセクションな いしはモジュール10に入る。各漕は第1図に示された様式の構造全もつ。しか し°ハかなる適切な漕lいしはタンクハウスのデザインも本発明方法に用いるこ とができ、単一セクションのみ金剛いるこのタンクハウスのデザイン(ζ分析を 温源Kjるために用いられる。電解液はセクション10r循環し、不純な陽極全 純粋な銅陰極に電解相線することに関与したのち、排出管14を経て排出される 。電解液中のチオ尿素類の流出液流中濃度は、オリフィス16で試料を採取し、 次・5)てこの試料全測定手段18で測定することにより測定さ几る。Referring to FIG. I enter module 10. Each row has a complete construction in the manner shown in FIG. deer However, any suitable boat or tank house design may also be used in the method of the present invention. With this tankhouse design (ζ analysis) there is only a single section It is used for heating the temperature source Kj. The electrolyte is circulated in section 10r, and all impure anodes are After participating in the electrolytic phase conduction to the pure copper cathode, it is discharged through the discharge pipe 14. . The concentration of thioureas in the electrolyte in the effluent stream is determined by taking a sample at the orifice 16, Next, 5) Measurement is carried out by measuring the whole sample using the lever measuring means 18.

流出液流中濃度全迅速にかつ正確に測定し、系の変更全速かに行うことができる 限り、御1足手段の位置は重要でない。Concentrations in the effluent stream can be measured quickly and accurately, and changes in the system can be made quickly. As long as the position of the foot means is not important.

水差パルスポーラログラフイー(d、iff、=rential pulsep olarography、 DPP) として知られている分析技術によシミ解 裂のチオ尿素類の赤変′(il−測定することが好ましい、、ボーラロラフとし て知られている分析装置筺、たとえばE G&G−プリンス トン・アプライド ・リサーチ・モデル≠384(プリンストン・アプライド・リサーチ社にュージ ャージー州プリンストン)によ、!7現在市販されており、その操作法は刊行物 EG&、Gプリンストン・アプライド・リサーチ社分析機器部門アプリケーンヨ ンノートP−2に記載されて2す、その記載上参考のため引用する)を用いるこ とにより%またこの機器を他の参照電極の挿入によってすなわちそこで推奨され ているAg−Ag(J電極の代わシにKNO3参照電極を用いることによって改 変することにより、100 ppb程度のチオ尿素類の濃度全記録することがで きる。タンクハウスの電解液は1/1o濃度に希釈して分析される。電解液全希 釈する理由は、存在する他の添加物、特に塩素による分析妨害?除くためである 。ポーラログラフの読みを最もよくディスプレーするため、ポーラログラフは約 2〜5mV/秒の遅い走査速度、および25mVのパルス高さの状態に設定する ことが好ましい。この手法によれば約100 J)pbの低さにまで正確な濃度 の読みが得られる。これは、製造業者は反対のことを上張しているが、この機械 の操作につき推奨された方法では達成できない。しかし適切なポーラログラフは いずれも直ちに本発明方法に用いるために退会させることができ、この程度のチ オ尿素類濃度を迅速にかつ正確にめることができる他の測定手段はいずれも本発 明方法に十分に適している。ただし現在は市販されていないと考えられる。water difference pulse polarography (d, if, = rential pulsep Analyzing stains using an analytical technique known as olaography (DPP) It is preferable to measure the red color of thioureas in the fission (IL), Analyzer housings known as ・Research model≠384 (published by Princeton Applied Research) Princeton, Jersey)! 7 Currently commercially available, its operating method is described in publications. EG&G Princeton Applied Research Company Analytical Instruments Department (quoted for reference in the description) and by % also this equipment by the insertion of other reference electrodes i.e. there is recommended Ag-Ag (modified by using KNO3 reference electrode instead of J electrode) By changing the temperature, it is possible to record the entire concentration of thioureas of about 100 ppb. Wear. The electrolyte in the tank house is diluted to 1/1o concentration and analyzed. Fully dilute electrolyte Is the reason for the analysis interference due to other additives present, especially chlorine? This is to remove . To best display the polarograph reading, the polarograph should be approximately Set to a slow scan rate of 2-5 mV/s, and a pulse height of 25 mV. It is preferable. This method allows accurate concentrations down to approximately 100 J) pb. The reading is obtained. This means that although the manufacturer claims to the contrary, this machine cannot be achieved using the recommended method for operation. But a proper polarograph is Both can be immediately withdrawn for use in the method of the present invention, and Any other measurement method that can quickly and accurately determine the concentration of ureas is based on this invention. It is well suited for the light method. However, it is thought that it is not currently commercially available.

