JPS6029481A - Electrolytic recovering method of copper - Google Patents
Electrolytic recovering method of copperInfo
- Publication number
- JPS6029481A JPS6029481A JP58136874A JP13687483A JPS6029481A JP S6029481 A JPS6029481 A JP S6029481A JP 58136874 A JP58136874 A JP 58136874A JP 13687483 A JP13687483 A JP 13687483A JP S6029481 A JPS6029481 A JP S6029481A
- Authority
- JP
- Japan
- Prior art keywords
- copper
- anode
- sulfuric acid
- continuous casting
- alloy
- 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
Links
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 15
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 15
- 239000010949 copper Substances 0.000 title claims abstract description 15
- 238000000034 method Methods 0.000 title claims abstract description 15
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000009749 continuous casting Methods 0.000 claims abstract description 6
- 229910000978 Pb alloy Inorganic materials 0.000 claims abstract description 5
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 4
- 229910001020 Au alloy Inorganic materials 0.000 claims description 7
- 239000003353 gold alloy Substances 0.000 claims description 7
- 238000011084 recovery Methods 0.000 claims description 7
- 230000002378 acidificating effect Effects 0.000 abstract description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 3
- 238000005520 cutting process Methods 0.000 abstract description 3
- 239000001301 oxygen Substances 0.000 abstract description 3
- 229910052760 oxygen Inorganic materials 0.000 abstract description 3
- 238000013508 migration Methods 0.000 abstract description 2
- 230000005012 migration Effects 0.000 abstract description 2
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 7
- 238000005266 casting Methods 0.000 description 4
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 241000473391 Archosargus rhomboidalis Species 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000010008 shearing Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- 239000003929 acidic solution Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910052745 lead Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
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
- Electrolytic Production Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】 を電解回収する方法に関する。[Detailed description of the invention] This invention relates to a method for electrolytically recovering .
従来、銅を含む硫酸酸性溶液からの鯛の電m回収には、
一般にPbまなはpb金合金の不溶性7ノードが用いら
れており、該アノード板は置型すなわち鋳型にpbまた
はpb金合金溶体を注湯する鋳造法により製造されるの
が普通であった。しかしながら、鋳型に1枚1枚注湯し
て出来な1ノードは、鋳造速度が遅いばかりでなく、1
枚1枚の厚さの不均一による重量バラツキが多く、シか
もアノード表面の冷却時のシワ、あるいは#型の劣化1
ζよるシワ等の表面の粗さも多く、しかもM型への注湯
がオープン注湯であるため酸素のまき込みが多く、良質
なアノードを得ることが困難であった。Conventionally, the recovery of electricity from sea bream from an acidic sulfuric acid solution containing copper requires
Generally, an insoluble 7-node of Pb gold alloy is used as a Pb manifold, and the anode plate is usually manufactured by a casting method in which a Pb or PB gold alloy solution is poured into a mold. However, one node, which is made by pouring metal into the mold one by one, not only has a slow casting speed, but also has one node.
There are many weight variations due to uneven thickness of each sheet, and there may be wrinkles on the anode surface during cooling, or #-type deterioration 1
There were many surface roughness such as wrinkles caused by ζ, and since the pouring into the M-type was open pouring, a large amount of oxygen was mixed in, making it difficult to obtain a high-quality anode.
本発明者は、上記従来法の問題点に鑑みアノード表面の
平滑度の向上とアノード厚みの均一性向上を目的に、1
ノードの連続鋳造を試みたところ、乙の方法で製造され
たアノードが、銅の電解回収の際に予想をはるかに上回
る寿命を示すことを見い出して本発明に至った。すなわ
ち本発明により[銅を含む硫酸酸性溶液からの鯛の電解
回収法において、連続鋳造法覆とよって得られた帯状の
pb金合金1ノード形状に切断し、Ml!l解用pb合
金として用いろことを特徴とするmのNm回収法」が提
供される。In view of the above-mentioned problems of the conventional method, the present inventors aimed at improving the smoothness of the anode surface and improving the uniformity of the anode thickness.
When we attempted continuous casting of nodes, we discovered that the anodes produced by the method described in B exhibited a far longer lifespan than expected during the electrolytic recovery of copper, leading to the present invention. That is, according to the present invention [in the electrolytic recovery method of sea bream from a sulfuric acid acidic solution containing copper, a strip-shaped PB gold alloy obtained by continuous casting is cut into a one-node shape, and Ml! A method for recovering Nm characterized in that it can be used as a PB alloy for decomposition is provided.
本発明に好適な連続鋳造装置としては、溶湯をタンディ
ツシュからモールドに注ぐ通常のタイプのものでよく、
モールドを通過して凝固したpb金合金、ピンチロール
により圧用され、さらにレベラーによって上下から狭止
された後シャーリングによりアノード形状に切断される
。このときタンディツシュからモールドに注湯されたp
b金合金、モールド内が還元性雰囲気であり、溶湯が凝
固するまではクローズドであるため、酸素まき込みが極
めて少ない。またアノード表面の平滑度やアノード厚み
の均一性が従来の置型鋳造法よりはるかに優れているた
め、電解時に電解槽中に正確に懸吊でき、かつアノード
とカソードの面間隔も一定になって局部的な電流の濃淡
が減少した結果pbのカソードへの移行が極めて少なく
なり、さらには電解効率も改良される等の効果が見られ
、それらの総合的効果としてアノードライフの延長がも
たらされた。また製造歩留まりも置型鋳造法に比較して
はるかに向上した。Continuous casting equipment suitable for the present invention may be of the conventional type, in which the molten metal is poured from a tundish into a mold;
The PB gold alloy solidified after passing through the mold is pressed by pinch rolls, and further narrowed from above and below by levelers, and then cut into an anode shape by shearing. At this time, p was poured into the mold from Tanditshu.
