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ABSTRACT
A method, based in leaching with SO
2
, to process low grade pyrolusite minerals has shown good results at laboratory scale. After the separation of the solid impurities, the dissolved manganese is subsequently precipitated using the SO
2
/O
2
gas mixture as oxidising agent. In this research it was obtained a mathematical model to estimate the oxidative precipitation process, as a function of temperature, pH and SO
2
gas flow rate. It was found that pH and temperature have the main influence in the reaction rate. An optimal SO
2
concentration in the mixture must be used to avoid generation of reductive conditions. It was observed a most efficient reaction with a low gas flow rate injection. The predicted reaction rates presents a good concordance with the experimental results (R
2
=0.97), showing a worthy potential for practical uses.