意外にもチオ尿素類の流出液中濃度がり/クハクス効率を最適化する際に重要な パラメーターであることが見出された。より詳細には、少なくとも痕跡濃度の値 の濃度の、すなわち少なくとも測定可能な量、好ましくは約100 ppb 以 上のチオ尿素類の流出液中濃度によシ、電流効率が増大し、いっそうむらのない 陰極が得られ、陽極と陰極の間の短絡が減少し、また陰極中の不純物濃度がより 低くなる。Surprisingly, the concentration of thioureas in the effluent increases/is important when optimizing the efficiency of thioureas. It was found that parameters. More specifically, at least trace concentration values i.e. in at least a measurable amount, preferably about 100 ppb or less. The concentration of the above thioureas in the effluent increases the current efficiency and makes it more uniform. The cathode is obtained, the short circuit between the anode and the cathode is reduced, and the impurity concentration in the cathode is more It gets lower.

循環する電解液は試料が16で採取されたのち、管20を経10 て流れ、タンク22に入る。これは新鮮な電解液、jなわちCu5O4およびH 2SO4の供給源として用いられる。新鮮な電極iはタンク22全出ると管24 およびポンプ送り手段26を通過して熱交換器30および青28に入る。これは 電解液の温度を約65℃にまで高め、そこで液体は管32を経て排出され、ヘッ ドタンク34に入り、これから出る。電解液は次いでチオ尿素類および他の添加 剤を補充されたのちセクション10に入り、サイクルは限りなく続く。この方法 の笑顔に際して、他の多くの再循環機構および付随する装置も本発明の範囲に入 ること全強調すべきである。電解液が排出液流中のチオ尿素類の含量全測定され たのち流入液流において希望する量のチオ尿素を補充されるまでの電解液の処理 法は、本方法の決定的部分を構成するものではないからである。The circulating electrolyte is passed through the tube 20 at 10 after the sample is taken at 16. and flows into tank 22. This is a fresh electrolyte, i.e. Cu5O4 and H Used as a source of 2SO4. When the fresh electrode i is completely discharged from the tank 22, the pipe 24 and passes through pumping means 26 into heat exchanger 30 and blue 28. this is The temperature of the electrolyte is increased to approximately 65°C, at which point the liquid is discharged through tube 32 and into the head. Enter Dotank 34 and leave now. The electrolyte is then added with thioureas and other additions. After replenishing the agent, section 10 is entered and the cycle continues indefinitely. this method Many other recirculation mechanisms and associated devices also fall within the scope of this invention. This should be fully emphasized. The total content of thioureas in the electrolyte stream was determined. Treatment of the electrolyte until it is subsequently replenished with the desired amount of thiourea in the influent stream. This is because the law does not constitute a decisive part of the method.

本発明の好ましい形態は、タンクハウスその他の適切な容器手段中で行われ、そ の改良点が電解液流出液流中のチオ尿素類の濃度全適切な測定手段によp(好1 しくは示差パルスポーラログラフイーにより)測定し、流出液流中濃度が希望す る範囲内にとどまるのに有効な量のチオ尿素#全流入液流Vこ添加することによ りチオ尿素類の濃度を再調整し、その範囲はそれ以上では不純物が銅陰極中に現 われる最大値およびそれ以下では小塊形成が促進される少なくとも測定可能fL 量、好ましくは約100 ppbである最小濃度を有し;上記の方法を周期的に 繰り返し、これによf)測定されたチオ尿素類の流出液流中濃度がこれらの最大 値と最小値の間、好ましくは一般的な電解相線タックハウスにつき約100〜2 5001)pbにとどまることよりなる、新規な改良された銅の電解精錬法から なる。A preferred form of the invention is carried out in a tank house or other suitable container means; The improvement is that the concentration of thioureas in the electrolyte effluent stream can be determined by appropriate measuring means, p (preferably 1 or by differential pulse polarography) to determine the desired concentration in the effluent stream. By adding an amount of thiourea effective to keep the total influent flow within The concentration of thioureas is readjusted, and beyond that range impurities will appear in the copper cathode. at least a measurable fL below which nodule formation is promoted. amount, preferably with a minimum concentration that is about 100 ppb; repeatedly, so that f) the measured concentration of thioureas in the effluent stream exceeds these maximum and the minimum value, preferably about 100 to 2 per typical electrolytic phase line tackhouse 5001) From a new and improved copper electrolytic refining process consisting of pb. Become.

