Comparison of Ni Based and Rh Based Catalyst Performance in the Oxidative Steam Reforming of Raw Bio-Oil

The effect of O 2 content in the oxidative steam reforming (OSR) of raw bio-oil has been studied, and the kinetic behavior, particularly deactivation, has been compared between two catalysts (Ni/La 2 O 3 -αAl 2 O 3 and Rh/CeO 2 -ZrO 2 ). The experiments have been carried out in an apparatus with two steps in series: (1) thermal treatment (at 500 °C, for the controlled deposition of pyrolytic lignin) and (2) catalytic in-line reforming in a fluidized bed. The reaction conditions have been as follows: oxygen/carbon ratio (O/C), 0, 0.17, 0.34, and 0.67; 700 °C; steam/carbon ratio (S/C), 6; space time, 0.3 g catalyst h/g bio-oil (for Ni/La 2 O 3 -αAl 2 O 3 ) and 0.15 g catalyst h/g bio-oil (for Rh/CeO 2 -ZrO 2 ); time on stream, 4 h. The content and morphology of the coke deposited on the catalysts has been determined by temperature-programmed oxidation (TPO), and the deterioration of the metallic properties of the catalysts by temperature-programmed reduction (TPR) and X-ray diffraction (XRD). The results (bio-oil conversion, product yield and their evolution with time on stream) show that for Rh/CeO 2 -ZrO 2 catalyst the decrease in coke deposition as O/C ratio is increased involves attenuation of catalyst deactivation. Consequently, this catalyst is stable after 24 h operation for high O/C ratios, thus keeping constant the activity for reforming reactions and the WGS reaction, with a high yield of H 2 and low yields of CO, CH 4, and hydrocarbons. However, for the Ni/La 2 O 3 -αAl 2 O 3 catalyst of lower activity than the Rh/CeO 2 -ZrO 2, the decrease in coke content as O/C ratio is increased does not involve a noticeable attenuation in catalyst deactivation, which is due to Ni sintering.