Catalytic
activity and stability, reflected in high conversion,
heat sink, and time on stream, are the major concerns of endothermic
hydrocarbon fuel cracking. In this work, we synthesized a stable MgAl2O4 spinel support by the co-precipitation method
and a Pt/MgAl2O4 catalyst by the liquid-phase
reduction-impregnation method (PMA-V) and incipient-wetness impregnation
method (PMA). PMA-V showed a better catalytic activity and stability
than PMA. Moreover, the heat sink and stability are significantly
superior to the Pt-based catalysts in our previous published works.
Through a series of catalyst characterization, we found that the high
catalytic activity and stability over PMA-V are owing to the “accessible”
Pt active sites with better dispersion and a smaller Pt size, which
can efficiently alleviate Pt sintering, stronger metal–support
interaction, suitable acidity–alkalinity, and a stable MgAl2O4 spinel structure. The valuable information provided
in this work provides an effective approach to improve both catalytic
activity and stability for hydrocarbon cracking.