Abstract
CO hydrogenation is a promising approach for the storage of renewable energy in the form of hydrocarbons via the Fischer-Tropsch synthesis (FTS). Since transient operation of FTS reactors might be necessary and even be beneficial, transient kinetics for a rational catalyst and reactor design are essential. In order to advance the development of such transient kinetics, the periodic transient kinetics (PTK) method was applied to the CO hydrogenation on a Co/TiO2 catalyst under FT-like conditions. It was revealed that there are two carbon species of different reactivity, Cα and Cβ, present on the catalyst surface during the reaction. Cα forms fast within a few seconds and is highly reactive, while Cβ forms slowly, is accumulating on the surface over a longer time and imposes an inhibiting effect. However, a contribution of Cβ to the chain growth reaction was shown. Finally, the transient experimental results are evaluated based on a material balance and the amounts of Cα and Cβ present on the catalyst surface during the reaction were determined.
Supplementary materials
Title
Supporting Information
Description
In the supporting information we provide additional data for the catalyst characterization, the dynamic experiments and the separation of Cα and Cβ.
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