本発明者らは理論に拘束されることは望寸ないが、タンクハウス内の桟々の地点 でチオ尿素類の濃度を測定するためにDPPを使用することによりまさにチオ尿 素がどのように消費さ1しるかが明ら刀1になると考える。チオ尿素類の厳密な 最適6度はセクンヲン毎に夏化し、各ユニットにつき実験的に定めなければなら ない。チオ尿素類は電解していない状態ですら経時的に減少する。たたしその消 費速度(iN電流密度比例すると思われる。Although the inventors do not wish to be bound by theory, the points of the piers inside the tank house By using DPP to measure the concentration of thioureas in I think that how the element is consumed becomes 1 sword. Strict thioureas The optimum 6th degree varies from unit to unit and must be determined experimentally for each unit. do not have. Thioureas decrease over time even in a non-electrolyzed state. Tashino erasure It seems that the cost speed (iN) is proportional to the current density.

最も意外な昶見は、不発明方法によりチオ尿素類の濃度ヶ監睨するここによって 電流密度が3〜6%改良され、かつ短絡が80%まで少なくなるという事夾であ る。第1表には工桑的精錬所における電流効率(C0E−)および短絡の回数全 4か月間にわたってまとめた。最初の1か月間はチオ尿素、グルーおよびアビト ンを一般に受け入れらnている慣習に従って電解液に添加することを含む一般的 な精錬技術?用い、一方最後の3か月間に本発明の自現な方法を用いた。最初の 測定では流出液中にチ万尿素が存在しないことが示されたが、本発明の技術に従 って流出液〒に測定可能fr、量のチ万尿素が検出される点捷でチオ尿素勿工解 放IC添7i0するの:ご伴って短絡の回数が減り、タンクハウスモジュールに おける平均゛成流効率が増大することが認められた。第2表には2棟のタンクハ ウスモジュールにおいて9日間にわたって、共に本発明方法全採用する前および 本方法を採用したのちに起こった短絡の回数金示す。The most surprising thing about Akemi is that he is monitoring the concentration of thioureas using an uninvented method. The result is a 3-6% improvement in current density and up to 80% reduction in short circuits. Ru. Table 1 shows the current efficiency (C0E-) and the total number of short circuits in the factory. It was compiled over a period of four months. Thiourea, Glue and Avit for the first month general procedures, including adding chlorine to the electrolyte according to generally accepted practice. What refining technology? during the last 3 months using the original method of the present invention. the first Although measurements showed the absence of thiourea in the effluent, according to the technique of the present invention, Therefore, it is possible to detect a measurable amount of thiourea in the effluent. Adding a radiator IC to the tank house module reduces the number of short circuits. It was observed that the average flow efficiency increased. Table 2 shows two tank tanks. for 9 days in a mouse module, both before and after employing the entire method of the invention. The number of short circuits that occurred after adopting this method is shown.

第1表および第2表に示されるN線電流効率の劇的な増大および短絡が起こった 回数の減少は、全く予期さniかった進歩2 である。よシ普通のエフアンはア/ft2(183アンはア/m2)と対比して 23アンペア/ft2(2487ンRア/正2)という高い電流効率が電流密度 r犠牲にすることなく達成された。結果は使用するタンクハウスの一々の特性に 応じて異なるであろうが、実質的に数十年間現在の状態で操業されてきた方法( でおいて実質的な経済的節約がなされたことはきわめて驚くべきかつ予想外の結 果であることは明らかである。A dramatic increase in N-line current efficiency and short circuits occurred as shown in Tables 1 and 2. The decrease in frequency was a totally unexpected development.2 It is. In contrast, the normal Efan is A/ft2 (183 An is A/m2) High current efficiency of 23 amps/ft2 (2487 amps/ft2) reduces current density. This was achieved without sacrificing anything. The results depend on the characteristics of each tank house used. The method that has been operating in its current state for decades (substantially It is a very surprising and unexpected result that substantial economic savings have been made in It is clear that this is the result.

