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This document summarizes a study on the oxidation kinetics of zinc sulphide concentrate in a fluidized bed reactor. The study examined the effects of initial concentrate mass, air flow rate, and temperature on the fractional conversion. It found that the time for complete conversion was affected by the molar ratio of oxygen to sulfur and temperature. The oxidation reaction was determined to be controlled by surface chemical reactions, with an activation energy of 87 kJ/mole supporting a chemically controlle

Author

akshuk

Language

EN