Coal gas desulfurization is one of the most important gas
cleaning steps previous to its use in a gas turbine in
integrated gasification combined cycle (IGCC) systems. In
this work, 12 different calcium based materials, both
natural, commercial and modified with several additives,
were tested in a drop tube reactor as potential H2S removal
agents at high temperatures and reducing conditions.
Three limestones and a dolomite were selected by their
different natures and reactivities. The commercial products
used were calcium hydroxide, calcium acetate (CA), and
calcium magnesium acetate (CMA). Moreover, two limestones
of different nature and reactivity were used as starting
material to prepare several calcium hydroxides modified
with calcium lignosulfonate (LGS) and calcium acetate (CA).
An important improvement in sulfur removal respect to
the sorbent prepared without additives was achieved when
using the modified sorbents. However, the highest sulfur
removal was obtained with CA and CMA sorbents due to
their ability to form highly porous cenospheres of thin
walls. H2S capture up to near the thermodynamic equilibrium
was achieved with dry-injection of the CA and CMA at
furnace gas temperatures of about 1000 and 800 °C,
respectively, a Ca/S molar ratio of 2, and 0.8 s of residence
time.