The
char-O2 reaction under high-temperature entrained flow
conditions was investigated experimentally and numerically to study
the effect of the stoichiometric ratio (SR) on char-nitrogen conversion.
A numerical model was established based on the unsteady convection-diffusion
and reaction equations, in which Stefan flow was considered. The change
of specific surface area during char combustion was considered by
locally using the Random Pore Model (RPM). The intrinsic reactivity
parameters of char-O2 and char-NO reactions were measured
using a thermal gravimetric analyzer (TGA) and drop tube furnace (DTF),
respectively. The numerical results indicated that the predictions
of carbon conversion and NO release agreed well with experimental
data. Based on numerical results, for a given carbon conversion, with
the decrease of SR, the kinetics-diffusion controlled char-O2 reaction is pushed toward the kinetics-controlled regime, leading
to more significant local carbon conversion and thus more developed
pore structure inside char particles, including higher porosity and
larger specific surface area. Therefore, the oxidation of char-nitrogen
occurs more deeply inside char particles and NO release prefers to
diffuse toward the particle center, rather than outward. The larger
specific surface area deep inside the char particle also gives rise
to the total char-NO reaction rate at a lower SR. As a result, the
total fractional conversion of char-N to NO decreases as SR decreases
under high-temperature entrained flow combustion conditions.