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- W1968657434 abstract "Abstract Published mathematical models for the steady-state operation of integral trickle-bed reactors are not all capable of predicting experimental results obtained for the catalytic oxidation of sulfur dioxide over activated carbon. Only the model of Mata and Smith (Chem. Eng. J., 22 (1981) 229), which considers variable gas composition within the reactor as well as the variability of the wetting efficiency with the liquid flow rate was successful. An empirical relationship between the wetting and the liquid flow rate was derived from steady-state data and found to coincide with that of Herskowitz (Chem. Eng. J., 22 (1981) 167)." @default.
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- W1968657434 date "1990-05-01" @default.
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- W1968657434 title "Steady-State models for SO2 oxidation in a trickle-bed reactor" @default.
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- W1968657434 doi "https://doi.org/10.1016/0300-9467(90)80013-3" @default.
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