A chemical kinetic model is developed for the non-catalytic reduction
of nitric oxide (NO) by hydrazine(N2H4). Since the reduction of NO was
observed in an experimental reaction with N2H4, the hydrazine has bee
n suggested as a new reductant of NO in addition to the conventional a
mmonia, urea and isocyanic acid. In the proposed kinetic model, a set
of fifty one chemical reactions that includes the various branching re
actions of N2H4 to NH2 and the well-known reaction NO + NH2 --> N-2 H2O is simultaneously considered with the usual partial equilibrium as
sumptions. The NO reduction is estimated to occur at a temperature ran
ge between 700 K and 1400 K, which is wider and lower than in the conv
entional Thermal DeNOx process. The, maximum amount of the reduced NO
is slightly less than that in the Thermal. DeNOx. The effects of the o
ther input parameters on the Ne) reduction rare are also discussed.