The steadily increasing
consumption of natural gas imposes a need
to facilitate the handling and distribution of the fuel, which presently
is compressed or condensed. Alternatively, reduced volatility and
increased tractability are achieved by converting the chemical energy
of the main component, methane, into liquid methanol. Previous studies
have explored direct methane-to-methanol conversion, but suitable
catalysts have not yet been identified. Here, the complete reaction
cycle for methane-to-methanol conversion over the Cu-SSZ-13 system
is studied using density functional theory. The first step in the
reaction cycle is the migration of Cu species along the zeolite framework
forming the Cu pair, which is necessary for the adsorption of O2. Methane conversion occurs over the CuOOCu and CuOCu sites,
consecutively, after which the system is returned to its initial structure
with two separate Cu ions. A density functional theory-based kinetic
model shows high activity when water is included in the reaction mechanism,
for example, even at very low partial pressures of water, the kinetic
model results in a turnover frequency of ∼1 at 450 K. The apparent
activation energy from the kinetic model (∼1.1 eV) is close
to recent measurements. However, experimental studies always observe
very small amounts of methanol compared to formation of more energetically
preferred products, for example, CO2. This low selectivity
to methanol is not described by the current reaction mechanism as
it does not consider formation of other species; however, the results
suggest that selectivity, rather than inherent kinetic limitations,
is an important target for improving methanol yields from humid systems.
Moreover, a closed reaction cycle for the partial oxidation of methane
has long been sought, and in achieving this over the Cu-SSZ-13, this
study contributes one more step toward identifying a suitable catalyst
for direct methane-to-methanol conversion.