Hydrogen production by biomass gasification in supercritical water over Ni/γAl 2O 3 and Ni/CeO 2-γAl 2O 3 catalysts

Abstract

Hydrogen production by supercritical water gasification (SCWG) is a promising technology for wet biomass utilization. Ni catalyst can realize the high gasification efficiency of biomass near the critical temperature of water. In this paper, Ni/γAl 2O 3 and Ni/CeO 2-γAl 2O 3 catalysts were prepared by an impregnation method. The catalyst performance for glucose gasification in supercritical water was tested in autoclave reactor. All experiments were carried out in the autoclave at 673 K, 24.5 MPa, and the concentration of glucose was 9.09 wt.%. The catalysts before and after reaction were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), BET specific surface area measurements, X-ray fluorescence spectrum (XRF) and Thermo-gravimetric analyses (TGA) in order to investigate on the chemical property and catalytic mechanism. The experimental results showed that hydrogen yield and hydrogen selectivity increased sharply with addition of Ni/γAl 2O 3 and Ni/CeO 2-γAl 2O 3 catalysts. The catalytic activity and H 2 selectivity of Ni/CeO 2-γAl 2O 3 was higher than that of Ni/γ-Al 2O 3 catalyst. The results revealed that carbon deposition and coking led to the deactivation of the catalysts. Ce in the Ni/CeO 2-γAl 2O 3 catalyst had a certain role in the inhibition of carbon deposition and coking.