Computational
fluid dynamics (CFD) tools are increasingly gaining
importance to obtain detailed insight into biomass gasification. A
major shortcoming of the current CFD tools to study biomass gasification
is the lack of computationally affordable chemical kinetic models,
which allows detailed predictions of the yield and composition of
various gas and tar species in complex reactor configurations. In
this work, a detailed mechanism is assembled from the literature and
reduced to a compact model describing the gas-phase reactions of biomass
gasification in the absence of oxygen. The reduction procedure uses
a graph-based method for unimportant kinetic pathways elimination
and quasi-steady-state species selection. The resulting reduced model
contains 39 gas species and 118 reactions and is validated against
the detailed model and two experimental configurations: the pyrolysis
of volatile species, such as levoglucosan, in a tubular reactor, and
the fast pyrolysis of biomass particles in a drop tube reactor. The
reduced model predicts the evolution of major gas products (e.g.,
CO, CO2, CH4, H2) and various classes
of tar (e.g., single-ring aromatics, oxygenated aromatics, PAHs) produced
during biomass gasification. The capability of the reduced model to
adequately capture the chemical process in a complex reactor geometry
at an acceptable computational cost is demonstrated by employing it
in a simulation of a pseudo two-dimensional laboratory-scale fluidized
bed reactor.