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An overview of PGM Smelting in Zimbabwe – Zimplats ... - saimm

An overview of PGM Smelting in Zimbabwe – Zimplats ... - saimm

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Operational practiceThe furnace matte is charged, and, dur<strong>in</strong>g blow<strong>in</strong>g, silica/quartz sized at 5-15 mm is charged at regular <strong>in</strong>tervals. Ladle dregs/reverts are charged <strong>in</strong>to theconverter at regular <strong>in</strong>tervals to control the temperature <strong>of</strong> the converter, andalso to boost production from ladle clean<strong>in</strong>gs. Silica is charged through feedpipes to flux the FeO, and the converter slag is skimmed at regular <strong>in</strong>tervals.The converter slag is returned to the furnace. Typical operat<strong>in</strong>g temperatureranges between 1100ºC and 1250ºC, and temperature monitor<strong>in</strong>g is through as<strong>in</strong>gle hood-mounted optical pyrometer per converter. Blower air, averag<strong>in</strong>g8 500 Nm 3 /h at 128 kPa, is blown <strong>in</strong>to the converter through the tuyeres. Localcontrol <strong>of</strong> the converter is by means <strong>of</strong> a SCADA system.The ma<strong>in</strong> reactions <strong>in</strong> the convert<strong>in</strong>g stage are oxidation <strong>of</strong> iron (II) sulphide,and slagg<strong>in</strong>g <strong>of</strong> iron (II) oxide by added silica/quartz flux.2FeS + 3O2 = 2FeO + 2SO2 (melt<strong>in</strong>g po<strong>in</strong>t <strong>of</strong> FeO is 1385 º C)2FeO + SiO2 = Fe2SiO4Formation <strong>of</strong> magnetite occurs near the tuyeres:3FeS + 5O2 = Fe3O4 + 3SO2 (melt<strong>in</strong>g po<strong>in</strong>t <strong>of</strong> Fe3O4 is 1597 º C)Oxygen reacts exothermically with iron sulphide, and hence supplies energy forthe converter. The temperature <strong>in</strong> the converter is controlled through theaddition <strong>of</strong> silica and cold reverts. There is no oxygen enrichment <strong>in</strong> theconverter process at <strong>Zimplats</strong>. Converter operations are complete at iron levels<strong>of</strong> 0.6 – 0.7% Fe.Converter tuyeres are kept clear <strong>of</strong> solid build-up by utilis<strong>in</strong>g a mechanicaltuyere puncher. The tuyere puncher is a rail-mounted carriage on which adouble-act<strong>in</strong>g air cyl<strong>in</strong>der is <strong>in</strong>stalled. The cyl<strong>in</strong>der drives up to three punchbars <strong>in</strong>to the tuyeres by means <strong>of</strong> guided yokes. The carriage moves along thetuyere l<strong>in</strong>e to punch successive tuyeres. The punch<strong>in</strong>g mach<strong>in</strong>e design alsomakes provision for mount<strong>in</strong>g a drill for drill<strong>in</strong>g the tuyere l<strong>in</strong>e <strong>of</strong> a newlyrel<strong>in</strong>ed converter.At the end <strong>of</strong> each batch cycle, after skimm<strong>in</strong>g <strong>of</strong> all the slag, the convertermatte is poured <strong>in</strong>to a converter matte ladle. The converter matte is taken formatte granulation at the matte granulation platform. The matte is then pouredonto a refractory-l<strong>in</strong>ed granulation spoon rest<strong>in</strong>g on a hydraulic platform. Thespoon <strong>in</strong>cludes a refractory bridge just ahead <strong>of</strong> the pour<strong>in</strong>g lip, designed tohold back any contam<strong>in</strong>at<strong>in</strong>g converter slag <strong>in</strong> the matte. Converter matte isdischarged over the spoon lip <strong>in</strong>to a f<strong>in</strong>ely distributed stream <strong>of</strong> granulationwater. The granulated matte discharges directly <strong>in</strong>to a steep-sided conicalbottomedtank.71

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