NH3-SCR over Cu-CHA catalysts is a key technology for NOx reduction, involving a CuII/CuI redox cycle. Formation of the greenhouse gas N2O during NH3-SCR remains a concern. Here, we use DFT calculations (CI-NEB and dimer methods) to examine the role of NO2 in standard SCR reduction and oxidation half-cycles and its consequences for N2O formation. In the reduction half-cycle, we compared N2-forming and NO-consuming standard SCR reactions with parallel NO2-consuming and N2O-forming steps over various CuII active sites: framework associated CuII (Z2Cu, ZCuOH), NH3-solvated mononuclear (Z2Cu(NH3), ZCuOH(NH3)), and binuclear CuII (ZCuO2CuZ(NH3)4). Both NO and NO2 reactions involve NOx attack on Cu-bound NH3 with proton transfer to the framework or Cu-bound O or OH-. Activation energies for NO2 reactions are generally higher than for NO, except for NH3-solvated ZCuOH, where they are comparable. Microkinetic models predict highest N2O selectivity on NH3-solvated ZCuOH (1-10%) at a NO2:NOx ratio of 0.1 and 473 K, due to favorable proton transfer from NH3 to OH- and greater product stability. Other CuII sites show less than 1% selectivity. N2O selectivity is greater on NH3-solvated mononuclear CuII sites than their framework-associated counterparts. In the oxidation half-cycle, we examine parallel oxidation of mononuclear CuI (CuI(NH3)2) species with O2 or NO2 and their subsequent reactions with NO and NO2. Computed Gibbs formation free energies suggest a strong thermodynamic driving force for the formation of Cu-nitrate or [CuNO3]I-like intermediates. DFT calculations indicate that reactions of Cu-nitrate species with NH3 can lead to N2O generation. The results are consistent with steady-state reactor experiments over Cu-SSZ-13 that showed N2O formation rates increase with feed NO2 pressure. The results suggest that suppressing NO2-driven side reactions in both reduction and oxidation half-cycles can mitigate N2O emissions during NH3-SCR over Cu-CHA.