Patent GB-379322-A (GB)
Title: Improvements in or relating to processes of treating nickel bearing materials
IPC: C22B3/46
Filed: 1931-04-24
Abstract: A solution containing nickel, and also copper and iron is treated with a metallic powder containing nickel to cement the copper, and to reduce the hydrogen ion concentration to such an extent as to permit of precipitation of ferric hydroxide on aeration, whereby a purified nickel solution is obtained, the acid set free restoring the hydrogen ion concentration approximately to its normal value appropriate for electrodeposition of nickel. Preferably, a low-temperature, gas-reduced nickeliferous powder is used, but reduction may be effected by charcoal.  In an application of the process, pulverized nickel-bearing materials such as Bessemer mattes, or nickel bottoms produced by the Orford process, are desulphurized by roasting, preferably in a down-draught sintering apparatus, and may then be leached with sulphuric acid to remove copper.  The residue is divided into two portions, constituting 95-97 and 3-5 per cent respectively. The minor part is ground and reduced preferably at 300-500 DEG  C., for example by water gas.  The major part is reduced with coke, coal or charcoal at 1500-1550 DEG  C. to form nickel anodes, which are placed in the anode compartment of an electrolytic cell separated from the cathode compartment by a pervious diaphragm.  The electrolyte flows from the latter compartment to the former at a velocity of 0,0006-0-0008 ft./min.  It is removed preferably continuously from the anode compartment, heated say to 55 DEG  C. and treated with the nickeliferous powder produced from the minor portion above-referred to so as to reduce the hydrogen ion concentration to a pH value of 5,6 or higher.  After separation of the cemented copper, ferric hydroxide is precipitated from the solution at 60-90 DEG  C. by air, and separated.  The solution, if necessary, after adjustment of the pH value to 4,5-5,6 by the addition of sulphuric acid, is returned to the cathode compartment.  The composition of the electrolyte, which contains nickel as the sulphate, is specified. Boric acid is present therein.  In a modification of the process, the major part of the desulphurized material may be converted directly to a nickel solution which is electrolyzed.  Reference has been directed by the Comptroller to Specification 372,958.ALSO:A solution containing nickel, and also copper and iron, is treated with a metallic powder containing nickel to cement the copper, and then aerated to precipitate ferric hydroxide. Preferably, a low-temperature, gas-reduced nickeliferous powder is used, but reductions may be effected by charcoal.  In an application of the process, pulverized nickel-bearing materials such as Bessemer mattes or nickel bottoms produced by the Orford process are desulphurized by roasting, and may then be leached with acid to remove copper.  The residue is divided into major and minor portions.  The minor part is ground and reduced preferably at 300-500 DEG  C., for example, by water gas.  The major part is reduced with coke, coal, or charcoal at 1500-1550 DEG  C. to form nickel anodes, which are placed in the anode compartment of an electrolytic cell.  The impure electrolyte is removed from the anode compartment, heated, say, to 55 DEG  C., and treated with the nickeliferous powder produced from the minor portion above-referred to.  After separation of the cemented copper, ferric hydroxide is precipitated by air, and separated.  The purified solution is returned from the cathode compartment.  Reference has been directed by the Comptroller to Specification 372,958.