The electrochemical
reduction of CO2 to chemical fuels
and value-added chemicals is a viable pathway to store renewably generated
electrical energy and to mitigate the negative impact of anthropogenic
CO2 production. Herein, we study how the local reaction
environment dictates the mechanism and kinetics of CO2 reduction
to CO at an Ag electrode. The local reaction environment is determined
using a hierarchical model that accounts for multistep reaction kinetics,
specific surface charging state at a given electrode potential, and
mass transport phenomena. The model reveals vital mechanistic insights
into the reaction behavior. The increasing Tafel slope with overpotential
is seen to be influenced by the surface charging relation and mass
transport effects. In addition, the decrease of the CO current density
at high overpotentials is found to be caused not only by the decrease
in CO2 concentration due to mass transport, surface charge
effects, and pH increase but also by lateral interactions between
HCOOad, COOHad, and Had. Moreover,
we explore how the electrolyte properties, including bicarbonate concentration,
solvated cation size, and CO2 partial pressure, tune the
local reaction environment.