The variables, kinetics, and mechanisms of heterogeneous reburning were studied in a flow reactor with a simulated flue gas. Ac efficiency of heterogeneous reburning depends on the origin of the char, char preparation history, and the presence of oxidants, CO2 and O-2 and the reducing agent CO, in reburning. Estimated intrinsic rate constants for surface NO reduction in various gaseous environments were compared with those published. In addition to its large surface area, the effectiveness of lignite char appears to be due to its ability to promote two consecutive reactions: (1) the gasification of char by CO2 and O-2 for production of CO; (2) the removal of surface oxygen complexes, including those formed after adsorption of NO, by, gaseous CO, for the regeneration of reactive sites. Moreover, lignite ash also catalyzes the decomposition of HCN, a major intermediate of NO conversion during gas reburning. These observations suggest that reburning by, a mixed fuel containing natural gas and lignite char can be a potentially, attractive route for the in-furnance control of nitrogen oxide.