Hydrogenolysis of xylitol can produce
value-added glycols and alcohols
for industrial chemicals.
However, it is often carried out under elevated temperature and pressure,
causing unfavorable catalyst deactivation and significant formation
of side products. Catalytic transfer hydrogenolysis of xylitol, under
much milder conditions, is largely unexplored in this field. Herein,
we reported transfer hydrogenolysis of xylitol with in situ-formed H2 in batch slurry reactors over synergistic Pd–Pt/TiO2 catalysts. Although monometallic Pd/TiO2 and Pt/TiO2 catalysts display poor activity and selectivity, bimetallic
Pd–Pt/TiO2 catalysts showed synergetic performances
for tandem H2 generation and hydrogenolysis of xylitol.
A combined yield of 41.1% to propylene glycol and ethylene glycol
was thus obtained on the Pd–Pt/TiO2 catalyst at
220 °C and 1 MPa N2. Detailed structure-dependency
studies on PdPt particle size (2.4–5.2 nm) revealed that C–H,
C–O, and C–C bond cleavage displays strong size-determining
trends. Therefore, conversion of xylitol displays an optimal selectivity
toward glycols and alcohols with a PdPt particle size of approximately
4.4 nm. In addition, influence of experimental parameters, including
temperature (200–230 °C), N2 pressure (0–3
MPa), and alkali/xylitol molar ratio (0–0.25), was also studied
with respect to conversion and production distribution. The outcome
of this work offers mechanistic insights into atom-efficient conversion
of bioderived oxygenates to renewable chemicals.