Jm. Veranth et al., NUMERICAL MODELING OF THE TEMPERATURE DISTRIBUTION IN A COMMERCIAL HAZARDOUS-WASTE SLAGGING ROTARY KILN, Environmental science & technology, 31(9), 1997, pp. 2534-2539
The gas, wall, and bed temperatures in a hazardous waste incineration
kiln were studied using a commercially available, CFD-based, reacting
flow code, which included radiation heat tra nsf er. The mod el was co
mpared to field measurements made on a co-current flow, 35 MW slagging
rotary kiln. Cases were run to determine the sensitivity of the predi
ctions to changes in the model assumptions and to simulate the normal
variation in combustion inputs. The model predictions of the peak bed
temperature, of the axial temperature profile, and of the gas temperat
ure at the exit-plane were consistent with the measurements at a full-
scale waste incinerator during normal operation. The model and the fie
ld observations both indicate that the peak bed temperature occurs nea
r the middle of the kiln and that the difference between the peak bed
temperature and the exit-plane gas temperature depends on the inlet fl
ows. The geometry of the transition between the kiln and the secondary
combustion chamber and the fuel-to-air equivalence ratio have the gre
atest effect on the calculated temperature distribution. Modeling stud
ies provide useful information such as the relationship between availa
ble measurements and the temperature at inaccessible lo cations inside
a full-scale kiln.