明らかに上記の技術を考慮に入れて本発明方法につき多数のイー正および変更金 なしうる。従って、請求の範囲の限度内で不発明は上記に詳述された以外の形態 で芙施しうると解すべきである。Obviously, taking into account the above techniques, a large number of modifications and changes have been made to the method of the present invention. It can be done. Therefore, within the scope of the claims, non-inventions do not include forms other than those detailed above. It should be understood that it is possible to give alms.

第1表 月 モジュール 短絡の回数 流出1色中のチ万尿g”c、E、%1か戸当 人  67g 93.18 B 749 92.43 0 759 − 90.15 2か月間 A 336 + 96.32B 382 工 9611 ※※ C381+/ −94,79 D 330 94.38 E 322 4− 94.58 3か月間 A 327 + 96.54B 371 + 96.33 C270495,76 D 149 + 96.97 E 174 + 96.54 4か月間 A 213 97.80 B 21g 196.83 g 149 + 97.33 ※ チオ尿素の測定は1か月間および2か月間、lらひに3か月間の19日l1 では週1回行われ、その後は1日1回行われた。Table 1 Month module number of short circuits leaked 1 color of urine g"c, E, %1 or doorstop person 67g 93.18 B 749 92.43 0 759 - 90.15 2 months A 336 + 96.32B 382 labor 9611 ※※ C381+/-94,79 D 330 94.38 E 322 4-94.58 3 months A 327 + 96.54 B 371 + 96.33 C270495,76 D 149 + 96.97 E 174 + 96.54 4 months A 213 97.80 B 21g 196.83 g 149 + 97.33 * Thiourea measurements were taken for 1 month and 2 months, and on the 19th for 3 months. This was done once a week, and then once a day thereafter.

※※ セクションCは2か月間の中頃、チオ尿素の読みがゼロからプラスに変わ った。※※ In Section C, the thiourea reading changed from zero to positive in the middle of the two-month period. It was.

14 1 402 115 415 121 2 433 134 406 105 3 409 92 399 124 4 485 92 389 129 5 410 134 282 86 6 335 66 346 101 7 4.39 75 421 114 8 557 58 452 123 9 469 61 389 101 ※ 読みはアサルニ・インコーボレーテーイッ)゛のアマリロ脣t:錬タンクハ ウスで行われた。14 1 402 115 415 121 2 433 134 406 105 3 409 92 399 124 4 485 92 389 129 5 410 134 282 86 6 335 66 346 101 7 4.39 75 421 114 8 557 58 452 123 9 469 61 389 101 *Pronunciation: Asaruni Inkoboretei) ゛'s Amarillo 脣t: Ren Tankha It was held in U.S.

特却060−500453 (5) FIG、2 国際調査報告Tokuho 060-500453 (5) FIG.2 international search report

Claims (1)

