Pilot verification of a two-stage fluidized bed gasifier with a downer pyrolyzer using oxygen-rich air

A novel two-stage fluidized bed gasification system coupling a downer pyrolyzer and a riser gasifier was proposed, and a pilot facility of 15 kg/h of feedstock was further built and tested, by which the resulting technology gains its advantages of realizing the two-stage gasification principle in fluidized beds and having the large tolerance to biomass quality and size. Gasification of pine chips was in turn investigated at various equivalent ratios of air by changing the O-2 concentration of gasifying agent composed of nitrogen and oxygen. The pilot facility was successfully operated at an ER value of 0.15, which generated 1.33 Nm(3) product gas per kilogram of feedstock and containing 26.5% CO, 13.6% CO2, 8.89% H-2, 12.6% CH4 and 0.63% C(n)H(m)yyy. The LHV of the obtained fuel gas was as high as 9.35 MJ/Nm(3) with a reasonably low tar content at 8.08 g/Nm(3). By increasing the ER from 0.15 to 0.3, the temperatures of the pyrolyzer and gasifier were increased from 790 to 823 degrees C and from 881 to 925 degrees C, respectively. The gas yield was decreased to 1.1 Nm(3)/kg to have a reduced cold gas efficiency of 65.5% and a lower tar content of 4.35 g/Nm(3) in the gas. These thus verified the technical feasibility of the proposed two-stage gasifier consisting of a downer and a riser.

Automated summary

A novel two-stage fluidized bed gasification system was proposed, allowing for the realization of the two-stage gasification principle in fluidized beds and providing tolerance to biomass quality and size. Gasification of pine chips was successfully conducted in a pilot facility, resulting in a high heating value fuel gas.