Nanoarchitectonics of Ni/CeO2 Catalysts: The Effect of Pretreatment on the Low-Temperature Steam Reforming of Glycerol

CeO2 nanosphere-supported nickel catalysts were prepared by the wetness impregnation method and employed for hydrogen production from glycerol steam reforming. The dried catalyst precursors were either reduced by H-2 after thermal calcination or reduced by H-2 directly without calcination. The catalysts that were reduced by H-2 without calcination achieved a 95% glycerol conversion at a reaction temperature of only 475 degrees C, and the catalytic stability was up to 35 h. However, the reaction temperature required of catalysts reduced by H-2 with calcination was 500 degrees C, and the catalysts was rapidly inactivated after 25 h of reaction. A series of physicochemical characterization revealed that direct H-2 reduction without calcination enhanced the concentration of oxygen vacancies. Thus, the nickel dispersion was improved, the nickel nanoparticle size was reduced, and the reduction of nickel was increased. Moreover, the high concentration of oxygen vacancy not only contributed to the increase of H-2 yield, but also effectively reduced the amount of carbon deposition. The increased active nickel surface area and oxygen vacancies synergistically resulted in the superior catalytic performance for the catalyst that was directly reduced by H-2 without calcination. The simple, direct hydrogen reduction method remarkably boosts catalytic performance. This strategy can be extended to other supports with redox properties and applied to heterogeneous catalytic reactions involving resistance to sintering and carbon deposition.

Automated summary

CeO2 nanosphere-supported nickel catalysts were directly reduced by H-2 without calcination, which enhanced the concentration of oxygen vacancies, improved the nickel dispersion and reduction, and resulted in superior catalytic performance for hydrogen production from glycerol steam reforming.