This paper presents a new method for the determination of NOx formation fro
m industrial boilers. The flow and temperature fields within the furnace, o
btained through CFD codes, are approximated by a network of ideal reactors.
This approach allows using a very detailed and comprehensive kinetic model
, without losing the detailed thermal and fluidynamic information. The mean
ing of this work is to move a further step in the direction of a better des
cription of both kinetic and fluidynamic aspects during combustion. The pre
diction of pollutant byproducts, whose amount is in terms of ppms or even p
pbs, necessarily requires the use of a detailed description of the process
chemistry. Moreover, in the case of NOx formation, the air and fuel staging
, as applied to more recent plants, implies the interactions between nitric
oxides and hydrocarbon radicals. A detailed description of these reaction
paths is extremely important to correctly reproduce the final emissions. Th
e comparison of the obtained predictions with the experimental industrial r
esults shows a quite satisfactory agreement. qualitatively and quantitative
ly, in different operating conditions and plant configurations. (C) 2001 El
sevier Science Ltd. All rights reserved.