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- W2006609081 abstract "A simulation of the performance of several reactor types with different contact patterns between reactants and catalyst is presented for the vanadium catalysed SO2-Oxidation process. The numerical calculations are based on a kinetic model, previously derived in an extensive investigation in our laboratory. A dual-reactor system in which the liquid catalyst is circulated between two reactors, each held at a different temperature and with different feed composition, is shown to be better than any single reactor configuration in an important range of SO2 conversion. Advantages of this mode of operation are pointed out both as regards to kinetic studies and for industrial processing. Also beyond the specific reaction treated in this study a systematic comparison of different contacting patterns between reactants and catalyst may prove to be valuable. It may ultimately contribute to the selection of the best reactor type when the catalytic cyclus and the tranport parameters are given for the system." @default.
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- W2006609081 date "1982-01-01" @default.
- W2006609081 modified "2023-09-27" @default.
- W2006609081 title "Steady state operation of a dual-reactor system with liquid catalyst" @default.
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- W2006609081 doi "https://doi.org/10.1016/0009-2509(82)80140-1" @default.
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