Many catalyst devices employ flow through porous structures, which leads to a
complex macroscopic mass and heat transport. To unravel the detailed dynamics
of the reactive gas flow, we present an all-encompassing model, consisting of
thermal lattice Boltzmann model by Kang et al., used to solve the heat and mass
transport in the gas domain, coupled to a finite differences solver for the
heat equation in the solid via thermal reactive boundary conditions for a
consistent treatment of the reaction enthalpy. The chemical surface reactions
are incorporated in a flexible fashion through flux boundary conditions at the
gas-solid interface. We scrutinize the thermal FD-LBM by benchmarking the
macroscopic transport in the gas domain as well as conservation of the enthalpy
across the solid-gas interface. We exemplify the applicability of our model by
simulating the reactive gas flow through a microporous material catalysing the
so-called water-gas-shift reaction