GB1327525A - Elimination of floating slime during electrolytic refining of copper - Google Patents
Elimination of floating slime during electrolytic refining of copperInfo
- Publication number
- GB1327525A GB1327525A GB1691371A GB1691371A GB1327525A GB 1327525 A GB1327525 A GB 1327525A GB 1691371 A GB1691371 A GB 1691371A GB 1691371 A GB1691371 A GB 1691371A GB 1327525 A GB1327525 A GB 1327525A
- Authority
- GB
- United Kingdom
- Prior art keywords
- electrolyte
- iii
- floating slime
- copper
- pentavalent
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/12—Electrolytic production, recovery or refining of metals by electrolysis of solutions of copper
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
1327525 Electro-refining copper BOLIDEN AB 25 May 1971 [28 May 1970 (3)] 16913/71 Heading C7B Cu anodes containing more than 200g/ton of Sb and/or more than 100g/ton of Bi are electrorefined in an electrolyte in which the quantities of trivalent As, pentavalent As and pentavalent Sb are regulated so that in the steady state the contents of As (III) and As (V) exceed 1 and 2g/l respectively and the quantity of Sb (V) is less than 0À05g/l, to eliminate floating slime during electro-deposition of cathode Cu. The quantity of As (III) may be maintained by continually adding As 2 O 3 e. g. to a withdrawn part stream of electrolyte which is then recirculated, or by charging to the electrolyte in the form of As alloyed in the anodes. To regulate the ratio between As (III) and As (V), As (V) is reduced to As (III) by adding SO 2 gas to a withdrawn portion of the electrolyte which is then returned. The formation of floating slime and anode passivation may be both avoided by periodically reversing the current for periods of 1-15% of the total electrolysis period. The electrolyte may comprise an aqueous solution of 35-50g/l Cu (as CuSO 4 ) and 150-250 g/l H 2 SO 4 , with glue, a thiocarbamide and lignosulphonic acid. To prevent formation of Sb(V), the electrolyte may be covered with plastic bodies or cloth or oil. During electrolysis, crystalline Sb(OH) 2 AsO 4 and BiAsO 4 precipitate.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE07380/70A SE347999B (en) | 1970-05-28 | 1970-05-28 | |
| SE07382/70A SE348001B (en) | 1970-05-28 | 1970-05-28 | |
| SE07381/70A SE348000B (en) | 1970-05-28 | 1970-05-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1327525A true GB1327525A (en) | 1973-08-22 |
Family
ID=27354436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB1691371A Expired GB1327525A (en) | 1970-05-28 | 1971-05-25 | Elimination of floating slime during electrolytic refining of copper |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US3753877A (en) |
| AT (1) | AT309090B (en) |
| BE (1) | BE767811A (en) |
| CA (1) | CA989345A (en) |
| DE (1) | DE2126141A1 (en) |
| ES (1) | ES391620A1 (en) |
| FI (1) | FI52743C (en) |
| GB (1) | GB1327525A (en) |
| NO (1) | NO127405B (en) |
| PH (1) | PH9417A (en) |
| ZM (1) | ZM7171A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5435892A (en) * | 1977-08-25 | 1979-03-16 | Sumitomo Metal Mining Co | Process for removing arsenic* antimony and bismuth in sulfuric acid solution |
| PT3794166T (en) * | 2018-05-16 | 2022-09-20 | Aurubis Beerse | IMPROVEMENT OF ELECTROLYTIC COPPER REFINING |
| CN111020634B (en) * | 2019-12-27 | 2021-07-02 | 中南大学 | A method for precipitation and separation of arsenic from copper electrolyte based on directional crystal control |
-
1971
- 1971-05-25 GB GB1691371A patent/GB1327525A/en not_active Expired
- 1971-05-25 US US00146663A patent/US3753877A/en not_active Expired - Lifetime
- 1971-05-26 DE DE19712126141 patent/DE2126141A1/en active Pending
- 1971-05-26 ZM ZM71/71A patent/ZM7171A1/en unknown
- 1971-05-27 AT AT459371A patent/AT309090B/en not_active IP Right Cessation
- 1971-05-27 CA CA114,055A patent/CA989345A/en not_active Expired
- 1971-05-27 ES ES391620A patent/ES391620A1/en not_active Expired
- 1971-05-27 NO NO01997/71A patent/NO127405B/no unknown
- 1971-05-28 BE BE767811A patent/BE767811A/en unknown
- 1971-05-28 FI FI711493A patent/FI52743C/en active
- 1971-05-28 PH PH12511*UA patent/PH9417A/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| ZM7171A1 (en) | 1971-12-22 |
| US3753877A (en) | 1973-08-21 |
| NO127405B (en) | 1973-06-18 |
| PH9417A (en) | 1975-11-14 |
| CA989345A (en) | 1976-05-18 |
| DE2126141A1 (en) | 1971-12-09 |
| BE767811A (en) | 1971-10-18 |
| FI52743C (en) | 1977-11-10 |
| AT309090B (en) | 1973-08-10 |
| ES391620A1 (en) | 1974-08-01 |
| FI52743B (en) | 1977-08-01 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed [section 19, patents act 1949] |