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This paper compares two modeling approaches of the dynamic behavior of a fixed bed that contains treated sewage sludge for biogas desulfurization.
The behavior of a fixed bed consisting of amalgamated copper screens has been investigated for the electrolytic reduction of nitrobenzene to p-aminophenol under potentiostatic condition (controlled potential).
The dynamic behavior of a fixed bed reactor has been examined using benzene hydrogenation on Ni/kieselguhr, poisoned by thiophene, as a model reaction.
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The behavior of a reactor of a fixed bed composed by high-productive V2O5 TiO2 (anatase) supported catalysts for oxidation of o-xylene into phthalic anhydride is theoretically and experimentally investigated.
Another thing about crossover that should be analyzed is the behavior of TSc for a fixed m while n increases continuously.
The same general behavior was also observed upon titration of a fixed amount of Av1 with different CRs of Av2 at pH 9.5, although the amounts of product formed per time are much smaller than at pH 7.8.
Allowing for cells with different behavior, allows the cells to continue 'aging' in a tumor of a fixed size.
The proposed control algorithm was tested in the control of a fixed bed catalytic reactor, which has a complex dynamic behavior.
The value of Nuw that is used in a simulation of a fixed bed catalytic reactor can have a strong effect on the predicted behavior.
and the influence of a fixed bar.
The poisoning kinetics of thiophene on Ni-kieselguhr catalysts and the deactivation behavior of nonisothermal fixed bed reactors have been studied experimentally using benzene hydrogenation as a model exothermic reaction.
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