Yield Optimization and Scaling of fluidized Beds for Tar Production form Biomass

摘要

A numerical study is performed in order to evaluate the performance and optimal operating conditions of fluidized bed pyrolysis reactors sued for condensable tar production from bioass. For this purpose, a previously validate biomass particle pyrolysis model is coupled with a detailed Hydrodynamic model for the binary gas particle mixture. The kinetics scheme is based on Superimposed cellulose, hemicellulose, an lignin reactions.