文摘
The role of transport effects in experiments on the gasification reactivity of biomass char, conducted in a26-mm-diameter bench-scale fluidized bed (FB) reactor, is analyzed. Gasification rates of char were measuredat various particle sizes, CO2 partial pressures, temperatures, and initial char batches. A dedicated methodologyenables evaluation of the transport effects from gas measurements. The separate contributions of fluid-dynamics,external film, and porous diffusional resistances in a typical FB char gasification test are addressed. An optimaladjustment of the operating conditions of the FB is proposed to reduce mass-transport effects as much aspossible. When transport effects cannot be completely eliminated, this work shows how to treat the data toobtain an average reactivity that is useful for reactor simulations.