Rate equations and kinetic parameters were obtained for various reactions involved in the bacterial oxidation of pyrite. The rate constants were 3.5 ,LM Fe2+ per min per FeS2 percent pulp density for the spontaneous pyrite dissolution, 10 ,uM Fe21 per min per mM Fe3+ for the indirect leaching with Fe3+, 90 ,uM 02 per min per mg of wet cells per ml for the Thiobacillusferrooxidans oxidation of washed pyrite, and 250 ,uM 02 per min per mg of wet cells per ml for the T. ferrooxidans oxidation of unwashed pyrite. The Km values for pyrite concentration were similar and were 1.9, 2.5, and 2.75% pulp density for indirect leaching, washed pyrite oxidation by T. ferrooxidans, and unwashed pyrite oxidation by T. ferrooxidans, respectively. The last reaction was competitively inhibited by increasing concentrations of cells, with a Ki value of 0.13 mg of wet cells per ml. T. ferrooxidans cells also increased the rate of Fe2' production from Fe3+ plus pyrite. Bacterial leaching of sulfide ores is a complex process potentially involving many different reactions, such as direct action by bacteria, indirect action by ferric iron, and electrochemical interaction of minerals (3, 4, 9, 17). These biological, chemical, and electrochemical reactions are interrelated, and their favorable interaction should lead to a successful bacterial leaching. We have selected a simple sulfide, pyrite (FeS2), as a test mineral and have attempted to estimate the rates of some of these reactions and to compare them with the overall bacterial leaching rates. In this work we have studied the spontaneous solubilization of pyrite, the indirect leaching of pyrite with Fe3", and the bacterial leaching of pyrites (washed and unwashed) and have tried to interrelate the rates of these reactions. MATERIALS AND METHODS Pyrite. The pyrite sample used was provided to us by the Mines Branch of Manitoba Energy and Mines. It was ground to-140 mesh (100-,um diameter by microscopic observation) and contained 45.9% Fe, 45.1% S, and 9% impurities. Media. The standard reaction medium used throughout this study was the HP medium (7, 10) consisting of 0.1 g of K2HPO4, 0.4 g of (NH4)2SO4, and 0.4 g of MgSO4 7H20 per liter, adjusted to pH 2.3 with H2SO4. The growth medium for Thiobacillus ferrooxidans was the HP medium plus 33.3 g of FeSO4 7H20 per liter (7, 10) and that for Thiobacillus thiooxidans was the HP medium with unsterilized powdered sulfur, 50 g/liter, as substrate (15). Organisms. T. ferrooxidans SM-4 and T. thiooxidans SM-6 were isolated from a sulfide ore mine site (7). T. ferrooxidans SM-4 was grown as described previously (16), and the harvested cells were washed and suspended in the HP medium to a concentration of 50 mg of wet cells per ml. T. thiooxidans was grown in 2.7-liter Fernbach flasks containing 1 liter of the HP medium. After inoculation with a 2.5% culture, 50 g of powdered elemental sulfur (sulfur precipitated; BDH Chemicals, Toronto, Canada) was spread evenly on the liquid surface. The flasks were incubated at 28°C for 5 days under stationary co...