The application of
oxygen carrier materials has one of its origins
in the chemical looping combustion processes, which aim at inherent
CO2 sequestration by realizing fuel oxidation in the absence
of combustion air. This concept can be transferred to conventional
fluidized bed combustion processes, the so-called oxygen carrier aided
combustion. The replacement of the conventionally applied bed material
with an oxygen carrier focuses mainly on large-scale circulating fluidized
bed combustion plants. The main stated performance improvements include
the reduction of carbon monoxide emissions even at lower excess air
ratios and the enhancement of the combustion efficiency. Nevertheless,
the ability of shifting oxygen in space and time is of certain interest
especially in small-scale bubbling fluidized bed systems. Imperfect
fuel mixing, limited residence time in the dense bed zone, as well
as limited system complexity often mitigate their combustion performance.
Process conditions in bubbling fluidized beds differ from those prevalent
in circulating beds regarding bed material particle size distribution,
fluidization velocities, or particle volume fraction in the bed. Within
this study, the widely used oxygen carrier ilmenite serves as bed
material in a laboratory bubbling fluidized bed combustion. The focus
was on the oxygen distribution profiles and their shift by ilmenite
into the bed during methane combustion. The variation of the excess
air ratio, fluidization velocity, and bed height reveal a significant
increase of the in-bed CO2 yield (max. 55%) within ilmenite
experiments. Moreover, the oxygen conversion profile confirms the
shift of the oxygen supply by ilmenite from the lower reactor part
to the reduction dominated zone. The amount of shifted oxygen increases
at lower excess air ratios. Thus, full conversion is not achieved
as kinetics and limited residence time in the bed inhibit the fuel
conversion.