Since the gold alloy b has a reducing atmosphere inside the mold and is closed until the molten metal solidifies, there is extremely little oxygen intrusion. In addition, the smoothness of the anode surface and the uniformity of the anode thickness are far superior to those of conventional stationary casting methods, so it can be accurately suspended in the electrolytic bath during electrolysis, and the spacing between the anode and cathode surfaces is also constant. As a result of the local current density being reduced, the migration of PB to the cathode is extremely reduced, and the electrolytic efficiency is also improved, and the overall effect is to extend the anode life. Ta. The manufacturing yield was also much improved compared to the stationary casting method.
以下実施例によりさらに具体的に説明す実施例1
容量5トンの溶解鍋にPbを溶解し、該溶体に320〜
340℃テPb 1000 Kg当りSn5Kgヲ加え
て溶解した後、430±30℃まで昇渇し、径3mm
の小孔を多数設けたセラミック容藷ニCaショッ トを
Pb 1000 Kg当り1.2Kgとなるように入れ
て前記溶体に浸漬し、Arガスで1光拌して溶mした。Example 1: Pb is dissolved in a melting pot with a capacity of 5 tons, and Pb is added to the solution in a more specific manner.
After adding and melting 5 kg of Sn per 1000 kg of Pb at 340°C, the temperature was raised to 430±30°C, and the diameter was 3 mm.
A ceramic container with a large number of small pores (Ca shot) was placed in the solution at a concentration of 1.2 kg per 1000 kg of Pb, immersed in the solution, and stirred with Ar gas for 1 hour to dissolve.
(この方法は、本出願人の先願発明特開昭56−146
84Or合金製造法」に基づく)このようにして得られ
た溶体をクンディツシュからモールドに通過させ、凝固
したpb金合金第一ピンチロールおよび第二ピンチロー
ルで圧延した後、レベラーによって上下から厚さ12m
mに調整し、シャーリングによって縦980mm1構9
60mmのアノード形状に切断してアノード板45枚を
製造した。(This method is based on the patent application filed in Japanese Patent Application Laid-Open No. 56-146).
The solution obtained in this way (based on the ``84Or alloy manufacturing method'') was passed through a kundish into a mold, rolled with solidified PB gold alloy first pinch rolls and second pinch rolls, and then rolled with a leveler from above and below to a thickness of 12 m.
m, and by shearing, one structure of 980 mm in length9
45 anode plates were manufactured by cutting into 60 mm anode shapes.
得られたアノードの組成は、CaO,12重置火、5n
O05重量%残部がpb であった。かくして得られた
アノード45枚と、銅カソード46枚を銅を含む硫酸酸
性溶液中【こ懸吊して電流密度250A/T11+で銅
の電解回収試験を反復実施した。The composition of the obtained anode was: CaO, 12 times overheating, 5n
The balance of O05% by weight was pb. 45 anodes and 46 copper cathodes thus obtained were suspended in an acidic sulfuric acid solution containing copper, and a copper electrolytic recovery test was repeatedly conducted at a current density of 250 A/T11+.
比較のために製造しtこ従来法置型アノードとこれを用
いて行った電解回収試験の結果とを表1に並べて記載し
た。For comparison, a conventional vertically mounted anode manufactured and the results of an electrolytic recovery test conducted using the same are listed in Table 1.
出願人 小名浜製錬株式会社 代理人 萩野谷 徹Applicant: Onahama Smelting Co., Ltd. Agent Toru Haginoya
Claims (1)
連続鋳造法によって得られた帯状のpb金合金アノード
形状に切断し、銅電解用pb合金1ノードとして用いる
ことを特徴とする 銅の電解回収法。In the electrolytic recovery method of copper from a sulfuric acid solution containing copper,
A method for electrolytic recovery of copper, characterized in that a strip-shaped PB gold alloy anode obtained by a continuous casting method is cut into strips and used as one node of a PB alloy for copper electrolysis.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58136874A JPS6029481A (en) | 1983-07-28 | 1983-07-28 | Electrolytic recovering method of copper |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58136874A JPS6029481A (en) | 1983-07-28 | 1983-07-28 | Electrolytic recovering method of copper |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58157105A Division JPS60106988A (en) | 1983-08-30 | 1983-08-30 | Production of pb alloy anode for copper electrolysis |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6029481A true JPS6029481A (en) | 1985-02-14 |
JPS624470B2 JPS624470B2 (en) | 1987-01-30 |
Family
ID=15185545
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58136874A Granted JPS6029481A (en) | 1983-07-28 | 1983-07-28 | Electrolytic recovering method of copper |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6029481A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60150071U (en) * | 1984-03-14 | 1985-10-05 | 日本電気株式会社 | clip |
-
1983
- 1983-07-28 JP JP58136874A patent/JPS6029481A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60150071U (en) * | 1984-03-14 | 1985-10-05 | 日本電気株式会社 | clip |
Also Published As
Publication number | Publication date |
---|---|
JPS624470B2 (en) | 1987-01-30 |
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