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- W2029122396 abstract "The performance of a trickle bed is analyzed in terms of a mixing-cell concept in which the three-phase reactor is visualized as a number of mixing cells in series. Results are presented for an isothermal system involving a reaction of general-order kinetics and incorporating all mass transfer resistances. Limiting cases of very slow, and rapid, gas—liquid mass transfer are also considered. The utility of the new model is illustrated with an application to the oxidation of formic acid and by using the method to compare the performance of slurry and trickle-bed reactors." @default.
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- W2029122396 title "Mixing-cell method for design of trickle-bed reactors" @default.
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- W2029122396 doi "https://doi.org/10.1016/0300-9467(79)85002-9" @default.
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