A new incineration facility that has a disposal rate of 48 ton day(-1) has
been constructed for design concept analysis. Local temperatures inside the
furnace and concentrations of carbon monoxide and oxygen in the stack were
continuously monitored during the experiments. Computational fluid dynamic
s (CFD) were employed to analyse the flow field in the furnace. Equations f
or radiation and turbulence as well as chemical reactions were solved. The
results of temperature measurement were used to set the boundary condition
for the CFD analysis. Computation and experiment were compared and cross-ch
ecked to evaluate the combustion gas flow performance. The temperature dist
ribution above the waste bed indicated the combustion state of the waste. I
n the active reaction zone, the temperature changed rapidly in both positio
n and time due to inhomogeneous reaction, whereas, in the cooling zone, the
temperature had an almost constant value. The CFD analysis based on the as
sumptions of the bed combustion overpredicted the gas phase reaction rate.
However, it showed reasonable agreement with the experimental results regar
ding the flow pattern and mixing performance. Three dead zones were detecte
d by the CFD analysis. The predicted temperature and oxygen concentration s
howed poor mixing performance inside the initial incinerator design.