| 摘要 |
<p>1391893 Cu and Ni recovery; ferric sulphate INSPIRATION CONSOLIDATED COPPER CO 17 Jan 1973 [18 Feb. 1972] 2457/73 Heading C1A [Also in Division C7] Cu and/or Ni is recovered from Fe-bearing cupriferous and/or nickeliferous material by leaching such material with an aqueous H 2 SO 4 solution which contains hexavalent Cr ions, separating the leach solution depleted in acid at a pH or not less than 0À6 and containing divalent copper and/or nickel, trivalent iron and trivalent chromium ions from the undissolved residue, hydrolyzing the separated leach solution under superatmospheric pressure at a temperature of not less than 130‹ C. to form a basic ferric sulphate salt precipitate, separating said precipitate from the residual solution, subjecting said residual solution to a first "bifluid electrolysis" as catholyte to deposit metallic copper and/or nickel and then as anolyte to regenerate H 2 SO 4 and partially to reoxidize trivalent chromium ions to hexavalent chromium ions, subjecting the anolyte from said first "bifluid electrolysis" to a second "bifluid electrolysis" to oxidize substantially all remaining trivalent chromium ions to hexavalent chromium ions and recycling anolyte from said second bifluid electrolysis to leach a further quantity of said cupriferous and/or nickeliferous material. "Bifluid electrolysis" means electrolysis in which a permeable diaphragm separates anolyte from catholyte. The Fig. illustrates the process and also illustrates : (a) prevention of Cr loss with the Fe-containing precipitate arising from the hydrolysis step. (As illustrated, the hydrolysis occurs in the autoclave). (b) prevention of build-up of too much sulphate in the system, e.g. derived from sulphur-containing ores. (c) Treatment of the material not dissolved by the leaching to recover elemental sulphur and other materials therefrom.</p> |
