manganese.14 Phosphorus removal through chemical beneficiation requires comminution, flotation, and/or leaching Dephosphorisation of ferromanganese under to be followed by agglomeration, the technoeconomics of oxidising conditions is difficult to achieve without which is not considered suitable.14 Dephosphorisation in significant manganese loss. The present study gaseous form is not suitable because the partial pressure of identifies the suitable conditions for selective manganese is higher than that of phosphorus at smelting removal of phosphorus using BaCO 3 based fluxes.temperatures. The reaction product of dephosphorisation Initially Ba-P-O predominance diagrams for both under reducing conditions is phosphide, which produces standard and non-standard conditions were toxic phosphene in contact with moisture.4 Therefore, all constructed, and studied to identify the best the methods mentioned above suffer from serious practical possible flux composition for selective removal of limitations. phosphorus without significant manganese loss.In view of the difficulties associated with those methods, Experiments were conducted by varying the flux the favourable choice is the removal of phosphorus from composition (BaCO 3 , BaF 2 ), flux rate, metal liquid ferromanganese under oxidising conditions for the composition, and temperature under the desired following reasons. conditions for phosphorus removal. A method was 1. The process is favoured at lower temperatures since evolved to melt BaCO 3 based flux at temperatures the reaction is exothermic. below 1400°C. A flux composition consisting of 2. The activity coefficient of phosphate is much lower 66% BaCO 3 and 34% BaF 2 added at the rate of than that of phosphide in molten basic fluxes; thus, the flux 16 wt-% of the amount of ferromanganese charged consumption is much less for the formation of phosphate.14 was found to be most effective.I&S/1562 3. The reaction product does not create any environmental problems.