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This work focuses on the removal of the tar derived from biomass gasification by catalytic steam reforming on Ni/Al2O3 catalysts. Different tar model compounds (phenol, toluene, methyl naphthalene, indene, anisole and furfural) were individually steam reformed (after dissolving each one in methanol), as well as a mixture of all of them, at 700°C under a steam/carbon (S/C) ratio of 3 and 60min on stream...
Catalytic steam reforming of phenol over Ni/Al2O3 catalyst with 10wt% of Ni loading was carried out in a fixed bed reactor. The effect of temperature (650–800°C), reaction time (20–80min) and catalyst amount (0–2g corresponding to 0–4.5gcathgphenol−1) on carbon conversion, H2 potential and catalyst deactivation was studied. High efficiency of Ni/Al2O3 catalyst in steam reforming of phenol is observed...
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