Reduction–oxidation cycles in oxides are ubiquitous
in oxygen
storage and transport, chemical looping processes, and fuel cells.
O-atom addition and removal are mediated by coupling reactions of
oxidants and reductants at surfaces with diffusion of O-atoms within
oxide crystals, with either or both processes as limiting steps. CeO2–ZrO2 solid solutions (CZO) are ubiquitous
in practice. They are used here to illustrate general experimental
strategies and reaction–diffusion formalisms for nonideal systems
that enable assessments of the kinetic relevance of the steps that
mediate O-atom addition and removal in these materials; these experiments
are described within the context of models that describe the driving
forces for reaction and diffusion rigorously in terms of oxygen chemical
potentials (μO). These strategies assess the rate
consequences of varying the fluid phase redox potential, through changes
in the identity and pressures of the reactants and products used in
redox cycles (O2; CO/CO2; H2/H2O; N2O/N2), of introducing dispersed
metal nanoparticles that capture and react lattice O-atoms in CZO
using CO or H2, and of imposing intervening dwells without
reaction within redox cycles. O-removal rates depend on reductant
pressures, even when CO/CO2 and H2/H2O ratios are chosen to maintain the same surface μO if surface reactions were quasi-equilibrated. These data, taken
together with significant rate enhancements in O-removal when Pt nanoparticles
are present at CZO crystal surfaces and with similar rates before
and after inert dwells, demonstrate that reduction rates by both CO
and H2 are limited by surface reactions without the presence
of consequential spatial gradients in μO within CZO
crystals. In contrast, O-addition rates to partially reduced CZO crystals
are similar for N2O and O2 reactants and are
not affected by the presence of Pt nanoparticles; O-addition rates
are significantly higher after intervening inert dwells during CZO
oxidation, indicative of spatial gradients in μO,
which relax during nonreactive periods. These methods and models,
illustrated here for CZO redox cycles at conditions relevant to oxygen
storage practice, allow systematic assessments of the kinetic relevance
of lattice diffusion and surface reactions for systems that use solids
for the reversible storage and release of atoms, irrespective of the
identity of the solids or the atoms (e.g., O, H, N, and S).