Selectivity Trends and Role of Adsorbate-Adsorbate Interactions in CO Hydrogenation on Rhodium Catalysts
Martin Deimel (1), Hector Prats (2), Michael Seibt (1), Karsten Reuter, (3), Mie Andersen (4, 5) ((1) Chair for Theoretical Chemistry and, Catalysis Research Center, Technical University of Munich, Garching, Germany,, (2) Department of Chemical Engineering

TL;DR
This study uses advanced kinetic Monte Carlo simulations with explicit adsorbate interactions to clarify how Rh catalyst surface structure influences selectivity in CO hydrogenation, resolving previous discrepancies in theoretical predictions.
Contribution
It introduces a systematic approach to include adsorbate-adsorbate interactions in microkinetic modeling, improving accuracy in predicting selectivity trends on Rh surfaces.
Findings
Rh(111) favors methane production
Rh(211) produces methane and acetaldehyde
Coverage-dependent models are insufficient to capture selectivity
Abstract
Predictive-quality computational modeling of heterogeneously catalyzed reactions has emerged as an important tool for the analysis and assessment of activity and activity trends. In contrast, more subtle selectivities and selectivity trends still pose a significant challenge to prevalent microkinetic modeling approaches that typically employ a mean-field approximation (MFA). Here, we focus on CO hydrogenation on Rh catalysts with the possible products methane, acetaldehyde, ethanol and water. This reaction has already been subject to a number of experimental and theoretical studies with conflicting views on the factors controlling activity and selectivity towards the more valuable higher oxygenates. Using accelerated first-principles kinetic Monte Carlo (KMC) simulations and explicitly and systematically accounting for adsorbate-adsorbate interactions through a cluster expansion…
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