【特許請求の範囲】[Claims] 1.有効濃度の硫酸および硫酸銅の水溶液からなる銅精練用電解液を調製し、該 溶液は多重量の添加剤を含有し2、そのうち1種はチオ尿素類であp1#電解液 が精錬中に流入液流および流出液流の導通手段を経由する電解液の流入液流およ び流出液流の双方を備えた適切な容器手段中に存在し;チオ尿素類の流出液流中 濃度を少なくとも痕跡濃度以上の値に維持するのに十分な量のチオ尿素類全流入 液流に添加し:そして 該容器手段中で銅を電解精錬する; ことよシなる鋼の電解精錬法。 2、電解液中のチオ尿素類の流出液流中濃度?有効な測定手段によυ短期的に両 足する、請求の範囲第1項記載の方法。 3、測定手段が示差パルスポーラログラフイーである、請求の範囲第2項記載の 方法。 4、チオ尿素類の最低流出液流中濃度が約100 ppb である、請求の範囲 第1項記載の方法。 5、流出液流中のチオ尿素類濃度の望ましい範囲が約100〜5000 ppb  でちる、請求の範囲第1項記載の方法。 6 容器が銅精錬用タンクハウスである、請求の範囲第1項記載の方法。1. Prepare an electrolytic solution for copper scouring consisting of an aqueous solution of sulfuric acid and copper sulfate at an effective concentration, and The solution contains a large number of additives, one of which is thiourea, which is a p1# electrolyte. The influent and effluent streams of the electrolyte pass through the influent and effluent stream conduction means during refining. in suitable container means with both the thioureas and the effluent stream; Total influx of thioureas in an amount sufficient to maintain the concentration at least above the trace concentration. Add to the liquid stream: and electrolytically refining copper in the vessel means; The most important method of electrolytic refining of steel. 2. Concentration of thioureas in the electrolyte in the effluent stream? υ In the short term with effective measurement methods 2. The method according to claim 1, wherein: 3. The method according to claim 2, wherein the measuring means is differential pulse polarography. Method. 4. The claim that the minimum concentration of thioureas in the effluent stream is about 100 ppb. The method described in paragraph 1. 5. The desired range of thioureas concentration in the effluent stream is about 100-5000 ppb The method according to claim 1. 6. The method according to claim 1, wherein the container is a tank house for copper refining.
JP58501347A 1983-02-28 1983-02-28 Method for adding thioureas to electrolytic solutions useful for copper smelting Granted JPS60500453A (en)

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PCT/US1983/000298 WO1984003307A1 (en) 1983-02-28 1983-02-28 Method of maintaining and testing for proper concentrations of thiourea in copper refining electrolysis cells

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JPS60500453A true JPS60500453A (en) 1985-04-04
JPS6230271B2 JPS6230271B2 (en) 1987-07-01

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* Cited by examiner, † Cited by third party
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JP2011209033A (en) * 2010-03-29 2011-10-20 Pan Pacific Copper Co Ltd Inspection method for scale state in pipe
JP2013040371A (en) * 2011-08-15 2013-02-28 Pan Pacific Copper Co Ltd Apparatus and method of producing metal

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TR22348A (en) * 1984-06-14 1987-02-23 Asorco Inc YOENTEM ADDING TIOUERE TO ELECTRICITY COEZELTES, USED IN COPPER PURIFICATION

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US4146437A (en) * 1975-12-31 1979-03-27 The Curators Of The University Of Missouri Method for evaluating a system for electrodeposition of metals
JPS5690993A (en) * 1979-12-21 1981-07-23 Furukawa Electric Co Ltd:The Electrolytic refining of copper

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US4146437A (en) * 1975-12-31 1979-03-27 The Curators Of The University Of Missouri Method for evaluating a system for electrodeposition of metals
US4146437B1 (en) * 1975-12-31 1987-07-14
JPS5417301A (en) * 1977-07-09 1979-02-08 Yutaka Mochida Mouth apparatus for pressure drilling
JPS5690993A (en) * 1979-12-21 1981-07-23 Furukawa Electric Co Ltd:The Electrolytic refining of copper

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011209033A (en) * 2010-03-29 2011-10-20 Pan Pacific Copper Co Ltd Inspection method for scale state in pipe
JP2013040371A (en) * 2011-08-15 2013-02-28 Pan Pacific Copper Co Ltd Apparatus and method of producing metal

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EP0137776A4 (en) 1985-07-30
IN163215B (en) 1988-08-20
FI77059B (en) 1988-09-30
AU558737B2 (en) 1987-02-05
FI844070L (en) 1984-10-16
EP0137776B1 (en) 1988-04-06
JPS6230271B2 (en) 1987-07-01
FI77059C (en) 1989-01-10
DE3376228D1 (en) 1988-05-11
WO1984003307A1 (en) 1984-08-30
ATE33408T1 (en) 1988-04-15
AU1472483A (en) 1984-09-10
FI844070A0 (en) 1984-10-16
EP0137776A1 (en) 1985-04-24

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