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• W2077883602 abstract "A theoretical model is presented for describing the performance of bubble-column reactors used for Fischer-Tropsch synthesis. The model accounts for axial dispersion in both the gas and liquid phases, and for non-uniform distribution of catalyst. The influence of H2 and CO concentrations in the liquid phase on the stoichiometry and kinetics of the synthesis and water-gas-shift reactions are treated rigorously. Calculations have been carried out to illustrate the influence of transport parameters on syngas conversion and axial distribution of reactants and products. Comparisons are also made with recently reported experimental results, to demonstrate the capability of the model to predict the dependence of the syngas conversion and H2CO consumption ratio on feed composition and velocity." @default.
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• W2077883602 date "1985-01-01" @default.
• W2077883602 modified "2023-10-12" @default.
• W2077883602 title "A theoretical model for the performance of bubble-column reactors used for Fischer-Tropsch synthesis" @default.
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• W2077883602 doi "https://doi.org/10.1016/0009-2509(85)80027-0" @default.
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