Steam/oxygen biomass gasification at pilot scale in an internally circulating bubbling fluidized bed reactor

The result assessment allowed to evaluate the system flexibility to the gasifying agent and acquire data on the gas producible with this specific configuration. Based on the dry compositions, LHVs in the range 5.9-6.7 MJ/Nm3dry, 6.3-8.4 MJ/Nm3dry and 10.9-11.7 MJ/Nm3dry were respectively calculated for the three product gases. Correspondingly, an increase in the cold gas efficiency from 0.5 up to 0.7 was also estimated. Concerning the contaminant loads, in the case of the tests related to steam/O2 biomass gasification, particle and tar contents were found in the range 6-10 g/Nm3dry and 12-18 g/Nm3dry, respectively, while H2S, HCl and NH3 were at concentrations below 100 ppms (v).