Carbon-supported mono- and bimetallic
catalysts prepared via incipient
wetness impregnation were systematically studied in aqueous-phase
reforming (APR) of xylitol aiming at hydrogen production from biomass.
The catalytic performance of several VIII group metals and their combinations,
such as Pt, Ni, Pt–Ni, Re, Pt–Re, Ru, Pt–Ru,
and Pt–Co, was compared for xylitol APR in a fixed-bed reactor
at 225 °C and 29.7 bar (N2). Ni/C, Ru/C, and Re/C
catalysts displayed significantly lower activity compared to others.
Activity and selectivity to H2 of bimetallic Pt–Ni/C,
Pt–Co/C, and Pt–Ru/C catalysts were close to that of
Pt/C. Pt–Re/C catalyst showed an outstanding performance which
was accompanied by a shift of the reaction pathways to the alkane
formation and thereby lower hydrogen selectivity. Addition of the
second metal to Pt was not found to be beneficial for hydrogen production,
thus leaving Pt/C as the optimum carbon-supported catalyst.