GB262546A - Improvements in electro-chemical processes and apparatus for the extraction of copper and zinc from ores - Google Patents
Improvements in electro-chemical processes and apparatus for the extraction of copper and zinc from oresInfo
- Publication number
- GB262546A GB262546A GB23846/25A GB2384625A GB262546A GB 262546 A GB262546 A GB 262546A GB 23846/25 A GB23846/25 A GB 23846/25A GB 2384625 A GB2384625 A GB 2384625A GB 262546 A GB262546 A GB 262546A
- Authority
- GB
- United Kingdom
- Prior art keywords
- passed
- copper
- zinc
- tanks
- solution
- 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
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
- C22B3/06—Extraction of metal compounds from ores or concentrates by wet processes by leaching in inorganic acid solutions, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions
- C22B3/08—Sulfuric acid, other sulfurated acids or salts thereof
-
- 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
Abstract
262,546. Mackay, H. S. Sept. 24, 1925. Copper, obtaining from ores containing coppe: and zinc. A solution of copper and zinc sul phates is obtained and copper deposited there from by electrolysis until the concentration o copper sulphate is low relative to that of zinc sulphate; the zinc sulphate is then crystallized out by evaporation. In the plant shown, the ore is roasted in a furnace A and the residues or concentrates delivered bv a conveyer B to tanks F where they are leached with dilute sulphuric acid. Tanks G. H are provided to receive solutions of low acid content and of higher acid content respectively from the tanks F, the two solutions being used in the manner described in Specification 238,962. The product is passed to an agitator I where iron, aluminium, and other impurities are precipitated, and the solution is then passed through a filter press K to a bank L from which it passes to electrolytic cells M. The spent electrolyte is passed to an evaporating plant 11 heated by the products of combustion from the furnace A and when saturation point is reached is passed to crystallizing tanks 12. The solution from the tanks 12 is returned either to the evaporator or to the tank L. A line 15 is provided to return free sulphuric acid from the cells 11 to the tanks L, H whenever necessary for standardization. The crystallized zinc sulphate is passed to a tower 17 where it is redissolved and treated with calcium carbonate or zinc dust to precipitate copper present as impurity. The solution is decanted or passed by a filter press 18 to a storage tank 19. When calcium carbonate is used as precipitating agent, the copper hydrate is passed to the tower I and used for precipitating iron and aluminium. When zinc dust is used as precipitating agent, the precipitated copper is returned to the furnace A. The pure zinc sulphate solution is passed to an evaporator 22 or electrolyzed to deposit zinc. Specifications 26138/13 and 205,528, [Class 82 (i), Metals, Extracting- &c.], are referred to in the first Provisional Specification.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB23846/25A GB262546A (en) | 1925-09-24 | 1925-09-24 | Improvements in electro-chemical processes and apparatus for the extraction of copper and zinc from ores |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB23846/25A GB262546A (en) | 1925-09-24 | 1925-09-24 | Improvements in electro-chemical processes and apparatus for the extraction of copper and zinc from ores |
Publications (1)
Publication Number | Publication Date |
---|---|
GB262546A true GB262546A (en) | 1926-12-16 |
Family
ID=10202252
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB23846/25A Expired GB262546A (en) | 1925-09-24 | 1925-09-24 | Improvements in electro-chemical processes and apparatus for the extraction of copper and zinc from ores |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB262546A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108179276A (en) * | 2018-01-02 | 2018-06-19 | 燕山大学 | The method of waste and old copper aluminum composite material recycling |
-
1925
- 1925-09-24 GB GB23846/25A patent/GB262546A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108179276A (en) * | 2018-01-02 | 2018-06-19 | 燕山大学 | The method of waste and old copper aluminum composite material recycling |
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