The application of structured reactors provides a number
of advantages
in chemical processes. In this paper, two different three-dimensional
(3D) Fe/SiC catalysts with a square cell geometry have been manufactured
by Robocasting: monoliths (D = 14 and H = 15 mm) and meshes (D = 24 and H = 2 mm) and studied in the catalytic phenol oxidation by hydrogen
peroxide (H2O2) for the sustainable production
of dihydroxybenzenes (DHBZ). The fluid dynamics, catalytic performance,
reaction rates, external mass transport limitation, and catalyst stability
have been compared in three different reactors, monolithic fixed-bed
reactor, multimesh fixed-bed reactor, and monolithic stirrer reactor,
at selected operating conditions. The results show that the mechanical
stirring of the 3D Fe/SiC monoliths avoids the external mass transfer
limitation caused by the presence of oxygen bubbles in the channels
(produced from the HO
x
· species in
autoscavenging radical reactions). In addition, the backmixing has
a positive effect on the efficient consumption of H2O2 but an adverse effect on the phenol selectivity to DHBZ since
they are overoxidized to tar products at longer contact times. On
the other hand, the wall porosity, and not the backmixing, affects
the susceptibility of the 3D Fe/SiC catalyst to the Fe leaching, as
occurs in the mesh structures. In conclusion, the monoliths operating
under plug-flow and external mass transfer limitation in the monolithic
fixed-bed reactor (MFB) provide an outstanding phenol selectivity
to DHBZ and catalyst stability.