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This document discusses the catalytic oxidation of SO2 in a multi-bed reactor system for producing sulfuric acid. Key points: 1) SO2 oxidation is exothermic and equilibrium limited, requiring multiple reactors with inter-bed cooling to achieve near 100% conversion. 2) Vanadium pentoxide is used as the catalyst, which must be in molten state above 673K to be effective. 3) A multi-bed reactor design with inter-bed heat exchange allows maintaining temperatures near the equilibrium line for high conversion

Author

Luthando

Language

EN