ABSTRACT
The history and variety of commercial Platinum Group Metal (PGM) matte converting processes are explored. Aspects unique to pneumatic converting of high iron, lower grade mattes (typically up to 30% NiCuCo), often containing chrome (0.5–2% Cr2O3), to PGM-enriched (1500–25000 g/t PGM) converter mattes, to endpoints specific to promote downstream refining to final metal are described. The range of converter vessels, involving batch, to staged, to continuous converting processes are presented, along with some of the operating requirements and challenges.
Acknowledgements
Permission by Anglo American Platinum Ltd. to publish and assistance with manuscript collation by Lettie Chomane and Luke Ngubane are gratefully acknowledged, as are contributions from Steve Burks, Dan Legrand, Louis Mabiza, Robert Matusewicz, Loucas Pouroulis, Greg Roset and Nico Steenekamp.
Disclosure statement
No potential conflict of interest was reported by the authors.
Notes
1 Sulphur-deficient, or metallized matte is generally accepted to refer to matte with sulphur content below that stoichiometrically required to combine, in sequence of sulphur allocation, all copper, cobalt, nickel and iron, except for any iron associated with oxygen as magnetite, typically as the sulphides Cu2S, Co9S8, Ni3S2 and FeS, respectively (Bustos, Ip et al. Citation1988 Citation; Donald et al. Citation2005). While the specific sequence of metallisation is argued to be more complex and composition dependent (Tsymbulov and Yertseva Citation2006), at Ni/Cu ratios of 1.6 typical of PGM converting, the rate of metallisation by iron is predicted to exceed nickel, so the sequence above remains directionally consistent.
2 ‘The mush consists of magnetite and silica double saturated slag. Solid nickel ferrite, NiO.Fe2O3, a very stable compound also forms as a distinct solid’ (Warner and Díaz Citation2003).