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GB141688A - Improvements in the electrolytic treatment of ores containing zinc and other metals - Google Patents

Improvements in the electrolytic treatment of ores containing zinc and other metals

Info

Publication number
GB141688A
GB141688A GB944520A GB944520A GB141688A GB 141688 A GB141688 A GB 141688A GB 944520 A GB944520 A GB 944520A GB 944520 A GB944520 A GB 944520A GB 141688 A GB141688 A GB 141688A
Authority
GB
United Kingdom
Prior art keywords
cadmium
zinc
solution
precipitate
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
Application number
GB944520A
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.)
Electrolytic Zinc Company of Australasia Ltd
Original Assignee
Electrolytic Zinc Company of Australasia Ltd
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 Electrolytic Zinc Company of Australasia Ltd filed Critical Electrolytic Zinc Company of Australasia Ltd
Publication of GB141688A publication Critical patent/GB141688A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C25C1/16Electrolytic production, recovery or refining of metals by electrolysis of solutions of zinc, cadmium or mercury
    • 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

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)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

A precipitate obtained by adding zinc dust, with or without a copper salt, to sulphate solutions prepared from ores containing zinc and cadmium, with or without copper and cobalt, is treated for the recovery of cadmium, zinc, and, if present, copper, in the following manner. If substantially free from cobalt, the precipitate is oxidized and leached with sufficient dilute sulphuric acid to dissolve a maximum of zinc and cadmium and a minimum of copper. From the residue the copper is recovered by smelting or otherwise. Alternatively, the precipitate, oxidation of which is guarded against, may be leached with sufficient acid to dissolve the zinc, the residue being then oxidized and further treated to dissolve the cadmium. In either case, the solution containing the cadmium is treated with zinc dust in quantity insufficient for complete precipitation of the cadmium, which is thus obtained free from zinc. In this treatment, the solution should be slightly acid and air should be excluded as much as possible; about 1/2 gr. of cadmium per litre should remain after precipitation. A further treatment of the solution in a second vat with excess of zinc, and preferably in the presence of about 1/2 gr. of copper per litre, gives a zinc solution which is added to the purified ore solution, and a precipitate which can be used again in the first vat. The precipitated cadmium is roasted and dissolved in dilute sulphuric acid or spent electrolyte. Copper is removed by excess of the cadmium precipitate, metallic cadmium, or cadmium oxide, and the solution, then containing about 100 gr. cadmium per litre, is electrolyzed. After electrolysis, the solution should contain 60 gr. of acid per litre. An alternative method of separating the zinc from the cadmium consists in agitating the solution with zinc oxide or hydrate at 60 DEG C. for some time, and then cooling to 35 DEG C. so as to precipitate the zinc as basic sulphate. When the original precipitate contains cobalt, it is oxidized and leached with zinc sulphate solution or just sufficient dilute sulphuric acid to dissolve out most of the cadmium and cobalt, and the residue is then treated as in the first case. The solution of cadmium and cobalt is treated with zinc dust as described above so as to obtain zinc-free cadmium, which is added to that obtained from the residue above mentioned, and a solution of zinc and cobalt, from which a pigment may be prepared, for instance by adding sodium carbonate and drying and heating the precipitate.
GB944520A 1919-04-04 1920-04-01 Improvements in the electrolytic treatment of ores containing zinc and other metals Expired GB141688A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AU141688X 1919-04-04

Publications (1)

Publication Number Publication Date
GB141688A true GB141688A (en) 1921-07-01

Family

ID=3704378

Family Applications (1)

Application Number Title Priority Date Filing Date
GB944520A Expired GB141688A (en) 1919-04-04 1920-04-01 Improvements in the electrolytic treatment of ores containing zinc and other metals

Country Status (1)

Country Link
GB (1) GB141688A (en)

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