Modeling the effects of the operational parameters on H2 composition in a biomass fluidized bed gasifier

In this study, effects of the operational parameters such as gasifier temperature, bed operational velocity, equivalence ratio, biomass particle size and biomass-to-steam ratio on hydrogen production from an atmospheric biomass FB gasifier is simulated by presently developed model. The model is one-dimensional, isothermal and steady state, and the fluid-dynamics are based on the two-phase theory of fluidization. Tar conversion is taken into account in the model. The model simulation results are also compared with and validated against experimental data given in the literature. As a result of this study, it is observed that H2 composition increased remarkably with the rise of the gasifier temperature. Small biomass particles improves H2 composition. It is unfeasible to apply too small or too large ER in biomass air–steam gasification. The increases in the mole fractions of H2 with increases in the steam flow rate indicated that the gas shift reaction has a substantial effect in air–steam gasification.