A. Jensen et Je. Johnsson, MODELING OF NOX EMISSIONS FROM PRESSURIZED FLUIDIZED-BED COMBUSTION -A PARAMETER STUDY, Chemical Engineering Science, 52(11), 1997, pp. 1715-1731
Simulations with a mathematical model of a pressurized bubbling fluidi
zed-bed combustor (PFBC) combined with a kinetic model for NO formatio
n and reduction are reported. The kinetic model for NO formation and r
eduction considers NO and NH3 as the fixed nitrogen species, and inclu
des homogeneous reactions and heterogeneous reactions catalyzed by bed
material and char. Simulations of the influence of operating conditio
ns: air staging, load, temperature, fuel particle size, bed particle s
ize and mass of bed material on the NO emission is presented and compa
red to results from the literature. In general, the trends predicted b
y the model are in good agreement with the experimental observations.
A rate of production analysis for the nitrogenous species is used to i
dentify the important reactions for formation and reduction of NO. Acc
ording to the kinetic model, the reduction of NO by CO catalyzed by be
d material is very important, especially at low temperatures where the
CO concentration in the bed is high. The sum of the reduction of NO b
y char and by CO catalyzed by char increases with increasing temperatu
re, but is lower than usually attributed to these reactions. In the te
mperature range 973-1273 K, 20-30% of the fuel-N in the form of NH3 is
oxidized catalytically to N-2 over bed material and so this reaction
is important for a low conversion of fuel-N to NO. The importance of t
he homogeneous oxidation of NH3 to NO and reduction of NO by NH3 incre
ases with increasing temperature. The sensitivity of the simulated NO
emission with respect to hydrodynamic and combustion parameters in the
model is investigated and the mechanisms by which the parameters infl
uence the emission of NO is explained. The analysis shows that the mos
t important hydrodynamic parameters are the minimum fluidization veloc
ity, the bubble size, the bubble rise velocity and the gas interchange
coefficient between bubble and dense phase. The most important combus
tion parameters are the rates of CO and CH4 combustion and the CO/(CO
+ CO2) ratio from char combustion. (C) 1997 Elsevier Science Ltd.