The behaviour of chalcopyrite and pyrite in the rougher-scavenger and regrind-retreatment circuits in the Warrego concentrator is discussed. The effects of change in xanthate addition on the separation of chalcopyrite and pyrite is described. The effect of the regrind mill on the (flotation rate of particles containing chalcopyrite and pyrite is discussed with particular reference to the importance of removing sub-mesh particles from the feed to the regrind mill.