Partial
oxidation catalysis is often fraught with selectivity problems,
largely because there is a tendency of oxidation products to be more
reactive than the starting material. One industrial process that has
successfully overcome this problem is partial oxidation of methanol
to formaldehyde. This process has become a global success, with an
annual production of 30 million tons. Although ruthenium catalysts
have not shown activity as high as the current molybdena or silver-based
industrial standards, the study of ruthenium systems has the potential
to elucidate which catalyst properties facilitate the desired partial
oxidation reaction as opposed to deep combustion due to a pressure-dependent
selectivity “switch” that has been observed in ruthenium-based
catalysts. In this work, we find that we are able to successfully
rationalize this “pressure gap” using near-ab initio
steady-state microkinetic modeling on RuO2(110). We obtain
molecular desorption prefactors from experiment and determine all
other energetics using density functional theory. We show that, under
ambient pressure conditions, formaldehyde production is favored on
RuO2(110), whereas under ultrahigh vacuum pressure conditions,
full combustion to CO2 takes place. We glean from our model
several insights regarding how coverage effects, oxygen activity,
and rate-determining steps influence selectivity and activity. We
believe the understanding gained in this work might advise and inspire
the greater partial oxidation community and be applied to other catalytic
processes which have not yet found industrial success.