Nitrous oxide (N 2 O) is a significant greenhouse gas and its emissions from fluidized bed combustion systems can be controlled using catalytic conversion and decomposition. The catalytic decomposition of N 2 O was studied in a quartz fixed-bed reactor at 450-700 • C. The low-cost catalyst was prepared from fly ash and iron oxides, and was characterized in terms of the BET specific surface area and XRD. This study showed that both the Fe content on the catalyst surface and the calcination temperature during the preparation of the catalyst should be optimized in order to significantly improve the catalyst performance when used for N 2 O decomposition. The influences of O 2 , H 2 O, CO 2 and SO 2 on the N 2 O decomposition were investigated at the most reactive temperature. Experimental results showed that O 2 had a small negative effect on the catalytic activity, while CO 2 had no obvious effect on the N 2 O decomposition. The N 2 O conversion was still high even when H 2 O was present. However, the N 2 O conversion dropped sharply when H 2 O and O 2 were both present. The catalytic activity was reduced by SO 2 because of its reaction with the catalyst. The difference between the N 2 O conversion with H 2 O present and with both H 2 O and O 2 present was analyzed in order to determine the N 2 O decomposition mechanism. Two mechanisms for the N 2 O catalytic decomposition mechanism have been considered, of which the one with formation of oxygen atoms at two sites with migration and recombination shows better agreement with our experimental results.