A PROCESS FOR PRODUCING METALLIC COPPER

摘要

1362601 Electrolytically recovering copper COPPER PROCESS Ltd 24 Jan 1972 [25 Jan 1971] 3301/72 Heading C7B Copper is recovered from Cu ore (or concentrate) by leaching the ore with a solution comprising a soluble cupric salt (e.g. chloride) and a solubilizing agent for cuprous Cu (e.g. NaCl, KF, LiBr or other alkali metal halide, or CaCl 2 , HCl, HBr or HI) to form a soluble cuprous complex (e.g. sodium cuprous chloride), separating the remaining solids from the resulting leach liquid, electrolytically reducing one portion of the leach liquid to precipitate Cu metal which is recovered and electrolytically oxidizing another portion of the leach liquid to produce a solution comprising cupric salt, combining the reduced and oxidized solutions and recycling as further leaching solution. Oxygen free conditions are maintained throughout. The S.G. of the reduced solution is lesser and of the oxidized solution is greater than that of the leach liquid, so that electrolysis is preferably effected in a cell having alternating anode and cathode compartments separated by ion permeable membranes, e.g. of woven asbestos or fibreglass, equal halves of the leach liquid being fed respectively to the top of the anode compartments and bottom of the cathode compartments, and the oxidized and reduced solutions being collected respectively from the bottom and top of such compartments. The electrodes may be of carbon e.g. graphite, Cu, Cu-Si or Al 2 O 3 . The Cu ore may also contain Ag with or without Mn, Sb, Bi, Fe, Pb, Zn, Co, Ni, Mo, Ti, Cr and/or Hg, which are at least partly removed from the resulting leach liquid prior to electrolysis by precipitation of their oxides with CaO; at least part of the Ag may be precipitated from solution by metal interchange with Cu metal subsequent to CaO precipitation. The ore may be pulverized during and/or prior to leaching. Remaining solids may be washed with a ferrous chloride solution and after separation at least part of the Cu in the separated wash solution may be precipitated by metal interchange with Fe metal. Any sulphur in the washed remaining ore may be removed by floatation. The solvent for the cupric salt and solubilizing agent may be aqueous or a C 1 -C 5 alcohol, phenol, organic acid. The cathode compartments may be provided with Cu powder collecting chambers containing an inert liquid.