The
method combining density functional theory (DFT) calculations
with microkinetic modeling has attracted increasing attention in obtaining
a deeper understanding of catalytic reactions. While product desorption
is conventionally regarded as an equilibrated process in the microkinetic
modeling, it might be influential to product selectivity when competing
reactions should be considered. In this work, a complex reaction network
is established first for the methane steam reforming reaction using
the equilibrium and immobile models over Ni, Pd, and Pt surfaces.
This provides a basis to further investigate the reaction mechanism
and kinetic modeling results. The results show that when different
desorption models are considered, the total activity regarding methane
conversion and the coverage and DRC value of the main species at the
steady state are the same on each surface. In contrast, the mechanism
of CO2 formation is varied based on different desorption
models. Consequently, the rate and selectivity of CO2 generation
on each metal catalyst are significantly improved when the barrier
of CO desorption is considered in the microkinetic modeling compared
with the modeling only with barrierless CO desorption.