We investigated the steady-state and transient effects of reductants (CO, H 2 and C 3 H 6 ) on NO 2 reduction, NH 3 -SCR (selective catalytic reduction), NH 3 adsorption and oxidation, and N 2 O production on a Cu-SSZ-13 monolithic catalyst. The three reductants affect to different extents the standard SCR (NO + NH 3 + O 2 ), fast SCR (NO + NH 3 + NO 2 ), and slow SCR (NH 3 + NO 2 ). This study underscores the importance of accounting for the impact of reducing agents on conventional NH 3 -SCR reaction mechanism when SCR catalyst is subjected to either rich regeneration of integrated systems (LNT + SCR, SCR on DPF) or cold-start. Propylene is most effective in promoting NO 2 reduction to NO by formation of organic intermediates. CO effectively reduces nitrates to nitrites that then react with NO 2 , releasing NO. H 2 can follow a similar pathway as CO but is less effective. In addition, H 2 can also enable a H 2 -based SCR pathway through the reduction of Cu cations to Cu 0 which then catalyze the NOx reduction. This pathway is particularly evident at high temperatures and low O 2 levels. As for NH 3 -SCR reactions, propylene competes with NH 3 for adsorbed NO 2 , which generates NO and thus increases the NO/NOx ratio. This leads to the dominance of either fast or standard SCR for a slow SCR (NH 3 + NO 2 ) feed condition when C 3 H 6 is present. CO has only a minor effect on both standard and fast SCR but a promoting effect on slow SCR. The ineffective reduction of NO 2 to NO by H 2 at low temperature (T < 250 o C) results in a negligible effect on slow SCR. In contrast to steady-state operation, lean/rich cycling enhances cycle-averaged NOx conversion for each of the NH 3 -SCR reactions when adding either C 3 H 6 or a CO + H 2 mixture in the rich phase. A decreased N 2 O generation rate from the slow SCR reaction is observed when any of the three reductants are present due in part to their reaction with ammonium nitrates.