A computational fluid dynamics model,
consisting of a mixing chamber coupled with a catalytic converter,
is developed for the selective catalytic reduction (SCR) of NO
x
using urea. The NH3 required for
the SCR reactions is produced from the injection and decomposition
of urea in the mixing chamber. The conversion efficiency and concentration
distribution of NH3 from the mixing chamber are analyzed
for a range of operating conditions. The flow and species distribution
profiles from the mixing chamber are incorporated as inlet boundary
conditions at the entrance of the downstream SCR convertor. The SCR
convertor comprises a central catalytic monolith and inlet and outlet
diffuser sections. Variations in NO
x
concentration
were observed within the monolith due to heat losses and nonuniformities
in ammonia concentrations. While heat effects under non-isothermal
conditions slightly improved the NO
x
conversion
efficiency, nonuniformities in ammonia concentrations did not significantly
influence the SCR performance. Thus, the radial variations in NH3 concentrations, owing to nonuniformity at the outlet of the
mixing chamber, did not considerably impact the overall performance
of the SCR. The effects of temperature, NO:NO2 ratio, and
inlet velocity were investigated.