The
supercritical water gasification of xylose, a model substrate
for hemicellulose, was carried out at 400 and 450 °C and at a
constant pressure of 25 MPa in the presence of acetic acid using a
continuous flow reactor. More specifically, we aimed to compare the
reaction rate constants of xylose decomposition in both the presence
and absence of acetic acid. Upon the application of a residence time
of 0.5–5 s, a xylose concentration of 1.5 wt %, and an acetic
acid concentration of 1.5 wt %, we successfully elucidated the effect
of acetic acid on each reaction within the reaction network for the
first time. In the presence of acetic acid, the retro-aldol reactions
and carbon gasification production (i.e., the radical reactions) were
suppressed, while the acetic-acid-catalyzed dehydration of xylulose
to furfural (i.e., an ionic reaction) was enhanced by 2 orders of
magnitude. As such, reaction control through the addition of chemical
species to either stabilize ions or react with radicals appears possible.