Pyrometallurgical upgrading of PGM-rich leach residues from the Western Platinum base metals refinery through roasting, smelting and alloy atomisation

摘要

The production of Platinum Group Metals (PGM) normally entails the smelting of PGM flotation concentrates, converting of the furnace matte and removal of the bulk of the Ni, Cu, Co, S and Fe through atmospheric and pressure leaching in a base metals refinery to produce a PGM-rich concentrate. A number of impurities, mostly Se, Te, As, Bi, Os and Pb, are not removed significantly during the oxidising leach process in sulphuric acid media. In addition slag inclusions in matte leads to contamination of the PGM residues with silica, fayalite, magnetite and trevorite phases. In addition some Cu, Ni, Fe and S also remain. For this reason a typical Precious Metal Refinery (PMR) feed material contains about 55% to 65% PGMs. The PMR is based on a chloride process and requires contaminants to be within narrow specification limits to prevent the formation of PGM residues that must be reprocessed or tolled, leading to poor first pass metal efficiencies and extending the duration of the production pipeline for efficient recovery. Lonmin, through its subsidiary Western Platinum, has developed a novel process to significantly upgrade the BMR leach residues through pyrometallurgical processing, which include a multistep process of roasting under oxidising and reducing atmospheres, a two-step smelting process of the roasted calcine (with engineered slag chemistry and slag-refractory interactions) and subsequent atomisation of the molten alloy which can be fed as a slurry into the HCL/C1_2 dissolution reactors in the precious metals refinery. These pyrometallurgical steps upgrade the BMR residue from a 45-50% grade up to an alloy grade of circa 90% PGMs, whilst removing the most deleterious elements with major process impacts on the PMR. Western Platinum published a Patent Cooperation Treaty (PCT) patent application on this process. This paper will focus primarily on the roasting step and it will investigate the thermochemical and mineralogical changes occurring during roasting. These changes were evaluated through a combination of thermochemical modelling and experimental investigation. The roasting step needs to be a multi-step approach combining an oxidative and reductive environment in order to achieve the vaporization of Se, Te, As, Os and S. The speciation of PGM's and their vaporization behaviour will be addressed, as well as the sensitivity of precious metals deportment to changes in roast conditions.