A model for simulating reburning in semi-industrial scale has been dev
eloped. It consists of a recently developed reaction mechanism for reb
urning with C-1 and C-2 hydrocarbons, in combination with ideal reacto
r modeling and a simplified mixing approach. The reaction mechanism as
well as the mixing model has been validated separately against experi
mental data from laboratory and pilot scale tests. Modeling prediction
s have been compared with experimental data from a number of pilot sca
le studies of gas reburning with good results. The large differences i
n reburn efficiency reported in different low-temperature pilot scale
experiments are reconciled in terms of the different operating conditi
ons used. The model has been used to assess the potential of the rebur
n process at low temperatures, and recommendations for process optimiz
ation are provided. Results show that the low-temperature gas reburn p
rocess has a significant potential for NO reduction and that both the
reburn and burnout regions are important in process optimization.