Partial Oxidation of Methane
to Syngas Over γ‑Al<sub>2</sub>O<sub>3</sub>‑Supported
Rh Nanoparticles: Kinetic and
Mechanistic Origins of Size Effect on Selectivity and Activity
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Abstract
A series of supported Rh/γ-Al<sub>2</sub>O<sub>3</sub> catalysts
with an overall metal loading of 0.005 wt % was synthesized by impregnation
of γ-Al<sub>2</sub>O<sub>3</sub> with a toluene solution containing
colloidally prepared well-defined (1.1, 2.5, 2.9, 3.7, and 5.5 nm)
Rh nanoparticles (NP). The size of NP was not found to change after
their deposition on γ-Al<sub>2</sub>O<sub>3</sub> and even after
performing partial oxidation of methane (POM) to synthesis gas at
1073 K for 160 h on stream. Apparent CO formation turnover rates and
CO selectivity strongly decrease with an increase in this size. Contrarily,
the overall scheme of POM is size-independent, i.e. CO and H<sub>2</sub> are mainly formed through reforming reactions of CH<sub>4</sub> with
CO<sub>2</sub> and H<sub>2</sub>O at least under conditions of complete
oxygen conversion. The size effect on the activity and selectivity
was related to the kinetics of interaction of CH<sub>4</sub>, O<sub>2</sub>, and CO<sub>2</sub> with Rh/γ-Al<sub>2</sub>O<sub>3</sub> as concluded from our microkinetic analysis of corresponding transient
experiments in the temporal analysis of products reactor. The rate
constants of CH<sub>4</sub>, O<sub>2</sub>, and CO<sub>2</sub> activation
decrease with an increase in the size of supported Rh NP thus influencing
both primary (methane combustion) and secondary (reforming of methane)
pathways within the course of POM