Abstract

This paper describes the leaching behaviour of nickeliferous pyrrhotite concentrates in hot nitric acid. The effect of the following parameters was investigated by applying a conventional leach procedure, where pyrrhotite was leached in a solution containing excess HNO 3 temperature, solids content, [HNO 3] and particle size. The reaction products were, Fe(NO 3) 3 Ni(NO 3) 2 elemental sulphur, SO 4 2− and NO gas. Sulphate formation has a strong negative effect on the efficiency and economics of any nitric acid based leach process and special attention has been given, therefore, to the mechanism of formation of SO 4 2− Sulphate formation can be minimized by applying a so-called controlled leach technique. This technique involves activation of the dissolution reaction of pyrrhotite by addition of a small excess of HNO 3 followed by slow addition of HNO 3 keeping the acid concentration at a constant low level. By applying this technique the efficiency and kinetics of the leach are improved as well. Finally a method for recovery of Ni as a Ni-sulphide concentrate is discussed and a conceptual flowsheet is proposed, in which Fe will be produced as well grown and clean hematite, sulphur as elemental sulphur and Ni as a Ni-sulphide concentrate.

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