Ricerc@Sapienza

The large amount of tar produced along with the syngas during biomass gasification is one of the major obstacle for the diffusion of gasifiers at industrial scale. Catalytic cracking and reforming are the most suitable processes for the transformation of tar into lighter gases. The selection of suitable catalysts is a critical step. The catalysts must own high activity and high resistance to deactivation for coke deposition.

The problem of the production of tar along with syngas in gasification processes limits the diffusion of this technology. In this work, the tar abatement capacity of four bed materials was investigated. The bed materials, namely, activated carbon, aluminum oxide, olive residue char, and pumice stone, listed in order of decreasing surface area, were chosen to investigate their effect on the abatement capacity. Furthermore, the deactivation of these materials with time on stream was measured, and the results were used to develop a kinetic model.