The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.
The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.
Patent No.:
Date of Patent:
Jun. 22, 1976
Filed:
Oct. 19, 1973
Godefridus Maria Swinkels, Rossland, CA;
Robert Arthur Furber, Edmonton, CA;
Edward Francis Milner, Warfield, CA;
Roman Michael Genik-Sas-Berezowsky, Edmonton, CA;
Charles Ray Kirby, Rossland, CA;
Sherritt Gordon Mines Limited, Toronto, CA;
Cominco Ltd., Vancouver, CA;
Abstract
A hydrometallurgical process for treating iron containing metal sulfides for rendering iron and non-ferrous metal values active and amenable for selective extraction and separate recovery. Sulfur values can be controllably produced as elemental sulfur or as sulfuric acid to supply acid requirements of the process, while substantially obviating the discharge of sulfur-containing gases to the atmosphere. Ores and concentrates of the sulfides are thermally activated by sequentially heating and reducing said sulfides in a countercurrent flow of heating and reducing gases respectively in a reactor whereby the reaction products of the reducing gas and sulfides, together with liberated labile sulfur, are controllably combusted with oxygen to satisfy heat requirements of the thermal activation process and to convert sulfur values to SO.sub.2 gas. The activated sulfides are subjected to an acid leach in aqueous sulfuric acid for production of ferrous sulfate and evolution of H.sub.2 S gas which are separated from the solid sulfide residue containing concentrated non-ferrous metal values. The ferrous sulfate is oxidized and hydrolysed to precipitate the iron, which is removed from the system, and to regenerate sulfuric acid. At least a portion of the SO.sub.2 gas from said heating step and at least a portion of the H.sub.2 S from the acid leach are converted to sulfuric acid to satisfy the acid requirements of the process, and remaining SO.sub.2 is combined and catalytically reacted with remaining H.sub.2 S to produce elemental sulfur. The solids residue from the acid leach is subsequently subjected to further treatment for recovery of metal values.